公开(公告)号：US20080182912A1

公开(公告)日：2008-07-31

申请号：US11933989

申请日：2007-11-01

申请人： Robert Erwin Van Den Berg ,  Franciscus Gerardus Van Dongen ,  Thomas Paul Von Kossak-Glowczewski ,  Hendrik Jan Van Der Ploeg ,  Pieter Lammert Zuideveld

发明人： Robert Erwin Van Den Berg ,  Franciscus Gerardus Van Dongen ,  Thomas Paul Von Kossak-Glowczewski ,  Hendrik Jan Van Der Ploeg ,  Pieter Lammert Zuideveld

IPC分类号： C07C27/00

CPC分类号： C10G2/332 ,  C10G2/32 ,  C10G2300/1022 ,  C10G2300/202 ,  C10G2300/805 ,  C10J3/485 ,  C10J3/845 ,  C10J2200/09 ,  C10J2200/152 ,  C10J2300/0903 ,  C10J2300/093 ,  C10J2300/0943 ,  C10J2300/0959 ,  C10J2300/1659 ,  C10J2300/1678 ,  C10J2300/1823 ,  C10J2300/1846 ,  C10K1/002 ,  C10K1/004 ,  C10K1/005 ,  C10K1/006 ,  C10K1/007 ,  C10K1/04 ,  C10K1/08 ,  C10K1/101 ,  C10K1/143 ,  C10K1/16 ,  C10K1/165 ,  C10K3/04 ,  F02C3/28 ,  F05D2220/722 ,  Y02E20/18

摘要： A process to prepare a paraffinic hydrocarbon from a solid carbonaceous feedstock, preferably coal by performing the following steps, (a) feeding an oxygen comprising gas and the carbonaceous feedstock to a burner positioned horizontal and firing into a reactor vessel, (b) performing a partial oxidation of the carbonaceous feedstock in said burner to obtain a stream of hot synthesis gas which flows upwardly relative to the burner and a liquid slag which flows downwardly relative to the burner, (c) cooling the hot synthesis gas by first cooling the gas to a temperature of between 500 and 900° C. by injecting a gaseous or liquid cooling medium into the synthesis gas and subsequently second cooling the gas in to below 500° C. by directly contacting with water, (d) separating solids from the cooled synthesis gas by means of a water scrubbing process step, (e) performing a water shift reaction on at least part of the scrubbed synthesis gas, (f) separating sulphur compounds, carbon dioxide and other possible impurities from the shifted gas to obtain a purified synthesis gas, and (g) performing a Fischer-Tropsch synthesis using the purified synthesis gas of step (f) to obtain a synthesis product comprising paraffinic hydrocarbons.

摘要翻译： （a）通过进行以下步骤从固体碳质原料，优选煤制备链烷烃，（a）将包含气体和含碳原料的氧气供给到水平放置并燃烧到反应器容器中的燃烧器，（b） 在所述燃烧器中部分氧化碳质原料以获得相对于燃烧器向上流动的热合成气流和相对于燃烧器向下流动的液态炉渣，（c）通过首先将气体冷却至 通过将气体或液体冷却介质注入合成气中并随后通过与水直接接触将气体再次冷却至低于500℃，（d）从冷却的合成物中分离固体，从而将温度介于500和900℃之间 （e）在洗涤的合成气的至少一部分上进行水转化反应，（f）分离硫化合物，二氧化碳 和来自转移气体的其它可能的杂质以获得纯化的合成气，和（g）使用步骤（f）的纯化合成气进行费 - 托合成，以获得包含链烷烃的合成产物。

公开(公告)号：US07741377B2

公开(公告)日：2010-06-22

申请号：US11933989

申请日：2007-11-01

申请人： Robert Erwin Van Den Berg ,  Franciscus Gerardus Van Dongen ,  Thomas Paul Von Kossak-Glowczewski ,  Hendrik Jan Van Der Ploeg ,  Pieter Lammert Zuideveld

发明人： Robert Erwin Van Den Berg ,  Franciscus Gerardus Van Dongen ,  Thomas Paul Von Kossak-Glowczewski ,  Hendrik Jan Van Der Ploeg ,  Pieter Lammert Zuideveld

