WO2008022998A2 - Method and apparatus for treating a hydrocarbon stream - Google Patents
Method and apparatus for treating a hydrocarbon stream Download PDFInfo
- Publication number
- WO2008022998A2 WO2008022998A2 PCT/EP2007/058648 EP2007058648W WO2008022998A2 WO 2008022998 A2 WO2008022998 A2 WO 2008022998A2 EP 2007058648 W EP2007058648 W EP 2007058648W WO 2008022998 A2 WO2008022998 A2 WO 2008022998A2
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- stream
- gas
- liquid separator
- feeding point
- liquid
- Prior art date
Links
Classifications
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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
- C10G5/00—Recovery of liquid hydrocarbon mixtures from gases, e.g. natural gas
- C10G5/06—Recovery of liquid hydrocarbon mixtures from gases, e.g. natural gas by cooling or compressing
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- 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
- F25J3/0204—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 feed stream
- F25J3/0209—Natural gas or substitute natural gas
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- 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
- F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
-
- 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
-
- 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
- F25J3/0204—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 feed stream
- F25J3/0209—Natural gas or substitute natural gas
- F25J3/0214—Liquefied natural gas
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- 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
- F25J3/0233—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 CnHm with 1 carbon atom or more
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- 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
- F25J3/0238—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 CnHm with 2 carbon atoms or more
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- 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
- F25J2200/00—Processes or apparatus using separation by rectification
- F25J2200/02—Processes or apparatus using separation by rectification in a single pressure main column system
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- 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
- F25J2205/00—Processes or apparatus using other separation and/or other processing means
- F25J2205/02—Processes or apparatus using other separation and/or other processing means using simple phase separation in a vessel or drum
- F25J2205/04—Processes or apparatus using other separation and/or other processing means using simple phase separation in a vessel or drum in the feed line, i.e. upstream of the fractionation step
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- 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
- F25J2205/00—Processes or apparatus using other separation and/or other processing means
- F25J2205/30—Processes or apparatus using other separation and/or other processing means using a washing, e.g. "scrubbing" or bubble column for purification purposes
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- 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
- F25J2210/00—Processes characterised by the type or other details of the feed stream
- F25J2210/62—Liquefied natural gas [LNG]; Natural gas liquids [NGL]; Liquefied petroleum gas [LPG]
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- 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
- F25J2240/00—Processes or apparatus involving steps for expanding of process streams
- F25J2240/02—Expansion of a process fluid in a work-extracting turbine (i.e. isentropic expansion), e.g. of the feed stream
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- 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
- F25J2270/00—Refrigeration techniques used
- F25J2270/90—External refrigeration, e.g. conventional closed-loop mechanical refrigeration unit using Freon or NH3, unspecified external refrigeration
- F25J2270/904—External refrigeration, e.g. conventional closed-loop mechanical refrigeration unit using Freon or NH3, unspecified external refrigeration by liquid or gaseous cryogen in an open loop
Definitions
- the present invention relates to a method and/or apparatus of treating a hydrocarbon stream such as a natural gas stream.
- a problem of the known method is that it is rather complicated thereby resulting in high capital expenses (CAPEX), but at the same time it does not obtain a satisfactory recovery of in particular ethane. Also the amount of fuel gas produced is not optimal, because the focus of US 2005/0268649 Al is mainly on the liquefaction of natural gas rather than on the production of 'residual streams' and recovery of ethane therefrom.
- the present invention provides a method of treating a hydrocarbon stream such as a natural gas stream, in a plant, the method at least comprising the steps of:
- step (c) expanding the liquid stream obtained in step (b) and feeding it into a second gas/liquid separator at a first feeding point;
- step (g) removing from the bottom of the second gas/liquid separator a liquid stream; wherein the liquefied natural gas stream as fed in step (e) is obtained from a source of liquefied natural gas from a separate plant.
- Fig. 1 schematically shows a process scheme in accordance with the present invention.
- Embodiments of the present invention relate to the treatment of a natural gas stream, and may involve recovery of at least some of the ethane, propane, butanes and higher hydrocarbons such as pentane from the natural gas.
- the recovery of hydrocarbons may be done for several purposes.
- One purpose may be the production of hydrocarbon streams consisting primarily of hydrocarbon products heavier than methane such as natural gas liquids (NGLs; usually composed of ethane, propane and butanes), liquefied petroleum gas (LPG; usually composed of propane and butane) or condensates (usually composed of butanes and heavier hydrocarbon components).
- Another purpose may be the adjustment of e.g. the heating value of the hydrocarbon stream to correspond to desired specifications of sales gas.
