• 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:

    公开号:SU1052155A3
    申请号:SU792802995
    申请日:1979-08-13
    公开日:1983-10-30
    发明作者:Эрпенбах Хайнц；Германн Клаус；Кюббелер Ханс-Клаус；Шмитц Клаус
    申请人:Хехст Аг (Фирма)；
    IPC主号:
    专利说明:

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    The invention relates to a process for the production of acetic anhydride, which finds various applications in chemical, pharmaceutical and polymeric industry.
    A known method of producing acetic anhydride by oxosynthesis from methyl acetate, carbon monoxide and hydrogen in the presence of cobalt iodide in N-methylpyrrolidone at 190. and pressure up to 700 atm for 12–20 hours does not exceed 60%
    However, the use of high pressures with a low yield of the target product limits the possibility of widespread use.
    Closest to the predalgamate is the method of producing acetic anhydride with oxosynthesis from methyl acetate and / or dimethyl ether, which in the process is converted into methyl acetate and further to the target anhydride. ; ./
    The process is conducted in the presence of a catalytic system, including salts of noble metals. Periodic systole groups - palladium., iridium or rhodium and promoter) / salts or other compounds of chromium of iron, cobalt or nickel, as well as nitrogen or organophosphorus compound. . ..: ..,
    As organic nitrogen. compounds use tertiary amines of the formula. Rk% N, where R., R.. R.- al kil, I CEC loal kil, aryl, acyl, or a heterocyclic compound selected from the group: polyvinylpyridine, polyvinylpyrrolidone, pyridine, quinoline, hydroxyquinoline, imidazole, methylimidazod, and also imides of aliphatic or aromatic acids. . As an organophosphorus compound, various substituted phosphines are used.
    These compounds, being promoters, form complex compounds with selected salts of noble metals, for example, trichlorotripyridine and others. The process is carried out at 100-350 C, mostly at 175-255s, and a pressure of 0.07-350 kg / cm, mainly 10-35 kg / cm, in the presence of rhodium trichlorohydrate, methyl iodide, pyridine and chromium hexacarbonyl to obtain acetic anhydride yield from 26 to 62% depending on the process time (1-1.5 hours).
    The use of 2-picoline- increases the yield per hour to 72.4%, and the use of methyl iazole reduces to 38, 7%, 3-picoline - 50.6%, lutidine. 45.2% 2.
    However, in this process, when acetic anhydride is isolated by distillation, chromium salts are deposited on the walls of the column.
    sublimates, thereby causing a decrease in their concentration in the catalytic system and a corresponding drop in catalyst activity upon repeated use, which leads to a decrease in productivity from 433 to 4.5 g of acetic acid per anhydride per gram of labor per hour.
    The purpose of the invention is to simplify the process and increase its productivity.
    The goal is achieved by the fact that according to the method of producing acetic anhydride, oxosynthesis from methyl acetate and / or dimethyl
    V5 ether at 127-202 G and carbon monoxide pressure of 2Q-150 at in the presence of a catalytic system, vtpotpuyuy noble metal salt - swarm, palladium or iridium, iodide me20 promoter with nitrogen-containing heterocyclic compound, and the promoter used is aliphatic carbolic acid I; a heterocyclic compound selected from the group N-methylpyridine iodide; K, M - dimethyl lidazolinium; N-methyl 3-picolinium iodide N-methyl-2,4-lutidine iodide; N-methyl-3, 4-lutidinium iodide; N-methylquinoli. Iodide}, pyriium-acetate 7 (H methyl 30 imidazolium acetate; 3-picoliniace. Tat; 2,4-lutidinium acetate or 3,4-lutidinium acetate, at a molar ratio of noble metal, iodine methyl, carbonic acid and
    35 heterocyclic compounds equal to 1: 14-1299 b (22-1754 b (16-1008;.
    The use of aliphatic carbolic acid considerably simplifies the process of the depreciation of both acetic anhydride and the catalytic system, which as a residue after DISTANCE. RELATIONS are returned to the process. Sixfold use of the catalytic process returned to the process.
    Af system does not affect its activity and performance.
    These heterocyclic compounds, being good solvents for complexes of noble metals, are simultaneously well-wringed with acetic anhydride.
    The process can use carbon monoxide containing up to 10% by volume of hydrogen,
    The method is carried out as follows.
    The starting methyl acetate and / or dimethyl ether is fed to the synthesis reactor at a certain temperature and pressure of carbon monoxide. Unreacted carbon monoxide is returned to the reactor, and a small part is washed and removed from the system. Fresh carbon monoxide is added to the recovered gas.
    From the bottom of the reactor, the effluent is sent to a distillation where low boilers are separated. products: methyl acetate, dimethyl ether and methyl iodide, and then the residue is subjected in the evaporator to the separation of acetic anhydride and catalysis. tic system, which is returned to the stage of synthesis.
