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JANUARY/FEBRUARY 2002 • PHARMACEUTICAL ENGINEERING 1 Process Simulation The Role of Process Simulation in Pharmaceutical Process Development and Product Commercialization by Demetri P. Petrides, Alexandros Koulouris, and Pericles T. Lagonikos This article describes how batch process simulators can be used to facilitate and expedite development and commercialization of pharmaceutical products. Introduction T he development and commercialization of a new pharmaceutical product is a painstaking process that takes 7 to 12 years to complete requiring sizeable invest- ments ranging from $100 million to $500 mil- lion. In addition, 80 to 85% of products in devel- opment fail somewhere in the development pipe- line, often after undergoing expensive clinical trials 1 . The pharmaceutical industry spends considerably more on the development and evaluation of products that eventually fail than on successful products. Consequently, any meth- odologies and tools that can be used to evaluate alternatives and speed up the development ef- fort can have a tremendous impact on the bot- tom line. Computer Aided Process Design (CAPD) and simulation tools have been successfully used in the chemical and oil industries since the early 60s to expedite development and optimize the design and operation of integrated processes. Similar benefits can be expected from the ap- plication of CAPD and simulation in the phar- maceutical industries. The primary emphasis of this article is on the role of CAPD and simulation in expediting process development. The responsibilities of process development include: 2 Figure 1. Addition of unit procedures and stream lines to the flowsheet. Reprinted from The Official Journal of ISPE PHARMACEUTICAL ENGINEERING® January/February 2002, Vol. 22 No. 1 ©Copyright ISPE 2001
Transcript
Page 1: Reprinted from The Official Journal of ISPE ......With process development nearing completion at the pilot plant level, CAPD and simulation tools are used to systemati-cally design

JANUARY/FEBRUARY 2002 • PHARMACEUTICAL ENGINEERING 1

Process Simulation

The Role of Process Simulation inPharmaceutical ProcessDevelopment and ProductCommercialization

by Demetri P. Petrides, Alexandros Koulouris, and Pericles T. Lagonikos

This articledescribes howbatch processsimulators can beused to facilitateand expeditedevelopment andcommercializationof pharmaceuticalproducts.

Introduction

The development and commercializationof a new pharmaceutical product is apainstaking process that takes 7 to 12

years to complete requiring sizeable invest-ments ranging from $100 million to $500 mil-lion. In addition, 80 to 85% of products in devel-opment fail somewhere in the development pipe-line, often after undergoing expensive clinicaltrials1. The pharmaceutical industry spendsconsiderably more on the development andevaluation of products that eventually fail thanon successful products. Consequently, any meth-odologies and tools that can be used to evaluatealternatives and speed up the development ef-

fort can have a tremendous impact on the bot-tom line.

Computer Aided Process Design (CAPD) andsimulation tools have been successfully used inthe chemical and oil industries since the early60s to expedite development and optimize thedesign and operation of integrated processes.Similar benefits can be expected from the ap-plication of CAPD and simulation in the phar-maceutical industries. The primary emphasisof this article is on the role of CAPD andsimulation in expediting process development.The responsibilities of process developmentinclude:2

Figure 1. Addition of unitprocedures and stream lines tothe flowsheet.

Reprinted from The Official Journal of ISPE

PHARMACEUTICAL ENGINEERING® January/February 2002, Vol. 22 No. 1

©Copyright ISPE 2001

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2 PHARMACEUTICAL ENGINEERING • JANUARY/FEBRUARY 2002

Process Simulation

• supply of initial quantities of the Active PharmaceuticalIngredient (API) for toxicological screening and formula-tion studies

• supply of Drug Product (DP) to support clinical trials

• development of a practical, environmentally sound, andeconomically feasible route for producing the API and DP onan industrial scale

• selection, scale-up, and validation of these processes, en-suring the smooth transfer of technology from the pilotplant to the ultimate production site(s)

Process simulation tools can be used throughout the life cycleof process development and product commercialization. Thebenefits at the various stages of the commercialization processare explained below.

Idea GenerationWhen product and process ideas are first conceived, processsimulation is used for project screening/selection and strategicplanning based on preliminary economic analyses.

Process DevelopmentWhile the pre-clinical and clinical testing of the candidate drugcompound is going on, the company’s process developmentgroup is looking into the many options available for manufac-turing, purifying, characterizing the drug substance, and for-mulating it as a drug product. At this stage, the processundergoes constant changes. New synthetic routes are beinginvestigated. New recovery and purification options are evalu-ated. Alternative formulations also are explored. Typically, alarge number of scientists and engineers are involved in theimprovement and optimization of individual processing steps.Simulation tools at this point can introduce a common lan-guage of communication and facilitate team interaction. Acomputer model of the entire process can provide a commonreference and evaluation framework to facilitate process de-velopment. The impact of process changes can be readilyevaluated and documented in a systematic way. Once a reli-able model is available, it can be used to pinpoint the most cost-sensitive areas — the economic “hot-spots” — of a complexprocess. These are usually steps of high capital and operatingcost or low yield and production throughput. The findings fromsuch analyses can be used to judiciously focus further lab and

Figure 2. The operations associated with the first unit procedure of Figure 1.

pilot plant studies in order to optimize those portions of theprocess. Being able to experiment on the computer with alter-native process setups and operating conditions reduces thecostly and time-consuming laboratory and pilot plant effort.The environmental impact of a process is another issue thatcan be readily evaluated with computer models. Materialbalances calculated for the projected large scale manufactur-ing reveal the environmental hot-spots. These are usuallysolvents and regulated materials that are costly to dispose of.Environmental issues not addressed during process develop-ment may lead to serious headaches during manufacturing.This is the case because after a process has been approved bythe regulatory agencies, it is extremely costly and time-con-suming to make process changes. This is particularly true forbiopharmaceuticals where it is commonly said that “the pro-cess makes the product.”

Facility Design and/or SelectionWith process development nearing completion at the pilotplant level, CAPD and simulation tools are used to systemati-cally design and optimize the process for commercial produc-tion. Availability of a good computer model can facilitate thetransfer of process technology and facility design. If a newfacility needs to be built, process simulators can be used to sizeprocess equipment and supporting utilities, and estimate therequired capital investment. In transferring production toexisting manufacturing sites, process simulators can be usedto evaluate the various sites from a capacity and cost point ofview and select the most appropriate one. The same can applyto outsourcing of manufacturing to contract manufacturers.

ManufacturingIn large scale manufacturing, simulation tools are primarilyused for process scheduling, debottlenecking, and on-goingprocess optimization. Simulation tools that are capable oftracking equipment utilization for overlapping batches canidentify bottleneck candidates and guide the user through thedebottlenecking effort.

Commercially Available ToolsProcess simulators for continuous chemical processes havebeen in use in the petrochemical industries since the early1960s. Established simulators for the petrochemical indus-tries include: Aspen Plus (from Aspen Technology, Inc.),ChemCAD (from Chemstations, Inc. ), HYSYS (from Hyprotech,Ltd./AEA Engineering Software), and PRO/II (from Simula-tion Sciences, Inc.).

The time-dependency of batch processes makes develop-ment of batch process simulators more challenging. “Batches”from Batch Process Technologies (West Lafayette, IN -www.bptech.com) was the first simulator specific to batchprocesses. It was commercialized in the mid 1980s. All of itsoperation models are dynamic and simulation always involvesintegration of differential equations over a period of time. Thissimulator has found applications in pharmaceuticals,biochemicals, and food processing.3

In the mid 1990s, Aspen Technology, Inc. (Cambridge, MA- www.aspentech.com) introduced Batch Plus, a recipe-drivensimulator that targeted batch pharmaceutical processes. Ataround the same time, Intelligen, Inc. (Scotch Plains, NJ -www.intelligen.com) introduced SuperPro Designer. SuperProhas its roots in BioPro Designer, the development of which wasinitiated at MIT in the late 1980s to address the needs of the

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JANUARY/FEBRUARY 2002 • PHARMACEUTICAL ENGINEERING 3

Process Simulation

Please be aware that the Garbage-In, Garbage-Out (GIGO) principleapplies to all computer models. If some of the assumptions and input data are

incorrect, so will be the outcome of the simulation.“ “

biopharmaceutical industries. SuperPro Designer was createdto address other related industries (e.g., synthetic pharmaceu-ticals, agrochemicals, food processes, etc.) as well as waterpurification and end-of-pipe treatment processes. More re-cently (late 1990s), Hyprotech, Ltd. (a subsidiary of AEAEngineering Software - www.hyprotech.com) introduced BatchDesign Kit (BDK), a tool originally developed at MIT which isquite similar in philosophy and functionality to Batch Plus.

Batch Plus, BDK, and SuperPro Designer differ from“Batches” in their basic approach to modeling. More specifi-cally, most of their unit operation models are not dynamic, butrather simple algebraic models, whose solution does not re-quire integration of differential equations. This shortens thecomputation time and enables the user to evaluate a largernumber of scenarios in a shorter period. Batch Plus is recipedriven. In other words, the user develops a model by creatinga text recipe (similar to a batch sheet), and the modeling enginecreates a Process Flow Diagram (PFD) as an output. BDK andSuperPro Designer build their process models using a graphi-cal user interface with a PFD view. A batch sheet is generatedas an output report. SuperPro Designer can handle batch andcontinuous processes equally well; whereas the other threetools are practically limited to batch processes.

SuperPro Designer will be used to illustrate the role ofprocess simulators in the design and development of bulksynthetic pharmaceutical processes. Information on the role ofprocess simulators in the design and development ofbiopharmaceuticals can be found in the literature.4

Generation of a Batch Process Simulation ModelTo model an integrated process on the computer, the userstarts by developing a flowsheet that represents the overallprocess. Figure 1, for instance, displays part of the flowsheet ofa synthetic pharmaceutical process. The flowsheet is devel-oped by putting together the required unit procedures (seenext paragraph for explanation), and joining them with mate-rial flow streams. Next, the user initializes the flowsheet byregistering the various materials that are used in the processand specifying operating conditions and performance param-eters for the various operations. The simulator is equippedwith two component databases, its own of 450 compounds anda version of DIPPR that includes 1,700 compounds. It alsocomes with a user database where modified and newly createdcompounds can be registered. All database files are in MSAccess format.

Most bulk pharmaceutical processes operate in batch orsemi-continuous mode. This is in contrast to petrochemicaland other industries that handle large throughputs and usecontinuous processes. In continuous operations, a piece ofequipment performs the same action all the time (which isconsistent with the notion of unit operations). In batch process-ing, on the other hand, a piece of equipment goes through acycle of operations. For instance, a typical Nutsche filtrationcycle includes charge of slurry, filtration under vacuum orpressure, cake washing, occasionally cake drying, and removalof cake. In SuperPro, the set of operations that comprise a

processing step is called a “unit procedure” (as opposed to aunit operation). Each unit procedure contains individual tasks(e.g., charge, heat, react, etc.) called operations. A unit proce-dure is represented on the screen with a single equipment icon(for example, P-1/R-101 in Figure 1 represents the first proce-dure P-1 that takes place in stirred-tank reactor R-101). Inessence, a unit procedure is the recipe of a processing step thatdescribes the sequence of actions required to complete thatstep. Figure 2 displays the dialog through which the recipe ofa vessel unit procedure is specified. On the left-hand side ofthat dialog, the program displays the operations that areavailable in a vessel procedure; on the right-hand side, itdisplays the registered operations. The significance of the unitprocedure is that it enables the user to describe and model thevarious activities of batch processing steps in detail.

For every operation within a unit procedure, the simulatorincludes a mathematical model that performs material andenergy balance calculations. Based on the material balances, itperforms equipment-sizing calculations. Unlike typical modelswhere batch time is specified, this simulator provides the abilityto calculate batch cycle time by estimating the cycle-time ofscale-dependent unit operations. If multiple operations within aunit procedure dictate different sizes for a certain piece ofequipment, the software reconciles the different demands andselects an equipment size that is appropriate for all operations.In other words, the equipment is sized so that it is large enoughthat it will not be overfilled during any operation, but it is nolarger than necessary (in order to minimize capital costs). Inaddition, the software checks to ensure that the vessel contentswill not fall below a user-specified minimum volume (e.g., aminimum stir volume) for applicable operations.

Before any simulation calculations can be done, the usermust initialize the various operations by specifying operatingconditions and performance parameters through appropriatedialog windows. After initialization of the operations, thesimulator performs material and energy balances for theentire process, and estimates the required sizes of equipmentand the batch cycle time. Optionally, the simulator may beused to carry out cost analysis and economic evaluation calcu-lations. The fundamentals of process economics are describedin the literature.4

Other tasks that can be handled by process simulatorsinclude process scheduling, environmental impact assessment,debottlenecking, and throughput analysis. Issues of processscheduling and environmental impact assessment will beaddressed in the next section. In throughput analysis anddebottlenecking, the engineer analyzes the capacity and timeutilization of equipment and resources (e.g., utilities, labor,raw materials), and tries to identify opportunities for increas-ing throughput with the minimum possible capital invest-ment.

