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公开(公告)号：US20100076235A1
公开(公告)日：2010-03-25
申请号：US12562925
申请日：2009-09-18
IPC分类号： C07C1/04
CPC分类号： C10J3/00 , C01B3/586 , C01B2203/0445 , C01B2203/047 , C10J3/482 , C10J2300/093 , C10J2300/0956 , C10J2300/0959 , C10J2300/0973 , C10J2300/0986 , C10J2300/1662 , C10J2300/1671 , C10J2300/1675 , C10J2300/1687 , C10J2300/1807 , C10J2300/1884 , C10K3/04 , C10L3/08
摘要： The present invention relates to processes for preparing gaseous products, and in particular, methane via the catalytic gasification of carbonaceous feedstocks in the presence of steam and an oxygen-rich gas stream. The processes comprise using at least one catalytic methanator to convert carbon monoxide and hydrogen in the gaseous products to methane and do not recycle carbon monoxide or hydrogen to the catalytic gasifier.
摘要翻译： 本发明涉及通过在蒸汽和富氧气流的存在下通过碳质原料的催化气化来制备气态产物，特别是甲烷的方法。 该方法包括使用至少一种催化甲烷化器将气态产物中的一氧化碳和氢气转化成甲烷，并且不将一氧化碳或氢气循环到催化气化器中。
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公开(公告)号：US08328890B2
公开(公告)日：2012-12-11
申请号：US12562925
申请日：2009-09-18
CPC分类号： C10J3/00 , C01B3/586 , C01B2203/0445 , C01B2203/047 , C10J3/482 , C10J2300/093 , C10J2300/0956 , C10J2300/0959 , C10J2300/0973 , C10J2300/0986 , C10J2300/1662 , C10J2300/1671 , C10J2300/1675 , C10J2300/1687 , C10J2300/1807 , C10J2300/1884 , C10K3/04 , C10L3/08
摘要： The present invention relates to processes for preparing gaseous products, and in particular, methane via the catalytic gasification of carbonaceous feedstocks in the presence of steam and an oxygen-rich gas stream. The processes comprise using at least one catalytic methanator to convert carbon monoxide and hydrogen in the gaseous products to methane and do not recycle carbon monoxide or hydrogen to the catalytic gasifier.
摘要翻译： 本发明涉及通过在蒸汽和富氧气流的存在下通过碳质原料的催化气化来制备气态产物，特别是甲烷的方法。 该方法包括使用至少一种催化甲烷化器将气态产物中的一氧化碳和氢气转化成甲烷，并且不将一氧化碳或氢气循环到催化气化器中。
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公开(公告)号：US20100287835A1
公开(公告)日：2010-11-18
申请号：US12778552
申请日：2010-05-12
IPC分类号： C01B3/32
CPC分类号： C10J3/00 , C01B3/36 , C01B3/48 , C01B3/50 , C01B32/40 , C01B32/50 , C01B2203/0465 , C01B2203/047 , C01B2203/0475 , C01B2203/0485 , C01B2203/86 , C10J3/86 , C10J2300/093 , C10J2300/0959 , C10J2300/0973 , C10J2300/0986 , C10J2300/1618 , C10J2300/1662 , C10J2300/1687 , C10J2300/1838 , C10J2300/1884 , C10J2300/1892 , C10K1/002 , C10K1/004 , C10K1/005 , C10K1/006 , C10K1/007 , C10K1/026 , C10K1/08 , C10K1/101 , C10K1/122 , C10K1/143 , C10K1/146 , C10K1/165 , C10K3/04 , C10L3/08 , Y02P30/30
摘要： The present invention relates to processes for preparing gaseous products, and in particular methane, via the hydromethanation of a carbonaceous feedstock in the presence of steam, syngas, a hydromethanation catalyst and an oxygen-rich gas stream.
摘要翻译： 本发明涉及通过在蒸汽，合成气，氢化甲烷化催化剂和富氧气流的存在下，通过含碳原料的氢化反应来制备气态产物，特别是甲烷的方法。
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14.发明授权
公开(公告)号：US5466857A
公开(公告)日：1995-11-14
申请号：US288118
申请日：1994-08-10
IPC分类号： B01J8/24 , B01J12/02 , C01C3/02 , C07C253/24 , C07C253/26 , C07C253/34 , C07C255/08 , C07C253/18
CPC分类号： C07C253/24 , C07C253/26 , Y02P20/52
摘要： A process for the reduction in the amount of waste material generated during the manufacture of acrylonitrile comprising introducing an additional amount of oxygen containing gas, preferably air, in the substantial absence of any oxygenate compounds, into the upper portion of the fluid bed reactor to react with at least some of the unreacted ammonia to reduce the amount of unreacted ammonia present in the reactor effluent.
