公开(公告)号：US08562933B2

公开(公告)日：2013-10-22

申请号：US12749221

申请日：2010-03-29

申请人： Herbert E. Andrus, Jr. ,  John. H. Chiu ,  Gregory N. Liljedahl ,  Paul R. Thibeault ,  Carl R. Bozzuto ,  Corinne Beal ,  Michal T. Bialkowski ,  Andreas Brautsch ,  Laurent Maghdissian ,  Michel Vandycke

发明人： Herbert E. Andrus, Jr. ,  John. H. Chiu ,  Gregory N. Liljedahl ,  Paul R. Thibeault ,  Carl R. Bozzuto ,  Corinne Beal ,  Michal T. Bialkowski ,  Andreas Brautsch ,  Laurent Maghdissian ,  Michel Vandycke

IPC分类号： C01B3/02 ,  C01B5/00 ,  C10B3/02 ,  C01F11/46

CPC分类号： C10J3/00 ,  C10J3/725 ,  C10J2300/093 ,  C10J2300/0976 ,  C10J2300/0996 ,  C10J2300/1807 ,  F23C2900/99008 ,  Y02E20/346

摘要： A hot solids process selectively operable for purposes of generating at least one predetermined output based on what the specific nature of the primary purpose of the hot solids process is for which the at least one predetermined output that is selected from a multiplicity of predetermined outputs, such as H2 and CO2, is being produced, and wherein such primary purpose of the hot solids process is designed to be pre-selected from a group of primary purposes of the hot solids process that includes at least two of the generation of H2 for electric power purposes, the generation of SynGas for electric power production as well as for other industrial uses, the production of steam for electric power generation as well as for other uses, the production of process heat, the production of CO2 for agricultural purposes, and the generation of a feedstock such as H2 for use for the production of liquid hydrocarbons.

摘要翻译： 热固体过程选择性地可操作用于基于热固体过程的主要目的的特定性质产生至少一个预定输出，对于该固体过程，选择多个预定输出的至少一个预定输出，例如 作为H 2和CO 2，并且其中热固体过程的这种主要目的被设计为从热固体过程的一组主要目的中预先选择的，所述热固体过程包括产生用于电力的H2中的至少两个 目的，生产用于电力生产和其他工业用途的SynGas，生产用于发电和其他用途的蒸汽，生产过程热量，用于农业生产的二氧化碳，以及生成 的诸如H 2的原料用于生产液体烃。

公开(公告)号：US5372618A

公开(公告)日：1994-12-13

申请号：US998341

申请日：1992-12-30

申请人： Herbert E. Andrus, Jr.

发明人： Herbert E. Andrus, Jr.

IPC分类号： C10J3/72

CPC分类号： C10J3/72 ,  C10K1/026 ,  C10J2300/0906 ,  C10J2300/093 ,  C10J2300/0956 ,  C10J2300/1807 ,  Y02E20/18 ,  Y10S48/02

摘要： A temperature measuring device for a gasifier of a gasifier system wherein the gasifier has a through opening formed thereon. The temperature measuring device includes a slag shield mounted on the gasifier so that a portion of the slag shield extends into the interior of the gasifier through the opening with which the gasifier is provided for this purpose, and a temperature measuring instrument mounted in supported relation within the slag shield so that a line-of-sight exists from the temperature measuring instrument into the interior of the gasifier whereat the temperature is desired to be measured. The slag shield is designed to protect the temperature measuring instrument from the slag flow within the gasifier. The temperature measuring instrument further includes cooling means for cooling at least that portion of the slag shield that extends into the interior of the gasifier, and purge gas means for supplying a flow of purge gas in surrounding relation to the temperature measuring instrument to purge particulate matter therefrom in order to ensure that the line-of-sight between the temperature measuring instrument and the interior of the gasifier remains unobscured.

