公开(公告)号：US20170152140A1

公开(公告)日：2017-06-01

申请号：US15430654

申请日：2017-02-13

Applicant: ThermoChem Recovery International, Inc.

Inventor： RAVI CHANDRAN ,  Daniel Michael Leo ,  Shawn Robert Freitas ,  Dave G. Newport ,  Hamilton Sean Michael Whitney ,  Daniel A. Burciaga

IPC: C01B3/58 ,  C01B3/56 ,  C01B3/38 ,  B01D53/26 ,  B01D53/14 ,  B01D5/00 ,  B01D17/02 ,  B01D29/27 ,  B01D29/66 ,  B01D47/10 ,  B01D53/18 ,  B01D53/04 ,  B01D46/00 ,  B01D53/32 ,  B01D53/047 ,  B01D50/00 ,  B01D61/36 ,  B01D53/48 ,  B01D53/76 ,  B01D53/12 ,  C01B3/52

CPC classification number: C01B3/52 ,  B01D5/0027 ,  B01D5/006 ,  B01D5/0072 ,  B01D5/0075 ,  B01D5/009 ,  B01D17/0208 ,  B01D29/27 ,  B01D29/66 ,  B01D46/0036 ,  B01D47/10 ,  B01D50/006 ,  B01D53/0423 ,  B01D53/0462 ,  B01D53/047 ,  B01D53/0476 ,  B01D53/12 ,  B01D53/1406 ,  B01D53/1412 ,  B01D53/1431 ,  B01D53/1462 ,  B01D53/1468 ,  B01D53/1487 ,  B01D53/18 ,  B01D53/265 ,  B01D53/326 ,  B01D53/48 ,  B01D53/76 ,  B01D61/362 ,  B01D2252/102 ,  B01D2252/103 ,  B01D2252/20436 ,  B01D2252/504 ,  B01D2252/602 ,  B01D2256/16 ,  B01D2256/20 ,  B01D2257/304 ,  B01D2257/306 ,  B01D2257/406 ,  B01D2257/504 ,  B01D2257/60 ,  B01D2257/708 ,  B01D2259/402 ,  C01B3/24 ,  C01B3/38 ,  C01B3/382 ,  C01B3/386 ,  C01B3/56 ,  C01B3/58 ,  C01B2203/0227 ,  C01B2203/0233 ,  C01B2203/025 ,  C01B2203/0261 ,  C01B2203/04 ,  C01B2203/0415 ,  C01B2203/042 ,  C01B2203/043 ,  C01B2203/0435 ,  C01B2203/045 ,  C01B2203/0465 ,  C01B2203/0475 ,  C01B2203/048 ,  C01B2203/0485 ,  C01B2203/061 ,  C01B2203/062 ,  C01B2203/068 ,  C01B2203/0877 ,  C01B2203/1235 ,  C01B2203/1241 ,  C01B2203/142 ,  C01B2203/147 ,  C01B2203/84 ,  H05K999/99 ,  Y02P20/13 ,  Y02P30/30

Abstract: A system and method for processing unconditioned syngas first removes solids and semi-volatile organic compounds (SVOC), then removes volatile organic compounds (VOC), and then removes at least one sulfur containing compound from the syngas. Additional processing may be performed depending on such factors as the source of syngas being processed, the products, byproducts and intermediate products desired to be formed, captured or recycled and environmental considerations.

公开(公告)号：US20170152139A1

公开(公告)日：2017-06-01

申请号：US15430633

申请日：2017-02-13

Applicant: ThermoChem Recovery International, Inc.

