• 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 ethyl carboxylates by reacting a mixture containing carbon monoxide and hydrogen with the corresponding methyl carboxylates, in the liquid phase, at a temperature of between 175 and 250¬ C, under a total pressure of between 50 and 600 bars, in the presence of ruthenium and an iodine-containing promoter, the atomic ratio I/Ru being greater than or equal to 5, characterised in that the reaction is carried out in the simultaneous presence of cobalt, the atomic ratio Co/Ru being less than or equal to 1, at least one alkyl iodide and at least one inorganic or organic ionic iodide in which the cation is chosen from the group comprising alkali metal cations, alkaline earth metal cations and quaternary ammonium or phosphonium cations.
    公开号:SU1194269A3
    申请号:SU803222495
    申请日:1980-12-19
    公开日:1985-11-23
    发明作者:Готье-Лафайе Жан；Перрон Робер
    申请人:Рон-Пуленк Эндюстри (Фирма)；
    IPC主号:
    专利说明:

    one .
    The invention relates to an improved process for the preparation of ztyl acetate, which is a valuable product of organic synthesis.
    The purpose of the invention is to increase the productivity of the process.
    Example 1. In a 250 ml autoclave with a capacity of 250 ml, 80 ml of methyl acetate (1002 mmol) 5 of 20 ml of acetic acid (350 mmol), 510 mg of methyl iodine (3.54 mmol), 4.85 g of methyl triphenylphosphonium iodide (12 mmol ), 36.8 g of dicobaltoctacarbonyl (0.22 mg Co), 279.2 mg of trienium dodecacarbonyl (1.31 mg Ru) (50 mmol), concentration of Ru 13.1), 50 mmol of lithium acetate.
    The ratio of Co (Ru and Cf / Ru are given in Table 7.
    The autoclave is fired and a pressure of 140 bar is established using an H2 / CO 2/1 mixture (molar). The mixture is stirred on a rocking chair and the autoclave is brought to 25 minutes using an annular oven. The pressure in the autoclave is 220 bar and it is maintained between 230 and 260 bar by repeated consecutive loads of the initial mixture H ,, / WITH.
    After 40 min of reaction at the indicated temperature, heating and stirring are stopped; the autoclave is cooled and degassed. The final reaction mixture was analyzed by gas chromatography (after dilution in a mixture of 56/44 water and dimethoxy-1, 2-ethane and oxidation in sulfuric acid). It contains, g: ethyl acetate 24,25; methanol 1.85; acetaldehyde 0.45; ethanol 1.95. and acetic acid 35545,
    Reaction productivity on an ethyl acetate: 365 g / chtl; 270 ruthenium; 2900 g / t of cobalt.
    Examples 1 a-1e. The process is carried out as in Example 1.
    In example a, do not take dicobaltoctacarbonyl.
    In 1b do not take triruenium dodecacarbonyl.
    In Example 1c, dicobaltoctacarbonyl is replaced by an equivalent amount of iron pentacarbonyl (0.21 mg atm),
    In the example of Id, tri-ruthenium dodecacarboxyl is replaced by an equivalent amount of ferropentacarbonyl (1.3 mg of iron).
    4269i
    In example 1e, methyltriphenylphosphonium iodide is not taken, therefore the O / Ru ratio is only 2.7.
    The conditions of examples 1, 1a-1e and the results obtained are presented in Table. one .
    The ratios of Co / Ru and L / Ru are shown in Table. 7
    From tab. 1 shows the particular nature of the 10 addition of a small amount of cobalt to ruthenium. On the other hand, Example 1e reveals the importance of the number of iodine initiators present in the reaction medium. ) 5 Examples 2-4. In the autoclave of Example 1, a series of experiments was carried out, placing in each of the experiments 0.215 mg of cobalt in the form of dikobalcatocarbonyl, 1.31–20 ruthenium in the form of tri-rhenium dodecacarbonyl (concentration 13.1 mg.at / l), 12 mmol of sodium iodide (examples 3 and 4) or 12 mmol of methyltriphenylphosphonium iodide (Example 2). .
