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REF. No.: 3034-00-ED-QC-PCR-VP-0390-0038-A3
PERSIAN GULF STAR OIL COMPANY PROJECT:
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VP 0390 0038
A3
14.Mar.2013
REFINERY PROJECT
DOCUMENT TITLE : FACTORY PERFORMANCE TEST PROCEDURE FOR EQ0390 EQUIPMENT NAME : VERTICAL PUMP ITEM NO. :ALL ITEMS P-4561 A/B, P-4562 A/B, P-4563 A/B P-4564 A/B, P-4565 A/B, P-4566 A/B P-4567 A/B, P-2501 A/B/C/D
STATUS DATE:
APPROVED
01.May.13 APPROVED WITH COMMENTS
SIGNATURE:
COMMENTED
M.Jalili
REJECTED
Next Issue Description
SHALL BE FILLED BY CLIENT A3
12-Apr-2013
ISSUED FOR APPROVAL
W.Cherry
L.Tino
C.Ryan
A2
14-Mar-2013
ISSUED FOR APPROVAL
W.Cherry
L.Tino
C.Ryan
A1
04-Mar-2013
ISSUED FOR APPROVAL
W.Cherry
L.Tino
C.Ryan
A0
06-Feb-2013
ISSUED FOR APPROVAL
T.Anne
L.Tino
C.Ryan
REV.
DATE
DESCRIPTION
PREPARED
CHECKED
APPROVED
DEEP BLUE PUMP CO.
REF. No.: 3034-00-ED-QC-PCR-VP-0390-0038-A3
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REF. No.: 3034-00-ED-QC-PCR-VP-0390-0038-A3
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Content Chapter
Content
Page
1
Scope
4
2
Applicable Codes and Standards
4
3
4
4
Test Requirements Performance Test
5
NPSH Test
10
6
Mechanical Running Test (Complete unit test)
12
7
Vibration test
14
8
Sound level test
17
9
Temperature Rise Test
17
10
Apparatus, Instruments and Accessories
17
App.1
Check List Format Per Item
18
App.2
Sketch of Test System
19
5
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FACTORY PERFORMANCE TEST PROCEDURE 1. Scope 1.1 This test procedure describes the requirements, apparatus and accessories, methods, acceptance criteria and records of factory performance test containing performance test (capacity, head, efficiency, and shaft power), NPSH, vibration and temperature rise, etc. for centrifugal pump. COMPANY/EMPLOYER : Persian Gulf Star Oil Company. PROJECT : Bandar Abbas Gas Condensate Refinery (BAGCR) Project. VENDOR: DEEP BLUE PUMP CO. GOODS : VERTICAL PUMP. JOB-SITE : Bandar Abbas ( Iran ). 1.2 This is applicable to overhung, between-bearing and vertical types of pumps designated per API 610 Standard Tenth Edition, October 2004 Table 1 manufactured by pump vendor. 1.3 The exact scope of tests shall be in accordance with approved inspection and test plan (ITP) or agreed upon between purchaser and vendor, not limited to this procedure. 2. Applicable Codes and Standards API 610 Standard Tenth Edition, October 2004 ISO9906:1999 Rotodynamic Pump – Hydraulic performance acceptance tests GB3214 Methods for Measurement of Capacity of Pump 3. Test Requirements 3.1 General
3.1.1 The exact scope of tests shall be in accordance with the CONTRACT and the test points will be according to item 4.1 of this procedure. The test includes:
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1). Performance Test 2). NPSH test (will only performed for the NPSHa-NPSHr margin less than 0.6 m). 3). Mechanical Running Test (Complete unit test) 4). Vibration Test 5). Noise Level Test 6) Temperature Rise Test 3.1.2 Unless otherwise specified, each pump shall be given a performance test. Performance tests shall be performed using water (The specific gravity of the water is 1, and the chloride of the water is less than 50ppm) at a temperature less than 65 degree C. 3.1.3 Check and Verify calibration of all test apparatus and instruments which shall be in the valid period. 4. Performance Test 4.1 The performance test shall be performed at five points they are: Point 1)Shut off point (no vibration data required), Point 2)minimum continuous stable flow, Point 3)midway points between minimum and rated flow; Point 4)rated flow; Point 5)maximum allowable flow (as a minimum, 120% percent of best efficiency point). 4.2 Test Method The capacity, head, shaft power, efficiency, running speed, vibration, bearing temperature shall be measured or calculated at each point specified in Chapter 4,5,6,7,8 and 9 below. 4.3.1 Capacity 4.3.1.1 The test method of capacity is in accordance with standard GB3214. 4.3.1.2 GB3214 is Methods for Measurement of Capacity of Pump standard which specified requirements for the flow meter and the measuring methods.
