公开(公告)号：WO2015130481A2

公开(公告)日：2015-09-03

申请号：PCT/US2015/015723

申请日：2015-02-13

Applicant: API INTELLECTUAL PROPERTY HOLDINGS, LLC

Inventor： SZCZEPANIK, Mark

CPC classification number: C08B37/0003 ,  B01D53/507 ,  B01D2258/0283 ,  C08H8/00 ,  C12P19/02 ,  C12P2201/00 ,  Y02P20/136

Abstract: What is disclosed is a biorefining process and system including the steps of extracting, hydrolyzing, and/or digesting a lignocellulosic biomass feedstock, or a component thereof, with a liquid or vapor solution comprising reactant sulfur dioxide or a derivative thereof, to generate cellulose-rich solids and an intermediate liquid stream; combusting or gasifying a sulfur-containing fuel to generate heat and an exhaust gas stream comprising produced sulfur dioxide; contacting the exhaust gas stream with the intermediate liquid stream to dissolve the produced sulfur dioxide into the intermediate liquid stream; and then recycling the intermediate liquid stream to reuse the produced sulfur dioxide as the reactant sulfur dioxide. The sulfur- containing fuel may be sulfonated lignin generated by reaction of lignin (derived from the feedstock) with the reactant sulfur dioxide, resulting in a closed loop for sulfur dioxide in the biorefmery.

Abstract translation: 所公开的是一种生物精制方法和系统，其包括用包含反应物二氧化硫或其衍生物的液体或蒸气溶液提取，水解和/或消化木质纤维素生物质原料或其组分的步骤，以产生纤维素 - 富含固体和中间液体流; 燃烧或气化含硫燃料以产生热量和包含生成的二氧化硫的废气流; 使废气流与中间液体流接触以将产生的二氧化硫溶解到中间液体流中; 然后再循环中间液体流以再生所产生的二氧化硫作为反应物二氧化硫。 含硫燃料可以是通过木质素（衍生自原料）与反应物二氧化硫的反应产生的磺化木质素，导致生物反应器中二氧化硫的闭环。

公开(公告)号：WO2014138600A1

公开(公告)日：2014-09-12

申请号：PCT/US2014/021815

申请日：2014-03-07

Applicant: XYLECO, INC.

Inventor： MEDOFF, Marshall ,  MASTERMAN, Thomas Craig ,  MUKHERJEE, Maia Stapleton ,  COOPER, Christopher

IPC: C12P7/10

CPC classification number: B01D61/445 ,  B01D15/02 ,  B01D53/32 ,  B01D61/44 ,  B01J19/085 ,  B01J2219/0869 ,  B01J2219/0879 ,  B01J2219/0886 ,  B65G27/00 ,  B65G53/04 ,  B65G53/40 ,  C07C29/149 ,  C07C31/12 ,  C10G1/00 ,  C10L1/023 ,  C10L1/026 ,  C10L9/08 ,  C10L2200/0469 ,  C10L2200/0476 ,  C10L2290/36 ,  C12M47/00 ,  C12M47/10 ,  C12P7/04 ,  C12P7/06 ,  C12P7/10 ,  C12P7/52 ,  C12P7/56 ,  C12P19/02 ,  C12P19/14 ,  C12P2201/00 ,  C12P2203/00 ,  C13K1/02 ,  C13K13/002 ,  D21C9/007 ,  E04B1/92 ,  E04B2001/925 ,  G21F7/00 ,  H01J37/317 ,  H01J2237/202 ,  H01J2237/31 ,  H01J2237/3165 ,  Y02E50/16 ,  Y02E50/17 ,  Y02E50/32 ,  Y02E50/343 ,  Y02E60/17 ,  Y02P20/136 ,  Y02W10/33 ,  Y02W10/37

Abstract: Biomass (e.g., plant biomass, animal biomass, and municipal waste biomass) is processed to produce useful intermediates and products, such as energy, fuels, foods or materials.. Systems, methods and equipment are described for upgrading process streams using electrodialysis or electrodialysis reversal. ] Many potential lignocellulosic feedstocks are available today, including agricultural residues, woody biomass, municipal waste, oilseeds/cakes and seaweed, to name a few.

