-
21.发明授权
公开(公告)号：US3232861A
公开(公告)日：1966-02-01
申请号：US21876962
申请日：1962-08-22
发明人： EVERETT GORIN , STRUCK ROBERT T , ZICLKE CLYDE W
-
公开(公告)号：US1993316A
公开(公告)日：1935-03-05
申请号：US1993316D
IPC分类号： C10B57/18
CPC分类号： C10B57/18 , Y10S261/17
-
-
-
-
-
公开(公告)号：US20220081620A1
公开(公告)日：2022-03-17
申请号：US17357504
申请日：2021-06-24
IPC分类号： C10B53/02 , C10G1/02 , C10C5/00 , C10G1/10 , C10G3/00 , C10L1/02 , C10B53/00 , C10K3/02 , C10B57/18 , C10B53/07 , C10B57/12
摘要： A method for producing a pyrolysis oil is described. In said method, a feedstock to be treated is first pyrolyzed in a pyrolysis zone, in which the feedstock is heated to a temperature of 250 degrees Celsius to 700 degrees Celsius; and pyrolyzed solids and pyrolysis vapors are formed. The pyrolysis vapors are then reformed at a temperature of 450 degrees Celsius to 1,200 degrees Celsius in a post-conditioning zone, in which the pyrolysis vapors are brought into contact with a catalyst bed, wherein the pyrolysis oil is formed. In this case, the catalyst comprises a pyrolyzed solid, which can be obtained according to the pyrolysis, described above. Finally the pyrolysis oil is separated from the additional pyrolysis products, which are formed, in a separation unit.
-
公开(公告)号：US11066604B2
公开(公告)日：2021-07-20
申请号：US15684448
申请日：2017-08-23
IPC分类号： C10B53/02 , C10G3/00 , C10G1/02 , C10C5/00 , C10G1/10 , C10L1/02 , C10B53/00 , C10K3/02 , C10B57/18 , C10B53/07 , C10B57/12
摘要： A method for producing a pyrolysis oil is described. In said method, a feedstock to be treated is first pyrolyzed in a pyrolysis zone, in which the feedstock is heated to a temperature of 250 degrees Celsius to 700 degrees Celsius; and pyrolyzed solids and pyrolysis vapors are formed. The pyrolysis vapors are then reformed at a temperature of 450 degrees Celsius to 1,200 degrees Celsius in a post-conditioning zone, in which the pyrolysis vapors are brought into contact with a catalyst bed, wherein the pyrolysis oil is formed. In this case, the catalyst comprises a pyrolyzed solid, which can be obtained according to the pyrolysis, described above. Finally the pyrolysis oil is separated from the additional pyrolysis products, which are formed, in a separation unit.
-
公开(公告)号：US20210024829A1
公开(公告)日：2021-01-28
申请号：US16940190
申请日：2020-07-27
IPC分类号： C10B57/18 , B01J27/19 , B01J27/199 , B01J27/188 , C10G3/00 , C10B53/02 , B01D53/86
摘要： The present disclosure relates to a device that includes a filter element and a catalyst, where the filter element is configured to remove particulate from a stream that includes at least one of a gas and/or a vapor to form a filtered stream of the gas and/or the vapor, the catalyst is configured to receive the filtered stream and react a compound in the filtered stream to form an upgraded stream of the gas and/or the vapor, further including an upgraded compound, and both the filter element and the catalyst are configured to be substantially stable at temperatures up to about 500° C.
-
公开(公告)号：US10273411B2
公开(公告)日：2019-04-30
申请号：US15309707
申请日：2015-05-07
申请人： Academia Sinica , Frank H. Shu
发明人： Frank H. Shu , Fen-Tair Luo , Michael J. Cai
摘要： A compact, transportable batch-process supertorrefaction system includes at least one supertorrefying unit, a liquid tank containing molten salt, and a wash tank including a plurality of basins containing water having different temperatures and different salinity. The liquid tank and the wash tank sequentially supply the molten salt and the water to a receiving space of the at least one supertorrefying unit to supertorrefy the biomass into charcoal and to rinse and cool the charcoal, respectively. The plurality of basins of the wash tank sequentially supply water having different temperatures and salinity to the same receiving space to gradually rinse and cool the charcoal. The biomass is not moved in the at least one supertorrfeying unit during biomass supertorrefaction. The charcoal is not moved during charcoal cooling.
-
-
-
-
-
-
-
-
-
搜索结果
90 条记录 (耗时 0.015 秒)
