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1. 发明公开

US20230204287A1 BIOMASS COMBUSTION SYSTEM FOR CERAMIC ROLLER KILN AND BIOMASS COMBUSTION METHOD 审中-公开
公开(公告)号：US20230204287A1
公开(公告)日：2023-06-29
申请号：US18060637
申请日：2022-12-01
申请人： GUANGZHOU INSTITUTE OF ENERGY TESTING
发明人： Kuo HUANG , Yuanming ZHANG , Xiaozhou LIU , Qilun LU , Chao FENG , Guoyu CHEN , Liling CHEN , Wei XIAO , Huixuan LIANG
IPC分类号： F27B9/12 , F27B9/02 , F27B9/40 , C10J3/72 , C10J3/82
CPC分类号： F27B9/12 , F27B9/029 , F27B9/40 , C10J3/723 , C10J3/82 , C10J2300/0916 , C10J2300/0953 , F27B2009/122 , F27B2009/124
摘要： A biomass combustion system for ceramic roller kiln, including a roller kiln including a preheating section, a combustion section and a cooling section; a biomass gasifier with a feed port, a first gas inlet, a second gas inlet and an gas outlet; a fuel manifold; and a pentane gasification device connected to the fuel manifold. The biomass or biomass waste is fed through the feed port. The gas outlet is connected to the fuel manifold through a heat exchanger. The premixer is configured to mix part of the hot air discharged from the cooling section with a mixture of biomass gas and gaseous pentane transported by the fuel manifold to obtain an air-fuel mixture, and distribute the mixture to the combustion section through burners. A biomass combustion process is also provided.

2. 发明申请

US20150337224A1 MICROWAVE ACCELERATION OF CARBON GASIFICATION REACTIONS 审中-公开
标题翻译：微波加速碳排放反应
公开(公告)号：US20150337224A1
公开(公告)日：2015-11-26
申请号：US14708369
申请日：2015-05-11
申请人： The Florida State University Research Foundation, Inc.
发明人： Albert E. Stiegman
IPC分类号： C10J3/02
CPC分类号： C10J3/02 , C10J2300/0903 , C10J2300/0916 , C10J2300/094 , C10J2300/0943 , C10J2300/0953 , C10J2300/0966 , C10J2300/0969 , C10J2300/0976 , C10J2300/123 , C10J2300/1853 , C10L3/08 , Y02P20/145
摘要： A method for the gasification of carbon to yield products including carbon monoxide, hydrogen, and methane. The method comprises irradiating a source of carbon with radiation having a frequency between 300 GHz and 300 MHz and contacting the source of carbon with a reactant such as water, carbon dioxide, hydrogen, and a nitrogen oxide. The choice of reactant dictates the resultant product.
摘要翻译：一种用于气化碳以产生包括一氧化碳，氢气和甲烷的产物的方法。该方法包括用频率在300GHz和300MHz之间的辐射照射碳源，并将碳源与诸如水，二氧化碳，氢气和氮氧化物的反应物接触。反应物的选择决定了所得产物。

3. 发明公开

US20230348803A1 SYNGAS/HYDROGEN PRODUCTION METHOD FROM BIOMASS FEED STOCK 审中-公开
公开(公告)号：US20230348803A1
公开(公告)日：2023-11-02
申请号：US18348383
申请日：2023-07-07
申请人： KING FAHD UNIVERSITY OF PETROLEUM AND MINERALS
发明人： Mohammad Mozahar HOSSAIN , Tareq Ali Salem AL-ATTAS
IPC分类号： C10J3/06 , C10J3/20 , C01B3/02
CPC分类号： C10J3/06 , C10J3/20 , C01B3/02 , C10J2300/0916 , C10J2300/092 , C10J2300/0953 , C10J2300/0956 , C10J2300/0969 , C10J2300/0906
摘要： The invention is directed to a co-gasification process that uses biomass and VGO as a feedstock to produce syngas which includes a mixture of carbon monoxide and hydrogen.

