dalian leo huaneng pump co., ltd 2004 ~...

Medium Capacitym/hHead

mTemp.

2004.10 KazakstanCHINA PETROLEUMENGINEERING&CONSTRUCTIONCORP.

Kenkyak oilfield industrialproduction project

80AY60 API 610 OH2 Water cut of crude oil 45 60 0-55 1 C-6 YB160M2-2 15



100AY60 API 610 OH2 Water cut of crude oil 60 60 0-55 2 C-6 YB180M-2 22






80AY60 API 610 OH2 Clean water 30 60 0-55 2 C-6 YB160M2-2 15



80AY60 API 610 OH2 Water cut of crude oil 45 60 0-55 1 C-6 YB160M2-2 15




Qty API 610Material Grade Motor TypeMotor Power

KW

EXPORT REFERENCE LIST

2004 ~ 2012DALIAN LEO HUANENG PUMP CO., LTD

Delivery End User / EPCCountry Pump Model

Technical Parameters

RelativeStandardProject Name


mTemp.


KW








HSM151-250 API 610 BB1 Clean water 198-310 68-82 4-40 1 C-6 Y315S-2 110



HC100-315 ISO2858 OH1 Waste oil, sewage 120-240 100-125 4-40 2 C-6 Y315S-2 110



TR32-200 API 610 VS1 Corrosion inhibitor 19.3 20 AMB 2 C-6 YB132S1-2 5.5



HDR65-506 API 610 BB5 Water cut of crude oil 34.5 325 380 2 C-6 YB280M-2 90

2005.05 Sudan KHARTOUM REFINERY COMPANYLIMITEDThe improvement for 0.33millionton/year aviation kerosene ofproducing equipment

100AY120A API 610 OH2 Hydrofining diesel oil 62.3 116 50 2 S-5 YB225M-2TAW 45


80AY1002 API 610 OH2 Diesel 45.2 148 340 2 C-6 YB200L1-2TAW 30


mTemp.


KW







80AY1002 API 610 OH2 Boat coal slipped into 28.4 164 40 2 S-5 YB200L1-2TAW 30

2006.8 Cuba HAVANA REFINERY Equipment modification HSM302-360 API 610 BB1 Gas oil 912.00 40.84 15.5-40 1 S-5 YB355M1-4W 160

2006.8 Cuba HAVANA REFINERY Equipment modification HSM252-400 API 610 BB1 Gasoline 684.00 64.00 10-35 1 S-5 YB355M1-4W 160

2006.8 Cuba HAVANA REFINERY Equipment modification HE50-250 API 610 OH2 Slop 68.40 85.40 15-90 1 S-5 YB200L1-2W 30

2006.8 Cuba HAVANA REFINERY Equipment modification 80AY60 API 610 OH2 Kerosene 163GPM37266FT

81385F196 1 S-6 YB160M2-2W 15

2006.8 Cuba HAVANA REFINERY Equipment modification 100AY120 API 610 OH2 Light diesel 226GPM51139FT

42437F225 2 S-6 YB160M--4W 11


mTemp.


KW






2006.8 Cuba HAVANA REFINERY Equipment modification 150AY150 API 610 OH2 Atm pumpparound 930GPM211397FT

121490-520F254-271 2 S-6 YB280S-2W 75

2006.8 Cuba HAVANA REFINERY Equipment modification HE40-315 API 610 OH2 Light naphtha 130GPM30610FT

18695-130F

35-54 2 C-6 YB200L2-2W 37

2006.8 Cuba HAVANA REFINERY Equipment modification 80AY100 API 610 OH2 Naphtha 221GPM48480FT

146110-150F

43-66 2 S-6 YB200L2-2W 37

2006.8 Cuba HAVANA REFINERY Equipment modification TD408 API 610 VS6 HC liquid60.2/80.2GP

M14/18

1295FT395

110F43 2 S-6 YB200L2-2W 37

2006.8 Cuba HAVANA REFINERY Equipment modification 65AY1002 API 610 OH2 HC liquid 85.5/95GPM19/22616FT

188 395F202 2 S-6 YB180M-2W 22

2006.8 Cuba HAVANA REFINERY Equipment modification 100AYa120 API 610 OH2 Naphtha 224GPM51638FT

194105F

41 1 S-6 YB250M-2W 55


mTemp.


