• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
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  • 优先权
    • 专利摘要:
    A method for producing complex; carbonic acid esters is oxidized by lower C, Sc-alcohol and -aldehyde by means of oxygen-containing gas in the liquid phase under heating and pressure using a metal catalyst, characterized in that, in order to increase the selectivity of the process, oxidation is carried out at 30 - 100 C and pressure of 1-50 kg / cm, and a catalyst containing an intermetallic compound of the general formula A,., Pd, .5, where A is Pb, T1, Hg or Bi, or a catalyst of the general formula is used as a metal catalyst. 4.5-10. 0.5-10.0 1-20 where A is Pb, T1, Hg or Bi; B — Na, K, Li, Mg, or Ca, g, and numerical values are the weight percentages of metals in (V) relative to the carrier, with a Pd: A ratio of 1: (O, 4-20) and used as a carrier SiO,, activated carbon,, MgO or CaCOj. with about with 00 ate
    公开号:SU1190985A3
    申请号:SU802923551
    申请日:1980-05-15
    公开日:1985-11-07
    发明作者:Аосима Ацуси；Ямамацу Сецуо；Ямагути Тацуо；Сузуки Есио
    申请人:Асахи Касеи Когио Кабусики Кайся (Фирма)；
    IPC主号:
    专利说明:

    one
     The invention relates to methods for producing carboxylic acid esters that can be used in the chemical industry as solvents, as well as intermediates of organic synthesis.
    The purpose of the invention is to increase the selectivity of the process.
    Example 1. Assist; H, 100 ml of acetone dissolved 5.5 g of palladium bis (benzonitrile) (C, H, CN) 2PdCl2 dichloride and a solution of 10 g of lead acetate () P6H in 70 ml of methanol was added to form a brown precipitate, The precipitate is separated by filtration and dried, after which 4.5 g of the precipitate is dispersed in 50 ml of water, and 4 ml of an aqueous solution of formaldehyde and 20 ml of 1 Hi aqueous solution of sodium hydroxide are added to the dispersion to obtain a black insoluble substance. The product is separated by filtration, washed with water, dried; and then subjected to X-ray diffraction in order to find out that the product is an intermetallic compound and its diffraction X-ray diffraction pattern corresponds to the X-ray diffraction pattern in the ASTM card. The melting point of the Jep products is by differential thermal analysis. It is equal to 220 ° C, which corresponds to the melting point of Pd., Pb. In the X-ray diffraction experiment, CuCa is used as a radiation source.
    PRI me R 2 (reference). 12.8 g of palladium chloride is dissolved in 100 ml of dilute hydrochloric acid, followed by the addition of 40 ml of an aqueous solution dissolved in 9.1 g of lead acetate. The resulting mixture is evaporated to dryness in a water bath and calcined in air at 300 ° C for 3 hours. The mixture is then reduced in a hydrogen stream for 12 hours. The catalyst thus obtained is subjected to X-ray diffraction and is found to be mainly intermetallic compound. and contains a small amount of the Pdj-Pb intermetallic compound. The diffraction peaks of these compounds, and coincide with the peaks of PdgPb, and in the ASTM card, respectively. Diffraction
    90985 - 2
    The peak of metal palladium is not determined. .
    Example 1. 1.76 g of magnesium acetate are dissolved in 40 cm of water.
    5 (CH5COO) 2Mg4Hj, 0 and add
    0.92 g of lead acetate () Pb-3NO and then g of silica gel (Fuji Davidson 5D), is impregnated with a solution, followed by evaporation to dryness with stirring in a boiling water bath, calcined in air for
    3 hours, added to an aqueous dilute hydrochloric acid solution containing 0.83 g of palladium chloride
    5 PdClg, heated to 60 ° C and impregnated with palladium with stirring. After adding 2 ml of an aqueous solution of formaldehyde and 1N. an aqueous solution of sodium hydroxide obtained
    0 catalyst on the support is separated
    by filtration, washed with water, then dried. In accordance with the results of catalyst x-ray diffraction, diffraction peaks appear 5 s at 29 38.6 j 44.8; 65.4 and 78.6 ie The catalyst is an intermetallic compound Pd-Pb. The diffraction peak of a metallic Pd is undefined.
    In a four-neck flask with a capacity of 200 ml, equipped with a condenser with a dry ice-methanol system, a gas tube, a stirrer and a thermometer, 100 ml of methanol are placed,
    4 g of catalyst prepared as 5 described by Bbmie, and 7 g of methacrolein.
