公开(公告)号：US20110313061A1

公开(公告)日：2011-12-22

申请号：US12984902

申请日：2011-01-05

申请人： Harold A. Wright ,  Belma Demirel ,  Sergio Mohedas ,  Bahman Rejai ,  Ray Huang ,  Deena Ferdous ,  Jesse W. Taylor ,  Dawid J. Duvenhage ,  Sara L. Rolfe

发明人： Harold A. Wright ,  Belma Demirel ,  Sergio Mohedas ,  Bahman Rejai ,  Ray Huang ,  Deena Ferdous ,  Jesse W. Taylor ,  Dawid J. Duvenhage ,  Sara L. Rolfe

IPC分类号： B01J8/18 ,  C07C1/04 ,  B01J37/18 ,  B01J31/02 ,  B01J37/16

CPC分类号： B01J8/006 ,  B01J8/18 ,  B01J8/1809 ,  B01J23/745 ,  B01J33/00 ,  B01J35/023 ,  B01J37/0045 ,  B01J37/18 ,  C10G2/32 ,  C10G2/33 ,  C10G2/332 ,  C10G2300/703

摘要： A method of preparing a spray dried catalyst by combining spray dried catalyst particles with wax so the spray dried catalyst particles are coated with wax, yielding wax coated catalyst particles, and shaping the wax coated catalyst to provide shaped wax coated catalyst. A method of activating Fischer-Tropsch catalyst particles containing oxides by contacting the catalyst particles with a reducing gas in an activation vessel to produce an activated catalyst, wherein contacting is performed in the absence of a liquid medium under activation conditions. A system for activating a Fischer-Tropsch catalyst containing an activation reactor configured to introduce an activation gas to a fixed or fluidized bed of the Fischer-Tropsch catalyst in the absence of a liquid medium and at least one separation device configured to separate a gas stream comprising entrained catalyst fines having an average particle size below a desired cutoff size from the activation reactor.

摘要翻译： 通过将喷雾干燥的催化剂颗粒与蜡组合来制备喷雾干燥的催化剂的方法，使喷雾干燥的催化剂颗粒用蜡涂覆，产生蜡涂覆的催化剂颗粒，并使蜡涂覆的催化剂成形以提供成形的涂蜡催化剂。 通过使催化剂颗粒与活化容器中的还原气体接触以产生活化的催化剂来活化含有氧化物的费 - 托催化剂颗粒的方法，其中在不存在液体介质的条件下进行接触。 一种用于活化费 - 托催化剂的系统，其包含活化反应器，所述活化反应器配置成在没有液体介质的情况下将活化气体引入费 - 托催化剂的固定或流化床，以及至少一个分离装置，其被配置为分离气流 包括夹带的催化剂细粒，其具有低于来自活化反应器的所需截留尺寸的平均粒度。

公开(公告)号：US07915193B2

公开(公告)日：2011-03-29

申请号：US12272960

申请日：2008-11-18

申请人： Belma Demirel ,  Charles B. Benham ,  Dan Fraenkel ,  Richard Bley ,  Jesse W. Taylor ,  Bahman Rejai ,  Sara Rolfe ,  Harold A. Wright

发明人： Belma Demirel ,  Charles B. Benham ,  Dan Fraenkel ,  Richard Bley ,  Jesse W. Taylor ,  Bahman Rejai ,  Sara Rolfe ,  Harold A. Wright

IPC分类号： B01J23/42

CPC分类号： B01J37/18 ,  B01J21/08 ,  B01J23/745 ,  B01J23/78 ,  B01J37/03 ,  C10G2/332 ,  C10G2300/4006 ,  C10G2300/703

摘要： A method of activating an iron Fischer-Tropsch catalyst by introducing an inert gas into a reactor comprising a slurry of the catalyst at a first temperature, increasing the reactor temperature from the first temperature to a second temperature at a first ramp rate, wherein the second temperature is in the range of from about 150° C. to 250° C., introducing synthesis gas having a ratio of H2:CO to the reactor at a space velocity, and increasing the reactor temperature from the second temperature to a third temperature at a second ramp rate, wherein the third temperature is in the range of from about 270° C. to 300° C. The iron Fischer-Tropsch catalyst may be a precipitated unsupported iron catalyst, production of which is also provided.