KW






2006.8 Cuba HAVANA REFINERY Equipment modification 65AYa100 API 610 OH2 Light HC 110GPM25387FT

118105F

41 2 S-6 YB160M2-2W 15

2006.8 Cuba HAVANA REFINERY Equipment modification 100AY60 API 610 OH2 Light HC 385GPM87182FT

55127F

53 2 S-6 YB180M-2W 22

2006.8 Cuba HAVANA REFINERY Equipment modification 80AY100 API 610 OH2 Light HC 264GPM60446FT

136138F

59 2 S-6 YB200L2-2W 37

2006.8 Cuba SANTIAGO REFINERY Equipment modification HEr40-250 API 610 OH2 Heavy naphtha 28 104 38 2 S-5 YB160L-2W 18.5

2006.8 Cuba SANTIAGO REFINERY Equipment modification HEr40-200 API 610 OH2 Slop 25 75 38-120 1 S-6 YB160M2-2W 15

2006.8 Cuba SANTIAGO REFINERY Equipment modification HE200-315 API 610 OH2 Gasoline super 318 42 38 2 S-5 YB225M-4W 45


mTemp.


KW






2006.8 Cuba SANTIAGO REFINERY Equipment modification HSM203-640 API 610 BB1 Disel 636 141 38 2 S-5 YB450S1-4W 315

2006.8 Cuba SANTIAGO REFINERY Equipment modification HE150-500 API 610 OH2 Disel 318 91.4 35 1 S-5 YB315M-4W 132

2006.8 Cuba SANTIAGO REFINERY Equipment modification HE250-560 API 610 OH2 Disel 636 114.2 35 1 S-5 YB400M2-4W 280

2006.8 Cuba SANTIAGO REFINERY Equipment modification HE50-200 API 610 OH2 Slop 50 56 38 1 S-6 YB160L-2W 18.5

2006.8 Cuba SANTIAGO REFINERY Equipment modification HE50-200 API 610 OH2 Slop 35 70 38 1 S-6 YB160L-2W 18.5

2006.8 Cuba SANTIAGO REFINERY Equipment modification HSM302-500 API 610 BB1 Water 1022 53 40 1 S-5 YB400M2-6W 220


mTemp.


KW






2006.8 Cuba SANTIAGO REFINERY Equipment modification HEr50-250 API 610 OH2 Water 69.3 59.13 26.67 1 S-5 YB180M-2W 30

2006.8 Cuba SANTIAGO REFINERY Equipment modification HDB508 API 610 BB4 Heavy naphtha 34 670 220 1 S-6 YB280M-2W 90

2006.8 Cuba SANTIAGO REFINERY Equipment modification HE250-560 API 610 OH2 Naphtha 650 119.7 35 1 S-5 YB400M1-4W 250

2006.8 Cuba SANTIAGO REFINERY Equipment modification DL3-15X10 API 610 VS6 Water 3.5 216 90 2 S-6 YB160M2-2W 15

2006.8 Cuba SANTIAGO REFINERY Equipment modification DL3-15X11 API 610 VS6 Light hydroc 3.5 236 35 2 S-6 YB160M1-2W 11

2006.8 Cuba SANTIAGO REFINERY Equipment modification HE50-401 API 610 OH2 Vacuum tower bottom 90 260 375 1 C-6 YB315M1-2W 132


mTemp.


KW






2007.1 Kazakstan CNPC AKTOBE OIL AND GASSTOCK COMPANYZanarol oilfield third oil and gastreatment plant phase I Project

HL40-315 API 610 VS4 Liquid sulfur 15 40 160 3 A-7 YB180M-4W 18.5


HA250-400 ISO2858 OH1 Lean amine 575 50 53 2 A-8(316L) YB315M-4W 132


HA250-400 ISO2858 OH1 Lean amine 485 50 140 2 A-8(316L) YB280M-4W 90


HA250-400 ISO2858 OH1 Rich amine 464 45 64 2 A-8(316L) YB280M-4W 90


HA80-400 ISO2858 OH1 Propane 132/50 150 40 2 S-5 YB280S-2W 75


HA100-315 ISO2858 OH1 Sulfur-containing waste water 130/150/170 100 25 2 D-2 YB280M-2WF2 90


mTemp.


KW






2008.1 Russia RUSSIA CASPIAN SEA OILREFINERY COMPANY Refinery project HA80-400 ISO2858 OH1 Oil, sulfide 0,56-1,27% 148/170 175 10~20 2 S-5 YB315M-2W 132

2008.1 Russia RUSSIA CASPIAN SEA OILREFINERY COMPANY Refinery project HE100-400 API 610 OH2Crude oil and gasoline, sulfide

-0,56-1,27% 202/232 178 220~230 2 S-6 YB315L1-2W 160

2008.1 Russia RUSSIA CASPIAN SEA OILREFINERY COMPANY Refinery project HA50-315 API 610 OH2Gasoline, distillate. E., -85,

and -0,01%, sulfide 40~60 125 60 2 S-5 YB225M-2W 45

2008.1 Russia RUSSIA CASPIAN SEA OILREFINERY COMPANY Refinery project HA100-250 ISO2858 OH1Kerosene, fraction.160-200, -

0,1% C, sulfide 115/132 81 132 2 S-6 YB250M-2W 55

2008.1 Russia RUSSIA CASPIAN SEA OILREFINERY COMPANY Refinery project HE100-315 API 610 OH2Kerosene, fraction.200-250, -

1,1% C, sulfide 145/167 101 196 2 S-6 YB280S-2W 75

2008.1 Russia RUSSIA CASPIAN SEA OILREFINERY COMPANY Refinery project HE80-400 API 610 OH2Heavy oil, fraction.>350, -1,1%

C, sulfide 103/119 150 330 2 S-6 YB280M-2W 90


mTemp.


