SHORTCOMING REPLY: BHAGWAN MAHAVIR SUPERSPECIALITY GOVERNMENT HOSPITAL AT PLOT NO. H-4, 5, PITAMPURA, DELHI BY M/s PUBLIC WORKS DEPARTMENT (HEALTH), GOVT. OF NCT, DELHI

1. Submit copy of valid consent to establish/consent to operate issued by DPCC for existing hospital project

Reply- Consent to Establish/ consent to Operate is to be obtained by PP.

Annexure 1- CTO from DPCC is obtained

2. Submit copy of authorization under bio-medical waste management rules , 2016 issued by DPCC

Reply- Authorization under bio-medical waste management rules, 2016 issued by DPCC is

obtained.

Annexure 2- BMW authorisation letter obtained

3. Details of ETP and STP to be provided Reply- STP of 253 KLD capacity is proposed based on MBR Technology.

The design of sewage network shall be done in accordance with the CPHEEO guideline, NBC guidelines and reverent Indian Standards. Sewage generation is assumed to be 100%

of flushing water and 80% of domestic water. The following parameters/ site conditions shall be kept in mind when designing the sewage,

Sludge and storm water drainage system.

Natural slope of the area.

Layout of different facility in the complex;

Possibility of using complete or part of the existing sewage network;

Sub-soil water table;

Provision of Sewage lifting station; ( if required)

Provision of venting arrangement for manholes;

Construction of manholes & laying of pipes considering ground condition;

Termination of vent cowl at terrace level;

Provision of adequate slope for horizontal header in the under slung pipes especially

for public toilets

Sewage flow starts with fractional capacity and builds up to full capacity in due

course. An operational plan to meet this demand from a low flow to full flow will be

part of the design.

A summary of board design parameters to be adopted for designing Sewage supply system

is given below.

Table 1: Design Parameters for Sewage Collection System

Different Use Norm Used

Type of Collection System Separate System

Design Period -30 years for sewers and appurtenances -15

years for pumps and electric equipment’s

Peak Factor 3

Minimum velocity 0.6 m/sec

Maximum velocity 3.0 m/sec

Minimum size of pipe 250 mm (ID)

Minimum depth of Sewer 1.0 m from FGL (0.6 m minimum

cushion)

Hydraulic Formula for calculation for

design of sewer lines (As per CPHEEO

manual 3.4.2.1 page no-36)

Manning’s formula V= 1/n*(R^2/3)

*(S^1/2 ) V= Velocity R = Hydraulic mean

depth = A/P S = Slope

Flow conditions in pipe up to 400 mm dia 0.50 full

Flow conditions in pipe up to 300 mm dia 0.67 full

Manning’s Co-efficient ‘n’ 0.011

Shape of sewers Circular

Material of sewers HDPE

Manhole Sizes As per manual on sewerage and sewerage

treatment/ IS4111:1985

For depth above 0.9m & up to 1.65m 900 mm diameter

For depth 1.65m & up to 2.3m 1200 mm diameter

For depth 2.3m & up to 9.0m 1500 diameter

The alignment and slope of the sewer line will follow the road network, drains or natural

ground surface and will be connected to the trunk sewers. The discharge point will be a

treatment plant, a pumping station, a water course or an intercepting sewer. Pumping

stations would be provided at places where the natural slope of the terrain is insufficient to

permit gravity flow or the cost of excavation is uneconomical to do the same

Following are the benefits of providing the Sewage Treatment Plant in the present

circumstances:

Reduced net daily water requirements, source for Horticultural purposes by

utilization of the treated wastewater. This shall consequently lead to a lower

withdrawal from the underground aquifer water sources.

Reduced dependence on the public utilities for water supply and sewerage systems.

Sludge generated from the Sewage Treatment Plant shall be rich in organic content

and an excellent fertilizer for horticultural purposes.

Technology Proposed

Membrane Bio Reactor (MBR)

The MBR is a suspended growth-activated sludge system that utilizes micro porous

membranes for solid/liquid separation instead of secondary clarifiers.

An external sewage network shall collect the sewage from all units, and flow by gravity to

the proposed sewage treatment plant

The STP is being proposed with state-of-the-art membrane separation technology called as

Membrane Bio-Reactor (MBR) which can produce very good quality with highest possible

bacterial reduction without adding any chemicals. MBR (Membrane Bio Reactor) is the

latest technology in wastewater treatment. MBR has many advantages such as higher

quality of treated water, smaller space for installation and easier operation compared to

conventional activated sludge process.

