Abstract: A catalyst for the partial oxidation of an alcohol to a corresponding aldehyde. The catalyst includes a monolithic structured inert carrier and an active catalytic mixture of oxides of molybdenum and either chromium, vanadium, aluminum, iron, tungsten, manganese or mixtures thereof in a molar ratio of the molybdenum oxide to the other oxide or oxides of between 1 and 5. The catalyst has a reduced pressure drop compared to a particulate catalyst bed.

Abstract: A process for the preparation of carbonyl compounds by the oxydehydrogenation of (C.sub.1 -C.sub.4)-alcohols is carried out at a temperature from 400.degree. to 700.degree. C. in the presence of a silicate catalyst which has been doped with silver and silver ions. By means of the process carried out at relatively low temperatures, for example, are that high yields are achieved, the content of carbon monoxide is low and the product gas contains, apart from carbon dioxide, no further determinable by-products and has a low water/formaldehyde ratio.

Abstract: Conversion of alcohol to organic compounds which comprises contacting the alcohol with a heterogeneous catalyst composition comprising at least one member selected from the group consisting of(a) crystalline LnAl.sub.1.67+0.67X (B.sub.4 O.sub.10)O.sub.X, and(b) crystalline LnAl.sub.2.67+0.33Z (B.sub.4 O.sub.11)O.sub.Zwhere Ln is at least one transition element selected from the group consisting of Group IIIB of the Periodic Table, X is a number ranging from 0 to 1, and Z is a number ranging from 0 to 2, each crystalline phase having a characteristic X-ray diffraction pattern.

Abstract: A process for the preparation of carbonyl compounds by oxidation of alcohols in the gas phase with a gas containing oxygen in the presence of catalysts containing copper or silver and a phosphorus compound that is volatile under the conditions of the reaction, the ratio of the mass of phosphorus to the mass of the alcohol being less than 0.5 ppm.

Abstract: A method for the ultrasonic treatment of dilute alcoholic solution in which a vibrator member placed in a dilute alcoholic solution is subjected to ultrasonic vibrations to produce cavitation in the solution in such a way that alcohol in the solution is vaporized and collected in a high concentration. The alcohol may be readily converted into a corresponding aldehyde.

Abstract: An aqueous formaldehyde solution having a formaldehyde concentration of 37 to 60% by weight is produced with less consumption of methanol under methanol-rich mild reaction conditions from a feed gas containing methanol, air, and steam, and, if necessary, an inert gas by subjecting the feed gas to catalytic reaction over a silver catalyst, contacting the resulting product gas with absorbing water, thereby absorbing the formaldehyde into the absorbing water from the product gas in an absorption column, and recovering the desired aqueous formaldehyde solution as bottoms of the absorption column, wherein a total of a corresponding amount of water to that of steam to be added to the feed gas and a necessary amount of water for adjusting the concentration of the product aqueous formaldehyde solution is added to the top of the absorption column as the absorbing water, and an aqueous solution containing 0.1 to 3.0% by weight of methanol and 0.1 to 1.

Abstract: Formaldehyde is prepared by (a) passing a mixture of methanol and water with a concentration of between 50 and 90% by weight, based on the total weight of the two substances, of methanol into a packed column which possesses a packing having a total layer thickness of not less than 50 cm and a total surface area of not less than 0.5 cm.sup.2 per cm.sup.3 of packing, a liquid circulation of from 15 to 90 g/min per g/min of methanol fed to the column, and a concentration of from 10 to 45% by weight of methanol in the recycle liquid, the temperature at the point of entry of the recycle liquid in the column being from 50.degree. to 86.degree. C. and the bottom temperature being 10.degree.-25.degree. C. lower than this, i.e. from 40.degree. to 70.degree. C., (b) separating off methanol and water from the column by stripping with air, an inert gas and/or exit gas, the throughput being from 0.5 to 3 tonnes of methanol and water per hour per m.sup.

