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公开(公告)号：US11634650B2
公开(公告)日：2023-04-25
申请号：US17850838
申请日：2022-06-27
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: B01J19/24 , B01J4/00 , C10J3/72 , C10G2/00 , C10J3/12 , C10J3/10 , C10J3/24 , C10J3/32 , 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.
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公开(公告)号：US20220325194A1
公开(公告)日：2022-10-13
申请号：US17850838
申请日：2022-06-27
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
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.
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公开(公告)号：US10364398B2
公开(公告)日：2019-07-30
申请号：US15251494
申请日：2016-08-30
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 , Emily Jane Schultheis , Kelly Ann Kishton
IPC: C10J3/12 , C01B3/02 , C10J3/10 , C10J3/24 , C10J3/32 , C10J3/72 , C10J3/84 , C10G5/06 , C10G1/04 , C10L1/04 , F02B43/08 , C10G2/00 , C10L5/46
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.
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4.发明授权公开(公告)号：US10280081B2
公开(公告)日：2019-05-07
申请号：US16117039
申请日：2018-08-30
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 , B01D29/66 , C01B3/24 , B01D17/02 , B01D5/00 , B01D47/10 , B01D53/12 , B01D53/14 , B01D53/18 , B01D53/32 , B01D53/047 , C01B3/56 , B01D29/27 , B01D53/26 , C01B3/58 , C01B3/38 , B01D61/36 , B01D53/76 , B01D53/48 , B01D53/04 , B01D50/00 , B01D46/00
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.
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5.发明授权公开(公告)号：US10214418B2
公开(公告)日：2019-02-26
申请号：US15793252
申请日：2017-10-25
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 , B01D29/66 , C01B3/24 , B01D17/02 , B01D5/00 , B01D47/10 , B01D53/12 , B01D53/14 , B01D53/18 , B01D53/32 , B01D53/047 , C01B3/56 , B01D29/27 , B01D46/00 , B01D50/00 , B01D53/04 , B01D53/48 , B01D53/76 , B01D61/36 , C01B3/38 , C01B3/58 , B01D53/26
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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Patent Agency Ranking
公开(公告)号：US09920712B1
公开(公告)日：2018-03-20
申请号：US15786993
申请日：2017-10-18
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 , Emily Jane Schultheis , Kelly Ann Kishton
IPC: C10B57/00 , C10B39/00 , C10B31/00 , C10G2/00 , F02P13/00 , F02M21/02 , C10B37/00 , C10J3/82 , C10J3/72
CPC classification number: F02M21/029 , C10G2/00 , C10J3/723 , C10J3/82 , C10J2200/15 , C10J2300/0906 , C10J2300/165 , C10J2300/1659 , F02M21/0209 , F02P13/00
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.
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公开(公告)号：US09783417B2
公开(公告)日：2017-10-10
申请号：US14939040
申请日：2015-11-12
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.
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公开(公告)号：US20160060110A1
公开(公告)日：2016-03-03
申请号：US14939040
申请日：2015-11-12
Applicant: ThermoChem Recovery International, Inc.
Inventor： Ravi Chandran , Daniel Michael Leo , Shawn Robert Freitas , Dave G. Newport , Hamilton Sean Michael Whitney , Daniel A. Burciaga
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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9.发明申请公开(公告)号：US20140296586A1
公开(公告)日：2014-10-02
申请号：US14355948
申请日：2012-11-05
Applicant: ThermoChem Recovery International, Inc.
Inventor： Ravi Chandran , Daniel Michael Leo , Shawn Robert Freitas
CPC classification number: C10G1/045 , B01J6/008 , C10B49/22 , C10B53/00 , C10B53/02 , C10G1/02 , C10J3/482 , C10J3/62 , C10J2300/0916 , C10J2300/094 , C10J2300/0946 , C10J2300/0976 , C10J2300/0993 , C10J2300/0996 , C10J2300/1246 , C10J2300/1807 , C10J2300/1884 , C10J2300/1892 , C10K1/026 , C10K3/06 , Y02E50/14 , Y02P20/145
Abstract: A feedstock flexible process for converting feedstock into oil and gas includes (i) indirectly heated hydrous devolatilization of volatile feedstock components, (ii) indirectly heated thermochemical conversion of fixed carbon feedstock components, (iii) heat integration and recovery, (iv) vapor and gas pressurization, and (v) vapor and gas clean-up and product recovery. A system and method for feedstock conversion includes a thermochemical reactor integrated with one or more hydrous devolatilization and solids circulation subsystems configured to accept a feedstock mixture, comprised of volatile feedstock components and fixed carbon feedstock components, and continuously produce a volatile reaction product stream therefrom, while simultaneously and continuously capturing, transferring, and converting the fixed carbon feedstock components to syngas.
Abstract translation: 用于将原料转化为油和气的原料柔性方法包括（i）间接加热挥发性原料组分的水合脱挥发分，（ii）间接加热固定碳原料组分的热化学转化，（iii）热积分和回收，（iv）蒸气和 气体加压，（v）蒸汽和气体清理和产品回收。 用于原料转化的系统和方法包括与一个或多个含水脱挥发分和固体循环子系统集成的热化学反应器，其构造成接收由挥发性原料组分和固定碳原料组分组成的原料混合物，并从其中连续产生挥发性反应产物流， 同时并连续地将固定碳原料组分捕获，转移和转化成合成气。
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公开(公告)号：US20140252276A1
公开(公告)日：2014-09-11
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
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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