子分类：
| 序号 | 专利名 | 申请号 | 申请日 | 公开（公告）号 | 公开（公告）日 | 发明人 |
|---|---|---|---|---|---|---|
| 21 | Process for the Oxidative Coupling of Hydrocarbons | US14072971 | 2013-11-06 | US20140066677A1 | 2014-03-06 | Sivadinarayana Chinta; Joseph L. Thorman; James R. Butler; Joe Hunter; Taylor Rives |
| A method for the oxidative coupling of hydrocarbons, such as the oxidative coupling of methane to toluene, includes providing an oxidative catalyst inside a reactor, and carrying out the oxidative coupling reaction under a set of reaction conditions. The oxidative catalyst includes (A) at least one element selected from the group consisting of the Lanthanoid group, Mg, Ca, and the elements of Group 4 of the periodic table (Ti, Zr, and Hf); (B) at least one element selected from the group consisting of the Group 1 elements of Li, Na, K, Rb, Cs, and the elements of Group 3 (including La and Ac) and Groups 5-15 of the periodic table; (C) at least one element selected from the group consisting of the Group 1 elements of Li, Na, K, Rb, Cs, and the elements Ca, Sr, and Ba; and (D) oxygen. | ||||||
| 22 | Process for the Oxidative Coupling of Hydrocarbons | US13867295 | 2013-04-22 | US20130231513A1 | 2013-09-05 | Sivadinarayana Chinta; Joseph Thorman; James Butler; Joe Hunter; Taylor Rives |
| A method for the oxidative coupling of hydrocarbons, such as the oxidative coupling of methane to toluene, includes providing an oxidative catalyst inside a reactor, and carrying out the oxidative coupling reaction under a set of reaction conditions. The oxidative catalyst includes (A) at least one element selected from the group consisting of the Lanthanoid group, Mg, Ca, and the elements of Group 4 of the periodic table (Ti, Zr, and Hf); (B) at least one element selected from the group consisting of the Group 1 elements of Li, Na, K, Rb, Cs, and the elements of Group 3 (including La and Ac) and Groups 5-15 of the periodic table; (C) at least one element selected from the group consisting of the Group 1 elements of Li, Na, K, Rb, Cs, and the elements Ca, Sr, and Ba; and (D) oxygen. | ||||||
| 23 | Process for the oxidative coupling of hydrocarbons | US12494138 | 2009-06-29 | US08450546B2 | 2013-05-28 | Sivadinarayana Chinta; Joseph Thorman; James Butler; Joe Hunter; Taylor Rives |
| A method for the oxidative coupling of hydrocarbons, such as the oxidative coupling of methane to toluene, includes providing an oxidative catalyst inside a reactor, and carrying out the oxidative coupling reaction under a set of reaction conditions. The oxidative catalyst includes (A) at least one element selected from the group consisting of the Lanthanoid group, Mg, Ca, and the elements of Group 4 of the periodic table (Ti, Zr, and Hf); (B) at least one element selected from the group consisting of the Group 1 elements of Li, Na, K, Rb, Cs, and the elements of Group 3 (including La and Ac) and Groups 5-15 of the periodic table; (C) at least one element selected from the group consisting of the Group 1 elements of Li, Na, K, Rb, Cs, and the elements Ca, Sr, and Ba; and (D) oxygen. | ||||||