Having developed a good model using a process simulator,the user may begin experimenting on the computer withalternative process setups and operating conditions. This hasthe potential of reducing the costly and time-consuming labo-ratory and pilot plant effort. Please be aware that the Garbage-

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4 PHARMACEUTICAL ENGINEERING • JANUARY/FEBRUARY 2002

Process Simulation

In, Garbage-Out (GIGO) principle applies to all computermodels. If some of the assumptions and input data are incor-rect, so will be the outcome of the simulation. Consequently, acertain level of model validation is necessary. In its simplestform, a review of the results by an experienced engineer canplay the role of validation.

Illustrative ExampleThe objective of this example is to illustrate how batch processsimulators can be used to model, visualize, and analyze bulkpharmaceutical processes. This example deals with the pro-duction of around 171 kg per batch of an intermediate pharma-ceutical compound. This task is accomplished using three1,000 gal reactors, two 4 m2 filters, and one 10 m2 tray dryer.

Process DescriptionThe entire flowsheet of the batch process is shown in Figure 3.It is divided into four sections: 1) Product Synthesis, 2) Isola-tion and Purification, 3) Final Purification, and 4) Crystalliza-tion and Drying. A flowsheet section in SuperPro is simply a setof unit procedures (processing steps). The unit procedures ofeach section are marked by distinct colors (green, blue, purple,and black for section one, two, three, and four, respectively).Due to space limitations, the description below is not compre-

hensive and is not intended to be an exact representation of theactual process. The following sections are merely intended toillustrate the usage of a simulation tool in designing andanalyzing a sample process.

The formation of the desired product in this example in-volves 12 unit procedures. The first reaction step (procedure P-1) involves the chlorination of quinaldine. Quinaldine is dis-solved in carbon tetrachloride (CCl4) and reacts with gaseousCl2 to form chloroquinaldine. The conversion of the reaction isaround 98% (based on amount of quanaldine fed). The gener-ated HCl is neutralized using Na2CO3. The stoichiometry ofthese reactions follows:

Quinaldine + Cl2 ===> Chloroquinaldine + HClNa2CO3 + HCl ===> NaHCO3 + NaClNaHCO3 + HCl ===> NaCl + H2O + CO2

The small amounts of unreacted Cl2, generated CO2, andvolatilized CCl4 are vented. The above three reactions occursequentially in the first reactor vessel (R-101). Next, HCl isadded in order to produce chloroquinaldine-HCl. The HCl firstneutralizes the remaining NaHCO3 and then reacts withchloroquinaldine to form its salt, according to the followingstoichiometries:

Figure 3. The flowsheet for the example pharmaceutical intermediate compound.

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JANUARY/FEBRUARY 2002 • PHARMACEUTICAL ENGINEERING 5

Process Simulation

NaHCO3 + HCl ===> NaCl + H2O + CO2

Chloroquinaldine + HCl ===> Chloroquinaldine.HCl

The small amounts of generated CO2 and volatilized CCl4 arevented. The presence of water (added with HCl as hydrochloricacid solution) and CCl4 leads to the formation of two liquidphases. Then the small amounts of unreacted quinaldine andchloroquinaldine are removed with the organic phase. Thechloroquinaldine-HCl remains in the aqueous phase. Thissequence of operations (including all charges and transfers)requires about 15.8 hours.

After removal of the unreacted quinaldine, the condensa-tion of chloroquinaldine and hydroquinone takes place inreactor R-102 (procedure P-2). First, the salt chloroquinaldine-HCl is converted back to chloroquinaldine using NaOH. Then,hydroquinone reacts with NaOH and yields hydroquinone-Na.Finally, chloroquinaldine and hydroquinone-Na react andyield the desired intermediate product. Along with productformation, roughly 2% of the chloroquinaldine dimerizes andforms an undesirable by-product impurity. This series ofreactions and transfers takes roughly 16.3 hours. The stoichi-ometry of these reactions follows:

Chloroquinaldine.HCl + NaOH ===> NaCl + H2O +Chloroquinaldine

2Chloroquinaldine + 2NaOH ===> 2H2O + 2NaCl + ImpurityHydroquinone + NaOH ===> H2O + Hydroquinone .NaChloroquinaldine + Hydroquinone.Na ===> Product + NaCl

Both the Product and Impurity molecules formed during thecondensation reaction precipitate out of solution and arerecovered using a Nutsche filter (procedure P-3, filter NFD-101). The product recovery yield is 90%. The filtration, wash,and cake transfer time is 5.4 hours.

Next, the product/impurity cake recovered by filtration isadded into a NaOH solution in reactor R-103 (procedure P-4).The product molecules react with NaOH to form product-Na,which is soluble in water. The impurity molecules remain inthe solid phase, and are subsequently removed during proce-dure P-5 in filter NFD-101. The product remains dissolvedin the liquors. Procedure P-4 takes about 10.9 hours, andprocedure P-5 takes approximately 3.5 hours. Notice that filterNFD-101 is used by several different procedures. The reactorsalso are used for multiple procedures during each batch.Please note that the equipment icons in Figure 3 represent

unit procedures, as opposed to unique pieces of equipment. Theprocedure names (P-1, P-3, etc.) below the icons refer to theunit procedures, whereas the equipment tag names (R-101, R-102, etc.) refer to the actual physical pieces of equipment. Inother words, the process flow diagram in this simulator isessentially a graphical representation of the batch “recipe”that shows the sequence of execution of the various steps.

After the filtration in procedure P-5, the excess NaOH isneutralized using HCl and the product-Na salt is convertedback to product in reactor R-101 (procedure P-6). Since theproduct is insoluble in water, it precipitates out of solution.The product is then recovered using another filtration step inNFD-101 (procedure P-7). The product recovery yield is 90%.The precipitation procedure takes roughly 8.1 hours, and thefiltration takes about 4.8 hours. The recovered product cake isthen solubilized in isopropanol and treated with charcoal toremove coloration. This takes place in reactor R-102 underprocedure P-8. After charcoal treatment, the solid carbonparticles are removed using another filtration step in NFD-102(procedure P-9). The times required for charcoal treatmentand filtration are 17.6 hours and 4.4 hours, respectively.

In the next step (procedure P-10), the solvent is distilled offuntil the solution is half its original volume. The product isthen crystallized in the same vessel with a yield of 97%. Thecrystalline product is recovered with a 90% yield using a finalfiltration step in NFD-102 (procedure P-11). The distillationand crystallization step takes approximately 13.1 hours, andthe filtration requires roughly 3.6 hours per cycle. The recov-ered product crystals are then dried in a tray dryer (procedureP-12, TDR-101). This takes an additional 12.4 hours.

Figure 4. Equipment utilization in three consecutive batches. Figure 5. Purified Water demand in five consecutive batches.

Table A. Raw material requirements (1 batch = 171 kg MP).

Raw Material kg/Year kg/Batch kg/kg MP

Chlorine 14,534 89 0.52Na2CO3 17,057 104 0.61USP Water 481,484 2,936 17.12HCl (20% w/w) 58,034 354 2.06NaOH (50% w/w) 33,206 202 1.18Methanol 89,827 548 3.19Hydroquinone 27,836 170 0.99Carb. TetraCh 80,743 492 2.87Quinaldine 24,132 147 0.86Sodium Hydroxide 12,041 73 0.43Isopropanol 322,303 1,965 11.46Charcoal 2,574 16 0.09HCl (37% w/w) 35,325 215 1.26Nitrogen 180,336 1,100 6.41

Total 1,379,432 8,411 49.05

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6 PHARMACEUTICAL ENGINEERING • JANUARY/FEBRUARY 2002

Process Simulation

Table D. Cost of raw materials.

Raw Material Price ($/kg) Annual Cost ($) %

Chlorine 3.30 47,961 2.74Na2CO3 6.50 110,870 6.33USP Water 0.10 48,148 2.75NaOH (50% w/w) 0.15 4,981 0.28Methanol 0.24 21,558 1.23Hydroquinone 4.00 111,345 6.35Carb. TetraCh 0.80 64,594 3.69Quinaldine 32.00 772,227 44.07Sodium Hydroxide 2.00 24,082 1.37Isopropanol 1.10 354,534 20.23Charcoal 2.20 5,662 0.32HCl (37% w/w) 0.17 6,005 0.34Nitrogen 1.00 180,336 10.29

TOTAL 1,752,000 100.00

Material BalancesTable A displays the raw material requirements in kg per year,per batch, and per kg of main product (MP = purified product).The plant processes 164 batches per year. Note that around 49kg of raw materials (solvents, reagents, etc) are used per kg ofmain product produced. Thus, the product to raw materialratio is only 2%, an indication that large amounts of waste aregenerated by this process.

Process Scheduling, Resource Tracking, and CapacityUtilizationFigure 4 displays the scheduling and equipment utilizationchart for three consecutive batches. The plant batch time isapproximately 81 hours. This is the total time between thestart of the first step of a batch and the end of the last step ofthat batch. However, since most of the equipment items areutilized for much shorter periods within a batch, a new batchcan be initiated every 48 hours. Multiple bars on the same line(e.g., for R-101, R-102, R-103, NFD-101, and NFD-102) repre-sent reuse (sharing) of equipment by multiple procedures. Ifthe cycle times of procedures that share the same equipmentoverlap, the program generates an error message. White spacerepresents idle time. The equipment with the least idle time

between consecutive batches is the time (or scheduling) bottle-neck (R-102 in this case) that determines the maximum num-ber of batches per year. Its occupancy time (approximately 44.2hours) is the minimum possible time between consecutivebatches (also known as Minimum Effective Plant Batch Time).This plant operates around the clock and processes 164 batchesper year. The simulator also keeps track and displays theutilization of auxiliary equipment, such as Clean-In-Place(CIP) and Steam-In-Place (SIP) skids.

Scheduling in the context of a simulator is fully processdriven and the impact of process changes can be analyzed in amatter of seconds. For instance, the impact of an increase inbatch size (that affects the duration of charge, transfer, filtra-tion, distillation, and other scale-dependent operations) on theplant batch time and the maximum number of batches can beseen instantly. Due to the many interacting factors involvedwith even a relatively simple process, simulation tools thatallow users to describe their processes in detail, and to quicklyperform what-if analyses, can be extremely useful.

Another characteristic of batch processing is the variabledemand for resources (e.g., labor, utilities, and raw materials)as a function of time. For instance, Figure 5 displays thedemand for Purified Water for five consecutive batches. Thered lines represent the instantaneous demand; whereas thegreen line represents the cumulative demand and correspondsto the y-axis on the right-hand side. The blue line correspondsto daily demand (the averaging period can be adjusted by theuser). High purity water is a common potential bottleneck inbiopharmaceutical processes. It is commonly used for multipleprocessing steps simultaneously in activities such as fermen-tation media preparation, buffer making, and equipment clean-ing. If not enough instantaneous (or cumulative) capacity isavailable, one or more process steps may be delayed, possiblywith severe consequences. The graph of Figure 5 along with theraw material inventory graph (not shown here) play a crucialrole in the sizing of utilities for a batch manufacturing facility.The program generates similar graphs for any raw material,heating and cooling utilities, and electric power consumption.

In addition to instantaneous demand of resources, thesimulator provides the means to track the volumetric utiliza-tion of all vessels throughout the batch cycle. This allows theuser to track maximum working volumes over time, andensure that the minimum stir volume is always met at anyrelevant point in a process. The volume content of vessels isalso used in sizing new vessels and calculating the capacityutilization of existing vessels.

Economic EvaluationCost analysis and project economic evaluation is important fora number of reasons. For a new product, if the company lacksa suitable manufacturing facility that has available capacity,it must decide whether to build a new plant or outsource theproduction. Building a new plant is a major capital expendi-ture and a lengthly process. To make a decision, managementmust have information on capital investment required andtime to complete the facility. To outsource the production, onemust still do a cost analysis and use it as basis for negotiationwith contract manufacturers. A sufficiently detailed computermodel can be used as the basis for the discussion and negotia-tion of the terms. Contract manufacturers usually base theirestimates on requirements of equipment utilization and laborper batch, which is information that is provided by a goodmodel. The simulator performs thorough cost analysis and

Table B. Key economic evaluation results.

Direct Fixed Capital $9.7 millionTotal Capital Investment $10.7 millionPlant Throughput 28,120 kg/yearManufacturing Cost $7.2 million/yearUnit Production Cost $257/kg

Selling Price $500/kgRevenues $14.1 million/yearGross Profit $6.8 million/yearTaxes (40%) $2.7 million/yearNet Profit $5.0 million/year

IRR (after taxes) 34.0%NPV (for 7% discount interest) $22.3 million

Table C. Breakdown of manufacturing cost.

Cost Item Annual Cost ($) %

Facility-Dependent 1,817,000 25.1Raw Materials 1,752,000 24.2Labor-Dependent 2,562,000 35.4Lab/QC/QA 384,000 5.3Waste Treatment/Disposal 724,000 10.0

TOTAL 7,240,000 100.00

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project economic evaluation calculations. It estimates capitalas well as operating cost. The cost of equipment is estimatedusing built-in cost correlations that are based on data derivedfrom a number of vendors and sometimes literature sources.The fixed capital investment is estimated based on totalequipment cost and using various multipliers, some of whichare equipment specific (e.g., installation cost) while others areplant specific (e.g., cost of piping, buildings, etc.). The approachis described in detail in the literature.4 The rest of this sectionprovides a summary of the cost analysis results for thisexample process.

