公开(公告)号：US07846413B2

公开(公告)日：2010-12-07

申请号：US11946747

申请日：2007-11-28

申请人： Lloyd Anthony Clomburg, Jr. ,  Andreas Nicholas Matzakos ,  Peter Veenstra ,  Scott Lee Wellington

发明人： Lloyd Anthony Clomburg, Jr. ,  Andreas Nicholas Matzakos ,  Peter Veenstra ,  Scott Lee Wellington

IPC分类号： C01B31/20 ,  C01B3/24 ,  C01B3/26 ,  C01B3/16

CPC分类号： C01B3/384 ,  B01J8/0285 ,  B01J2208/00274 ,  B01J2208/00504 ,  B01J2219/00006 ,  C01B3/382 ,  C01B3/48 ,  C01B3/501 ,  C01B3/56 ,  C01B2203/0233 ,  C01B2203/0288 ,  C01B2203/0294 ,  C01B2203/0405 ,  C01B2203/041 ,  C01B2203/043 ,  C01B2203/047 ,  C01B2203/0475 ,  C01B2203/048 ,  C01B2203/0495 ,  C01B2203/0811 ,  C01B2203/0883 ,  C01B2203/1041 ,  C01B2203/1047 ,  C01B2203/1058 ,  C01B2203/1076 ,  C01B2203/1241 ,  C01B2203/1294 ,  C01B2203/142 ,  C01B2203/146 ,  C01B2203/148 ,  C01B2203/1623 ,  C01B2203/82

摘要： A process and a system are provided for producing and separating hydrogen and carbon dioxide from a hydrocarbon and steam. A hydrocarbon and steam are steam reformed and the reformed gas is shift reacted to produce a shift gas. Hydrogen is removed from the shift gas, and the hydrogen-depleted gas is reformed and shift reacted again to produce more hydrogen and carbon dioxide. The hydrogen and carbon dioxide are then separated.

摘要翻译： 提供了用于从烃和蒸汽中生产和分离氢气和二氧化碳的方法和系统。 将烃和蒸汽进行蒸汽重整，重整气体发生反应以产生换档气体。 从移动气体中除去氢气，并且将贫氢气体重整并再次反应以产生更多的氢气和二氧化碳。 然后分离氢气和二氧化碳。

公开(公告)号：US08088185B2

公开(公告)日：2012-01-03

申请号：US12939014

申请日：2010-11-03

申请人： Lloyd Anthony Clomburg, Jr. ,  Andreas Nicholas Matzakos ,  Peter Veenstra ,  Scott Lee Wellington

发明人： Lloyd Anthony Clomburg, Jr. ,  Andreas Nicholas Matzakos ,  Peter Veenstra ,  Scott Lee Wellington

IPC分类号： B01J8/00

CPC分类号： C01B3/384 ,  B01J8/0285 ,  B01J2208/00274 ,  B01J2208/00504 ,  B01J2219/00006 ,  C01B3/382 ,  C01B3/48 ,  C01B3/501 ,  C01B3/56 ,  C01B2203/0233 ,  C01B2203/0288 ,  C01B2203/0294 ,  C01B2203/0405 ,  C01B2203/041 ,  C01B2203/043 ,  C01B2203/047 ,  C01B2203/0475 ,  C01B2203/048 ,  C01B2203/0495 ,  C01B2203/0811 ,  C01B2203/0883 ,  C01B2203/1041 ,  C01B2203/1047 ,  C01B2203/1058 ,  C01B2203/1076 ,  C01B2203/1241 ,  C01B2203/1294 ,  C01B2203/142 ,  C01B2203/146 ,  C01B2203/148 ,  C01B2203/1623 ,  C01B2203/82

摘要： A system is provided for producing and separating hydrogen and carbon dioxide from a hydrocarbon and steam. A hydrocarbon and steam are steam reformed and the reformed gas is shift reacted to produce a shift gas in the system. Hydrogen is removed from the shift gas, and the hydrogen-depleted gas is reformed and shift reacted again to produce more hydrogen and carbon dioxide in the system. The hydrogen and carbon dioxide are then separated.

