JP6188125B2 - 統合圧縮機及びポンプを備えた単一システム及び方法 - Google Patents
統合圧縮機及びポンプを備えた単一システム及び方法 Download PDFInfo
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- 238000000034 method Methods 0.000 title claims description 16
- 239000012530 fluid Substances 0.000 claims description 148
- 239000012071 phase Substances 0.000 claims description 121
- 244000309464 bull Species 0.000 claims description 35
- 238000001816 cooling Methods 0.000 claims description 15
- 239000007788 liquid Substances 0.000 claims description 10
- 230000008859 change Effects 0.000 claims description 8
- 238000005086 pumping Methods 0.000 claims description 8
- 230000007246 mechanism Effects 0.000 claims description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 3
- 230000006835 compression Effects 0.000 claims description 2
- 238000007906 compression Methods 0.000 claims description 2
- 239000007789 gas Substances 0.000 claims 14
- 239000007792 gaseous phase Substances 0.000 claims 1
- 239000007791 liquid phase Substances 0.000 description 11
- 238000010586 diagram Methods 0.000 description 6
- 239000000203 mixture Substances 0.000 description 6
- 238000005516 engineering process Methods 0.000 description 5
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- 239000010779 crude oil Substances 0.000 description 2
- 230000006870 function Effects 0.000 description 2
- 239000003921 oil Substances 0.000 description 2
- 238000010248 power generation Methods 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- 230000007704 transition Effects 0.000 description 2
- 239000012808 vapor phase Substances 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 1
- 239000000356 contaminant Substances 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000005553 drilling Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 238000012544 monitoring process Methods 0.000 description 1
- 238000010587 phase diagram Methods 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 239000010734 process oil Substances 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000005057 refrigeration Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04B—POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS
- F04B41/00—Pumping installations or systems specially adapted for elastic fluids
- F04B41/06—Combinations of two or more pumps
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04D—NON-POSITIVE-DISPLACEMENT PUMPS
- F04D13/00—Pumping installations or systems
- F04D13/12—Combinations of two or more pumps
- F04D13/14—Combinations of two or more pumps the pumps being all of centrifugal type
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04D—NON-POSITIVE-DISPLACEMENT PUMPS
- F04D25/00—Pumping installations or systems
- F04D25/16—Combinations of two or more pumps ; Producing two or more separate gas flows
- F04D25/163—Combinations of two or more pumps ; Producing two or more separate gas flows driven by a common gearing arrangement
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04D—NON-POSITIVE-DISPLACEMENT PUMPS
- F04D29/00—Details, component parts, or accessories
- F04D29/58—Cooling; Heating; Diminishing heat transfer
- F04D29/582—Cooling; Heating; Diminishing heat transfer specially adapted for elastic fluid pumps
- F04D29/5826—Cooling at least part of the working fluid in a heat exchanger
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04D—NON-POSITIVE-DISPLACEMENT PUMPS
- F04D31/00—Pumping liquids and elastic fluids at the same time
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
- F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