Table B shows the key economic evaluation results for thisproject. Key assumptions for the economic evaluations in-clude: 1) a new manufacturing facility will be built and dedi-cated to production of this product; 2) the entire direct fixedcapital is depreciated linearly over a period of 10 years; 3) theproject lifetime is 15 years, and 4) 28,120 kg of final productwill be produced per year.

For a plant of this capacity, the total capital investment isaround $10.7 million. The unit production cost is $257/kg ofproduct. Assuming a selling price of $500/kg, the project yieldsan after-tax Internal Rate of Return (IRR) of 34% and a NetPresent Value (NPV) of $22.3 million (assuming a discountinterest of 7%). Based on these results, this project representsan attractive investment. However, if amortization of up-frontR&D cost is considered in the economic evaluation, the num-bers change dramatically. For instance, a modest amount of$10 million cost for up-front R&D amortized over a period of 10years reduces the IRR to 15.3%. This reinforces the point thatR&D expenditures should be considered in estimating andjustifying the pricing of pharmaceuticals.

Table C breaks down the manufacturing cost. Labor is themost important cost item accounting for 35% of the overall cost.The program estimated that 16 operators are required to runthe plant around the clock supported by four QC/QA scientists.This cost can be reduced by increasing automation or bylocating the facility in a region of low labor cost. The facility-dependent cost, which primarily accounts for the depreciationand maintenance of the plant, is in the second position (25% oftotal). This is common for high-value products that are pro-duced in single-product, small facilities. To reduce the impactof this cost, the pharmaceutical industry tends to use flexible,multi-product facilities, where a number of products are manu-factured in campaigns throughout the year. Raw materialsalso make up a large portion of the manufacturing cost.Furthermore, if we look more closely at the raw material costbreakdown, it becomes evident that quinaldine and isopro-panol make up by far the largest portions of this cost - Table D.Together they account for approximately 64% of raw materialscost. If a lower-priced quinaldine vendor could be found, theoverall manufacturing cost would be reduced significantly. Interms of the isopropanol cost, perhaps the charcoal treatmentprocedure should be studied to determine whether the amountof this solvent could be reduced. Decreasing the amount ofisopropanol would significantly improve the overall processeconomics because it would decrease the waste disposal costsas well as the raw material costs. Alternatively, perhaps someof the waste solvent which is currently being discarded couldbe purified and reused. This would decrease both disposal costsand raw material costs.

After a computer model for the entire process is developed,process simulators can be used to ask and readily answer“what if” questions and carry out sensitivity analyses with

respect to key design variables. In this example, we looked atthe impact of production scale on unit manufacturing cost.When a new drug is commercialized, it takes years to fullypenetrate the market. During that period, production is gradu-ally ramped up to meet demand. If the facility is designed tomeet demand at full market penetration, then, in the interimit is underutilized. The unit production cost as a function ofproduction scale in the interim period is shown in Figure 6. Itwas assumed that at lower production scale the plant simplyprocesses fewer batches per year (e.g., two per week instead ofone every two days) without handling any other products. Atlower annual throughputs the unit cost increases substan-tially because the same fixed cost is charged to a lower amountof product.

SummarySimulation tools can play an important role throughout thecommercialization process. In process development, they arebecoming increasingly useful as a means to analyze, commu-nicate, and document process changes. During the transitionfrom development to manufacturing, they facilitate technol-ogy transfer, and facility selection or construction. In manufac-turing, they assist engineers in dealing with production sched-uling and planning, throughput analysis and debottlenecking,and on-going process optimization.

Batch industries such as pharmaceuticals have just begunmaking significant use of process simulation to support processdevelopment and optimize manufacturing. Increasingly, uni-versities are incorporating the use of batch process simulators indesign courses. In the future, we can expect to see increased useof this technology and integration with other enabling technolo-gies, such as advanced process control, computerized batchrecipe generation, and on-line analysis and optimization. Theresult will be more robust processes developed faster and at alower cost; making higher quality products.

References1. Polastro, E.T. 1996. Managing Primary Process Develop-

ment. Pharmaceutical Manufacturing International, P.A.Barnacal (ed), Sterling Publications Ltd, London, p. 67-70.

2. Petrides, D.P., Calandranis, J., and Cooney, C.L., 1996.Bioprocess Optimization Via CAPD and Simulation for

Figure 6. Unit cost as a function of production scale.

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Process Simulation

Product Commercialization. Genetic Engineering News,Vol. 16 No. 16, p. 24-40.

3. Hwang, F. 1997. Batch Pharmaceutical Process Design andSimulation. Pharmaceutical Engineering, January/Feb-ruary 1997, p. 28-43.

4. Petrides, D., 2001. BioProcess Design and Economics. Itwill be appear as a chapter of a new bioseparations textbookpublished by Oxford University Press in the spring of 2002.Document available at www.intelligen.com/downloads/book_chapter/book_chapter.htm.

AcknowledgementThe authors greatly appreciate the initial work on the subjectmatter by Douglas Cameron Carmichael.

About the AuthorsDemetri P. Petrides is the President ofIntelligen, Inc. He has extensive experience inapplying simulation tools to model, analyze,and optimize integrated biochemical, phar-maceutical, and specialty chemical processes.Petrides holds a BS from National TechnicalUniversity of Athens (Greece) and a PhD fromMIT, both in chemical engineering. He is amember of ISPE, AIChE, and ACS.

Intelligen, Inc., 2226 Morse Ave., Scotch Plains, NJ 07076,1-908/654-0088, Email: [email protected].

Alexandros Koulouris is the Business De-velopment Manager of Intelligen Europe. Heis an expert in Process Modeling and Automa-tion. Koulouris holds a BS from Aristotle Uni-versity of Thessaloniki (Greece) and MS andPhD degrees from MIT, all in chemical engi-neering. Koulouris is a member of AIChE.

Intelligen Europe, PO Box 328, 57001Thermi, Thessaloniki, Greece, +30 310-498292,

Email: [email protected].

Pericles T. Lagonikos is a Senior PrincipalEngineer for Schering-Plough Research Insti-tute (SPRI). He has extensive experience indevelopment, scale-up, and commercializationof synthetic pharmaceutical processes and haspioneered the use of computer-aided processdesign tools at SPRI. Lagonikos holds BS andMS degrees from NJIT, both in chemical engi-neering.

SPRI, Chemical Process Technologies, 1011 Morris Ave., U-1-1-1525, Union, NJ 07083, 1-908/820-6572, Email:[email protected].

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JANUARY/FEBRUARY 2002 • PHARMACEUTICAL ENGINEERING 1

E-Commerce Data Centers

Facilities and InfrastructureRequirements for High ReliabilityE-Commerce Data Centers

by Clifford “Bud” Frith

Internet DataCenters (IDC)are required forthe successfuldeployment of e-commerceapplications. Thisarticle definesthe requirementsfor facilities andinfrastructuredesign,construction,operation, andmaintenancecriteria.

Introduction

What does e-commerce have to dowith the ISPE mission as the globalresource for healthcare technology

information? The key is “global resource” em-ploying the latest advancements for communi-cations and data transfer. Twenty-one yearsago, the founders of the International Societyfor Pharmaceutical Engineering focused on theglobal healthcare professionals. Now, 24 hoursa day, 7 days a week, we are in touch withtechnical specialists by e-mail and receive thelatest information using the Internet, WorldWide Web. The technology revolution, only 15years old, has expanded at a rate that moretechnical information has been developed andefficiently stored for retrieval in the past 10years than from the beginning of time.

Controlled environments, data centers, andnow Internet Data Centers (IDC) are requiredto support the advancements of technologiesand communications for the pharmaceutical,biotechnology, medical, aerospace, and semi-conductor industries.

This article will discuss the facilities andinfrastructure requirements for keeping pace

Figure 1. A programmableaccess card is used for high levelIDC security.

with the e-commerce revolution. The recentevents in New York City and Washington, DChave placed an even higher priority on theinfrastructure and security requirements forhigh speed, reliable electronic communications,storage, and data transfer. The 100+ Megabitsper second (Mbps) speeds and Terabits storagecapacity are standard Internet terminologyemploying fiber optics carrier systems and se-cure networks. Reliability levels or “up time”requirements >five-nines (99.999%) are cur-rent standards for mission critical applications.1

E-commerce first appeared to be a sales andmarketing responsibility. However, e-mail, webconferencing, electronic funds transfer, and on-line purchasing are now common requirementsfor almost every department. With the terror-ists’ activities of September 11, 2001 in theUnited States, we will experience a major para-digm shift in business practices for all domesticand international business.

The subjects of 21 CFR Part 11, ElectronicRecords and Electronic Signatures will not beaddressed in this article, but will be covered ina future article. However, the reliability andsecurity of the facilities and infrastructure

for Internet applicationsare major issues thatmust be understood andaddressed before the fullpotential of e-commercewill be realized in regu-lated industries.

Mainframe DataCenters to

Internet DataCenters (IDC)

Data centers originatedseveral decades ago asthe critical require-ments for mainframeand super computerswere defined. Tempera-ture, Relative Humidity(RH), and cleanliness

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levels were controlled with higher levels of security as themacro black boxes were scaled down to micro dimensions.Initially, the data center facility design, operations, and main-tenance criteria used the cleanroom guidelines as their modelwithout the airborne particle controls. Raised floors, StaticElectricity Elimination (ESD), temperature, and RH controlwere standard construction requirements. Monitoring of theseparameters included data acquisition systems. Special secu-rity protocols for data center access, the hardware, and soft-ware were initiated.

The recent invention of the Internet for global communica-tions has continued to expand the demand for technologies andinfrastructure that provide cost effective consumer, industrial,and government transactions. The semiconductor and tele-communications industries continue to achieve milestonesaccording to Moore’s law that states, “Advanced technologieswill double every 18 months.” With the micro-miniaturizationscales projected and the increasing speeds and capacitiesforecasted, the environmental and security controls for theInternet are critical. Therefore, the Information Technology(IT) professionals must recognize the skills and knowledge ofthe environmental control specialists. No longer are the hostservers, routers, and switching equipment safe in the office,the utility closet, or the air-conditioned “special” room. Con-nectivity to the Internet network backbones through severallayers of service providers is unacceptable. And, the highspeed, high capacity bandwidth must be scalable for the futurerequirements that may be as soon as next year. The Internethardware requires its own controlled, secure environment andutilities with redundancy. The power requirements-Uninterruptible Power Supplies (UPS) and on-site back upgenerators are very important. A recent IT management sur-vey reported; however, that 73% of companies had not in-spected and verified their Internet Service Providers (ISPs)infrastructure and facilities.1

In-House or Outsourced IDCInternet data centers for very large companies may be locatedin-house with the appropriate facilities and services. But thesecompanies must have multiple locations with data centers toprovide backup for their Disaster Recovery Plan (DRP). TheIDC is not compatible with the mainframe computer datacenter required for managing the MIS or ERP operations.Network integration between the two data centers is possible,but the technical specialists employed for each center gener-ally have different skills and training.

For most companies; however, co-location Internet datacenters are the most cost-effective facility and managed ser-vices. With the explosion of the Dot coms in 1998-2000, verylarge co-location facilities were constructed in major metro-politan areas with 100,000-800,000 square feet of secure,environmentally controlled space with high bandwidth capaci-ties, multiple carriers, and at least two redundant tier oneISPs. These facilities are called IDC “Hotels.” Unfortunately,the IT specialists or network administration personnel need totravel long distances in metropolitan traffic to perform ser-vices for maintaining their Internet operations. This is expen-sive, time consuming, discourages the personnel, and is thereason to maintain all hardware in-house. Recently, the co-location IDCs began providing managed services with highlyqualified personnel on a 24/7 basis. There still is some resis-tance for delegating such a sensitive responsibility to someonenot an employee of the company and their IT department.

More recently, strategically located, smaller co-locationIDCs are being constructed with the same secure, controlledfacilities and services. These may serve as the primary datacenter or the mirror DRP back-up facility. Also, with theadvancements in the telecommunications equipment industryfor smaller foot print hardware, the large IDC hotels maybecome extinct.

Regardless of the decision for internal or external services,the financial requirement must be addressed. This meansother budget items for the facilities and IT departments thatusually have not been considered.

Facilities RequirementsThe physical security, environmental controls, utilities, andconnectivity including redundancy are the responsibility of thefacilities group. A proper designed, constructed, operated, andmaintained IDC is an insurance policy for mission critical e-commerce applications. Therefore, contracting to an InternetService Provider (ISP) without providing adequate writtenrequirements and a validation inspection is not acceptable.

SecurityA programmable card access system (Figure 1) is typicallyused for independent one-customer rooms or suites. Customershared open areas that house equipment racks or equipmentcabinets are available on an “escort only” basis which requiresNetwork Operations Center (NOC) personnel present at alltimes that customer(s) will be in the secured area. Onlyapproved employees or agents for the customer are allowed intheir specific data center area. NOC personnel are available24/7.

A video monitoring system records all activities in andaround the premises continuously. These records are availablefor review under specific conditions by IDC customers.