摘要翻译： 提供一种用于从烃和蒸汽中生产和分离氢气和二氧化碳的系统。 蒸汽重整碳氢化合物和蒸汽，并且重整气体被移动反应以在系统中产生换档气体。 从移动气体中除去氢气，并且将贫氢气体重整并再次反应以在系统中产生更多的氢和二氧化碳。 然后分离氢气和二氧化碳。

公开(公告)号：US20110044861A1

公开(公告)日：2011-02-24

申请号：US12939014

申请日：2010-11-03

申请人： Lloyd Anthony CLOMBURG, JR. ,  Andreas Nicholas Matzakos ,  Peter Veenstra ,  Scott Lee Wellington

发明人： Lloyd Anthony CLOMBURG, JR. ,  Andreas Nicholas Matzakos ,  Peter Veenstra ,  Scott Lee Wellington

IPC分类号： B01J8/00

CPC分类号： C01B3/384 ,  B01J8/0285 ,  B01J2208/00274 ,  B01J2208/00504 ,  B01J2219/00006 ,  C01B3/382 ,  C01B3/48 ,  C01B3/501 ,  C01B3/56 ,  C01B2203/0233 ,  C01B2203/0288 ,  C01B2203/0294 ,  C01B2203/0405 ,  C01B2203/041 ,  C01B2203/043 ,  C01B2203/047 ,  C01B2203/0475 ,  C01B2203/048 ,  C01B2203/0495 ,  C01B2203/0811 ,  C01B2203/0883 ,  C01B2203/1041 ,  C01B2203/1047 ,  C01B2203/1058 ,  C01B2203/1076 ,  C01B2203/1241 ,  C01B2203/1294 ,  C01B2203/142 ,  C01B2203/146 ,  C01B2203/148 ,  C01B2203/1623 ,  C01B2203/82

摘要： A system is provided for producing and separating hydrogen and carbon dioxide from a hydrocarbon and steam. A hydrocarbon and steam are steam reformed and the reformed gas is shift reacted to produce a shift gas in the system. Hydrogen is removed from the shift gas, and the hydrogen-depleted gas is reformed and shift reacted again to produce more hydrogen and carbon dioxide in the system. The hydrogen and carbon dioxide are then separated.

摘要翻译： 提供一种用于从烃和蒸汽中生产和分离氢气和二氧化碳的系统。 蒸汽重整碳氢化合物和蒸汽，并且重整气体被移动反应以在系统中产生换档气体。 从移动气体中除去氢气，并且将贫氢气体重整并再次反应以在系统中产生更多的氢和二氧化碳。 然后分离氢气和二氧化碳。

公开(公告)号：US20080179569A1

公开(公告)日：2008-07-31

申请号：US11946747

申请日：2007-11-28

申请人： Lloyd Anthony CLOMBURG ,  Andreas Nicholas Matzakos ,  Peter Veenstra ,  Scott Lee Wellington

发明人： Lloyd Anthony CLOMBURG ,  Andreas Nicholas Matzakos ,  Peter Veenstra ,  Scott Lee Wellington

IPC分类号： C01B3/38 ,  B01J7/00

CPC分类号： C01B3/384 ,  B01J8/0285 ,  B01J2208/00274 ,  B01J2208/00504 ,  B01J2219/00006 ,  C01B3/382 ,  C01B3/48 ,  C01B3/501 ,  C01B3/56 ,  C01B2203/0233 ,  C01B2203/0288 ,  C01B2203/0294 ,  C01B2203/0405 ,  C01B2203/041 ,  C01B2203/043 ,  C01B2203/047 ,  C01B2203/0475 ,  C01B2203/048 ,  C01B2203/0495 ,  C01B2203/0811 ,  C01B2203/0883 ,  C01B2203/1041 ,  C01B2203/1047 ,  C01B2203/1058 ,  C01B2203/1076 ,  C01B2203/1241 ,  C01B2203/1294 ,  C01B2203/142 ,  C01B2203/146 ,  C01B2203/148 ,  C01B2203/1623 ,  C01B2203/82

摘要： A process and a system are provided for producing and separating hydrogen and carbon dioxide from a hydrocarbon and steam. A hydrocarbon and steam are steam reformed and the reformed gas is shift reacted to produce a shift gas. Hydrogen is removed from the shift gas, and the hydrogen-depleted gas is reformed and shift reacted again to produce more hydrogen and carbon dioxide. The hydrogen and carbon dioxide are then separated.

