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1. 发明申请

WO2010056692A2 MULTIPLE GASIFIERS MANIFOLDED TO MULTIPLE FISCHER-TROPSCH REACTORS WITH OPTIONAL RECYCLE TO THE REACTORS 审中-公开
标题翻译：向多个费希尔反应器输送多种气体，并可选择回收反应器
公开(公告)号：WO2010056692A2
公开(公告)日：2010-05-20
申请号：PCT/US2009/063957
申请日：2009-11-11
申请人： RENTECH, INC. , LEE, Joshua G. , IBSEN, Mark , HOGSETT, Robert F. , WRIGHT, Harold A.
发明人： LEE, Joshua G. , IBSEN, Mark , HOGSETT, Robert F. , WRIGHT, Harold A.
IPC分类号： C10J3/06 , C10L3/10 , C10G2/00
CPC分类号： C10J3/721 , C10G2/32 , C10J3/723 , C10J2300/1659 , C10K1/004 , Y02E60/324
摘要： A method of producing synthesis gas via gasification in a Fischer-Tropsch plant, the method including providing a number of gasifiers, the number of gasifiers provided being at least one more than the base number required to provide 100% plant capacity of synthesis gas when each gasifier is operated at 100% gasifier capacity. A method of continually producing synthesis gas via gasification of a carbonaceous feed in a Fischer-Tropsch plant by providing a number of gasifiers, the number of gasifiers provided being at least one more than the base number required to provide 100% plant capacity of synthesis gas when each gasifier is operated at 100% gasifier capacity; and adjusting the amount of synthesis gas produced by adjusting the number of online gasifiers, the flow rate of carbonaceous feed to each gasifier, or a combination thereof. A system for carrying out the method is also provided.
摘要翻译：在费 - 托装置中通过气化生产合成气的方法，所述方法包括提供多个气化器，所提供的气化器的数量比提供100个所需的基数多至少一个当每台气化器在100％气化器容量下运行时，合成气的设备容量百分比。通过提供多个气化器，通过在费 - 托装置中碳化物进料的气化来连续生产合成气的方法，所提供的气化器的数量比提供100％装置容量的合成气所需的基数多至少一个当每个气化器以100％的气化器容量运行时; 以及通过调节在线气化器的数量，到每个气化器的碳质进料的流速或其组合来调节生产的合成气的量。还提供了执行该方法的系统。

2. 发明申请

WO2009035974A1 COMMERCIAL FISCHER-TROPSCH REACTOR 审中-公开
标题翻译：商业FISCHER-TROPSCH反应堆
公开(公告)号：WO2009035974A1
公开(公告)日：2009-03-19
申请号：PCT/US2008/075709
申请日：2008-09-09
申请人： RENTECH, INC. , IBSEN, Mark , MOHEDAS, Sergio , HOGSETT, Frank , BOHN, Mark , WRIGHT, Harold A.
发明人： IBSEN, Mark , MOHEDAS, Sergio , HOGSETT, Frank , BOHN, Mark , WRIGHT, Harold A.
IPC分类号： B01J19/00 , B01J35/00 , B01J8/00 , C07C27/00
CPC分类号： B03C1/02 , B01J8/005 , B01J8/007 , B01J8/22 , B01J8/228 , B01J35/0033 , B03C1/288 , B03C1/30 , B03C2201/18 , C10G2/33 , C10G2/332 , C10G2/342 , C10G45/00 , C10G45/58 , C10G47/00
摘要： A catalytic reaction system comprising: a catalytic reactor fluidly connected with at least two slurry loops, wherein the reactor comprises at least as many reactor product outlets and at least as many slurry return inlets as slurry loops; wherein each slurry loop comprises a separation system comprising a separation system inlet, a separation system product outlet, and a concentrated catalyst slurry outlet; a slurry offtake fluidly connecting the separation system inlet with one of the reactor product outlets; and a slurry return fluidly connecting the separation system outlet with one of the slurry return inlets. The system may comprise at least three slurry loops. The system may comprise at least four slurry loops. A method for converting synthesis gas into liquid hydrocarbons via the catalytic reaction system in also disclosed.
摘要翻译：一种催化反应系统，包括：与至少两个淤浆环流体连接的催化反应器，其中所述反应器至少包含反应器产物出口和至少与淤浆循环一样多的浆料返回入口; 其中每个浆料回路包括分离系统，其包括分离系统入口，分离系统产物出口和浓缩的催化剂浆料出口; 将分离系统入口与其中一个反应器产物出口流体连接的出料浆料; 以及将分离系统出口与其中一个浆料回流入口流体连接的浆料返回。该系统可以包括至少三个淤浆循环。该系统可以包括至少四个浆料循环。还公开了通过催化反应系统将合成气转化为液态烃的方法。