Inventor： Ravi Chandran ,  Daniel Michael Leo ,  Shawn Robert Freitas ,  Dave G. Newport ,  Hamilton Sean Michael Whitney ,  Daniel A. Burciaga

IPC: C01B3/58 ,  C01B3/56 ,  C01B3/38 ,  B01D5/00 ,  B01D17/02 ,  B01D29/27 ,  B01D29/66 ,  B01D47/10 ,  B01D53/14 ,  B01D53/18 ,  B01D53/04 ,  B01D46/00 ,  B01D53/32 ,  B01D53/047 ,  B01D50/00 ,  B01D61/36 ,  B01D53/48 ,  B01D53/76 ,  B01D53/12 ,  B01D53/26 ,  C01B3/52

CPC classification number: C01B3/52 ,  B01D5/0027 ,  B01D5/006 ,  B01D5/0072 ,  B01D5/0075 ,  B01D5/009 ,  B01D17/0208 ,  B01D29/27 ,  B01D29/66 ,  B01D46/0036 ,  B01D47/10 ,  B01D50/006 ,  B01D53/0423 ,  B01D53/0462 ,  B01D53/047 ,  B01D53/0476 ,  B01D53/12 ,  B01D53/1406 ,  B01D53/1412 ,  B01D53/1431 ,  B01D53/1462 ,  B01D53/1468 ,  B01D53/1487 ,  B01D53/18 ,  B01D53/265 ,  B01D53/326 ,  B01D53/48 ,  B01D53/76 ,  B01D61/362 ,  B01D2252/102 ,  B01D2252/103 ,  B01D2252/20436 ,  B01D2252/504 ,  B01D2252/602 ,  B01D2256/16 ,  B01D2256/20 ,  B01D2257/304 ,  B01D2257/306 ,  B01D2257/406 ,  B01D2257/504 ,  B01D2257/60 ,  B01D2257/708 ,  B01D2259/402 ,  C01B3/24 ,  C01B3/38 ,  C01B3/382 ,  C01B3/386 ,  C01B3/56 ,  C01B3/58 ,  C01B2203/0227 ,  C01B2203/0233 ,  C01B2203/025 ,  C01B2203/0261 ,  C01B2203/04 ,  C01B2203/0415 ,  C01B2203/042 ,  C01B2203/043 ,  C01B2203/0435 ,  C01B2203/045 ,  C01B2203/0465 ,  C01B2203/0475 ,  C01B2203/048 ,  C01B2203/0485 ,  C01B2203/061 ,  C01B2203/062 ,  C01B2203/068 ,  C01B2203/0877 ,  C01B2203/1235 ,  C01B2203/1241 ,  C01B2203/142 ,  C01B2203/147 ,  C01B2203/84 ,  H05K999/99 ,  Y02P20/13 ,  Y02P30/30

Abstract: A system and method for processing unconditioned syngas first removes solids and semi-volatile organic compounds (SVOC), then removes volatile organic compounds (VOC), and then removes at least one sulfur containing compound from the syngas. Additional processing may be performed depending on such factors as the source of syngas being processed, the products, byproducts and intermediate products desired to be formed, captured or recycled and environmental considerations.

公开(公告)号：US20170058221A1

公开(公告)日：2017-03-02

申请号：US15347138

申请日：2016-11-09

Applicant: Thermochem Recovery International, Inc.

Inventor： Ravi CHANDRAN ,  Jonathan A. ZENE ,  Dave G. NEWPORT ,  Hamilton Sean Michael WHITNEY

IPC: C10J3/72 ,  C10J3/48 ,  C01B3/02 ,  C10J3/46

CPC classification number: C10J3/721 ,  B01J8/004 ,  B01J8/0055 ,  B01J8/26 ,  B01J8/388 ,  B01J2208/00132 ,  B01J2208/00398 ,  B01J2208/00415 ,  B01J2208/00752 ,  B01J2208/00761 ,  C01B3/02 ,  C10J3/466 ,  C10J3/48 ,  C10J3/482 ,  C10J3/485 ,  C10J3/723 ,  C10J2200/09 ,  C10J2300/0916 ,  C10J2300/093 ,  C10J2300/094 ,  C10J2300/0946 ,  C10J2300/0959 ,  C10J2300/0976 ,  C10J2300/0983 ,  C10J2300/0986 ,  C10J2300/1246 ,  C10J2300/1261 ,  C10J2300/1625 ,  C10J2300/1637 ,  C10J2300/1687 ,  C10J2300/1807 ,  C10J2300/1838 ,  C10J2300/1846 ,  C10J2300/1853 ,  C10J2300/1892 ,  C10K1/026 ,  Y02P20/13

