• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    1. Process for the preparation of acetic derivatives by reacting, with methanol, a mixture comprising hydrogen and carbon monoxide, the carbon monoxide representing at least 75 mol %, at a temperature lower than or equal to 180 degrees C, in the presence of an effective amount of cobalt, characterised in that the process is carried out in the presence of at least one ionic iodide and at least one halogen-containing promoter, the cation of the ionic iodide being chosen from the group comprising alkali metal cations, alkaline earth metal cations, ammonium cations, quaternary ammonium cations, phosphonium cations and quaternary phosphonium cations, the ratio I**- /Co (in gram-atoms) being greater than or equal to 10, and the ratio X/I**- (in gram-atom), in which X represents a halogen atom originating from a halogen-containing promoter, being between 0.01 and 0.3.
    公开号:SU967274A3
    申请号:SU792832608
    申请日:1979-10-30
    公开日:1982-10-15
    发明作者:Готье-Лафай Жан；Перрон Робер
    申请人:Рон-Пуленк Эндюстри (Фирма)；
    IPC主号:
    专利说明:

    The invention relates to methods for producing acetic acid or its mixture with methyl acetate by carbonylation of methanol in the presence of a cobalt containing catalyst. Shioro acetic acid is known or it can be mixed with methyl acetate by reacting methanol with a mixture containing hydrogen and 70–95 mol. % carbon monoxide at 120 160С and pressure of 180 -320 atm in the presence of cobalt acetate and metals selected from the group of Pd, Pt, I g, Rujfl. The disadvantage of this method is the low productivity of the process (according to the calculated data, the capacity according to Example 5 below is 28 g / h per 1 g of Co and 117 g / per 1 l of the reaction volume). The purpose of the invention is to increase the productivity of the process. This goal is achieved by the fact that according to the method of producing acetic acid or. its mixtures with methyl acetate by the interaction of methanol with a mixture containing hydrogen and 80–95 mol% carbon monoxide at 120–160 ° C and pressure of 140–250 atm in the presence of a cobalt containing catalyst, the process is carried out in the presence of alkali metal or ammonium iodide or quaternary ammonium , or frsfoni, or quaternary phophony and bromide or alkyl iodide with a ratio of - (g-atom) equal to 21-52, and ratios X / G, where X iodine, bromine, iodide or methyl bromide, equal to 4.1-25 weight. % of the number of ions 1. As the promoter are particularly suitable iodides, quaternary ammonium such derivatives lower trialkylamines, such as trimethylamine, triethylamine, tributylamine, or respectively alkylarylamino such as dimetilamilin. Or cyclic tertiary amines such as N-alkyl-pyrrolidines or piperidines, N-alkyl-hexamethylene - amines, pyrrole, pyridine, alkylpyridines, quaternized by treatment with esters of hydroiodic acid and aliphatic alcohols. Bis-quaternized ammonium iodides, derivatives of, for example, tetraalkylsylenediamines, can be used. The use of iodide phosphonium derivatives, for example, triarylphosphines, readily available, such as triphenylphosphine, tritolylphosphine, trixylphosphine, or readily available trialkylphosphines, such as trimethylphosphine, tributylphosphine or tricyclehexylphosphine, and quantized alkylacrylphenyls, and ian-glunophosphine, and quantized alkylacrylphosphine or tricyclelohexylphosphine, and quaternized alkyl nitroxyphosphine, and triacylphosphine, triticylphosphine, and triacylphosphine. Bis-quaternized phosphonium iodides, derivatives, for example bis-o, W- (diphenylphosphino) -alkanes, can be used. A preferred embodiment of the invention includes the use of alkali metal iodides, such as Li 1, Nal, K1. The invention also requires the use of at least one halogen-containing promoter: methyl bromide or iodide alkyl. According to the invention, the effect created by the halogen-containing promoter is noticeable even for insignificant amounts, on the order of 1 g-atom of halogen (hereinafter referred to as X) per 100 g of the indicated iodides, i.e. for an X / 1 ratio of 4%. It is undesirable to exceed a value of 25% for this ratio for technological reasons, especially to limit corrosion of the apparatus. . Operate preferably with a ratio X / G of 4.1 - 25%. The proposed method is implemented in the presence of cobalt, and can be used: any source of cobalt that can react with carbon monoxide in the reaction medium to produce a complex of cobalt carbonyl, cobalt bicarbonyl or cobalt carbonylate. Typical sources of cobalt are, for example, finely ground cobalt metal, inorganic salts such as cobalt carbonate, organic salts, especially fatty acids. Cobalt carbonyls, cobalt hydrocarbonyls or their complexes can also be used, and among cobalt derivatives cobalt acetate and formate, halo cobalt genides, especially cobalt iodide, Dicobaltoctacarbonyl can be used. Take an effective amount of cobalt, i.e. such an amount in which the ratio of the number of mg-atoms of cobalt to the number of moles of methanol (Co / CH3PH) is 0.05-1. Carbonyl is preferably carried out in the liquid phase. Since methanol is most often used in excess, the simultaneous use of additional solvent is usually unnecessary, but solvents such as hydrocarbons, esters, ethers, and reaction products can be used. Pre-purification or dehydration of methanol is