KW






2008.1 Russia RUSSIA CASPIAN SEA OILREFINERY COMPANY Refinery project HE50-400 API 610 OH2Diesel, fraction.230 (240) --

350 (360), and --0,4%, sulfide 41/47 150 240 2 S-6 YB225M-2W 45

2008.1 Russia RUSSIA CASPIAN SEA OILREFINERY COMPANY Refinery project HA40-400 ISO2858 OH1Kerosene, fraction.180-240, C,

sulfide - 0,1% 20/23 138 166 2 S-6 YB225M-2W 45

2008.1 Russia RUSSIA CASPIAN SEA OILREFINERY COMPANY Refinery project HA40-315 ISO2858 OH1Gasoline, kerosene,

fraction.140-180, 0,1% andsulfide

11/13 130 103 2 S-6 YB180M-2W 22

2008.1 Russia RUSSIA CASPIAN SEA OILREFINERY COMPANY Refinery project HA50-250 ISO2858 OH1Gasoline, fraction.85-140, -

0,01% and sulfide 30/35 76 60 2 S-5 YB180M-2W 22

2008.1 Russia RUSSIA CASPIAN SEA OILREFINERY COMPANY Refinery project HA50-400 ISO2858 OH1Gasoline, distillate. E., -180, --

0,11% and sulfide 40/46 215 40 2 S-5 YB280S-2W 75

2008.1 Russia RUSSIA CASPIAN SEA OILREFINERY COMPANY Refinery project HE50-400 API 610 OH2Asphalt, fraction.>500, --3,1%

and sulfide 42/48 172 360 2 C-6 YB250M-2W 55


mTemp.


KW






2008.1 Russia RUSSIA CASPIAN SEA OILREFINERY COMPANY Refinery project HE50-400 API 610 OH2Ship oil fraction.420-500 and -

-1,9%, sulfide 50/58 80/156 325 2 C-6 YB250M-2W 55

2008.1 Russia RUSSIA CASPIAN SEA OILREFINERY COMPANY Refinery project HE50-315 API 610 OH2Ship oil fractions.350-420, --

0,1% and sulfide. 52/60 50/127 255 2 S-6 YB225M-2W 45

2008.1 Russia RUSSIA CASPIAN SEA OILREFINERY COMPANY Refinery project HE50-400 API 610 OH2Diesel oil, distillate. < 350 and

sulfide --1,1%. 41/47 132 170 2 S-6 YB225M-2W 45

2008.1 Russia RUSSIA CASPIAN SEA OILREFINERY COMPANY Refinery project HDA80*8 API 610 BB4Diesel, fraction.230 (240) --

350 (360) --0,4% and sulfide. 68/78 600 60 2 S-5 YB355S-2W 200

2008.1 Russia RUSSIA CASPIAN SEA OILREFINERY COMPANY Refinery project HE40-315 API 610 OH2- 3-4 --

0,01%20~22 115 40 2 S-5 YB180M-2W 22

2008.1 Russia RUSSIA CASPIAN SEA OILREFINERY COMPANY Refinery project HA40-250 ISO2858 OH1Gasoline, kerosene, sulfide --

0,1% 13/15 84 29 2 S-5 YB160M1-2W 11


mTemp.


KW






2008.1 Russia RUSSIA CASPIAN SEA OILREFINERY COMPANY Refinery project HA40-250 ISO2858 OH1Gasoline, kerosene, sulfide --

0,1% 15/17 63 60 2 S-5 YB132S2-2W 7.5

2008.1 Russia RUSSIA CASPIAN SEA OILREFINERY COMPANY Refinery project HY32-160 API 610 VS4Fraction.180-240 and

fraction,.230 (240) - sulfide --0,4%

12.5/14.3 35 90 2 S-5 YB132S2-2W 7.5

2008.1 Russia RUSSIA CASPIAN SEA OILREFINERY COMPANY Refinery project HA40-250 ISO2858 OH1Fraction.230 (240) --350 (360),

and --0,4%, sulfide 15/17 66 60 2 S-5 YB160L2-2W 18.5

2008.1 Russia RUSSIA CASPIAN SEA OILREFINERY COMPANY Refinery project HA40-160 ISO2858 OH1 15% Alkali solution 12.5/14 13.8/17 35~45 1 S-5 YB100L-2W 3

2008.1 Russia RUSSIA CASPIAN SEA OILREFINERY COMPANY Refinery project HA40-160 ISO2858 OH1 Alkali 18.2/20 32 40 2 S-5 YB160M1-2W 11

2008.1 Russia RUSSIA CASPIAN SEA OILREFINERY COMPANY Refinery project HA40-160 ISO2858 OH1 Alkali 10/12 33 50 2 S-5 YB160M1-2W 11


mTemp.