3. 发明申请

WO2013016703A2 GASIFICATION SYSTEM AND METHOD 审中-公开
公开(公告)号：WO2013016703A2
公开(公告)日：2013-01-31
申请号：PCT/US2012/048715
申请日：2012-07-27
申请人： RENTECH, INC. , JIANG, Weibin , MCCOMISH, Bruce , BORUM, Bryan C. , CARRYER, Benjamin , IBSEN, Mark , ROBERTSON, Mark , ELROD, Eric , WEEKS, Sim , WRIGHT, Harold A.
发明人： JIANG, Weibin , MCCOMISH, Bruce , BORUM, Bryan C. , CARRYER, Benjamin , IBSEN, Mark , ROBERTSON, Mark , ELROD, Eric , WEEKS, Sim , WRIGHT, Harold A.
IPC分类号： C10J3/48 , C10J3/72 , C10G2/00 , C07C1/04 , F02C3/28
CPC分类号： C10J3/466 , B01J19/00 , C01B3/583 , C01B2203/044 , C01B2203/047 , C01B2203/062 , C10G2/332 , C10J3/485 , C10J3/56 , C10J2300/0909 , C10J2300/0916 , C10J2300/0923 , C10J2300/093 , C10J2300/0946 , C10J2300/12 , C10J2300/1618 , C10J2300/1637 , C10J2300/165 , C10J2300/1659 , C10J2300/1671 , C10J2300/1807 , C10J2300/1823 , C10K3/00 , F02G3/00 , Y02E50/32 , Y02P20/129 , Y02P20/145
摘要： A system configured for the production of at least one product selected from the group consisting of syngas, Fischer-Tropsch synthesis products, power, and chemicals, the system comprising a dual fluidized bed gasification apparatus and at least one apparatus selected from power production apparatus configured to produce power from the gasification product gas, partial oxidation reactors configured for oxidation of at least a portion of the product gas, tar removal apparatus configured to reduce the amount of tar in the product gas, Fischer-Tropsch synthesis apparatus configured to produce Fischer-Tropsch synthesis products from at least a portion of the product gas, chemical production apparatus configured for the production of at least one non-Fischer-Tropsch product from at least a portion of the product gas, and dual fluidized bed gasification units configured to alter the composition of the product gas. Methods of operating the system are also provided.

4. 发明申请

WO2013016702A2 GASIFICATION SYSTEM AND METHOD 审中-公开
标题翻译：气化系统和方法
公开(公告)号：WO2013016702A2
公开(公告)日：2013-01-31
申请号：PCT/US2012/048714
申请日：2012-07-27
申请人： RENTECH, INC. , JIANG, Weibin , MCCOMISH, Bruce , BORUM, Bryan C. , CARRYER, Benjamin , IBSEN, Mark , ROBERTSON, Mark , ELROD, Eric , WEEKS, Sim , WRIGHT, Harold A.
发明人： JIANG, Weibin , MCCOMISH, Bruce , BORUM, Bryan C. , CARRYER, Benjamin , IBSEN, Mark , ROBERTSON, Mark , ELROD, Eric , WEEKS, Sim , WRIGHT, Harold A.
IPC分类号： C10J3/48 , C10J3/72 , C10G2/00 , C10J3/84 , C07C1/04
CPC分类号： C10J3/466 , B01J19/00 , C01B3/583 , C01B2203/044 , C01B2203/047 , C01B2203/062 , C10G2/332 , C10J3/485 , C10J3/56 , C10J2300/0909 , C10J2300/0916 , C10J2300/0923 , C10J2300/093 , C10J2300/0946 , C10J2300/12 , C10J2300/1618 , C10J2300/1637 , C10J2300/165 , C10J2300/1659 , C10J2300/1671 , C10J2300/1807 , C10J2300/1823 , C10K3/00 , F02G3/00 , Y02E50/32 , Y02P20/129 , Y02P20/145
摘要： A system configured for the production of at least one product selected from the group consisting of syngas, Fischer-Tropsch synthesis products, power, and chemicals, the system comprising a dual fluidized bed gasification apparatus and at least one apparatus selected from power production apparatus configured to produce power from the gasification product gas, partial oxidation reactors configured for oxidation of at least a portion of the product gas, tar removal apparatus configured to reduce the amount of tar in the product gas, Fischer-Tropsch synthesis apparatus configured to produce Fischer-Tropsch synthesis products from at least a portion of the product gas, chemical production apparatus configured for the production of at least one non-Fischer-Tropsch product from at least a portion of the product gas, and dual fluidized bed gasification units configured to alter the composition of the product gas. Methods of operating the system are also provided.
摘要翻译：配置用于生产从由合成气，费 - 托合成产物，动力和化学品组成的组中选择的至少一种产物的系统，所述系统包括双流化床气化装置，并且至少选自配置为从气化产物气体产生能量的发电装置，配置用于氧化至少一部分产物气体的部分氧化反应器，配置成减少产物气体中焦油量的焦油去除装置，费 - 托合成装置，其被配置成从至少一部分产物气体生产费 - 托合成产物;化学生产装置，其被配置用于从至少一部分产物气体生产至少一种非费 - 托产物;以及双流化床气化单元，其被配置为改变产物气体的组成。还提供了操作系统的方法。

