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公开(公告)号:US20120024843A1
公开(公告)日:2012-02-02
申请号:US12847672
申请日:2010-07-30
IPC分类号: H05B6/64
摘要: A method of treating a carbonaceous material is disclosed. The method includes heating the carbonaceous material in a reactor with microwave energy, at a pressure less than about 5 atmospheres, to generate a mixture comprising char, oil and gas.
摘要翻译: 公开了一种处理含碳材料的方法。 该方法包括在小于约5个大气压的压力下用微波能量在反应器中加热含碳材料,以产生包含焦炭,油和气体的混合物。
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公开(公告)号:US20080134666A1
公开(公告)日:2008-06-12
申请号:US11609109
申请日:2006-12-11
IPC分类号: F01B23/00
CPC分类号: F23C99/00 , C01B3/12 , C01B3/50 , C01B3/52 , C01B3/56 , C01B13/0229 , C01B2203/0283 , C01B2203/0415 , C01B2203/043 , C01B2203/0475 , C01B2203/0485 , C01B2203/147 , C01B2203/84 , C01B2210/0046 , C10J3/482 , C10J3/725 , C10J2300/093 , C10J2300/0956 , C10J2300/0973 , C10J2300/1606 , C10J2300/1637 , C10J2300/165 , C10J2300/1675 , C10J2300/1678 , C10J2300/1807 , C10J2300/1853 , F23C10/00 , F23C2900/99008 , Y02E20/16 , Y02E20/18 , Y02E20/346 , Y02P20/13
摘要: Disclosed herein are systems and method for using unmixed fuel processors. In one embodiment, a system for using an unmixed fuel processor comprises: an unmixed fuel processor and a power generating unit. The unmixed fuel processor comprises: a gasification reactor, an oxidation reactor and a regeneration reactor. The gasification reactor comprises a CO2 sorbent material. The oxidation reactor comprises an oxygen transfer material. The regeneration reactor is configured to receive spent CO2 sorbent material from the gasification reactor and to return regenerated CO2 sorbent material to the gasification reactor, and configured to receive oxidized oxygen transfer material from the oxidation reactor and to return reduced oxygen transfer material to the oxidation reactor. The power generating unit configured to receive an oxygen depleted stream from the oxidation reactor and to produce electricity.
摘要翻译: 本文公开了用于使用未混合燃料处理器的系统和方法。 在一个实施例中,一种用于使用未混合燃料处理器的系统包括:未混合燃料处理器和发电单元。 未混合的燃料处理器包括:气化反应器,氧化反应器和再生反应器。 气化反应器包括CO 2吸附剂材料。 氧化反应器包括氧转移材料。 再生反应器被配置为从气化反应器接收废CO 2吸附剂材料并将再生的CO 2吸附剂材料返回到气化反应器,并且被配置为接收氧化的氧转移 来自氧化反应器的材料并将还原的氧转移材料返回到氧化反应器。 所述发电单元被配置为接收来自所述氧化反应器的贫氧流并产生电力。
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