KW






2008.1 Russia RUSSIA CASPIAN SEA OILREFINERY COMPANY Refinery project HA40-200 ISO2858 OH1 Alkali 17/20 37.6 60 2 S-5 YB160M1-2W 11

2008.7 Indonesia INDONESIA SPV Sulfur recovery project HL25-200 API 610 VS4 Liquid sulfur 3~6 35 120~150 2 A-7 YB132S-2WTH 7.5

2008.7 Indonesia INDONESIA SPV Sulfur recovery project HL25-200 API 610 VS4 Liquid sulfur 3~6 35 120~150 4 A-7 YB132S2-2WTH 7.5

2008.7 Indonesia INDONESIA SPV Sulfur recovery project HL40-160 API 610 VS4 Liquid sulfur 18 18 120~150 2 A-7 YB132S2-2WTH 7.5

2008.7 Indonesia INDONESIA SPV Sulfur recovery project HL25-315 API 610 VS4 Liquid sulfur 8 120 120~150 2 A-7 YB225M-2WTH 45

2008.7 Indonesia INDONESIA SPV Sulfur recovery project HL25-315 API 610 VS4 Liquid sulfur 8 120 120~150 1 A-7 YB225M-2WTH 45


mTemp.


KW






2009.1 TurkmenistanSICHUAN PETROLEUMADMINISTRATION BUREAU OFTURKMENISTAN EPCC PROJECTDEPARTMENT

Bagg Delle contract area A blocksurface engineering of natural gastreatment plant

HY32-200 API 610 VS4 MDEA solution 10 55 40 4 A-8 YB132S2-2W 7.5












HLD50-302 API 610 VS4 Liquid sulfur 25/28 46 150 2 A-8 YB225S-4W 37



HA25-200 ISO2858 OH1 Sour gas field water 3/7.2 40 2560 6 A-8 YB100L-2W 3


mTemp.


KW








HA200-630 ISO2858 OH1 MDEA solution 263/315 130 87.7 8 A-8 YB450S1-4 200



HDR65-506 API 610 BB5 Asphalt 34.5 325 380 2 C-6 YB280M-2 90

2009.12 Niger CNPC INTERNATIONAL LIMITEDCOMPANY OF WEST AFRICAHeavy oil catalytic cracking unit ofrefinery of Agadem oilfieldintegration project

HE50-450 API 610 OH2 Crude gasoline 41/50 266 60 2 S-5 YB280M-2WTA 90


65AYP1002 API 610 OH2 Acidic water 9.0/12.0 193 40 2 A-8 YB200L1-2WTA 30


HDA408 API 610 BB4 Burning oil 20.5/24 265 40 2 S-5 YB200L2-2WTA 37


HE80-315 API 610 OH2 Condensed oil 4.34/108.7/136 102 40 2 S-5 YB250M-2WTA 55


mTemp.


KW







HE80-250 API 610 OH2 Absorption tower bottom oil 85.9/110 71 45 2 S-5 YB200L2-2WTA 37


HE80-250 API 610 OH2 Return oil absorption towerone 80.1/100 60 47 2 S-5 YB200L1-2WTA 30


HE80-250 API 610 OH2 The second return oilabsorption tower 81.4/102 60 42 2 S-5 YB200L1-2WTA 30


HE80-315 API 610 OH2 Liquid gas 67.2/95 100 40 2 S-5 YB225M-2WTA 45


80AYP1002 API 610 OH2 Stabilized gasoline 32.7/40 180 40 2 S-5 YB200L2-2WTA 37


HDH6-356 API 610 BB4 Condensate oil 5.3/8.5 200 40 2 S-5 YB160L-2WTA 18.5


mTemp.