4. 发明申请

US20160002034A1 METHODS FOR FUEL CONVERSION 审中-公开
标题翻译：燃料转换方法
公开(公告)号：US20160002034A1
公开(公告)日：2016-01-07
申请号：US14766086
申请日：2014-02-05
申请人： OHIO STATE INNOVATION FOUNDATION
发明人： Liang-Shih Fan , Siwei Luo , Liang Zeng
IPC分类号： C01B3/34 , C10J3/57
CPC分类号： C01B3/344 , B01J8/12 , C01B2203/02 , C01B2203/0255 , C01B2203/1241 , C10J3/57 , C10J2300/0916 , C10J2300/093 , C10J2300/0953 , C10J2300/1807 , Y02E60/324 , Y02P20/134
摘要： In one embodiment described herein, fuel may be converted into syngas by a method comprising feeding the fuel and composite metal oxides into a reduction reactor in a co-current flow pattern relative to one another, reducing the composite metal oxides with the fuel to form syngas and reduced composite metal oxides, transporting the reduced composite metal oxides to an oxidation reactor, regenerating the composite metal oxides by oxidizing the reduced composite metal oxides with an oxidizing reactant in the oxidation reactor, and recycling the regenerated composite metal oxides to the reduction reactor for sub-sequent reduction reactions to produce syngas. The composite metal oxides may be solid particles comprising a primary metal oxide and a secondary metal oxide.
摘要翻译：在本文所述的一个实施方案中，燃料可以通过包括将燃料和复合金属氧化物相对于彼此以并流流动模式进入还原反应器的方法转化为合成气，用燃料还原复合金属氧化物以形成合成气和还原的复合金属氧化物，将还原的复合金属氧化物输送到氧化反应器，通过在氧化反应器中用氧化反应物氧化还原的复合金属氧化物，再生复合金属氧化物，并将再生的复合金属氧化物再循环到还原反应器中后续的还原反应产生合成气。复合金属氧化物可以是包含一次金属氧化物和二次金属氧化物的固体颗粒。

5. 发明申请

US20150298970A1 A METHOD AND ASSEMBLY FOR THE PRODUCTION OF HYDROGEN GAS 有权
标题翻译：用于生产氢气的方法和装置
公开(公告)号：US20150298970A1
公开(公告)日：2015-10-22
申请号：US14647227
申请日：2012-11-27
申请人： Real Time Engineering Pte Ltd.
发明人： Song Yeng WONG
IPC分类号： C01B3/08 , C10K1/04 , C10J3/20 , C10K1/00 , C10G2/00 , C10J3/06
CPC分类号： C01B3/08 , B01J38/60 , C07C1/04 , C07C1/0425 , C07C1/043 , C07C1/0435 , C10G2/32 , C10G2/332 , C10J3/06 , C10J3/18 , C10J3/20 , C10J3/26 , C10J3/82 , C10J2300/0916 , C10J2300/0953 , C10J2300/0983 , C10J2300/1238 , C10J2300/1646 , C10J2300/1659 , C10J2300/1807 , C10K1/007 , C10K1/04 , Y02E50/32 , Y02E60/36 , Y02P20/145
摘要： Provided is a process for producing hydrogen gas in a separate stream from syngas. An assembly for producing hydrogen gas in a separate stream from syngas and a method of producing hydrogen are also provided.
摘要翻译：提供了在与合成气分离的流中产生氢气的方法。还提供了一种用于从与合成气分离的流中产生氢气的组件和一种生产氢的方法。