Designed to produce high quality treated water from wastewater the Membrane Bio Reactor

(MBR) is among the latest technologies in biological treatment.

The characteristic of the MBR process is the use of revolutionary submerged polymeric

hollow fibre membranes in the biological process water tank, so as to produce high quality

permeate from domestic sewage, primary and secondary waste water, cooling tower blow

down etc. The MBR is also ideal for retrofitting/augmenting capacity/quality of existing

wastewater plants.

The hollow fibers are combined into bundles and wound around a carrier cartridge, which

gives the membranes the required strength and allows for high-pressure air scour for

cleaning. The MBR can handle very high sludge concentrations in the aeration tank because

of which the size of the aeration tank reduces four to five folds. As the membrane acts as a

fine filter, it does not require any further treatment using sand filters, activated carbon filters,

etc. The MBR is available in standard and customized modules.

Process Description

Figure below shows the principle of the filtration for the flat sheet type submerged

membrane. Activated sludge in the aeration tank is clearly removed by the flat sheet type

submerged membrane. The membrane module consists of housing, aeration diffuser;

permeate water manifold and membrane elements. The membrane element consisting of flat

sheet membranes sandwiching a support panel is set up vertically. Feed water including

activated sludge is filtrated by flat sheet membranes with pore size of 0.1 micron meter. The

air bubbles supplied from the bottom of the membrane elements continuously scour off cake

of activated sludge accumulated on the membrane surface. This is continuous filtration

operation. The air bubbles are also used for the biological reaction to decompose organic

substances included in the raw sewage.

MBR Module

The material of the membrane is PVDF (Poly vinylidene fluoride). PVDF is fluorine

polymer, which has high stability for chemicals and good physical strength. The form of

membrane is fibre reinforced flat sheet membrane. The membrane has small and uniform

pore size. Therefore, the rejection property of this membrane is excellent. Almost all

particles with sizes more than 0.1 micron meter can be removed effectively using this

membrane.

Operation

Sewage from main drain line is collected through gravity pipes into a screen chamber. This

manually cleaned screen is provided to remove floating and big size particles, which may

choke the pumps and pipe lines.

Screened sewage is then passed through equalization tank to homogenize the sewage quality

and also even out flow fluctuations and feed sewage of uniform quality at constant rate to

subsequent treatment units. Air mixing is also provided to mix the contents of the

equalization tank. A coarse bubble aeration grid is provided to distribute air uniformly at the

base of the equalization tank.

After above treatment, raw sewage is fed into aeration basin.

In aeration tank, MLSS (mixed liquor suspended solids) in the range of 12000 to 15000

mg/l are maintained. The high amount of bacteria gives better and complete removal of

organic matter from the raw sewage in relatively small area. Oxygen required for the

bacteria is supplied through the blower. The air is used both for scouring of membranes and

supplying oxygen to bacteria.

The filtration is carried out by the suction pump directly sucking permeates water. The

permeate water produced is clear and devoid of bacteria and viruses to the minimum levels.

As the membranes are continuously under operation, they are polluted with organic or

inorganic substances. Hence, chemical cleaning is carried out once in two to three months

for removing substances polluting and clogging the membranes. Normal cleaners used are

sodium hypo chloride and citric acid.

Preventive measures to Avoid Leaching

Treated sewage from Sewage Treatment Plant will be conveyed to Treated Sewage Tank

through pipelines. All the joints from piping system will be checked periodically and

carrying treated wastewater pipes will be laid in conduits wherever road crossings are

expected. Thus no leaching of treated sewage into nearby water courses shall take place.

Figure 1: Schematic Diagram of MBR Technology STP

Supervisors will be employed for overall operation & maintenance of water supply, waste

water treatment and other utility services

Effluent treatment technology

The design of effluent network shall be done in accordance with the CPHEEO guideline,

NBC guidelines and reverent Indian Standards. ETP of 98 KLD shall be installed for

hospital wastewater.

The main objective of Effluent Treatment Plant (ETP) is to remove as much of the

suspended solids and organic matter as possible before the waste water is discharged back to

the environment. When untreated wastewater mixes with groundwater it can create

significant health risks by causing serious infectious diseases to people who have suppressed

immune systems.

