Abstract:
A process for coal gasification whereby coal is converted to carbon monoxide, hydrogen and other gaseous products by contact with molten sodium sulfate, said sodium sulfate being reduced to sodium sulfide, which is regenerated with oxygen to sodium sulfate to provide a cyclic process.
Abstract:
A method for the preparation of 1,3-dimethyl substituted polycyclic aromatic compounds which comprises (1) subjecting a compound of structure
Abstract:
PROCESS OF DEHYDROCYCLIZING C6-C10 HYDROCARBONS HAVING AT LEAST A C6 BACKBONE USING A LI,NA OR K ZEOLITE X OR Y OR FAUJASITE IMPREGNATED WITH 0.3 TO 1.4 PERCENT PT AT FROM 500 TO 560*C. AND PREFERABLY 510 TO 550*C. USING A PARTIAL PRESSURE OF H2 OF FROM 10 TO 300 P.S.I. AND PREFERABLY 50 TO 200 P.S.I. TO FORM BENZENE AND ALKYLBENZENES. OPTIONALLY THE CATALYST CAN BE TREATED WITH CHLORINE SO THAT IT CONTAINS FROM 0.3 TO 1.5 WEIGHT PERCENT CHLORINE WHICH IMPROVES THE EFFECTIVESS OF THE CATALYST.
Abstract:
AN IMPROVED METHOD FOR THE PREPARATION OF 2,3-DIMETHYLBUTANE ADMIXED WITH A BRANCHED C8 ALKYLATE MIXTURE BY SULFRIC ACID ALKYLATION IS PROVIDED IN A TWO-STAGE PROCESS WHEREIN ISOBUTYLENE ARE CO-DEMERIZED IN THE PRESENCE OF ISOBUTANE AND SULFRIC ACID UNDER REACTION CONDITIONS WHICH FAVOR THE FORMATION OF 3,3-DIMETHYL-1-BUTYL SULFATE, AND THEREAFTER THE SAID 3,3-DIMETHYL-1-BUTYL SULFATE IS REACTED WITH THE ISOBUTANE UNDER CONDITION WHICH FAVOR THE FORMATION OF 2,3-DIMETHYLBUTANE. THIS PROCESS IS ADVANTAGEOUS IN THAT IT PERMITS THE INCORPORATION OF ETHYLENE INTO A SULFRIC ACID ALKYLATION REACTION WITHOUT THE FORMATION OF LARGE AMOUNTS OF UNWANTED ETHYL SULFATE.
WHERE R1 AND R2 AR HYDROGEN OR HYDROCARBYL RADICAL HAVING 1 TO 20 CARBON ATOMS, Q REPRESENTS A DIVALENT AROMATIC SUBSTITUTE ETHER RADICAL HAVING 6 TO 20 CARBON ATOMS, AND N REPRESENTS THE NUMBER OF SUCH REPETING UNITS WHICH ARE PRODUCED. THESE THERMOPLASTIC RESINS ARE VALUABLE IN THE MANUFACTURE OF MOLDED AND EXTRUDED ARTICLES.
Abstract:
WHERE R1 AND R2 ARE HYDROGEN OR HYDROCARBYL RADICAL HAVING 1 TO 20 CARBON ATOMS, AR REPRESENTS A DIVALENT AROMATIC HYDROCARBON RADICAL AND N REPRESENTS THE NUMBER OF SUCH REPEATING UNITS WHICH ARE PRODUCED. THESE THERMOPLASTIC RESINS ARE VALUABLE IN THE MANUFACTURE OF MOLDED AND EXTRUDED ARTICLES.