| 24 | PROCESS FOR THE OXIDATIVE COUPLING OF HYDROCARBONS | EP10794571.9 | 2010-06-25 | EP2448887A1 | 2012-05-09 | CHINTA, Sivadinarayana; THORMAN, Joseph; BUTLER, James, R.; HUNTER, Joe; RIVES, Taylo |
| A method for the oxidative coupling of hydrocarbons, such as the oxidative coupling of methane to toluene, includes providing an oxidative catalyst inside a reactor, and carrying out the oxidative coupling reaction under a set of reaction conditions. The oxidative catalyst includes (A) at least one element selected from the group consisting of the Lanthanoid group, Mg, Ca, and the elements of Group 4 of the periodic table (Ti, Zr, and Hf); (B) at least one element selected from the group consisting of the Group 1 elements of Li, Na, K, Rb, Cs, and the elements of Group 3 (including La and Ac) and Groups 5 - 15 of the periodic table; (C) at least one element selected from the group consisting of the Group 1 elements of Li, Na, K, Rb, Cs, and the elements Ca, Sr, and Ba; and (D) oxygen. | ||||||
| 25 | PROCESSES FOR CONVERTING CHLORINATED ALKANE BYPRODUCTS OR WASTE PRODUCTS TO USEFUL, LESS CHLORINATED ALKENES | EP93920064.8 | 1993-08-13 | EP0662941B1 | 1997-12-10 | ITO, Larry, N.; HARLEY, A., Dale; HOLBROOK, Michael, T.; SMITH, David, D.; MURCHISON, Craig, B.; CISNEROS, Mark, D. |
| A process for the catalytic conversion of various chlorinated alkane byproducts and waste products especially to reaction products including a useful or salable less chlorinated alkene, in which a chlorinated alkane feedstock is reacted with hydrogen in the presence of a catalyst including a Group VIII metal such as platinum in elemental or compound form, and a Group IB metal such as copper in elemental or compound form. | ||||||
| 26 | PROCESS FOR CONVERTING 1,2-DICHLOROPROPANE TO PROPYLENE | EP93920061.4 | 1993-08-13 | EP0662937B1 | 1997-03-19 | ITO, Larry, N.; HARLEY, A., Dale; HOLBROOK, Michael, T.; SMITH, David, D.; MURCHISON, Craig, B.; CISNEROS, Mark, D. |
| A process for the catalytic conversion of 1,2-dichloropropane to propylene with a high degree of conversion and selectivity, in which 1,2-dichloropropane is reacted with hydrogen in the presence of a catalyst including a Group VIII metal such as platinum in elemental or compound form, and a Group IB metal such as copper in elemental or compound form. | ||||||
| 27 | Oxidative coupling method of hydrocarbon | JP2012517753 | 2010-06-25 | JP2012532105A | 2012-12-13 | チンタ，シバデイナラヤナ; ソーマン，ジヨセフ; バトラー，ジエイムズ・アール; ハンター，ジヨー; ライブス，テイラー |
| 炭化水素の酸化カップリング方法、例えばメタンとトルエンの酸化カップリング方法などに、酸化用触媒を反応槽内に準備しそして酸化カップリング反応を一連の反応条件下で起こさせることを含める。 その酸化用触媒は、（Ａ）ランタノイド族、Ｍｇ、Ｃａおよび周期律表の４族の元素（Ｔｉ、ＺｒおよびＨｆ）から成る群より選択した少なくとも１種の元素、（Ｂ）周期律表の１族の元素であるＬｉ、Ｎａ、Ｋ、Ｒｂ、Ｃｓおよび３族の元素（ＬａおよびＡｃを包含）および５−１５族の元素から成る群より選択した少なくとも１種の元素、（Ｃ）１族の元素であるＬｉ、Ｎａ、Ｋ、Ｒｂ、Ｃｓおよび元素Ｃａ、ＳｒおよびＢａから成る群より選択した少なくとも１種の元素および（Ｄ）酸素を含有する。 | ||||||
| 28 | How to convert to vinyl chloride and / or ethylene 1,1,2-trichloroethane | JP50902394 | 1993-08-13 | JPH08502066A | 1996-03-05 | エヌ． イトー，ラリー; ディー． シスネロス，マーク; ディー． スミス，デビッド; ハーレー，エー．デイル; ティー． ホルブルック，マイケル; ビー． マーチソン，クレイグ |