1. Preliminary Stage: This stage is also called as pretreatment which is the most essential

treatment process in most of the ETP. It involves bar screens which comes in variety of

shapes and sizes to remove large sized suspended solids like paper, plastics, metals, debris,

rags and many such from incoming raw wastewater/sewage. If these materials are not

removed then they may cause serious damage to plant equipment’s. When wastewater

enters into grit chamber, it slows down the flow of water and thereby removes sand, grit,

sand stones and this process is called as sedimentation.

2. Primary Stage: It uses physical and chemical methods to improve the quality of the

wastewater which was not achieved in previous stage. When wastewater enters to

sedimentation tank or primary clarifiers, heavier solid particles settle to the bottom of the

tank and lighter particles will float up and will be skimmed off from top of the surface using

a process called skimming and thereby removing 60-65% of total suspended solids from

liquid wastewater. This stage may use grit chamber to remove grit. The settled solid is

known as primary sludge which will send to sludge digester for further processing. Now

partially clarified water flows on to the next stage.

3. Secondary Stage: This is the stage which can remove about 80-90% of organic matter by

using a process called biological treatment methods. Most of the hospital ETP uses

“activated sludge process” in which liquid wastewater enters into aeration tank where

wastewater mixes with air to encourage the growth of microbes and hence breakdown of

organic matter takes place. When aerated water enters into secondary clarifier, floatable

matter will be removed and heavier matter settles to bottom which is called as “active

sludge” or secondary effluent. Part of the sludge which still contains microbes will be re-

circulated back to aeration tank to increase the rate of organic matter decomposition. The

left over microorganisms are handled separately in next stage called disinfection.

4. Tertiary stage: This is the final stage which is also known as disinfection stage. This stage

removes any residual suspended solids and other materials which were not removed in

previous stages. The effectiveness depends on the quality of the water being treated. The

major objective of disinfection is to reduce number of microorganisms in the waste water to

be disposed into the natural environment. Disinfection technologies consist of ozone,

chlorine, and Ultraviolet (UV) rays to eliminate toxic chemicals that exist in the wastewater.

This stage removes nitrogen, phosphorous and other toxic contaminants.

Figure 2-Conventional treatment process in ETP

4. Details that the prescribed land use of the area is as per the master plan. (The surrounding area appears to be residential) and is the hospital permitted in the area by the competent authorities.

Reply- It is super specialty Govt. hospital having existing facility of 200 beds, The Hospital started

in the Year 2003 and began with Out Patient Services. Gradually Emergency services and

inpatient services were initiated along with ancillary services such as radiology and laboratory, the

land was allotted for the public facility by DDA.

Annexure 3- DUAC approval letter

5. Details of plans to ensure that infectious chemicals and contagious pathogens are not allowed to come in contact with patients/workers/staff and general public during disposal, recycle, reuse, or use in dual plumbing and flushing

Reply- Agreed, It will be ensured that infectious chemicals and contagious pathogens are not

allowed to come in contact with patients/workers/staff and general public during disposal,

recycle, reuse. For the infectious wastewater from the hospital shall be treated in an in house ETP

and after the tertiary treatment, wastewater shall be discharged to the nearby municipal sewer.

However General wastewater from the block shall be treated in in an in-house STP and after

primary secondary and tertiary treatment, treated water shall be re-use for flushing, horticulture,

HVAC cooling and other miscellaneous purposes.

Annexure 4- dual Plumbing plan is attached

6. Proposals to implement the provisions of the noise rules, and its amendments regarding establishing silence zones around the hospitals

Reply- Necessary measures shall be taken.

7. The certificate shall be obtained from the local body supplying water, specifying the total annual water availability with the local authority, the quantity of water already committed, the quantity of water allotted to the project under consideration and the balance water available. This should be specified separately for ground water and surface water sources, ensuring that there is no impact on other users.

Reply- As the project is already in operational stage since 2003, for the existing project main

source of water is DJB, and no groundwater is being abstracted. However for the expansion site,

Source shall be DJB only. No groundwater shall be abstract during construction as well as

operational stage.

Water bill from DJB is attached as ANNEXURE- III

Annexure 5- DJB bills are attached for the existing facility

8. The air quality index shall be calculated for base level air quality

Reply- Air quality monitoring and analysis has been done by NABL accredited lab.

Annexure 6- Lab data is attached

9. A detailed report on compliance to ECBC 2017 norms Reply- Detailed ECBC compliance Report for the proposed hospital project is attached

Annexure 7- ECBC compliance report

10. Plan for corporate environment responsibility as specified under MoEF&CC memorandum shall be prepared and submitted.

Reply- Corporate Environment Responsibility as specified under MoEF & CC has been prepared.