摘要翻译： 一种用于气化器系统的气化器的温度测量装置，其中气化器具有形成在其上的通孔。 温度测量装置包括安装在气化器上的炉渣屏蔽物，使得一部分炉渣屏蔽件通过与此气化器一起设置的开口延伸到气化器内部;以及温度测量仪器， 炉渣屏蔽，使得从温度测量仪器到视觉温度希望测量的气化器内部存在视线。 渣屏设计用于保护温度测量仪器免受气化炉内的渣流。 温度测量仪器还包括冷却装置，用于至少冷却延伸到气化器内部的炉渣屏蔽部分的部分，以及吹扫气体装置，用于提供与温度测量仪器相关的净化气体流以清除颗粒物质 从而确保温度测量仪器与气化器内部之间的视线保持视野不变。

公开(公告)号：US07988752B2

公开(公告)日：2011-08-02

申请号：US12239232

申请日：2008-09-26

申请人： Herbert E. Andrus, Jr. ,  Michael S. McCartney

发明人： Herbert E. Andrus, Jr. ,  Michael S. McCartney

IPC分类号： C10J3/46

CPC分类号： F23J15/04 ,  B01D53/96 ,  B01D2258/0283 ,  C01B3/105 ,  C01B3/56 ,  C01B2203/0283 ,  C01B2203/042 ,  C01B2203/0475 ,  C01B2203/86 ,  C10J3/54 ,  C10J3/56 ,  C10J2300/093 ,  C10J2300/0956 ,  C10J2300/0973 ,  C10J2300/0983 ,  C10J2300/1618 ,  C10J2300/1637 ,  C10J2300/1861 ,  C10J2300/1869 ,  C10J2300/1884 ,  F23J2215/50 ,  F23J2219/60 ,  Y02E20/16 ,  Y02E20/18 ,  Y02E20/185 ,  Y02E60/36 ,  Y02P20/152 ,  Y02P30/30

摘要： A gasifier 10 includes a first chemical process loop 12 having an exothermic oxidizer reactor 14 and an endothermic reducer reactor 16. CaS is oxidized in air in the oxidizer reactor 14 to form hot CaSO4 which is discharged to the reducer reactor 16. Hot CaSO4 and carbonaceous fuel received in the reducer reactor 16 undergo an endothermic reaction utilizing the heat content of the CaSO4, the carbonaceous fuel stripping the oxygen from the CaSO4 to form CaS and a CO rich syngas. The CaS is discharged to the oxidizer reactor 14 and the syngas is discharged to a second chemical process loop 52. The second chemical process loop 52 has a water-gas shift reactor 54 and a calciner 42. The CO of the syngas reacts with gaseous H2O in the shift reactor 54 to produce H2 and CO2. The CO2 is captured by CaO to form hot CaCO3 in an exothermic reaction. The hot CaCO3 is discharged to the calciner 42, the heat content of the CaCO3 being used to strip the CO2 from the CaO in an endothermic reaction in the calciner, with the CaO being discharged from the calciner 42 to the shift reactor 54.

摘要翻译： 气化器10包括具有放热氧化剂反应器14和吸热还原反应器16的第一化学处理回路12.在氧化反应器14中，CaS在空气中被氧化以形成热的CaSO 4，其被排放到还原反应器16中。热的CaSO 4和碳质 在还原反应器16中接收的燃料利用CaSO 4的热含量进行吸热反应，碳质燃料从CaSO 4中除去氧气以形成CaS和富含CO的合成气。 CaS被排放到氧化反应器14中，合成气排出到第二化学处理回路52.第二化学处理回路52具有水煤气变换反应器54和煅烧炉42.合成气的CO与气态H 2 在换档反应器54中产生H 2和CO 2。 CO 2被CaO捕获以在放热反应中形成热的CaCO 3。 将热的CaCO 3排放到煅烧炉42中，CaCO 3的热含量用于在煅烧炉中的吸热反应中从CaO中分离CO 2，CaO从煅烧炉42排出到变换反应器54。

公开(公告)号：US20100281769A1

公开(公告)日：2010-11-11

申请号：US12749199

申请日：2010-03-29

申请人： Herbert E. ANDRUS, JR. ,  John H. CHIU ,  Gregory N. LILJEDAHL ,  Paul R. THIBEAULT ,  Carl R. BOZZUTO ,  Corinne BEAL ,  Michal T. BIALKOWSKI ,  Andreas BRAUTSCH ,  Laurent MAGHDISSIAN ,  Michel VANDYCKE