KW







HE25-250 API 610 OH2 Light gasoline 7 70 40 1 S-5 YB132S2-2WTA 7.5


HDH6-356 API 610 BB4 Gasoline 3.9/5.1 180 40 2 S-5 YB160M1-2WTA 11


HDH6-356 API 610 BB4 Heavy oil 3.9/4.5 210 141 2 S-5 YB160M1-2WTA 11

2010.6 KazakstanTHE KAZAKHSTAN REPUBLICCNPC-AKTOBE OIL AND GASSTOCK COMPANY

Hope oilfield construction (project)fourth oil and gas processing plant

HGP50-250 API 610 OH3 Clean water 5 20 70 2 A-8 Y90L-4 1.5



HE100-315 API 610 OH2 Stabilized crude oil 250 120 43.32 4 S-6 YB315S-2W 110



DL6-15*11 API 610 VS6 Original stable lighthydrocarbon 6.4 160 50.15 2 S-6 YB132S2-2 7.5


mTemp.


KW








HGPH150-315 API 610 OH3 Oily wastewater 150 100 60 2 S-5 YB2280S-2 75



HGPH100-315 API 610 OH3 Crude oil or oil purification 80 100 60 2 S-5 YB2225M-2 45



DL6-15*9 API 610 VS6 The hydrocarbon containingwastewater 4 130 40 1 S-6 YB132S2-2WF 7.5



DLA3-15*3 API 610 VS6 Crude oil or oily wastewater 3 40 60 1 S-5 YB112M-2 4

2010.9 Turkmenistan TURKMENISTAN EPCC PROJECTDEPARTMENTBagg Delle contract area A blocksurface engineering

HYB50*5 API 610 VS4 Sulfur-containing waste oil,sewage 12.5 45 AMB 1A-8

(316L) YB132M-4W 7.5

2010.9 Turkmenistan TURKMENISTAN EPCC PROJECTDEPARTMENTBagg Delle contract area A blocksurface engineering

HYB50*5 API 610 VS4 Sulfur-containing waste oil,sewage 12.5 45 AMB 1A-8

(316L) YB132M-4W 7.5


mTemp.


KW






2010.11 Uzbekistan CPECC UZBEKISTAN SUBSIDIARY The natural gas pipeline projectEPC03/04HGPN81-160 API 610 OH3 Hot water 40 36 20-80 4 S-5 Y2160M1-2 11

2010.11 Uzbekistan CPECC UZBEKISTAN SUBSIDIARY The natural gas pipeline projectEPC03/04HGPN40-200 API 610 OH3 Hot water 2 20 20-80 4 S-5 Y290S-2 1.5

2010.11 Uzbekistan CPECC UZBEKISTAN SUBSIDIARY The natural gas pipeline projectEPC03/04HGPN40-200 API 610 OH3 Hot water 2 12 20-80 4 S-5 Y290L-4 1.5

2010.11 Iraq CPECC IRAQ BRANCH AHDBE Project HY150-450 API 610 VS4 Utility water 182 61.1 53 2 A-8 YB250M-4W 55

2010.11 Iraq CPECC IRAQ BRANCH AHDBE Project HY50-40X2 API 610 VS4 Oil water 15/30/35 79.8 50-60 4 D-1 YB180M-4W 22

2010.11 Iraq CPECC IRAQ BRANCH AHDBE Project HY50-315 API 610 VS4 Produced water 35 30 70 2 D-1 YB160M1-4W 11


mTemp.


KW






2010.11 Iraq CPECC IRAQ BRANCH AHDBE Project HY80-315 API 610 VS4 Produced water 30/60/70 29.8 40/60 2 D-1 YB180M-4W 22

2011 Uzbekistan CPECC UZBEKISTAN SUBSIDIARY2# MR-EPC0304-WKC2-MEC-017 diesel pump station projectprocurement planning

HC32-160 ISO2858 OH1 Diesel 10 10 AMB 1 A-7 Y90S-2 1.5KW

2011 Cuba CHINA PETROLEUM TECHNOLOGY& DEVELOPMENT CORPORATION Refinery project HSM251-280 API 610 BB1 Diesel 568 32.3 34 1 A-7 6BT5.9-G 110

2011 Singapore Sewage treatment HE25-315 API 610 OH2 Oil 10 88.5 60/80 2 S-5 M2JA160M2-2 15

2011 Singapore Sewage treatment HEO50-400 API 610 OH2 Waste water 30 40 45 2 A-8 M2JA-W160M-4 11

2011 Singapore Sewage treatment HEO100-400 API 610 OH2 Waste water 80 40 45 2 A-8 M2JA-W180M-4 18.5


mTemp.


KW






2011 Singapore Sewage treatment HEO100-400 API 610 OH2 Waste water 115 50 45 2 A-8 M2JA-W200L-4 30

2011 Singapore Sewage treatment HYK32-200 API 610 VS4 Waste water 6 10 AMB 2 A-8 M2JA-W100L1-4 2.2

2011 Singapore Sewage treatment HE25-315 API 610 OH2 Oil 2 30 40 2 S-5 M2JA-W112M-4 4

2011 Singapore Sewage treatment HE25-200 API 610 OH2 Oil 4.5 10 AMB 1 S-5 Y90L-4W 2.2

2011 Singapore Sewage treatment HE25-200 API 610 OH2 Oil 4.5 10 AMB 1 S-8 Y90L-4W 2.2

2011 IraqCHINA PETROLEUMENGINEERING&CONSTRUCTIONCORP.

Halfaya Project Surface FacilityEarly Fcp

HLB32-200 API 610 VS4 Crude oil 5 10 40~75 2 S-5 YB2 112M-4W 3


mTemp.