    PRI P R 1- In a hastello autoclave with CO 40 atta, temperature was synthesized from methyl acetate (250 g) in the presence of 1.6 g of rhodium trichloride trihydrate, 50 g of methyl iodide, 50 g of Uxus acid and 60 g of N -methyl-3-picolinium iodide (molar ratio 1: 58: 137: 4 2). After 45 minutes, the resulting reaction mixture is discharged from the autoclave, low boiling point products and acetic anhydride are distilled off, and the residual catalyst system is reused in the synthesis, - -.- ..-. . -.
    271 g of acetic anhydride is obtained in distillate, which is 578 g, per gram of genus per hour. -. Following the sixfold use of the catalytic system, a decrease in catalytic activity has not been established.
    The data of this example, as well as the implementation of the synthesis in the presence of different promoters under various conditions, is shown in the table.
    Example 12 (comparative). The process is carried out according to Example 4 of the known method t2}.
    In an autoclave from Hastello at 175 ° C and pressure of 25.6 ata, synthesis from methyl acetate (350 g) is carried out in the presence of 2.25 g of rhodium trichloride trihydrate, 57 g of methyl iodide, 17 g of 2-picoline and 7.5 g of chromium hexacarbonyl during iremidation. After an hour, the reaction mixture was discharged and 381 g of U1 SUSNOGRE anhydride was discharged by distillation, which yielded 433 g per gram of rodi per hour.
    However, during the distillation nab. luda.ts the deposition of chromium salts,
    Some are sublimated in the process. The distillation residue, as a catalytic system, is sent to re-synthesis with the same amounts of the starting methyl acetate. The productivity of acetic anhydride is 228 grams per gram of labor per hour. : After five times of use of the catalytic system, the productivity of acetic anhydride is reduced to 45 g per gram native per hour.

    Similarly, when using triphenylphosphine together with the salt of xpc both of these products are lost
    5 during the isolation process.
    Example 21 (continuous% process). The process is carried out in a continuous hastello unit comprising a reactor for 2 liters of the reaction mixture, where 2.2 kg / h of methyl acetate are continuously supplied. The average temperature in the reactor is 177 ° C and the pressure is 50 atm due to the continuous supply of CO. Rhodi concentration (VNSGz
    -K3H2Q) is 18 mmol per liter
    the reaction mixture. N-methyl-3-picolium iodide and H, H-dimethylimidazolinium iodide were used as bases, taken in a molar ratio of 1: 2.
    0 Coming out of the reactor. holds about 9% by weight of methyl acetate, about 55% by weight of acetic anhydride, about 10% by weight of acetic acid, about 10% by weight of methyl iodide and
    5 about 13 wt.% Quaternary salt, the above bases.
    Isolation of the desired product and separation are carried out by distillation, and un- reacted substances are recycled to the process.
    The result is 3 kg / h of acetic anhydride or a volumetric capacity; 1500 g / l “h or, 811 g per gram of labor per hour. Thus, counting on the reacted methyl acetate, acetic anhydride is obtained practically with quantitative. exit
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    权利要求:
    Claims (1)
    [1]
    METHOD FOR PRODUCING ACETIC / ANHYDRID by oxosynthesis from methylacet. . tat and / or dimethyl ether at '127-202 ° С and Carbon monoxide Pressure '20 -150 ata in the presence of salts of bla-, urban metals - palladium, rhodium * or iridium, methyl iodide, a promoter and a nitrogen-containing heterocyclic compound, distinguishes 'and I am Gem, that, in order to simplify the process and increase its productivity, an aliphatic carbolic acid is used as a promoter: C L —C 4 th, a heterocyclic compound selected from the group: N-methylpyridinium iodide; Ν, Ν-dimethylimidazolinium iodide; N-methyl-Z-picol · niyiodide; N-methyl-2,4-lutidinium iodide; N-methyl-3 g 4-lutidinium iodide; N-methylquinolinium iodide; pyridinium acetate; N-methylimide aolinium acetate; 3-picolinium acetate; 2,4-lutidinium acetate or 3,4-lutidinium acetate, with a molar ratio of noble metal, methyl iodide, carboxylic acid and heterocyclic compound equal to 1: (14-1299): (22-1754): (16-1008 I.
