Abstract: There is described an improved SRC reactor quench system using a condensed product which is recycled to the reactor and provides cooling by evaporation. In the process, the second and subsequent reactors of a series of reactors are cooled by the addition of a light oil fraction which provides cooling by evaporation in the reactor. The vaporized quench liquid is recondensed from the reactor outlet vapor stream.

Abstract: Catalytically active amorphous silicas are prepared by dehydrating a silica hydrogel or precipitate prepared from an acidified aqueous silicate solution containing an amine of pK.sub.a above 10 or a cation containing either a nitrogen or phosphorus atom bonded to four carbon atoms. The resultant amorphous silica is catalytically active for, among other chemical reactions, the isomerization of ortho-xylene and the cracking of hydrocarbons.

Abstract: A feedstock for carbon artifact manufacture is obtained by heat soaking a steam cracker tar or component thereof in a hydrogen atmosphere and thereafter removing 10% to 50% of the oils present therein, if any.

Abstract: An element selected from Groups IA, IB, IIB, IIIA and IIIB is incorporated into an iron bismuth molybdate oxide complex catalyst by impregnation.

Abstract: A feedstock for carbon artifact manufacture is obtained from a steam cracker tar by heat soaking the steam cracker tar or a vacuum stripped steam cracker tar with a polycondensed aromatic oil thereby providing a pitch suitable for carbon artifact manufacture.

Abstract: A fluid coking process is provided in which a catalyst comprising an alkaline earth metal ferrite is present in the fluid coking zone.

Abstract: A process is disclosed for upgrading a hydrocarbon oil feed having a significant content of metals, especially vanadium, to provide a higher grade of oil products by contacting the feed under sorbing conditions in an upgrading zone with a high surface area, high pore volume sorbent material containing an added alkaline metal to neutralize acidic cracking sites. Upgrading conditions are such that coke and metals are deposited on the sorbent in the upgrading zone. Coked sorbent is regenerated by contact with an oxygen containing gas under regeneration conditions to remove the coke, and regenerated sorbent is recycled to the upgrading zone for contact with fresh feed. The added alkaline metal is present on the sorbent in an amount sufficient to neutralize substantially all of the acidic cracking sites and provide a sorbent material having a MAT relative activity in the range of about 0 to about 1 percent.

Abstract: A method and apparatus for recovering oil from shale comprises forming a bed of oil bearing shale particles on a plurality of rotatable apertured cylindrical rollers having filler members in the nip between adjacent rollers; transporting the bed by rotating the rollers to frictionally engage the shale particles and transfer them onto and across the filler members to continuously agitate the particles as they are being transported at a velocity substantially lower than the circumferential velocity of the rollers; passing through the moving bed at spaced points a plurality of discrete streams of nonoxidizing gas heated to different temperatures sufficiently high to educe different weight fractions of oil from the kerogen in the shale as vapors into the gas streams; and separating the different weight oil fractions from the gas streams.

Abstract: An improvement in a method of preparing catalysts for the manufacture of maleic anhydride by oxidizing a saturated hydrocarbon. The catalyst is prepared by a process in which a catalyst precursor, containing tetravalent vanadium, is formed into agglomerates and calcined, the improvement being calcining the catalyst precursor at 325.degree.-375.degree. C. in the presence of oxygen and a saturated aliphatic hydrocarbon.

Abstract: A process is disclosed for decarbonization-demetallization of a poor quality residual oil feed boiling above about 650.degree. F. and comprising substantial Conradson carbon components to provide a higher grade of oil feed by contacting the poor quality oil feed with sorbent particle material containing one or more metal additives selected to catalyze the endothermic removal of coke with CO.sub.2. Sorbent decarbonization conditions are selected so that substantial quantities of carbonaceous material and metals are deposited on the sorbent in the decarbonizing zone. Sorbent material with metals and hydrocarbonaceous deposits is regenerated in the presence of an oxygen and carbon dioxide containing gas streams in separate sorbent regeneration zones at a temperature sufficiently elevated to remove residual coke to a desired low level. Regenerated sorbent particle material at an elevated temperature below about 1500.degree. F.

Abstract: The present invention provides a process which is adapted for cyclodimerization of 1,3-butadiene to 4-vinylcyclohexene under Diels-Alder conditions in the presence of a large-pore carbon molecular sieve.

