NOVEC 1230 Total Flooding System_EGEC Calculations Sheet.xlsx

September 12, 2017 | Author: Hassan Adel Hassan | Category: Volume, Nozzle, Pressure, Pipe (Fluid Conveyance), Gases
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Computed By:

Project:

Checked By:

Date:

Approved By:

NOVEC 1230 Total Flooding System Calculations Hazard Area No.1 Protected Hazard Dimensions Name of Protected Hazard Area Height Area

Tel 3.0

m

100.0

m2

Volume

300

m3

Volume of Fixed Structures Impervious to Agent vapor

0.0

m3

Design Parameters Class of Fire Hazard Net Volume of Hazard Area Design Temperature in Hazard Area Agent Specific Volume @ 1 Atm. pressure

A 300.0 20 0.072

m3 o

C

m3/kg

Minimum Design Concentration

4.2

% per volume

Agent Design Concentration

5.4

% per volume

Tee Count of Piping System

6.0

Hazard Area Pressure

1.0

Design Safety Factor

0.02

atm

System Sizing Agent Net Capacity

243.0

kg

Computed By:

Project:

Checked By:

Date:

Agent Net Capacity Percentage Total Agent Flow Rate Required No. of discharge Nozzels Acual Flow per Nozzel

Approved By:

67 24.3

% kg/sec

3 8.1

kg/sec

Nozzel and Branch Pipe Diameters

1 1/2

inch

Main Pipe Diameter

2 1/2

inch

Computed By:

Project:

Checked By:

Date:

Approved By:

Hazard Area No.2 Protected Hazard Dimensions Name of Protected Hazard Area Height

elect 3.0

m

Area

50.0

m2

Volume

150

m3

Volume of Fixed Structures Impervious to Agent vapor

0.0

m3

Design Parameters Class of Fire Hazard Net Volume of Hazard Area Design Temperature in Hazard Area Agent Specific Volume @ 1 Atm. pressure

C 150.0 20 0.072

m3 o

C

m3/kg

Minimum Design Concentration

4.2

% per volume

Agent Design Concentration

5.4

% per volume

Tee Count of Piping System

6.0

Hazard Area Pressure

1.0

Design Safety Factor

0.02

atm

System Sizing Agent Net Capacity Agent Net Capacity Percentage

121.5

kg

33

%

Computed By:

Project:

Checked By:

Date:

Total Agent Flow Rate Required No. of discharge Nozzels Acual Flow per Nozzel Nozzel and Branch Pipe Diameters Main Pipe Diameter

Approved By:

12.1

kg/sec

2 6.1

kg/sec

1 1/2

inch

2

inch

Computed By:

Project:

Checked By:

Date:

Approved By:

Combined System Sizing Agent Total Net Capacity

364.5

Container Size Selection

Container Size 900 Ib

Total Required No. of Containers

kg

1

Agent Net Capacity in Each Container

364.5 803.5

kg Ibs

Total Agent Flow Rate

36.4

kg/sec

Maximum Agent Flow Rate per Nozzel

9.07

kg/sec

Total Required No. of discharge Nozzels

5

System Main Pipe Diameter

3

inch

Checking Agent Concentration in a Combind Space with Directional Valve Name of Protected Hazard Area Height Area

Tel 3.0

m

200.0

m2

Volume

600

m3

Volume of Fixed Structures Impervious to Agent vapor

0.0

m3

Design Parameters Class of Fire Hazard Minimum Design Concentration Net Volume of Hazard Area

B 4.2 600.0

% per volume m3

Computed By:

Project:

Checked By:

Date:

Design Temperature in Hazard Area Agent Specific Volume @ 1 Atm. pressure

Approved By:

27 0.074

Tee Count of Piping System

6.0

Hazard Area Pressure

1.0

Design Safety Factor

0.02

Agent Design Concentration

4.2

o

C

m3/kg

atm

%

Computed By:

Project:

Checked By:

Date:

Approved By:

General Design Considerations - Max. No. of Nozzels in the System - Maximum Agent Flow Rate per Nozzel - Maximum Discharge Time - Nozzel Maximum Coverage Radius - Min. Nozzel Pressure - Maximum Ceiling Height - Nozzel Max. Distance from Ceiling - False Ceiling or Raised Floor Min. Height - Space Min. agent percentage in combind system

20 9.07 10 8.70 10.90 73 4.87 0.30 0.30 10

kg/sec sec m psi m m m %

- Beams that are less than 0.3 m below the slab need not be considered. Obstructions greater than 300 mm (12”) can affect the distribution of agent and may require additional nozzles. - The max. elevation difference between the container outlet and the furthest horizontal pipe run or discharge nozzle (whichever is furthest) shall not exceed 9.1 m.

- The max. elevation difference between the furthest horizontal pipe runs or discharge nozzles (whicheve is furthest) shall not exceed 9.1 m. - The agent design concentration shall be checked to insure that it is under NOAEL at maximum anticipated temperature in the hazard space. - Sizing is based on NFPA-2001

Eng. H.S & E.S Eng. M. Gamal Dr. H. Soliman

em Calculations

1076.4

ft2

535.7

Ibs

ّّ

Eng. H.S & E.S Eng. M. Gamal Dr. H. Soliman

Accepted 53.6

Ibs/sec

17.9 Ibs/sec

3

Eng. H.S & E.S Eng. M. Gamal Dr. H. Soliman

538.2

ft2

267.8

Ibs

ّّ

Accepted

Eng. H.S & E.S Eng. M. Gamal Dr. H. Soliman

26.8

Ibs/sec

13.4 Ibs/sec

2 1/2

Eng. H.S & E.S Eng. M. Gamal Dr. H. Soliman

803.5

Ibs

Minimum Fill ###Ibs 455

Accepted 80.4

Ibs/sec

20

Ibs/sec

Accepted 3

with Directional Valve

2152.8

ft2

Eng. H.S & E.S Eng. M. Gamal Dr. H. Soliman

Accepted

Eng. H.S & E.S Eng. M. Gamal Dr. H. Soliman

20

Ibs/sec

360o Nozzel Type 180o Nozzel Type

dered. Obstructions greater than 300 onal nozzles.

e furthest horizontal pipe run or

e runs or discharge nozzles (whichever

s under NOAEL at maximum

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