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序号	专利名	申请号	申请日	公开（公告）号	公开（公告）日	发明人
121	Acetic acid by carbonylation of methanol, the production method of the methyl acetate and acetic anhydride	JP376394	1994-01-18	JP2880060B2	1999-04-05	GEN SEICHIN; KAN SEIKAN; GO SHUNU; SHU GOSHIN

122	Coal gasification combined cycle power plant	JP17304289	1989-07-06	JP2578210B2	1997-02-05	OGAWA KIICHIRO; OOSAWA YASUKO; MYAKE JUNSUKE

123	Production method of carbon monoxide and hydrogen-containing gas	JP22392986	1986-09-24	JP2509192B2	1996-06-19	サンテンスベン; ベンテルラルス

124	JPS5946995B2 -	JP14181083	1983-08-02	JPS5946995B2	1984-11-16	KIISU ROBAATO WAIRUDO

125	JPS5756519B2 -	JP848073	1973-01-19	JPS5756519B2	1982-11-30

126	Method of removing hydrogen cyanide from gassy current	JP4184581	1981-03-24	JPS56144728A	1981-11-11	SHIRIRU TERISU

127	JPS53381B2 -	JP173072	1971-12-24	JPS53381B2	1978-01-07

128	PROCESSES FOR CONVERTING LIGNOCELLULOSICS TO REDUCED ACID PYROLYSIS OIL	PCT/US2012043066	2012-06-19	WO2013019328A3	2013-06-13	KOCAL JOSEPH A; BRANDVOLD TIMOTHY A
Processes for producing reduced acid lignocellulosic-derived pyrolysis oil are provided. In a process, lignocellulosic material is fed to a heating zone. A basic solid catalyst is delivered to the heating zone. The lignocellulosic material is pyrolyzed in the presence of the basic solid catalyst in the heating zone to create pyrolysis gases. The oxygen in the pyrolysis gases is catalytically converted to separable species in the heating zone. The pyrolysis gases are removed from the heating zone and are liquefied to form the reduced acid lignocellulosic-derived pyrolysis oil.
129	Production of fuel	US14900609	2014-06-17	US09834728B2	2017-12-05	Karen Fleckner; Michael Kraft Neylon
The present invention concerns the production and use of feedstock streams. Specifically, the present invention provides a process for the production of a commodity using two or more feedstock streams. Each feedstock stream is processed into a common intermediate and subsequently processed into a final product, such as electrical energy, a liquid fuel or a liquefied fuel, such as methanol, dimethyl ether, synthetic gasoline, diesel, kerosene, or jet fuel. The common intermediate may be synthetic gas (syngas), producer gas or pyrolysis gas.
130	Systems and methods for oxidation of synthesis gas tar	US14864590	2015-09-24	US09822318B2	2017-11-21	Herman Feldmann
A method is provided for removing tar from a gas by contacting a first gas containing tar with a second gas containing oxygen for time period sufficient to effect oxidation of at least a portion of the tar in the first gas, thus producing an oxidized product gas that contains less tar than the first gas. The method can also include heating a fluidized particulate material in a combustor, introducing the heated fluidized particulate material from the combustor and a biomass feedstock into a gasifier, such that heat from the heated fluidized particulate material causes the gasification of at least a portion of the biomass feedstock to form a tar-containing product gas, the first gas may contain at least a portion of the tar-containing gas, and the tar-containing gas may be extracted from the gasifier prior to contacting the first gas with the second gas.
131	Synthesis gas separation and reforming process	US14031182	2013-09-19	US09764277B2	2017-09-19	Richard Peter Glynn Jewell; Melissa Gaucher; Louis Denomme
A method of obtaining purified hydrogen and purified carbon monoxide from crude synthesis gas. A first crude synthesis gas stream is passed through a first separation zone to separate a hydrogen stream from a stream comprising carbon monoxide and methane. The carbon monoxide and methane are subjected to thermal reforming to produce a second crude synthesis gas, which is passed through a second separation zone to separate carbon monoxide from the second crude synthesis gas stream.
132	PRODUCTION OF DIMETHYL ETHER	US14900609	2014-06-17	US20160152899A1	2016-06-02	Karen Fleckner; Michael Kraft Neylon
The present invention concerns the production and use of feedstock streams. Specifically, the present invention provides a process for the production of a commodity using two or more feedstock streams. Each feedstock stream is processed into a common intermediate and subsequently processed into a final product, such as electrical energy, a liquid fuel or a liquefied fuel, such as methanol, dimethyl ether, synthetic gasoline, diesel, kerosene, or jet fuel. The common intermediate may be synthetic gas (syngas), producer gas or pyrolysis gas.
133	System for recovering high-purity CO2 from gasification gas containing CO, CO2, COS and H2S	US14019951	2013-09-06	US09278312B2	2016-03-08	Fumiaki Sato; Shinji Ogino; Motonari Aihara; Yudai Kato; Kazuo Ishida; Seiji Kakesako