| (57)【要約】 1，1，2-トリクロロエタンを工業上十分な割合で塩化ビニル及びエチレンの一方もしくは両方を含む反応生成物に触媒を用いて転化する方法であって、元素もしくは化合物形状の１種以上のIB族金属（例えば銅）及び元素もしくは化合物形状の１種以上のVIII族金属（例えば白金）を含む触媒の存在下において1，1，2-トリクロロエタンを水素と反応させる方法。 | ||||||
| 29 | How to convert the 2-chloropropane to propylene | JP50902194 | 1993-08-13 | JPH08502065A | 1996-03-05 | エヌ． イトー，ラリー; ディー． スミス，デビッド; ディー． チスネロス，マーク; ハーレー，エー．デイル; ティー． ホルブルック，マイケル; ビー． マーチソン，クレイグ |
| (57)【要約】 触媒を用いて2-クロロプロパンをプロピレンに転化する方法であって、元素もしくは化合物形状の１種以上のIB族金属（例えば銅）及び元素もしくは化合物形状の１種以上のVIII族金属（例えば白金）を含む触媒の存在下において2-クロロプロパンを水素と反応させることを特徴とする方法。 | ||||||
| 30 | How to convert 1,1,1,2-tetrachloroethane to vinylidene chloride | JP50901994 | 1993-08-13 | JPH08502063A | 1996-03-05 | エヌ． イトー，ラリー; ディー． シスネロス，マーク; ディー． スミス，デビッド; ハーリー，エー．デイル; ティー． ホルブルック，マイケル; ビー． マーチソン，クレイグ |
| (57)【要約】 1,1,1,2-テトラクロロエタンを工業上十分な割合で塩化ビニリデンを含む反応生成物に触媒転化する方法であって、元素もしくは化合物形状の１種以上のIB族金属（例えば銅）及び元素もしくは化合物形状の１種以上のVIII族金属（例えば白金）を含む触媒の存在下において1,1,1,2-テトラクロロエタンを水素と反応させる方法。 | ||||||
| 31 | How to convert to vinyl chloride and / or ethylene 1,1,2-trichloroethane | JP50902394 | 1993-08-13 | JP2818623B2 | 1998-10-30 | エヌ． イトー，ラリー; ディー． シスネロス，マーク; ディー． スミス，デビッド; ハーレー，エー．デイル; ティー． ホルブルック，マイケル; ビー． マーチソン，クレイグ |
| 32 | Process for converting 1,2-dichloropropane to propylene | JP50902593 | 1993-08-13 | JP2670189B2 | 1997-10-29 | エヌ． イトー，ラリー; ディー． シスネロス，マーク; ディー． スミス，デビッド; ハーレー，エー．デイル; ティー． ホルブルック，マイケル; ビー． マーチソン，クレイグ |
| 33 | Process for converting 1,2-dichloropropane to propylene | JP50902593 | 1993-08-13 | JPH08502067A | 1996-03-05 | エヌ． イトー，ラリー; ディー． シスネロス，マーク; ディー． スミス，デビッド; ハーレー，エー．デイル; ティー． ホルブルック，マイケル; ビー． マーチソン，クレイグ |
| (57)【要約】 1,2-ジクロロプロパンを高い転化率及び選択率でプロピレンに触媒を用いて転化する方法であって、元素もしくは化合物形状の１種以上のIB族金属（例えば銅）及び元素もしくは化合物形状の１種以上のVIII族金属（例えば白金）を含む触媒の存在下において1,2-ジクロロプロパンを水素と反応させる方法。 | ||||||
| 34 | Process for converting 1,2,3-trichloropropane to allyl chloride and propylene | JP50902093 | 1993-08-13 | JPH08502064A | 1996-03-05 | エヌ． イトー，ラリー; ディー． シスネロス，マーク; ディー． スミス，デビッド; ハーレー，エー．デイル; ティー． ホルブルック，マイケル; ビー． マーチソン，クレイグ |
| (57)【要約】 l,2,3-トリクロロプロパンを良好な収率及び選択率でプロピレン及び塩化アリルを含む反応生成物に触媒転化する方法であって、元素もしくは化合物形状のIB族金属（例えば銅）及び元素もしくは化合物形状のVIII族金属（例えば白金）を含む触媒の存在下において1,2,3-トリクロロプロパンを水素と反応させる方法。 | ||||||
| 35 | 탄화수소의 산화성 짝반응을 위한 방법 | KR1020117030880 | 2010-06-25 | KR1020120115081A | 2012-10-17 | 친타,시바디나라야나; 토만,조셉; 버틀러,제임스,알.; 헌터,조; 리브즈,타일러 |
| 톨루엔에 대한 메탄의 산화성 짝반응과 같은 탄화수소의 산화성 짝반응을 위한 방법은, 반응기 내에서 산화성 촉매를 제공하는 단계와, 한 세트의 반응 조건 하에 산화성 짝반응을 수행하는 단계를 포함한다. 산화성 촉매는, (A) 란탄족, Mg, Ca, 및 주기율표의 4족 원소(Ti, Zr, 및 Hf)로 이루어진 군으로부터 선택된 적어도 하나의 원소와, (B) Li, Na, K, Rb, Cs의 1족 원소와 주기율표의 3족(La와 Ac 포함) 및 5 - 15족의 원소로 이루어진 군으로부터 선택된 적어도 하나의 원소와, (C) Li, Na, K, Rb, Cs의 1족 원소와 원소 Ca, Sr, 및 Ba로 이루어진 군으로부터 선택된 적어도 하나의 원소와, (D) 산소를 포함한다. | ||||||
| 36 | HYDROALKYLATION PROCESS | EP12799461.4 | 2012-11-30 | EP2819975A1 | 2015-01-07 | BECKER, Christopher, L.; LATTNER, James, R.; KUECHLER, Keith, H.; NAIR, Hari |