Abstract translation: 生物质（例如，植物生物量，动物生物量和城市废物生物质）被加工以产生有用的中间体和产品，例如能量，燃料，食品或材料。描述了使用电渗析或电渗析来改进工艺流的系统，方法和设备 逆转。 许多潜在的木质纤维素原料今天可用，包括农业残留物，木质生物质，城市废物，油籽/蛋糕和海藻等等。

公开(公告)号：WO2014138550A1

公开(公告)日：2014-09-12

申请号：PCT/US2014/021632

申请日：2014-03-07

Applicant: XYLECO, INC.

Inventor： MEDOFF, Marshall ,  MASTERMAN, Thomas Craig ,  PARADIS, Robert

IPC: G01T7/08

CPC classification number: B01D61/445 ,  B01D15/02 ,  B01D53/32 ,  B01D61/44 ,  B01J19/085 ,  B01J2219/0869 ,  B01J2219/0879 ,  B01J2219/0886 ,  B65G27/00 ,  B65G53/04 ,  B65G53/40 ,  C07C29/149 ,  C07C31/12 ,  C10G1/00 ,  C10L1/023 ,  C10L1/026 ,  C10L9/08 ,  C10L2200/0469 ,  C10L2200/0476 ,  C10L2290/36 ,  C12M47/00 ,  C12M47/10 ,  C12P7/04 ,  C12P7/06 ,  C12P7/10 ,  C12P7/52 ,  C12P7/56 ,  C12P19/02 ,  C12P19/14 ,  C12P2201/00 ,  C12P2203/00 ,  C13K1/02 ,  C13K13/002 ,  D21C9/007 ,  E04B1/92 ,  E04B2001/925 ,  G21F7/00 ,  H01J37/317 ,  H01J2237/202 ,  H01J2237/31 ,  H01J2237/3165 ,  Y02E50/16 ,  Y02E50/17 ,  Y02E50/32 ,  Y02E50/343 ,  Y02E60/17 ,  Y02P20/136 ,  Y02W10/33 ,  Y02W10/37

Abstract: Materials, such as biomass feedstocks (e.g., plant biomass, animal biomass, and municipal waste biomass) are processed to produce useful products, such as fuels. Conveying systems, such as flowing gas conveying systems and such as closed-loop flowing gas conveying systems are described. Many potential lignocellulosic feedstocks are available today, including agricultural residues, woody biomass, municipal waste, oilseeds/cakes and seaweed, to name a few.

Abstract translation: 诸如生物质原料（例如，植物生物质，动物生物质和城市废物生物质）之类的材料被加工以生产有用的产品，例如燃料。 描述了诸如流动气体输送系统和闭环流动气体输送系统之类的输送系统。 许多潜在的木质纤维素原料今天可用，包括农业残留物，木质生物质，城市废物，油籽/蛋糕和海藻等等。

公开(公告)号：WO2014138549A1

公开(公告)日：2014-09-12

申请号：PCT/US2014/021630

申请日：2014-03-07

Applicant: XYLECO, INC.

Inventor： MEDOFF, Marshall ,  MASTERMAN, Thomas, Craig ,  PARADIS, Robert

IPC: B01J19/08

CPC classification number: B01D61/445 ,  B01D15/02 ,  B01D53/32 ,  B01D61/44 ,  B01J19/085 ,  B01J2219/0869 ,  B01J2219/0879 ,  B01J2219/0886 ,  B65G27/00 ,  B65G53/04 ,  B65G53/40 ,  C07C29/149 ,  C07C31/12 ,  C10G1/00 ,  C10L1/023 ,  C10L1/026 ,  C10L9/08 ,  C10L2200/0469 ,  C10L2200/0476 ,  C10L2290/36 ,  C12M47/00 ,  C12M47/10 ,  C12P7/04 ,  C12P7/06 ,  C12P7/10 ,  C12P7/52 ,  C12P7/56 ,  C12P19/02 ,  C12P19/14 ,  C12P2201/00 ,  C12P2203/00 ,  C13K1/02 ,  C13K13/002 ,  D21C9/007 ,  E04B1/92 ,  E04B2001/925 ,  G21F7/00 ,  H01J37/317 ,  H01J2237/202 ,  H01J2237/31 ,  H01J2237/3165 ,  Y02E50/16 ,  Y02E50/17 ,  Y02E50/32 ,  Y02E50/343 ,  Y02E60/17 ,  Y02P20/136 ,  Y02W10/33 ,  Y02W10/37

Abstract: Biomass ( e.g ., plant biomass, animal biomass, and municipal waste biomass) is processed to produce useful intermediates and products, such as energy, fuels, foods or materials. For example, equipment, systems and methods are described that can be used to treat feedstock materials, such as cellulosic and/or lignocellulosic materials, in a vault in which hazardous gases are removed, destroyed and/or converted. The treatments are efficient and can reduce the recalcitrance of the lignocellulosic material so that it is easier to produce an intermediate or product, e.g ., sugars, alcohols, sugar alcohols and energy, from the lignocellulosic material.

