JP5778034B2 - 非混和性流体の分離方法及び装置 - Google Patents
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D17/00—Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion
- B01D17/02—Separation of non-miscible liquids
- B01D17/0208—Separation of non-miscible liquids by sedimentation
- B01D17/0214—Separation of non-miscible liquids by sedimentation with removal of one of the phases
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D17/00—Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion
- B01D17/02—Separation of non-miscible liquids
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D17/00—Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion
- B01D17/02—Separation of non-miscible liquids
- B01D17/04—Breaking emulsions
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D17/00—Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion
- B01D17/02—Separation of non-miscible liquids
- B01D17/04—Breaking emulsions
- B01D17/045—Breaking emulsions with coalescers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D19/00—Degasification of liquids
- B01D19/0042—Degasification of liquids modifying the liquid flow
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D19/00—Degasification of liquids
- B01D19/0042—Degasification of liquids modifying the liquid flow
- B01D19/0047—Atomizing, spraying, trickling
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D21/00—Separation of suspended solid particles from liquids by sedimentation
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G33/00—Dewatering or demulsification of hydrocarbon oils
- C10G33/06—Dewatering or demulsification of hydrocarbon oils with mechanical means, e.g. by filtration
-
- E—FIXED CONSTRUCTIONS
- E21—EARTH OR ROCK DRILLING; MINING
- E21B—EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
- E21B43/00—Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/20—Characteristics of the feedstock or the products
- C10G2300/201—Impurities
- C10G2300/208—Sediments, e.g. bottom sediment and water or BSW
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/40—Characteristics of the process deviating from typical ways of processing
- C10G2300/4081—Recycling aspects
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/80—Additives
- C10G2300/805—Water
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- Fluid Mechanics (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Geochemistry & Mineralogy (AREA)
- Separating Particles In Gases By Inertia (AREA)
- Removal Of Floating Material (AREA)
- Physical Water Treatments (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
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- Apparatus Associated With Microorganisms And Enzymes (AREA)
- Extraction Or Liquid Replacement (AREA)
Description
Claims (15)
- 第1の流体(3)及び第2の流体(4)を含む容器(2)を備えるウォッシュ・セパレータ(1)であって、
前記第2の流体(4)は前記第1の流体(3)とは異なる密度を有し、
前記第1の流体(3)は前記第2の流体(4)とは混合されず、前記第1及び第2の流体は界面(5)によって互いに分離し、前記第2の流体(4)内に分配された供給ストリーム(15,24,31,61)が、前記第2の流体(4)内を通過する際に、前記供給ストリーム(15,24,31,61)中で分散相を形成している前記第2の流体(4)が該第2の流体(4)内へと取り込まれ、かつ、前記供給ストリーム(15,24,31,61)中で連続相を形成している前記第1の流体(3)が前記第2の流体(4)とは混合されずに前記界面(5)によって該第2の流体(4)と互いに分離されている前記第1の流体(3)に取り込まれ、
前記供給ストリーム(15,24,31,61)が設けられ、前記供給ストリーム(15,24,31,61)は、連続相を構成する前記第1の流体(3)内に分散した液滴状の分散相を前記第2の流体(4)が形成するように、前記第1及び第2の流体(3,4)の分散体を含んでおり、
分配エレメント(6)が、前記供給ストリーム(15,24,31,61)を前記第2の流体(4)に分配するために、前記容器(2)内に設けられ、
(i)合一を促進するためのエレメント(14)が、前記分配エレメント(6)の排出開口(23)と前記界面(5)との間、及び/又は(ii)前記界面(5)は、前記合一を促進するためのエレメント(14)内に位置するように前記合一を促進するためのエレメント(14)が設けられる、
ウォッシュ・セパレータ(1)。 - 前記供給ストリームは、第1の供給ストリーム(24,31,61)及び第2の供給ストリーム(15)を含み、第2の流体の補充ストリームを前記第1の供給ストリーム(24,31,61)に加えるための供給エレメント(10)が、予め設けられていることを特徴とする請求項1に記載のウォッシュ・セパレータ。
