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1.发明申请公开(公告)号：US20100313475A1
公开(公告)日：2010-12-16
申请号：US12867451
申请日：2009-02-04
CPC分类号： B01J8/1818 , B01J2208/00752 , C10G1/02
摘要： A process for refining raw materials containing oil and/or bitumen includes supplying the raw materials to a reactor. The reactor is operated under a pressure of from 0.001 to 1 bar and at a reactor temperature of from 300 to 1000° C. so as to volatize fuel gases and obtain solids and non-evaporated fractions of heavy hydrocarbons. The solids and non-evaporated fractions of heavy hydrocarbons are introduced into a furnace. The non-evaporated fractions of heavy hydrocarbons are burned in the furnace at a furnace temperature of from 600 to 1500° C. so as to obtain hot solids in the furnace. The hot solids are recirculated from the furnace into the reactor. An oxidizing atmosphere of the furnace is separated from an atmosphere of the reactor by a sealing device.
摘要翻译： 用于精炼含有油和/或沥青的原料的方法包括将原料供应到反应器中。 反应器在0.001至1巴的压力和300至1000℃的反应器温度下运行，以便挥发燃料气体并获得重质烃的固体和非蒸发馏分。 将重质烃的固体和非蒸发馏分引入炉中。 重质烃的非蒸发馏分在炉中在600至1500℃的炉温下燃烧，以便在炉中获得热固体。 热固体从炉再循环到反应器中。 通过密封装置将炉的氧化气氛与反应器的气氛分离。
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2.发明授权公开(公告)号：US08936657B2
公开(公告)日：2015-01-20
申请号：US12867451
申请日：2009-02-04
CPC分类号： B01J8/1818 , B01J2208/00752 , C10G1/02
摘要： A process for refining raw materials containing at least one of oil and bitumen includes supplying the raw materials to a reactor and volatilizing fuel gas in the reactor at a temperature of from 300 to 1000° C. and a pressure of from 0.001 to 1 bar. Solids remaining in the reactor, including non-evaporated fractions of heavy hydrocarbons, are introduced into a furnace. A staged combustion of the non-evaporated fractions of heavy hydrocarbons is performed in a substoichiometric stage and in a superstoichiometric stage in the furnace at a furnace temperature of from 600 to 1500° C. as to obtain hot solids in the furnace. The hot solids are recirculated from the furnace into the reactor. A sealing device separates an oxidizing atmosphere of the furnace from an atmosphere of the reactor.
摘要翻译： 用于精炼含有油和沥青中的至少一种的原料的方法包括将原料供应到反应器中并在300-1000℃的温度和0.001至1巴的压力下使反应器中的燃料气体挥发。 残留在反应器中的固体，包括重质烃的非蒸发馏分，被引入炉中。 未蒸发馏分的重质烃的分段燃烧是在600至1500℃的炉温下在化学计量阶段和炉中的超化学计量阶段进行的，以便在炉中获得热固体。 热固体从炉再循环到反应器中。 密封装置将炉的氧化气氛与反应器的气氛分离。
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公开(公告)号：US20140290480A1
公开(公告)日：2014-10-02
申请号：US14351883
申请日：2012-10-10
IPC分类号： B03C3/00
CPC分类号： B03C3/00
摘要： A process for dedusting a dust laden vapor gas mixture (VGM) obtained by pyrolysis of a material containing hydrocarbons includes treating the dust laden VGM in a dry electrostatic precipitator at a temperature in a range from 380 to 480° C. so as to separate dust from the VGM. Then, the VGM is cooled to a temperature in a range from 310 to 360° C.
摘要翻译： 通过对含有烃的材料进行热解而获得的含灰尘蒸汽气体混合物（VGM）的除尘方法包括在380-480℃的温度范围内，在干式静电除尘器中处理载有灰尘的VGM，以分离灰尘 来自VGM。 然后，将VGM冷却至310〜360℃的温度。
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公开(公告)号：US09221062B2
公开(公告)日：2015-12-29
申请号：US14351883
申请日：2012-10-10
IPC分类号： B03C3/00
CPC分类号： B03C3/00
摘要： A process for dedusting a dust laden vapor gas mixture (VGM) obtained by pyrolysis of a material containing hydrocarbons includes treating the dust laden VGM in a dry electrostatic precipitator at a temperature in a range from 380 to 480° C. so as to separate dust from the VGM. Then, the VGM is cooled to a temperature in a range from 310 to 360° C.
