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PROCESS CALCULATION CENTRAL REGION PROJECTS DIVISION

WASEA BULK PLANT

WASEA

SAUDI ARABIAN OIL COMPANY

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EDSD/2616-0399.doc

Saudi Aramco 2616-ENG (03/99)

PR-CAL-001

SAUDI ARABIA

REV.NO.SHT.NO.DRAWING NO.INDEXPLANT NO.DWG.TYPE

PROCESS CALCULATION

WASEA BULK PLANT

BI-10-00795

ISSUED FOR CONSTRUCTION

DECEMBER 2010

PREPARED BY:

A. Al-Saihati, A. Fattani & O. Al-Othman Consulting Engineering Co.

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WASEA BULK PLANT

WASEA


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EDSD/2616-0399.doc


PR-CAL-001

SAUDI ARABIA


TABLE OF CONTENTS

TABLE OF CONTENTS ......................................................................................................... 21.0 INTRODUCTION ........................................................................................................ 32.0 FOAM WATER SYSTEM FOR LOADING RACK AREA ........................................... 33.0 FOAM WATER SYSTEM FOR PUMP STATION AREA- DIESEL ............................ 54.0 OILY WATER SUMP CALCULATION ....................................................................... 65.0 DIESEL LOADING PUMPS ........................................................................................ 86.0 GASOLINE LOADING PUMPS .................................................................................. 97.0 DIESEL INTERFACE PUMPS .................................................................................. 108.0 GASOLINE INTERFACE PUMPS ............................................................................ 119.0 GASOLINE/DIESEL INTERFACE PRODUCT BULK TRANSFER PUMPS............ 1210.0 OILY WATER SUMP PUMPS (TANK AREA): ........................................................ 1310.1 OWS Maximum Flow Pumps: ................................................................................ 1311.0 OILY WATER FEED PUMPS ................................................................................... 1512.0 RECOVERED OIL PUMPS ...................................................................................... 1613.0 RECOVERED OIL TRANSFER PUMP .................................................................... 1714.0 SANITARY SUM PUMPS ......................................................................................... 1815.0 POTABLE WATER PUMPS ..................................................................................... 2016.0 FIRE WATER FEED PUMPS ................................................................................... 2117.0 ATTACHMENTS ....................................................................................................... 22

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WASEA


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EDSD/2616-0399.doc


PR-CAL-001

SAUDI ARABIA


1.0 INTRODUCTION

This project provides a new grass roots bulk plant, named as WASEA Bulk Plant in the South Western corner of the Saudi Aramco land reservation at EWPS #3. This bulk plant will originally supply regular gasoline (91RON) and Ultra low sulfur diesel. It will ultimately supply two grades of gasoline and two grades of diesel. Although the initial demand at start-up will be approximately 185 MBD, this plant is being designed for a demand of 250 MBD in the year 2019.

This project will also install a 16-inch diameter nozzle on DR-1 pipeline and a 16-inch transfer line from the DR-1 pipeline to the pipeline receiving station in the Tank Farm Area of the WASEA Bulk plant for gasoline supply. A 20-inch transfer line from the DR-2 pipeline to the pipeline Receiving Station in the Tank Farm Area of the bulk plant will also be provided by this project for diesel supply.

The design calculation report includes pump head, pressure drop, line velocity, size and motor rating calculations.

2.0 FOAM WATER SYSTEM FOR LOADING RACK AREA

Minimum Foam Solution Flow Rate : Firewater demand for MRA as per 5.6.2 of SAES-B-017 = 0.1 L/m2-sec Width of diesel loading rack canopy = 20 m Length of diesel loading rack canopy = 40 m Area of diesel loading rack canopy = 800 m2 Minimum firewater flow required = 80 L/ sec = 1268 GPM Foam Water Flow Based on Sprinklers: (5 Bays Rack Max.) Width of diesel loading rack canopy = 20 m Length of diesel loading rack canopy = 40 m Maximum allowable spacing between foam spray heads shall be 3m as per SAES-B-070 Space between branches = 2.8 m Distance between Sprinkler = 2.8 m Protection area per sprinkler = 7.84 m2 Number of sprinkler required = 102 Sprinkler Number of branches = 14.29 Branches

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WASEA


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EDSD/2616-0399.doc


PR-CAL-001

SAUDI ARABIA


Number of sprinkler per branch = 7.143 Sprinkler Residual pressure = 30 PSI K Factor = 3 Flow per sprinkler = 17.32 GPM Total foam water flow anticipated to 5 bays rack = 1767 GPM Assume 20% excess = 2121 GPM Foam Conc. Discharge Rate: Foam conc. discharge rate = 63.63 GPM 3% Fluroprotein foam conc. Add 20% excess = 76.35 GPM Selected foam concentrate pumps capacity = 90 GPM Foam Concentrate Quantity: The foam supply shall be sufficient for 20 min. as per SAES-B-070 Foam concentrate quantity = 1527 Gallons Add 15% excess = 1756 Gallons Provided 2000 Gallons (Net capacity) foam concentrate tank Fire Water Discharge Rate: Fire water discharge rate = 2057 GPM (Fire water % = 97%) Line Size Calculation & Delivery Time: Nos. of Bays = 5 Line size (inch) Inner Dia.