PHENYLENE)-O-SO2-AR-SO2)N- -(O-(1,4-PHENYLENE)-(1-R1,5-R2-ADAMANTAN-7,3-YLENE)-(1,4- NOVEL SOLID POLYSULFONATES HAVING THE STRUCTURE:
Abstract:
A PROMOTED POLYMERIZATION OF ISOBUTENE TO FORM A POLYISOBUTENE OIL HAVING A VISCOSITY INDEX OF FROM 95 TO 130, USING PHOSPHORUS TRICHLORIDE OR PHOSPHORUS OXYCHLORIDE AS THE PROMOTER, STANNIC CHLORIDE AS THE CATALYST, AND NITROMETHANE AS THE SOLVENT AT FROM -30*C. TO 100*C. AND PREFERABLY FROM 0*C. TO 50*C. THE STANNIC CHLORIDE IS PRESENT IN FROM 0.1 TO 40 AND PREFERABLY 1 TO 20 VOLUME PERCENT AS BASED ON NITROMETHANE AND PHOSPHORUS COMPOUND IS PRESENT IN A VOLUME RATIO OF FROM 0.1:1 TO 5:1 PHOSPHORUS COMPOUND:STANNIC CHLORIDE.
Abstract:
Adamantane hydrocarbons of the C10-C30 range having one to four open bridgehead positions are ethylated by the reaction of a mixture of boron fluoride etherate and sulfuric acid (90-100 percent H2SO4 equivalent by weight) or fluorosulfonic acid (HFSO3) at a temperature in the range of -10* to 100* C. During the reaction, the adamantane nucleus remains intact and any alkyl groups attached thereto in the adamantane hydrocarbon charge remain at the original position. Ethylation occurs only at bridgehead positions of the nucleus and from one to four alkyl or cycloalkyl groups can be substituted if such bridgehead positions are open in the starting hydrocarbon. The ethylation product has one or more ethyl substituents than the starting hydrocarbon, which substituents are attached to the adamantane nucleus at bridgehead positions.
Abstract translation:具有一至四个开放桥头位置的C10-C30范围的金刚烷烃通过氟化硼醚合物和硫酸(90-100%H 2 SO 4当量重量)或氟磺酸(HFSO 3)的混合物在温度为 在-10℃至100℃的范围内。在反应过程中,金刚烷核保持完整,金刚烷烃电荷中附着的任何烷基保留在原始位置。 乙酰化仅在核的桥头位置发生,并且如果起始烃中的这种桥头位置是开放的,则1-4个烷基或环烷基可被取代。 乙基化产物与起始烃具有一个或多个乙基取代基,该取代基在桥头位置连接到金刚烷核上。
Abstract:
An improved method of lubrication of a controlledslip differential comprises using a lubricant comprising a static friction reducing amount of an aliphatic phosphate ester and a hydrocarbon base stock having a kinematic viscosity at 210*F. in the range of 1.5-200.0 c.s. and containing a major amount of a hydrogenated polymer of C3-C12 olefin, such as a ''''true'''' isobutylene oligomer or of a blend of at least one C13-C29 naphthene and from 0.1-20 parts by weight, based on said naphthene of at least one member from at least one of the following groups (a), (b), (c) and (d): A. A SYNTHETIC LIQUID C3-C8 olefin homopolymer copolymer, or terpolymer; B. A MEMBER FROM GROUP (A) ABOVE WHICH IS AT LEAST PARTIALLY HYDROGENATED; C. A SEVERELY HYDROREFINED NAPHTHENIC LUBE CONTAINING LESS THAN 1% OF GEL AROMATIC HYDROCARBONS; AND D. A SEVERELY HYDROREFINED PARAFFINIC LUBE CONTAINING LESS THAN 1% OF GEL AROMATIC HYDROCARBONS; AND WHEREIN THE AMOUNT OF SAID BLEND WHICH IS PRESENT IN SAID BASE STOCK IS SUFFICIENT TO PROVIDE A GREATER COEFFICIENT OF TRACTION, MEASURED AT 600 FT./MIN., 200*F., 400,000 p.s.i., than would be provided by substitution of the same amount of ASTM Oil No. 3 for said blend in said base stock. The preferred lubricant also contains an extreme pressure additive (e.g. tricresyl phosphate).
Abstract:
A process for preparing 2-pyrrolidone which comprises reacting maleic acid or maleic anhydride with hydrogen and ammonia in an aqueous system at a mole ratio of ammonia to acid or anhydride of from 1.0:1 to 1.2:1, at a temperature of from about 200* to about 300*C, at a pressure of from about 1,000 to about 3,000 psig, for a time of about 0.5 to about 8 hours, and in the presence of a catalyst of palladium supported on carbon.