发明人： Herbert E. ANDRUS, JR. ,  John H. CHIU ,  Gregory N. LILJEDAHL ,  Paul R. THIBEAULT ,  Carl R. BOZZUTO ,  Corinne BEAL ,  Michal T. BIALKOWSKI ,  Andreas BRAUTSCH ,  Laurent MAGHDISSIAN ,  Michel VANDYCKE

IPC分类号： C10L5/00

CPC分类号： C10L9/08 ,  C10J3/00 ,  C10J3/12 ,  C10J3/46 ,  C10J3/54 ,  C10J3/725 ,  C10J2300/0993 ,  C10J2300/0996 ,  C10J2300/1807 ,  C10L9/10 ,  F23C2900/99008 ,  Y02E20/346

摘要： A hot solids process selectively operable for purposes of generating a predetermined output based on the nature of the specific application for which the predetermined output is being produced, and wherein such specific application is designed to be pre-selected from a group of specific applications that includes a new steam generator application, a retrofit steam generator application, a CO2 capture ready Hot Solids Combustion application, a CO2 capture ready hot solids gasification application, a CO2 capture hot solids combustion application, a CO2 capture hot solids gasification application, a partial CO2 capture hot solids combustion application, and a partial CO2 capture hot solids gasification application.

摘要翻译： 热固体过程选择性地可操作地用于基于正在产生预定输出的特定应用的性质来生成预定输出，并且其中这种特定应用被设计为从包括以下的特定应用的组中预先选择： 新的蒸汽发生器应用，改进的蒸汽发生器应用，二氧化碳捕集就绪热固体燃烧应用，二氧化碳捕集就绪热固体气化应用，二氧化碳捕获热固体燃烧应用，二氧化碳捕获热固体气化应用，部分二氧化碳捕获 热固体燃烧应用和部分二氧化碳捕获热固体气化应用。

公开(公告)号：US20100288678A1

公开(公告)日：2010-11-18

申请号：US12749238

申请日：2010-03-29

申请人： Herbert E. ANDRUS, JR. ,  John H. CHIU ,  Gregory N. LILJEDAHL ,  Paul R. THIBEAULT ,  Carl R. BOZZUTO ,  Corinne BEAL ,  Michal T. BIALKOWSKI ,  Andreas BRAUTSCH ,  Laurent MAGHDISSIAN ,  Michel VANDYCKE

发明人： Herbert E. ANDRUS, JR. ,  John H. CHIU ,  Gregory N. LILJEDAHL ,  Paul R. THIBEAULT ,  Carl R. BOZZUTO ,  Corinne BEAL ,  Michal T. BIALKOWSKI ,  Andreas BRAUTSCH ,  Laurent MAGHDISSIAN ,  Michel VANDYCKE

IPC分类号： C10G1/00

CPC分类号： C10G1/00 ,  C10G29/02 ,  C10G2300/202 ,  C10G2300/807 ,  C10J3/00 ,  C10J3/12 ,  C10J3/725 ,  C10J2300/0993 ,  C10J2300/0996 ,  C10J2300/1807

摘要： A hot solids process wherein a predetermined output, which is designed to be suitable for use as an input to a petrochemical process, is capable of being generated through the use of the hot solids process. The mode of operation of such a hot solids process is designed to be such that preferably a portion of the otherwise normally unusable product output, which is produced from a petrochemical process, is designed to be utilized as an input to the hot solids process for purposes of generating from the hot solids process the predetermined output that is suitable for use as an input to a petrochemical process.