Security for the data stored and transmitted is an area thatneeds more technical development. Corporate management isusually skeptical since the internal sensitive information isnot fully protected unless the proper security or “firewalls” arein place and tested frequently. The “hackers” or Internetterrorists have become very advanced with their tools andskills. Recent examples of high profile targets such as the FBI,CIA, and DOD are the reported cases. Many companies areexposed and are not aware of the intruders and to what files.New businesses providing internal and external auditingservices to validate the security of the system are available.

Managed services at IDCs can provide very secure firewallsfor software and hardware. Complete packages are availableand require a limited amount of operator time for good secu-rity. In a co-location IDC, clients can manage their ownfirewalls or use the expertise of the IDC personnel and variousnetwork or server intrusion monitoring devices. The highestsecurity level requires that all transmissions to and from theInternet must go through the firewall and be monitored.Charles Semeria, 3Com, published an excellent technicalpaper “Internet Firewalls and Security: A Technical Over-view” that covers the subject at the novice level.2

Software “viruses” are a very big concern for both IT admin-istrators and data center managers. The information “viruses”are just as dangerous as unwanted biological viruses. Excel-lent protection is available through commercial software pack-ages, but constant surveillance is essential. There are on-linereports that advise of new virus activity. Specialist are avail-able that have skills to detect and cleanse the network and

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E-Commerce Data Centers

individual applications. E-commerce users must be on thealert constantly for virus disruption.

The external electric power wiring and communicationscables are normally installed into the data center at twoseparate locations from two different utility sub stations andthe Internet connectivity from at least two ISPs. Currentconstruction practices require that only one digging project beactive in proximity to the facility and all redundant conduitscarrying power or communications cabling be 50 feet apart.Survey maps of the external conduits should be maintained forexcavation projects. These requirements should be standardfor new real estate developments that are specified as Technol-ogy Parks.

Environmental Controls and MonitoringTemperature, relative humidity, equipment/power grounding,static electricity (ESD), smoke-fire detection, and suppressionmust be monitored and controlled with products designed forsuch operations.

HVACRedundant computer grade air conditioning units with humid-ity control are standard products for the industry - Figure 2.Design of the air handling distribution system is critical.Efficiency models prove that a raised floor with removable

Figure 2. Temperature and humidity are maintained with redundant computer grade HVAC units.

perforated panels to balance the heat load (Figure 3) and anunder floor plenum with epoxy paint sealant and no utilities orplumbing is the best design.

Temperature controls within 70 °F +/- 2 and RH of 45+/- 5%are normal specifications with 45% RH minimum in drygeographical regions.

ESDAn area being ignored by most data center planners is thedissipation of the static electricity from personnel and activi-ties in the IDC. Similar to microelectronic chip manufacturing,high speed and high volume electronic data transfer is verysensitive to the immediate environment. This is an issue thatneeds serious study as we advance to the gigabit/second trans-mission level. To protect the equipment and cables, a chemicalgrounding well adjacent to the building housing the IDC isrequired with special wiring and special grounded flooringtiles to eliminate even the lowest levels of static electricity.Water pipe grounding will not meet the conditions for protect-ing the equipment, power, and the transmission network.Equipment racks and cabinets, as well as electrical circuits,must have a proper grounding to the chemical well. Thisinstallation must be certified and documented. Levels <2 ohmsresistance are recommended throughout the entire IDC.

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E-Commerce Data Centers

Smoke and Fire DetectionThe high tech cleanroom particle monitoring systems havebeen valuable for smoke and possible fire detection usingsubmicron laser monitors - Figure 4. The trace out-gassingfrom an overheated fan or circuit card can sound the warningmany days or hours before the source becomes an issue. Sinceparticle counting is not required, normal IDC environmentbackgrounds are below the threshold of the out-gassing smokeparticles. This macro-detection system can be set to release thefire suppression chemical in localized areas to minimize theimpact on the entire IDC.

Smoke and Fire SuppressionHalon was used for many years as the best fire extinguisher inenvironments where water would not be effective or woulddestroy the expensive facility or equipment. Halon was veryeffective since it would extinguish any class of fire by quicklyreplacing the oxygen that was needed for combustion. Halonwas removed from the list of chemicals acceptable for firesuppression, since it also was very dangerous to the personnel.

A new material FM200 is just as effective and is personnelsafe and non-destructive to the facility and equipment. It is thesame chemical used in inhalers for asthma patients, but isused as a very concentrated vapor. FM200 will break the bondbetween the material and the heat source in less than 15seconds and then dissipate quickly into the environment. It isexpensive to use, but the cost is relative when compared to thevalue provided in protecting the IDC and the equipment.

Electric UtilitiesGlobal industries, especially in healthcare applications, arevery aware of the supply and reliability issues for electricpower. The recent issues in California and the instability of theworld gas and oil suppliers make long range planning forreliable energy difficult. Both the power generation and distri-bution grid systems are a risk.

Onsite GeneratorBackup electric power is provided by onsite generation withdiesel or natural gas units. This is essential as outages areunpredictable and the quality of the utility supplied power isvariable for the level required to support IDC operations. The

issues faced by IDC developers installing a generator are localregulations and possible resistance from the utility compa-nies. The generator supplies the UPS, HVAC, lighting, secu-rity, and power outlets within the IDC.

Uninterruptable Power Supply (UPS)The IDC must be operated with “clean” power that avoidsspikes, fluctuations, and intermittent service. Redundant com-puter grade UPS units with battery backup are installed -Figure 5. The stable, sine wave, power supplied throughout theIDC is controlled by the UPS regardless of the source or qualityof power. With the speed and volume of data being transferred,individual equipment UPS units are not acceptable. The ground-ing of the UPS is also very important.

Communications TransmissionE-commerce is becoming the cost-effective business process forsuccessful companies to increase their profitable revenue. Thespeeds and volume of data being transmitted are acceleratingat a dramatic rate. Fiber optic cabling is already installedworldwide in conduits that are projected to meet demand for2005.3 SONET Rings, a fail-safe transmission circuit, areinstalled around most metropolitan areas in the US. Technol-ogy advancements are predicted to improve the reliability andscalability factors four fold in the next three years whichshould enhance the profitability of this industry several timescurrent performance. The 2003 revenue projections for the USInternet infrastructure industry exceed $16 billion.3

An example of the volume and speed of transmission is therecent report by Alcatel, a Paris based telecommunications-equipment producer. They claim the current world record forsub-ocean transmission by transmitting across the AtlanticOcean, 6,850km, 3.65 Terabits/second (Tbps) on a single opti-cal fiber. In layman terms, this is equivalent to the simulta-neous throughput of 45 million voice calls, 552 CD-ROMs, 35Encyclopedia Britannicas, or 16 high definition movies over asingle optical fiber.4

Figure 3. Raised floor with perforated tiles provides an efficient HVAC distributionplenum.

Figure 4. Laser trace smoke detector provides early warning of a problem.

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E-Commerce Data Centers

ConnectivityThe most confusing issues for Internet users relate to the levelof service provided and how the Internet industry defines theterminology. In order for the Internet or World Wide Web(www) to be deployed successfully, a minimum level of conduitwith “lighted” fiber was required. Major global telecommuni-cations carriers initiated the process of installing parallel fibernetworks in strategic locations. In its infancy, the Internet wasoperated through the standard copper telephone lines. How-ever, the speed and volume of transmission was greatly re-stricted due to the capability of the telephone communicationssystem which was already overloaded at peak times of thebusiness day with voice and fax traffic.

In the US, the major ISPs are considered Tier One serviceproviders. Most businesses are connected to the Tier Onethrough regional Tier Two and Tier Three ISPs. Reliability canbe influenced by the service each tier provides. The quality ofservice is a major issue since there are no standards estab-lished for the industry. Eventually, the Tier One performancewill be available at most locations as the infrastructure isimproved and standards are established.

Additionally, the redundancy of ISP services will preventthe interruptions or delays being experienced currently. Thisis a major advantage provided by most co-location IDCs as theyare connected to multiple Tier One ISPs and manage theloading of their systems for optimum service.

Telecommunications Wiring StandardsThe Electronic Industries Association (EIA) and the Telecom-munications Industry Association (TIA) jointly prepared sev-eral building telecommunications standards and technicalbulletins. These standards are being revised since buildingwiring codes before the 1990s were only for voice transmission(4kHz) and Local Area Network (LAN) with 10MHz.5 Currentlevels of >100MHz and the new levels in the Gig Hz range needexacting standards to support e-commerce applications. Pre-wiring the buildings and data centers is inexpensive duringnew construction compared to wiring or cabling for renovationof an existing building. Certification of the cabling by theinstalling company is also recommended before the projectreceives final acceptance.

BandwidthThe term for describing the capacity or capability for transmit-ting data, voice, and video communications from point to pointis bandwidth. This is used for both analog and digital signals.It is a measure of the difference between the lowest and highestfrequency of transmission. When expressed as n bits/second, itis describing the quantity of data a particular transmissionline can carry each second.

The term T1 is common communications language and wasdeveloped in the 1960s using twisted pair copper wire trans-mission. It is now used for optical fiber, coaxial cable, anddigital microwave. The first (T1) transmission rate, 1.544Mbps,is in wide use today. The T(n) designation corresponds to thedigital service (DS) hierarchy. The following table illustratesthe T system hierarchy:

T1 = 1.544Mbps = 24 voice or data channels at 64KbpsT2 = 6.312Mbps = 96 voice or data channels at 64KbpsT3 = 44.736Mbps = 672 voice or data channels at 64KbpsT4 = 274.176Mbps = 4032 voice or data channels at 64Kbps

Therefore, a T2 rate is four times the capacity of a T1, a T3 is28 times a T1, and a T4 is 168 times the T1.6 Telecommunica-tions companies lease lines to customers depending on capac-ity required.

Co-location IDCs rent bandwidth to clients either as 1)dedicated or 2) burstable services. This is a cost-effectivemethod to achieve optimum levels of transmission for e-commerce operations. The dedicated service puts a cap on theamount of total bandwidth that can be used at a given time.The burstable service allows the sharing of bandwidth for peakdemand and is billed on a use rate basis. An example of theburstable service is a client may lease a fractional T1 level,512Kbps, and pay a flat rate. During a peak period, the actualuse may exceed the base level and burst to 1.544Mbps. Moni-toring by NOC operations allows the increase and the cus-tomer is billed for the additional percentage used over a 30 dayperiod. Since leased bandwidth is very expensive if not used,this burstable plan for shared services reduces operating costs.

Transmission technology using optical fiber is the founda-tion of e-commerce. The designations for optical carrier levels(OC-1 to OC-192) are typical of the expanded capability, i.e.OC-1 = 51.84Mbps and OC-192 = 9,952Mbps.6 Additionally,the advantage of the fiber circuit is the synchronous opticalnetwork (SONET), a standard protocol adopted by ANSI. TheInternet will advance rapidly as connectivity using fiber to thelocal area networks is expanded.

ConclusionThe design, operation, and maintenance of the IDC facilitiesand Internet infrastructure for e-commerce have many areasthat need standardization. The technology advancements areincreasing at a high rate and the commitment to improvedfacilities and infrastructure must keep pace. Environment,security, utilities, connectivity, monitoring, and verificationare critical areas that must be addressed to support successfulInternet applications and our status as the global resource forhealthcare technology information.

References1. StorNet Storage Newsletter, September 24, 2001.

2. Semeria, Charles, Internet Firewalls and Security; A Tech-nology Overview, 3Com Corporation Technical Paper, 1996.

Figure 5. Redundant UPS units provide “clean,” reliable power to the IDC.

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6 PHARMACEUTICAL ENGINEERING • JANUARY/FEBRUARY 2002

E-Commerce Data Centers

3. TelecomBiz.com Newsletter, August 29, 2001.

4. TelecomBiz.com Newsletter, November 30, 2001.

5. EIA/TIA-568, Commercial Building TelecommunicationsWiring Standards, 1995.

6. Newton’s Telecom Dictionary, 16th Edition, Telecom BooksPublishing, NY, NY, 2000.

Glossary of Terms and DefinitionsANSI- American National Standards Institute.

Bandwidth - A measure of the difference between the lowestand highest frequency of a data, voice, or video transmission.

ERP - Enterprise Resource Planning.

ESD - Electric Static Discharge.

Gigabits/second - 1,000 million bits per second.

HVAC - Heating, Ventilation, Air Conditioning.

IDC - Internet Data Center.

MIS - Management Information System.

SONET Ring - Synchronous Optical Network.

Tier One ISP - The highest level of network connectivity for theInternet, World Wide Web.

AcknowledgementThe author would like to thank Jason Parker, Array BioPharma,for review of this article.

About the AuthorClifford “Bud” Frith is Vice President, DCS,Inc., a custom software developer and InternetData Center construction and managementcompany. He is a charter member of ISPE andhas more than 40 years of experience in thepharmaceutical, biotechnology, medical de-vice, aerospace, and semiconductor industries.Frith graduated from the Virginia Military

Institute with a BS and continued graduate studies at North-eastern University. Frith was a pioneer for the design, opera-tions, and maintenance of cleanrooms developing the originalUSAF documents that were used for preparing Federal Stan-dard 209. Additionally, Frith pioneered the high purity waterstandards and equipment for laboratory and process applica-tions, filtration membranes for contamination analysis andcontrol, and was a founder and CEO of Anatel Corporation andDataTrax. His employment also included the USAF, Millipore,Vaponics, and Osmonics. Frith has chaired numerous ASTMstandards committees and is a Technical Editor of the IEST.He has lectured internationally and published more than 50articles and chapters concerning contamination analysis andcontrol. Frith has served as senior management of large publiccompanies and start-up ventures. Frith can be reached at 1-303/228-1066 or [email protected].

