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51.
公开(公告)号:US10011483B2
公开(公告)日:2018-07-03
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: C01B3/38 , C01B3/58 , C01B3/52 , C01B3/56 , 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
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.
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公开(公告)号:US09920268B2
公开(公告)日:2018-03-20
申请号:US15347138
申请日:2016-11-09
Applicant: Thermochem Recovery International, Inc.
Inventor: Ravi Chandran , Jonathan A. Zenz , Dave G. Newport , Hamilton Sean Michael Whitney
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.
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公开(公告)号:US09920267B2
公开(公告)日:2018-03-20
申请号:US15347079
申请日:2016-11-09
Applicant: Thermochem Recovery International, Inc.
Inventor: Ravi Chandran , Jonathan A. Zenz , Dave G. Newport , Hamilton Sean Michael Whitney
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.
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公开(公告)号:US09499404B2
公开(公告)日:2016-11-22
申请号:US14347431
申请日:2012-09-27
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 , C01B3/56 , B01D53/047 , B01D53/12 , B01D53/14 , B01D53/18 , B01D53/32 , C01B3/24 , B01D5/00 , B01D47/10 , B01D17/02 , B01D29/27 , B01D29/66
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.
Abstract translation: 用于处理未条件合成气的系统和方法首先除去固体和半挥发性有机化合物(SVOC),然后除去挥发性有机化合物(VOC),然后从合成气中除去至少一种含硫化合物。 可以根据诸如待处理的合成气的来源,期望形成,捕获或再循环的产物,副产物和中间产物等因素进行附加处理和环境考虑。
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55.
公开(公告)号:US12203040B2
公开(公告)日:2025-01-21
申请号:US18232439
申请日:2023-08-10
Applicant: ThermoChem Recovery International, Inc.
Inventor: Ravi Chandran , Dave G. Newport , Daniel A. Burciaga , Daniel Michael Leo
Abstract: A two-stage syngas production method to produce a final product gas from a carbonaceous material includes producing a first product gas in a first reactor, separating char from the first product gas to produce separated char and char-depleted product gas, and separately reacting the separated char and the char-depleted product gas with an oxygen-containing gas in a second reactor to produce a final product gas. The separated char is introduced into the second reactor above the char-depleted product gas. The solids separation device may include serially connected cyclones, and the separated char may be entrained in a motive fluid in an eductor to produce a char and motive fluid mixture prior to being transferred to the second reactor. A biorefinery method produces a purified product from the final product gas.
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56.
公开(公告)号:US20240059991A1
公开(公告)日:2024-02-22
申请号:US18232439
申请日:2023-08-10
Applicant: ThermoChem Recovery International, Inc.
Inventor: Ravi Chandran , Dave G. Newport , Daniel A. Burciaga , Daniel Michael Leo
CPC classification number: C10J3/721 , C10K1/005 , C10K1/026 , C10J2300/0946 , C10J2300/1261 , C10J2300/1853 , C10J2300/1618 , C10J2300/0959 , C10J2300/1815 , C10J2300/1846 , C10J2300/1637
Abstract: A two-stage syngas production method to produce a final product gas from a carbonaceous material includes producing a first product gas in a first reactor, separating char from the first product gas to produce separated char and char-depleted product gas, and separately reacting the separated char and the char-depleted product gas with an oxygen-containing gas in a second reactor to produce a final product gas. The separated char is introduced into the second reactor above the char-depleted product gas. The solids separation device may include serially connected cyclones, and the separated char may be entrained in a motive fluid in an eductor to produce a char and motive fluid mixture prior to being transferred to the second reactor. A biorefinery method produces a purified product from the final product gas.
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57.
公开(公告)号:US20230071045A1
公开(公告)日:2023-03-09
申请号:US17957670
申请日:2022-09-30
Applicant: ThermoChem Recovery International, Inc.
Inventor: Ravi Chandran , Dave G. Newport , Daniel A. Burciaga , Daniel Michael Leo
Abstract: A two-stage syngas production method to produce a final product gas from a carbonaceous material includes producing a first product gas in a first reactor, separating char from the first product gas to produce separated char and char-depleted product gas, and separately reacting the separated char and the char-depleted product gas with an oxygen-containing gas in a second reactor to produce a final product gas. The separated char is introduced into the second reactor above the char-depleted product gas. The solids separation device may include serially connected cyclones, and the separated char may be entrained in a motive fluid in an eductor to produce a char and motive fluid mixture prior to being transferred to the second reactor. A biorefinery method produces a purified product from the final product gas.
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58.
公开(公告)号:US11555157B2
公开(公告)日:2023-01-17
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: C01B3/34 , C10J3/84 , C07C41/01 , C07C29/151 , C10K3/06 , C10K1/00 , C10L1/02 , C10L1/06 , C10L1/08 , C10G2/00 , C01B3/50 , C12P7/06 , B01J19/24 , B01J19/00
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.
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59.
公开(公告)号:US11466223B2
公开(公告)日:2022-10-11
申请号:US17012901
申请日:2020-09-04
Applicant: ThermoChem Recovery International, Inc.
Inventor: Ravi Chandran , Dave G. Newport , Daniel A. Burciaga , Daniel Michael Leo
Abstract: A two-stage syngas production method to produce a final product gas from a carbonaceous material includes producing a first product gas in a first reactor, separating char from the first product gas to produce separated char and char-depleted product gas, and separately reacting the separated char and the char-depleted product gas with an oxygen-containing gas in a second reactor to produce a final product gas. The separated char is introduced into the second reactor above the char-depleted product gas. The solids separation device may include serially connected cyclones, and the separated char may be entrained in a motive fluid in an eductor to produce a char and motive fluid mixture prior to being transferred to the second reactor. A biorefinery method produces a purified product from the final product gas.
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公开(公告)号:US11208605B2
公开(公告)日:2021-12-28
申请号:US16451356
申请日:2019-06-25
Applicant: ThermoChem Recovery International, Inc.
Inventor: Ravi Chandran , Dave G. Newport , Daniel Michael Leo , Daniel A. Burciaga , Justin Kevin Miller , Kaitlin Emily Harrington , Brian Christopher Attwood , Emily Jane Schultheis , Kelly Ann Kishton
Abstract: A solids discharge system (SDS) is configured to separate solids from product gas. The system includes a solids separation device and at least one solids transfer conduit configured to receive solids from the solids separation device. The solids transfer conduit is selectively partitioned into a plurality of compartments (or “sections”) along its length by isolation valves. A gas supply conduit and a gas discharge conduits are connected to one of the sections to facilitate removal of solids. A filter in fluid communication with that section is configured to prevent solids from passing through the gas discharge conduit so that the solids can be removed from one of the sections of the solids transfer conduit. A product gas generation system incorporates first and second reactors, the latter of which receives products created by the second reactor.
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