Abstract: A solids circulation system receives a gas stream containing char or other reacting solids from a first reactor. The solids circulation system includes a cyclone configured to receive the gas stream from the first reactor, a dipleg from the cyclone to a second reactor, and a riser from the second reactor which merges with the gas stream received by the cyclone. The second reactor has a dense fluid bed and converts the received materials to gaseous products. A conveying fluid transports a portion of the bed media from the second reactor through the riser to mix with the gas stream prior to cyclone entry. The bed media helps manipulate the solids that is received by the cyclone to facilitate flow of solids down the dipleg into the second reactor. The second reactor provides additional residence time, mixing and gas-solid contact for efficient conversion of char or reacting solids.

Abstract translation: 固体循环系统从第一反应器接收含有焦炭或其它反应固体的气流。 固体循环系统包括被配置为接收来自第一反应器的气流的旋风分离器，从旋风分离器到第二反应器的液体流，以及来自第二反应器的提升管与由旋风分离器接收的气流合并。 第二反应器具有致密的流化床并将接收的材料转化为气态产物。 输送流体将来自第二反应器的床介质的一部分通过提升管输送，以在旋风分离器进入之前与气流混合。 床介质有助于操纵由旋风分离器接收的固体，以促进固体向下流入第二反应器。 第二反应器提供额外的停留时间，混合和气固接触以有效地转化炭或反应固体。

公开(公告)号：US20250011668A1

公开(公告)日：2025-01-09

申请号：US18817482

申请日：2024-08-28

Applicant: ThermoChem Recovery International, Inc.

Inventor： Ravi Chandran ,  Daniel A. Burciaga ,  Daniel Michael Leo ,  Shawn Robert Freitas ,  Dave G. Newport ,  Justin Kevin Miller ,  Kaitlin Emily Harrington ,  Brian Christopher Attwood

IPC: C10J3/12 ,  C01B3/02 ,  C10G1/04 ,  C10G2/00 ,  C10G5/06 ,  C10J3/10 ,  C10J3/24 ,  C10J3/32 ,  C10J3/72 ,  C10J3/84 ,  C10L1/04 ,  C10L5/46 ,  F02B43/08

Abstract: A feedstock delivery system transfers a carbonaceous material, such as municipal solid waste, into a product gas generation system. The feedstock delivery system includes a splitter for splitting bulk carbonaceous material into a plurality of carbonaceous material streams. Each stream is processed using a weighing system for gauging the quantity of carbonaceous material, a densification system for forming plugs of carbonaceous material, a de-densification system for breaking up the plugs of carbonaceous material, and a gas and carbonaceous material mixing system for forming a carbonaceous material and gas mixture. A pressure of the mixing gas is reduced prior to mixing with the carbonaceous material, and the carbonaceous material to gas weight ratio is monitored. A transport assembly conveys the carbonaceous material and gas mixture to a first reactor where at least the carbonaceous material within the mixture is subject to thermochemical reactions to form the product gas.

公开(公告)号：US12077435B2

公开(公告)日：2024-09-03

申请号：US18233028

申请日：2023-08-11

Applicant: ThermoChem Recovery International, Inc.