Flow GPM

Vel. (Ft/Sec)

L (Ft) Time (Sec)

10 7.981 2121 13.61 600 44.08 8 3.068 1000 43.44 30 0.69 6 2.067 500 47.83 15 0.31

Calculated delivery time to reach the sprinkler = 45 Seconds Delivery time is within one minute from activation of the hand station or heat detector as per SAES-B-070. This will be verified by Fire Water System Design Vendor.

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EDSD/2616-0399.doc


PR-CAL-001

SAUDI ARABIA


3.0 FOAM WATER SYSTEM FOR PUMP STATION AREA- 16 DIESEL PUMPS

Minimum Foam Solution Flow Rate : Firewater demand for MRA as per 5.6.2 of SAES-B-017 = 0.34 l/m2-sec Width of diesel loading rack canopy = 7 m Length of diesel loading rack canopy = 60 m Area of diesel loading rack canopy = 420 m2 Minimum firewater flow required = 142.8 L/ sec = 2263.4 GPM Foam Water Flow Based on Sprinklers : Width of diesel loading rack canopy = 7 m Length of diesel loading rack canopy = 60 m Maximum allowable spacing between foam spray heads shall be 3m as per SAES-B-070 Space between branches = 2.8 m Distance between Sprinkler = 2.8 m Protection area per sprinkler = 7.84 m2 Number of sprinkler required = 53.571 Sprinkler Number of branches = 21.429 BranchesNumber of sprinkler per branch = 2.5 Sprinkler Residual pressure = 30 PSI K Factor = 3 Flow per sprinkler = 17.321 GPM Total foam water flow anticipated to 6 bays rack = 927.88 GPM Assume 15% excess = 1067.1 GPM Foam Conc. Discharge Rate: Foam conc. discharge rate = 32.012 GPM 3% Fluroprotein foam conc. Add 20% excess = 38.414 GPM Selected foam concentrate pumps capacity = 90 GPM Foam Concentrate Quantity: The foam supply shall be sufficient for 20 min. as per SAES-B-070 Foam concentrate quantity = 768.29 Gallons Add 15% excess = 883.53 Gallons Provided 2000 Gallons (Net capacity) foam concentrate tank

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EDSD/2616-0399.doc


PR-CAL-001

SAUDI ARABIA


Fire Water Discharge Rate: Fire water discharge rate = 1035.1 GPM (Fire water % = 97%) Line Size Calculation & Delivery time:

Line size (inch) Inner Dia.

Flow GPM

Vel. (Ft/Sec)

L (Ft) Time (Sec)

6 6.065 1067 11.86 400 33.73 4 4.026 534 13.46 30 2.23 2 2.067 67 6.38 15 2.35

Calculated delivery time to reach the sprinkler = 38 Seconds Delivery time is within one minute from activation of the hand station or heat detector as per SAES-B-070. This will be verified by Fire Water System Design Vendor.

4.0 OILY WATER SUMP CALCULATION

As per section 8.6 of SAES-B-70, the sump is to be designed for at least 5 minutes

Foam water supply in the loading rack = 2120 GPM Hose reel allowance = 400 GPM Total fire water = 2520 GPM Total foam fire water in 5 minutes = 12600 Gallons

Drain from OME building is Wash down assumed = 40 cu m / month = 1.33 cu m/day = 0.24 GPM (Neglected) Drain from the tank 0.05% of turnover of WASEA = 2.17 GPM (Neglected) (Drainage of water from the tank farm area although done on a periodic basis is negligible)

As per section 8.6 of SAES-B-70, the sump is to be designed for also emergency drain of truck, So Capacity of one truck = 32000 Liter

= 8465.61 Gallons

Effective capacity of sump = 21065.61 Gallons = 79.74 m3

Consider 20% margin = 95.69 m3

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EDSD/2616-0399.doc


PR-CAL-001

SAUDI ARABIA


Sump inside dimensions

Length (Assumed) = 7.62 m Width (Assumed) = 7.62 m Area = 58.06 m2 Effective depth required (say) = 1.65 m

Consider a min. level for stop pump Low level alarm = 1 m

Inverted depth = 3.01 m High High alarm above pump start = 0.3 m

Depth of pit = 5.96 m

Cross Check with new dimension Volume = 95.6904 m3

OWS System: Capacity of maximum flow pump 3000 GPMCapacity of minimum flow pump 300 GPM

Capacity check of sump based on larger capacity pump (Max Flow Pump) per 4.14.7 of SAES-B-20

v = Ct x Q /4

Where: V = Minimum required capacity m (gallons)

CT = Minimum time in minutes of one pumping cycle between successive motor starts. Minimum CT shall be 15 minutes

Q = Maximum flow pump capacity, m/min (gallon/minute), or increment in pumping capacity when multiple operating pumps are used

CT = 15 Q = 3000

Put all value V = 11250 Gallons

Which is less than the effective sump capacity

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OPERATIONS

CERTIFIED

8

OF 406

DOCX12 A

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10-00795-0002

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-045

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YSY

12/10

SHK

12/10

12/10

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WASEA BULK PLANT

WASEA


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EDSD/2616-0399.doc


PR-CAL-001

SAUDI ARABIA


5.0 DIESEL LOADING PUMPS

Velocity:

Noofpumps = 16Flowthroughonepump = 1200 GPMTotalflow = 19200 GPMSuctionheader = 36 inchVelocity = 1.96 m/sIndividualSuctionLine = 10 inchVelocity = 1.51 m/sIndividualDischargeLine = 8 inchVelocity = 2.39 m/sDischargeHeader = 30 inchVelocity = 2.85 m/s

NPSHAvailable:

Specificgravity = 0.84 Atmospherepressure = 101.3 Kpa Vapor pressure = 8.00 Kpa Suctionpressure = 95.61 Kpa Suctionpressureat120%flow = 81.67 Kpa NPSHa = 10.43 mNPSHaat120%flow = 8.77 m

MotorRating:

Pumpefficiencyassumed = 70 %Pressuredifferential = 512 Kpa Duty = 76 hp15%allowance = 87.4 hpMotorRating = 90 hp(LinePressureDropandPumpHeadcalculationsattached)

DES

CR

IPTI

ON

RE

VN

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JO/E

WO

DAT

EO

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GG

PMT

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DATE:

DATE:

DATE:

DATE:

DATE:

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TE:

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:

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PROJECTENGINEER

CONSTRUCTIONAGENCY

DISCIPLINEENGINEER

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(DC

C) N

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____

____

____

____

OPERATIONS

CERTIFIED

9

OF 406

DOCX12 A

JO / EWO:

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10-00795-0002

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0002

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YSY

12/10

SHK

12/10

12/10

12/10

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12/10

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MQ

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10-0

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WASEA BULK PLANT

WASEA


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EDSD/2616-0399.doc


PR-CAL-001

SAUDI ARABIA


6.0 GASOLINE LOADING PUMPS

Velocity:

Noofpumps = 12Flowthroughonepump = 1200 GPMTotalflow = 14400 GPMSuctionheader = 36 inchVelocity = 1.50 m/sIndividualSuctionLine = 10 inchVelocity = 1.54 m/sIndividualDischargeLine = 8 inchVelocity = 2.45 m/sDischargeHeader = 30 inchVelocity = 2.16 m/s

NPSHAvailable:

Specificgravity = 0.76Atmospherepressure = 101.30 Kpa Vapor pressure = 69.00 Kpa Suctionpressure = 115.90 Kpa Suctionpressureat120%flow = 111.60 Kpa NPSHa = 6.17 mNPSHaat120%flow = 5.61 m

MotorRating:

Pumpefficiencyassumed = 70 %Pressuredifferential = 435.5 Kpa Duty = 65 hp15%allowance = 74.75 hpMotorRating = 75 hp(LinePressureDropandPumpHeadcalculationsattached)

DES

CR

IPTI

ON

RE

VN

O.

JO/E

WO

DAT

EO

PRN

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PMT

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DATE:

DATE:

DATE:

DATE:

DATE:

DA

TE:

BY

:

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NTR

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NU

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PROJECTENGINEER

CONSTRUCTIONAGENCY

DISCIPLINEENGINEER

VE

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(DC

C) N

O. _

____

____

____

____

____

OPERATIONS

CERTIFIED

10 OF 406

DOCX12 A

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10-00795-0002

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0002

-045

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YSY

12/10

SHK

12/10

12/10

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MQ

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10-0

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WASEA BULK PLANT

WASEA


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EDSD/2616-0399.doc


PR-CAL-001

SAUDI ARABIA


7.0 DIESEL INTERFACE PUMPS (WILL BE CONFIRMED AFTER SURGE STUDY)

Velocity:

No of pumps = 21 + 1 Stand By Flow through one pump = 22 GPM Suction Line = 2 inch Velocity = 0.65 m/s Discharge Line = 2 inch Velocity = 0.66 m/s

NPSH Available:

Specific gravity = 0.84Atmosphere pressure = 101.3 KPA Vapor pressure = 8.00 KPA Suction pressure = 98.8 KPA Suction pressure at 120 % flow = 94 KPA NPSHa = 10.80 m NPSHa at 120 % flow = 10.24 m

Motor Rating:

Pump efficiency assumed = 75 % Pressure differential = 456 Kpa Duty = 1.16 hp 15% allowance = 1.33 hp Motor Rating = 1.5 hp (Line Pressure Drop and Pump Head calculations attached)

DES

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IPTI

ON

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VN

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JO/E

WO

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EO

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SEN

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DATE:

DATE:

DATE:

DATE:

DATE:

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TE:

BY

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PROJECTENGINEER

CONSTRUCTIONAGENCY

DISCIPLINEENGINEER

VE

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TIF

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(DC

C) N

O. _

____

____

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____

____

OPERATIONS

CERTIFIED

11 OF 406

DOCX12 A

JO / EWO:

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10-00795-0002

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YSY

12/10

SHK

12/10

12/10

12/10

DCO

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12/10

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MQ

DC

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10-0

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02

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00


WASEA BULK PLANT

WASEA


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EDSD/2616-0399.doc


PR-CAL-001

SAUDI ARABIA


8.0 GASOLINE INTERFACE PUMPS (WILL BE CONFIRMED AFTER SURGE

STUDY) Velocity:

No of pumps = 21 + 1 Stand By Flow through one pump = 22 GPM Suction Line = 2 inch Velocity = 0.59 m/s Discharge Line = 2 inch Velocity = 2.58 m/s

NPSH Available:

Specific gravity = 0.76Atmosphere pressure = 101.3 KPA Vapor pressure = 79.00 KPA Suction pressure = 101.6 KPA Suction pressure at 120 % flow = 100 KPA NPSHa = 2.97 m NPSHa at 120 % flow = 2.76 m

Motor Rating:

Pump efficiency assumed = 75 % Pressure differential = 450 KPA Duty = 1.02 hp 15% allowance = 1.18 hp Motor Rating = 1.5 hp (Line Pressure Drop and Pump Head calculations attached)

DES

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DATE:

DATE:

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DATE:

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PROJECTENGINEER

CONSTRUCTIONAGENCY

DISCIPLINEENGINEER

VE

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CE

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(DC

C) N

O. _

____

____

____

____

____

OPERATIONS

CERTIFIED

12 OF 406

DOCX12 A

JO / EWO:

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10-00795-0002

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0002

-045

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YSY

12/10

SHK

12/10

12/10

12/10

DCO

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12/10

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MQ

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FO

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10-0

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02

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00


WASEA BULK PLANT

WASEA


THIS

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EDSD/2616-0399.doc


PR-CAL-001

SAUDI ARABIA


9.0 GASOLINE/DIESEL INTERFACE PRODUCT BULK TRANSFER PUMPS (Worst Case for Gasoline)

Velocity:

No of Pumps = 21 Gasoline and 1 Diesel Flow through one pump = 50 GPMSuction Line = 6 inch Velocity = 0.62 m/s Discharge Line = 4 inch Velocity = 1.4 m/s

NPSH Available:

Specific gravity = 0.76Atmosphere pressure = 101.3 KPA Vapor pressure = 79.00 KPA Suction pressure = 109.6 KPA Suction pressure at 120 % flow = 95 KPA NPSHa = 4.03 m NPSHa at 120% flow = 2.11 m

Motor Rating:

Pump efficiency assumed = 75 % Pressure differential = 229 KPA Duty = 4.70 hp 15% allowance = 5.41 hp Motor Rating = 5 hp (Line Pressure Drop and Pump Head calculations attached)

DES

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IPTI

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EO

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DATE:

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:

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DISCIPLINEENGINEER

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(DC

C) N

O. _

____

____

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____

____

OPERATIONS

CERTIFIED

13 OF 406

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10-00795-0002

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YSY

12/10

SHK

12/10

12/10

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WASEA BULK PLANT

WASEA


THIS

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EDSD/2616-0399.doc


PR-CAL-001

SAUDI ARABIA


10.0 OILY WATER SUMP PUMPS (TANK AREA): 10.1 OWS Maximum Flow Pumps:

Velocity:

No of Pumps = 21 + 1 Stand By Flow through one pump = 3000 GPM Suction Line = 18 inch Velocity = 1.30 m/s Discharge Line = 16 inch Velocity = 1.65 m/s

NPSH Available:

NPSHa = Pb-Vp-Ls-Hf Pb = Barometric pressure in feet absolute. Vp= Vapor pressure of the liquid at maximum pumping temperature, in feet absolute. Ls = Maximum static suction lift in feet. Hf = Friction loss in feet in suction pipe at required capacity

Pb = 14.7 psi = 33.95 ft

Vp = 1 psi = 2.31 ft

Ls = 19.68 ft Suction header pressure losses = 1.09 psi

= 2.52 ft NPSHa = 9.44 ft

Motor Rating:

Pump efficiency assumed = 50 % Pressure differential = 451 Kpa Duty = 228.00 hp 15% allowance = 262.20 hp Motor Rating = 260 hp (Line Pressure Drop and Pump Head calculations attached)

DES

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DATE:

DATE:

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PROJECTENGINEER

CONSTRUCTIONAGENCY

DISCIPLINEENGINEER

VE

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CE

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(DC

C) N

O. _

____

____

____

____

____

OPERATIONS

CERTIFIED

14 OF 406

DOCX12 A

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10-00795-0002

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YSY

12/10

SHK

12/10

12/10

12/10

DCO

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12/10

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MQ

DC

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10-0

0795

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02

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00


WASEA BULK PLANT

WASEA


THIS

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CO

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EDSD/2616-0399.doc


PR-CAL-001

SAUDI ARABIA


10.2 OWS Normal Flow Pumps:

Velocity:

No of Pumps = 21 + 1 Stand By Flow through one pump = 150 GPM Suction Line = 4 inch Velocity = 1.16 m/s Discharge Line = 4 inch Velocity = 1.17 m/s Discharge Line = 6 inch Velocity = 0.51 m/s

NPSH Available:


Pb = 14.7 psi = 33.95 ft

Vp = 1 psi = 2.31 ft


= 1.11 ft NPSHa = 10.85 ft

Motor Rating:


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RE

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DATE:

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DATE:

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:

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CONSTRUCTIONAGENCY

DISCIPLINEENGINEER

VE

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CE

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FIC

ATE

(DC

C) N

O. _

____

____

____

____

____

OPERATIONS

CERTIFIED

15 OF 406

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10-00795-0002

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YSY

12/10

SHK

12/10

12/10

12/10

DCO

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12/10

YS

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MQ

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10-0

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02

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WASEA BULK PLANT

WASEA


THIS

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EDSD/2616-0399.doc


PR-CAL-001

SAUDI ARABIA


11.0 OILY WATER FEED PUMPS

Velocity:

No of pumps = 21 + 1 Stand By Flow through one pump = 300 GPMSuction Line = 8 inch Velocity = 0.50 m/s Discharge Line = 6 inch Velocity = 1.03 m/s

NPSH Available:

Specific gravity = 1Atmosphere pressure = 101.3 Kpa Vapor pressure = 8.00 Kpa Suction pressure = 100.0 Kpa Suction pressure at 120 % flow = 98 Kpa NPSHa = 9.20 m NPSHa at 120 % flow = 9.00 m

Motor Rating:

Pump efficiency assumed = 75 % Pressure differential = 99.6 Kpa Duty = 3.60 hp 15% allowance = 4.14 hp Motor Rating = 5 hp (Line Pressure Drop and Pump Head calculations attached)

DES

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PR-CAL-001

SAUDI ARABIA


12.0 RECOVERED OIL PUMPS

Velocity:

No of Pumps = 21 + 1 Stand By Flow through one pump = 50 GPM Suction Line = 2 inch Velocity = 1.49 m/s Discharge Line = 2 inch Velocity = 1.49 m/s

NPSH Available:


Pb = 14.7 psi = 33.95 ft

Vp = 1 psi = 2.31 ft


= 4.73 ft NPSHa = 15.43 ft

Motor Rating:


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PR-CAL-001

SAUDI ARABIA


13.0 RECOVERED OIL TRANSFER PUMP

Velocity:

No of pumps = 1Flow through one pump = 200 GPM Suction Line = 6 inch Velocity = 0.69 m/s Discharge Line = 4 inch Velocity = 1.57 m/s

NPSH Available:

Specific gravity = 0.84Atmosphere pressure = 101.3 Kpa Vapor pressure = 8.00 Kpa Suction pressure = 94.9 Kpa Suction pressure at 120 % flow = 91.5 Kpa NPSHa = 10.35 m NPSHa at 120% flow = 9.94 m

Motor Rating:


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PR-CAL-001

SAUDI ARABIA


14.0 SANITARY SUM PUMPS

14.1 SANITARY SUM PUMPS (OPERATOR SHELTER AND INSPECTION

BUILDING)

Velocity:

No of pumps = 21 + 1 Stand By Flow through one pump = 50 GPMDischarge Line = 3 inch Velocity = 0.67 m/s

NPSH Available:

Specific gravity = 1Atmosphere pressure = 101.4 Kpa Vapor pressure = 8.00 Kpa Suction pressure = 101.4 Kpa NPSHa = 9.34 m

Motor Rating:


14.2 SANITARY SUM PUMPS (MAIN SANITARY LIFT STATION)

Velocity:


NPSH Available:

Specific gravity = 1

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PR-CAL-001

SAUDI ARABIA


Atmosphere pressure = 101.4 Kpa Vapor pressure = 8.00 Kpa Suction pressure = 101.4 Kpa NPSHa = 9.34 m

Motor Rating:


14.3 SANITARY SUMP PUMPS (EMPLOYEE HOUSING)

Velocity:


NPSH Available:

Specific gravity = 1Atmosphere pressure = 101.4 Kpa Vapor pressure = 8.00 Kpa Suction pressure = 101.4 Kpa NPSHa = 9.34 m

Motor Rating:


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PR-CAL-001

SAUDI ARABIA


15.0 POTABLE WATER PUMPS

NoofPumps = 21+1StandByFlowthroughonepump = 125 GPMSuctionLine = 4 inchVelocity = 0.96 m/sDischargeLine = 4 inchVelocity = 0.96 m/s

NPSHAvailable:

Specificgravity = 1Atmospherepressure = 101.3 Kpa Vapor pressure = 8.00 Kpa Suctionpressure = 105.0 Kpa Suctionpressureat120%flow = 103.8 Kpa NPSHa = 9.70 mNPSHaat120%flow = 9.58 m

MotorRating:

Pumpefficiencyassumed = 70 %Pressuredifferential = 1170 Kpa Duty = 17.00 hp15%allowance = 19.55 hpMotorRating = 20 hp(LinePressureDropandPumpHeadcalculationsattached)

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PR-CAL-001

SAUDI ARABIA


16.0 FIRE WATER FEED PUMPS

Velocity:

No of Pumps = 21 + 1 Stand By Flow through one pump = 175 GPMSuction Line = 6 inch Velocity = 0.62 m/s Discharge Line = 4 inch Velocity = 1.36 m/s

NPSH Available:

Specific gravity = 1Atmosphere pressure = 101.3 Kpa Vapor pressure = 8.00 Kpa Suction pressure = 100.0 Kpa Suction pressure at 120 % flow = 97 Kpa NPSHa = 9.20 m NPSHa at 120 % flow = 8.90 m

Motor Rating:


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PR-CAL-001

SAUDI ARABIA


17.0 ATTACHMENTS

Following HYSYS line pressure drop and pump head calculation is attached with report.