    The ratio of Co / Ru and I / Ru are shown in Table. 7
    The general conditions of the test are as follows: H2 / CO: 2,, 1 (molar). Temperature . The total pressure at the specified temperature is 260 bar, the duration of the experiment at the same temperature is 1 h 15 min.
    The conditions of the experiments and the results obtained are presented in Table. 2
    Examples 5-11. In the autoclave of Example 1, a series of experiments was carried out, in each of which 1000 mmol of methyl acetate, 350 mmol of acetic acid, 10 mmol of iodis, sodium, 1.31 ruthenium in the form of triunine dodecacarbonyl (concentration 13.1 mg.at / l , iodomethyl and dicobaltoctacarbonyl, if necessary.
    The ratio of Co / Ru and I / Ru is indicated in Table 5. 7
    The general conditions of the test are as follows: H2 / CO: 2/1 (molar), temperature. The total pressure at the specified temperature is 260 bar, unless otherwise indicated.
    Conditions and results are shown in Table. 3
    Examples 12-16. In the autoclave of Example 1, a series of 55 experiments were carried out, in each of which 0.22 cobalt was taken in the form of dicobaltoctacarbonyl, ruthenium in the form of tri-rhenium dodecacarbonyl, 3.55 mol
    3
    methyl iodide, 12 mmol methyltriphenylphosphonium iodide, 1100 mmol methyl acetate, 350 mmol of acetic acid (if not otherwise indicated).
    The ratios of Co / Ru and I / Ru are shown in Table. 7
    The general conditions of the test are as follows: H2 / CO: 2/1 (molar), temperature 215 ° C. The total pressure at the specified temperature is 260 bar.
    The duration of the experiment at the same temperature is 1 h 15 min.
    Special conditions and the results obtained for these examples are presented in Table. four.
    Examples 17-20. In the autoclave of Example 1, a series of experiments were carried out, for this purpose 75 ml of methyl acetate, 20 ml of acetic acid, 5 ml of water, 18 mmol of iodine methyl, 0.22 mmol of tetrahydrated cobalt acetate, 1.31 mg ruthenium in the form of trirhenium dodecacarbonyl (concentration of RU 13.1), sodium acetate, the amount of which is listed in Table. five.
    The ratio of Co / Ru and I / Ru is shown in Table. 7
    The general conditions of the test are as follows: H2 / CO: 2/1 (molar). Temperature . The total pressure at the specified temperature is 260 bar, the duration of the experiment at the same temperature is 40 minutes.
    The specific conditions and results obtained for these examples are given in table. five.
    Control Example 20f was carried out in the absence of sodium acetate.
    Example 21-23. In the autoclave of Example 1, a series of experiments was carried out; for this, 5 ml of methyl acetate, 20 ml of acetic acid, 5 ml of water, 18 mmol iodine methyl, 0.22 mmol of tetrahydrated cobalt acetate, 1.31 mg ruthenium in the form of tri-rhenium dodecabarbonium (concentration of Ru 13.1), lithium acetate, the amount of which is given in table. 6
    The ratio of Co / Ru and I / Ru is shown in Table. 7
    The general conditions of the test are as follows: H2 / CO: 2/1 (molar). Temperature . The total pressure at the specified temperature is 260 bar, the duration of the experiment at the same temperature is 40 minutes.
    94269
    The specific conditions of the experiment and the results obtained for these examples are given in table. 6
    Control 23f carried out in the absence of lithium acetate.
    Example 24. In the apparatus according to Example 1, the experiment was carried out, with 77 ml of methyl acetate, 20 ml of acetic acid, 3 ml of water, 35 mmol of 10 iodine methyl, 0.22 mmol of hydrated cobalt acetate, 1.3 mg ruthenium taken. (concentration of Ru 13.1) in the form of trienium dodecacarbonyl and 17 mmol of lithium acetate (the ratio of CO / RU and I / RU is shown in Table 7). After 40 min, the reaction at 215c and a total pressure of 250 bar of H2 / CO-2/1 (molar) mixture is, g: AcQEt 7.37 (capacity 220 g / h h l); 20 MeOH 2,; 92; AcH 0.90; EtOH 1.79; . AcOH 34.5.