摘要翻译： 通过对含有烃的材料进行热解而获得的含灰尘蒸汽气体混合物（VGM）的除尘方法包括在380-480℃的温度范围内，在干式静电除尘器中处理载有灰尘的VGM，以分离灰尘 来自VGM。 然后，将VGM冷却至310〜360℃的温度。
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公开(公告)号：US09090984B2
公开(公告)日：2015-07-28
申请号：US14362629
申请日：2012-11-28
申请人： Nikola Anastasijevic , Jan Holst , Andreas Orth , Markus Schuster , Bernd Schurtakow , Michael Stroeder
发明人： Nikola Anastasijevic , Jan Holst , Andreas Orth , Markus Schuster , Bernd Schurtakow , Michael Stroeder
IPC分类号： B01D53/32 , B03C3/16 , C25B15/08 , C07C1/12 , C25B1/04 , B03C3/017 , B01D53/86 , C01B13/02 , C25B9/06
CPC分类号： C25B15/08 , B01D53/323 , B01D53/8671 , B01D2256/16 , B01D2257/104 , B03C3/017 , B03C3/16 , C01B13/0207 , C07C1/12 , C25B1/04 , C25B9/06 , Y02C20/20 , Y02E60/366 , C07C9/04
摘要： A process for producing hydrogen for use in a subsequent methanation process includes electrochemically converting water into hydrogen and oxygen. The hydrogen is depleted with electrolyte aerosols. Then, the electrolyte aerosols are separated from the depleted hydrogen in a wet electrostatic precipitator in a hydrogen atmosphere.
摘要翻译： 用于后续甲烷化处理的用于生产氢的方法包括将水电化学转化为氢和氧。 氢气用电解质气溶胶消耗。 然后，在氢气氛中，在湿式静电除尘器中将电解质气溶胶与贫化氢分离。
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公开(公告)号：US09034076B2
公开(公告)日：2015-05-19
申请号：US14352061
申请日：2012-10-10
申请人： Hermann Sieger , Christian Binder , Hans-Joachim Werz , Nikola Anastasijevic , Andreas Orth , Aleksandr Kaidalov , Kirill Kaidalov
发明人： Hermann Sieger , Christian Binder , Hans-Joachim Werz , Nikola Anastasijevic , Andreas Orth , Aleksandr Kaidalov , Kirill Kaidalov
摘要： A process for winning oil from a vapor gas mixture (VGM) containing a plurality of oil fractions obtained by the pyrolysis of a hydrocarbon containing material includes dedusting and cooling the VGM. The dedusted and cooled VGM are fractionated in at least two electrostatic precipitator stages at respective temperatures corresponding to respective boiling points of the oil fractions so as to separate the oil fractions.
摘要翻译： 从含有通过含烃材料的热分解获得的多个油馏分的蒸气混合物（VGM）中获得油的方法包括除尘和冷却VGM。 除尘和冷却的VGM在至少两个静电除尘器阶段中在对应于油馏分的相应沸点的相应温度下分馏，以分离油馏分。
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公开(公告)号：US20140251132A1
公开(公告)日：2014-09-11
申请号：US14352061
申请日：2012-10-10
申请人： Hermann Sieger , Christian Binder , Hans-Joachim Werz , Nikola Anastasijevic , Andreas Orth , Aleksandr Kaidalov , Kirill Kaidalov
发明人： Hermann Sieger , Christian Binder , Hans-Joachim Werz , Nikola Anastasijevic , Andreas Orth , Aleksandr Kaidalov , Kirill Kaidalov
IPC分类号： B03C3/011
摘要： A process for winning oil from a vapor gas mixture (VGM) containing a plurality of oil fractions obtained by the pyrolysis of a hydrocarbon containing material includes dedusting and cooling the VGM. The dedusted and cooled VGM are fractionated in at least two electrostatic precipitator stages at respective temperatures corresponding to respective boiling points of the oil fractions so as to separate the oil fractions.