摘要翻译： 一种通过将惰性气体引入反应器中来激活铁费 - 托催化剂的方法，所述反应器包括在第一温度下的催化剂浆料，以第一升高速率将反应器温度从第一温度升至第二温度，其中第二 温度在约150℃至250℃的范围内，以空间速度将具有H 2 :CO比例的合成气引入反应器，并将反应器温度从第二温度升至第三温度 第二斜坡率，其中第三温度在约270℃至300℃的范围内。费 - 托催化剂铁可以是沉淀的未负载的铁催化剂，也提供其生产。

公开(公告)号：US5504259A

公开(公告)日：1996-04-02

申请号：US968588

申请日：1992-10-29

申请人： James P. Diebold ,  John W. Scahill ,  Helena L. Chum ,  Robert J. Evans ,  Bahman Rejai ,  Richard L. Bain ,  Ralph P. Overend

发明人： James P. Diebold ,  John W. Scahill ,  Helena L. Chum ,  Robert J. Evans ,  Bahman Rejai ,  Richard L. Bain ,  Ralph P. Overend

IPC分类号： C07C29/04 ,  C07C41/06 ,  C10B49/12 ,  C10B53/00 ,  C10B53/02 ,  C10B53/07 ,  C10G1/00 ,  C07C41/05 ,  C07C1/00

CPC分类号： C10B49/12 ,  C10B53/00 ,  C10B53/02 ,  C10B53/07 ,  C10G1/002 ,  Y02E50/14 ,  Y02P20/143

摘要： A process for conversion of a feedstock selected from the group consisting of biomass and refuse derived fuel (RDF) to provide reformulated gasoline components comprising a substantial amount of materials selected from the group consisting of ethers, alcohols, or mixtures thereof, comprising: drying said feedstock; subjecting said dried feedstock to fast pyrolysis using a vortex reactor or other means; catalytically cracking vapors resulting from said pyrolysis using a zeolite catalyst; condensing any aromatic byproduct fraction; catalytically alkylating any benzene present in said vapors after condensation; catalytically oligomerizing any remaining ethylene and propylene to higher olefins; isomerizing said olefins to reactive iso-olefins; and catalytically reacting said iso-olefins with an alcohol to form ethers or with water to form alcohols.

摘要翻译： 用于转化选自生物质和垃圾衍生燃料（RDF）的原料的方法，以提供重组汽油组分，其包含大量选自醚，醇或其混合物的材料，其包括：将所述 原料; 使用涡流反应器或其他方式对所述干燥原料进行快速热解; 使用沸石催化剂从所述热解产生的催化裂化蒸气; 冷凝任何芳族副产物馏分; 在冷凝后催化烷基化存在于所述蒸气中的任何苯; 将任何剩余的乙烯和丙烯催化低聚成高级烯烃; 将所述烯烃异构化成反应性异烯烃; 并使所述异烯烃与醇反应以形成醚或与水反应形成醇。

公开(公告)号：US20210155995A1

公开(公告)日：2021-05-27

申请号：US17048512

申请日：2019-04-15

申请人： Robert Bartek ,  Bahman Rejai

发明人： Robert Bartek ,  Bahman Rejai

IPC分类号： C13K1/02 ,  C13K13/00 ,  B01J23/745 ,  C12P39/00 ,  C12P19/02

摘要： A method for treating biomass including lignocellulosic polymers. The biomass is treated in a mixture of water with at least one oxidizing agent and steam at a temperature in a range of from about 130° C. to about 220° C. for a period from about 5 seconds to about 10 hours. The pH of the mixture is periodically measured for substantially an entire duration of the treating step. As necessary, based on the measured pH of the mixture, adjusting the pH of the mixture into a range of from about pH 4.5 to about pH 7.5 by adding a base to the mixture.