A method and system for recovering CO2 from gasification gas, prevents the recovered CO2 from being contaminated with COS, without repeating cooling and heating operations and without increasing the steam consumption. Gasification gas being produced in a gasifier 10 and containing CO, CO2, COS and H2S is subjected to dust removal in a scrubber 20. Then, a part of the gas is subjected to a CO shift reaction, in which CO is converted into CO2, in a CO shift reactor 30. Another part of the gasification gas is not subjected to the CO shift reaction by means of a bypass 34, and is mixed with the gas after the CO shift reaction. Thereby, the temperature of the mixture gas is set at 180° C. to 300° C., and COS in the mixture gas is converted into H2S in a COS converter 40.
134	Systems and methods for oxidation of synthesis gas tar	US14575587	2014-12-18	US09193589B2	2015-11-24	Herman Feldmann
A method for removing tar from a gas by contacting a first gas containing tar with a second gas containing oxygen for time period sufficient to effect oxidation of at least a portion of the tar in the first gas, thus producing an oxidized product gas that contains less tar than the first gas.
135	Feed injector tip cap	US13830833	2013-03-14	US09022302B2	2015-05-05	Danielle Yarber Archangel
A system includes a gasification feed injector. The gasification feed injector includes a tip portion disposed at a fluid exit region of the gasification feed injector, and a tip cap coupled to the tip portion of the gasification feed injector and configured to serve as a thermal barrier for the tip portion during gasification reactions.
136	SYSTEMS AND METHODS FOR OXIDATION OF SYNTHESIS GAS TAR	US14575587	2014-12-18	US20150102263A1	2015-04-16	HERMAN FELDMANN
A method for removing tar from a gas by contacting a first gas containing tar with a second gas containing oxygen for time period sufficient to effect oxidation of at least a portion of the tar in the first gas, thus producing an oxidized product gas that contains less tar than the first gas.
137	Method and apparatus for treating a syngas	US13369018	2012-02-08	US08974555B2	2015-03-10	Alice Fourcault; Jean-Paul Robert-Arnouil; Erika Edme
Treating a synthesis gas includes generating a plasma jet from a non-transferred arc torch having a main axis, the jet having a propagation axis substantially collinear with the torch main axis. The plasma torch is mounted on a feed enclosure. The syngas is received at an inlet port of the feed enclosure, downstream from the plasma torch and feeding the syngas so the flow encounters the plasma jet to mix the syngas and plasma jet in a distribution chamber. The mixture is propagated in a reactor downstream from the feed enclosure to convert the syngas into an outlet gas. The reactor is in communication in its upstream portion with the feed enclosure through a flared segment, and has a longitudinal axis that is substantially collinear with the propagation axis of the plasma jet. The outlet gas is extracted via an outlet port and particles are captured by a submerged conveyor.
138	Systems and methods for oxidation of synthesis gas tar	US13293512	2011-11-10	US08969637B2	2015-03-03	Herman Feldmann
A process of gasification and the production of synthesis gas. A process of biomass gasification and the reduction or elimination of tars from the hydrocarbon-rich product gas derived from biomass gasification. Systems and methods for the reduction of tar from a synthesis gas derived from biomass gasification are provided.
139	Processes for converting lignocellulosics to reduced acid pyrolysis oil	US13194718	2011-07-29	US08927793B2	2015-01-06	Joseph Anthony Kocal; Timothy A. Brandvold
Processes for producing reduced acid lignocellulosic-derived pyrolysis oil are provided. In a process, lignocellulosic material is fed to a heating zone. A basic solid catalyst is delivered to the heating zone. The lignocellulosic material is pyrolyzed in the presence of the basic solid catalyst in the heating zone to create pyrolysis gases. The oxygen in the pyrolysis gases is catalytically converted to separable species in the heating zone. The pyrolysis gases are removed from the heating zone and are liquefied to form the reduced acid lignocellulosic-derived pyrolysis oil.
140	FEED INJECTOR TIP CAP	US13830833	2013-03-14	US20140263746A1	2014-09-18	Danielle Yarber Archangel
A system includes a gasification feed injector. The gasification feed injector includes a tip portion disposed at a fluid exit region of the gasification feed injector, and a tip cap coupled to the tip portion of the gasification feed injector and configured to serve as a thermal barrier for the tip portion during gasification reactions.

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