KW






2011 IraqCHINA PETROLEUMENGINEERING&CONSTRUCTIONCORP.

Halfaya Project Surface FacilityEarly Fcp

HE50-315 API 610 OH2 Fresh water 65 85


mTemp.


KW






2012 TurkmenistanSICHUAN PETROLEUMADMINISTRATION BUREAU OFTURKMENISTAN EPCC PROJECTDEPARTMENT

Turkmenistan South Iolotan gasfield, 100*108m3/a gasproductivity construction project

HEG80-250 API 610 OH2 Liquid sulfur 49.2 60 125-140 2 A-8(316L)YBXn 200L2-

2W 37



HL80-250 API 610 VS4 Liquid sulfur 32.15/64.30/70.73 20 135-158 12A-8

(316L) YBXn 180M-4W 18.5




(316L) YBXn 180M-4W 18.5




(316L) YBXn 200L-4W 30



HE25-200 API 610 OH2 Steam condensation water 3.345/6.69/7.36 20 110 12 S-6 YBXn S100L-2 3



HE40-160 API 610 OH2 Gas field water 25 30 40 4 A-8(316L) YBXn 132S1-2 5.5


mTemp.


KW








HLF50-25-146 API 610 VS4

In addition, in addition todischarge sewage

sedimentation tank of oilequipment

2 30 0-30 2 A-8(316L) YBXn 100L-2 3



HA100-250 ISO2858 OH1Concentrated brine

discharged from the reverseosmosis device

150 60 0-30 2 A-8(316L) YBXn 225M-2 45



HA50-250 ISO2858 OH1 Water, amine liquid wastealkali liquid gas system 50 60 0-30 2A-8

(316L) YBXn 160L-2 18.5



HA50-160 ISO2858 OH1 Gas field water 30 30 0-30 2 A-8(316L) YBXn 132S1-2 5.5



HE250-630 API 610 OH2 The hot lean amine liquid 592 130 95.5 12 A-8(316L) YB 450M2-4 355

2012 Venezuela PDVSA Transformation of the refinery HLB250-315 API 610 VS4 Oily wastewater 318 13.9 AMB 4 S-6 YBXN225M-6W 30


mTemp.


KW






2012 Venezuela PDVSA Transformation of the refinery HLB50-315 API 610 VS4 Oil 39.8 40.9 AMB 2 S-6 YBXN180M-4W 18.5

2012 India SHANGHAI JUYOU CHEMICALENGINEERING CO.,LTD HA25-200 ISO2858 OH1 EG 7.9 42 53 2 A-7 Y3 112M-2 4

2012 India SHANGHAI JUYOU CHEMICALENGINEERING CO.,LTD HC32-160 ISO2858 OH1 EG 5 20 32 1 A-7 YB3 100L-2 3

2012 India SHANGHAI JUYOU CHEMICALENGINEERING CO.,LTD HAO40-315 ISO2858 OH1 Tio2/EG Slurry 10 32 25 1 A-7 Y3 132M-4 7.5

2012 India SHANGHAI JUYOU CHEMICALENGINEERING CO.,LTD HE25-200 API 610 OH2The bottom of the tower

separation EG 5.9 34 185 1 A-7 Y3 112M-2 4

2012 India SHANGHAI JUYOU CHEMICALENGINEERING CO.,LTD HC250-400 ISO2858 OH1 Cooling water 700 30 32 4 S-5 Y3 280M-4W 90


mTemp.


KW






2012 India SHANGHAI JUYOU CHEMICALENGINEERING CO.,LTD HC150-400 ISO2858 OH1 Cooling water 300 40 13 3 S-5 Y3 250M-4W 55

2012 India SHANGHAI JUYOU CHEMICALENGINEERING CO.,LTD HA50-250 ISO2858 OH1 EG 15 15 43 1 A-7 Y3 100L2-4 3

2012 India SHANGHAI JUYOU CHEMICALENGINEERING CO.,LTD HC32-160 ISO2858 OH1 EG 3.5 20 45 2 A-7 Y3 90L-2 2.2

2012 India SHANGHAI JUYOU CHEMICALENGINEERING CO.,LTD HC80-250 ISO2858 OH1 EG 135 87 46.5 2 A-7 Y3 250M-2 55

2012 India SHANGHAI JUYOU CHEMICALENGINEERING CO.,LTD HC50-250 ISO2858 OH1 EG 50 84 32.5 2 A-7 Y3 200L1-2 30

2012 India SHANGHAI JUYOU CHEMICALENGINEERING CO.,LTD HC50-200 ISO2858 OH1 EG 35.6 55 55 2 A-7 Y3 160M2-2 15


mTemp.