Inventor： Ravi Chandran ,  Daniel Michael Leo ,  Shawn Robert Freitas ,  Dave G. Newport ,  Hamilton Sean Michael Whitney ,  Daniel A. Burciaga

IPC: C01B3/52 ,  B01D5/00 ,  B01D17/02 ,  B01D29/27 ,  B01D29/66 ,  B01D46/00 ,  B01D47/10 ,  B01D50/60 ,  B01D53/04 ,  B01D53/047 ,  B01D53/12 ,  B01D53/14 ,  B01D53/18 ,  B01D53/26 ,  B01D53/32 ,  B01D53/48 ,  B01D53/76 ,  B01D61/36 ,  C01B3/24 ,  C01B3/38 ,  C01B3/56 ,  C01B3/58

CPC classification number: C01B3/52 ,  B01D5/0027 ,  B01D5/006 ,  B01D5/0072 ,  B01D5/0075 ,  B01D5/009 ,  B01D17/0208 ,  B01D29/27 ,  B01D29/66 ,  B01D46/0036 ,  B01D47/10 ,  B01D50/60 ,  B01D53/0423 ,  B01D53/0462 ,  B01D53/047 ,  B01D53/0476 ,  B01D53/12 ,  B01D53/1406 ,  B01D53/1412 ,  B01D53/1431 ,  B01D53/1462 ,  B01D53/1468 ,  B01D53/1487 ,  B01D53/18 ,  B01D53/265 ,  B01D53/326 ,  B01D53/48 ,  B01D53/76 ,  B01D61/3621 ,  C01B3/24 ,  C01B3/38 ,  C01B3/382 ,  C01B3/386 ,  C01B3/56 ,  C01B3/58 ,  H05K999/99 ,  B01D2252/102 ,  B01D2252/103 ,  B01D2252/20436 ,  B01D2252/504 ,  B01D2252/602 ,  B01D2256/16 ,  B01D2256/20 ,  B01D2257/304 ,  B01D2257/306 ,  B01D2257/406 ,  B01D2257/504 ,  B01D2257/60 ,  B01D2257/708 ,  B01D2259/402 ,  C01B2203/0227 ,  C01B2203/0233 ,  C01B2203/025 ,  C01B2203/0261 ,  C01B2203/04 ,  C01B2203/0415 ,  C01B2203/042 ,  C01B2203/043 ,  C01B2203/0435 ,  C01B2203/045 ,  C01B2203/0465 ,  C01B2203/0475 ,  C01B2203/048 ,  C01B2203/0485 ,  C01B2203/061 ,  C01B2203/062 ,  C01B2203/068 ,  C01B2203/0877 ,  C01B2203/1235 ,  C01B2203/1241 ,  C01B2203/142 ,  C01B2203/147 ,  C01B2203/84 ,  Y02P20/129 ,  Y02P30/00

Abstract: A system and method for processing unconditioned syngas first removes solids and semi-volatile organic compounds (SVOC), then removes volatile organic compounds (VOC), and then removes at least one sulfur containing compound from the syngas. Additional processing may be performed depending on such factors as the source of syngas being processed, the products, byproducts and intermediate products desired to be formed, captured or recycled and environmental considerations.

公开(公告)号：US20230407197A1

公开(公告)日：2023-12-21

申请号：US18137863

申请日：2023-04-21

Applicant: ThermoChem Recovery International, Inc.

Inventor： Ravi Chandran ,  Daniel A. Burciaga ,  Daniel Michael Leo ,  Shawn Robert Freitas ,  Dave G. Newport ,  Justin Kevin Miller ,  Kaitlin Emily Harrington ,  Brian Christopher Attwood

IPC: C10J3/12 ,  C10J3/10 ,  C10J3/24 ,  C10J3/32 ,  C10J3/72 ,  C10J3/84 ,  C10G5/06 ,  C10G1/04 ,  C10L1/04 ,  F02B43/08 ,  C10G2/00 ,  C10L5/46 ,  C01B3/02