    Example 25: Reproduce Example 24, varying only the volume of methyl acetate (80 ml) and the amount of 25 methyl iodine (30 m. Mols).
    As a result, they have, g: AcOEt 8.71 (productivity 260, g / h x l); MeOH 1.88; AcH 0.58; EtOH 1.80; AcOH 33.2,
    Example 26. Reproduced
    30 Example 25, replacing lithium acetate with 30 mmol of sodium acetate.
    As a result, they have, g: AcOEt 11.7 (capacity 350 g / h x l); MeOH 2.57; AcH 1.02; EtOH 1.62; 35 AcOH 35.6.
    Example 27. Reproduce Example 25, replacing lithium acetate with 17 mmol of tetrahydrated magnesium acetate.
    40 As a result, they have, g: AcOEt 8.50 (capacity 260 g / h x l); MeOH 1.72; AcH 1.18; EtOH 1.05; AcOH 35.1.
    Example 28. In the autoclave on. 45 to Example 1, a mixture of hydrogen gases and carbon monoxide (molar ratio 2/1) is added to 80 ml of methyl acetate, 20 ml of acetic acid, 3 ml of water, 0.22 mmol of cobalt iodide, 50 1.31 mg-ruthenium in the form of trienium dodecadecarbonyl (concentration RU 13.1), 30 mmol sodium iodide.
    The ratio of Co / Ru and I / Ru is indicated in Table 55. 7
    After 20 min of reaction at 215 C and a total pressure of 250 bar are, g: AcOEt 6.88 (capacity
    51
    210 g / h (X L); MeOH 2.41; AcH 0.49; EtOH 2.081 AcOH 35.3.
    Example 29. In the autoclave of Example 1, a mixture of hydrogen and carbon monoxide (molar ratio 2/1) was added to 76 ml of methyl acetate, 20 ml of acetic acid, 3 ml of water, 0.22 mmol of tetrahydrated cobalt acetate, 1.31 mg "at ruthenium in the form of trienium dodecacarbonyl (concentration of Ru 13.1 mg.at / l) 15 mmol of lithium iodide, 15 mmol of methyltriphenylphosphonium iodide.
    The ratio of Co / Ru and 1 / Ru is shown in Table. 7
    After 20 min of reaction at 215 ° C and a total pressure of 250 bar are, g: AcOEt 7.79 (capacity 230 g / h X l); MeOH 1.97; AcH 2.77; EtOH 1.09; AcOH 39.6 and 650 mg.
    Example 30. In the autoclave of Example 1, a mixture of hydrogen and carbon monoxide in a molar ratio of 2/1 was added to 80 ml of methyl acetate, 20 ml of acetic acid, 3 ml of water, 0.22 mmol of tetrahydrated cobalt acetate, 1.31 ruthenium in the form of trienium dodecarbonyl (Ru concentration 13.1 mg-at / l), 30 mmol sodium iodide, 17 mmol tetrahydrated magnesium acetate.
    The ratio of Co / Ru and I / Ru is shown in Table. 7
    After 20 min of reaction at a temperature of 215 ° C and a pressure of 250 bar, they have, g .: AcOEt 8.39
    942696
    (capacity 250 g / h x l); MeOH 1.99; AcH 0.99; EtOH 2.08; AcOH 37.4 and 370 mg.
    In tab. 7 shows the generalized 5 data on the molar ratios of CO / RU and I / RU in each of the 30 examples of the proposed method.
    An analysis of the results suggests that most of the examples are implemented at 260 bar total pressure. Example 6 is carried out at a pressure of 160 bar. Most of the examples are implemented at a temperature (example 5–15 at), in most examples the molar ratio is 2/1, but in example 5 this ratio is 1.
    Examples 2 to 12 are realized in the absence of acetic acid, the presence of acetic acid is an option only optional.