5. 发明申请

WO2013016706A3 GASIFICATION SYSTEM AND METHOD 审中-公开
公开(公告)号：WO2013016706A3
公开(公告)日：2013-01-31
申请号：PCT/US2012/048719
申请日：2012-07-27
申请人： RENTECH, INC. , JIANG, Weibin , MCCOMISH, Bruce , BORUM, Bryan C. , CARRYER, Benjamin , IBSEN, Mark , ROBERTSON, Mark , ELROD, Eric , WEEKS, Sim , WRIGHT, Harold A.
发明人： JIANG, Weibin , MCCOMISH, Bruce , BORUM, Bryan C. , CARRYER, Benjamin , IBSEN, Mark , ROBERTSON, Mark , ELROD, Eric , WEEKS, Sim , WRIGHT, Harold A.
IPC分类号： C10J3/46 , C10G2/00 , B01J19/00 , C07C1/04
摘要： A system configured for the production of at least one product selected from the group consisting of syngas, Fischer-Tropsch synthesis products, power, and chemicals, the system comprising a dual fluidized bed gasification apparatus and at least one apparatus selected from power production apparatus configured to produce power from the gasification product gas, partial oxidation reactors configured for oxidation of at least a portion of the product gas, tar removal apparatus configured to reduce the amount of tar in the product gas, Fischer-Tropsch synthesis apparatus configured to produce Fischer-Tropsch synthesis products from at least a portion of the product gas, chemical production apparatus configured for the production of at least one non-Fischer-Tropsch product from at least a portion of the product gas, and dual fluidized bed gasification units configured to alter the composition of the product gas. Methods of operating the system are also provided.

6. 发明申请

WO2010075047A2 CATALYST ACTIVATION IN FISCHER-TROPSCH PROCESSES 审中-公开
标题翻译： FISCHER-TROPSCH过程中的催化剂活化
公开(公告)号：WO2010075047A2
公开(公告)日：2010-07-01
申请号：PCT/US2009/067944
申请日：2009-12-14
申请人： RENTECH, INC. , IBSEN, Mark , MOHEDAS, Sergio
发明人： IBSEN, Mark , MOHEDAS, Sergio
IPC分类号： B01J37/16 , B01J23/745 , B01J23/75 , B01J38/58 , C10G2/00
CPC分类号： B01J37/18 , B01J23/745 , B01J23/75 , B01J23/78 , B01J37/08 , B01J37/16 , C10G2/332 , C10G2300/703
摘要： A system for activating Fischer-Tropsch catalyst comprising a reactor having an outlet for overhead gas and operable under conditions whereby a catalyst in a volume of liquid carrier comprising Fischer-Tropsch diesel, hydrocracking recycle oil, or a combination thereof may be activated in the presence of an activation gas; a condenser comprising an inlet fluidly connected to the reactor outlet for overhead gas and comprising a condenser outlet for condensed liquids; and a separation unit comprising an inlet fluidly connected to the condenser outlet and a separator outlet for a stream comprising primarily Fischer-Tropsch diesel; and a recycle line fluidly connecting the separator outlet, a hydrocracking unit, or both to the reactor, whereby Fischer-Tropsch diesel recovered from reactor overhead gas, hydrocracking recycle oil, or a combination thereof may serve as liquid carrier for catalyst in the reactor. A method for activating Fischer-Tropsch catalyst is also provided.
摘要翻译：一种用于活化费 - 托催化剂的系统，其包括具有塔顶气体出口的反应器，并且在条件下可操作，其中包含费 - 托柴油，加氢裂化循环油或其组合的一定体积液体载体中的催化剂可在存在下活化的活化气体; 冷凝器，包括流体连接到塔顶气体的反应器出口的入口，并且包括用于冷凝液体的冷凝器出口; 以及分离单元，其包括流体连接到冷凝器出口的入口和用于主要包含费 - 托柴油的物流的分离器出口; 以及将分离器出口，加氢裂化单元或两者流体连接到反应器的再循环管线，由此从反应器塔顶气体回收的费 - 托柴油，加氢裂化循环油或其组合可用作反应器中催化剂的液体载体。还提供了一种活化费 - 托催化剂的方法。