CPC classification number: C10J3/12 ,  C10J2300/0976 ,  C10J3/24 ,  C10J3/32 ,  C10J3/723 ,  C10J3/721 ,  C10J3/845 ,  C10G5/06 ,  C10G1/045 ,  C10L1/04 ,  F02B43/08 ,  C10G2/32 ,  C10L5/46 ,  C01B3/02 ,  C10J2200/09 ,  C10J2200/15 ,  C10J2200/36 ,  C10J2300/0903 ,  C10J2300/0946 ,  C10J2300/094 ,  C10J2300/0956 ,  C10J2300/0959 ,  C10J2300/0969 ,  C10J2300/0993 ,  C10J2300/1246 ,  C10J2300/1606 ,  C10J2300/1637 ,  C10J2300/165 ,  C10J2300/1659 ,  C10J2300/1656 ,  C10J2300/1846 ,  C10J2300/1853 ,  C10G2300/1003 ,  C10G2300/205 ,  C10G2400/04 ,  C10G2400/08 ,  C10L2270/026 ,  C10L2270/04 ,  C10L2290/04 ,  C10L2290/06 ,  C10L2290/08 ,  C10L2290/02 ,  C10L2290/145 ,  C10L2290/24 ,  C10L2290/42 ,  C10L2290/58 ,  C10L2290/54 ,  C10L2290/148 ,  Y02E50/10 ,  Y02E20/16 ,  Y02E50/30 ,  C10J2200/154 ,  C01B2203/146 ,  C01B2203/0475 ,  C01B2203/062 ,  C01B2203/061 ,  C01B2203/0405 ,  Y02T10/30 ,  C10J3/10

Abstract: A feedstock delivery system transfers a carbonaceous material, such as municipal solid waste, into a product gas generation system. The feedstock delivery system includes a splitter for splitting bulk carbonaceous material into a plurality of carbonaceous material streams. Each stream is processed using a weighing system for gauging the quantity of carbonaceous material, a densification system for forming plugs of carbonaceous material, a de-densification system for breaking up the plugs of carbonaceous material, and a gas and carbonaceous material mixing system for forming a carbonaceous material and gas mixture. A pressure of the mixing gas is reduced prior to mixing with the carbonaceous material, and the carbonaceous material to gas weight ratio is monitored. A transport assembly conveys the carbonaceous material and gas mixture to a first reactor where at least the carbonaceous material within the mixture is subject to thermochemical reactions to form the product gas.

公开(公告)号：US11370982B2

公开(公告)日：2022-06-28

申请号：US16512750

申请日：2019-07-16

Applicant: ThermoChem Recovery International, Inc.

Inventor： Ravi Chandran ,  Daniel A. Burciaga ,  Daniel Michael Leo ,  Shawn Robert Freitas ,  Dave G. Newport ,  Justin Kevin Miller ,  Kaitlin Emily Harrington ,  Brian Christopher Attwood

IPC: C10J3/12 ,  C10G2/00 ,  C10J3/10 ,  C10J3/24 ,  C10J3/32 ,  C10J3/72 ,  C10J3/84 ,  C10G5/06 ,  C10G1/04 ,  C10L1/04 ,  F02B43/08 ,  C10L5/46 ,  C01B3/02

Abstract: A feedstock delivery system transfers a carbonaceous material, such as municipal solid waste, into a product gas generation system. The feedstock delivery system includes a splitter for splitting bulk carbonaceous material into a plurality of carbonaceous material streams. Each stream is processed using a weighing system for gauging the quantity of carbonaceous material, a densification system for forming plugs of carbonaceous material, a de-densification system for breaking up the plugs of carbonaceous material, and a gas and carbonaceous material mixing system for forming a carbonaceous material and gas mixture. A pressure of the mixing gas is reduced prior to mixing with the carbonaceous material, and the carbonaceous material to gas weight ratio is monitored. A transport assembly conveys the carbonaceous material and gas mixture to a first reactor where at least the carbonaceous material within the mixture is subject to thermochemical reactions to form the product gas.

公开(公告)号：US20220154930A1

公开(公告)日：2022-05-19

申请号：US17589131

申请日：2022-01-31

Applicant: ThermoChem Recovery International, Inc.