Abstract translation: 加工生物质（例如，植物生物质，动物生物质和城市废物生物质）以产生有用的中间体和产品，例如能量，燃料，食品或材料。 例如，描述了可用于处理有毒气体被去除，破坏和/或转化的库中的原料如纤维素和/或木质纤维素材料的设备，系统和方法。 这些处理是有效的并且可以降低木质纤维素材料的顽固性，从而更容易从木质纤维素材料生产中间体或产物，例如糖，醇，糖醇和能量。

公开(公告)号：WO2014088644A1

公开(公告)日：2014-06-12

申请号：PCT/US2013/047306

申请日：2013-06-24

Applicant: CHEVRON U.S.A. INC.

Inventor： JADHAV, Raja Ankush

IPC: B01D53/06 ,  B01D53/62 ,  B01D53/96 ,  F23L7/00 ,  C01B13/08

CPC classification number: F23L7/007 ,  B01D53/265 ,  C01B13/08 ,  F23C2900/99008 ,  F23J15/02 ,  F23J15/06 ,  F23L7/005 ,  Y02C10/04 ,  Y02C10/08 ,  Y02E20/344 ,  Y02E20/346 ,  Y02P20/136 ,  Y02P20/152

Abstract: An oxyfiring system and method for capturing carbon dioxide in a combustion process is disclosed. The oxyfiring system comprises (a) an oxidation reactor for oxidizing a reduced metal oxide; (b) a decomposition reactor wherein oxidized metal oxide sorbents are reduced with oxygen being released and a flue gas with an oxygen enriched carbon dioxide stream is produced; (c) a fuel combustion reactor for combusting a primary fuel and the oxygen enriched carbon dioxide stream into a primary flue gas; and (d) separation apparatus for separating a portion of the primary flue gas so that a carbon dioxide enriched stream can be sent to the decomposition reactor. Steam may be added to assist in controlling the partial pressure of oxygen during decomposition of the metal oxide and a condenser may be used to remove water from the oxygen enriched flue gas.

Abstract translation: 公开了一种用于在燃烧过程中捕获二氧化碳的氧发射系统和方法。 氧发生系统包括（a）用于氧化还原的金属氧化物的氧化反应器; （b）分解反应器，其中氧气被释放氧化的金属氧化物吸附剂被还原，产生具有富氧二氧化碳气流的烟气; （c）燃料燃烧反应器，用于将主要燃料和富氧二氧化碳流燃烧成主烟道气; 和（d）用于分离一部分原烟气的分离装置，使得富二氧化碳流可以被送到分解反应器。 可以加入蒸汽以帮助控制金属氧化物分解期间的氧分压，并且可以使用冷凝器从富氧烟道气中除去水。

公开(公告)号：WO2014027368A2

公开(公告)日：2014-02-20

申请号：PCT/IN2013/000493

申请日：2013-08-12

Applicant: COUNCIL OF SCIENTIFIC & INDUSTRIAL RESEARCH

Inventor： GHOSH, Pushpito, Kumar ,  MONDAL, Dibyendu ,  MAITI, Pratyush ,  PRASAD, Kamalesh ,  MAITI, Subarna ,  SHAH, Bharti, Gunvantray ,  SIDDHANTA, Arup, Kumar

IPC: C10L1/02

CPC classification number: C07D307/46 ,  C02F1/04 ,  C02F1/283 ,  C02F2303/02 ,  C05D1/00 ,  C05D1/02 ,  C07C51/31 ,  C07H3/02 ,  C08B37/0042 ,  C10L1/02 ,  C10L1/1881 ,  C10L1/1885 ,  C10L1/2493 ,  C10L5/44 ,  C10L2290/02 ,  C10L2290/04 ,  C10L2290/10 ,  C10L2290/12 ,  C10L2290/24 ,  C10L2290/28 ,  C10L2290/38 ,  C10L2290/44 ,  C10L2290/543 ,  C10L2290/544 ,  C10L2290/547 ,  C10L2290/548 ,  Y02E50/10 ,  Y02E50/30 ,  Y02P20/125 ,  Y02P20/136 ,  Y02W10/37