摘要翻译： 热固体过程，其中设计为适合用作石油化学工艺的输入的预定输出能够通过使用热固体过程产生。 这种热固体过程的操作模式被设计成使得优选地，由石油化学工艺生产的一部分通常不可用的产品输出被设计为用作热固体过程的输入，以用于目的 从热固体处理产生适合用作石油化学工艺的输入的预定输出。

公开(公告)号：US20090211503A1

公开(公告)日：2009-08-27

申请号：US12392355

申请日：2009-02-25

申请人： Herbert E. Andrus, JR. ,  Gregory N. Liljedahl ,  John L. Marion ,  Nsakala Ya Nsakala

发明人： Herbert E. Andrus, JR. ,  Gregory N. Liljedahl ,  John L. Marion ,  Nsakala Ya Nsakala

IPC分类号： F23J15/00 ,  F23C10/00 ,  F22B31/00 ,  F23J15/06 ,  F23J99/00 ,  F23L7/00 ,  F22B31/08 ,  F23C7/06

CPC分类号： F23C10/10 ,  F22B31/0007 ,  F23C9/00 ,  F23J15/006 ,  F23J15/06 ,  F23J2215/50 ,  F23L7/007 ,  F23L15/04 ,  F23L2900/07001 ,  F23L2900/07003 ,  F23L2900/15042 ,  Y02E20/322 ,  Y02E20/326 ,  Y02E20/344 ,  Y02E20/348

摘要： A combustor 110 is operative to effect therewith the combustion of fossil fuel 114′ in order to thereby both heat to a working fluid 102 and generate a flue gas 104. An air preheater 144 receives the flue gas 104 generated in the combustor 110. A blower 180 causes air 188 to flow to the air preheater 144 when operating in an air fired mode, and causes both O2 and recycled flue gas 188′ to flow when operating in the O2 firing mode. The air preheater 144 is operative to transfer heat from the flue gas 150 received thereby to the air 188 that is received when operating in an air fired mode or to both the received O2 and the recycled flue gas 188′ that is received when operating in the O2 firing mode in order to thereby effect a preheating of the air 188 or of both the O2 and recycled flue gas, 188′ depending upon the specific nature of the mode of operation thereof, and to thereby effect therewith a cooling of the flue gas received thereby. The preheated air 142 or both the preheated O2 and the recycled flue gas 142′, depending upon the specific nature of the mode of operation, is caused to flow from the air preheater 144 to the combustor 110 in order to thereby effect therewith a fluidization of the fossil fuel 114′.

摘要翻译： 燃烧器110可操作以通过化石燃料114'的燃烧来实现燃烧，从而由此二者加热到工作流体102并产生烟道气体104.空气预热器144接收在燃烧器110中产生的烟道气104.鼓风机 当在空气燃烧模式下操作时，180使空气188流到空气预热器144，并且当在O 2点火模式下操作时，O 2和再循环烟道气188'都流动。 空气预热器144可操作以将热量从其接收的烟道气150转移到在空气燃烧模式下运行时接收的空气188，或者在接收的O2和被回收的废气188' O2烧制模式，从而根据其操作模式的具体特性来实现空气188或者二氧化碳和再循环烟道气188'的预热，从而使所接收到的烟气冷却 从而。 使预热的空气142或预热的氧气和再循环烟道气142'两者都取决于操作模式的具体特性，从空气预热器144流到燃烧器110，从而使其流化 化石燃料114'。

公开(公告)号：US20090211500A1

公开(公告)日：2009-08-27

申请号：US12392436

申请日：2009-02-25

申请人： Herbert E. Andrus, JR. ,  Gregory N. Liljedahl ,  John L. Marion ,  Nsakala Ya Nsakala

发明人： Herbert E. Andrus, JR. ,  Gregory N. Liljedahl ,  John L. Marion ,  Nsakala Ya Nsakala

IPC分类号： F23J3/00

CPC分类号： F23C10/10 ,  F22B31/0007 ,  F23C9/00 ,  F23J15/006 ,  F23J15/06 ,  F23J2215/50 ,  F23L7/007 ,  F23L15/04 ,  F23L2900/07001 ,  F23L2900/07003 ,  F23L2900/15042 ,  Y02E20/322 ,  Y02E20/326 ,  Y02E20/344 ,  Y02E20/348