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4.3.1.3 The instrument for capacity measurement is electromagnetic flow meter, the parameter of capacity can be read directly from the flow meter during actual duration of test. 4.3.2 Head measuring 4.3.2.1 Head of pump should be calculated according to the standard ISO 9906:1999. 4.3.2.2 The formula of head:
P 2 − P1 + (Z2 - Z1)+ +ρg
H= Among them, H=Head of pump
P1=Suction pressure P2=Discharge pressure (Z2-Z1)= The distance between pump suction centerline and discharge surface. V2= Velocity of medium flow through pump discharge V2= Q (capacity)/Ad (surface area of the discharge) V1= velocity of medium flow through pump suction V1= Q (capacity)/As( surface area of the suction)
4.3.3 Running speed shall be read from digital meter used. The test speed shall be within 3 percent of the rated speed shown on the pump data sheet. 4.3.4 Shaft Power Shaft power Pa should be the following when efficiency ηmot of motor is known (Pgr is input power of motor). Pa = Pgr × ηmot 4.3.5 Calculation of efficiency of pump η=
Pu Pa
×100%
Pu: Hydraulic power. Pu=Qsp * Hsp * SG *9.8* / 3600 Qsp = Capacity at Rated speed( m3/h), Hsp = Head at Rated speed( m)
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nsp = Rated speed (rpm) SG: Specific gravity of test water (1.0) 4.3.6 Correction of test result at the rated speed Qsp = Capacity at n × (nsp / n) Hsp = Head at n × (nsp / n)2 Psp = Shaft power at n × (nsp / n)3 NPSH at nsp = NPSH at n × (nsp / n)2 Where: nsp — Rated speed n — Testing speed NPSH—NPSH required 4.4 Acceptance Criteria Pumps shall perform within the tolerances given in Table 14 of API610 10th Edition.
Condition Rated differential head
Table 14-Performance tolerances Rated Point %
0 m to 150 m (0 ft to 500 ft) 151 m to 300 m (501 ft to 1 000 ft) Over 300 m (1 000 ft) Rated power Rated NPSH NOTE Efficiency is not a rating value.
Shut off %
-2 +5 -2 +3 -2 +2
+10 -10 a +8 -8 a +5 -5 a
+4 b
---
+0
---
a. If a rising head flow curve is specified (see 5.1.13 cited from API 610), the negative tolerance specified here shall be allowable only if the test curve still shows a rising characteristic. b. Under any combination of above (cumulative tolerance are not acceptable). Maximum allowable noise level is 87 dB(A) @ 1 m for the pump and 90 dB(A) @ 1 m for the complete train. Don't allow positive tolerance.
REF. No.: 3034-00-ED-QC-PCR-VP-0390-0038-A3
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4.4Test report
4.4.1 PUMP PERFORMANCE TEST REPORT Contract No.: Item No:
Test Date:
Record No:
Pump Model:
Test Equipment/Instrument
Manufacture Serial No:
Name
Impeller Diameter For first stage: Impeller Diameter For other stage:
mm mm
Specification
Capacity Meter
DN
Calibration Period
(mm)
1 Year
KW
Suction Manometer
Motor Efficiency:
%
Discharge Manometer
MPa
1 Year
Rated Capacity:
m3/h
Speed Meter
rpm
1 Year
m
Power Meter
Motor Type:
Rated Total Head: Rated Speed:
r/min
Test Liquid temperature liquid:
Calculating Constant
℃
Precision
1 Year
Watte Meter Suction Position
1 Year Discharge Position (m)
DN Suction(mm)
DN Discharge(mm)
-----
Testing Actual Value Discharge Head (P2)
Suction Head(P1)
Differential Velocity Head
MPa/(m)
mm MPa Hg/ /(m) (m)
m
Total Head (H) Test Rated Speed Speed m
m
Capacity (Q) Test Speed
Rated Speed
m3/h
m3/h
The difference between test head and rated head %. Remarks
Test Speed (n)
r/min
Shaft Power (Pa) Power Meter
Test Speed
Rated Speed
----
KW
KW
Tested By: Result
Corrected shaft power gravity. Signed and stamped by TPI/ Purchaser
kw due to specific
Inspected By:
Efficiency (η)
%
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4.4.2 PUMP PERFORMANCE TEST REPORT (Vibration, Noise and Oil Temp.) PUMP PERFORMANCE TEST REPORT (Vibration, Noise and Oil Temp.)