- F25J3/0228—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream characterised by the separated product stream
- F25J3/0266—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream characterised by the separated product stream separation of carbon dioxide
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
- F25J3/06—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by partial condensation
- F25J3/063—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by partial condensation characterised by the separated product stream
- F25J3/067—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by partial condensation characterised by the separated product stream separation of carbon dioxide
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2256/00—Main component in the product gas stream after treatment
- B01D2256/22—Carbon dioxide
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/80—Water
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/26—Drying gases or vapours
- B01D53/265—Drying gases or vapours by refrigeration (condensation)
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2230/00—Processes or apparatus involving steps for increasing the pressure of gaseous process streams
- F25J2230/20—Integrated compressor and process expander; Gear box arrangement; Multiple compressors on a common shaft
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2230/00—Processes or apparatus involving steps for increasing the pressure of gaseous process streams
- F25J2230/80—Processes or apparatus involving steps for increasing the pressure of gaseous process streams the fluid being carbon dioxide
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2235/00—Processes or apparatus involving steps for increasing the pressure or for conveying of liquid process streams
- F25J2235/80—Processes or apparatus involving steps for increasing the pressure or for conveying of liquid process streams the fluid being carbon dioxide
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02C—CAPTURE, STORAGE, SEQUESTRATION OR DISPOSAL OF GREENHOUSE GASES [GHG]
- Y02C20/00—Capture or disposal of greenhouse gases
- Y02C20/40—Capture or disposal of greenhouse gases of CO2
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Structures Of Non-Positive Displacement Pumps (AREA)
- Diaphragms For Electromechanical Transducers (AREA)
Description
12 圧縮機部
14 ポンプ部
16 ケーシング
20 単一のブルギア
22 ピニオン
18 ギアボックス
24 シャフト
23 シャフト
25 ピニオン
26 ギア
30−1〜30−6 6つの段
32 全体入口
36 全体出口
Claims (8)
- 気相の流体を加圧し且つ稠密相の流体をポンプ送給するよう構成されたシステムであって、
前記気相の流体を加圧するよう構成され、流体連結する複数のインペラを有する圧縮機部と、
前記圧縮機部に接続され、前記気相の流体を受けるよう且つ前記複数のインペラに流体を提供するよう構成された圧縮機部入口と、
所定密度以上の密度で前記気相の流体を提供するよう構成された圧縮機部出口と、
前記圧縮機部出口に接続され且つ流体を稠密相に変えるよう構成された温度変化装置と、
稠密相の流体をポンプ送給するよう構成された少なくとも1つのインペラを有するポンプ部と、
前記圧縮機部出口から前記温度変化装置を経て稠密相の流体を受けるよう構成されたポンプ部入口と、
前記システムから稠密相の流体を出力するよう構成されたポンプ部出口と、
所定速度で軸方向軸線の周りを回転するよう構成された単一のブルギアと、
前記単一のブルギアに接触し、互いに異なる所定速度で回転するよう構成され且つ各々が対応する圧縮機部インペラを作動させるよう構成されている複数のピニオンと、
前記ポンプ部から延び且つ前記単一のブルギアに係合して前記ポンプ部の少なくとも1つのインペラを回転させるよう構成されたポンプシャフトと、
を備え、
前記圧縮機部の少なくとも1つのインペラが、前記ポンプ部の少なくとも1つのインペラとは異なる速度を有し、稠密相は、前記所定密度よりも高い密度を有する流体によって定められ、
前記稠密相が、前記流体はガスであるが、ポンプで送給されるときには液体のように振る舞うほど高密度の相である、
システム。 - 前記温度変化装置が、冷却装置、チラー、又は膨張器のうちの1つであり、前記圧縮機部出口と前記ポンプ部入口との間に設けられ、前記流体がCO2であり、前記圧縮機部が、気相のCO2を受け取り且つ気相のCO2を放出するよう構成され、前記ポンプ部が、稠密相のCO2を受け取り且つ稠密相のCO2を放出するよう構成されている、請求項1に記載のシステム。
- 前記温度変化装置が、気相の流体のエンタルピーを前記流体の臨界点のエンタルピー以下にまで低減するよう構成されている、請求項1または2に記載のシステム。
- 前記ブルギアを駆動する単一の駆動機構を更に備える、請求項1から3のいずれかに記載のシステム。
- 前記圧縮機部及び前記ブルギアを収容するよう構成された圧縮機ケーシングと、
前記ポンプ部を受けるよう構成されたポンプケーシングと、
を備え、
