公开(公告)号：US20110085967A1

公开(公告)日：2011-04-14

申请号：US12578661

申请日：2009-10-14

申请人： Troy Michael Raybold ,  Gregory Joseph Panuccio ,  Jerome Thomas Jankowiak ,  Vasilis Papavassiliou ,  Raymond Francis Drnevich

发明人： Troy Michael Raybold ,  Gregory Joseph Panuccio ,  Jerome Thomas Jankowiak ,  Vasilis Papavassiliou ,  Raymond Francis Drnevich

IPC分类号： C01B3/26 ,  B01J10/00

CPC分类号： C01B3/382 ,  C01B3/384 ,  C01B3/48 ,  C01B3/56 ,  C01B2203/0233 ,  C01B2203/0244 ,  C01B2203/0283 ,  C01B2203/0288 ,  C01B2203/0294 ,  C01B2203/0415 ,  C01B2203/043 ,  C01B2203/0445 ,  C01B2203/0475 ,  C01B2203/0816 ,  C01B2203/0822 ,  C01B2203/0827 ,  C01B2203/0838 ,  C01B2203/0866 ,  C01B2203/0883 ,  C01B2203/0894 ,  C01B2203/1023 ,  C01B2203/1047 ,  C01B2203/1052 ,  C01B2203/1058 ,  C01B2203/1064 ,  C01B2203/107 ,  C01B2203/1235 ,  C01B2203/1241 ,  C01B2203/1258 ,  C01B2203/1294 ,  C01B2203/141 ,  C01B2203/142 ,  C01B2203/1604 ,  C01B2203/1619 ,  C01B2203/169 ,  Y02P20/128

摘要： A method and apparatus for producing a hydrogen containing product in which hydrocarbon containing feed gas streams are reacted in a steam methane reformer of an existing hydrogen plant and a catalytic reactor that reacts hydrocarbons, oxygen and steam. The catalytic reactor is a retrofit to the existing hydrogen plant to increase hydrogen production. The resulting synthesis gas streams are combined, cooled, subjected to water-gas shift and then introduced into a production apparatus that can be a pressure swing adsorption unit. The amount of synthesis gas contained in a shifted stream made available to the production apparatus is increased by virtue of the combination of the synthesis gas streams to increase production of the hydrogen containing product. The catalytic reactor is operated such that the synthesis gas stream produced by such reactor is similar to that produced by the steam methane reformer and at a temperature that will reduce oxygen consumption within the catalytic reactor.

摘要翻译： 一种生产含氢产物的方法和装置，其中含烃原料气流在现有氢气厂的蒸汽甲烷重整器和反应烃，氧气和蒸汽的催化反应器中反应。 催化反应器是对现有氢气厂的改造，以增加氢的产生。 将所得合成气流合并，冷却，进行水煤气变换，然后导入可以是变压吸附单元的生产装置中。 通过合成气流的组合来提高可用于制备装置的转移流中包含的合成气的量，以增加含氢产物的产生。 操作催化反应器使得由这种反应器产生的合成气流类似于由蒸汽甲烷重整器产生的合成气流，并且在降低催化反应器内的氧消耗的温度下。

公开(公告)号：US20120041242A1

公开(公告)日：2012-02-16

申请号：US12855408

申请日：2010-08-12

申请人： Gregory Joseph Panuccio ,  Vasilis Papavassiliou ,  Raymond Francis Drnevich

发明人： Gregory Joseph Panuccio ,  Vasilis Papavassiliou ,  Raymond Francis Drnevich

IPC分类号： C07C5/02 ,  B01J19/00

CPC分类号： C10L3/08 ,  C10G70/02 ,  C10G2300/1025 ,  C10G2300/1092 ,  C10G2300/4006 ,  C10G2300/4081 ,  C10G2300/807 ,  C10G2400/28

摘要： A method and apparatus for producing a substitute natural gas stream to be added to a natural gas stream in which at least part of a refinery gas stream is reacted in a catalytic reactor to hydrogenate olefins into saturated hydrocarbons. The extent to which hydrogen and olefins are reacted in the catalytic reactor is controlled to reduce the concentration of olefins in the resulting substitute natural gas stream and to increase the interchangeability of the substitute natural gas stream with the natural gas. This control can be effectuated by by-passing part of the refinery off gas to an intermediate product stream produced by the catalytic reactor and thereby forming the substitute natural gas stream from the by-passed refinery gas stream and the intermediate product stream.

摘要翻译： 一种用于生产待添加到天然气流中的替代天然气流的方法和装置，其中至少部分炼油气流在催化反应器中反应以将烯烃氢化成饱和烃。 控制氢和烯烃在催化反应器中反应的程度以降低所得替代天然气流中烯烃的浓度，并增加替代天然气流与天然气的互换性。 可以通过将炼厂废气的一部分旁通至由催化反应器产生的中间产物流，从而形成来自旁路炼油厂气流和中间产物流的替代天然气流来实现该控制。

公开(公告)号：US09680350B2

公开(公告)日：2017-06-13

申请号：US14119087

申请日：2012-05-23

申请人： Gregory Joseph Panuccio ,  Raymond Francis Drnevich ,  Minish Mahendra Shah

发明人： Gregory Joseph Panuccio ,  Raymond Francis Drnevich ,  Minish Mahendra Shah

IPC分类号： F02C1/00 ,  H02K7/18 ,  F25J3/04 ,  F02C6/06 ,  F02C6/18 ,  F02C3/30 ,  F02C3/20

CPC分类号： H02K7/1823 ,  F02C3/20 ,  F02C3/30 ,  F02C6/06 ,  F02C6/18 ,  F25J3/046 ,  F25J3/04836 ,  F25J3/04842 ,  F25J2240/70 ,  F25J2240/82

摘要： The present invention provides a method and apparatus for separating air and generating electrical power. A compressed air stream produced in a main air compressor is introduced into an air separation unit that cryogenically rectifies the air into component products. During turndown conditions of the air separation unit, a combustion air stream formed from all or part of the compressed air stream is introduced into a combustor in which a fuel is combusted to produce a heated and pressurized combustion stream. Such stream is introduced to a turbine connected to an electrical generator to generate electrical power. The combustion air stream can be saturated with moisture to increase power output. Further, the combustion air stream can also be preheated with an exhaust of a gas turbine.