CAS: 13569-63-6; Rhenium(Iii) Chloride

上下游产品

CAS号13596-35-5 氯化铼(V) | CAS号14099-01-5 五羰基氯铼(I) | CAS号13596-35-5 氯化铼(V)

📜Potassium Hexachlororhenate(Iv) 以 Not Given 用作溶剂,化学反应生成氯化铼(III)
参考文献:Manchot,W.; Duesing,J.,Zeitschrift Fur Anorganische Chemie,1933,Vol. 212,P. 29-29
标题:Manchot,W.; Duesing,J.,Zeitschrift Fur Anorganische Chemie,1933,Vol. 212,P. 29-29

专利信息

专利号:US-7910048-B2
优先权日:2004-01-26
标题:Apparatus for plasma synthesis of rhenium nano and micro powders
发明人：JUREWICZ JERZY W; GUO JIAYIN
权利人:TEKNA PLASMA SYSTEMS INC
摘要:The process for the synthesis of rhenium powders comprises the injection of ammonium perrhenate powder through a carrier gas in a plasma torch of a plasma reactor operated using a mixture including hydrogen as the plasma gas, yielding metallic rhenium under the following chemical reaction:n n2NH 4 ReO 4 +4H 2 →2Re+N 2 ↑+8H 2 O↑.n nThe reactor is provided with a quench zone for cooling the metallic rhenium so as to yield rhenium nano and micro powders.

专利号:US-9079164-B2
优先权日:2012-03-26
标题:Single reaction synthesis of texturized catalysts
发明人：WOODFIELD BRIAN F; SMITH STACEY; SELCK DAVID; BARTHOLOMEW CALVIN H; MA XUCHU; XU FEN; OLSEN REBECCA E; ASTLE LYNN
权利人:UNIV BRIGHAM YOUNG
摘要:Methods are described for making a texturized catalyst. The textural promoter may be a high-surface area, high-porosity, stable metal oxide support. The catalyst is manufactured by reacting catalyst precursor materials and support materials in a single, solvent deficient reaction to form a catalyst. The catalyst may be particles or a coating or partial coating of a support surface.

专利号:US-4806699-A
优先权日:1986-11-06
标 题 :Process for the production of aromatic hydrocarbons incorporating by-product utilization
发明人：SMITH DAVID J H; WOODFIN WILLIAM T
权利人:BRITISH PETROLEUM CO PLC
摘要:Aromatic hydrocarbons are produced from a feedstock comprising ethane and/or propane and/or butane by the steps of: n (A) reacting the feedstock in the presence of a dehydrocyclodimerization catalyst to produce a product comprising aromatic hydrocarbons, hydrogen and methane, n (B) separating the product of step (A) into an aromatic hydrocarbon fraction, a methane-rich gaseous fraction and a hydrogen-rich gaseous fraction, n (C) feeding all or part of the methane-rich gaseous fraction separated in step (B) to a synthesis gas production unit, thereby to produce synthesis gas, and n (D) contacting the synthesis gas from step (C) together with all or part of the hydrogen-rich gaseous fraction separated in step (B), thereby increasing the hydrogen to carbon monoxide ratio of the synthesis gas, with a Fischer-Tropsch conversion catalyst to produce a hydrocarbon product.

专利号:US-4801573-A
优先权日:1987-10-23
标 题:Catalyst for production of hydrocarbons
发明人：GOODWIN JAMES G JR; ERI SIGRID; MARCELIN GEORGE; RIIS TRYGVE
权利人:NORSKE STATS OLJESELSKAP
摘要:A catalyst and process for converting synthesis gas composed of hydrogen and carbon monoxide to hydrocarbons. The catalyst includes cobalt in catalytically active amounts up to about 60wt% of the catalyst and rhenium in catalystically active amounts of about 0.5 to 50wt% of the cobalt content of the catalyst supported on alumina. A metal oxide promoter may be added. A preferred process includes the step of contact the synthesis gas feed with the catalyst at reaction conditions.

专利号:US-8598239-B2
优先权日:2010-10-11
标题 :Anderson-type heteropoly compound-based catalyst compositions and their use conversion of synthesis gas to oxygenates
发明人：MANIKANDAN PALANICHAMY; BARTON DAVID G; MILLAR DEAN M
权利人:MANIKANDAN PALANICHAMY; BARTON DAVID G; MILLAR DEAN M; DOW GLOBAL TECHNOLOGIES LLC
摘要:Use a transition metal-containing, Anderson-type heteropoly compound catalyst to convert synthesis gas to an oxygenate, especially an alcohol that contains from one carbon atom to six carbon atoms.

专利号:US-4857559-A
优先权日:1987-10-23
标题 :Process for production of hydrocarbons
发明人：GOODWIN JAMES G JR; ERI SIGRID; MARCELIN GEORGE; RIIS TRYGVE
权利人:GAS TO OIL INC
摘要:A process for converting synthesis gas composed of hydrogen and carbon monoxide to hydrocarbons. The process includes the step of contacting at reaction conditions a synthesis gas feed to a catalyst which includes cobalt in catalytically active amounts up to about 60 wt % of the catalyst and rhenium in catalytically active amounts of about 0.5 to 50 wt % of the cobalt content of the catalyst supported on alumina. A metal oxide promoter may be added.