摘要:
Ketones are converted in one step to saturated dimeric ketones by passing them over a zeolite having a silica to alumina ratio of at least 12 and a Constraint Index of from 1 to 12 and containing a Group VIII metal.
摘要:
A mixture of carbon monoxide and hydrogen is contacted with a mixture comprising an element selected from the group consisting of ruthenium, rhodium and osmium carbon monoxide reduction catalyst and a crystalline alumino-silicate providing a pore dimension greater than about 5 Angstroms and a constraint index in the range of 1 to 12 to produce hydrocarbon mixtures useful in forming gasoline boiling range products, aromatic rich hydrocarbons, and chemical intermediates.
摘要:
The high boiling fraction of Fischer-Tropsch synthesis is upgraded by contact with a catalyst comprising a high-silica, large pore zeolite and a hydrogenation component. The products are a distillate fraction characterized by low sulfur and nitrogen content, high isoparaffin content and low pour point and a lube fraction characterized by its high viscosity index and low pour point.
摘要:
In the conversion of coal to gaseous and liquid products, the heat value of the coal is more completely retained by the products through the selective high efficiency conversion of coal to a low ratio syngas utilizing a portion of the Fischer-Tropsch generated heat recovered as steam, conversion of the low ratio syngas with a water gas shift F-T catalyst to a product comprising C.sub.1 to C.sub.50 hydrocarbons and oxygenates, converting the F-T product to premium gas and increased liquid fuels comprising gasoline and distillate with a special zeolite catalyst and recovering the SNG and LPG products of the selective steps to provide an improved product slate. A portion of the produced fuel gas is used in lieu of coal to provide some of the heat energy requirements of the combination process.
摘要:
A gaseous mixture of carbon monoxide and hydrogen is contacted in a first reactor with an iron Fischer-Tropsch catalyst such as potassium promoted iron under special conditions and the total products from said contact are then converted in a second reactor containing HZSM-5 to obtain either a highly olefinic or highly aromatic product depending on reaction conditions.
摘要:
High severity catalytic conversion of olefinic naphthas which contain diolefins is conducted over special catalysts to yield a product stream which contains little or no non-aromatics boiling in the range of benzene, toluene and xylene. The catalysts are combinations of zinc and a metal of Groups I B and VIII of the Periodic Table with a crystalline aluminosilicate zeolite having a silica/alumina ratio greater than 12 and a constraint index not less than one nor greater than 12.
摘要:
A process for alkylating aromatic compounds wherein the product aromatics are provided with one or more alkyl groups possessing at least two carbon atoms is disclosed wherein starting aromatic compound(s) and an alkylating atent which is a mixture of hydrogen and/or a hydrogen-containing substance which provides hydrogen under process conditions and a carbon oxide, e.g., a mixture of syngas (hydrogen and carbon monoxide) are reacted at elevated temperature in the presence of an activated catalyst containing metal values selected from the group consisting of iron, cobalt, ruthenium, manganese, rhodium and osmium, and a zeolite having a constraint index of 12 or less, e.g., ZSM-5. The alkylated aromatics can be dealkylated by known and conventional means to provide olefin and the dealkylated aromatics can be recycled to the alkylation zone.
摘要:
The conversion of less than 1 H.sub.2 /CO ratio syngas to high yield of C.sub.3 plus product is accomplished with a CO reducing catalyst comprising shift characteristics and the product of Fischer-Tropsch synthesis is converted to premium gasoline and distillate fuels by contact with acidic ZSM-5 zeolite.The syngas conversion may be accomplished in any catalyst system permitting a very close temperature control on the exotherm encountered and the gasoline-distillate yield relationship may be varied as a function of temperature and pressure.
摘要翻译:通过包含转移特性的CO还原催化剂实现小于1 H 2 / CO比合成气转化为高产率的C3加产物,并且通过与酸性ZSM-3接触将费 - 托合成的产物转化为优质汽油和馏出燃料, 5沸石。 合成气转化可以在任何催化剂体系中完成,允许对所遇到的放热进行非常接近的温度控制,并且汽油馏出物收率关系可以随着温度和压力的变化而变化。
摘要:
A process for effecting an endothermic and an exothermic reaction, under conversion conditions, in a single reaction zone wherein ethane is endothermically converted to C.sub.3 + hydrocarbons, and wherein an unconverted portion of ethane is simultaneously exothermically hydrogenated to methane in the presence of a catalyst system comprising a crystalline aluminosilicate zeolite having a uniform structure characterized by pores, the major dimension of which is less than 6 Angstroms and ZSM-5 type aluminosilicate zeolite, containing a minor amount of Zn in combination with a Group VIII noble metal or a Group IB metal, the exothermic reaction providing sufficient heat to maintain the reaction zone at a temperature capable of sustaining the endothermic reaction.
摘要:
Naphthas are upgraded in a two-stage process to give improved yields of high octane gasoline. The first stage operates at low temperatures of 100.degree.-300.degree. F using a highly active chlorinated alumina containing a metal of the platinum group, while the second stage operates at high temperatures using a reforming catalyst.