    Joint venture>
    I
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    同族专利:
    公开号 | 公开日
    PL217793A1|1980-04-21|
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    EP0008396A1|1980-03-05|
    JPS5715097B2|1982-03-29|
    CA1111065A|1981-10-20|
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    AU4999279A|1980-02-21|
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    PL115828B1|1981-05-30|
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    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    DE2450965C2|1974-10-26|1983-06-09|Hoechst Ag, 6230 Frankfurt|Process for the production of acetic anhydride|
    CA1058636A|1975-03-10|1979-07-17|Nabil Rizkalla|Process for preparing carboxylic acid anhydrides|
    US4002678A|1975-12-22|1977-01-11|Halcon International, Inc.|Preparation of carboxylic acid anhydrides|DE2939839A1|1979-10-02|1981-04-23|Hoechst Ag, 6000 Frankfurt|METHOD FOR PRODUCING ACETIC ACID ANHYDRIDE|
    US4284585A|1979-12-26|1981-08-18|Halcon Research And Development Corp.|Process for the preparation of acetic anhydride|
    US4284586A|1979-12-26|1981-08-18|Halcon Research And Development Corp.|Process for the preparation of acetic anhydride|
    DE3032853A1|1980-09-01|1982-04-22|Hoechst Ag, 6000 Frankfurt|METHOD FOR PRODUCING WATER-FREE ALKYL IODIDE|
    FR2507597B1|1981-06-12|1985-12-13|Rhone Poulenc Chim Base|PROCESS FOR CARBONYLATION OF METHYL ACETATE|
    EP0098689B1|1982-06-05|1986-12-17|BP Chemicals Limited|Process for the production of monocarboxylic acid anhydrides|
    GB8319619D0|1983-07-20|1983-08-24|Bp Chem Int Ltd|Acetic anhydride|
    DE3329781A1|1983-08-18|1985-02-28|Hoechst Ag, 6230 Frankfurt|METHOD FOR SEPARATING IODINE AND ITS COMPOUNDS FROM CARBONYLATION PRODUCTS OBTAINED FROM CARBONYLATING DIMETHYL ETHER, METHYL ACETATE OR METHANOL|
    JPS60203152A|1984-03-26|1985-10-14|Yasushi Kuno|Preparation of dried rice cake|
    DE3429179A1|1984-08-08|1986-02-20|Hoechst Ag, 6230 Frankfurt|METHOD FOR THE SIMULTANEOUS PRODUCTION OF CARBONIC ACIDS AND CARBONIC ACID ANHYDRIDES AND IF ANY. CARBONIC ACID ESTERS|
    GB8705699D0|1987-03-11|1987-04-15|Shell Int Research|Carbonylation of olefinically unsaturated compounds|
    DK158221C|1987-06-30|1990-09-10|Topsoe Haldor As|PROCEDURE FOR THE PREPARATION OF ACETIC ACID, METHYL ACETATE, ACETIC ACYE ANHYDRIDE OR MIXTURES THEREOF|
    DE3823645C1|1988-07-13|1989-11-30|Hoechst Ag|
    US5442107A|1989-04-06|1995-08-15|Bp Chemicals Limited|Preparing carboxylic acids|
    GB9021454D0|1990-10-03|1990-11-14|Bp Chem Int Ltd|Process|
    JPH0468912U|1990-10-17|1992-06-18|
    JPH0468913U|1990-10-17|1992-06-18|
    US5097069A|1991-04-08|1992-03-17|Eastman Kodak Company|Process for decomposing α,β-unsaturated carbonyl compounds in refining acetic anhydride and/or acetic acid|
    GB9218346D0|1992-08-28|1992-10-14|Bp Chem Int Ltd|Process|
    US5672743A|1993-09-10|1997-09-30|Bp Chemicals Limited|Process for the production of acetic acid|
    JPH07190821A|1993-12-24|1995-07-28|Nippondenso Co Ltd|Flowmeter|
    GB9806527D0|1998-03-26|1998-05-27|Bp Chem Int Ltd|Process|
    US5922911A|1998-04-24|1999-07-13|Eastman Chemical Company|Process for the manufacture of acetic anhydride|
    US6222070B1|1999-09-07|2001-04-24|Eastman Chemical Company|Method for reducing EDA in acetic anhydride production|
    DE10138778A1|2001-08-07|2003-02-20|Basf Ag|Joint production of formic acid with a carboxylicacid or derivatives, involves transesterifying a formic ester with a carboxylic acid, followed by carbonylation of the ester obtained|
    CN1315771C|2002-05-06|2007-05-16|伊斯曼化学公司|Continuous carbonylation process|
    DE10249928A1|2002-10-26|2004-05-06|Basf Ag|Flexible process for the joint production offormic acid,a carboxylic acid with at least two carbon atoms and / or its derivatives anda carboxylic acid anhydride|
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    US7582792B2|2006-06-15|2009-09-01|Eastman Chemical Company|Carbonylation process|
    US7253304B1|2006-06-20|2007-08-07|Eastman Chemical Company|Carbonylation process|
    US7629491B2|2006-06-26|2009-12-08|Eastman Chemical Company|Hydrocarboxylation process|
    US20090247783A1|2008-04-01|2009-10-01|Eastman Chemical Company|Carbonylation process|
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    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    DE19782836084|DE2836084A1|1978-08-17|1978-08-17|METHOD FOR PRODUCING ACETIC ACID ANHYDRIDE|
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