    25 In addition, from table. 7 it follows that the minimum value of the Co / Ru atomic ratio is 0.09 (example 7), the maximum value is 1.00 (example 16); the minimum value of 30 atomic ratio I / Ru is 11.67 (example 10), the maximum is 70, 59 (example 16).
    Thus, the proposed method allows to significantly increase the 35 productivity of the process by ethyl acetate to 350 g / hl versus 200–200 g / hl by a known method.
    Table 1
    Undefined Example Example Example
    eight
    Table 2
    . | T a b i c a 3 is made at 170 C, the molar ratio, pressure is 230 bar. Completed at a pressure of 160 bar, with 474 mmol 1, 08 mg of Owl form of CoS. h. e. The amount of water indicated in the table does not take into account hydrated water. . Hereinafter, S is the molar selectivity calculated as the ratio of the AcOEt formed to the sum (AcOEt + EtOH + AcOH + AcH),% ...
    eleven
    12
    1194269 Table 7
    权利要求:
    Claims (4)
    [1]
    1. METHOD FOR PRODUCING ETHYL ACETATE by reacting methyl acetate with a mixture of carbon monoxide and hydrogen at a molar ratio of Hj,: CO, equal to 1-2 in the liquid phase at a temperature of 170 - 215 ° C, under a pressure of 160-260 bar, in the presence of cobalt and halogen-substituted compounds, characterized in that, in order to increase productivity, the process is conducted in the presence of 2.2-13.3 mg.at / l of ruthenium, methyl iodide and inorganic or organic iodide, the cation of which is selected from the group consisting of alkali metal cations and methyltriphenylphosphonium cation, and about ess is conducted at an atomic ratio of Co: Ru, equal 0,09-1, and an atomic ratio of J-Ru, 11,67-70,59 equal.
    [2]
    2. The method of pop. ^ characterized in that the ionic iodide cation is selected from alkali metal cations. ·
    [3]
    3. The method according to PP. 1 and 2, characterized in that the process is carried out in the presence of alkali or alkaline earth metal acetate as a cocatalyst.
    [4]
    4. The method according to p. 3, characterized in that the process is carried out in the presence of lithium, sodium, potassium or magnesium acetate as a cocatalyst.
    SI „„ 1194269
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    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    US3285948A|1965-01-22|1966-11-15|Commercial Solvents Corp|Halides of ruthenium and osmium in conjunction with cobalt and iodine in the production of ethanol from methanol|
    NL7708158A|1976-07-28|1978-01-31|Montedison Spa|METHOD FOR PREPARING ESTERS.|
    DE2731962A1|1977-07-15|1979-02-01|Imhausen Chemie Gmbh|METHOD FOR MANUFACTURING CARBONIC ETHYLESTER|
    CA1138898A|1978-04-04|1983-01-04|Jimmy Peress|Phenylethyl alcohol preparation with mixedfeeds|
    EP0031606B1|1979-12-21|1983-08-24|Shell Internationale Researchmaatschappij B.V.|Process for the co-production of carboxylic acids and carboxylic acid esters|FR2507597B1|1981-06-12|1985-12-13|Rhone Poulenc Chim Base|PROCESS FOR CARBONYLATION OF METHYL ACETATE|
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    DE3267030D1|1981-09-22|1985-11-28|Shell Int Research|Process for the co-production of carboxylic acids and carboxylic acid esters|
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    US4511741A|1983-12-02|1985-04-16|Union Carbide Corporation|Production of aldehydes from organic acid esters|
    DE3413021C2|1984-04-06|1992-02-20|Hoechst Ag, 6230 Frankfurt, De|
    FR2576203B1|1985-01-24|1987-06-26|Moulinex Sa|HOUSEHOLD APPLIANCE FOR CULINARY PREPARATIONS SUCH AS SAUCES OR PASTRY LINKS|
    US5672743A|1993-09-10|1997-09-30|Bp Chemicals Limited|Process for the production of acetic acid|
    US7615671B2|2007-11-30|2009-11-10|Eastman Chemical Company|Hydrogenation process for the preparation of 1,2-diols|
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