Abstract: A process for liquefying and gasifying coal by thermal treatment in the presence of hydrogen gas for hydrocracking is disclosed. The process comprises a sequence of the following two steps:(1) coal fines are injected into a heated hydrogen gas stream at a pressure of from 35 to 250 kg/cm G such that they are rapidly heated to a temperature of from 750.degree. to 1100.degree. C. for thermal cracking thereof; and(2) the resulting liquid product is subjected to hydrocracking for a period of from 1.0 to 60 seconds at a temperature that is lower than the temperature used in the first step and which is in the range of from 570.degree. to 850.degree. C.

Abstract: The synthetic fuel slate of products derived from wet natural gas is expanded to include both aromatic gasoline from the methane rich dry gas portion via steam reforming to synthesis gas, the production of methanol from synthesis gas and the conversion of methanol to gasoline over a ZSM-5 type catalyst, plus high quality jet fuel, diesel fuel and lubricating oils from the C.sub.3.sup.+ paraffin rich fraction of wet natural gas via thermal cracking of the paraffin rich fraction to olefins and the conversion of the olefins to gasoline and distillate boiling range hydrocarbons over a ZSM-5 type catalyst. Methane separated from the thermal cracked product can be mixed with the dry gas fraction for synthesis gas production and a portion of the hydrogen from the synthesis gas may be used to hydrogenate the distillate fraction from the catalytic conversion of the thermal cracked product.

Abstract: Raw shale is supplied to a pyrolyzer where it is pyrolyzed by fuel gas and hot spent shale derived from a gasifier. Typically, the raw shale is Eastern U.S. shale and the pyrolyzer includes a fluidized bed. The pyrolyzed shale having given up its oil and volatile hydrocarbons, rises to the top of the fluidized bed of raw shale where it is transferred to the gasifier. Oxygen and steam are supplied to the gasifier. This composite gas reacts with the carbon of the pyrolyzed shale in a fluidized bed to produce synthesis or fuel gas. The oxygen is supplied in such quantities as not to react completely with the carbon in the pyrolyzed shale. The steam reacts with the excess of carbon. Predominantly hydrogen and carbon monoxide are produced; in addition there is a smaller quantity of carbon dioxide and methane. This hot fuel gas is transferred to the pyrolyzer. In addition, hot spent shale is transferred to the pyrolyzer. The hot fuel gas fluidizes the raw shale in the pyrolyzer.

Abstract: A method is described by which sour liquid hydrocarbon streams are sweetened by subjecting said streams to oxidizing conditions in the presence of a hydrocarbon soluble alkanolamine.

Abstract: A process is disclosed for treating hydrocarbon streams for the purpose of removing mercaptans and also converting the remaining mercaptans to disulfides which remain in the hydrocarbon stream being treated. The hydrocarbons rise through a contacting column countercurrently to a descending stream of an aqueous alkaline solution. A limited amount of an oxygen-containing gas is passed into an intermediate point in the column thereby dividing it into an upper sweetening section and a lower extraction section. The flow rate of the oxygen-containing stream is preferably low enough that any gas not consumed in the catalytic oxidation of mercaptans becomes dissolved in the hydrocarbon product stream, and preferably remains dissolved at atmospheric pressure.

Abstract: Process for the synthesis of the 3-keto-cyclopentene-5-oxy derivatives (rethrolones) having the general formula: ##STR1## wherein: R.sub.1 is hydrogen, saturated or unsaturated C.sub.1 -C.sub.10 alkyl.R.sub.2 is saturated or unsaturated C.sub.1 -C.sub.10 alkyl.R.sub.3 is hydrogen or benzoyl characterized as having insecticide activity.The process comprises as a basic operation the photoisomerization of a transenedicarbonylic intermediate to the corresponding cis form and then its cyclization to a rethrolone.

Abstract: A partially deactivated alkaline earth metal perovskite-containing catalyst is reactivated by contact with a reducing gas at reducing conditions. The reactivated catalyst is useful in hydrocarbon treating processes such as catalytic cracking and fluid coking.

Abstract: A petroleum cracking catalyst having thereon metals usually found in petroleum, e.g., iron, nickel and vanadium, is modified by addition of potassium to increase significantly the rate of hydrogen production when employing the thus-modified catalyst for cracking of petroleum.

Abstract: A fluid coking process is provided in which a catalyst comprising a perovskite comprising at least one transition metal cation is present in the fluid coking zone.