17.1 DIESEL LOADING PUMPS

17.2 GASOLINE LOADING PUMPS

17.3 DIESEL INTERFACE PUMPS

17.4 GASOLINE INTERFACE PUMPS

17.5 GASOLINE/DIESEL INTERFACE PRODUCT BULK TRANSFER PUMPS

17.6 OWS MAXIMUM FLOW PUMPS

17.7 OWS NORMAL FLOW PUMPS

17.8 OILY WATER FEED PUMPSS

17.9 RECOVERED OIL PUMPS

17.10 RECOVERED OIL TRANSFER PUMP

17.11 SANITARY SUM PUMPS (OPERATOR SHELTER AND INSPECTION

BUILDING)

17.12 SANITARY SUM PUMPS (MAIN SANITARY LIFT STATION)

17.13 SANITARY SUM PUMPS (EMPLOYEE HOUSING)

17.14 POTABLE WATER PUMPS

17.15 FIRE WATER FEED PUMPS

SOFCON GroupP.O. Box 3998, Al Khobar 31952Kingdom of Saudi Arabia

Case Name: DLP-FINAL WITH 16 PUMPS.HSC

Unit Set: SI

Date/Time: Fri Dec 17 17:42:14 2010

Material Stream: P1-D1Fluid Package: Basis-1

Property Package: Peng Robinson - LK

CONDITIONS

Vapour / Phase FractionTemperature: (C)Pressure: (kPa)Molar Flow (kgmole/h)Mass Flow (kg/h)Std Ideal Liq Vol Flow (m3/h)Molar Enthalpy (kJ/kgmole)Molar Entropy (kJ/kgmole-C)Heat Flow (kJ/h)Liq Vol Flow @Std Cond (m3/h)

Overall0.0000

40.18608.21033

2.367e+005273.0

-4.893e+005256.6

-5.055e+008273.0 *

Liquid Phase1.0000

40.18608.21033

2.367e+005273.0

-4.893e+005256.6

-5.055e+008273.0

PROPERTIES

Mass Heat of Vap.Phase Fraction [Molar Basis]Surface TensionThermal ConductivityViscosityWater Dew Point[Gas]HC Dew Point[Gas]Water Content In mg/m3[Gas]Wobbe Index[Gas]Mass Density (Std. Cond)[Gas]Higher Heating Value[Gas]Lower Heating Value[Gas]Cv (Semi-Ideal)Mass Cv (Semi-Ideal)CvMass CvCv (Ent. Method)Mass Cv (Ent. Method)Cp/Cv (Ent. Method)Liq. Vol. Flow - Sum(Std. Cond)API 5B1.1[RVP]API 5B1.2[RVP]ASTM D323-73/79[RVP]ASTM D323-82[RVP]ASTM D4953-91[RVP]ASTM D5191-91[RVP]Reid VP at 37.8 CTrue VP at 37.8 CPartial Pressure of H2SMolecular WeightMolar DensityMass DensityAct. Volume FlowMass EnthalpyMass EntropyHeat CapacityMass Heat CapacityLower Heating Value

(kJ/kg)

(dyne/cm)(W/m-K)

(cP)(C)(C)

(MJ/m3)(kg/m3)(MJ/m3)(MJ/m3)

(kJ/kgmole-C)(kJ/kg-C)



(m3/h)(kPa)(kPa)(kPa)(kPa)(kPa)(kPa)(kPa)(kPa)(kPa)

(kgmole/m3)(kg/m3)(m3/h)(kJ/kg)

(kJ/kg-C)(kJ/kgmole-C)

(kJ/kg-C)(kJ/kgmole)

Overall399.5

0.000028.39

0.15104.344

---419.3

---129.415.94466.8433.3432.71.889396.41.731419.01.8291.053273.0

0.53440.34800.4929

------------

0.49450.0000

229.13.712850.2278.4-21361.120441.01.925

---

Liquid Phase---

1.000028.39

0.15104.344

---419.3

---129.415.94466.8433.3432.71.889396.41.731419.01.8291.053273.0

0.53440.34800.4929

------------

0.4945---

229.13.712850.2278.4-21361.120441.01.925

---

Hyprotech Ltd. Aspen HYSYS Version 7.1 (23.0.0.7119) Page 1 of 130* Specified by user.Licensed to: A. AL-SAIHATI, A. FATTAN



Unit Set: SI


Material Stream: P1-D1 (continued)Fluid Package: Basis-1


PROPERTIES

Mass Lower Heating ValuePhase Fraction [Vol. Basis]Phase Fraction [Mass Basis]Partial Pressure of CO2Cost Based on FlowAct. Gas FlowAvg. Liq. DensitySpecific HeatStd. Gas FlowStd. Ideal Liq. Mass DensityAct. Liq. FlowZ FactorWatson KUser PropertyCp/(Cp - R)Cp/CvHeat of Vap.Kinematic ViscosityLiq. Mass Density (Std. Cond)Liq. Vol. Flow (Std. Cond)Liquid FractionMolar VolumeViscosity Index