公开(公告)号：US08530366B2

公开(公告)日：2013-09-10

申请号：US12984902

申请日：2011-01-05

申请人： Harold A. Wright ,  Belma Demirel ,  Sergio Mohedas ,  Bahman Rejai ,  Ray Huang ,  Deena Ferdous ,  Jesse W. Taylor ,  Dawid J. Duvenhage ,  Sara L. Rolfe

发明人： Harold A. Wright ,  Belma Demirel ,  Sergio Mohedas ,  Bahman Rejai ,  Ray Huang ,  Deena Ferdous ,  Jesse W. Taylor ,  Dawid J. Duvenhage ,  Sara L. Rolfe

IPC分类号： B01J20/34 ,  C07C27/00

CPC分类号： B01J8/006 ,  B01J8/18 ,  B01J8/1809 ,  B01J23/745 ,  B01J33/00 ,  B01J35/023 ,  B01J37/0045 ,  B01J37/18 ,  C10G2/32 ,  C10G2/33 ,  C10G2/332 ,  C10G2300/703

摘要： A method of preparing a spray dried catalyst by combining spray dried catalyst particles with wax so the spray dried catalyst particles are coated with wax, yielding wax coated catalyst particles, and shaping the wax coated catalyst to provide shaped wax coated catalyst. A method of activating Fischer-Tropsch catalyst particles containing oxides by contacting the catalyst particles with a reducing gas in an activation vessel to produce an activated catalyst, wherein contacting is performed in the absence of a liquid medium under activation conditions. A system for activating a Fischer-Tropsch catalyst containing an activation reactor configured to introduce an activation gas to a fixed or fluidized bed of the Fischer-Tropsch catalyst in the absence of a liquid medium and at least one separation device configured to separate a gas stream comprising entrained catalyst fines having an average particle size below a desired cutoff size from the activation reactor.

摘要翻译： 通过将喷雾干燥的催化剂颗粒与蜡组合来制备喷雾干燥的催化剂的方法，使喷雾干燥的催化剂颗粒用蜡涂覆，产生蜡涂覆的催化剂颗粒，并使蜡涂覆的催化剂成形以提供成形的涂蜡催化剂。 通过使催化剂颗粒与活化容器中的还原气体接触以产生活化的催化剂来活化含有氧化物的费 - 托催化剂颗粒的方法，其中在不存在液体介质的条件下进行接触。 一种用于活化费 - 托催化剂的系统，其包含活化反应器，所述活化反应器配置成在没有液体介质的情况下将活化气体引入费 - 托催化剂的固定或流化床，以及至少一个分离装置，其被配置为分离气流 包括夹带的催化剂细粒，其具有低于来自活化反应器的所需截留尺寸的平均粒度。

公开(公告)号：US20090111684A1

公开(公告)日：2009-04-30

申请号：US12272960

申请日：2008-11-18

申请人： Belma Demirel ,  Charles B. Benham ,  Dan Fraenkel ,  Richard Bley ,  Jesse W. Taylor ,  Bahman Rejai ,  Sara Rolfe ,  Harold A. Wright

发明人： Belma Demirel ,  Charles B. Benham ,  Dan Fraenkel ,  Richard Bley ,  Jesse W. Taylor ,  Bahman Rejai ,  Sara Rolfe ,  Harold A. Wright

IPC分类号： B01J23/72 ,  B01J21/06 ,  B01J27/20 ,  B01J31/28 ,  B01J23/02

CPC分类号： B01J37/18 ,  B01J21/08 ,  B01J23/745 ,  B01J23/78 ,  B01J37/03 ,  C10G2/332 ,  C10G2300/4006 ,  C10G2300/703

摘要： A method of activating an iron Fischer-Tropsch catalyst by introducing an inert gas into a reactor comprising a slurry of the catalyst at a first temperature, increasing the reactor temperature from the first temperature to a second temperature at a first ramp rate, wherein the second temperature is in the range of from about 150° C. to 250° C., introducing synthesis gas having a ratio of H2:CO to the reactor at a space velocity, and increasing the reactor temperature from the second temperature to a third temperature at a second ramp rate, wherein the third temperature is in the range of from about 270° C. to 300° C. The iron Fischer-Tropsch catalyst may be a precipitated unsupported iron catalyst, production of which is also provided.

摘要翻译： 一种通过将惰性气体引入反应器中来激活铁费 - 托催化剂的方法，所述反应器包括在第一温度下的催化剂浆料，以第一升高速率将反应器温度从第一温度升至第二温度，其中第二 温度在约150℃至250℃的范围内，以空间速度将具有H 2 :CO比例的合成气引入反应器，并将反应器温度从第二温度升至第三温度 第二斜坡率，其中第三温度在约270℃至300℃的范围内。费 - 托催化剂铁可以是沉淀的未负载的铁催化剂，也提供其生产。