Abstract: Process for the preparation of ethylidene diacetate and/or ethyl acetate by hydrogenating acetic anhydride in the presence of a homogeneous ruthenium catalyst, methyl iodide and, optionally, lithium iodide. The process can also be utilized to hydrogenate mixtures of acetic anhydride and ethylidene diacetate to produce ethyl acetate.
Abstract: In a process for the recovery of acetic acid by extracting acetic acid from an aqueous acetic acid solution containing a metallic salt of sulfuric acid with an organic extractant comprising a tertiary amine and an organic diluent and recovering acetic acid from the liquid extract, a mixture of a tertiary amine containing sulfuric acid and an organic diluent is used as an organic extractant so as to suppress energy consumption and to increase extraction efficiency.
Type:
Grant
Filed:
May 14, 1986
Date of Patent:
November 28, 1989
Assignee:
Daicel Chemical Industries, Ltd.
Inventors:
Kunio Koga, Koji Shima, Mutsumi Samejima
Abstract: A process for the preparation of ethyltrifluoroacetoacetate is provided. In this first step, ethyltrifluoroacetate is condensed with ethyl acetate in the presence of sodium ethoxide in cyclohexane. In a second step, the condensation product is neutralized with a protonic acid, such as formic acid, to release an enol. In the third step, the ethyltrifluoroacetoacetate obtained is separated by distillation. The ethyltrifluoroacetoacetate is used as an intermediate in syntheses in the pharmaceutical or plant protection industry.
Abstract: A process is provided for the oxydehydrogenation of saturated carboxylic acids or a lower alkyl ester thereof with oxygen in the presence of iron phosphorus oxide catalysts containing promoters selected from the group Ag, Al, B, Be, Cd, Co, Cu, Ga, Ge, In, Mn, Ni, Te, Th, Ti, Tl, U, V, Zn, Zr, rare earths and mixtures thereof.
Type:
Grant
Filed:
August 17, 1982
Date of Patent:
September 5, 1989
Inventors:
S. Erik Pedersen, James L. Callahan, Harley F. Hardman
Abstract: A carboxylic acid of formula RCO.sub.2 H where R is a C.sub.1 to C.sub.10 aliphatic hydrocarbyl group is prepared by heating under substantially anhydrous conditions an ester of formic acid of formula HCO.sub.2 R where R is as defined above in the presence of carbon monoxide and an effective amount of a catalyst system comprising a Group VIII metal, a halide and a compound containing a quaternary Group V atom. The quaternary Group V atom can be formed in situ by adding a compound containing a trivalent nitrogen, phosphorus or arsenic atom quaternizable under the reaction conditions and a quaternizing agent. Acetic acid is prepared by heating methyl formate in the presence of a catalyst system containing a rhodium compound, an iodide and a quaternary nitrogen-containing heterocyclic base.
Abstract: Methyl formate is produced continuously by reacting methanol in the liquid phase with molecular oxygen in the presence as catalyst of a soluble chromium compound which can be deliberately added or can result from corrosion of a reaction vessel fabricated in stainless steel or other chromium-containing metal alloy. Initiation of the oxidation can be accomplished by feeding a material more susceptible to oxidation than methanol, either with or without methanol, and optionally in the presence of a soluble chromium compound.
Abstract: A process is disclosed for producing vinyl acetate from methanol, carbon monoxide and hydrogen which comprises the following five steps:(a) methanol is hydrocarbonylated in a hydrocarbonylation zone to produce ethanol, acetaldehyde, methyl acetate and dimethylacetal, and the products are separated in a separation zone;(b) methyl acetate is carbonylated in a carbonylation zone to produce acetic anhydride;(c) the acetaldehyde and dimethylacetal produced in the step (a) and the acetic anhydride produced in the step (b) are converted to ethylidene diacetate and methyl acetate; (d) the ethylidene diacetate produced in the step (c) is thermally decomposed to vinyl acetate and acetic acid, and the products are separated in a separation zone; and(e) the methyl acetate produced and separated in the step (a), (c) or (d) is supplied to the carbonylation step (b).
