Labofina, S.a.

Cosden Technology, Inc.

Fina Research, S.a.

Georges E De Clippeleir

Raymond M Cahen

Guy L Debras

Steinar Kvisle

James M Watson

Jacques F Grootjans

Marshall W Abernathy

Andre Vanderlinden

Elizabeth B Ofstad

Francisco A Martins Mendes Cerejo

Elizabeth Baumann Ofstad

The present invention relates to a process for removing carbonyl sulfide from a liquid hydrocarbon feedstock, said process comprising the steps of (a) passing said hydrocarbon feedstock over an absorbent material comprising nickel deposited on a support material wherein nickel is present as both nickel oxide and metallic nickel and wherein the absorbent material has been conditioned by passing an inert gas flow containing a minor amount of propylene; and (b) recovering a liquid hydrocarbon stream having substantially reduced carbonyl sulfide content.

Process for removing carbonyl-sulfide from liquid hydrocarbon feedstocks

A process for production of gasoline comprising oligomerizing a C.sub.2 -C.sub.6 olefin containing feedstock over an intermediate pore size siliceous crystalline molecular sieve catalyst. The catalyst may take the form of silicalite, halogen stabilized silicalite, or a zeolite. Water may be supplied to the oligomerization reaction. The product from the oligomerization reaction is then subjected to an etherification reaction in the presence of methanol over an acid cation exchange catalyst to provide a gasoline product of enhanced octane number.

Process for producing gasoline

A process is described for the catalytic dehydrogenation of paraffinic hydrocarbons preferably having from 3 to 6 carbon atoms in the presence of a catalyst containing at least one metal of the platinum group, a co-catalyst and a promoter, the noble metal of the platinum group being deposited into the alumina support in two steps, the first one being followed by a calcination and a reduction, the second one being followed by a calcination.

Process for the preparation of a dehydrogenation catalyst

Process and catalyst for the catalytic dehydrogenation of hydrocarbons

The present invention relates to a process for removing carbonyl sulfide from a liquid hydrocarbon feedstock, said process comprising the steps of (a) passing said hydrocarbon feedstock over an absorbent material comprising nickel deposited on a support material wherein nickel is present as both nickel oxide and metallic nickel and wherein the absorbent material has been conditioned by passing an inert gas flow containing a minor amount of propylene; and (b) recovering a liquid hydrocarbon stream having a substantially reduced carbonyl sulfide content.

Alkynes are selectively hydrogenated in alkene rich hydrocarbon feeds, such as 1,3-butadiene-rich C.sub.4 cuts, by passing the hydrocarbon feed at least partially in liquid phase over a palladium-based catalyst in the presence of hydrogen, preferably in trickle mode, followed by passing the effluent, at least partially in liquid phase preferably containing about 300-400 ppmw alkynes, over a copper-based catalyst in the presence of hydrogen thereby producing a hydrocarbon product of significantly reduced alkyne concentration.

Process for the selective hydrogenation of alkynes

A catalytic treatment process is disclosed, which is carried out under pressure, in the presence of water, and with a molecular sieve catalyst which is TEA-silicate or silicalite previously stabilized by halogenation. This process may be applied to the aromatization or to the isomerization of hydrocarbon feedstocks, and to the oligomerization of olefins. The conversion rate of the process is very stable as a function of time.

Catalytic treatment process

The present invention relates to a process for removing carbonyl sulfide from a liquid olefinic hydrocarbon feedstock comprising (a) passing said hydrocarbon feedstock over an absorbent material comprising zinc oxide and a promoter selected from the group consisting of alumina, silico-aluminas and any combination thereof; and (b) recovering a liquid olefinic hydrocarbon stream having a substantially reduced carbonyl sulfide content.

A process for the selective alkylation of monoalkylbenzene into dialkylbenzenes wherein the para isomer of the disubstituted product is present in a concentration greater than in a thermodynamic equilibrium is provided. The method comprises passing the monoalkylbenzene and an alkylating agent capable of methylation, ethylation or propylation through a reaction zone containing an unmodified crystalline silica catalyst of the silicalite type having the monoclinic symmetry.

Process for para selective alkylation of aromatic hydrocarbons

A process for the isomerization of n-butenes, comprising contacting, at elevated temperatures, a feed containing n-butenes with a catalyst comprising a crystalline silica polymorph of the silicalite type in the presence of stream to recover a steam containing isobutene. The reaction can be carried out in either liquid or vapor phase.

Process for the isomerization of olefins

A halogen-containing alumina catalyst for the polymerization of olefins to liquid polymers containing a major proportion of polymers having a molecular weight higher than the trimers, said catalyst selectively polymerizing isobutene from a mixture of butenes to produce liquid polyisobutene having a molecular weight higher than about 280; said catalyst containing from about 2 to about 20 wt. % chlorine, bromine or a mixture thereof, and being prepared from an alumina having a purity of at least 99% and a surface area greater than about 150 m.sup.2 /g with at least 10% of the pores having a diameter higher than about 200 .ANG.; said preparation being effected by contacting the alumina with a dry gaseous stream comprising a halogenation agent consisting essentially of volatile chlorinated and/or brominated saturated oliphatic organic compound having a vapor pressure of at least 100 mm of Hg at a temperature of 200.degree.-230.degree. C. and having a low hydrogen content, together with a non-reducing gaseous carrier at a temperature from about 230.degree. to about 300.degree. C. during a period of time t in hours such that the ratio t/R, wherein R is the mole ratio of gaseous carrier to halogenation agent, ranges between about 0.35 and about 20.

Halogen-containing alumina catalysts prepared from alumina of at least

A process for producing isobutene, comprising contacting, at elevated temperatures, a feed containing propylene with a catalyst comprising a crystalline silica polymorph of the silicalite type in the presence of steam to recover a stream containing isobutene. The reaction can be carried out in either liquid or vapor phase.

Process for producing isobutene

Catalytic dehydrogenation of alkyl- or dialkyl- aromatic hydrocarbons such as ethylbenzene or ethyltoluene to vinyl aromatic hydrocarbons is achieved by passing the aromatic hydrocarbons on a crystalline silica which has been calcined under an inert atmosphere and which contains from about 0.05 to about 1 weight percent of an alkali metal oxide such as sodium oxide. In the preparation of the crystalline silica, limited washing of the crystalline silica precursor is performed to obtain an amount of alkali metal oxide remaining in the crystalline silica between about 0.05 and about 1 weight %.

Dehydrogenation process

A process for selectively producing liquid polyisobutene contacting a feed stream containing mixed butenes with a dry chlorinated alumina catalyst at a temperature of from about -15.degree. to about 50.degree. C. wherein the chlorinated alumina contains from about 2 to 20% by weight of chlorine and the alumina has a purity of at least 99% and a surface area greater than 150 m.sup.2 /g with at least 10% of the pores having a mean diameter larger than 200A and recovering polyisobutenes having a molecular weight between about 280 and 4000.

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Sint-Pieters-Leeuw, Belgium

Georges E De Clippeleir