摘要翻译： 一种减少在制造丙烯腈期间产生的废料量的方法，包括在基本没有任何含氧化合物的情况下将额外量的含氧气体（优选空气）引入流化床反应器的上部以进行反应 与至少一些未反应的氨以减少反应器流出物中存在的未反应的氨的量。
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15.发明授权
公开(公告)号：US5288473A
公开(公告)日：1994-02-22
申请号：US959237
申请日：1992-10-09
申请人： Wilfrid G. Shaw , Kenneth L. Bigler , Louis R. Trott , Steve J. Miko , Vincent G. Reiling , Michael J. Seely , Dev D. Suresh , Maria S. Friedrich , Paul E. Bott , Edward J. Sockell , Albert R. Shuki, Jr. , Kenneth P. Keckler , Frank J. Kojancic
发明人： Wilfrid G. Shaw , Kenneth L. Bigler , Louis R. Trott , Steve J. Miko , Vincent G. Reiling , Michael J. Seely , Dev D. Suresh , Maria S. Friedrich , Paul E. Bott , Edward J. Sockell , Albert R. Shuki, Jr. , Kenneth P. Keckler , Frank J. Kojancic
IPC分类号： B01D53/58 , C07C253/24 , C07C253/26 , C07C255/00 , C01C3/00
CPC分类号： B01D53/58 , C07C253/26
摘要： A process for the substantial or complete elimination of ammonium sulfate generated during the production of acrylonitrile by the direct ammoxidation of propylene/propane, ammonia and an oxygen containing gas (e.g. air) over a fluid bed catalyst wherein the improvement comprises introducing an organic compound(s) into said reactor at a location where the compound(s) reacts with substantially all of the excess ammonia without affecting the acrylonitrile yield. Preferably, the organic compound is methanol which is introduced into the reactor at below its coking temperature.
摘要翻译： 通过丙烯/丙烷，氨和含氧气体（例如空气）在流化床催化剂上的直接氨氧化生产丙烯腈期间产生的硫酸铵的实质或完全消除的方法，其中改进包括引入有机化合物 s）在化合物与基本上所有过量的氨反应而不影响丙烯腈产率的位置处于所述反应器中。 优选地，有机化合物是在低于其焦化温度下被引入反应器中的甲醇。
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16.发明授权
公开(公告)号：US5457223A
公开(公告)日：1995-10-10
申请号：US104752
申请日：1993-08-11
申请人： Wilfrid G. Shaw , Kenneth L. Bigler , Louis R. Trott , Steve J. Miko , Vincent G. Reiling , Michael J. Seely , Dev D. Suresh , Maria S. Friedrich , Paul E. Bott , Edward J. Sockell , Albert R. Shuki, Jr. , Kenneth P. Keckler , Frank J. Kocjancic , Steven J. Rowe
发明人： Wilfrid G. Shaw , Kenneth L. Bigler , Louis R. Trott , Steve J. Miko , Vincent G. Reiling , Michael J. Seely , Dev D. Suresh , Maria S. Friedrich , Paul E. Bott , Edward J. Sockell , Albert R. Shuki, Jr. , Kenneth P. Keckler , Frank J. Kocjancic , Steven J. Rowe
IPC分类号： B01J23/88 , B01D53/58 , C01C3/02 , C07B61/00 , C07C5/08 , C07C253/24 , C07C253/26 , C07C253/32 , C07C255/00 , C07C255/08 , C07C253/34
CPC分类号： B01D53/58 , C07C253/26 , Y02P20/52
摘要： A process for the substantial or complete elimination of ammonium sulfate generated during the production of acrylonitrile by the direct ammoxidation of propylene/propane, ammonia and an oxygen containing gas (e.g. air) over a fluid bed catalyst wherein the improvement comprises introducing methanol into said reactor in the upper portion of the reactor at a location where the methanol reacts with at least a portion if not substantially all of the excess ammonia without affecting the acrylonitrile yield. Preferably, methanol is introduced into the reactor at below its coking temperature. In particular, when an oxygen lean fluid bed catalyst is utilized, an additional oxygen containing gas is introduced into the reaction at a distance between about 8 to 14 inches from the methanol feed location.
摘要翻译： 通过在流化床催化剂上丙烯/丙烷，氨和含氧气体（例如空气）的直接氨氧化在生产丙烯腈期间实质上或完全消除硫酸铵的方法，其中改进包括将甲醇引入所述反应器 在反应器的上部，其中甲醇与至少一部分（如果基本上不全部）过量氨反应而不影响丙烯腈产率的位置。 优选地，在低于其焦化温度下将甲醇引入反应器中。 特别地，当使用贫氧流化床催化剂时，将额外的含氧气体以距甲醇进料位置约8至14英寸的距离引入反应中。
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