摘要翻译： 提供了用于从烃和蒸汽中生产和分离氢气和二氧化碳的方法和系统。 将烃和蒸汽进行蒸汽重整，重整气体发生反应以产生换档气体。 从移动气体中除去氢气，并且将贫氢气体重整并再次反应以产生更多的氢气和二氧化碳。 然后分离氢气和二氧化碳。

公开(公告)号：US07063145B2

公开(公告)日：2006-06-20

申请号：US10279292

申请日：2002-10-24

申请人： Peter Veenstra ,  Eric Pierre de Rouffignac ,  John Michael Karanikas ,  Harold J. Vinegar ,  Scott Lee Wellington

发明人： Peter Veenstra ,  Eric Pierre de Rouffignac ,  John Michael Karanikas ,  Harold J. Vinegar ,  Scott Lee Wellington

IPC分类号： E21B7/04 ,  E21B36/02 ,  E21B43/24 ,  E21B47/022

CPC分类号： E21B43/2401 ,  B09C1/02 ,  B09C1/06 ,  B09C2101/00 ,  C10G9/24 ,  C10G45/00 ,  E21B17/028 ,  E21B43/168 ,  E21B43/24 ,  E21B43/243 ,  E21B43/305 ,  E21B47/02208 ,  G01V3/26 ,  Y02P30/30 ,  Y02P30/44 ,  Y10S210/901 ,  Y10T137/0391

摘要： In an embodiment, a method for heating a hydrocarbon containing formation may include providing heat from one or more heaters to an opening in the formation. A first end of the opening may contact the earth's surface at a first location and a second end of the opening may contact the earth's surface at a second location. The heat may be allowed to transfer from the opening to at least a part of the formation. The transferred heat may pyrolyze at least some hydrocarbons in the formation. In certain embodiments, providing the heat to the opening may include providing heat, heated materials, and/or oxidation products from at least one heater to the opening.

公开(公告)号：US08858784B2

公开(公告)日：2014-10-14

申请号：US13314893

申请日：2011-12-08

申请人： Stanley Nemec Milam ,  Michael Anthony Reynolds ,  Scott Lee Wellington ,  Frederik Arnold Buhrman

发明人： Stanley Nemec Milam ,  Michael Anthony Reynolds ,  Scott Lee Wellington ,  Frederik Arnold Buhrman

IPC分类号： C10G65/12 ,  C10G47/06 ,  C10G47/26 ,  B01J27/049 ,  B01J37/03 ,  B01J35/10 ,  C10G65/02 ,  C10G47/02 ,  B01J27/043 ,  B01J27/051 ,  B01J27/045

CPC分类号： C10G65/12 ,  B01J27/043 ,  B01J27/045 ,  B01J27/049 ,  B01J27/0515 ,  B01J35/1014 ,  B01J35/1038 ,  B01J35/1061 ,  B01J35/1066 ,  B01J35/1071 ,  B01J37/031 ,  C10G47/02 ,  C10G47/06 ,  C10G47/26 ,  C10G65/02 ,  C10G2300/1096 ,  C10G2300/202 ,  C10G2300/301 ,  C10G2300/4006 ,  C10G2300/4012 ,  C10G2400/30

摘要： A process for treating a hydrocarbon-containing feedstock is provided in which a hydrocarbon-containing feedstock comprising at least 20 wt. % of heavy hydrocarbons is mixed with hydrogen and a catalyst to produce a vapor comprising a first hydrocarbon-containing product. The vapor comprising the first hydrocarbon-containing product is separated from the mixture, and, apart from the mixture, the first hydrocarbon-containing product is contacted with hydrogen and a catalyst containing a Column 6 metal to produce a second hydrocarbon-containing product.