KW






2012 India SHANGHAI JUYOU CHEMICALENGINEERING CO.,LTD HA25-200 ISO2858 OH1 EG 2.3 20 45 2 A-7 Y3 90S-2 1.5

2012 India SHANGHAI JUYOU CHEMICALENGINEERING CO.,LTD HC50-250 ISO2858 OH1 EG 51.5 82 46 2 A-7 Y3 200L1-2 30

2012 India SHANGHAI JUYOU CHEMICALENGINEERING CO.,LTD HC40-250 ISO2858 OH1 EG 20 85 32 2 A-7 Y3 160L-2 18.5

2012 India SHANGHAI JUYOU CHEMICALENGINEERING CO.,LTD HC32-250 ISO2858 OH1 EG 16.8 57 56 2 A-7 Y3 160M1-2 11

2012 India SHANGHAI JUYOU CHEMICALENGINEERING CO.,LTD HC32-160 ISO2858 OH1 EG 2.3 20 45 2 A-7 Y3 90S-2 1.5

2012 India SHANGHAI JUYOU CHEMICALENGINEERING CO.,LTD HC40-250 ISO2858 OH1 EG 38.6 82 46 2 A-7 Y3 200L1-2 30


mTemp.


KW






2012 India SHANGHAI JUYOU CHEMICALENGINEERING CO.,LTD HC32-250 ISO2858 OH1 EG 15 84 32 2 A-7 Y3 160M2-2 15

2012 India SHANGHAI JUYOU CHEMICALENGINEERING CO.,LTD HC32-200 ISO2858 OH1 EG 13.7 52 60 2 A-7 Y3 132S2-2 7.5

2012 Kazakstan KAZAKHSTAN PKOP COMPANY 4000t/a Sulfur recovery unit HL25-3152 API 610 VS4 Liquid sulfur 5/6 50 138-170 2 A-8(316L) YB2 180M-4W 22

2012 Kazakstan KAZAKHSTAN PKOP COMPANY 4000t/a Sulfur recovery unit HEG25-200 API 610 OH2 Liquid sulfur 5 40 140 2 A-8(316L) YB2 132S2-2W 7.5


TDA6-35*10 API 610 VS6 Sour oil, sulfur containingwastewater 2.6/4 300 AMB 2 S-8 YB3 200L1-2 30

2012 Burma CNPC SOUTH-EAST ASIA PIPELINECOMPANY LIMITED HYB32-160 API 610 VS4 Crude oil 10 30 5-45 1 S-6YB3 112M-

2WTH 4


mTemp.


KW







2WTH 4


2WTH 4


2WTH 4

2012 Kazakstan CPE SOUTHWEST BRANCH4000t/a sulfur recovery unit ofKazakhstan PKOP company

HL25-3152 API 610 VS4 Liquid sulfur 5/6 50 138-170 2 A-8(316L) YB2 180L-4W/22 22

2012 Kazakstan CPE SOUTHWEST BRANCH4000t/a sulfur recovery unit ofKazakhstan PKOP company

HEG API 610 OH2 Liquid sulfur 5 40 140 2 A-8(316L) YB2 132S2-2W/7.5 7.5

2012 Indonesia SHANGHAI JUYOU CHEMICALENGINEERING CO.,LTD Exported to Indonesia project HE200-560 API 610 OH2A mixture of biphenyl and

biphenyl ether 350 103.5 AMB 1 S-5YB2 315L1-

4/160 160


mTemp.


KW






2012 TurkmenistanGOODS&MATERIALS INDUSTRIALDEVELOPMENT CORPORATION OFSICHUAN PEROLEUM

Second Bagg Delle contract areaof second natural gas treatmentplant

TDA6-35*10 API 610 VS6 Sour oil, sulfur containingwastewater 2.6/4 300 AMB 2 S-8 YB3 200L1-2/30 30

2012 Burma CNPC SOUTH-EAST ASIA PIPELINECOMPANY LIMITEDMyanmar oil and gas pipelineproject (Burma section) No. fourth

HYB32-160 API 610 VS4 Crude oil 10 30 5-45 1 S-6 YB3 112M-2WTH/4 4







2012 TurkmenistanCHINA PETROLEUMENGINEERING&CONSTRUCTIONCORP.

Bagg Delle contract area B blocknatural gas processing

HYB32-200 API 610 VS4 Sulfur-containing waste oil,sewage 12.5 45 AMB 1 A-8(316L)YB3 160M1-2WF2 / 11kW 11


mTemp.