| In a process for producing phenol, benzene is hydroalkylated with hydrogen in the presence of a catalyst under conditions effective to produce a hydroalkylation reaction product comprising cyclohexylbenzene and cyclohexane. At least a portion of the cyclohexane from said hydroalkylation reaction product is then dehydrogenated to produce a dehydrogenation effluent comprising benzene, toluene and hydrogen. At least a portion of the dehydrogenation effluent is washed with a benzene-containing stream to transfer at least a portion of the toluene from the dehydrogenation effluent to the benzene-containing stream. | ||||||
| 37 | PROCESS FOR CONVERTING 2-CHLOROPROPANE TO PROPYLENE | EP93918729.0 | 1993-08-13 | EP0662936B1 | 1996-10-23 | ITO, Larry, N.; HARLEY, A., Dale; HOLBROOK, Michael, T.; SMITH, David, D.; MURCHISON, Craig, B.; CISNEROS, Mark, D. |
| A process for the catalytic conversion of 2-chloropropane to propylene, characterized in that 2-chloropropane is reacted with hydrogen in the presence of a catalyst including a Group VIII metal such as platinum in elemental or compound form, and a Group IB metal such as copper in elemental or compound form. | ||||||
| 38 | PROCESSES FOR CONVERTING CHLORINATED ALKANE BYPRODUCTS OR WASTE PRODUCTS TO USEFUL, LESS CHLORINATED ALKENES | EP93920064.0 | 1993-08-13 | EP0662941A1 | 1995-07-19 | ITO, Larry, N.; HARLEY, A., Dale; HOLBROOK, Michael, T.; SMITH, David, D.; MURCHISON, Craig, B.; CISNEROS, Mark, D. |
| A process for the catalytic conversion of various chlorinated alkane byproducts and waste products especially to reaction products including a useful or salable less chlorinated alkene, in which a chlorinated alkane feedstock is reacted with hydrogen in the presence of a catalyst including a Group VIII metal such as platinum in elemental or compound form, and a Group IB metal such as copper in elemental or compound form. | ||||||
| 39 | PROCESS FOR CONVERTING 1,1,2-TRICHLOROETHANE TO VINYL CHLORIDE AND/OR ETHYLENE | EP93920059.0 | 1993-08-13 | EP0662940A1 | 1995-07-19 | ITO, Larry, N.; HARLEY, A., Dale; HOLBROOK, Michael, T.; SMITH, David, D.; MURCHISON, Craig, B.; CISNEROS, Mark, D. |
| A process for the catalytic conversion of 1,1,2-trichloroethane to reaction products including one or both of ethylene and vinyl chloride in a commercially substantial proportion, in which 1,1,2-trichloroethane is reacted with hydrogen in the presence of a catalyst including a Group VIII metal such as platinum in elemental or compound form, and a Group IB metal such as copper in elemental or compound form. | ||||||
| 40 | PROCESS FOR CONVERTING 1,2-DICHLOROPROPANE TO PROPYLENE | EP93920061.0 | 1993-08-13 | EP0662937A1 | 1995-07-19 | ITO, Larry, N.; HARLEY, A., Dale; HOLBROOK, Michael, T.; SMITH, David, D.; MURCHISON, Craig, B.; CISNEROS, Mark, D. |
| A process for the catalytic conversion of 1,2-dichloropropane to propylene with a high degree of conversion and selectivity, in which 1,2-dichloropropane is reacted with hydrogen in the presence of a catalyst including a Group VIII metal such as platinum in elemental or compound form, and a Group IB metal such as copper in elemental or compound form. | ||||||
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