Abstract: The invention relates to an integrated process for the production of 5-hydroxymethyl furfural (HMF), K 2 SO 4 , levulinic acid and formic acid from κ-carrageenan, the latter being obtained from fresh Kappaphycus alvarezii seaweed biomass after expelling the juice. Mg(HSO 4 ) 2 was used in HMF synthesis, with co-production of galactose. The aqueous stream after HMF extraction was treated with the seaweed juice which process facilitated recovery of K 2 SO 4 in pure form. The galactose may be utilised for synthesis of levulinic acid and formic acid before or after K 2 SO 4 recovery or, alternatively, utilised for other purposes. Catalysts required in the synthetic reactions are generated in the process itself while the process energy required is met out of additional supplies of the seaweed biomass which is subjected to combustion/gasification.

Abstract translation: 本发明涉及生产5-羟甲基糠醛（HMF），K 2 SO 4，乙酰丙酸和甲酰胺的整合方法 来自κ-角叉菜胶的酸，后者在排出果汁后从新鲜的Kappaphycus alvarezii海藻生物质获得。 在HMF合成中使用Mg（HSO 4）2 2与半乳糖共同产生。 用海藻汁处理HMF萃取后的水流，该过程有利于以纯形式回收K 2 SO 4。 半乳糖可用于在K 2 SO 4回收之前或之后合成乙酰丙酸和甲酸，或者可用于其它目的。 合成反应中所需的催化剂在工艺本身中产生，而所需的工艺能量通过经受燃烧/气化的海藻生物质的额外供应来满足。

公开(公告)号：WO2013051003A1

公开(公告)日：2013-04-11

申请号：PCT/IN2012/000139

申请日：2012-02-29

Applicant: TRANSCARB ENERGY PRIVATE LIMITED ,  VIJAY, Kumar, Narayan ,  KRISHNAN, Neelakantan ,  PRADEEP, Kuber

Inventor： VIJAY, Kumar, Narayan ,  KRISHNAN, Neelakantan ,  PRADEEP, Kuber

IPC: C02F9/14 ,  C02F3/00 ,  C05F9/04 ,  B09B5/00 ,  B09B3/00

CPC classification number: B09B3/00 ,  B09B5/00 ,  C02F3/28 ,  C02F2303/10 ,  C05F17/0018 ,  C05F17/0027 ,  C12M21/04 ,  C12M23/58 ,  C12M43/00 ,  Y02E50/343 ,  Y02P20/129 ,  Y02P20/136 ,  Y02P20/145 ,  Y02P20/59 ,  Y02W10/30 ,  Y02W30/20 ,  Y02W30/43 ,  Y02W30/47

Abstract: A self-sustainable integrated solid and liquid waste management, treatment, and energy generation system, said system comprises: (a) feed preparation module adapted to receive waste feed and further adapted to segregate said received waste feed, said feed preparation module further comprises: (i) Waste Oil Treatment Process Module; (ii) Sewage and Liquid Organic Effluent Treatment Module; (iii) Solid Organic Waste Treatment Module; (b) energy production module adapted to receive prepared feed from said feed preparation module and further adapted to generate biogas, electrical power, and fertiliser, said energy production module further comprises: (i)Biomethanation and Anaerobic Digestion Module; (ii) Biogas Cleanup Module; (iii) Pilot Fuel / Duel Fuel Biogas Engine Generator Module; (c) auxiliary processing module adapted to receive hot exhaust gas, organic digestate, hot condensate water in order to provide energy to vapour absorption chiller and to obtain cooled exhaust gas rich in carbon-dioxide which will provide energy for green house, organic fertiliser, cold storage propelling refrigerant, processed water and residue feeds, said auxiliary processing module further comprises: (i) Biogas Engine Exhaust Gas Waste Heat Recovery Module; (ii) Organic Fertiliser Module; (iii) Vapour Absorption Chiller and Cold Storage Module; and (iv) Reverse Osmosis Waste Water Treatment Module.