KW







Bagg Delle contract area B blocknatural gas processing

HA40-160 ISO2858 OH1 Corrosion inhibitor 12.5 32 AMB 1 S-6 YB3 132S2-2WF1 / 7.5kW 7.5


CPECC Turkmenistan ofbagtyjiarlyk contractual area Bblock of natural gas treatmentplant EPCC project

HA200-500 ISO2858 OH1 Product condensate 300 80 5/64 4 A-8(316L)YB3 355M1-4 W

/ 220kW 220

2012 KazakhstanCHINA PETROLEUMENGINEERING&CONSTRUCTIONCORP.

Kazakhstan Hope Oilfield EPCproject in fourth oil and gasprocessing

HA100-400 ISO2858 OH1Mineralization of sewage containing oil,containing impurities25500mg/L cl-13000mg/L H2S550mg/L Containing

a small amount of mud and sand

120 45 0~80 1 A-8(316L)YBPT 200L-4WF1 / 30kW 30





170 120 0~80 1 A-8(316L)YBPT 315S-2WF1 / 110kW 110





170 60 0~80 1 A-8(316L)YPT 250M-4WF1 / 55kW 55

2012 HKD80-70X8 API 610 BB4 Product condensate 100 550 5-40 2 S-8 YB2 400 1-2/185KW 185

Turkmenistan CNPC(Turkmenistan)Amu DaryaTurkmenistan of bagtyjiarlykcontractual area second natural


mTemp.


KW






2012 HYA32-250 API 610 VS4 SC(steam condensate) 6 15 80 1 304 4KW-4P 4

2012 Venezuela GLOBAL TECHNOLOGY COMPANY HE40-160 API 610 OH2 Alcohol solvent 9.1 9.1 35 1 S-5 3KW 1450r/min 3

2012 Venezuela GLOBAL TECHNOLOGY COMPANY HE40-160 API 610 OH2 Alcohol solvent 9.1 7 35 1 S-5 1.5KW1450r/min 1.5

2012 Iran Shahid Tond GouyanPetrochemical PlantRevamping&Modifying of PET-2Plant

HA25-250 ISO2858 OH1 EG 3.5 20 45 2 304 Y 100L-4 3

2012 KazakstanCHINA PETROLEUMENGINEERING&CONSTRUCTIONCORP.

Zanarol oilfield natural gastreatment and comprehensiveutilization of third oil and gasprocessing plant in II, III phase ofthe project

HA200-450 ISO2858 OH1 Condensate oil 440 62 40 3 S-8 75KW-4 75



HA80-400 ISO2858 OH1 Condensate oil 140 140 40 2 S-8 75KW-2 75

Turkmenistan Company contractual area second naturalgas treatment plant


mTemp.


KW








HYB50-450 API 610 VS4 Discharge of steam injectionboiler 25 25 120 2 S-5 5.5kW-6W 5.5



HE250-560 API 610 OH2 Lean amine liquid 550 100 40 4 S-8 YB2 400-4W 280



HYA25-200 API 610 VS4 Waste lubricating oil 3.6 40 20 1 S-5 YB3 132S1-2W 5.5



HYA40-200 API 610 VS4 Amine liquid 16 55 AMB 2 S-8 YB3 160M1-2W 11



HE250-400 API 610 OH2 Heat the lean solution pump 460 55 107.64 4 S-8 YB3 315M-4W 132



SAD1500-70 API 610 BB1 Circulating cooling water 1260 75 25-42 1 S-5 YKK450-4W 355


mTemp.


KW








SAD2850-60 API 610 BB1 Circulating cooling water 2020 75 25-42 2 S-5 YKK500-6W 560



HE150-250 API 610 OH2 The condensation of water 155 13.3 120-138 1 C-6 YXn160M-4W 11



HE50-250 API 610 OH2 Out of salt water 60 71.4 AMB 1 C-6 YXn200L1-2W 30



MAD300-854 API 610 BB3 The condensation of water 155 91.8 120-138 2 C-6 YXn280S-4W 75



MAS200-956 API 610 BB3 The condensation of water 80 142.8 120-138 1 C-6 YXn280S-4W 75



HE50-250 API 610 OH2 Out of salt water 60 81.6 AMB 2 C-6 YXn200L1-2W 30


mTemp.


KW








HYA32-250 API 610 VS4 Steam condensation water 15 70 50-125 4 S-8 YB160M2-2W 15

Dalian Leo Huaneng Pump Co., Ltd

Adress: No.19,Xinyi Street, GanJingZi District, Dalilan

Emial: [email protected]

Website: www.leogroup.com

dalian leo huaneng pump co., ltd 2004 ~...

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