- the CAPEX can be significantly lowered. As an example no (partial) reflux of the gaseous overhead stream from the second gas/liquid separator is needed.
- a further advantage is that more sales gas is produced, in particular if the overhead gas is not subsequently liquefied or refluxed to the second gas/liquid separator (contrary to e.g. US 2005/0268649 Al) .
- the hydrocarbon feed stream may be any suitable hydrocarbon-containing stream to be treated, but is usually a natural gas stream which may be obtained from natural gas or petroleum reservoirs.
- the natural gas stream may also be obtained from another source, also including a synthetic source such as a Fischer-Tropsch process.
- the feed stream is comprised substantially of methane.
- the feed stream comprises at least 60 mole% methane, more preferably at least 80 mole% methane .
- the feed stream may contain varying amounts of hydrocarbons heavier than methane such as ethane, propane, butanes and pentanes as well as some aromatic hydrocarbons .
- the feed stream may also contain non-hydrocarbons such as H2O, N2, CO2, H2S and other compounds, and the like.
- the feed stream containing the natural gas may be pre-treated before feeding it to the first gas/liquid separator.
- This pre-treatment may comprise removal of undesired components such as CO2 and H2S, or other steps such as pre-cooling, pre-pressurizing or the like. As these steps are well known to the person skilled in the art, they are not further discussed here.
- the hydrocarbon feed stream contains ⁇ (less than) 1 mole% CO2.
- the first and second gas/liquid separator may be any suitable means for obtaining at least a gaseous stream and a liquid stream, such as a scrubber, distillation column, etc. If desired, three or more gas/liquid separators may be present.
- the second gas/liquid separator is a de-methanizer, i.e. the overhead stream of the second gas/liquid separator being methane-enriched and the bottom stream of the second gas/liquid separator being ethane-enriched when compared with the hydrocarbon feed stream.
- the gaseous and liquid streams may be expanded before feeding them into the second gas/liquid separator.
- the person skilled in the art will understand that the steps of expanding may be performed in various ways using any expansion device (e.g. using a throttling valve, a flash valve or a common expander) .
- treated hydrocarbon streams may be further processed, if desired. Also, further intermediate processing steps between the first and second gas/liquid separator may be performed.
- the invention provides methods and apparatuses wherein a C2+ lean gaseous stream is produced in a plant, whereby a liquefied natural gas (LNG) stream is employed that is obtained from a source of liquefied natural gas from a separate plant .
- LNG liquefied natural gas
- the LNG stream may be fed into the second gas/liquid separator.
- the LNG stream has a temperature below - 100 0 C and is at least partially condensed and comprises more than 60 mole% methane, preferably more than 80 mole% methane.
- source of liquefied natural gas from a separate plant means that the LNG is produced in a separate plant from the plant in which the C2+ lean gaseous stream is produced.
- No LNG stream is used that is generated in the hydrocarbon treating plant of the invention, such as any LNG stream produced during the treating itself or downstream of the treating (e.g. downstream of the second gas/liquid separator) .
- an already existing LNG stream is used that has been produced elsewhere, for example an LNG stream produced in a separate liquefaction plant.
- the separate source may be a storage tank or a stream from a nearby liquefaction plant.
- the LNG stream may have been obtained from an offloading LNG carrier vessel.
- the LNG stream is obtained from a separate plant at an LNG import terminal, such as an LNG storage tank at an LNG import terminal.
- a gaseous stream is removed from the top of the second gas/liquid separator.
- the gaseous stream obtained in step (f) is a C2+ lean gaseous stream.
- C2+ lean is meant a gaseous stream which has a low proportion of hydrocarbons having two or more carbon atoms, including a stream rich in methane, with only a minor proportion of hydrocarbons having two or more carbon atoms.
- the gaseous stream obtained in step (f) is provided with a composition and/or heating value required for used as a sales gas.
- the C2+ lean gaseous stream removed from the top of the second gas/liquid separator in step (f) may comprise ⁇ (less than) 10 mole% hydrocarbons having 2 of more carbon atoms, preferably ⁇ 5 mole%, more preferably ⁇ 2 mole% and even more preferably ⁇ 1 mole%.
- the gaseous stream obtained in step (f) is sent to a gas network and not liquefied to obtain a methane-rich LNG stream. Further it may be that the gaseous stream obtained in step (f) is heat exchanged against the feed stream.
- a liquid stream is removed from the bottom of the second gas/liquid separator.
- This liquid stream may be further processed.
- this liquid stream is subjected to fractionation thereby obtaining two or more products, including ethane .