not necessary. You can use technical grade methanol, the original used methanol can contain up to 50% water and / or methyl acetate. A mixture of carbon monoxide and hydrogen is reacted with methanol. The mixture contains at least 75 mol%. carbon monoxide. Preferably, mixtures comprising 80-98% carbon monoxide are used. The gaseous mixture may contain prims, such as, for example, carbon dioxide, oxygen ,. v methane and nitrogen. The reaction requires the use of a total pressure of usually 140-250 atm. The reaction temperature is 120-160 ° C. Symbols used. in the examples below, the following:, AcOMe - methyl acetate; AcOH is acetic acid, C is a combination of the resulting products containing 4 carbon atoms in the molecule, namely, butenal and / or butanal and / or butanol) MeOM-dimethyl ether (product recycled to the reaction). The RR-for this product is equal to the ratio of the number of moles of the product in question obtained during the reaction to the number of moles of methanol introduced into the reaction, with the exception of RR (C4) and RR (MeOMe), which are twice the ratio. Z PP is cyMiviy RR, for the totality of the observed liquid products with the exception of dimethyl ether. Performance is expressed in grams of potential acetic acid per hour in relation to either the reaction volume (g / H (, l); or the mass of cobalt added tr / h -g So). EXAMPLE 1-5. Into an autoclave of stainless steel Z8-CND T 17-12 (norm AFNOR) with a capacity of 125 ml load 100. Ml of matanol, 0.58 mg / cobalt atom in the form of dicobaltoctacarbonyl 24 mmol of sodium iodide 1 mmol of ethyl iodide (Co / CHjOH .0,237) . After the autoclave is closed, a pressure of 140 atm is established using a mixture of CO / H.j | 95/5 (initial hydrogen pressure 7 atm). The stirring of the system is activated, and the inoculation in the autoclave is adjusted to approximately 20 minutes using a ring-shaped furnace. The total pressure in the autoclave is 250 atm and it is maintained at 238–250 atm: periodic loads of carbon monoxide. After reaction for 1 h 40 min at the indicated temperature (complete absorption of 104 atm carbon monoxide), heating and stirring are stopped, the autoclave is cooled and degassed.
    The resulting reaction mixture was analyzed by gas chromatography, after dilution with water and acidification with sulfuric acid.
    Individual conditions, as well as the results obtained are presented in Table. one.
    Examples 6-13. With the exception of the opposite indications, 100 ml of methanol a, O, 58 mg atom of coboshite are loaded into the form of “dicobalt octacarbonyl} 12 mmol of potassium iodide; 3 mmol of methyl iodide.
    Consequently, Co / CH, OH 0.237j G / Co 21, X / G 25% is shipped.
    The reaction time, with the exception of the opposite indication, is 1 h 40 min. The results: are presented in Table; 2, in which K.Nd,) means initially, the pressure of hydrogen and P. means D Zlenye.
    X (b
    e
    1196727412
    权利要求:
    Claims (1)
    [1]
    The claims of the invention or of the quaternary phosphonium and bromis method for producing acetic acid with a ratio I / CO (g-atom) equal to
    or its mixtures with methyl inter-21-52, and the ratio X / I, where X is iodine,
    by the action of methanol with a mixture containing bromine, iodide or methyl bromide, hydrogen and 80-95 mol.% of oxide 5la, equal to 4.1-25 wt.% of the carbon carbon at 120-160 C and an increased amount of ions 1 and pressure of 140 pressure in the presence of cobaltssoder-250 atm. The catalyst is characterized in that, for the purpose of higher sources of information,
    The NIN of the productivity of the process, the continuous process during the examination of the latter is carried out in the presence of an alkali metal iodide or a1 «1 moni, or 1. Belgian Patent No. 808716,
    Quaternary ammonium, or phosphonium, cl. C 07 C, 1974 (prototype). addition or alkyl iodide Cj-C
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    同族专利:
    公开号 | 公开日
    EP0011043A1|1980-05-14|
    FR2440349B1|1981-04-17|
    EP0011043B1|1981-09-02|
    CA1125305A|1982-06-08|
    BR7907035A|1980-07-15|
    ES485528A1|1980-05-16|
    DD146944A5|1981-03-11|
    EP0011043B2|1986-03-26|
    JPS6323978B2|1988-05-18|
    JPS5564533A|1980-05-15|
    AT180T|1981-09-15|
    DE2969751D1|1981-11-26|
    FR2440349A1|1980-05-30|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    US4356320A|1976-11-08|1982-10-26|The Halcon Sd Group, Inc.|Preparation of carboxylic acids|US4320230A|1979-09-24|1982-03-16|Exxon Research & Engineering Co.|Methanol homologation using iron-cobalt carbonyl cluster catalyst|
    DE3377125D1|1982-03-30|1988-07-28|Shell Int Research|A process for carbonylating methanol to acetic acid and/or methyl acetate|
    JPH0469136B2|1983-09-02|1992-11-05|Daicel Chem|
    CA1228867A|1984-05-03|1987-11-03|G. Paull Torrence|Methanol carbonylation process|
    JPH042273U|1990-04-19|1992-01-09|
    WO1994005421A1|1992-09-10|1994-03-17|Daicel Chemical Industries, Ltd.|Process for producing acetic acid or methyl acetate and catalyst|
    EP0631814A4|1992-09-10|1995-04-19|Daicel Chem|Ru-Sn HETEROPOLYNUCLEAR COMPLEX AND PROCESS FOR PRODUCING ACETIC ACID OR METHYL ACETATE BY USING THE SAME.|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    FR7831635A|FR2440349B1|1978-10-31|1978-10-31|
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