IPC分类号： C07C27/00 ,  C01B3/32 ,  C10G47/00

CPC分类号： C10G2/332 ,  C10G2/32 ,  C10G2300/1022 ,  C10G2300/202 ,  C10G2300/805 ,  C10J3/485 ,  C10J3/845 ,  C10J2200/09 ,  C10J2200/152 ,  C10J2300/0903 ,  C10J2300/093 ,  C10J2300/0943 ,  C10J2300/0959 ,  C10J2300/1659 ,  C10J2300/1678 ,  C10J2300/1823 ,  C10J2300/1846 ,  C10K1/002 ,  C10K1/004 ,  C10K1/005 ,  C10K1/006 ,  C10K1/007 ,  C10K1/04 ,  C10K1/08 ,  C10K1/101 ,  C10K1/143 ,  C10K1/16 ,  C10K1/165 ,  C10K3/04 ,  F02C3/28 ,  F05D2220/722 ,  Y02E20/18

摘要： A process to prepare a paraffinic hydrocarbon from a solid carbonaceous feedstock, preferably coal by performing the following steps,(a) feeding an oxygen comprising gas and the carbonaceous feedstock to a burner positioned horizontal and firing into a reactor vessel,(b) performing a partial oxidation of the carbonaceous feedstock in said burner to obtain a stream of hot synthesis gas which flows upwardly relative to the burner and a liquid slag which flows downwardly relative to the burner,(c) cooling the hot synthesis gas by first cooling the gas to a temperature of between 500 and 900° C. by injecting a gaseous or liquid cooling medium into the synthesis gas and subsequently second cooling the gas in to below 500° C. by directly contacting with water, (d) separating solids from the cooled synthesis gas by means of a water scrubbing process step, (e) performing a water shift reaction on at least part of the scrubbed synthesis gas, (f) separating sulphur compounds, carbon dioxide and other possible impurities from the shifted gas to obtain a purified synthesis gas, and (g) performing a Fischer-Tropsch synthesis using the purified synthesis gas of step (f) to obtain a synthesis product comprising paraffinic hydrocarbons.

摘要翻译： （a）通过进行以下步骤从固体碳质原料，优选煤制备链烷烃，（a）将包含气体和含碳原料的氧气供给到水平放置并燃烧到反应器容器中的燃烧器，（b） 在所述燃烧器中部分氧化碳质原料以获得相对于燃烧器向上流动的热合成气流和相对于燃烧器向下流动的液态炉渣，（c）通过首先将气体冷却至 通过将气体或液体冷却介质注入合成气中并随后通过与水直接接触将气体再次冷却至低于500℃，（d）从冷却的合成物中分离固体，从而将温度介于500和900℃之间 （e）在洗涤的合成气的至少一部分上进行水转化反应，（f）分离硫化合物，二氧化碳 和来自转移气体的其它可能的杂质以获得纯化的合成气，和（g）使用步骤（f）的纯化合成气进行费 - 托合成，以获得包含链烷烃的合成产物。

公开(公告)号：US08685119B2

公开(公告)日：2014-04-01

申请号：US11416432

申请日：2006-05-02

申请人： Robert Erwin Van Den Berg ,  Franciscus Gerardus Van Dongen ,  Thomas Paul Von Kossak-Glowczewski ,  Henrik Jan Van Der Ploeg ,  Pieter Lammert Zuideveld

发明人： Robert Erwin Van Den Berg ,  Franciscus Gerardus Van Dongen ,  Thomas Paul Von Kossak-Glowczewski ,  Henrik Jan Van Der Ploeg ,  Pieter Lammert Zuideveld

IPC分类号： B01J7/00

CPC分类号： C10J3/845 ,  C10J3/466 ,  C10J3/84 ,  C10J2300/093 ,  C10J2300/0956 ,  C10J2300/0959 ,  C10J2300/1807 ,  C10K1/101 ,  F28C3/06

摘要： A method and system for producing synthesis gas comprising CO, CO2, and H2 from a carbonaceous stream using an oxygen containing stream. A stream containing a carbonaceous material, and a stream containing oxygen are injected into a gasification reactor, where the carbonaceous stream is partially oxidized to obtain a raw synthesis gas. The raw synthesis gas is removed from the gasification reactor and directed into a quenching section wherein a liquid, preferably water, is injected in the form of a mist.