Abstract: In a process for producing chemical substances comprising steps of cooling, condensing and solvent-absorbing the reaction product gas having a high temperature formed in a reactor, an absorption type refrigerator or an absorption type heat pump is driven by using, as the driving source, a heat source having such a temperature as not to be advantageous for the heat exchange in the process, which heat source has been taken out of the steps of cooling the reaction product gas, condensing it or solvent-absorbing it to obtain a refrigerant or a hot water having a temperature higher than the temperature of the heat source, and the refrigerant or the hot water is used as a cooling source or a heating source in the steps comprised in said process for producing chemical substances.

Abstract: A process for the ammoxidation of methanol or formaldehyde to hydrogen cyanide or oxidation of methanol to formaldehyde using a catalyst comprising boron and phosphorus oxides, wherein the boron to phosphorus atomic ratio is 0.8:1 to 1.25:1.

Abstract: Methanol is converted to formaldehyde by oxidative dehydrogenation using as catalyst sputtered or ion plated silver or silver/gold alloy on an inert hard, nonporous support.

Abstract: Formaldehyde manufacture by oxidative-dehydrogenation of methanol over a silver or copper catalyst. Aqueous formaldehyde solution is obtained from the reaction and is stripped of a mixture of methanol, formaldehyde and water by a low energy process at relatively low temperature and low reflux in a still comprising at least about 1.5 theoretical plates, the stripping conditions being selected to allow substantial reduction of the methanol content of the aqueous formaldehyde solution and recycle of the methanol to the reactor.

Abstract: The invention relates to a process for purifying, by treatment with an acid ion exchanger and, if desired, a basic ion exchanger, the methanol employed in the preparation of formaldehyde.

Abstract: In a process for oxidizing methanol to formaldehyde which comprises passing the methanol with molecular oxygen through two sequential silver-based catalysts, with the second of said catalysts being a bed of particulate silver such as, specifically, silver crystals, the process efficiency, and especially the efficiency of the reaction taking place in the second catalyst bed, is improved by controlling (a) the ratio of formaldehyde to methanol in the reactant gases entering the second catalyst bed and (b) the specific reaction rate in said second bed. The specific reaction rate is defined as the quantity of methanol converted in said second bed per unit time per unit of cross-sectional area of the bed.

Abstract: A process for converting methanol to formaldehyde at 450.degree. to 750.degree. C. using as catalyst silver, silver-gold alloys or copper-gold alloys in which from 0.001 to 15 parts per million, based on methanol, of phosphorus or phosphorus from a phosphorus compound is present.

Abstract: A process for the oxidative dehydrogenation of methanol to form formaldehyde using silver crystals as catalyst which silver crystals are supported on a screen formed of an alloy containing at least 20 weight percent gold and the remainder silver is disclosed.

Abstract: Alcohols such as those containing from about 1 to about 10 carbon atoms may be converted to aldehydes by treating the alcohols with an oxygen-containing gas such as air or oxygen in the presence of a catalyst comprising at least two oxides of metals selected from the group consisting of molybdenum, tungsten, cobalt, nickel, manganese, iron and chromium, at least one of said oxides being molybdenum oxide or tungsten oxide composited on a high surface area support. The conversion reaction may be effected at a temperature ranging from about 200.degree. to about 400.degree. C. and a pressure in the range of from about atmospheric to about 50 atmospheres. By employing this particular catalyst, good conversion rates and high selectivity to the aldehydes will be obtained.

Abstract: New catalysts comprising lead and silver on supports having relatively low surface areas and their use have been found to be useful in the oxidative dehydrogenation of methanol to formaldehyde at elevated temperatures.

Abstract: This invention is concerned with catalysis. More especially, the invention relates to catalytic metal or alloy or both in a form having enhanced catalytic properties, and to the use thereof in catalytic processes. In more detail a catalyst or catalyst substrate according to the invention comprises at least one metal and/or alloy body made by a melt spun or a melt extraction process.

Abstract: Lead-silver catalysts have been found to be useful in the production of formaldehyde by oxidative dehydrogenation of methanol vapor with an oxygen-containing gas at elevated temperatures.