(kJ/kg)

(kPa)(Cost/s)

(ACT_m3/h)(kgmole/m3)

(kJ/kgmole-C)(STD_m3/h)

(kg/m3)(m3/s)

(kJ/kgmole)(cSt)

(kg/m3)(m3/h)

(m3/kgmole)

Overall------

2.122e-3140.00000.0000

---3.784441.0

2.443e+004866.8

7.732e-0026.290e-002

11.57---

1.0191.112

9.150e+0045.109866.9273.01.000

0.26940.4072

Liquid Phase---

1.0001.000

---0.0000

---3.784441.0

2.443e+004866.8

7.732e-0026.290e-002

11.57---

1.0191.112

---5.109866.9273.01.000

0.26940.4072

Material Stream: P1-S1aFluid Package: Basis-1


CONDITIONS


Overall0.0000

39.9795.611033

2.367e+005273.0

-4.895e+005256.3

-5.057e+008273.0 *

Liquid Phase1.0000

39.9795.611033

2.367e+005273.0

-4.895e+005256.3

-5.057e+008273.0

PROPERTIES

Molecular WeightMolar DensityMass DensityAct. Volume FlowMass EnthalpyMass EntropyHeat CapacityMass Heat CapacityLower Heating Value




Overall229.13.710849.8278.5-21371.119441.11.926

---

Liquid Phase229.13.710849.8278.5-21371.119441.11.926

---




Unit Set: SI


Material Stream: P1-S1a (continued)Fluid Package: Basis-1


PROPERTIES

Mass Lower Heating ValuePhase Fraction [Vol. Basis]Phase Fraction [Mass Basis]Partial Pressure of CO2Cost Based on FlowAct. Gas FlowAvg. Liq. DensitySpecific HeatStd. Gas FlowStd. Ideal Liq. Mass DensityAct. Liq. FlowZ FactorWatson KUser PropertyCp/(Cp - R)Cp/CvHeat of Vap.Kinematic ViscosityLiq. Mass Density (Std. Cond)Liq. Vol. Flow (Std. Cond)Liquid FractionMolar VolumeMass Heat of Vap.Phase Fraction [Molar Basis]Surface TensionThermal ConductivityViscosityCv (Semi-Ideal)Mass Cv (Semi-Ideal)CvMass CvCv (Ent. Method)Mass Cv (Ent. Method)Cp/Cv (Ent. Method)Liq. Vol. Flow - Sum(Std. Cond)Reid VP at 37.8 CTrue VP at 37.8 CPartial Pressure of H2SViscosity Index

(kJ/kg)

(kPa)(Cost/s)

(ACT_m3/h)(kgmole/m3)

(kJ/kgmole-C)(STD_m3/h)

(kg/m3)(m3/s)

(kJ/kgmole)(cSt)

(kg/m3)(m3/h)

(m3/kgmole)(kJ/kg)

(dyne/cm)(W/m-K)

(cP)(kJ/kgmole-C)



(kJ/kg-C)

(m3/h)(kPa)(kPa)(kPa)

Overall------

2.122e-3140.00000.0000

---3.784441.1

2.443e+004866.8

7.736e-0029.899e-003

11.57---

1.0191.112

1.198e+0055.139866.9273.01.000

0.2695522.9

0.000028.41

0.15114.367432.81.889396.61.732419.31.8301.052273.0

---0.49450.00000.4098

Liquid Phase---

1.0001.000

---0.0000

---3.784441.1

2.443e+004866.8

7.736e-0029.899e-003

11.57---

1.0191.112

---5.139866.9273.01.000

0.2695---

1.000028.41

0.15114.367432.81.889396.61.732419.31.8301.052273.0

---0.4945

---0.4098

Material Stream: P2-D2Fluid Package: Basis-1


CONDITIONS

Vapour / Phase FractionTemperature: (C)Pressure: (kPa)Molar Flow (kgmole/h)Mass Flow (kg/h)Std Ideal Liq Vol Flow (m3/h)

Overall0.0000

40.18608.21033

2.367e+005273.0

Liquid Phase1.0000

40.18608.21033

2.367e+005273.0




Unit Set: SI




CONDITIONS

Molar Enthalpy (kJ/kgmole)Molar Entropy (kJ/kgmole-C)Heat Flow (kJ/h)Liq Vol Flow @Std Cond (m3/h)