摘要翻译： 一种使用含氧流从含碳物流生产包含CO，CO 2和H 2的合成气的方法和系统。 将含有碳质材料的流和含氧气流注入气化反应器中，其中碳质物流被部分氧化以获得原始合成气。 将原始合成气从气化反应器中取出并导入淬火部分，其中以雾状喷射液体，优选水。

公开(公告)号：US08986631B2

公开(公告)日：2015-03-24

申请号：US12264121

申请日：2008-11-03

申请人： Wouter Detlof Berggren ,  Franciscus Gerardus Van Dongen ,  Thian Hoey Tio ,  Pieter Lammert Zuideveld

发明人： Wouter Detlof Berggren ,  Franciscus Gerardus Van Dongen ,  Thian Hoey Tio ,  Pieter Lammert Zuideveld

IPC分类号： B01J8/06 ,  B01J8/00 ,  B01J8/04 ,  C01B3/38

CPC分类号： B01J8/067 ,  B01J8/008 ,  B01J8/0449 ,  B01J8/0496 ,  B01J8/062 ,  B01J2208/00309 ,  B01J2208/00495 ,  B01J2208/00504 ,  C01B3/382 ,  C01B3/384 ,  C01B2203/00 ,  C01B2203/0233 ,  C01B2203/0244 ,  C01B2203/025 ,  C01B2203/0255 ,  C01B2203/0405 ,  C01B2203/042 ,  C01B2203/062 ,  C01B2203/0844 ,  C01B2203/1052 ,  C01B2203/1058 ,  C01B2203/1064 ,  C01B2203/1082 ,  C01B2203/1241 ,  C01B2203/141 ,  C01B2203/142 ,  C01B2203/143 ,  C01B2203/148 ,  C01B2203/82

摘要： A reactor vessel for performing a steam reforming reaction having a vessel inlet for natural gas and steam; a vessel inlet for a hot gaseous medium; a vessel outlet for the steam reforming product; and a reactor space which is a bed of steam reforming catalyst, which reactor space inlet is fluidly connected to the inlet for natural gas and steam and at its outlet end fluidly connected with the outlet for the gaseous product; wherein inside the catalyst bed a passageway is provided fluidly connected to the vessel inlet for the hot gaseous medium for passage of hot gaseous mixture counter currently to the flow of reactants in the catalyst bed.

摘要翻译： 一种用于进行具有用于天然气和蒸汽的容器入口的蒸汽重整反应的反应器容器; 用于热气体介质的容器入口; 用于蒸汽重整产物的容器出口; 以及作为蒸汽重整催化剂床的反应器空间，该反应器空间入口流体地连接到用于天然气和蒸汽的入口，并且其出口端与气态产物的出口流体连接; 其中在催化剂床内部设有流体连接到用于热气态介质的容器入口的通道，用于将热气体混合物计数器当前通到催化剂床中的反应物流。

公开(公告)号：US20090126272A1

公开(公告)日：2009-05-21

申请号：US12264121

申请日：2008-11-03

申请人： Wouter Detlof Berggren ,  Franciscus Gerardus Van Dongen ,  Thian Hoey Tio ,  Pieter Lammert Zuideveld

发明人： Wouter Detlof Berggren ,  Franciscus Gerardus Van Dongen ,  Thian Hoey Tio ,  Pieter Lammert Zuideveld