Contract No.
Test Equipment/ Instrument
Item No.
Name
Pump Model
Capacity Meter
Test Date
Discharge Manometer
Record No.
Speed Meter
Manufacture Serial No.
Infrared Thermometer
Rated Capacity
m3/h
Rated Head
Specification
Calibratio n Period
Precision
Noise Meter
m
Vibration Meter Testing Actual Value
No.
Discharge Head
Running Capacity
Speed
(P2)
(Q)
(n)
MPa
m3/h
r/min
Vibration
Noise
Oil Sump Temperature
mm/s
dB
°C
1 2 3 4 5 6 7 8
Result
Remark
Tested by Inspected by
Signed and stamped by TPI/ Purchaser
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5. NPSH Test 5.1 NPSH Test will only performed for the NPSHa-NPSHr margin less than 0.6 m 5.2 NPSH test (if any) shall be performed at four points, they are: Point1) minimum continuous stable flow; Point 2) midway points between minimum and rated flow; Point 3) rated flow; Point 4) maximum allowable flow (as a minimum, 120% percent of best efficiency point). 5.3 NPSH test will be performed for the pumps NPSH margin less than 0.6m. 5.4 NPSH test for vertical pumps shall be done with installed strainer. 5.5 3 % drop in head (first stage head on multistage pumps) shall be interpreted as indicating performance impairment. The first stage head of pumps with two or more stages shall be measured using a separate connection to the first stage discharge if possible. If this is not feasible, testing of the first stage only should be considered.
5.5 Acceptance Criteria NPSHR at the rated point shall not exceed the quoted value (see API Table 14)., Pumps NPSH test shall perform within the tolerances given in Table 14 of API610 10th Edition, please refer to item 4.4 Table 14-Performance tolerances Dismantling to correct NPSHR requires a retest (see API 7.3.3.5 and 7.4.3.1).
REF. No.: 3034-00-ED-QC-PCR-VP-0390-0038-A3
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5.6 Test report NPSH TEST REPORT Test Date:
Contract No. Item No.
Record No.
Pump Model
Manufacture Serial No. Differential Position
Test Condition Diameter of Suction
mm
Water Temperature
℃
No.
Working capacity 3
m /h
Velocity head m
NPSHR Required
m
Speed
r/min
Vapor Pressure
m
Atmosphere Pressure
m
Capacity 3 m /h
Rated Working Point
Total Head m
Suction Head mm Hg
m
Discharge Head MPa
m
NPSH m
2 3 4 5 6 7 8 9 10 Test By Remarks Inspected By Signed and stamped by TPI/ Purchaser
Discharge m
Speed r/min
1
Result
Suction m
Total Head
3 % drop in head
m
m
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6. Mechanical Running Test 6.1 When the performance test had been finished, mechanical run test shall be performed in the capacity which does not affect the motor; rated capacity as usual. The test standard will be referred to Clause 7.3.4.7.3 of API 610, 10th edition. 6.2 The duration for the mechanical run test is 4 hours after oil temperature has been stabilized. 6.3 The test data shall be recorded each 30 minutes for the whole performance test length, such as running speed, temperature rise, vibrations, sound level, flow rate and discharge pressure, etc. 6.4 During mechanical running test contract motor, seal, seal system, coupling skid shall be used to make sure run the pumps with the complete unit.
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6.5 Test report RUNNING TEST REPORT
Contract No.
Test Equipment/Instrument
Item No.
Name
Product Type
Manufacture No.
Calibration Period
Precision
Capacity Meter
Test Date
Discharge Manometer
Report No.
Speed Meter
Manufacture Serial No.