摘要翻译： 从含有通过含烃材料的热分解获得的多个油馏分的蒸气混合物（VGM）中获得油的方法包括除尘和冷却VGM。 除尘和冷却的VGM在至少两个静电除尘器阶段中在对应于油馏分的相应沸点的相应温度下分馏，以分离油馏分。
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公开(公告)号：US20110013662A1
公开(公告)日：2011-01-20
申请号：US12675448
申请日：2008-08-28
CPC分类号： B01J8/24 , B01J8/1818 , B01J8/1827 , B01J8/1836 , B01J8/1863 , B01J2208/00176 , B01J2208/00371 , B01J2208/00504 , B01J2208/0053 , B01J2208/00752 , B01J2208/00761 , F23C6/04 , F23C10/10 , F23C2900/10002 , F27B15/02 , F27B15/10
摘要： A process for at least one of a chemical and a physical treatment of fluidizable substances in a reactor. The process includes introducing a hot gas into an interior of the reactor through a gas supply tube and cooling at least one of the hot gas and the gas supply tube with a coolant. The cooling is performed by contacting the hot gas with the coolant so as to provide a temperature of a wall of the gas supply tube at least 50° C. lower than a temperature of the gas at an inlet of the gas supply tube facing away from the interior of the reactor.
摘要翻译： 一种反应器中可流化物质的化学和物理处理中的至少一种的方法。 该方法包括通过气体供应管将热气引入反应器的内部，并用冷却剂冷却至少一个热气体和气体供应管。 通过使热气体与冷却剂接触来进行冷却，从而使供气管壁的温度比气体供给管的入口处的气体的温度低至少50℃， 反应堆的内部。
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公开(公告)号：US08833275B2
公开(公告)日：2014-09-16
申请号：US12675448
申请日：2008-08-28
CPC分类号： B01J8/24 , B01J8/1818 , B01J8/1827 , B01J8/1836 , B01J8/1863 , B01J2208/00176 , B01J2208/00371 , B01J2208/00504 , B01J2208/0053 , B01J2208/00752 , B01J2208/00761 , F23C6/04 , F23C10/10 , F23C2900/10002 , F27B15/02 , F27B15/10
摘要： A process for at least one of a chemical and a physical treatment of fluidizable substances in a reactor. The process includes introducing a hot gas into an interior of the reactor through a gas supply tube and cooling at least one of the hot gas and the gas supply tube with a coolant. The cooling is performed by contacting the hot gas with the coolant so as to provide a temperature of a wall of the gas supply tube at least 50° C. lower than a temperature of the gas at an inlet of the gas supply tube facing away from the interior of the reactor.
摘要翻译： 一种反应器中可流化物质的化学和物理处理中的至少一种的方法。 该方法包括通过气体供应管将热气引入反应器的内部，并用冷却剂冷却至少一个热气体和气体供应管。 通过使热气体与冷却剂接触来进行冷却，从而使供气管壁的温度比气体供给管的入口处的气体的温度低至少50℃， 反应堆的内部。
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10.发明申请公开(公告)号：US20140083010A1
公开(公告)日：2014-03-27
申请号：US14115376
申请日：2012-03-29
申请人： Andreas Orth , Agnes Von Garnier
发明人： Andreas Orth , Agnes Von Garnier
IPC分类号： C10J3/84
CPC分类号： C10J3/84 , C10J3/482 , C10J3/86 , C10J2300/093 , C10J2300/0959 , C10J2300/0976 , C10J2300/1884 , C10J2300/1892 , C21B13/0073 , C21C5/5217 , Y02P10/216
摘要： A process for producing fuel gas and for carrying out a metallurgical process includes providing first and second process stages. In the first process stage, biomass is reacted with an oxygen-containing gas so as to obtain a fuel gas containing at least one of carbon monoxide, hydrogen, carbon dioxide and steam. The fuel gas is cooled to a temperature in a range from 300 to 600° C. The cooled fuel gas is subjected to a solids separation. In the second process stage, the fuel gas after the solids separation is directly supplied to at least one burner of the metallurgical process, the temperature of the fuel gas being maintained above the condensation temperature of tar and within the range from 300 to 600° C. by supplying heat.
摘要翻译： 用于生产燃料气体和用于进行冶金工艺的方法包括提供第一和第二工艺阶段。 在第一工艺阶段，生物质与含氧气体反应，以获得含有一氧化碳，氢气，二氧化碳和蒸汽中的至少一种的燃料气体。 将燃料气体冷却至300至600℃的温度。冷却的燃料气体进行固体分离。 在第二工艺阶段，将固体分离后的燃料气体直接供给至少一个冶金过程的燃烧器，燃料气体的温度保持在焦油的冷凝温度以上，范围为300-600℃ 通过供热。
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