DCS, Inc., 450 Courtney Way, Lafayette, CO 80026.

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JANUARY/FEBRUARY 2002 • PHARMACEUTICAL ENGINEERING 1

E-Technology Application

E-Technology ApproachIntegrates Basis of Designthrough Turnover Package toFacility Management

by Daniel P. Collins, PE and Edward N. Pedersen, RA

This articlediscusses how totransform designbasis criteria intoreadily accessibleinformationwithin a databaseto help build cost-effective cGMPfacilities.

We are in an era characterized byexploding technology, expandingregulation, and time to market fo-

cus for new therapeutic products. This has chal-lenged current Good Manufacturing Practice(cGMP) facility planners, consultants, construc-tors, and facility managers to increase theirefficiency and effectiveness. The design/buildprocess generates a huge amount of raw datawhich needs to be captured and passed to thefacilities manager. A way to do this is to trans-form design basis criteria into readily acces-sible information within a database system.According to Robert Lipman of the NationalInstitute of Standards and Technology (NIST),“an effective project delivery process dependson the availability of current and correct infor-mation for all the participants, wherever theyare and wherever they need it.”1 This informa-tion, once made available, can be used to createknowledge-rich and intelligent constructiondocuments. At project completion, this informa-

tion can be packaged into a facility manage-ment system.

This approach can be called the e-technologyapproach, which when utilized produces thedrawings and specifications required to com-plete construction, along with a way to organizethe information the facility manager can referto and rely on for years to come. This facilitymanagement system can be provided to thecustomer at approximately the same cost as theconstruction documents alone. This article de-scribes a system recently developed in-house fora client.

Step 1: Harnessing the DataA cGMP facility must be responsive and sup-portive of the business goals. The business strat-egy, organizational structure, and individualwork environments must be defined throughprogramming sessions with an open dialoguebetween all participants. Upper management,finance, production, human resources, material

Figure 1. User inputs.

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E-Technology Application

handling, R&D, quality assurance, safety, information tech-nology, regulatory, maintenance, and operations must providedata and information forming the Basis Of Design (BOD).2

Figure 1 illustrates the user requirements to define the facilityrequirements and BOD. This BOD input becomes the databaseand is accessible to group pieces of data together, find singlebits of information, format many kinds of output, and maintainthe accuracy of that information. The database system allowsmany people to look at information simultaneously and fromdifferent locations.

The BOD database will include process/control criteria, anequipment list and unit equipment diagrams, and a listing offunctional space that will house the required equipment,people, materials, and movement patterns. Space need alloca-tions also must encompass infrastructure support and distri-bution spaces. Infrastructure support space includes laborato-ries, control rooms, weigh rooms, and maintenance areas.Distribution space includes piping corridors, locker rooms,storage and staging areas, quarantine areas, shipping, andreceiving. In addition to allocating space for specific functions,allocations have to be made for unassigned spaces such asmechanical rooms and chases, structure, corridors, and verti-cal circulation. The final functional space listing with typicalroom sheets quantifies the design performance characteristicsand technical requirements for each space including HVAC,plumbing, electrical, finishes and relationships to other spaces,equipment, and utility needs. The result is a quantified set ofarchitectural and engineering parameters that define thescope of the facility and establishes the basis for a realisticbudget estimate.

How is this data management accomplished? Data is bro-ken into general categories: documents, drawings, and equip-

ment - Figure 2. Each of these categories has a dedicateddatabase to manage that information. These dedicated data-bases are linked together by a common element (a projectnumber or customer) enabling a free flow of informationbetween these databases.

The Documents, or “Docs” database can include BOD infor-mation, Meeting Minutes, Construction Notices, Requests forInformation, Submittals, Transmittals, and Project Sched-ules. Search functions are built in to allow quick and logicallocation of data. Like any database system, the use of consis-tent and constant updates is key.

Basis of DesignAs PFDs, P&IDs, and construction drawings are created, anintelligent database file is written semi-automatically whichrecords important data about each element of the design. Keydata is recorded in the database, including vessel dimensions,pressure ratings, capacity, heat exchanger jacketing, materialand thickness, and pipes to and from the reactor. As the PFDis developed into a more detailed P&ID, that same data may beaccessed. Next, details such as pipe size, material, schedule,instrumentation, and control devices are added to the P&ID.Finally, a 3-D model of the process is constructed in Computer-Aided Design (CAD) software that shows the equipment usingthe correct dimensions and locations. In this way, the PFDs,P&IDs, and construction drawings are all linked to the designdatabase.

The power and benefits of the 3-D model are realized duringdocumentation for validation, construction, process safetymanagement, operations, maintenance, and renovation. De-spite the fact that all the data mentioned above is typicallyincluded in construction drawings or design reports under theconventional method of project design, the data is often searchedfor and keyed into multiple locations over and over again inorder to create all the required documentation. However, usingthe 3-D modeling approach, all of this information only has tobe reviewed and entered once. The data is subsequently ma-nipulated and displayed in different formats to satisfy require-ments such as equipment schedules, design reports, validationdocuments, and process safety management databases.

Meeting MinutesThe Meeting Minutes section enables the user to track indi-vidual action items or minutes across meetings and acrossprojects for the same client. The user enters all associatedmeeting minutes, categorizing them as Action Items, Com-ment Only Items, or Long Term Items. These minutes are alsocategorized by discipline. Consequently, from that one dataentry, the user can generate Meeting Minute Reports, InternalAction Item Summaries, Incomplete Item Reports, etc., alldisplaying consistent bits of information, but re-grouped andre-formatted to meet the needs of individuals. This system alsoenables cross project reports at the same site. For example, adiscipline manager, at the click of a button, can find out whataction items from his particular discipline across multipleprojects have yet to be completed. Additionally, the Docsdatabase enables the user to find in seconds, an individualmeeting minute across projects, based on one or two remem-bered words. If these meeting minutes were generated inindividual Word documents, that kind of searching and report-ing could take days, not seconds.

Figure 2. Database diagram.

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E-Technology Application

Requests for InformationThe Request for Information section of the database is apowerful way to track any questions that may be generatedand submitted during the construction phase. Like the Meet-ing Minutes, the user can generate multiple reports from onedata entry. Response reports, RFI logs, and RFI withoutResponse logs are accurate and simple to generate. Addition-ally, a powerful search tool can be built into this database forlocating individual questions or answers quickly. More impor-tantly, the database can be used to track questions, for gener-ating trends for quality management. A cross project reportcan show the numbers of certain types of questions asked. Ifthe same types of questions are continually asked, then aquality management issue is uncovered that needs to beaddressed. Again, this type of tracking is much more difficultwhen the data is scattered over multiple files.

Construction NoticesThe Construction Notice database output shown in Figure 4 isused to track construction notices and sketch information. Itcontains searching capabilities and easy reporting available inother parts of the database.

As with RFIs, this part of the database enables tracking oftrends and patterns. If, for example, a project manager canbecome aware that certain delays or changes consistentlyoccur with certain contractors or at certain points within

construction, that manager can anticipate these needs andaddress them more effectively. These features enable thesystem to become a quality assurance tool.

Project scheduling, transmittals, and submittals include allthe features and benefits of the previously mentioned sectionsof the Docs database.

Project ScheduleThe Project Schedule part of the database is used to track theproject schedule and then generate reports for contractors ofupcoming actions or milestones.

TransmittalsThe Transmittal part of the database is used to enter and tracktransmittal information. One output shown in Figure 5 be-comes the transmittal letter, and another the transmittal log.

SubmittalsThe Submittal database is used to enter submittal informa-tion, specify required submittals, and transfer submittal infor-mation to a project.

The Drawing Database (TBInfo)The Title Block Information database (TBInfo) is used to trackconstruction drawings - Figure 6. Drawings are logged byproject with their associated revisions. From this information,

Figure 3. RFI query/response.

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E-Technology Application

Figure 4. Construction notice.

the user can generate reports on drawing packages and latestrevisions. TBInfo also enables the user to group drawingstogether by discipline or by date released. But perhaps themost powerful feature is the links built to CAD drawingplatforms such as Microstation and Autocad. These linksenable the user to generate coversheets, based on the groups ofdrawings in the database, create the title block on the indi-vidual drawing, and track the location of these drawings. Thisinformation can be entered either directly into the database, orentered from the drawing and the system tracks the date,scale, and drawn by information.

The Equipment DatabaseThe equipment database tracks information about individualpieces of equipment to be relocated or newly purchased. Thisdatabase has all the before mentioned benefits of a database,but is also the engine behind the next levels of this facilitymanagement system.

Step 2: Assigning/Relating Data for TurnoverDuring the design phase of a project, graphical and alphanu-

meric data is gathered. This data must be communicated to theteam and client. The best way to do this is to create a realisticgraphical model with alphanumeric data assigned to thegraphics. This allows all parties to see and “query” every aspectof a project before it actually exists.

When a 3-D drawing is produced, database information canbe attached to any given object - Figure 7. This allows the userto select any piece of equipment, piping, etc. retrieve all of itsrelated information which is stored in the database. Forexample, the user records the size, manufacturer, pressurerating, and supplier for a specific valve on the first floor of afacility in the database. This information in the database isthen linked to the 3-D drawing of that valve. The customer cannow click on that valve and see the size, manufacturer, etc.without ever opening the database. If every piece of equipmentin the drawing, i.e. every valve, every air handler, every fan, ishandled in this way, the “Smart Drawing” is created. Addition-ally, this approach allows for maintenance information to berecorded. Now, at the click of a mouse, the client also can seethe turnover or maintenance information on that piece ofequipment. As the data is maintained in the database, the

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E-Technology Application

“Smart Drawing” becomes more and more valuable. Ulti-mately, up-to-date data coupled with easy access provides theinformation needed to make efficient and timely decisions.This approach to project information management is namedthe Standard Projects And Records Knowledge System, orSPARKS.

Now, let us take this one step further. If we group manyindividual smart drawings together into one “facility plan” andpost them on the web, we have the e-technology facility navi-gator.

Step 3: Enabling Access to the DataThe Navigator is web-enabled access to multiple data sources.These data sources can be as diverse as facility and processdrawings, operational and maintenance turnover records, spaceusage information, and employee data. Although the conceptis quite simple, the power of the system comes from the designand upkeep of the databases.

Understanding the databases as the repositories for theinformation that is displayed by the Navigator is central tousing this approach to data management. The Navigatorprovides the customer with a familiar window, the web, throughwhich to view vast quantities of information. With this win-dow, they do not need to buy third party software and traintheir employees on its use. The customer also is given theability to update the information viewed by the navigator ifthey choose. When this updating of information is maintained,the Navigator becomes an invaluable tool for facility manage-ment, both during construction and long after construction isfinished.

Life-Cycle Cost ImprovementThis can be a powerful tool for the management and transferof data both during the construction turnover and mainte-nance phases of a project. It also positively affects the bottomline. According to an August 2001 article in ENR, firms “gobeyond interoperability to automation to slash 30 to 40% off

the cost and time of construction.”3 For example:During the design/construction phase, savings can be found

in the following areas:

• Constructibility reviews. The 3-D walk-throughs save moneybefore and during construction by providing a virtual check-ing tool for all involved parties. For example, a customer canvirtually “walk through” a building, and completely experi-ence the layout long before hundreds of thousands of dollarsare spent on construction. Additionally, an engineer can usethis same 3-D walk through to find places where piping hitsductwork, and make alterations before this becomes aconstruction nightmare. By the time actual constructionbegins, problems have been solved and a viable and pleas-ing plan is in place both from a design and aestheticstandpoint.

• Interdisciplinary communication. With all project data lo-cated in one central location and accessible to all working onthe project, interdisciplinary communication is greatly im-proved. Consider: the architectural lead holds meetings,and keeps his minutes in a file on the hard drive of hiscomputer. Now, he decides in a meeting with a customer tore-design the atrium of the building, notes an action item tonotify the other discipline leads in the minutes on his laptop, and then is out of town for a week. A week later, henotifies the other disciplines of the change, and they have toredo/undo a week’s worth of work, wasting both time andmoney. Now consider this: this same architect has this samemeeting with this same customer, and notes the sameaction item to tell the other leads, but this time it is notedin a centralized database. That action item now appears onthe personal action item lists of the other two leads the verysecond it is written. The week’s worth of lost work is nowsaved, and the project moves forward smoothly. This is oneexample of how the tracking and reporting project data in acentralized database greatly improves communicationwithin all disciplines.

• E-Commerce opportunities. Consider the following: Whiledesigning an RTO system, two engineers carefully decide onthe number, type, flow capacity etc. of their dust collectors.The first notes this information as text in a drawing, or

Figure 5. Transmittal.

Figure 6. Title block information.