- 前記供給ストリーム(15)中で前記分散相を形成する前記第2の流体(4)の分量は、前記分配エレメント内において、90容量%以下である、請求項1、又は2に記載のウォッシュ・セパレータ。
- 前記供給ストリーム(15)中で前記分散相を形成する前記第2の流体(4)の分量は、60容量%以下であることを特徴とする請求項3に記載のウォッシュ・セパレータ。
- 前記供給ストリーム(15)中で前記分散相を形成する前記第2の流体(4)の分量は、45容量%以下であることを特徴とする請求項3に記載のウォッシュ・セパレータ。
- 混合エレメント(12)が、前記分配エレメントの上流に配置されており、且つ/又は、混合エレメント(22)が前記第2の流体の排出ストリーム(21)中に配置されていることを特徴とする請求項1〜5のいずれか一項に記載のウォッシュ・セパレータ。
- 混合エレメント(12)が、静的ミキサーであることを特徴とする請求項6に記載のウォッシュ・セパレータ。
- 前記第2の流体(4)を、前記容器から前記第1の供給ストリーム(24,31,61)へと再利用するためのライン(17)が、予め設けられていることを特徴とする請求項2〜7のいずれか一項に記載のウォッシュ・セパレータ。
- 前記容器(2)は、底部(7)を有し、前記分配エレメント(6)は、少なくとも1つの排出開口(23)を有し、前記界面(5)と前記分配エレメント(6)の前記排出開口(23)との間の距離が、最大で10mであることを特徴とする請求項1〜8のいずれか一項に記載のウォッシュ・セパレータ。
- 前記界面(5)と前記分配エレメント(6)の前記排出開口(23)との間の距離が、最大でも3mであることを特徴とする請求項9に記載のウォッシュ・セパレータ。
- 前記供給ストリーム(15,24,31,61)は、ガス(18)及び/又は固相(19)を含み、前記固相(19)は、前記界面(5)の下に配置された固体保持エレメント(11)によって分離されることを特徴とする請求項1〜10のいずれか一項に記載のウォッシュ・セパレータ。
- 前記第1の流体(3)は油分であり、前記第2の流体(4)は水分であることを特徴とする請求項1〜11のいずれか一項に記載のウォッシュ・セパレータ。
- 請求項1〜12のいずれか一項に記載のウォッシュ・セパレータ(1)において実行される第1及び第2の非混和性流体を分離するための方法であって、前記第1及び第2の流体を含む前記供給ストリーム(15,24,31,61)を容器(2)に供給し、分配エレメント(6)によって前記供給ストリーム(15,24,31,61)を前記第2の流体(4)に分配する工程を含むことを特徴とする方法。
- 前記供給ストリーム(15,24,31,61)は、第1の供給ストリーム(24,31,61)及び第2の供給ストリーム(15)を含み、
前記第2の供給ストリーム(15)が前記分配エレメント(6)を離れる前に、第2の流体(4)を、前記第1の供給ストリーム(24,31,61)に加える工程をさらに含むことを特徴とする請求項13に記載の方法。 - 請求項1〜12のいずれか一項に記載のウォッシュ・セパレータ(1)の海底施設における使用。
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP08168628 | 2008-11-07 | ||
EP08168628.9 | 2008-11-07 | ||
PCT/EP2009/063498 WO2010052108A1 (en) | 2008-11-07 | 2009-10-15 | Separation method and apparatus for immiscible fluids |
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JP2012508100A JP2012508100A (ja) | 2012-04-05 |
JP5778034B2 true JP5778034B2 (ja) | 2015-09-16 |
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JP2011535066A Expired - Fee Related JP5778034B2 (ja) | 2008-11-07 | 2009-10-15 | 非混和性流体の分離方法及び装置 |
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Country | Link |
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US (2) | US20110309040A1 (ja) |
EP (1) | EP2355913B1 (ja) |
JP (1) | JP5778034B2 (ja) |
KR (2) | KR101781016B1 (ja) |
CN (1) | CN102215931B (ja) |
AU (1) | AU2009312944B2 (ja) |
BR (1) | BRPI0921610B1 (ja) |
CA (1) | CA2742875C (ja) |
MX (1) | MX356453B (ja) |
MY (1) | MY172866A (ja) |
RU (1) | RU2514989C2 (ja) |
WO (1) | WO2010052108A1 (ja) |
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EP2872233B1 (de) * | 2012-07-11 | 2016-09-14 | Basf Se | Abtrennung von ionischen flüssigkeiten mittels koaleszierfilter aus acrylphenolharz |
KR101463726B1 (ko) * | 2013-04-30 | 2014-11-21 | 한국과학기술원 | 해저 저압분리기를 이용한 원유가스 생산 시스템 |
US10137386B2 (en) * | 2013-12-02 | 2018-11-27 | Basf Se | Separation of ionic liquids in coalescing devices |
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KR101781016B1 (ko) | 2017-09-25 |
RU2514989C2 (ru) | 2014-05-10 |
US20110309040A1 (en) | 2011-12-22 |
MY172866A (en) | 2019-12-13 |
CA2742875C (en) | 2017-02-14 |
EP2355913A1 (en) | 2011-08-17 |
AU2009312944A1 (en) | 2010-05-14 |
MX2011004703A (es) | 2011-05-30 |
KR20160137688A (ko) | 2016-11-30 |
JP2012508100A (ja) | 2012-04-05 |
BRPI0921610A2 (pt) | 2015-12-29 |
WO2010052108A1 (en) | 2010-05-14 |
CA2742875A1 (en) | 2010-05-14 |
CN102215931A (zh) | 2011-10-12 |
AU2009312944B2 (en) | 2013-09-26 |
CN102215931B (zh) | 2015-07-22 |
MX356453B (es) | 2018-05-30 |
US10092861B2 (en) | 2018-10-09 |
KR20110081288A (ko) | 2011-07-13 |
BRPI0921610B1 (pt) | 2019-06-04 |
US20140284285A1 (en) | 2014-09-25 |
EP2355913B1 (en) | 2018-04-04 |
RU2011122793A (ru) | 2012-12-20 |
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