IPC分类号： C10J3/20

CPC分类号： B01J8/067 ,  B01J8/008 ,  B01J8/0449 ,  B01J8/0496 ,  B01J8/062 ,  B01J2208/00309 ,  B01J2208/00495 ,  B01J2208/00504 ,  C01B3/382 ,  C01B3/384 ,  C01B2203/00 ,  C01B2203/0233 ,  C01B2203/0244 ,  C01B2203/025 ,  C01B2203/0255 ,  C01B2203/0405 ,  C01B2203/042 ,  C01B2203/062 ,  C01B2203/0844 ,  C01B2203/1052 ,  C01B2203/1058 ,  C01B2203/1064 ,  C01B2203/1082 ,  C01B2203/1241 ,  C01B2203/141 ,  C01B2203/142 ,  C01B2203/143 ,  C01B2203/148 ,  C01B2203/82

摘要： A reactor vessel for performing a steam reforming reaction having a vessel inlet for natural gas and steam; a vessel inlet for a hot gaseous medium; a vessel outlet for the steam reforming product; and a reactor space which is a bed of steam reforming catalyst, which reactor space inlet is fluidly connected to the inlet for natural gas and steam and at its outlet end fluidly connected with the outlet for the gaseous product; wherein inside the catalyst bed a passageway is provided fluidly connected to the vessel inlet for the hot gaseous medium for passage of hot gaseous mixture counter currently to the flow of reactants in the catalyst bed.

摘要翻译： 一种用于进行具有用于天然气和蒸汽的容器入口的蒸汽重整反应的反应器容器; 用于热气体介质的容器入口; 用于蒸汽重整产物的容器出口; 以及作为蒸汽重整催化剂床的反应器空间，该反应器空间入口流体地连接到用于天然气和蒸汽的入口，并且其出口端与气态产物的出口流体连接; 其中在催化剂床内部设有流体连接到用于热气态介质的容器入口的通道，用于将热气体混合物计数器当前通到催化剂床中的反应物流。

公开(公告)号：US07462209B2

公开(公告)日：2008-12-09

申请号：US10552553

申请日：2004-04-13

申请人： Wouter Detlof Berggren ,  Franciscus Gerardus Van Dongen ,  Thian Hoey Tio ,  Pieter Lammert Zuideveld

发明人： Wouter Detlof Berggren ,  Franciscus Gerardus Van Dongen ,  Thian Hoey Tio ,  Pieter Lammert Zuideveld

IPC分类号： C01B3/36 ,  C01B3/24 ,  C01B3/26 ,  B01J8/00

CPC分类号： B01J8/067 ,  B01J8/008 ,  B01J8/0449 ,  B01J8/0496 ,  B01J8/062 ,  B01J2208/00309 ,  B01J2208/00495 ,  B01J2208/00504 ,  C01B3/382 ,  C01B3/384 ,  C01B2203/00 ,  C01B2203/0233 ,  C01B2203/0244 ,  C01B2203/025 ,  C01B2203/0255 ,  C01B2203/0405 ,  C01B2203/042 ,  C01B2203/062 ,  C01B2203/0844 ,  C01B2203/1052 ,  C01B2203/1058 ,  C01B2203/1064 ,  C01B2203/1082 ,  C01B2203/1241 ,  C01B2203/141 ,  C01B2203/142 ,  C01B2203/143 ,  C01B2203/148 ,  C01B2203/82

摘要： A reactor vessel for performing a steam reforming reaction having a vessel inlet for natural gas and steam; a vessel inlet for a hot gaseous medium; a vessel outlet for the steam reforming product; and a reactor space which is a bed of steam reforming catalyst, which reactor space inlet is fluidly connected to the inlet for natural gas and steam and at its outlet end fluidly connected with the outlet for the gaseous product; wherein inside the catalyst bed a passageway is provided fluidly connected to the vessel inlet for the hot gaseous medium for passage of hot gaseous mixture counter currently to the flow of reactants in the catalyst bed.

摘要翻译： 一种用于进行具有用于天然气和蒸汽的容器入口的蒸汽重整反应的反应器容器; 用于热气体介质的容器入口; 用于蒸汽重整产物的容器出口; 以及作为蒸汽重整催化剂床的反应器空间，该反应器空间入口流体地连接到用于天然气和蒸汽的入口，并且其出口端与气态产物的出口流体连接; 其中在催化剂床内部设有流体连接到用于热气态介质的容器入口的通道，用于将热气体混合物计数器当前通到催化剂床中的反应物流。