摘要翻译： 提供了一种处理含烃原料的方法，其中含烃原料包含至少20wt。 将重质烃的重量与氢气和催化剂混合以产生包含第一含烃产物的蒸汽。 包含第一含烃产物的蒸气与混合物分离，并且除混合物外，第一含烃产物与氢和含有第6列金属的催化剂接触以产生第二含烃产物。

公开(公告)号：US08834708B2

公开(公告)日：2014-09-16

申请号：US13314854

申请日：2011-12-08

申请人： Stanley Nemec Milam ,  Michael Anthony Reynolds ,  Scott Lee Wellington ,  Frederik Arnold Buhrman

发明人： Stanley Nemec Milam ,  Michael Anthony Reynolds ,  Scott Lee Wellington ,  Frederik Arnold Buhrman

IPC分类号： C10G65/12 ,  C10G47/06 ,  C10G47/26 ,  C10G45/04 ,  B01J27/051 ,  B01J37/03 ,  B01J35/00 ,  B01J35/10 ,  C10G47/02 ,  B01J37/00

CPC分类号： C10G65/12 ,  B01J27/0515 ,  B01J35/002 ,  B01J35/1019 ,  B01J35/1038 ,  B01J35/1066 ,  B01J37/009 ,  B01J37/031 ,  C10G45/04 ,  C10G47/02 ,  C10G47/06 ,  C10G47/26 ,  C10G2300/1096 ,  C10G2300/202 ,  C10G2300/207 ,  C10G2300/301 ,  C10G2300/4006 ,  C10G2300/4012 ,  C10G2400/30

摘要： A process for treating a hydrocarbon-containing feedstock is provided in which a hydrocarbon-containing feedstock comprising at least 20 wt. % of heavy hydrocarbons is mixed with hydrogen and a metal-containing non-acidic catalyst at a temperature of 375° C. to 500° C. to produce a vapor comprising a first hydrocarbon-containing product. The vapor comprising the first hydrocarbon-containing product is separated from the mixture, and, apart from the mixture, the first hydrocarbon-containing product is contacted with hydrogen and a catalyst containing a Column 6 metal at a temperature of 260° C.-425° C. to produce a second hydrocarbon-containing product.

摘要翻译： 提供了一种处理含烃原料的方法，其中含烃原料包含至少20wt。 ％的重质烃与氢气和含金属的非酸性催化剂在375℃至500℃的温度下混合以产生包含第一含烃产物的蒸气。 包含第一含烃产物的蒸汽与混合物分离，除混合物外，第一含烃产物与氢气和含有第6列金属的催化剂在260℃-255℃的温度下接触 ℃以产生第二含烃产物。

公开(公告)号：US08834707B2

公开(公告)日：2014-09-16

申请号：US13314781

申请日：2011-12-08

申请人： Stanley Nemec Milam ,  Michael Anthony Reynolds ,  Scott Lee Wellington ,  Frederik Arnold Buhrman

发明人： Stanley Nemec Milam ,  Michael Anthony Reynolds ,  Scott Lee Wellington ,  Frederik Arnold Buhrman

IPC分类号： C10G65/12 ,  C10G47/06 ,  C10G47/26 ,  B01J27/043

CPC分类号： C10G65/12 ,  B01J27/043 ,  C10G47/06 ,  C10G47/26 ,  C10G2300/202 ,  C10G2300/207 ,  C10G2300/301 ,  C10G2300/4006 ,  C10G2300/4012 ,  C10G2400/30

摘要： A process for treating a hydrocarbon-containing feedstock is provided in which a hydrocarbon-containing feedstock comprising at least 20 wt. % of heavy hydrocarbons is mixed with hydrogen, hydrogen sulfide and a metal-containing catalyst at a temperature of 375° C. to 500° C. and a pressure of from 6.9 MPa to 27.5 MPa to produce a vapor comprising a first hydrocarbon-containing product, where the hydrogen sulfide is mixed with the feedstock, metal-containing catalyst, and hydrogen at a mole ratio of hydrogen sulfide to hydrogen of at least 1:10. The vapor comprising the first hydrocarbon-containing product is separated from the mixture, and, apart from the mixture, the first hydrocarbon-containing product is contacted with hydrogen and a catalyst containing a Column 6 metal at a temperature of 260° C.-425° C. and a pressure of from 3.4 MPa to 27.5 MPa to produce a second hydrocarbon-containing product.