Overall-4.893e+005

256.6-5.055e+008

273.0 *

Liquid Phase-4.893e+005

256.6-5.055e+008

273.0

PROPERTIES

Mass Heat of Vap.Phase Fraction [Molar Basis]Surface TensionThermal ConductivityViscosityWater Dew Point[Gas]HC Dew Point[Gas]Water Content In mg/m3[Gas]Wobbe Index[Gas]Mass Density (Std. Cond)[Gas]Higher Heating Value[Gas]Lower Heating Value[Gas]Cv (Semi-Ideal)Mass Cv (Semi-Ideal)CvMass CvCv (Ent. Method)Mass Cv (Ent. Method)Cp/Cv (Ent. Method)Liq. Vol. Flow - Sum(Std. Cond)API 5B1.1[RVP]API 5B1.2[RVP]ASTM D323-73/79[RVP]ASTM D323-82[RVP]ASTM D4953-91[RVP]ASTM D5191-91[RVP]Reid VP at 37.8 CTrue VP at 37.8 CPartial Pressure of H2SMolecular WeightMolar DensityMass DensityAct. Volume FlowMass EnthalpyMass EntropyHeat CapacityMass Heat CapacityLower Heating ValueMass Lower Heating ValuePhase Fraction [Vol. Basis]Phase Fraction [Mass Basis]Partial Pressure of CO2Cost Based on FlowAct. Gas Flow

(kJ/kg)

(dyne/cm)(W/m-K)

(cP)(C)(C)

(MJ/m3)(kg/m3)(MJ/m3)(MJ/m3)




(m3/h)(kPa)(kPa)(kPa)(kPa)(kPa)(kPa)(kPa)(kPa)(kPa)




(kJ/kg)

(kPa)(Cost/s)

(ACT_m3/h)

Overall399.5

0.000028.39

0.15104.344

---419.3

---129.415.94466.8433.3432.71.889396.41.731419.01.8291.053273.0

0.53440.34800.4929

------------

0.49450.0000

229.13.712850.2278.4-21361.120441.01.925

---------

2.122e-3140.00000.0000

---

Liquid Phase---

1.000028.39

0.15104.344

---419.3

---129.415.94466.8433.3432.71.889396.41.731419.01.8291.053273.0

0.53440.34800.4929

------------

0.4945---

229.13.712850.2278.4-21361.120441.01.925

------

1.0001.000

---0.0000

---




Unit Set: SI




PROPERTIES

Avg. Liq. DensitySpecific HeatStd. Gas FlowStd. Ideal Liq. Mass DensityAct. Liq. FlowZ FactorWatson KUser PropertyCp/(Cp - R)Cp/CvHeat of Vap.Kinematic ViscosityLiq. Mass Density (Std. Cond)Liq. Vol. Flow (Std. Cond)Liquid FractionMolar VolumeViscosity Index

(kgmole/m3)(kJ/kgmole-C)

(STD_m3/h)(kg/m3)

(m3/s)

(kJ/kgmole)(cSt)

(kg/m3)(m3/h)

(m3/kgmole)

Overall3.784441.0

2.443e+004866.8

7.732e-0026.290e-002

11.57---

1.0191.112

9.150e+0045.109866.9273.01.000

0.26940.4072

Liquid Phase3.784441.0

2.443e+004866.8

7.732e-0026.290e-002

11.57---

1.0191.112

---5.109866.9273.01.000

0.26940.4072

Material Stream: P2-S2aFluid Package: Basis-1


CONDITIONS


Overall0.0000

39.9795.611033

2.367e+005273.0

-4.895e+005256.3

-5.057e+008273.0 *

Liquid Phase1.0000

39.9795.611033

2.367e+005273.0

-4.895e+005256.3

-5.057e+008273.0

PROPERTIES

Molecular WeightMolar DensityMass DensityAct. Volume FlowMass EnthalpyMass EntropyHeat CapacityMass Heat CapacityLower Heating ValueMass Lower Heating ValuePhase Fraction [Vol. Basis]Phase Fraction [Mass Basis]Partial Pressure of CO2Cost Based on FlowAct. Gas Flow




(kJ/kg)

(kPa)(Cost/s)

(ACT_m3/h)

Overall229.13.710849.8278.5-21371.119441.11.926

---------

2.122e-3140.00000.0000

---

Liquid Phase229.13.710849.8278.5-21371.119441.11.926

------

1.0001.000

---0.0000

---




Unit Set: SI


Material Stream: P2-S2a (continued)Fluid Package: Basis-1


PROPERTIES

Avg. Liq. DensitySpecific HeatStd. Gas FlowStd. Ideal Liq. Mass DensityAct. Liq. FlowZ FactorWatson KUser PropertyCp/(Cp - R)Cp/CvHeat of Vap.Kinematic ViscosityLiq. Mass Density (Std. Cond)Liq. Vol. Flow (Std. Cond)Liquid FractionMolar VolumeMass Heat of Vap.Phase Fraction [Molar Basis]Surface TensionThermal ConductivityViscosityCv (Semi-Ideal)Mass Cv (Semi-Ideal)CvMass CvCv (Ent. Method)Mass Cv (Ent. Method)Cp/Cv (Ent. Method)Liq. Vol. Flow - Sum(Std. Cond)Reid VP at 37.8 CTrue VP at 37.8 CPartial Pressure of H2SViscosity Index

(kgmole/m3)(kJ/kgmole-C)

(STD_m3/h)(kg/m3)

(m3/s)

(kJ/kgmole)(cSt)

(kg/m3)(m3/h)

(m3/kgmole)(kJ/kg)

(dyne/cm)(W/m-K)

(cP)(kJ/

PR-CAL-001

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Transcript of PR-CAL-001