Annexure 8- CER affidavit

Approval Letter

To,

VIKRAMJIT SINGH BHARAJ A-15, PAMPOSH ENCLAVE,G.K.-1, NEW DELHI -110048

OL-14061727020No. : Date : 03/08/2017

Code : 14061727062

fo"k; % ADDITION AND REMODELLING WORK FOR BHAGWAN MAHAVIR HOSPITAL, PITAMPURA, NEWDELHI

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Decisions:

Concept of the proposal accepted.

Observations:

1. The proposal was submitted directly by thearchitects for conceptual consideration of theCommission online.2. The concept of the proposal was foundacceptable.

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1) VIKRAMJIT SINGH BHARAJ A-15, PAMPOSH ENCLAVE, G.K.-1, NEW DELHI -1100482) Health projects Division (North)PWD – G.N.C.T.DSector-6, Rohini, Delhi- 110085

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I

GOVERNMf NT OF THE NATIONAL CAPITAL TERRITORY OF DELHI OFF ICE OF HfE MEDICAL SUPERINTENDENT

13HAGWAN MAHAVIR HOSPITAL PITAM PURA: DELHI - 110 034

Nn I 2 ( Hfl )/20011/DI f',/13M If/ Ar.c t 'i Da ted:

SANCTION ORDER No. r-

TltP l'.XpPnditure Si.l nct ion of Rs.9,27,639/- (Rupees Ni e Lakh Twenty Seven Thousand

.-1 nd Six Hundred Thirty Nine Only). is accorded by the competent authority in con nection w ith

pr1y111 P 11t l n Delhi Jal Board agilins t Rill No. 749077065344 issuing date 10/07/2018 for the period of

03/06/18 to 04/07/2018 .

The r ro rosal has been exa mined by the accounts fun ct ionary. The expenditure on this account is

cJ pb it ahle to th1~ major head "2210" 01 110 29 00 (13) OE Bhagwan Mahavir Hospital under demand No.

7 for the yr.ar 2018-19 and will _not exceed the fund s placed as the disposal of the scheme.

No F 2(80)/2004/DHS/BMH/Accts

Cory to :-

1. PAO XXV, Peera Garhi, Delhi.

2. DDO, BMH (with one spare copy) .

3. Dte . Of Audit , GNCTD

4. Guard file .

(DR . AJAY KUMAR GUPTA) HEAD OF OFFICE

Dated :

(DR. AJAY KUMAR GUPTA) HEAD OF OFFICE

- -- - -I ~

Delhi Jal Board --7 ( ) (Government ol NC T of Doi hi) -8 'lTI~ • ~~~------- HQ V;uunalaya Phase 11 , Karol Bagh, New Delhi - 110005

~--:-:~-'t Regu la r Wate r 8111 ,:m; Ir-~ PTTT•cTT ,/;'\ J!Yl

- - -'-- ---N.im o . THE ME DICAL SUPDT Consumer Category : CAT II Bill Date I C, 0\/1 O F NC T) Premise Detail : (No of lloo rs -1) 1 0-JUL-2018 Address · BHAGWAN MAHAVIR Water Usage : DELHI Bill Amount (Rs .) I •OS P ITAL H(4 -5 ),RD N0 .-43 , P IT AM GOVT .HOSPITAL/DISPENSARY 927639 PURi\ Delhi Meter No.: NA74 90770000 -

I Meter Type (DJB/Pvt) : PVT

Bill Due Date

1 Mobile No.: 9 899626367 Meter Size (mm) : 15 27-JUL-2018

I Zone/MR Code : NW3/ 193/BULK Bill No.: 749 077065344 Amount Paya ble After Due Date(Rs .)