6. 发明申请

US20170183585A1 GASIFICATION UNIT, INTEGRATED GASIFICATION COMBINED CYCLE FACILITY, AND METHOD FOR STARTING GASIFICATION UNIT 审中-公开
公开(公告)号：US20170183585A1
公开(公告)日：2017-06-29
申请号：US15312915
申请日：2015-07-02
申请人： MITSUBISHI HITACHI POWER SYSTEMS, LTD.
发明人： Shogo YOSHIDA , Yoshinori KOYAMA , Toshiyuki YAMASHITA
IPC分类号： C10J3/72 , F02C3/28 , F01K11/02 , F01K7/16 , F01K23/10 , F01D15/10 , F02C3/04 , F02C6/18
CPC分类号： C10J3/723 , C10J3/46 , C10J3/487 , C10J3/726 , C10J3/86 , C10J2300/093 , C10J2300/0953 , C10J2300/0956 , C10J2300/0959 , C10J2300/0969 , C10J2300/1223 , C10J2300/1653 , C10J2300/1678 , C10K1/024 , C10K1/026 , F01D15/10 , F01K7/16 , F01K11/02 , F01K23/067 , F01K23/10 , F02C3/04 , F02C3/28 , F02C6/18 , F05D2220/32 , F05D2220/72 , F05D2220/76 , F05D2240/35 , Y02E20/16 , Y02E20/18
摘要： There is provided coal gasification unit including: a coal gasifier; a char recovery unit; flare equipment; an air flow rate adjustment valve and an oxygen supply flow passage that supply oxygen-containing gas to the coal gasifier; an inert gas supply flow passage that supplies nitrogen gas to an upstream side of the char recovery unit; and a control unit that controls a supply amount of the oxygen-containing gas and a supply amount of the nitrogen gas, in which the coal gasifier has a starting burner, and in which the control unit controls the supply amount of the nitrogen gas prior to starting combustion of starting fuel by the starting burner so that an oxygen concentration of mixed gas in which combustion gas generated by combustion of the oxygen-containing gas and the starting fuel has been mixed with the nitrogen gas becomes not more than an ignition concentration.

7. 发明授权

US4322221A Process for the superatmospheric gasification of solid carbonaceous materials 失效
标题翻译：固体碳质材料超大气气化的工艺
公开(公告)号：US4322221A
公开(公告)日：1982-03-30
申请号：US180124
申请日：1980-08-21
申请人： John F. Kamody
发明人： John F. Kamody
IPC分类号： C10J3/46 , C10J3/00
CPC分类号： C10J3/466 , C10J3/506 , C10J3/78 , C10J3/84 , C10J2300/093 , C10J2300/0953 , C10J2300/0956 , C10J2300/0959 , C10J2300/0969 , C10J2300/0976 , C10J2300/1807 , Y10S48/02 , Y10S48/07
摘要： A process is disclosed for gasifying solid carbonaceous material at elevated temperature and pressure to produce a gas consisting of carbon monoxide and hydrogen, which comprises forming a slurry at atmospheric pressure of the carbonaceous material with a liquid having a specific gravity of from 1.1 to 1.9, a boiling temperature of at least 70.degree. F., a latent heat of vaporization less than about 200 BTU per pound, a critical temperature which is less than the incipient coking temperature of the carbonaceous material, a stability at temperatures up to 600.degree. F., an essentially inert chemical reaction with the carbonaceous material at temperatures less than about 600.degree. F., an immiscibility with water or solubility in water at no more than 5%, and a dissolving ability for hydrogen sulfide at temperatures of from -40 to 250.degree. F., and raising the formed slurry to a pressure of at least the gasification pressure and vaporizing said liquid and gasifying said carbonaceous material, either in the same or in separate steps. Examples of suitable slurrying liquids are: carbon tetrachloride, carbon disulfide, trichloroethylene, bromoethane, chlorobenzene, methane dichloride, chloroform, or mixtures thereof.
摘要翻译：公开了一种用于在升高的温度和压力下气化固体碳质材料以产生由一氧化碳和氢气组成的气体的方法，其包括在碳质材料的大气压下用比重为1.1至1.9的液体形成浆料，沸腾温度至少为70°F，蒸发潜热低于约200 BTU /磅，临界温度小于碳质材料的初始焦化温度，在高达600°F的温度下的稳定性。在低于约600°F的温度下与碳质材料发生基本上惰性的化学反应，与水的不混溶性或在水中的溶解度不超过5％，以及在-40至250℃的温度下硫化氢的溶解能力将所形成的浆料升至至少气化压力的压力并使所述液体蒸发并气化所述含碳材料，eithe r在相同或单独的步骤。合适的制浆液体的实例是：四氯化碳，二硫化碳，三氯乙烯，溴乙烷，氯苯，甲烷二氯化物，氯仿或其混合物。