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Figure 7. Smart drawings.

perhaps in an Excel spreadsheet, or even in a Word file. Thesecond enters this information in the centralized projectdata management system and links it to his cad drawing.Now the contractor needs to know how many dust collectorsof what type to order. The second engineer merely has to runa summary report and send it to the Contractor, who canpre-order the dust collectors. This pre-ordering minimizesequipment costs, giving the purchaser the opportunity to“shop around.” Additionally, he has the opportunity to orderit in a timely enough manner to have it arrive on time,rather than behind schedule. Start-up time for constructionis minimized because there is an organized repository of allproject information. The first engineer, on the other hand,has the specifications for the dust collectors scattered throughcad drawings, excel spreadsheets, and word documents. Hehas to take extra time to locate, ensure accuracy, andcompile the data. In this case, time and money is lost, andconstruction may be delayed.

Over the operation life phase of a project, savings can be foundin the following areas:

• The data that proved so useful during design and construc-tion now takes on another function. Where the technicaldata of the dust collectors was used before to pre-order themand save on construction time, it is now used for mainte-nance information. The data is linked to the maintenancework order system and can be accessed with one click on theequipment. Now, if the information is updated, a history ofthat equipment, including maintenance problems is dis-played. A maintenance person is no longer looking throughgrimy logs with ripped pages, but viewing clear electronicfiles. Better preventative maintenance programs can be putinto place to minimize potential downtime.

• In addition to maintenance information, the data thatserved as submittal information now turns into machinespecs and vender information without any added work.When a piece of equipment breaks, the maintenance personcan return to that same drawing he was using for mainte-nance, and click to find out the manufacturer of the personwho sold the equipment and contact information for re-

pairs. This creates a central location for SOP, O&M manu-als, and machine specs.

• Having one location and one system to learn, enables bettertraining of maintenance personnel. They can get used tofinding what they need in one way, rather than needing tolearn one system for maintenance, another for repairs, andyet another for vender information.

The process of 3-D modeling can be modified to fit manydifferent applications. For example, if PFDs and P&IDs al-ready exist, it is still more cost-effective to create constructiondrawings using 3-D modeling. This is because the CAD opera-tor only creates each design element once. It then selects anddisplays different views to produce plans, elevations, sections,and details. Commitment to this process has shown that it isactually less expensive to create 3-D models of facilities andprocesses for the production of construction documents than toutilize the conventional two-dimensional (2-D) approach.

Case StudyFinally, let us look at a case study of one customer using thissystem developed in house. Prior existing conditions:

• Schedules were created and input on a spreadsheet ratherthan a database. Schematics for new HVAC, piping, andelectrical systems for that project were included on draw-ings. Once the project was complete, these schedules andschematics would be updated and included on as-builtdrawings.

• As-built drawings. Once the project had been completed,redlined drawings from the contractors would be forwardedto the engineer for input into the computer. Prints weremade and issued to the customer for their use.

• Machine Specs have become a standard deliverable in late1999. These are provided in paper form in binders forbuilding managers and maintenance engineers to refer-ence. Information, such as schedules, OEM manuals, SOPs,and spare parts are included in machine specs.

Problems• As-built drawings created on a project by project basis start

to accumulate either hanging on racks or in rolls in thecustomer’s engineering and building manager’s workspace.

• Troubleshooting and maintenance of equipment consists offinding the location of system and also pertinent informa-tion required from drawings, schedules, schematics, andmachine specs. This includes sorting through rolls of as-built drawings to piece together systems, which could beshared with labs or offices from other projects. A quickresponse and troubleshoot was dependent on having correctdata. Downtime of lab or process becomes costly.

• Programming of new projects – facility engineers have tolocate as-built plans in rolls of drawings to scope outavailable space and capacity of existing systems to deter-mine cost ramifications of new labs or process.

• Building managers incorporating the equipment number-ing system take spreadsheet schedules and assign their

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E-Technology Application

equipment numbers to them. Maintenance scheduling orhistories of building systems require cross-referencing tothe engineering drawings, schedules, schematics, and ma-chine specs.

Solutions – Value Add• The engineer is now creating as-built drawings, schematics,

and machine specs by building rather than by project.Schedules are created using databases so that equipmentnumbers can be assigned early in the project and can belabeled on drawings, databases, schematics, and machinespecs. This creates easy links between drawings and ma-chine specs to equipment numbers to access pertinent datafor maintenance and troubleshooting. It also creates meansof asset management to track equipment for labs andprocesses.

• As-built drawings created by building allow the user toaccess floor plans, schedules, and schematics by buildingrather than by project. These building drawings have (orare) being created by the engineer and only have to beconfigured once. Each time a project is completed, the samedrawing only needs to be printed with the new information.This creates less rolls of drawings for the customer tomanage and it decreases time as-built information getsback to the customer after project is complete.

• The engineer created a Web-based knowledge system thatwill allow any user to look at building plans and locateinformation through the use of a common Web browser.This eliminates the need for CAD or database training tomake use of the electronic data created for projects. It alsoorganizes the information in a logical system that makes iteasy to locate information that is required by the user.

There are costs for the engineer to create tools listed above aswell as maintaining 3D model, facility drawings, and databasestructures once created. However, the use of these systemsprovides the customer with a useful tool and significant losttime savings. Below is a value-added analysis.

Benefits/Cost SavingsTime saved with implementation of Facility Navigator• building managers 12 hrs/week• maintenance engineers 4 hrs/week• computer management engineers 8 hrs/week• facility engineers 6 hrs/week

Total 30 hrs/week

• number of weeks/year 50• estimated cost/hr $ 60.00• total cost savings $90,000• one time start-up cost $65,000• maintenance cost of system $50,000• first year cost to customer $30,000• annual savings to customer hereafter $40,000

SummaryTo ensure success in building cost effective cGMP facilities, theplanning and design must begin on a strong foundation thatcarefully, but expediently organizes the client’s requirementsinto a logical implementation plan that establishes the goalsfor the facility, determines the means of achieving those goals,

and identifies the resources required to complete the project.This plan must be derived from the active participants of allthat will manage or operate the facility. The plan must care-fully balance budget and functional issues, and consider pro-viding the appropriate levels of technology, accommodation,and flexibility to meet the ever changing business goals of thecompany.

The use of the Navigator and its partner database in FDAregulated facilities is a streamlined approach that never sac-rifices quality, innovation, or responsiveness. In fact, applyingthis e-technology at each stage of a project, from programming,design, construction turnover, record keeping, and commis-sioning, is important in creating and operating a highly cost-effective and flexible facility.

References1. Lipman, Robert. “Product Data Standards for Steel Con-

struction.” Page 1, www.NIST.gov (12/4/2001).

2. Broadhead, Jeffrey and Pedersen, Edward. “Front EndPlanning for cGMP Facility Expansion.” Journal of GXPCompliance, Volume 6, Number 1, Page 3 (10/2001).

3. Roe, Andrew and Reina, Peter. “Learning to Share is Tougherthan Anyone Anticipated.” ENR. 8/13/01. (pp 41-44).

Glossary of TermsPFD - Process Flow Diagram

P&ID - Process and Instrumentation Diagram

RFI - Request for Information

CAD - Computer Aided Drafting

SOP - Standard Operating Procedure

O&M - Operator and Maintenance

About the AuthorsDaniel Collins, PE is a licensed engineer anda Vice President of Sear-Brown. Collins is alsoa manager for the firm’s Corporate Facilitiesand Industrial Division, which is active incorporate design, facility upgrades, and reno-vations and process integration for pharma-ceutical, high technology, and equipmentmanufacturing nationwide. At Sear-Brown,

he has been instrumental in developing the infrastructure andstaff capabilities for e-technology applications. He can bereached at 1-607/735-0909.

Edward Pedersen, RA is a process architectand Director of Facility Planning for Sear-Brown, Bio-Pharmaceutical Group providinga full range of process and facility designintegration services. Pedersen has 28 years ofexperience with both industry and consultantresponsibility involved in all phases of cGMPoperations. He can be reached at 1-607/735-

0909 or (919) 349-6553.Sear-Brown, 310 E. Church St., Elmira, NY 14901.

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IT Data Centers

Monitoring Mission-Critical 24/7IT Data Centers in aPharmaceutical Facility

by Nissan Cohen

This articlediscusses whatprocedures,documentation,and practices areneeded toestablish anIntegrated Powerand EnvironmentMonitoringSystem in apharmaceuticalfacility.

The IT environment is a non-productionarea of a pharmaceutical facility. The ITdata center and all constituent compo-

nents are included in FDA scrutiny. The ITenvironment includes the traditional IT equip-ment and non-traditional IT equipment. Thelatter describes power and environmental equip-ment installed to specifically support the ITenvironment. The power and environmentalequipment are installed to maintain a 24/7/365(24 hours a day/7 days a week/ 365 days a year)IT and communications network. The installa-tion of a real-time Integrated Power and Envi-ronment Monitoring System (IPEMS) has beeninstituted at pharmaceutical companies to moni-tor, manage, alarm, and notify IT managementon the health and sustenance of the local andremote IT environment.

What procedures, documentation, and prac-tices are needed to establish this equipment in

a pharmaceutical facility? How is the facilitymaintained? How can a monitoring system beinstalled in a 24/7 mission critical operationwithout unnecessary disruption? How can theprevention of downtime enhance performancegoals? These questions are answered in thefollowing article.

Information Technology and Non-Traditional Information Technology

DefinitionsThe operation and sustenance of a data centerrelies on different tiers of structure and sup-port: the Information Technology (IT) enter-prise, the non-traditional IT infrastructure,operational and financial personnel, and engi-neering staff are needed to maintain coherentand efficient operations.

IT is a heterogeneous environment encom-passing multi-vendored products. The single

Figure 1. Corporate pyramidbased on Mission-Critical 24/7Operations.

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crosslink to all components, regardless of vendor, is a NetworkManagement System (NMS). IBM, HP, Compaq, Convergent,and Tandem products etc. are integrated into a concise enter-prise using NMS software. The integration of divergent ven-dors has been accomplished due to open architecture software.Traditional computer hardware is only a small component ofthe IT environment. Telephone switching systems, PBXs,network routers, Internet connections, Intranet networks;WANs, and LANs are all 24/7 sub-groups of the IT environ-ment.

Global, regional, remote, and local monitoring schemes areintegrated into an enterprise monitoring system. This schemepermits the usage of a centralized Network Operations Center(NOC) to monitor the entire enterprise. The centralized NOCcan serve as a clearinghouse for alarms and troubleshooting ofunmanned and remote sites without the cost of physical on-siteintervention. The mission-critical denotation is no longer ap-plied only to the computers and mainframes of data centerenvironment, but to all of the support and foundation equip-ment of the enterprise.1

Non-traditional IT equipment supports the mission-criticalIT sector. Equipment, commonly denoted as foundation orsupport, is being emphasized as an integral element of the ITstrategy. Power elements devoted to maintaining the uptimeof IT equipment; Uninterruptible Power Supplies (UPS); Die-sel and Gas generators; Automatic Transfer Switches (ATS),and Power Distribution Units (PDU) are being continuallymonitored as critical components in the IT strategy. Environ-mental elements of the Data Center are being scrutinized withthe same veracity. Solitary air conditioning units, tempera-ture, and humidity sensors are strategically placed in DataCenters to ensure maximum cooling and temperature stabil-ity. Electrostatic Discharge (ESD) monitoring is recommendedto prevent static electricity build-up and discharge to the ITequipment. Hazard and safety components are regularly de-vised into the monitoring scheme to ensure IT safety from fire,flood, and external atmospheric influences. In total, all ele-ments encompassing the IT environment (traditional or non-traditional), mission-critical applications, and a 24/7 enter-prise are in jeopardy if any failure occurs.

A graphic pyramid of this interdependence on all aspects ofthe corporate structure can be illustrated in Figure 1. The baseof the pyramid constitutes the non-traditional IT elements.The second tier denotes the traditional IT and communicationsequipment. The third tier controls all mission-critical aspectsof the enterprise. Upper tier is divided into two sectors “Com-petitive Advantage” and “Financial Performance.” Any ele-

ment under the mission-critical banner affects the competitiveadvantage and the financial performance.

Downtime CalculationEvery facility has a downtime calculation. In the event of an IToutage, the pharmaceutical company can realize revenue loss,documentation loss, actual experimentation or batch loss, andloss productivity of employees. These losses can total a run rateof tens of thousands of dollars an hour to more than a milliondollars an hour. A survey conducted in 1997 of the Fortune1000 companies showed the average IT downtime lasted forfour hours at an expense of $330,000 and an annual cost ofalmost $3 million dollars.2 This included all companies of theFortune 1000 in many different industries. Some industriesare more susceptible to downtime than others.

Figure 2 shows the amount of downtime per year when theuptime is 99.0% - 99.9%. The downtime calculation of a 99.9%uptime operation is almost nine hours per year. If an hour ofdowntime can equal $1,200,000 when all totals are tallied,then the following scenario can be calculated:

• 99.9% uptime = 8.76 hours of downtime a year

• $1,200,000 x 8.76 hours = $10,512,000 per year of loss orunrecoverable revenue

At 99.0% uptime, the loss of revenue per year is staggering:

• $1,200,000 x 87.60 hours = $105,120,000 of lost and unre-coverable revenue

Obviously, hourly calculations of revenue loss are the easiestto calculate. Each pharmaceutical company has calculationsfor downtime and risk factors. Minimizing both factors isimperative. Uptime is costly, but downtime is more expensive!