摘要： A combustor 110 combust a fluidized bed of fossil fuel 114, 114′ to heat a working fluid 102 and generate flue gas 104. An air preheater 144 has first and second gas passageways 144a, 144b for respectively directing the generated flue gas 150 and another gas 250 with captured CO2 generated by combustion outside of the combustor 110. When operated in a non-CO2 capture, the air preheater 144 receives the flue gas 150, but not the other gas 250, and the first gas passageway 144a directs the flue gas 150 so as to preheat the air 188. However, when operated in the CO2 capture mode, the air preheater 144 receives the flue gas 150 and the other gas 250, and the second gas passageway 144b also directs the other gas 250 so as to preheat the air 188′. In either mode, the preheated air 188, 188′ is applied by the combustor 110 to fluidize a bed of fossil fuel 114, 114′.

摘要翻译： 燃烧器110燃烧化石燃料114,114'的流化床以加热工作流体102并产生烟气104.空气预热器144具有用于分别引导产生的烟道气150和另一种气体的第一和第二气体通道144a，144b 250，其具有由燃烧器110外部的燃烧产生的捕获的CO 2。当在非CO2捕获中操作时，空气预热器144接收烟道气150而不是另一气体250，并且第一气体通道144a引导烟道气150 以便预热空气188.然而，当以二氧化碳捕获模式操作时，空气预热器144接收烟道气150和另一气体250，并且第二气体通道144b也引导另一气体250以便预热 空气188'。 在任一模式中，预热空气188,188'由燃烧器110施加以使化石燃料114,114'的床流化。

公开(公告)号：US07445649B2

公开(公告)日：2008-11-04

申请号：US11422703

申请日：2006-06-07

申请人： Herbert E. Andrus, Jr. ,  Michael S. McCartney

发明人： Herbert E. Andrus, Jr. ,  Michael S. McCartney

IPC分类号： C10J3/46 ,  C10B1/00

CPC分类号： F23J15/04 ,  B01D53/96 ,  B01D2258/0283 ,  C01B3/105 ,  C01B3/56 ,  C01B2203/0283 ,  C01B2203/042 ,  C01B2203/0475 ,  C01B2203/86 ,  C10J3/54 ,  C10J3/56 ,  C10J2300/093 ,  C10J2300/0956 ,  C10J2300/0973 ,  C10J2300/0983 ,  C10J2300/1618 ,  C10J2300/1637 ,  C10J2300/1861 ,  C10J2300/1869 ,  C10J2300/1884 ,  F23J2215/50 ,  F23J2219/60 ,  Y02E20/16 ,  Y02E20/18 ,  Y02E20/185 ,  Y02E60/36 ,  Y02P20/152 ,  Y02P30/30

摘要： A gasifier 10 includes a first chemical process loop 12 having an exothermic oxidizer reactor 14 and an endothermic reducer reactor 16. CaS is oxidized in air in the oxidizer reactor 14 to form hot CaSO4 which is discharged to the reducer reactor 16. Hot CaSO4 and carbonaceous fuel received in the reducer reactor 16 undergo an endothermic reaction utilizing the heat content of the CaSO4, the carbonaceous fuel stripping the oxygen from the CaSO4 to form CaS and a CO rich syngas. The CaS is discharged to the oxidizer reactor 14 and the syngas is discharged to a second chemical process loop 52. The second chemical process loop 52 has a water-gas shift reactor 54 and a calciner 42. The CO of the syngas reacts with gaseous H2O in the shift reactor 54 to produce H2 and CO2. The CO2 is captured by CaO to form hot CaCO3 in an exothermic reaction. The hot CaCO3 is discharged to the calciner 42, the heat content of the CaCO3 being used to strip the CO2 from the CaO in an endothermic reaction in the calciner, with the CaO being discharged from the calciner 42 to the shift reactor 54.