8. 发明授权

US3904387A Fuel gas manufacture 失效
标题翻译：燃气生产
公开(公告)号：US3904387A
公开(公告)日：1975-09-09
申请号：US50081774
申请日：1974-08-26
申请人： BABCOCK & WILCOX CO
发明人： KERTAMUS NORBERT J , SAGE WARNIE L , PAISLEY MARK A
IPC分类号： C10J3/14 , C10J3/54 , C10J3/06
CPC分类号： C10J3/54 , C10J3/14 , C10J3/20 , C10J3/482 , C10J3/78 , C10J3/84 , C10J2300/0943 , C10J2300/0953 , C10J2300/0956 , C10J2300/0993 , C10J2300/1606 , C10J2300/1807
摘要： A process for gasifying char or coke with heated sulfur dioxide to produce a combustible fuel gas.
摘要翻译：用加热的二氧化硫气化焦炭或焦炭以产生可燃燃料气体的方法。

9. 发明授权

US11939547B2 Gasification of plastics and solid fossil fuels 有权
公开(公告)号：US11939547B2
公开(公告)日：2024-03-26
申请号：US17663684
申请日：2022-05-17
申请人： Eastman Chemical Company
发明人： William Lewis Trapp , Justin William Murphy , Nathan Mitchell West
IPC分类号： C10J3/48 , C10J3/00 , C10J3/46 , C10J3/50
CPC分类号： C10J3/485 , C10J3/002 , C10J3/466 , C10J3/506 , C10J2300/0906 , C10J2300/092 , C10J2300/0923 , C10J2300/093 , C10J2300/0943 , C10J2300/0946 , C10J2300/0953 , C10J2300/0959 , C10J2300/0973 , C10J2300/164 , C10J2300/1665 , C10J2300/1846 , Y02P20/143
摘要： Pre-ground plastics of small particle size not more than 2 mm are co-fed into a solid fossil fuel fed entrained flow partial oxidation gasifier. High solids concentrations in the feedstock stream can be obtained without significant impact on the feedstock stream stability and pumpability. A consistent quality of syngas can be continuously produced, including generation of carbon dioxide and a carbon monoxide/hydrogen ratio while stably operating the gasifier and avoiding the high tar generation of fluidized bed or fixed bed waste gasifiers and without impacting the operations of the gasifier. The subsequent syngas produced from this material can be used to produce a wide range of chemicals.

10. 发明授权

US11939546B2 Gasification of plastics and solid fossil fuels to produce organic compounds 有权
公开(公告)号：US11939546B2
公开(公告)日：2024-03-26
申请号：US17656044
申请日：2022-03-23
申请人： Eastman Chemical Company
发明人： William Lewis Trapp , Justin William Murphy , Nathan Mitchell West
IPC分类号： C10J3/48 , C10J3/00 , C10J3/46 , C10J3/50
CPC分类号： C10J3/485 , C10J3/002 , C10J3/466 , C10J3/506 , C10J2300/0906 , C10J2300/092 , C10J2300/0923 , C10J2300/093 , C10J2300/0943 , C10J2300/0946 , C10J2300/0953 , C10J2300/0959 , C10J2300/0973 , C10J2300/164 , C10J2300/1665 , C10J2300/1846 , Y02P20/143
摘要： Pre-ground plastics of small particle size not more than 2 mm are co-fed into a solid fossil fuel fed entrained flow partial oxidation gasifier. High solids concentrations in the feedstock stream can be obtained without significant impact on the feedstock stream stability and pumpability. A consistent quality of syngas can be continuously produced, including generation of carbon dioxide and a carbon monoxide/hydrogen ratio while stably operating the gasifier and avoiding the high tar generation of fluidized bed or fixed bed waste gasifiers and without impacting the operations of the gasifier. The subsequent syngas produced from this material can be used to produce a wide range of chemicals.

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