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公开(公告)号:WO2011099850A3
公开(公告)日:2011-10-06
申请号:PCT/NL2011050091
申请日:2011-02-09
Applicant: STICHTING ENERGIE , BOS ALEXANDER , ZWART ROBIN WILLEM RUDOLF
Inventor: BOS ALEXANDER , ZWART ROBIN WILLEM RUDOLF
CPC classification number: C10K1/08 , B01D53/1487 , B01D53/70 , B01D53/72 , B01D2251/306 , B01D2251/602 , B01D2251/604 , B01D2252/10 , B01D2252/20 , B01D2257/2066 , B01D2257/7022 , B01D2257/7027 , B01D2257/704 , B01D2257/708 , C10G70/06 , C10K1/16 , Y02P20/154
Abstract: The invention provides a method for the reduction of aerosol in an aerosol comprising gas by contacting the aerosol comprising gas with a liquid, wherein the aerosol comprises an aerosol compound and wherein the aerosol compound comprises an inorganic compound, wherein the liquid comprises a liquid compound and wherein the liquid compound comprises an inorganic compound and wherein the liquid comprises a liquid condensate of the aerosol, wherein the liquid has a higher temperature than the aerosol comprising gas, wherein the temperature difference is in the range of 5- 00 °C; and wherein the liquid has a temperature which is lower than the dew point of the aerosol comprising gas, wherein difference between the dew point temperature of the aerosol comprising gas and the temperature of the liquid is in the range of 5-200 °C.
Abstract translation: 本发明提供了一种通过使包含气体的气溶液与液体接触来减少包含气体的气溶胶的气溶胶的方法,其中所述气雾剂包括气溶胶化合物,并且其中所述气溶胶化合物包含无机化合物,其中所述液体包含液体化合物和 其中所述液体化合物包括无机化合物,并且其中所述液体包括所述气溶胶的液体冷凝物,其中所述液体具有比包含气体的气溶胶更高的温度,其中所述温度差在5-00℃的范围内; 并且其中所述液体的温度低于包含气体的气溶胶的露点,其中包含气体的气溶胶的露点温度与液体温度之间的差在5-200℃的范围内。
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公开(公告)号:CA2774700A1
公开(公告)日:2011-03-31
申请号:CA2774700
申请日:2010-09-24
Applicant: STICHTING ENERGIE
Inventor: ZWART ROBIN WILLEM RUDOLF , BOS ALEXANDER , KUIPERS JOHANNES
Abstract: Method and system for gasifying biomass. Tar loaded gas from the reactor for gasifying the biomass is subjected to a saturation and absorption treatment with a first and second fluid respectively. The first fluid comprises aromatic hydrocarbons whilst the second fluid comprises linear hydrocarbons. Tars received in the aromatic fluid is entered together with such fluid in a separation column. Separation is effected based on evaporation temperature and the lighter fraction is returned to the inflow of the saturation separator. The heavier fractions are either discharged or sent back to the biomass reactor. An intermediate buffer vessel can be provided between the discharge of the saturation cleaner and the separator.
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公开(公告)号:NL2009310C
公开(公告)日:2014-02-18
申请号:NL2009310
申请日:2012-08-10
Applicant: STICHTING ENERGIE
CPC classification number: C10K1/16 , B01D53/1406 , B01D53/1425 , B01D53/145 , B01D53/1487 , B01D53/1493 , B01D2252/205 , B01D2257/7027 , Y02C20/20
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公开(公告)号:NL2004220C2
公开(公告)日:2011-08-15
申请号:NL2004220
申请日:2010-02-10
Applicant: STICHTING ENERGIE
Inventor: BOS ALEXANDER , ZWART ROBIN WILLEM RUDOLF
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公开(公告)号:NL2003547C
公开(公告)日:2011-03-29
申请号:NL2003547
申请日:2009-09-25
Applicant: STICHTING ENERGIE
Inventor: ZWART ROBIN WILLEM RUDOLF , BOS ALEXANDER , KUIPERS JOHANNES
CPC classification number: C10K1/18 , C10J3/466 , C10J3/84 , C10J2300/0916 , C10K1/024 , C10K1/028 , C10K1/046 , Y02P20/145
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公开(公告)号:IN452MUN2015A
公开(公告)日:2015-09-11
申请号:IN452MUN2015
申请日:2015-03-03
Applicant: STICHTING ENERGIE
Abstract: Tar like components can be removed from gas streams resulting from gasification of coal waste or biomass by contacting the gas with a liquid organic aryl polysiloxane. The polysiloxane preferably contains alkyl groups and aryl groups and is in particular a polymethyl polyphenyl polysiloxane. The gas comprises one or more of hydrogen carbon monoxide carbon dioxide and methane.