Abstract translation: 一种自主可持续的综合固体和液体废物管理，处理和能量产生系统，所述系统包括：（a）适于接收废物进料并进一步适于分离所述接收到的废物进料的饲料制备模块，所述饲料制备模块还包括： （i）废油处理流程模块; （ii）污水和液体有机污水处理模块; （iii）固体有机废物处理模块; （b）能量生产模块，其适于从所述饲料制备模块接收准备的饲料，并且还适于产生生物气，电力和肥料，所述能量产生模块还包括：（i）生物降解和厌氧消化模块; （ii）沼气净化模块; （iii）燃油/决斗燃油沼气发动机模块试点; （c）辅助加工模块，适用于接收热废气，有机消解物质，热凝水，以便向蒸汽吸收式制冷机提供能量，并获得富含二氧化碳的冷却废气，为温室，有机肥料， 冷藏推进制冷剂，加工水和残渣进料，所述辅助处理模块还包括：（i）沼气发动机排气废热回收模块; （ii）有机肥料模块; （iii）蒸气吸收式冷水机组及冷藏模组; 和（iv）反渗透废水处理模块。

公开(公告)号：WO2011101137A1

公开(公告)日：2011-08-25

申请号：PCT/EP2011/000748

申请日：2011-02-16

Applicant: MEISSNER, Jan A. ,  FELDMANN, Michael

Inventor： FELDMANN, Michael

IPC: C12P5/02

CPC classification number: C12P5/023 ,  C07C29/1518 ,  C10L3/08 ,  C10L3/104 ,  C12M21/04 ,  C12M21/12 ,  C12M23/58 ,  C12M45/20 ,  C12M47/18 ,  Y02E50/32 ,  Y02E50/343 ,  Y02P20/128 ,  Y02P20/129 ,  Y02P20/134 ,  Y02P20/136 ,  C07C31/04

Abstract: Die vorliegende Erfindung betrifft ein Verfahren und Anlagen zur Erzeugung von treibhausgasreduziertem Biogas, zu dessen Aufbereitung zu treibhausgasreduziertem BioMethan und regenerativem Kohlenstoffdioxid (CO 2 ), zur Vermischung von treibhausgasreduziertem BioMethan und Erdgas (CNG) zu einem treibhausgasreduzierten Mischgas und zur Verwendung des treibhausgasreduzierten BioMethans und/oder des treibhausgasreduzierten Mischgases als treibhausgasreduzierte Energieträger, insbesondere als treibhausgasreduzierter Kraftstoff im Verkehr.

Abstract translation: 本发明涉及一种用于生产treibhausgasreduziertem沼气，其制备于treibhausgasreduziertem BioMethan和再生二氧化碳（CO2），用于BioMethan和天然气（CNG）混合treibhausgasreduziertem到温室气体减少混合气体和使用温室气体的减少的Biomet汉斯和/或方法和设备 温室气体减少混合气体作为温室气体减少能源，特别是作为温室气体减少运输燃料。

公开(公告)号：WO2010137028A3

公开(公告)日：2011-01-20

申请号：PCT/IN2009000644

申请日：2009-11-13

Applicant: CONCORD BLUE TECHNOLOGY PVT LTD ,  GOEL PRERAK ,  THANNHAEUSER CHRISTOPHER FREDERIK

Inventor： GOEL PRERAK ,  THANNHAEUSER CHRISTOPHER FREDERIK

IPC: C10J3/46 ,  C10B49/16 ,  C10J3/48

CPC classification number: C10K3/02 ,  C01B3/384 ,  C01B2203/0233 ,  C01B2203/0811 ,  C01B2203/0894 ,  C01B2203/1058 ,  C10B49/18 ,  C10B53/02 ,  C10J3/12 ,  C10J2300/0916 ,  C10J2300/0976 ,  C10J2300/0993 ,  C10J2300/1637 ,  C10J2300/1853 ,  C10J2300/1861 ,  C10K3/023 ,  Y02E50/14 ,  Y02P20/129 ,  Y02P20/136

Abstract: The present invention relates to a process and a system for generating energy from biomass / organic wastes. A process for generating a product gas from biomass comprises of pyrolyzing the biomass in a pyrolyser by contacting the biomass with hot heat carriers to obtain pyrolysis gas and char; passing the pyrolysis gas to a reformer containing a reactant to obtain a product gas; and firing a part of the product gas coming out of the reformer back to the heater tubes of the reformer. Firing a part of the product gas through the fired heater tubes of the reformer provides the heat for sustaining the reaction between the pyrolysis gas and the reactant to form the product gas.

Abstract translation: 本发明涉及用于从生物质/有机废物产生能量的方法和系统。 用于由生物质产生产物气体的方法包括通过使生物质与热热载体接触来热解热解器中的生物质以获得热解气体和焦炭; 使热解气体通过含有反应物的重整器以获得产物气体; 并且将从重整器出来的一部分产物气体发回到重整器的加热器管。 通过重整器的火焰加热器管使一部分产物气体燃烧提供热量以维持热解气体和反应物之间的反应以形成产物气体。

公开(公告)号：WO2010144556A1

公开(公告)日：2010-12-16

申请号：PCT/US2010/037944

申请日：2010-06-09

Applicant: SUNDROP FUELS, INC.

