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Production of the equine influenza vaccine using a baculovirus expression system in insect cell lines Part III: Downstream & process control Saioa Arza, Helena García, Oriol Cabau, Laia Puig GLOBAL OBJECTIVE Design of an industrial bioprocess plant with the simulator SuperPro Designer for the production of the equine influenza vaccine using a baculovirus expression system in insect cell lines, and subsequent analysis of its sustainability. To guarantee the quality of the final product, the process will be performed following the Good Manufacturing Practices (GMP) standards. In order to attain the fulfillment of the norms GMP a program Quality-by-Design (QbD) that will allow to control each point of the process efficiently has been designed. GMP PROCESS QbD PROGRAM BACULOVIRUS EXPRESSION SYSTEM PROCESS FLUX DIAGRAM CONTROL AND INSTRUMENTATION In order to guarantee the Quality-by-Design (QbD) program, instrumentation for process control has been installed. Details for the Bioreactor control and instrumentation: Process critical control loops: Air sterilization using HEPA filters Virus inactivation monitoring by virus quantification Protein production and purification In case one of the critical variables go out of the limits established the necessary measures would be carried out to go back to the normality. A closed control loop example: REFERENCES This is a simulation of the hole process that has been obtained from the block diagram using the process simulator SuperPro Designer. YIELD 70% UV light damages the DNA irreversibly eliminating the viral infectivity. Thymine dimers are an example of the damages that appears in the genetic material during this treatment. Thermal or chemical methods discarded for put in danger the stability of the protein. AEX chromatography binds virus and genetic material due to his negative charge. HA1 do not bind cause the working pH induces the protein to have a positive charge in his surface. As industrially stated, two different stages of viral clearence are performed. VIRAL CLEARENCE PROCESS ORGANIZATION Time organization in three consecutives batches with a total duration of 21 days. The critical step, and consequently the bottle neck is the bioreaction. Employers requirement during three consecutives batches. The employers demand is higher in the critical step with a peak of 12 workers. Process Analytical Technologies (PAT) implementation Control strategies by means of PAT are implemented to ensure product quality and operation efficacy in every stage of the downstream process. 21 g for each batch. HA1 is the 98.6% of the total protein at the end of the downstream. A highly purified product has been obtained. [1] → P.K.John. Instrumentation and Control Systems. Chapter 20. p. 411. Accessed 18 th April 2015 [2] → http://learn.parallax.com/pid-control. Accessed 27 th May 2015 [3] → http://commons.wikimedia.org/wiki/File:DNA_UV_mutation.png. Accessed 11 th April 2015 [4] → http://www.sartorius.es/fileadmin/DID/pdf/DID_Lit_Collection/Data_UVivatec_GMP_Lab-System_SPK2096-e.pdf . Accessed 14 th May 2015 [5] → http://faculty.southwest.tn.edu/rburkett/gb-Final%20Exam.htm. Accessed 21 th April 2015 [6] → http://www.verdotips2.com/our-products/easypack-chromatography-column/. Accessed 16 th February 2015 [7] → http://en.wikipedia.org/wiki/Ion_exchange. Accessed 16 th May 2015 Universitat Autònoma de Barcelona Biotecnologia 2015
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Page 1: Production of the equine influenza vaccine using a baculovirus … · Production of the equine influenza vaccine using a baculovirus expression system in insect cell lines Part III:

Production of the equine influenza vaccine using abaculovirus expression system in insect cell lines

Part III: Downstream & process controlSaioa Arza, Helena García, Oriol Cabau, Laia Puig

GLOBAL OBJECTIVE

Design of an industrial bioprocess plant with the simulatorSuperPro Designer for the production of the equine influenzavaccine using a baculovirus expression system in insect celllines, and subsequent analysis of its sustainability.

To guarantee the quality of the final product, theprocess will be performed following the GoodManufacturing Practices (GMP) standards.

In order to attain the fulfillment of the norms GMP aprogram Quality-by-Design (QbD) that will allow to controleach point of the process efficiently has been designed.

GMP PROCESS QbD PROGRAM

BACULOVIRUS EXPRESSION SYSTEM

PROCESS FLUX DIAGRAM CONTROL AND INSTRUMENTATION

In order to guarantee the Quality-by-Design (QbD)program, instrumentation for process control hasbeen installed. Details for the Bioreactor controland instrumentation:

Process critical control loops:

• Air sterilization using HEPA filters • Virus inactivation monitoring by virus

quantification• Protein production and purification

In case one of the critical variables go out of the limits established the necessary measures would be carried out to go back to the normality. A closed control loop example:

REFERENCES

This is a simulation of the holeprocess that has been obtained fromthe block diagram using the processsimulator SuperPro Designer.

YIELD 70%

UV light damages the DNA irreversiblyeliminating the viral infectivity. Thymine dimersare an example of the damages that appears inthe genetic material during this treatment.

Thermal or chemical methods discarded for put in danger the stability of the protein.

AEX chromatography binds virus and geneticmaterial due to his negative charge. HA1 do not bindcause the working pH induces the protein to have apositive charge in his surface.

As industrially stated, two different stages of viralclearence are performed.

VIRAL CLEARENCE PROCESS ORGANIZATION

Time organization in threeconsecutives batches with a totalduration of 21 days. The criticalstep, and consequently thebottle neck is the bioreaction.

Employers requirement duringthree consecutives batches. Theemployers demand is higher inthe critical step with a peak of12 workers.

Process Analytical Technologies (PAT) implementationControl strategies by means of PAT are implemented to ensure productquality and operation efficacy in every stage of the downstream process.21 g for each batch. HA1 is

the 98.6% of the totalprotein at the end of thedownstream. A highlypurified product has beenobtained.

[1] → P.K.John. Instrumentation and Control Systems. Chapter 20. p. 411. Accessed 18th April 2015[2] → http://learn.parallax.com/pid-control. Accessed 27th May 2015 [3] → http://commons.wikimedia.org/wiki/File:DNA_UV_mutation.png. Accessed 11th April 2015[4] → http://www.sartorius.es/fileadmin/DID/pdf/DID_Lit_Collection/Data_UVivatec_GMP_Lab-System_SPK2096-e.pdf . Accessed 14th May 2015

[5] → http://faculty.southwest.tn.edu/rburkett/gb-Final%20Exam.htm. Accessed 21th April 2015[6] → http://www.verdotips2.com/our-products/easypack-chromatography-column/. Accessed 16th February 2015[7] → http://en.wikipedia.org/wiki/Ion_exchange. Accessed 16th May 2015

Universitat Autònoma de Barcelona

Biotecnologia 2015

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