- > (more than) 75 mole% of hydrocarbons having 2 or more carbon atoms present in the partially condensed feed stream are recovered in the liquid stream obtained from the second gas/liquid separator, preferably > 80, more preferably > 85, even more preferably > 90, most preferably > 95 mole%.
- ⁇ (less than or equal to) 25 mole% of the hydrocarbons having 2 or more carbon atoms present in the partially condensed feed stream are transferred to the gaseous stream obtained in step (f), preferably ⁇ 20, more preferably ⁇ 15, even more preferably ⁇ 10, most preferably ⁇ 5 mole%.
- > (more than) 75 mole% of the ethane present in the partially condensed feed stream is recovered in the liquid stream obtained in step (g), preferably > 80, more preferably > 85, even more preferably > 90, most preferably > 95 mole%.
- ⁇ (less than or equal to) 25 mole% of the ethane present in the partially condensed feed stream is transferred to the gaseous stream obtained from the second gas/liquid separator in step (f), preferably ⁇ 20, more preferably ⁇ 15, even more preferably ⁇ 10, most preferably ⁇ 5 mole%.
- the pressure in the second gas/liquid separator is from 15 to 40 bar, preferably from 20 to 30 bar. Examples include from 23 to 27 bar and about 25 bar.
- Figure 1 schematically shows a process scheme (generally indicated with reference no. 1) for the treating of a hydrocarbon feed stream such as natural gas whereby ethane and heavier hydrocarbons are recovered to a certain extent.
- a hydrocarbon feed stream such as natural gas
- a partly condensed feed stream 10 containing natural gas is supplied to the inlet 21 of the first gas/liquid separator 2 at a certain inlet pressure and inlet temperature.
- the inlet pressure to the first gas/liquid separator 2 will be between 10 and 100 bar, preferably above 30 bar and preferably below 90 bar, more preferably below 70 bar.
- the temperature will usually be between 0 and -80 0 C.
- it may have been pre- cooled in several ways.
- the feed stream 10 may have been further pre-treated before it is fed to the first gas/liquid separator 2.
- H2O, CO2, H2S and hydrocarbon components having the molecular weight of pentane or higher may also at least partially have been removed from the feed stream 10 before entering the first separator 2.
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- Engineering & Computer Science (AREA)
- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Mechanical Engineering (AREA)
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- General Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Separation By Low-Temperature Treatments (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
Description
Claims
Priority Applications (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP07788495A EP2054685A2 (en) | 2006-08-23 | 2007-08-21 | Method and apparatus for treating a hydrocarbon stream |
CN2007800310082A CN101506606B (en) | 2006-08-23 | 2007-08-21 | Method and apparatus for treating a hydrocarbon stream |
JP2009525048A JP2010501657A (en) | 2006-08-23 | 2007-08-21 | Method and apparatus for treating hydrocarbon streams |
US12/438,032 US20100162753A1 (en) | 2006-08-23 | 2007-08-21 | Method and apparatus for treating a hydrocarbon stream |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP06119358.7 | 2006-08-23 | ||
EP06119358 | 2006-08-23 |
Publications (2)
Publication Number | Publication Date |
---|---|
WO2008022998A2 true WO2008022998A2 (en) | 2008-02-28 |
WO2008022998A3 WO2008022998A3 (en) | 2008-11-20 |
Family
ID=37831502
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/EP2007/058648 WO2008022998A2 (en) | 2006-08-23 | 2007-08-21 | Method and apparatus for treating a hydrocarbon stream |
Country Status (6)
Country | Link |
---|---|
US (1) | US20100162753A1 (en) |
EP (1) | EP2054685A2 (en) |
JP (1) | JP2010501657A (en) |
KR (1) | KR20090068213A (en) |
CN (1) | CN101506606B (en) |
WO (1) | WO2008022998A2 (en) |
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- 2007-08-21 US US12/438,032 patent/US20100162753A1/en not_active Abandoned
- 2007-08-21 JP JP2009525048A patent/JP2010501657A/en active Pending
- 2007-08-21 CN CN2007800310082A patent/CN101506606B/en not_active Expired - Fee Related
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RU2748142C1 (en) * | 2020-01-09 | 2021-05-19 | Андрей Владиславович Курочкин | Associated oil gas treatment plant with production of broad fraction of light hydrocarbons (versions) |
Also Published As
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EP2054685A2 (en) | 2009-05-06 |
US20100162753A1 (en) | 2010-07-01 |
KR20090068213A (en) | 2009-06-25 |
CN101506606B (en) | 2011-06-08 |
WO2008022998A3 (en) | 2008-11-20 |
CN101506606A (en) | 2009-08-12 |
JP2010501657A (en) | 2010-01-21 |
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