Abstract: A process for preparing a granular, supported silver catalyst by: contacting refractory porous granules having a tap volume of about 1 to 2 grams per cubic centimeter with water or a water soluble liquid having a boiling point of less than about 150.degree. C. so as to wet said granules and to absorb water or said soluble liquid within peripheral pores of said granules; contacting the wet granules with an ammoniated solution containing a silver salt which decomposes on calcination at a temperature below about 600.degree. C. and a fatty acid having from about 12 to 22 carbon atoms, the quantity of silver salt in said solution being sufficient to provide a metallic silver deposit onto said granules of from about 1 to 10% by weight of said dry granules; drying the silver solution on the granules, and heating the dried granules at a temperature sufficient to decompose the dried silver compounds to metallic silver.

Abstract: In catalytically oxidizing methanol in the vapor phase according to already-known processes for the production of formaldehyde, the hot formaldehyde-containing gaseous effluent of the catalytic converter is rapidly cooled by being passed through the tubes of a heat exchanger which are filled with balls composed of a solid which is substantially inert toward formaldehyde. As compared with a similar cooling system in which the tubes are empty or in which enhancement of heat transfer is attempted by using metal heat-transfer enhancement devices such as twisted metal ribbons, the present method affords reduced post-reaction decomposition of formaldehyde while at the same time allowing use of a relatively high temperature on the shell side of the heat exchanger whereby it becomes possible to raise steam at a pressure higher than that characteristic of the prior art.

Abstract: Formaldehyde manufacture by oxidative-dehydrogenation of methanol over a silver or copper catalyst. Aqueous formaldehyde solution is obtained from the reaction and is stripped of methanol and water by a low energy process at relatively low temperature by means of recycled inert gas in a stripping column comprising at least about 1.5 theoretical transfer units for stripping methanol.

Abstract: A process for converting methanol to formaldehyde wherein methanol along with a stream containing air, water, methanol and formaldehyde is fed to a primary reactor 5 containing a silver catalyst maintained at from 630.degree. to 650.degree. C. The effluent from the primary reactor 5 is cooled and fed along with a stream containing air, water, methanol and formaldehyde to a secondary reactor 9 containing a metal oxide catalyst, such as iron oxide-molybdenum oxide. The secondary reactor 9 is maintained at from 325.degree. to 400.degree. C. The product from the secondary reactor is fed to an absorber 11 which is cross connected top and bottom with a stripper 13. Water is fed to the absorber to absorb formaldehyde and the product solution of formaldehyde and water is removed from the absorber. Air is fed to the stripper and the effluent from the stripper which contains air, water, methanol and formaldehyde is fed to both the primary reactor 5 and the secondary reactor 9.

Abstract: The present invention is a reactor that consists of a single shell that contains a reaction zone and a regeneration zone. The reaction zone and regeneration zone are arranged in such a manner that (a) a particulate solid may be transferred by flow of gases from the regeneration zone to the reaction zone by a first route and then back to the regeneration zone by a second route; and (b) the gases passing through the regeneration zone are not transferred to the reaction zone and the gases passing through the reaction zone are not transferred to the regeneration zone.

Abstract: A catalyst supporting bed in a vertical reactor for production of formaldehyde by gas phase catalytic dehydrogenation of methanol in the presence of a solid metal catalyst, characterized in that the bed is made of a nickel alloy having a nickel content of not less than 25% by weight at least at the surface.

Abstract: This invention relates to the production of formaldehyde and to catalysts which may be used therefore. In more detail the invention relates to a process for the production of formaldehyde from methanol includes the passage, at an elevated temperature, of a gas stream containing methanol and oxygen through a catalyst, the catalyst comprising a monolithic support provided with channels for passage therethrough of the gas stream and with the channel wall surfaces coated or impregnated with one or more elements selected from the group consisting of copper, silver, gold and iron.

Abstract: This invention relates to the production of formaldehyde and to catalysts therefor.In particular the inventor relates to a process for the production of formaldehyde from methanol including the passage, at an elevated temperature, of a gas stream containing methanol and oxygen through a catalyst, the catalyst comprising a monolithic support provided with channels for passage therethrough of the gas stream and with the channel wall surfaces coated or impregnated with one or more elements selected from the group consisting of copper, silver, gold and iron.