摘要翻译： 提供了一种处理含烃原料的方法，其中含烃原料包含至少20wt。 ％的重质烃与氢，硫化氢和含金属的催化剂在375℃至500℃的温度和6.9MPa至27.5MPa的压力下混合以产生包含第一含烃的 产物，其中硫化氢与原料，含金属的催化剂和氢气以硫化氢与氢气的摩尔比混合至至少1:10。 包含第一含烃产物的蒸汽与混合物分离，除混合物外，第一含烃产物与氢气和含有第6列金属的催化剂在260℃-255℃的温度下接触 ℃，压力为3.4MPa至27.5MPa，以产生第二含烃产物。

公开(公告)号：US08613851B2

公开(公告)日：2013-12-24

申请号：US13087076

申请日：2011-04-14

申请人： Scott Lee Wellington ,  Stanley Nemec Milam

发明人： Scott Lee Wellington ,  Stanley Nemec Milam

IPC分类号： C10L1/04

CPC分类号： C10G45/00 ,  C10G65/04 ,  C10L1/04 ,  Y02P20/142

摘要： The present invention is directed to a crude product composition comprising hydrocarbons having a boiling range distribution of from 30° C. to 538° C., the crude product composition having, per gram of crude product composition, from 0.01 grams to 0.2 grams of hydrocarbons having a boiling range distribution of at most 204° C., where olefins comprise at least 0.02 grams per gram of the hydrocarbons having a boiling range distribution of at most 204° C., and from 0.000001 grams to 0.05 grams of hydrocarbons having a boiling range distribution of greater than 538° C.

摘要翻译： 本发明涉及一种粗产物组合物，其包含沸点范围分布为30℃至538℃的烃，粗产物组合物具有每克粗产物组合物0.01克至0.2克烃 其沸程分布最多为204℃，其中烯烃包含至少0.02克/克沸点分布最多为204℃的烃和0.000001克至0.05克具有沸点的烃 范围分布大于538°C

公开(公告)号：US08597496B2

公开(公告)日：2013-12-03

申请号：US13010927

申请日：2011-01-21

申请人： Michael Anthony Reynolds ,  Stanley Nemec Milam ,  Scott Lee Wellington

发明人： Michael Anthony Reynolds ,  Stanley Nemec Milam ,  Scott Lee Wellington

IPC分类号： C10G47/06 ,  C10G47/02 ,  C10G47/24 ,  C10G47/26

CPC分类号： C10G47/26 ,  B01J27/04 ,  B01J27/047 ,  B01J27/051 ,  B01J35/002 ,  B01J35/023 ,  B01J35/1014 ,  B01J35/1019 ,  B01J35/1038 ,  B01J35/1061 ,  B01J37/031 ,  C01G19/006 ,  C01G39/006 ,  C01P2004/62 ,  C01P2006/12 ,  C01P2006/14 ,  C01P2006/16 ,  C10G47/02 ,  C10G47/06 ,  C10G2300/202 ,  C10G2300/206 ,  C10G2300/207 ,  C10G2300/301 ,  C10G2300/4006 ,  C10G2300/4012

摘要： A process for treating a hydrocarbon-containing feedstock is provided in which a hydrocarbon-containing feed comprising at least 20 wt. % of heavy hydrocarbons is mixed with hydrogen and at least one catalyst to produce a hydrocarbon-containing product. The hydrocarbon-containing feedstock, the catalyst(s), and the hydrogen are provided to a mixing zone and blended in the mixing zone at a temperature of from 375° C. to 500° C. A vapor comprised of hydrocarbons that are vaporizable at the temperature and pressure within the mixing zone is separated from the mixing zone, and, apart from the mixing zone, the vapor is condensed to produce a liquid hydrocarbon-containing product. The hydrocarbon-containing feedstock is continuously or intermittently provided to the mixing zone at a rate of at least 350 kg/hr per m3 of the mixture volume in the mixing zone.

摘要翻译： 提供了一种处理含烃原料的方法，其中含烃进料包含至少20wt。 ％的重质烃与氢和至少一种催化剂混合以产生含烃产物。 将含烃原料，催化剂和氢气提供到混合区并在混合区中在375℃至500℃的温度下共混。由烃组成的蒸汽可以在 混合区内的温度和压力与混合区分离，并且除了混合区之外，蒸气冷凝以产生含液体烃的产物。 将含烃原料以混合区中每立方米混合物体积至少350kg / hr的速率连续或间歇地提供给混合区。