首页> 外国专利> 2- kuroro -1,1,1,2,3,3,3- heputahuruoropuropan, hexa- fluoro propene and method in order to produce 1,1,1,2,3,3,3- heputahuruoropuropan

2- kuroro -1,1,1,2,3,3,3- heputahuruoropuropan, hexa- fluoro propene and method in order to produce 1,1,1,2,3,3,3- heputahuruoropuropan

机译:2-Kuroro-1、1、1、2、3、3、3-Heputa Furuoro Propan,He fuuro丙烯和中性祖斯1,1,1,2,3,3,3-Heputa Furu Oropuropan

摘要

(A) the hydrogien fluoride, the halo propene of chlorine and formula CX3 CCl=CX2 and the halo propane of formula CX3 CClYCX3 (in formula, each X becoming independent, is F or Cl, it designates that the quantity of X and Y where Y is H, Cl or F, however, is F at total is 6 or less as a condition) at least including a kind of is selected from the group which consists of starting material, making the blend which becomes the chloridation fluorine conversion catalyst contact inside the reaction limits, CF3 CClFCF3, including HCl, HF and the too small fluorine conversion halogenation hydrocarbon intermediate field, the product which becomesMethod in order to produce 2- kuroro -1,1,1-3,3,3- heputahuruoropuropan which includes the fact that the blend is formed is disclosed. The entire quantity of the chrome atom in the aforementioned oxidation alpha chrome crystal lattice where this method is substituted, being the (i) crystalline oxidation alpha chrome, at least 0.05 atmoic % the nickel of the chrome atom in the oxidation alpha chrome crystal lattice, the trivalent cobalt or the nickel and the trivalent cobalt being both, however, 2 atmoic % or less of the chrome atom in the aforementioned oxidation alpha chrome crystal lattice to be substituted with the nickel, is substituted with the nickel and the trivalent cobalt 6 atmoic % the crystalline oxidation alpha chrome and to (ii) fluorine which designate that it is below as a condition at least a kind of is selected from the crystalline oxide (i) it is converted chrome contentIncluding the component, it is characterized by the chloridation fluorine conversion catalyst which becomes. Due to when under existing of the hydrogenation catalyst including CFC-217ba and hydrogen in the vapor phase in high temperature, also the method of producing the blend of HFC-227ea and hexa- fluoro propene by reacting the starting blend which becomes is disclosed. This method includes the fact that CFC-217ba is produced with the method of mentioning.
机译:(A)氟化氢,氯和式CX 3 的卤代丙烯CCl = CX2和式CX 3 的卤代丙烷CClYCX 3 (在公式中,每个X彼此独立,为F或Cl,它表示X和Y的数量作为条件,其中Y为H,Cl或F,但总计为F为6以下)。从起始原料组成的组中选择一种,使成为氯化氟转化催化剂的共混物在反应范围内接触CF 3 CClFCF 3 ,包括HCl公开了一种在HF,HF和氟转化卤代烃中间场太小的情况下生成2-kuroro -1,1,1-3,3,3-heputahuruoropuropan的方法,该方法包括形成共混物。 (i)结晶氧化α铬,在上述氧化α铬晶格中,铬原子的总量为(i)氧化α铬晶格中铬原子镍的至少0.05 atmo%,三价钴或镍和三价钴两者都是,但是,上述被镍取代的氧化α铬晶体晶格中铬原子的2原子%或更少被镍和三价钴6原子取代表示至少为一种条件的以下条件的至少一种晶态氧化α铬和(ii)氟选自晶态氧化物(i)被转化的铬含量包括组分,其特征在于氯化氟成为转化催化剂。由于当在高温下在气相中存在包含CFC-217ba和氢的氢化催化剂时,还公开了通过使所形成的起始共混物反应来生产HFC-227ea和六氟丙烯的共混物的方法。该方法包括通过提及的方法生产CFC-217ba的事实。

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