Downtime PreventionPrevention of downtime and guaranteeing uptime is para-mount in all mission-critical 24/7 operations. The non-tradi-tional IT infrastructure equipment is designed to enhance theuptime. Back-up systems for power, auxiliary power genera-tion, and corresponding power distribution systems are de-signed to enhance and alleviate the “dirty” and intermittentpower supply from the utility. Uninterruptible Power Supply(UPS) equipment conditions the power to supply constant andeven voltage to the needed IT equipment within small toler-ances of approximately 0.1%. Fluctuations from the power gridcan easily deviate to 10% of the prescribed voltage.

Ensuring the traditional IT infrastructure with conditionedand back-up power is only one way to enhance downtimeprevention. The ultimate assessment of uptime may rely onthe power back-up scheme and its monitoring.

All equipment can malfunction. Small deviations fromoperational norms can cause catastrophic outages. One datacenter, susceptible to chronic network bank failure, had diffi-culty in pinpointing the cause. Use of a real-time monitoringand management system help diagnose the problem. Theinstalled network cards were susceptible to Electrostatic Dis-charge (ESD). When the humidity in the data center roomdropped to 28%, static build-up and subsequent discharge wassufficient to render the network cards inoperable. The imple-mentation and use of an Integrated Power and EnvironmentalMonitoring System (IPEMS) allowed the data center manager

Figure 2. Uptime availability per year and the calculation of annual downtime inhours.

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IT Data Centers

to proactively assess and provide corrective actions inhibitingany further downtime due to ESD. The solution was simple:when the humidity fell to 30%, additional air conditioning anda stand-alone air conditioning unit provided humidity. TheIPEMS can watchdog many different and dynamic situationson a second-to-second basis and help in the management of theinfrastructure.

Although no system is infallible, use of IPEMS can improveuptime and reliability of the non-traditional infrastructure. Auser of IPEMS in Denver had 100% uptime for more than sixand a half years. This data center processes more than $50million in transactions per day. One hour of downtime equatesto more than $2 million in lost revenue. The cause of downtimeafter six and a half years of uptime was attributed to theengagement of an Emergency Power Off (EPO) switch, inad-vertently. The ensuring of uptime more than a six and a halfyear period translated into an estimated $100 - 200 million inadditional revenue to the company.

The IPEMS system should not be seen as a monitoringsystem only, but as a non-traditional infrastructure manage-ment tool.

Traditional Alarms Schemes versus IPEMSInstantaneous data, on-line measurement, and immediatenotification are inherent qualities of an IPEMS structure.

Proactive situational diagnostics of an excursion can impede orstifle an impending critical breakdown within the data center.

Traditional alarm schemes for status monitoring are of aBoolean nature. Status is monitored by a simple stop lightscheme. Red denotes alarm conditions and green denotesnormal operations. The traditional systems retain little or nodata archive, no graphical interpretation, nor definitive proac-tive actions. When an alarm is annunciated, many alarms maysimultaneously illuminate a panel or indicator board. Confu-sion may ensue due to the cacophony of buzzers and bellsproducing sensory overload. Since the indicators, panels, andboards do not archive historical data, “cause and effect” or“post-mortem” analysis will be severely hampered. A panelboard with many illuminated red lights does not allow fordiagnosis, rather it will indicate a change in status only, a basicchange from “good” to “bad.”

It is difficult to diagnose cause and effect where no historicaldata exists. Historical data is needed to compare normaloperating conditions versus abnormal or alarm conditions.

Historical data, graphing, relationship graphing, “causeand effect” scenarios, and near-term tactical and far-termstrategic planning can be elements of an IPEMS. IPEMS iscomprised of various data inputs: analog, digital, serial, andderived signals. Live inputs of analog, serial, and digitalsignals allow for a comprehensive monitoring scheme, but lack

Figure 3. Multi-channel graphing describes input voltages and changes over a 24-hour time span.

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finesse to define the total picture – Figure 3. Figure 3 depictsthe variations of voltages. A single voltage trace may indicatea condition or trend. The availability of multiple trace plottingand historical data display depicts the total conditions over aspecific time period. Long-term, short-term, and projectedtrend analysis provides proactive management of the powertrain.

A simple example:Temperature over a specified limit will cause an alarm.

Questions:- How long was the temperature rising before reaching the

limit?- Was there a sudden deviation from the normal and mean

temperatures? If yes, over what period of time?- Are there other channels of related equipment currently

being monitored which show a similar trend?- If the trend continues, what are the liabilities or risks?- Has a risk assessment been proffered of this condition

previously?- Are corrective measures, Standard Operating Proce-

dures (SOPs) or procedure steps documented and appli-cable to this condition?

- Can a decision be implemented before criticality causesmalfunction?

Although the questions above may seem trite, these questionsare valid and need historical data for verification, validation,and corrective action development to ensure that a similarexcursion in the future will be timely managed without disrup-tion to the IT environment.

Commissioning and DocumentationAlthough no control is administered in the above scenario,verification and validation of the installation and operation ofthe system is imperative in a regulatory environment. Com-missioning documentation is used during the installation andstart-up of the system. Verification of point-to-point datachannels is administered. Verification of values and alarmlimits is performed. Verification of communications schemes isdocumented.

Adherence to compatible instrumentation Installation Quali-fication (IQ), Operations Qualification (OQ), and Performance

Figure 4. Real-time information for pro-active management.

Qualification (PQ) documentation established in the pharma-ceutical facility is paramount. The installation and use ofsensors in the IT data center should correspond to the samedocumentation and maintenance rigors established for similarsensors in the production areas. The best example is theinstallation of temperature and humidity sensors in the ITdata center. A pharmaceutical facility in the northeast in-stalled similar temperature/humidity sensors as in the pro-duction area. These IT temperature/humidity sensors werevalidated using the same IQ, OQ, PQ, and maintenance docu-mentation.

Pharmaceutical Facility Local andRemote Monitoring

Many large pharmaceutical companies have a campus envi-ronment. One pharmaceutical company in the Midwest uses aDataTrax Foreseer IPEMS for monitoring distributed datacenters in a campus environment. All power and environmen-tal factors are monitored in real-time. Equipment monitoredincludes Uninterruptible Power Supplies (UPSs), generators,power distribution units (PDUs), air conditioning units, auto-matic transfer switches (ATS), power meters, fuel manage-ment systems for the generators, and battery monitoring. Notall equipment is installed in each building.

The IT Operations Center in the main data center main-tains the NT server. This NT server is the depository for allreal-time and historical data, alarms, alarm acknowledgements,reports, and notification schemes for all equipment connectedto the IPEMS server. Communication to the equipment in-stalled in buildings outside the data center is via TransmissionCommunications Protocol/Internet Protocol (TCP/IP). TCP/IPis the common communications protocol used in Internet andIntranet communications. The NT server queries a communi-cations device in the remote building. The remote communica-tions device transmits the data from the remote equipmentacross the network to the NT server. Local personnel areresponsible for the remote devices and buildings during busi-ness hours only. The IT Operations Center monitors all deviceson the entire campus 24 hours a day. During non-businesshours the IT Operations Center focuses on all operating pa-rameters of the entire enterprise. If an excursion or alarmshould occur, the IT Operations Center determines the sever-ity or criticality, and notifies the proper personnel.

Each piece of equipment is polled once a second for allcorresponding data. The DataTrax Foreseer IPEMS uses se-rial communication protocols to “talk” to a device. Serialcommunications allow for many different data values to betransmitted simultaneously. Serial communication schemesallow all of the data and channel values to be transmitted - notjust a singular value as in a digital form “c” contact. Someequipment use digital contacts for summary alarms. Althoughthe summary alarm provides adequate notification of an alarmon a given piece of equipment, it does not provide any data ofwhy the equipment malfunctioned or what predicated themalfunction.

Local and Remote MonitoringMonitoring schemes in the pharmaceutical industry includeglobal, regional, citywide, campus, and individual system’senvironments. As described above, a campus environment ismost often employed in the pharmaceutical industry. Manybuildings in the campus are connected via a communicationsnetwork using TCP/IP. Many sites on the campus can be

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JANUARY/FEBRUARY 2002 • PHARMACEUTICAL ENGINEERING 5

IT Data Centers

monitored in real-time using the network backbone providedby the IT department. Most multi-site pharmaceutical compa-nies have Wide Area Networks (WANs). This communicationsbackbone allows for Intranet and e-mail traffic at high-speeds.IPEMS are instituted to monitor the entire regional enter-prise, which may encompass many sites in a regional area ofthe United States. The aforementioned northeast pharmaceu-tical company monitors their main IT data center, local cam-pus, and a remote site in the Boston area on a single IPEMssystem across the WAN. Still, other companies utilize IPEMSfor monitoring of far-flung international operations in real-time across many time zones.

The crux of these operations is the imperative of providingdata and IT services 24/7/365. Multi-national, national, and24-hour pharmaceutical production facilities need access todata and IT operations at all times.

Capacity Planning Using IPEMSIPEMS can manage the infrastructure, predict needed capac-ity, and forewarn impending barriers or bottlenecks. IPEMScan accurately manage the non-traditional IT equipment withno adverse affect.3

As a data center is being populated with racks of equipment,each additional piece of equipment installed strains the envi-ronment, power, and sub-systems. If an UPS and a PDU havecertain capacities, the more equipment placed against thosecapacities will diminish the efficacy of the power supplied.What is the threshold of the “point of no return” when addi-tional equipment will overtax the supply? How many racksand banks of computers will it take to reach that point? Whenracks of computers are added, how much additional heat isgenerated? How much additional cooling is needed to offset theheat generation? Are the smoke, fire, and leak detectionsystems operational for the newly populated area?

Figure 4 depicts the load capacities of a DC rectifier plantcommonly used in telecommunication structures. The calcula-tion for load capacities is in real-time and congruent with thepeak and off-peak usage. Actual load calculations fluctuate ona second to second basis. As new equipment is populated thecapacity, load, and reserve characteristics change commensu-rate with the equipment power draw, as depicted in Figures 5and 6. These actual power calculations, for new equipment,can be pre-programmed as a derived channel and added to theexisting software before actual installation, thus, creating a

Figure 5. Power capacity vs. real-time load measurements per Power Distribution Unit. Calculation of watts per square foot for power density.

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6 PHARMACEUTICAL ENGINEERING • JANUARY/FEBRUARY 2002

IT Data Centers

Figure 6. UPS power load vs. capacity, KVA usage, and phase imbalance in real-time measurements.

“what-if” scenario with positive assessment before the instal-lation.

IPEMS can help with the resources to systematically allo-cate the proper hardware for each population addition in thedata center. As the new racks of computer hardware areinstalled, an equally important non-traditional IT componentis installed and functional. This exercise can beneficially helpfinancial planning, scheduling of installations, ordering ofequipment, project management, commissioning, and humanresources planning for the build, installation, initial, andcontinuous operation of a data center. All of these tasks are alengthy description of capacity planning.

SummaryMission critical 24/7 operations have unique and specializedfunctions and criteria. The investment by the data centeroperator in the computers, servers, networking equipment,routers, networks, communications, and connectivity devicesis in the millions of dollars.

The non-traditional IT equipment installed to support thedata center and communications gear is integral to the opera-tion and IT availability strategy.

The monitoring of the power, environmental, and indepen-dent systems installed to support the IT and communicationsenvironment is imperative to countermand downtime.

Historical trending, data, reports, records, real-time data,alarms, notification schemes, capacity planning, and trendingprognostication are elements shared by all financial, opera-tions, and engineering personnel.

The implementation of commissioning documentation, IQ,OQ, PQ and maintenance documentation where appropriate tonon-pharmaceutical production equipment, sensors, and ar-eas can meet and/or exceed FDA guidelines.

Uptime equals revenue. Action by the appropriate person-nel before an alarm or situation reaches criticality preventsdowntime, maintenance issues, and inoperative equipment.

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IT Data Centers

References1. Cohen, Nissan, “Monitoring Mission Critical 24/7 Data

Centers,” Jamaica Computer Society, Proceedings of theAnnual Meeting, October 26, 2001.

2. FIND/SVP, “System Downtime,” Information Advisor 2000,KM4:3.

3. DataTrax® Systems, “Power Management with the Fore-seer Software,” copyright 2001.

Additional Reference SourceAFCOM – The Leading Association for Data Center Profes-sionals, Web site www.afcom.com.

About the AuthorNissan Cohen has more than 25 years ofexperience in Mission-Critical Monitoring withemphasis in Semiconductor Manufacturing,Pharmaceutical Process and Production,Ultrapure Water and Chemical Systems,Nuclear Power, Foreign and Domestic Com-mercial and Governmental Data Centers, Fi-ber Optic Networks, and Internet Service Pro-

viders. Cohen has written more than 25 technical and peerreviewed articles for various publications including Pharma-ceutical Engineering, Pharmaceutical Technology,Ultrapure Water, Semiconductor International, Con-tamination and The Journal of the Institute for Environ-mental Sciences. Cohen is the International Sales Managerfor DataTrax Systems. Cohen received a BS from the Univer-sity of Wisconsin and a MS from Hebrew University, Israel.Cohen can be reached at: 1-303/665-5577 ornissan.cohen@datatrax. invensys.com.

