摘要:
This invention discloses an integrated process of alkylation of olefins and regeneration of spent sulfuric acid. The alkylation of olefins may be replaced by nitration of toluene or by chlor-alkali process. The sulfuric acid is used as a catalyst or a absorbent, and the spent sulfuric acid is regenerated in situ and is recycled in the alkylation of olefins, nitration of toluene or chlor-alkali processes.
摘要:
A process is disclosed for reactivating an agglomerated iridium and selenium containing catalyst and particularly platinum-iridium-selenium on alumina reforming catalysts. The process includes a reducing step involving contacting a decoked agglomerated catalyst with a reducing gas such as hydrogen to reduce agglomerated iridium oxides to the free metal, a hydrogen halide pretreatment step to provide a halide level to the catalyst of about 1.3 weight percent, and an elemental halogen/oxygen or wet oxygen redispersion step. The hydrogen halide pretreatment step is performed under elemental oxygen-free conditions prior to redispersion and allows high iridium redispersion values to be obtained. If no iridium oxides are initially present, the hydrogen step is optional.
摘要:
Carbonyl sulfide is removed from propylene by hydrolysis over a catalyst comprising platinum sulfide on alumina. Specifically, the propylene is passed through, successively, a C.sub.3 -splitter, a heater, the platinum sulfide catalyst bed, and a topping still where the resulting H.sub.2 S and CO.sub.2 are separated from the purified propylene.
摘要:
In a method of removing carbonyl sulfide from propylene by hydrolysis over a catalyst comprising platinum sulfide on alumina, the improvement comprising regenerating the catalyst by contacting the catalyst with a solvent for polypropylene under conditions such that any polypropylene on the catalyst will be readily dissolved. Specifically, the propylene is passed through, successively, a C.sub.3 -splitter, a heater, the platinum sulfide catalyst bed, and a topping still where resulting H.sub.2 S and CO.sub.2 are separated from the purified propylene. A preferred solvent is liquid propylene.
摘要:
A process for reactivating supported catalysts which contain palladium, copper and tellurium and which are used for the acyloxylation of unsubstituted or substituted butadiene to give butenediol esters, wherein the supported catalysts are heated at from 200.degree. to 900.degree. C. in the presence of a gas which is inert under these treatment conditions.
摘要:
A process for separating selenium, selenium compounds, sulfur and/or sulfur compounds from urethanes containing these elements and/or compounds by reacting said urethanes with an aqueous permanganate solution and then separating the resulting phase system.
摘要:
A process for regenerating a deteriorated iron-antimony oxide containing catalyst comprising as essential components (i) iron, (ii) antimony, (iii) at least one element selected from the group consisting of vanadium, molybdenum and tungsten and (iv) tellurium, having the crystalline structure of an iron-antimony oxide compound, being substantially free of free antimony trioxide (Sb.sub.2 O.sub.3) and containing at least 50 wt % of the original tellurium content of the fresh catalyst which comprises calcining said catalyst under a non-reducing atmosphere at a temperature of from about 600.degree. to 950.degree. C. and in the vicinity of or lower than the final calcining temperature used for producing the catalyst.
摘要翻译:一种用于再生含铁氧化锑的催化剂的方法,其包含作为必要组分(i)铁,(ii)锑,(iii)至少一种选自钒,钼和钨的元素和(iv)碲, 具有铁 - 氧化锑化合物的结晶结构,基本上不含游离的三氧化锑(Sb 2 O 3),并且含有至少50重量%的新鲜催化剂的原始碲含量,其包括在非还原气氛下煅烧所述催化剂 温度为约600℃至950℃,并且在用于制备催化剂的最终煅烧温度附近或以下。
摘要:
A process for producing a catalyst comprising an antimony-containing oxide which comprises the steps of (A) calcining a mixture of metal oxides containing, as essential components, an oxide of antimony and an oxide of at least one metal selected from the group consisting of iron, cobalt, nickel, manganese, uranium, tin and copper, said calcining being at temperatures of from about 500.degree. C to about 1000.degree. C; (B) impregnating with or spraying onto said calcined mixture of metal oxides (a) an aqueous solution or a suspension containing (1) at least one compound of a metal selected from the group consisting of molybdenum, vanadium and tungsten, said metal compound being thermally convertible to an oxide of said metal, and (2) a tellurium compound, said tellurium compound being thermally convertible to a tellurium oxide, or (b) an aqueous solution or a suspension containing said metal compound (1) and an aqueous solution or a suspension containing said tellurium compound (2); (C) drying said impregnated or sprayed mixture of metal oxides and (D) calcining said dried mixture of metal oxides at a temperature of from about 400.degree. C to about 850.degree. C, wherein said calcining (D) is at a temperature lower than said calcining (A).
摘要:
Disclosed in a process by which consumption of sulfuric acid alkylation catalyst is decreased and alkylate yield is increased by reacting the hydrocarbon contaminats contained within spent alkylation acid with an isoparaffin to yield alkylate and sulfuric acid. Ultrasonic energy is utilized to obtain intense mixing to promote the reaction of the contaminats with the isoparaffin in the acid phase. The resulting dispersion is more stable that emulsions obtained from mechanical mixing and affords a high surface area between the hydrocarbon and acid phases for increased alkylate formation and acid regeneration.