7. 发明申请

WO2009036069A2 HYDROGEN AND CARBON UTILIZATION IN SYNTHETIC FUELS PRODUCTION PLANTS 审中-公开
标题翻译：合成燃料生产厂的氢和碳利用
公开(公告)号：WO2009036069A2
公开(公告)日：2009-03-19
申请号：PCT/US2008/075863
申请日：2008-09-10
申请人： RENTECH, INC , MOHEDAS, Sergio , IBSEN, Mark
发明人： MOHEDAS, Sergio , IBSEN, Mark
IPC分类号： C01B3/56 , C01B3/40 , B01J23/89 , B01J23/75 , B01D53/02
CPC分类号： C10J3/00 , B01J37/16 , B01J37/18 , C01B3/34 , C01B3/56 , C01B2203/0405 , C01B2203/043 , C01B2203/046 , C01B2203/0485 , C01B2203/049 , C01B2203/062 , C10G2/332 , C10G45/60 , C10G47/02 , C10G49/02 , C10G2300/1011 , C10G2300/703 , C10J2300/0916 , C10J2300/093 , C10J2300/0943 , C10J2300/1618 , C10J2300/1659 , C10J2300/1823 , C10K3/00 , Y02P20/145 , Y02P20/52 , Y02P30/20
摘要： A method of utilizing hydrogen in synthesis gas production by forming synthesis gas from one or more carbonaceous materials, the synthesis gas comprising hydrogen and carbon monoxide; separating a hydrogen-rich product and a hydrogen-lean product from the synthesis gas to yield an adjusted synthesis gas product; and activating a hydrocarbon synthesis catalyst with at least a portion of the hydrogen-lean product. A system for carrying out the method is also provided, the system including at least one hydrogen extraction unit and an activation reactor operable to activate hydrocarbon synthesis catalyst, wherein the activation reactor comprises an inlet fluidly connected with the at least one hydrogen extraction unit whereby at least a portion of a hydrogen-lean gas stream, at least a portion of a hydrogen-rich gas stream, or at least a portion of both may be introduced into the activation reactor.
摘要翻译：一种通过从一种或多种含碳材料形成合成气而在合成气生产中利用氢的方法，所述合成气包含氢气和一氧化碳; 从合成气中分离富氢产物和贫氢产物以产生经调节的合成气产物; 以及用至少一部分所述富氢产物活化烃合成催化剂。还提供了一种用于实施该方法的系统，所述系统包括至少一个氢提取单元和可操作以活化烃合成催化剂的活化反应器，其中所述活化反应器包括与所述至少一个氢提取单元流体连接的入口，贫氢气流的至少一部分，富氢气流的至少一部分或两者的至少一部分可以被引入到活化反应器中。