Invensys, 520 Courtney Way, Lafayette, CO 80026.

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JANUARY/FEBRUARY 2002 • PHARMACEUTICAL ENGINEERING 1

Risk Assessment

Risk Assessment for IT Systems

by Chris Clark

This article wasadapted from apresentationdescribing theeffectiveness ofRisk Assessmentas a tool thatallows validationresources tofocus oncritical areas ofan automatedsystem.

Introduction

In today’s world of tighter regulation andseemingly ever increasing rates of change, itis becoming progressively more important

that companies can manage all risks with thepotential to adversely affect normal operations.

At present, companies will typically haveformulated plans to resume business after someform of disruption or failure. Companies alsoneed to understand the risks (and impacts)involved in installing new computer systems,both to patient safety and to the business.Such risks are commonplace, and may be assimple as the increased use of automation dis-tancing production operators, who had the ex-perience/ability to recognize and possibly pre-vent errors from the actual process.

Forward thinking companies now plan for‘risk avoidance’ or ‘risk management’ of boththeir day-to-day operations, and as part of newproduct, process, engineering, or information

Figure 1. Risk Assessment andthe validation process.

systems development. These plans aim to en-sure the continued operation and readiness ofcritical business processes. The pharmaceuti-cal industry also must consider the statutoryobligations imposed by EU and US cGMP regu-lations in general, and specifically with regardto Traceability, Product Recall, Product (Quali-fied Person) Release, and Adverse Event Re-porting. The widespread use of computerizedsystems throughout the industry means thatthese critical GMP functions are subject to regu-latory requirements for qualification and vali-dation.

The recognition that a computer system mayrequire validation often initiates the Risk As-sessment process. Regulatory authorities arevery likely to inquire about such an assessment,particularly if the company has systems thathave not been validated, but are apparentlyinvolved in GxP operations.

However, it is impractical and probably un-necessary to thor-oughly test everyaspect of a computersystem. Establishingthe extent of the vali-dation required by asystem is an issuethat causes muchdebate among bothregulators and vali-dation practitioners.Risk Assessment isan effective tool insupporting the deci-sion of which func-tions/sub functions ina large enterprisesystem require for-mal validation test-ing. Resolving thisissue, using a RiskAssessment process,allows the validationeffort to be focusedon critical areas,thereby allowing themost efficient alloca-tion of resources.

The informationprovided in this ar-

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PHARMACEUTICAL ENGINEERING® January/February 2002, Vol. 22 No. 1

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2 PHARMACEUTICAL ENGINEERING • JANUARY/FEBRUARY 2002

Risk Assessment

ticle is based on a GAMP Good Practice Guide to be publishedas part of GAMP 4. The technique, based upon Hazard Analy-sis Critical Control Point (HACCP), Hazard and Operabilitystudy (HAZOP), and Failure Mode and Effects Analysis (FMEA)principles, involves the use of a structured process consistingof a series of steps. The aim of this process is to establish whattypes of risks exist (GxP/business), under what situations theymay occur, and what level of impact they exert. This is pro-posed within a framework leading to formal documentation forsubsequent review by the business and the regulatory authori-ties.

The relationship between Risk Assessment and the valida-tion process is examined to determine the frequency by whichassessments should be performed.

Risk Assessment and theValidation Process

Due to the dynamic nature of a typical project lifecycle, riskpriorities can change over time. It is probable that risk assess-ments will need to be performed at different stages throughoutthe project. Although there is no specific rule regarding eitherthe number or timing of the Risk Assessments, generally they

are performed on a minimum of three occasions. Suggestedpoints for performing Risk Assessments within the validationprocess are:

• following the generation of the User Requirements Specifi-cation (URS)

• following the Supplier Assessment and prior to the develop-ment of the Functional Specification

• following the completion of the Design Review prior toValidation Test Development

These are illustrated in Figure 1.Performance of Risk Assessments at the above points en-

ables:

• user requirements and project needs to be critically as-sessed, and alternatives defined

• aids the supplier selection process• supports the definition of any mitigation steps• additional validation requirements and/or testing for the

project

The findings of these earlier Risk Assessments should beconstantly reviewed at later key points in the project, such asprior to making any changes while in routine operation toensure that assumptions and circumstances upon which theywere founded are still valid.

In addition to those assessment points recommended inFigure 1, there is a requirement to consider the continued useof Risk Assessment throughout the lifetime of the system,particularly at two key points. First the risks should be re-assessed at the time of signing off the validation and launchingthe live system. This need only be a simple exercise of review-ing the previous assessments performed earlier in the projectto ensure all mitigation measures have been implemented orplanned. The other key time to use the technique is during theprocess of change control. Many successfully validated sys-tems fail to maintain this hard earned status as a result ofpoorly performed change control and the introduction of theRisk Assessment technique as part of the change controlprocess will provide the means to avoid the unnecessary risk offailure. The technique will assist in identifying requirementsfor testing and qualification of the proposed changes, thussupporting the maintenance of the system validation.

The Risk Assessment ProcessIdentify Processes and GxP RiskThe first stage in assessing the risks affecting any system isthe establishment of the context for the assessment – Figure 2.For new IT systems, this may be found within the UserRequirement Specification and/or the Functional Specifica-tion. These documents can identify the system functions andtheir sub-functions (including any dependencies between them).

These functions/sub-functions must be formally documentedand described via summary details, including a name, whichshould convey something of the purpose of the function/sub-function. Once identified, each function/sub-function should

Figure 2. Overview of the risk assessment process.

Due to the dynamic nature of a typical project lifecycle,risk priorities can change over time.“ “

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JANUARY/FEBRUARY 2002 • PHARMACEUTICAL ENGINEERING 3

Risk Assessment

undergo a determination as to whether it represents a riskwhen assessed against a series of GxP criteria as laid down bythe standard international regulatory guidelines. If, for ex-ample, the risks that may be applied to the pharmaceuticalquality of the finished product are considered, they mayinclude:

• incorrect composition• raw materials errors• packaging materials errors• integrity of QC laboratory results• incorrect batch status• failure of storage conditions• batch recalls• lot traceability• labeling errors

As each function/sub-function is considered, the project teamshould make an assessment of the GxP impact and documentthe outcome of their discussions on the assessment form. Thisformal documentation also should include the justification foritems whereby no GxP risk has been assigned. This is useful forfuture reference to explain a particular validation approach toa third party, such as regulators.

This risk assessment approach also may be extended toinclude the identification of Business Risk. For example, risksto corporate reputation:

• adverse publicity• shareholder responsibilities• earnings impact• competitive advantage

Identify Risk Scenarios and Classify RiskHaving determined that a particular function/sub-functionmay have a GxP or business risk associated with it, theassessment should proceed to identify the various Risk Sce-

narios (i.e., the events that could lead to the system being putat risk). It is useful to consider for each event what the likelyoutcome will be (note that each event may have more than oneoutcome).

As an example, consider the Procurement Function and thesub-function of raising a Purchase Order. Analysis may sug-gest that an adverse event might well be the input of theincorrect grade of material during order entry. This couldresult one of several effects, ranging from the receipt of theincorrect grade of material, the rejection of material on receipt/analysis and an inventory shortage.

The next stage in the process is to determine the Likeli-hood (or probability) of an adverse event occurring. Thereare many ways to try to measure this concept, but a simplesuggestion is:

Low: the probability of the event occurring is perceivedto be less than one per year

Medium: the probability of the event occurring is perceivedto be between one per month and one per year

Figure 4. Risk priority.

Figure 3. Risk classification.

Modification of process or system design elements

• Avoidance:

The risks are so high that the new way of working should not beimplemented

• Process design:

One or more independent controls are incorporated into thecomputer-related process e.g., additional data verification checkswithin the system design in order to reduce data entry errors

• External Procedures:

Introduction of procedures to counter possible failures, such asdouble checking

• Product (or System) design:

Use is made of proven methods, tools and components; fault-tolerance may be built into the computer system (e.g., usingreplicated parts, system mirroring); the operating environment maybe controlled

Modification of project strategies

• Project structure:

This refers to the people chosen for the project, their experienceand qualifications; the type of project organization preferred; theamount of education and training provided

• Amount of (auditable) built-in quality:

Documentation is produced, approved and controlled – the usualmethod of demonstrating ‘validation’

Modification of validation approach

• Increased testing:

Increase the scope and level of testing applied during variousstages of the validation process, including the development ofspecialized testing aimed at the testing to failure of certainfunctions

• Decreased testing:

Decrease the scope and level of testing applied during variousphases of the validation process due to the extremely low riskassociated with occurrence and consequences of the faultconditions.

Table A. Mitigation strategies.

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4 PHARMACEUTICAL ENGINEERING • JANUARY/FEBRUARY 2002

Risk Assessment

High: the probability of the event occurring is perceivedto be between one per day and one per month

NOTE: If an estimate of the likelihood of an adverse event isdifficult to agree, the default value of “High” should be as-signed. As and when more information becomes available, thisvalue can be re-assigned as necessary during the subsequentrepeat Risk Assessments at later stages of the project.

Having determined the likelihood of the occurrence of anevent, the process moves on to consider the Impact on thebusiness of those effects, including impact on regulatory com-pliance, financial impact, company reputation with customersand suppliers, etc. For example, the immediate effect of a harddisk problem may be the corruption of some data stored on thatdisk, while the business impact of corrupt data relating toproduct distribution will eventually result in severe problemsin conducting a product recall. This would result in a criticalnon-compliance with the regulatory requirements and couldresult in the company having its manufacturing license with-drawn by the regulatory authorities. Again, a simple rule canbe applied as follows:

Low: expected to have a minor negative impact. Thedamage would not be expected to have a long-termdetrimental effect.

Medium: expected to have a moderate impact. The impactcould be expected to have short-term to medium-term detrimental effects.

High: expected to have an immediate and highly signifi-cant negative impact. The impact could be ex-pected to have significant long-term effects andpotentially catastrophic short-term effects.

The final step in determining the risk classification is to takethe values obtained for both the Likelihood of the riskoccurring and the level of Impact that such an event mayhave, and apply them to the simple matrix – Figure 3.

Plan Risk ManagementFirst, the process requires evaluation as to whether the riskevent can be recognized or detected by any other means in thesystem. For example, if a Level One Risk has a high probabil-ity of detection, it does not pose such a serious threat becauseit can be recognized quickly and suitable corrective actiontaken to mitigate its impact. Equally, if the same fault condi-tion has a low probability of detection, then the team mayneed to seriously consider a review of the design or theimplementation of alternative procedures to avoid the event.

A suggested method for estimating the probability of anevent being detected is as follows:

Low: detection of the fault condition is perceived to beunlikely (i.e., less than one event in every threetransactions or operations)

Medium: detection of the fault condition is perceived to bereasonably likely (i.e., one event in every twotransactions or operations)

High: detection of the fault condition is perceived to behighly likely (i.e., one event in every one transac-tion or operation)

By combining the values obtained for Risk Classificationwith the Probability of Detection in the simple matrix inFigure 4, the team can set an order of priority for developingmitigation measures:

The resultant Risk Priority of the fault conditionsnow provides a focus for the validation effort, offeringa structure for formulating a suitable mitigation strat-egy.

Mitigation StrategiesThere are several mitigation strategies available to modifyrisk levels, and several of them may be appropriate for a givensystem. Some examples are listed in Table A.

It should be noted that while this risk assessment techniquehelps to focus the effort required for successful validation, itdoes not provide the definitive answer. In some cases, it maybe necessary to increase the validation effort for certain failuremodes, even if the risk is calculated as being a low priority, forinstance, when regulatory requirements require a higher levelof validation than the failure mode indicates.

SummaryThe use of the simplified Risk Assessment process described inthis article provides:

1. the Support required for the successful development andimplementation of a computer system within the pharma-ceutical business

2. the required Focus ensuring that only those functionscritical and necessary for GxP and the business are vali-dated to a high level of assurance

3. the ability to both Scale-up and Scale-down the valida-tion effort as required

4. a formal means of documenting the Justification for thosekey decisions regarding the validation approach and thelevels of effort expended

About the AuthorChris Clark is Head of Quality Assurancewith NAPP Pharmaceuticals Ltd. and is re-sponsible for the implementation and mainte-nance of the processes and procedures thatform the basis of the company quality man-agement system. The scope of this role coversall major functions of the company, includingProduction and R&D, ensuring compliance to

current international regulatory requirements for GMP, GLP,and GCP. Included within this role is the responsibility for themanagement of the Validation Group who are involved in avariety of process-, product-, and equipment-related projects.He is currently involved as a member of the Core Project Teamseeking to implement an international corporate-wide elec-tronic document management and control solution. Clark is amember of the Industry Board and Steering Committee of theGAMP Forum and has spoken at ISPE conferences on subjectsrelated to the qualification and validation of computerizedsystems. He has more than 22 years of experience of QualityAssurance within the pharmaceutical and healthcare indus-tries, commencing with Sterling-Winthrop before moving toBaxter Healthcare Limited, joining NAPP in 1993.

NAPP Pharmaceuticals Ltd., Cambridge Science Park,Milton Road, Cambridge, CB4 0GW, United Kingdom.

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