摘要翻译： 气化器10包括具有放热氧化反应器14和吸热还原反应器16的第一化学处理回路12。 CaS在氧化反应器14中在空气中被氧化，形成被排出到还原反应器16的热CaSO 4。 热还原反应器16中接收的热CaSO 4和碳质燃料利用CaSO 4的热含量进行吸热反应，碳质燃料从CaSO _{4 以形成CaS和富含CO的合成气。 CaS被排放到氧化反应器14中，合成气被排放到第二化学处理回路52。 第二化学处理回路52具有水煤气变换反应器54和煅烧炉42。 合成气的CO与变换反应器54中的气态H 2 O 2反应以产生H 2和CO 2。 在放热反应中CO 2捕获CO 2以形成热的CaCO 3。 将热的CaCO 3 3排放到煅烧炉42中，用于从CaO中除去CO 2 3的CO 2的热含量 煅烧炉中的吸热反应，CaO从煅烧炉42排出到变换反应器54。}

公开(公告)号：US5622534A

公开(公告)日：1997-04-22

申请号：US336604

申请日：1994-11-09

申请人： Herbert E. Andrus, Jr.

发明人： Herbert E. Andrus, Jr.

IPC分类号： C10J3/46 ,  C10J3/48 ,  C10J3/72 ,  C10J3/78 ,  C10J3/76

CPC分类号： C10J3/485 ,  C10J3/482 ,  C10J3/76 ,  C10J3/78 ,  C10K1/026 ,  C10J2300/093 ,  C10J2300/1687 ,  C10J2300/1807 ,  C10J2300/1884 ,  Y02E20/18

摘要： A high performance, multi-stage, pressurized, airblown, entrained flow coal gasifier system and a method of operating such a gasifier system for generating therewithin fuel gas from coal. The subject gasifier system includes an outer, pressure containing vessel surrounding an inner, water-cooled vessel wherein the gasification reaction, through which the fuel gas is generated from coal, takes place. The inner, water-cooled vessel embodies a first stage within which the high temperatures required for the gasification reactions to take place as well as for slagging are generated from the combustion of char, a second stage within which the char is gasified to generate the subject fuel gas, and a third stage within which coal is devolatilized to produce the char for the first stage and the second stage and with a concomitant quenching being effected of the fuel gas as the latter flows through the third stage of the inner water-cooled vessel.

公开(公告)号：US5620487A

公开(公告)日：1997-04-15

申请号：US336440

申请日：1994-11-09

申请人： Herbert E. Andrus, Jr.

发明人： Herbert E. Andrus, Jr.

IPC分类号： C10J3/46 ,  C10J3/48 ,  C10J3/72 ,  C10J3/78 ,  C10J3/76

CPC分类号： C10J3/485 ,  C10J3/482 ,  C10J3/76 ,  C10J3/78 ,  C10K1/026 ,  C10J2300/093 ,  C10J2300/1687 ,  C10J2300/1807 ,  C10J2300/1884 ,  Y02E20/18

摘要： A high performance, multi-stage, pressurized, airblown, entrained flow coal gasifier system and a method of operating such a gasifier system for generating therewithin fuel gas from coal. The subject gasifier system includes an outer, pressure containing vessel surrounding an inner, water-cooled vessel wherein the gasification reaction, through which the fuel gas is generated from coal, takes place. The inner, water-cooled vessel embodies a first stage within which the high temperatures required for the gasification reactions to take place as well as for slagging are generated from the combustion of char, a second stage within which the char is gasified to generate the subject fuel gas, and a third stage within which coal is devolatilized to produce the char for the first stage and the second stage and with a concomitant quenching being effected of the fuel gas as the latter flows through the third stage of the inner water-cooled vessel.

摘要翻译： 一种高性能，多级，加压，气吹，夹带气流煤气化炉系统和操作这种气化器系统的方法，用于在煤中产生燃料气体。 本发明的气化器系统包括围绕内部水冷容器的外部包含压力的容器，其中进行从煤产生燃料气体的气化反应。 内部水冷容器体现了第一阶段，其中气化反应发生所需的高温以及结渣是由炭的燃烧产生的，其中炭被气化以产生物体 燃料气体和第三阶段，其中煤被脱挥发分以产生用于第一阶段和第二阶段的焦炭，并且随着燃料气体流过内部水冷却容器的第三阶段而伴随着淬火 。