Power Meter
Running Total Capcity
m3/ h
Running Total Head
m
Noise Meter Vibration meter Testing Actual Value
Time
Discharge Head (P2)
Running Capacity (Q)
Speed (n)
Vibration
Noise
Oil sump temperature
min
Mpa
m3/h
r/min
mm/s
dB
℃
15 30 45 60
Result
Tested By
Signed and stamped by TPI/ Purchaser
Inspected By
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7.Vibration test 7.1 Method: Using the vibration instrument (VT-63) to test the pump’s vibration from three directions (horizontal, vertical, and Shaft Direction). For detail standard information, please refer to Clause 5.9.3.6 of API 610. 7.2 Acceptance Criteria Pumps vibration test shall perform within the tolerances given in Table7 of API610 10th Edition, Fig. 28 of API 610
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Table 7-Vibration limits for vertical-suspended pumps
Criteria
Overall
Location of vibration measurement Pump thrust bearing housing or Pump shaft (adjacent to bearing) Motor mounting flange see Figure 28 Pump bearing type Hydrodynamic guide bearing All adjacent to accessible region of shaft Vibration at any flow rate within the pump’s preferred operating region Au < (6,2 x 106 / n)0.5 um peak-topeak 0.5 [(10 000 / n) mils peak-to-peak] Vu < 5,0 mm/s RMS (0,20 in/s RMS) Not to exceed: Au < 100 um peak-to-peak a (4,0 mils peak-to-peak) Vf < 0.67 Vu Af < 0,75Au
Discrete frequencies Allowable increase in vibration at flows outside the preferred 30% 30% operating region but within the allowable operating region Vibration velocity and amplitude values calculated from the basic limits shall be rounded of to two significant figures. Where: Vu is the unfiltered velocity, as measured; V f is the filtered velocity; Au is the amplitude of unfiltered displacement, as measured; A f is the amplitude of filtered displacement; f is the frequency; n is the rotational speed, expressed in revolutions per minute.
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7.3 Test report VIBRATION AND NOISE LEVEL TEST REPORT P.O No.
Item No.
Product Type
Manufacture Serial No.
3
Capacity
m /h
Running Speed
r/min
Head
m
Height From Upper Surface of Baseplate to The Center of Pump
mm
VIBRATION MEARAMENT
Position
Capacity
The Bearing Position Heading The Motor
Vertical (mm/s)
Horizontal (mm/s)
Shaft Direction (mm/s)
The Bearing Position Heading The Impeller
Vertical (mm/s)
Horizontal (mm/s)
m3/h
m3/h
m3/h
m3/h
m3/h
m3/h Tested by
Date
Result
Inspected By
Signed and stamped by TPI/ Purchaser
Shaft Direction (mm/s)
Measurement Result (mm/s)
Standard Requirement (mm/s)
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8. Sound level test 8.1 Sound level test shall be performed and accepted as agreed between the purchaser and the vendor, e.g. the sound level limit specified in approved datasheet in order or approved ITP. 8.2 Test report Sound level test report please refers to item 4.4.2. and item 6.5 9. Temperature Rise Test 9.1 The test of temperature of bearing oil sump shall be according to the requirements paragraph 5.10.2.4 of API610 code, so that, oil sump temperature shall be below 82°C. The sump oil temperature rise shall not exceed 39°C. 9.2 Test report Oil sump Temperature rise test report please refers to item 4.4.2 and item 6.5
10. Apparatus, Instruments and Accessories 10.1 Control cabinet. 10.2 Connecting cable between the pump unit and the control cabinet 10.3 Piping for testing 10.4 Pressure gauge 10.5 Flow meter 1 .6 Power meter 10.7 Running speed meter 10.8 Noise meter 10.9 Vibration meter 10.10 Schematic diagram of test racks 10.11 Temperature gauge 10.12 Sketch of test system for vertical pumps please kindly refers to APPENDIX 2. 10.13 For vertical pumps, suction strainer should be installed and considered during the NPSH test.
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APPENDIX1: CHECK LIST FORMAT PER ITEM Contact No.: Item No.
Description:
Date: Service
Pump Model
Serial No.
Nameplate
Painting Appearance
Pipe Assembly
General Arrangement Dimension
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APPENDIX 2 Sketch of Test System
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