8. 发明公开

EP2356199A2 MULTIPLE GASIFIERS MANIFOLDED TO MULTIPLE FISCHER-TROPSCH REACTORS WITH OPTIONAL RECYCLE TO THE REACTORS 审中-公开
标题翻译：与电抗器可选回收的更多关于多元费 - 托反应器中分布CARB
公开(公告)号：EP2356199A2
公开(公告)日：2011-08-17
申请号：EP09826637.2
申请日：2009-11-11
申请人： Rentech, Inc.
发明人： LEE, Joshua G. , IBSEN, Mark , HOGSETT, Robert F. , WRIGHT, Harold A.
IPC分类号： C10J3/06 , C10L3/10 , C10G2/00
CPC分类号： C10J3/721 , C10G2/32 , C10J3/723 , C10J2300/1659 , C10K1/004 , Y02E60/324
摘要： A method of producing synthesis gas via gasification in a Fischer-Tropsch plant, the method including providing a number of gasifiers, the number of gasifiers provided being at least one more than the base number required to provide 100% plant capacity of synthesis gas when each gasifier is operated at 100% gasifier capacity. A method of continually producing synthesis gas via gasification of a carbonaceous feed in a Fischer-Tropsch plant by providing a number of gasifiers, the number of gasifiers provided being at least one more than the base number required to provide 100% plant capacity of synthesis gas when each gasifier is operated at 100% gasifier capacity; and adjusting the amount of synthesis gas produced by adjusting the number of online gasifiers, the flow rate of carbonaceous feed to each gasifier, or a combination thereof. A system for carrying out the method is also provided.

9. 发明公开

EP2195111A1 COMMERCIAL FISCHER-TROPSCH REACTOR 有权
标题翻译：商业捕鱼 - 托反应器
公开(公告)号：EP2195111A1
公开(公告)日：2010-06-16
申请号：EP08830515.6
申请日：2008-09-09
申请人： Rentech, Inc.
发明人： IBSEN, Mark , MOHEDAS, Sergio , HOGSETT, Frank , BOHN, Mark , WRIGHT, Harold A.
IPC分类号： B01J19/00 , B01J35/00 , B01J8/00 , C07C27/00
CPC分类号： B03C1/02 , B01J8/005 , B01J8/007 , B01J8/22 , B01J8/228 , B01J35/0033 , B03C1/288 , B03C1/30 , B03C2201/18 , C10G2/33 , C10G2/332 , C10G2/342 , C10G45/00 , C10G45/58 , C10G47/00
摘要： A catalytic reaction system comprising: a catalytic reactor fluidly connected with at least two slurry loops, wherein the reactor comprises at least as many reactor product outlets and at least as many slurry return inlets as slurry loops; wherein each slurry loop comprises a separation system comprising a separation system inlet, a separation system product outlet, and a concentrated catalyst slurry outlet; a slurry offtake fluidly connecting the separation system inlet with one of the reactor product outlets; and a slurry return fluidly connecting the separation system outlet with one of the slurry return inlets. The system may comprise at least three slurry loops. The system may comprise at least four slurry loops. A method for converting synthesis gas into liquid hydrocarbons via the catalytic reaction system in also disclosed.

10. 发明公开

EP2737035A2 GASIFICATION SYSTEM AND METHOD 有权
标题翻译：气化系统和方法
公开(公告)号：EP2737035A2
公开(公告)日：2014-06-04
申请号：EP12818341.5
申请日：2012-07-27
申请人： Rentech, Inc.
发明人： JIANG, Weibin , MCCOMISH, Bruce , BORUM, Bryan C. , CARRYER, Benjamin , IBSEN, Mark , ROBERTSON, Mark , ELROD, Eric , WEEKS, Sim , WRIGHT, Harold A.
IPC分类号： C10J3/48 , C10J3/72 , C10G2/00 , C07C1/04 , F02C3/28
CPC分类号： C10J3/466 , B01J19/00 , C01B3/583 , C01B2203/044 , C01B2203/047 , C01B2203/062 , C10G2/332 , C10J3/485 , C10J3/56 , C10J2300/0909 , C10J2300/0916 , C10J2300/0923 , C10J2300/093 , C10J2300/0946 , C10J2300/12 , C10J2300/1618 , C10J2300/1637 , C10J2300/165 , C10J2300/1659 , C10J2300/1671 , C10J2300/1807 , C10J2300/1823 , C10K3/00 , F02G3/00 , Y02E50/32 , Y02P20/129 , Y02P20/145
摘要： A system configured for the production of at least one product selected from the group consisting of syngas, Fischer-Tropsch synthesis products, power, and chemicals, the system comprising a dual fluidized bed gasification apparatus and at least one apparatus selected from power production apparatus configured to produce power from the gasification product gas, partial oxidation reactors configured for oxidation of at least a portion of the product gas, tar removal apparatus configured to reduce the amount of tar in the product gas, Fischer-Tropsch synthesis apparatus configured to produce Fischer-Tropsch synthesis products from at least a portion of the product gas, chemical production apparatus configured for the production of at least one non-Fischer-Tropsch product from at least a portion of the product gas, and dual fluidized bed gasification units configured to alter the composition of the product gas. Methods of operating the system are also provided.

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