Inventor： PERKINS, Christopher ,  HILTON, Courtland ,  STRAND, Steven, R. ,  KELLEY, Donna ,  SIMMONS, Wayne ,  MINDEN, Andrew ,  HILTON, Joseph ,  JOVANOVIC, Zoran

IPC: F25B29/00

CPC classification number: C01B3/384 ,  B01J19/0013 ,  B01J19/0033 ,  B01J19/2445 ,  B01J19/245 ,  B01J2219/00117 ,  B01J2219/00186 ,  C01B3/22 ,  C01B3/34 ,  C01B2203/0216 ,  C01B2203/0233 ,  C01B2203/061 ,  C01B2203/0811 ,  C01B2203/1241 ,  C01B2203/1685 ,  C01B2203/84 ,  C07C29/15 ,  C07C29/1518 ,  C10G2/30 ,  C10G2/32 ,  C10G3/00 ,  C10G2300/1014 ,  C10G2300/1025 ,  C10G2300/807 ,  C10J3/00 ,  C10J3/466 ,  C10J3/482 ,  C10J3/485 ,  C10J3/506 ,  C10J3/54 ,  C10J3/56 ,  C10J3/58 ,  C10J3/60 ,  C10J3/62 ,  C10J3/721 ,  C10J3/723 ,  C10J3/82 ,  C10J3/84 ,  C10J2200/09 ,  C10J2200/15 ,  C10J2200/158 ,  C10J2300/0906 ,  C10J2300/0909 ,  C10J2300/0916 ,  C10J2300/094 ,  C10J2300/0973 ,  C10J2300/0976 ,  C10J2300/0989 ,  C10J2300/0993 ,  C10J2300/1223 ,  C10J2300/123 ,  C10J2300/1284 ,  C10J2300/1292 ,  C10J2300/1621 ,  C10J2300/1659 ,  C10J2300/1665 ,  C10J2300/1693 ,  C10J2300/1853 ,  C10J2300/1861 ,  C10K1/024 ,  C10L1/04 ,  C10L2200/0492 ,  C10L2290/02 ,  C10L2290/04 ,  C10L2290/06 ,  C10L2290/08 ,  C10L2290/28 ,  C10L2290/42 ,  C10L2290/50 ,  C10L2290/52 ,  C10L2290/547 ,  F24S20/20 ,  Y02B40/18 ,  Y02E10/41 ,  Y02E50/18 ,  Y02E50/32 ,  Y02P20/129 ,  Y02P20/134 ,  Y02P20/136 ,  Y02P20/145 ,  Y02P30/20 ,  Y02T50/678 ,  C07C31/04

Abstract: A method, apparatus, and system for a solar-driven chemical reactor are disclosed, including a solar thermal receiver aligned to absorb concentrated solar energy. Some embodiments include a solar driven chemical reactor that has multiple reactor tubes. Some embodiments include one of 1) one or more apertures open to an atmosphere of the Earth or 2) one or more windows, to pass the concentrated solar energy into the solar thermal receiver. This energy impinges on the multiple reactor tubes and cavity walls of the receiver and transfer energy by solar radiation absorption and heat radiation, convection, and conduction. In this way, the energy causes reacting particles to drive the endothermic chemical reaction flowing in the reactor tubes. The design of the multiple reactor tubes and solar thermal receiver can be adapted per a solar flux profile to take advantage of variations in the concentrations of solar flux in the profile.

Abstract translation: 公开了一种用于太阳能驱动的化学反应器的方法，装置和系统，包括对准以吸收集中的太阳能的太阳能热接收器。 一些实施例包括具有多个反应器管的太阳能驱动的化学反应器。 一些实施例包括以下之一：1）对于地球的大气开放的一个或多个孔，或2）一个或多个窗口，以将集中的太阳能传递到太阳能热接收器中。 该能量冲击接收器的多个反应器管和腔壁，并通过太阳辐射吸收和热辐射，对流和传导来传递能量。 以这种方式，能量引起反应颗粒驱动在反应器管中流动的吸热化学反应。 多反应管和太阳能热接收器的设计可以根据太阳能通量分布进行调整，以利用轮廓中太阳能通量浓度的变化。