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公开(公告)号:NL2009310C2
公开(公告)日:2014-02-18
申请号:NL2009310
申请日:2012-08-10
Applicant: STICHTING ENERGIE
Abstract: Tar-like components can be removed from gas streams resulting from gasification of coal, waste or biomass by contacting the gas with a liquid organic aryl polysiloxane. The polysiloxane preferably contains alkyl groups and aryl groups, and is in particular a polymethyl polyphenyl polysiloxane. The gas comprises one or more of hydrogen, carbon monoxide, carbon dioxide, and methane.
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公开(公告)号:NL2004220C
公开(公告)日:2011-08-15
申请号:NL2004220
申请日:2010-02-10
Applicant: STICHTING ENERGIE
Inventor: BOS ALEXANDER , ZWART ROBIN WILLEM RUDOLF
CPC classification number: C10K1/08 , B01D53/1487 , B01D53/70 , B01D53/72 , B01D2251/306 , B01D2251/602 , B01D2251/604 , B01D2252/10 , B01D2252/20 , B01D2257/2066 , B01D2257/7022 , B01D2257/7027 , B01D2257/704 , B01D2257/708 , C10G70/06 , C10K1/16 , Y02P20/154
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公开(公告)号:NL2003547C2
公开(公告)日:2011-03-29
申请号:NL2003547
申请日:2009-09-25
Applicant: STICHTING ENERGIE
Inventor: ZWART ROBIN WILLEM RUDOLF , BOS ALEXANDER , KUIPERS JOHANNES
Abstract: Method and system for gasifying biomass. Tar loaded gas from the reactor for gasifying the biomass is subjected to a saturation and absorption treatment with a first and second fluid respectively. The first fluid comprises aromatic hydrocarbons whilst the second fluid comprises linear hydrocarbons. Tars received in the aromatic fluid is entered together with such fluid in a separation column. Separation is effected based on evaporation temperature and the lighter fraction is returned to the inflow of the saturation separator. The heavier fractions are either discharged or sent back to the biomass reactor. An intermediate buffer vessel can be provided between the discharge of the saturation cleaner and the separator.
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公开(公告)号:ES2493891T3
公开(公告)日:2014-09-12
申请号:ES10763051
申请日:2010-09-24
Applicant: STICHTING ENERGIE
Inventor: ZWART ROBIN WILLEM RUDOLF , BOS ALEXANDER , KUIPERS JOHANNES
Abstract: Método para la gasificación de biomasa en un reactor (3) a una temperatura de entre 600 y1300°C y purificación del flujo de gas resultante del reactor para la eliminación de alquitranes de dicho flujo de gas, comprendiendo la eliminación de dichos alquitranes en dos fases, donde en la primera fase de limpieza (8) el gas del reactor (3) se satura a una temperatura de entre 250 y 900°C con un primer fluido basado en hidrocarburo que comprende hidrocarburos aromáticos y donde en una segunda fase de limpieza (18) después de la primera fase de limpieza (8) los alquitranes restantes son absorbidos del gas con un segundo fluido basado en hidrocarburo, donde una mezcla de los alquitranes y el primer fluido basado en hidrocarburo resultante de la primera fase de limpieza se lleva a una primera fase de separación (23) separada de dicho segundo fluido basado en hidrocarburo, caracterizado por el hecho de que en dicha primera fase de separación (23) la mezcla de alquitranes y el primer fluido basado en hidrocarburo se separan basándose en la temperatura de evaporación, y donde la parte ligera resultante de la primera fase de separación se añade al flujo de gas del reactor (3) en la primera fase de limpieza (8) y donde se elimina la parte pesada
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