Arc a Code : A- 1/Kanhaiya Nagar Bill Cycle : ZALL(B4 -2018 ) (5•4 ,urch.argo wlll bo .,ppllc4Jblo .J ft or duo t.l.ilo )

974021 I Old WCN : 92 112 Bill Basis : REGULAR If bill is not pa id till Bill Duo Dato-New KNO: 7490770000

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8 111 Details : Curre nt Pe riod ChArQes (OJ-J UN-2018 to 04 -JUL -20 18) Appllcablc Rate Period Doscrlpllon Amount(Rs .) 0-1 JUN-.'01 8 to 04-JUL-2018 Tot;il Consurnplion Chnrgos 569235 96 04 JUN-20 1~ lo 04-JUL-20 18 Soworogo Ch;_1rgo (60 % ol W~\or Consump1,on Chaigo ) 34 1541 50 (l ,J.JUN 20 '8 lo Qd.JUL-20 18 Service C,,argu . Consump11on > 100 KL 1361 61 (} l JUti-2018 tc, 04-JUL-201 8 Additiona l Sowc r.tgo Ma,ntcnanco Chnrgo for Ho~p,tals.lNH 15500 00 n-1 I\IN-701A In 04.JUL,2018 Subtotal 13111 Amount ')27639 15

Ad1uslnion1 Dc1a,1s Alo t. ,slod Below

I

>-Arrear. If any (Rs.) -0 .60

Opening Balance/Adjustment, If any (Rs .) 0

Total Consolidated Bill Amount Payable (Rs.) 927.§l9

Late Payment Surcharge (Rs .) 46381 .93 I Amount with LPSC (Rs .) 974021 81II History Payment Hi story

IJ I\\ Id Bill from Date BIii to Dale No ol Days Amount(Rs) Un\\s R•celpl Id Am ou nttR•J D:1tc 74 ~70)26987 04 -MAY-2016 03.JUN-2018 30 73607 1 2604 74907 /059506 736071 00 02-JUL-2016 , , 0 onao31 °o 03-t,Pf'l -7018 04-MAY-201 8 31 6066 19 2143 749077025728 60661 9 00 30-MAY-20 18 /JOM976,c,J9 OP,1AR,?018 03-APR-201 6 33 338435 11 86 749077088106 338435.00 03-MAY-2018 1400 795J5224 31 -JAN-201 8 01-MAR-?01 8 29 291510 1023 74 9077051 428 291510,00 23-MAR-2018 /0'1071 )409?7 0·1-JAN-201 A 3 1.JAN-20 18 27 246320 1028 749077086187 24 6320 00 06-MAR-20 18

Important Message U-.. r- , ... , online boosteir not only mcreasus cllance of water con1a,n,nat1on but also increases !ho llill Please do not use onlme boos ter

-..:..2:. Delhi Jal Board

-7 ?\"' Bill Payment Counter Foil (9--=-:-=:___:.. 1::rfTT! ~,==-t~:i'

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New KNO 7,190770000 Name THE MEDICAL SUPDT (GOVT Bill No, 749077065344 I OF NC T )

B111 Date 10-JUL-20 18 Bill Due Date 27-JUL-20 18 Bill Amoun t (Rs.) 927639

Bil l Amount with LPSC (Rs .): 974021 Payme nt Dale/Amount Paid(Rs.) Cash/Cheque No./0D No .: )

ll 11 Jlllll II. U II• 11:IIJ ll llll lJl!~lmll!ll ll ll~U IIDl!il:ll ll1ill· Name of Bank / Branch r

I I Srn·,co Cycle ZALL Service Route 1 Route Sequence I 92 - -

WEATHER:

ENERGY CONSERVATION AND

BUILDING CODE

Bh

agw

an

Ma

ha

vir H

osp

ital

ASSUMPTIONS:

S. NO. MODEL

INPUT

PARAMETER

S

PROPOSED CASE

1. Exterior Wall

Construction240 mm AAC Block

(U-Value = 0.67 W/m²·°C)

2. Roof

Construction

240mm RCC slab with 120mm Brick Bat Coba

(U – Value = 2.4 W/m²·K)

3. Glazing For Residential : U - factor: 5.6 W/m² mK SHGC : 0.25

4. Shading devices Shading Devices - As per design

5. Lighting Power

Density

[As per ECBC Standard]

Spaces: 7.5 w/sq.m.

Kitchen: 12.9 W/sq.m.

Toilet : 1.5 W/sq.m.