Abstract: Acrolein and acrylic acid are produced by vapor-phase catalytic oxidation of propylene in a multi-tubular, fixed-bed reaction vessel with the use of a composite oxide catalyst represented by the formula Mo.sub.a Bi.sub.b Fe.sub.c A.sub.d B.sub.e C.sub.f D.sub.g Si.sub.h O.sub.x, wherein A, B, C, and D represent components selectable from respective groups of elements, and the subscripts a through h and x are specific numbers of atoms of respective elements and groups of elements. This catalyst is adapted and packed in each reaction tube in a manner such that its activity is controlled to increase from the inlet toward the outlet of the tube.
Type:
Grant
Filed:
September 23, 1982
Date of Patent:
June 6, 1989
Assignee:
Mitsubishi Petrochemical Company Ltd.
Inventors:
Koju Kadowaki, Kohei Sarumaru, Takeshi Shibano
Abstract: Allyl formate is substantially selectively converted to isobutyric acid, n-butyric acid and/or glutaric acid by bringing the alyl formate into contact with activated carbon in the presence of carbon monoxide, water and formic acid and a halide promoted group VIII soluble metal catalyst optionally in the presence of a solvent. Isobutyric and n-butyric acids are preferentially formed in the presence of relatively low concentrations of water and formic acid whereas glutaric acid is preferentially formed in the presence of relatively higher concentrations of water and formic acid.
Abstract: Esters of carboxylic acids of the formula RCH.sub.2 COOR"' and R'CH:C(R")COOR"' are reacted to form a carboxylic acid and an aliphatic alcohol R"'OH wherein R, R', and R" are individually selected from the group consisting of --H, alkyl moieties of from 1 to 18 carbon atoms and aralkyl moieties, cycloalkyl moieties and alkylaryl moieties of 3 to 18 carbon atoms and R"' is an alkyl moiety of 1 to 18 carbon atoms in the presence of an AMS-1B borosilicate crystalline molecular sieve catalyst under reaction conditions.
Abstract: A process for the disproportionation of olefins comprising contacting said olefins under suitable reaction conditions with a neutral-carbene complex catalyst and then using anhydrous ammonia to effect separation of the catalyst and the organic products.
Abstract: The present invention provides a process for the production of methacrolein and methacrylic acid by the gas phase catalytic oxidation of isobutylene or t-butanol at high temperature using molecular oxygen in the presence of catalyst consisting of molybdenum, tungsten, bismuth, iron, nickel, antimony, and an alkali metal, to which zinc or lead is added, and further phosphorus sulfur, silicon, selenium, germanium or boron, and magnesium, cobalt, manganese or tin are added.
Abstract: A process for preparing carbonate esters by the oxidative carbonylation of an alcohol is provided. The process comprises reacting an alcohol with carbon monoxide in the presence of a dihydrocarbyl peroxide the process being characterized by the fact that the carbon monoxide pressure at the reaction temperature is less than 15 bars and by the fact that a catalyst comprising a platinum group metal and a copper compound is employed. The process is useful for preparing dimethyl carbonate from methanol and carbon monoxide.
Abstract: Alkylidene diesters such as ethylidene diacetate are selectively produced in high yields by reacting an ether and/or an ester under substantially anhydrous conditions with carbon monoxide and hydrogen in contact with a catalyst system comprising a rhodium compound, a halogen component, a palladium cocatalyst and a promoter component which is an agent for liberation of carboxylic acid anions. The process is carried out in the liquid phase in a solvent comprising a carboxylic acid at a temperature in the range of 150.degree. to 190.degree. C. and at a carbon monoxide partial pressure in the range from about 1.0 to 1100 kg/cm.sup.2 and a carbon monoxide/hydrogen mole ratio of 6:1 to 1:2 for the ester reaction and 10:1 to 1:2 for the ether reaction. When ethylidene diacetate is the product, it can then be decomposed to produce vinyl acetate and acetic acid by well-known techniques.