前記ポンプケーシングが前記圧縮機ケーシングに取り付けられる、
請求項1から4のいずれかに記載のシステム。 - N個の圧縮機インペラ及びM個のポンプインペラと、
前記気相の入力流体が前記N個の圧縮機インペラ全てを直列に通って駆動されるように前記N個の圧縮機インペラの出力及び入力を接続する配管と、
N番目の前記圧縮機インペラからの気相の流体が、相変化を受けた後にM個のポンプインペラ全てを直列に通って駆動されるように、前記M個のポンプインペラにN番目の前記圧縮機インペラの出力を接続する配管と、
圧縮機又はポンプインペラの出力と、次の圧縮機又はポンプインペラの入力との間に設けられる水除去装置と、
気相又は稠密相の流体の温度を次の圧縮機又はポンプインペラに流入する前に低下させるよう構成された、前記配管に沿った少なくとも1つの温度変化装置と、
を更に備え、
Nは2よりも大きく、Mは1以上である、
請求項1から5のいずれかに記載のシステム。 - 6つの圧縮機インペラと8つのポンプインペラがあり、気相のCO2の前記圧縮機部における入力圧力が1barであり、稠密相のCO2の前記ポンプ部における出力圧力が10と120barの間である、請求項2に記載のシステム。
- 圧縮機部及びポンプ部を含み、該圧縮機部が少なくとも1つの圧縮機部インペラを有し、前記ポンプ部が少なくとも1つのポンプ部インペラを有するシステムによって気相の流体を加圧し、稠密相の流体をポンプ送給するための方法であって、
前記圧縮機部の圧縮機部入口において気相の流体を受け取るステップと、
前記気相の流体を前記圧縮機部の1つ又はそれ以上の段において加圧、所定密度以上の密度で気相の流体として前記圧縮機部の圧縮機部出口に出てくるようにするステップと、
前記流体を前記圧縮機部から流出した後に冷却することにより前記流体の相を稠密相に転換するステップと、
前記ポンプ部のポンプ部入口にて前記稠密相の流体を受けるステップと、
前記ポンプ部の1つ又はそれ以上の段を通って前記稠密相の流体をポンプ送給し、前記ポンプ部入口よりも高い圧力を有する前記ポンプ部のポンプ部出口において前記流体が出てくるようにするステップと、
単一のブルギアを回転させて、少なくとも1つ又はそれ以上の圧縮機段及び少なくとも1つ又はそれ以上のポンプ段の全てを作動させるようにするステップと、
を含み、
前記稠密相は、前記所定密度よりも高い密度を有する流体により定義され、
前記稠密相が、前記流体はガスであるが、ポンプで送給されるときには液体のように振る舞うほど高密度の相である、
方法。
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
ITCO2010A000006A IT1398142B1 (it) | 2010-02-17 | 2010-02-17 | Sistema singolo con compressore e pompa integrati e metodo. |
ITCO2010A000006 | 2010-02-17 | ||
PCT/EP2011/052077 WO2011101296A1 (en) | 2010-02-17 | 2011-02-11 | Single system with integrated compressor and pump and method |
Publications (2)
Publication Number | Publication Date |
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JP2013519864A JP2013519864A (ja) | 2013-05-30 |
JP6188125B2 true JP6188125B2 (ja) | 2017-08-30 |
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JP2012553271A Active JP6188125B2 (ja) | 2010-02-17 | 2011-02-11 | 統合圧縮機及びポンプを備えた単一システム及び方法 |
Country Status (11)
Country | Link |
---|---|
US (1) | US9360002B2 (ja) |
EP (1) | EP2536955B1 (ja) |
JP (1) | JP6188125B2 (ja) |
CN (1) | CN102834619B (ja) |
AU (1) | AU2011217353B2 (ja) |
BR (1) | BR112012020442A2 (ja) |
CA (1) | CA2789424A1 (ja) |
ES (1) | ES2476282T3 (ja) |
IT (1) | IT1398142B1 (ja) |
MX (1) | MX2012009605A (ja) |
WO (1) | WO2011101296A1 (ja) |
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-
2010
- 2010-02-17 IT ITCO2010A000006A patent/IT1398142B1/it active
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2011
- 2011-02-11 AU AU2011217353A patent/AU2011217353B2/en not_active Ceased
- 2011-02-11 JP JP2012553271A patent/JP6188125B2/ja active Active
- 2011-02-11 CN CN201180019539.6A patent/CN102834619B/zh active Active
- 2011-02-11 MX MX2012009605A patent/MX2012009605A/es active IP Right Grant
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- 2011-02-11 ES ES11702673.2T patent/ES2476282T3/es active Active
- 2011-02-11 EP EP20110702673 patent/EP2536955B1/en active Active
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Also Published As
Publication number | Publication date |
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CN102834619B (zh) | 2016-04-20 |
JP2013519864A (ja) | 2013-05-30 |
BR112012020442A2 (pt) | 2016-05-17 |
AU2011217353B2 (en) | 2016-02-11 |
MX2012009605A (es) | 2012-09-28 |
US20130156543A1 (en) | 2013-06-20 |
EP2536955B1 (en) | 2014-05-21 |
ES2476282T3 (es) | 2014-07-14 |
ITCO20100006A1 (it) | 2011-08-18 |
CA2789424A1 (en) | 2011-08-25 |
CN102834619A (zh) | 2012-12-19 |
IT1398142B1 (it) | 2013-02-14 |
AU2011217353A1 (en) | 2012-08-30 |
US9360002B2 (en) | 2016-06-07 |
EP2536955A1 (en) | 2012-12-26 |
WO2011101296A1 (en) | 2011-08-25 |
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