Corriodor : 4.32 W/sq.m. (20% Reduction in common

spaces)

Stairs : 5.2 W/sq.m. (20% Reduction in common spaces)

Parking : 1.76 W/sq.m. (20% Reduction in common

spaces)

ENERGY CONSERVATION AND

BUILDING CODE

Bh

agw

an

Ma

ha

vir H

osp

ital

ASSUMPTIONS: S. NO. MODEL

INPUT

PARAMETER

S

PROPOSED CASE

9 Occupancy

Sensors

Provided

10 Daylight

Sensors

Provided

11 HVAC System

TypeAir Cooled Unitary

Packaged Terminal Air Conditioner

12 Cooling

EquipmentCategory: PTAC

COP : 3.52

13 Coil Capacity Cooling Coil Capacity : 100

Heating Coil Capacity : 100

14 Heating

Equipment

Electric Resistance

15 Base Utility Type: Elevators

Hourly Consumption: 60.0 kW

16 Utility Rates 5.25 Rs/ kWH

ENERGY CONSERVATION AND

BUILDING CODE

Bh

agw

an

Ma

ha

vir H

osp

ital

CONCLUSIONS:

• Criteria 8

- 7Points are being achieved in Criteria 8 due to achievement of benchmark

Energy Performance Index and EPI reduction of 48.7% over the base case.

Percentage Energy Performance Index Points

10% reduction from benchmark (Mandatory) 2

20% reduction from benchmark 3

30% reduction from benchmark 5

40% reduction from benchmark 7

50% reduction from benchmark 10

ENERGY CONSERVATION AND

BUILDING CODE

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1) ECM’S

2) Envelope Details

3) Sectional Details

4) Schedules

5) External Lighting Calculation

ANNEXURE:

ENERGY CONSERVATION AND

BUILDING CODE

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ENERGY CONSERVATIVE METHODS (ECM’S):

The proposed building achieves energy reduction by following

ECM’s

1. Efficient HVAC systems.

Residential Area – PTAC COP 3.5

2. Good envelope properties for wall, Roof and Glazing

Wall - 240 mm AAC Block (U-Value = 0.67 W/m²·°C)

Roof - 150mm RCC slab with 120mm Brick Bat

(U – Value = 2.2 W/m²·)

Glazing - U value for Residential = 1.6 W/m²·°C, VLT =

33%

3. Shading devices – As per Design.

ENERGY CONSERVATION AND

BUILDING CODE

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ENVELOPE DETAILS:

WALLS

ROOF

GLASS For Residential : U - factor: 5.6 W/m² KSHGC: 0.82

Autoclaved Aerated Concrete Blocks (AAC)

Material DescriptionThickness

(mm)Conductivity (w/m.c)

Resistance (m2.C/W)

Outside Surface Resist. 0.059

External Plaster (Cement plaster, sand

aggregate)16 0.72 0.027777778

AAC Block 240 0.17 1.212

Internal Plaster (Gypsum plaster, sand

aggregate)12 0.22 0.063636364

Inside Surface Resist. 0.121

R-Value 1.48U-Value 0.674

Roof

Material DescriptionThickness

(mm)Conductivity (w/m.c)

Resistance (m2.C/W)

Outside Surface Resist. 0.05864

China Mosaic 50 1.5996 0.031257814

20mm Mortar 20 0.72702 0.02750956

40mm Screed 40 0.72 0.055555556

40mm Screed 40 0.72 0.055555556

Brick Bat Coba 120 0.811 0.147965475

150mm RCC 150 1.4 0.107142857

Inside Surface Resist. 0.12063

R-Value 0.60U-Value 2.2

ENERGY CONSERVATION AND

BUILDING CODE

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ECBC COMPLIANCES. NO. MODEL INPUT

PARAMETERS

PROPOSED CASE

1. Exterior Wall Construction 240 mm AAC Block (U-Value = 0.67 W/m²·°C)

2. Roof Construction (Hall) 240mm RCC slab with 120mm Brick Bat Coba

(U – Value = 2.2 W/m² K)

3. Glazing Glazing properties: DGU: U - factor: 5.6 W/m²·mK SHGC : 0.82

4. Shading devices Shading Devices - As per design

5 Occupancy Sensors Provided

6 Daylight Sensors Provided

7 HVAC System Type Water Cooled Central Plant

8 Cooling Equipment Water Cooled Centrifugal Chiller , COP : 6.3

9 Coil Capacity Cooling Coil Capacity : 100

Heating Coil Capacity : 100

10 Heating Equipment Electric Resistance

11 Base Utility Type: Elevators ,Hourly Consumption: 60.0 kW

12 Utility Rates 5.25 Rs/ kWH

13 Solar Water heating Solar Cells –

A minimum of 20% of hot water required will be requirement will be met by solar

cells

13 Renewable Energy A total of 1.5% of the annual power consumption, will be met by solar energy

(i.e 25kVA)

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