Abstract: A process is disclosed for preparing compounds such as 4-acetoxybutyraldehyde which comprises contacting reactants such as allyl acetates with a cobalt carbonyl catalyst in the presence of various novel promoters. The promoters are selected from the group consisting of triphenyl germane, tetraphenyl germane, phenyl sulfide, succinonitrile and 2,2'-dipyridyl. The reaction is preferably conducted in the presence of a ketone solvent.
Abstract: 1,4-Diacyloxybut-2-enes and 3,4-diacyloxybut-1-enes are converted into one another in the gas phase or liquid phase at from 100.degree. to 350.degree. C. under atmospheric or superatmospheric pressure in the presence of a zeolite as a catalyst.
Type:
Grant
Filed:
July 23, 1984
Date of Patent:
February 21, 1989
Assignee:
BASF Aktiengesellschaft
Inventors:
Wolfgang Hoelderich, Rolf Fischer, Otto Hertel, Wolf D. Mross, Hans-Martin Weitz
Abstract: Disclosed is a process for producing methacrylic acid from methacrolein in high yields and at high selectivity which comprises vapor phase catalytic oxidation of methacrolein with molecular oxygen, characterized by using a catalyst represented by the formula: P.sub.a Mo.sub.b V.sub.c Cu.sub.d Zn.sub.e A.sub.f B.sub.g C.sub.h D.sub.i O.sub.
Abstract: A catalyst represented by the general formulaP.sub.a Mo.sub.b V.sub.c Fe.sub.d Cu.sub.e Z.sub.f X.sub.g Y.sub.h O.sub.iwherein X represents at least one or more of the elements selected form the group consisting of potassium, rubidium, cesium and thallium, Y represents at least one or more of the elements selected from the group consisting of tellurium, lanthanum, boron, silver, chromium, magnesium and barium, Z represents any one of the elements of zirconium or antimony, a to i denote atomic ratios of respective elements, and when b=12, a=0.3-4, c=0.01-3, d=0.01-4, e=0.01-3, f=0.01-3, g=0.01-3, h=0.001-5 and i denotes the number of oxygen atoms required for satisfying the valence number of the said ingredients, and a process for the production of methacrylic acid comprising contacting methacrolein in vapor phase in the presence of said catalyst.
Abstract: .delta.-Formylvalerates are prepared by a process wherein a 3-pentenoate is treated with an isomerization catalyst at elevated temperatures and a 4-pentenoate is distilled off, and the resulting 4-pentenoate is reacted with carbon monoxide and hydrogen at from 80 to 160.degree. C. under from 1 to 30 bar in the presence of a rhodium carbonyl complex which has been modified with tertiary organic phosphines or phosphites.
Type:
Grant
Filed:
May 9, 1984
Date of Patent:
January 31, 1989
Assignee:
BASF Aktiengesellschaft
Inventors:
Heinz-Walter Schneider, Rudolf Kummer, Volker Taglieber
Abstract: Described is a process for preparing 4,4A,5,6-tetrahydro-7-methyl-2-(3H)-naphthalenone having the structure: ##STR1## and intermediates useful in such process defined according to the structure: ##STR2## wherein one of R.sub.3 or R.sub.4 is hydrogen and the other of R.sub.3 or R.sub.4 is acetyl; and one of R.sub.1 or R.sub.2 is methyl and the other of R.sub.1 or R.sub.2 is acetoxy, said compound defined according to the structure: ##STR3## being useful in augmenting or enhancing the aroma or taste of consumable materials including foodstuffs, chewing gums, medicinal products, chewing tobaccos, toothpastes, smoking tobaccos, smoking tobacco articles, perfumes, colognes and perfumed articles including solid or liquid anionic, cationic, nonionic or zwitterionic detergents, fabric softeners, fabric softener articles and perfumed polymers.
Type:
Grant
Filed:
April 15, 1982
Date of Patent:
December 27, 1988
Assignee:
International Flavors & Fragrances Inc.
Inventors:
Alan O. Pittet, Ranya Muralidhara, Myrna L. Hagedorn