The British Petroleum Company, P.l.c.

David G Stewart

William J Ball

Keith W Palmer

Barry Nay

Brian R Gane

Leonard Cotton

George E Morris

Michael T Barlow

A catalyst composition of use in the production of hydrocarbons from synthesis gas comprises the essential metals

Catalyst composition, method for its production and its use in the

Unsaturated carboxylic acids and/or esters thereof are produced by reacting an aldehyde comprising formaldehyde or acetaldehyde with either a saturated carboxylic acid ester or anhydride in the vapor phase in the presence as catalyst of a high silica crystalline aluminosilicate zeolite in which the cation is H.sup.+ and/or a transition metal and/or a rare earth metal. In a modification of the process instead of formaldehyde there is used methanol/molecular oxygen and in the catalyst there is included either an oxidative or an oxidative/dehydrogenative component.

Process for the production of unsaturated carboxylic acids and/or esters

A catalyst composition suitable for use in the production of alcohols from synthesis gas comprises as essential elements:

Catalyst composition and its use in a process for the production of

Catalyst composition for the production of alcohols from synthesis gas

A catalyst composition for use in the production of hydrocarbons from synthesis gas comprises the essential metals

Catalyst composition, method for its production

A process for the production of a catalyst based on a crystalline aluminosilicate having a silica to alumina molar ratio greater than 12:1 which is obtained by mixing a source of silica, a source of alumina, a source of alkali metal, water and a source of ammonium ions in defined proportions, crystallizing the mixture, recovering the crystalline aluminosilicate so-formed, cation-exchanging and/or impregnating the recovered crystalline aluminosilicate and finally calcining, wherein either the recovered crystalline aluminosilicate or the cation-exchanged aluminosilicate or the impregnated aluminosilicate is washed with a solution containing either an organic base, a carboxylic acid, an alcohol, a glycol, a phenol or an ester. The washing treatment results in a reduction in the rate of decline in catalytic activity in reactions such as the conversion of aliphatic to aromatic hydrocarbons.

Process for the production of catalysts based on crystalline

C.sub.1 to C.sub.4 oxygenated hydrocarbons are produced by contacting synthesis gas at a temperature in the range 150.degree. C. to 450.degree. C. and a pressure in the range of 1 to 700 bars with a catalyst comprising a supported mixture of a rhodium component and a silver component. The preferred support is silica. Other metal components which may be incorporated on the support are iron, manganese, molybdenum, tungsten, ruthenium, chromium, thorium and zirconium. Furthermore the support can be activated prior to incorporation of the metal components.

Process for the production of C.sub.1 to C.sub.4 oxygenated hydrocarbons

An oxygenated hydrocarbon product comprising methanol and ethanol is produced by hydrogenating carbon monoxide at a temperature in the range 150.degree. to 450.degree. C. and a pressure in the range 1 to 700 bars in the presence as catalyst of a supported mixture of the metals rhodium, silver, zirconium and molybdenum and optionally also one or more of the metals iron, manganese, rhenium, tungsten, ruthenium, chromium, thorium and potassium. The preferred support is silica.

Process for the production of oxygenated hydrocarbons by the catalytic

The invention relates to a method for preparing a crystalline aluminosilicate having a high silica to alumina molar ratio and an X-ray diffraction pattern substantially the same as that of ZSM-5 zeolite which method comprises mixing a source of silica, a source of alumina, a source of alkali metal, water and at least one alkanolamine according to Formula (I): ##STR1## wherein any two of R.sup.1, R.sup.2 and R.sup.3 are independently alkylol groups and the remaining one of R.sup.1, R.sup.2 and R.sup.3 is a hydrogen atom or all of R.sup.1, R.sup.2 and R.sup.3 are independently alkylol group, the alkylol groups being --CH.sub.2 --R--OH, wherein R is --CH.sub.2 --, --CH.sub.2 CH.sub.2 --, or --CH(CH.sub.3)--, the ratio of said source of silica to said source of alumina being at least 20:1 based on the equivalent moles of silica and alumina in said respective sources, maintaining said mixture at a temperature above about 120.degree. C. and recovering the crystalline aluminosilicate formed.

Crystalline aluminosilicates

Crystalline aluminosilicates having a silica to alumina molar ratio greater than 12 are produced by mixing a source of silica, a source of alumina, a source of alkali metal, water and a source of ammonium ions, e.g. ammonia or an ammonium salt, in the absence of an alcohol or alkylene oxide, in the molar proportions (expressed in the case of the silica and alumina sources in terms of the equivalent moles of the oxide, in the case of the alkali metal source in terms of the equivalent moles of the hydroxide (MOH) and in the case of the source of ammonium ions in terms of free ammonia):

Process for the production of crystalline aluminosilicates and their use

Method for producing crystalline aluminosilicates and their use as

Crystalline aluminosilicates having a high silica to alumina molar ratio are prepared by mixing a source of silica, a source of alumina, a source of alkali metal, water and one or more substituted neopentylamines having the formula: ##STR1## wherein R.sup.2 is H, OH or NH.sub.2 and R.sup.1 is a C.sub.1 to C.sub.6 alkyl group, and maintaining the mixture under conditions of elevated temperature and pressure, typically in the range from 80.degree. to 210.degree. C. and autogenous pressure for a time sufficient to effect formation of the aluminosilicate, typically not less than 4 hours. The molar ratio of silica to alumina in the initial mixture is suitably in the range from 10:1 to 150:1 and the amounts of alkali metal and neopentylamine are suitably in the range from 2:1 to 0.02:1 and 10:1 to 0.02:1 respectively moles per mole equivalent of total silica and alumina in the respective sources. Depending on the ratio of silica to alumina in the initial mixture crystalline aluminosilicates having a mordenite structure or a ZSM-5 type zeolite structure or mixtures thereof may be prepared. Mordenites having a silica to alumina ratio greater than 10:1 can be prepared.

Method for preparing crystalline aluminosilicates

A process for the production of a product comprising ethanol which process comprises reacting at elevated temperature and pressure and in the liquid phase methanol with hydrogen and carbon monoxide in the presence of an inert, particulate solid comprising a high surface area form of silica, alumina, silica/alumina or carbon, a methanol soluble catalyst comprising either:

Process for the production of ethanol by the liquid phase

A process for the production of aromatic hydrocarbons which process comprises contacting at elevated temperature and in the vapor phase a C.sub.2 to C.sub.12 aliphatic hydrocarbon feedstock with a catalyst comprising a crystalline aluminosilicate having a silica to alumina molar ratio greater than 12:1 which has been modified by incorporation therein of aluminium either by exchange or impregnation.

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Epsom, United Kingdom

David G Stewart