Inventor： Ravi Chandran ,  Daniel A. Burciaga ,  Daniel Michael Leo ,  Shawn Robert Freitas ,  Dave G. Newport ,  Justin Kevin Miller ,  Kaitlin Emily Harrington ,  Brian Christopher Attwood

IPC: F23G5/30 ,  B01J8/04 ,  B01J19/00 ,  B01J19/24 ,  B09B3/00 ,  C01B3/02 ,  C10J3/48 ,  C10J3/72 ,  C10J3/84 ,  F23G5/00

Abstract: A multi-stage product gas generation system converts a carbonaceous material, such as municipal solid waste, into a product gas which may subsequently be converted into a liquid fuel or other material. One or more reactors containing bed material may be used to conduct reactions to effect the conversions. Unreacted inert feedstock contaminants present in the carbonaceous material may be separated from bed material using a portion of the product gas. A heat transfer medium collecting heat from a reaction in one stage may be applied as a reactant input in another, earlier stage.

公开(公告)号：US20210284924A1

公开(公告)日：2021-09-16

申请号：US16814892

申请日：2020-03-10

Applicant: ThermoChem Recovery International, Inc.

Inventor： Ravi CHANDRAN ,  Dave G. NEWPORT ,  Daniel A. BURCIAGA ,  Daniel Michael LEO ,  Justin Kevin MILLER ,  Brian Christopher ATTWOOD

IPC: C10J3/84 ,  C10K3/06 ,  C10K1/00 ,  C10L1/02 ,  C10L1/06 ,  C10L1/08 ,  C10G2/00 ,  C01B3/34 ,  C01B3/50 ,  C12P7/06 ,  B01J19/24 ,  B01J19/00 ,  C07C29/151 ,  C07C41/01

Abstract: A method of producing liquid fuel and/or chemicals from a carbonaceous material entails combusting a conditioned syngas in pulse combustion heat exchangers of a steam reformer to help convert carbonaceous material into first reactor product gas which includes carbon monoxide, hydrogen, carbon dioxide and other gases. A portion of the first reactor product gas is transferred to a hydrogen reformer into which additional conditioned syngas is added and a reaction carried out to produce an improved syngas. The improved syngas is then subject to one or more gas clean-up steps to form a new conditioned syngas. A portion of the new conditioned syngas is recycled to be used as the conditioned syngas in the pulse combustion heat exchangers and in the hydrocarbon reformer. A system for carrying out the method include, a steam reformer, a hydrocarbon reformer, first and second gas-cleanup systems, a synthesis system and an upgrading system.

公开(公告)号：US20190210873A1

公开(公告)日：2019-07-11

申请号：US16354521

申请日：2019-03-15

Applicant: ThermoChem Recovery International, Inc.

Inventor： Ravi Chandran ,  Daniel Michael Leo ,  Shawn Robert Freitas ,  Dave D. Newport ,  Hamilton Sean Michael Whitney ,  Daniel A. Burciaga

IPC: C01B3/52 ,  B01D53/26 ,  B01D5/00 ,  C01B3/58 ,  C01B3/38 ,  B01D61/36 ,  B01D53/76 ,  B01D53/48 ,  B01D53/14 ,  B01D53/047 ,  B01D53/04 ,  B01D50/00 ,  B01D46/00 ,  B01D29/66 ,  B01D29/27 ,  B01D17/02 ,  B01D47/10 ,  B01D53/12 ,  B01D53/18 ,  B01D53/32 ,  C01B3/56 ,  C01B3/24

Abstract: A system and method for processing unconditioned syngas first removes solids and semi-volatile organic compounds (SVOC), then removes volatile organic compounds (VOC), and then removes at least one sulfur containing compound from the syngas. Additional processing may be performed depending on such factors as the source of syngas being processed, the products, byproducts and intermediate products desired to be formed, captured or recycled and environmental considerations.