    The reaction is carried out at 40 ° C for 2 hours while the air flows through the flask at a rate of 10 liters per hour. After the reaction has been completed, the analysis is carried out using gas chromatography (chromosolb 101, 5 m long glass column, 210 s). The conversion of methacrolein is 75%. The yield of methyl methacrylate is 67.2% (89.6% selectivity). In addition, small amounts of propylene (0.8% selectivity) and carbon dioxide are obtained.
    0 Example2. 40 cm of water dissolve 1.76 g of magnesium acetate, add 10 g of silica gel (Fuji David sleep 5D), dry it with a solution, evaporate to dryness in a boiling water bath, calcine in air at 500 s for 3 h and then added to a dilute hydrochloric acid solution containing g 3. palladium chloride and 0.92 g of lead acetate, as the solution is heated at 60 ° C to impregnate the silica gel with the solution. The silica thus treated is separated by filtration, dried, reduced in a stream of hydrogen at 300 ° C for 3 hours, washed with a dilute aqueous solution of sodium hydroxide, water, and dried. The results of rent-Evnovian diffraction of the catalyst confirm that the product is an intermetallic compound Pd, Pb. When the reaction was carried out according to the conditions of Example 1 using a catalyst, methacrolein conversion was 67%, and the yield of methyl methacrylate was 58% (86.6% selectivity). Small amounts of propylene (0.5% selectivity) and carbon dioxide were obtained. Example 1 (comparative). The catalyst on silica gel was prepared analogously to example 1 (with the exception of not using Evin da acetate). The conversion of methacrolein is equal to 44.8%, and the yield of methyl methacrylate is 14.2% (30.5% selectivity). In this case, significant amounts of carbon dioxide and propylene are obtained (18.8% selectivity). I Example 3: The reaction was carried out analogously to example 1, but methacrolein was replaced with 3.5 g of metal alcohol. The conversion of metal alcohol is 100%, the yield of methacrolein is 33.5%, methyl methacrylate lat is 52.5%, and methacrylic acid is 1.4%. Methyl formate and small amounts of propylene (1.9% yield) and carbon dioxide were obtained as by-products. EXAMPLE 2 (comparative) .. The reaction is carried out analogously to example 1 using the catalyst of comparative example 1. Methyl alcohol conversion is 100%, the yield of methacrolein is 27.5% methyl methacrylate - 14.9%. Large quantities of gaseous by-products were obtained. The propylene yield is 50.2%. PRI me R 4, the Catalyst on alumina is obtained analogously to example 1, but using: T-alumina (Neobeal, trademark of the company Mitsusawa Chemicals Co., Ltd.), and the amount of palladium chloride 854 is 0.42 g. Education intermetallic compound is confirmed by x-ray diffraction. A 300 ml mixing type reactor with a stirrer, condenser, gas tube, thermometer, liquid inlet and liquid outlet is charged with 36 g of catalyst (2.5% palladium content) obtained by this method, 300 ml of methanol and 30 ml of methacrolein, air is blown into it at a rate of 10 l / h with for carrying out a batch reaction for 3 h. Then a 20% solution of methacrolein in methanol is charged at a speed of 25 ml / h and a solution of 1.6 g of NaOH in 1 l at a speed of 5 ml / h so that the pH at the outlet of the reaction solution can be from 6 to 8. Through 150 h of methacrolein conversion is 74.5%, the yield of methyl methacrylate is 68.4% (, 91.8% selectivity), small amounts of methacrylic acid (3.3t selectivity), methyl formate (6 mol.% / MMA ), propylene (0.5% selectivity) and carbon dioxide. After 1000 hours, the catalyst did not reduce its activity, methacrolein conversion was 76%, methyl methacrylate yield was 68.7% (90.4% selectivity). Examples 5-7. The reaction is carried out analogously to example 1, but methacrolein (example 1) is substituted for each of the aldehydes shown in Table. 1 (aldehyde 0.1 mol; methanol 1.00 ml; catalyst 4 rj reaction time I, air 10 l / h). , and 2 ch1 ... ... and c a 1 t a b l Isobutyraldehyde 61.0 56.7 93.0 Benzaldehyde 66.1 59.0 89.2 Pro.Pyroiddehyde 74.9 67.7 90.4 The amount of carbon dioxide and the corresponding hydrocarbons obtained as by-products is very small. PRI me R 8. 4 g of catalyst (example 4) and 40 g of N-propanol are loaded into the reactor. Oxygen is blown into the reactor at a rate of 3 l / hr for carrying out the reaction for 2.5 hours. 0.65 g of propionaldehyde, 0.06 g of propionic acid and 3.56 g of propyl propionate are obtained, and in addition, ethane and carbon dioxide, each in an amount of 0.5 mmol or less. PRI m e. P 3 (comparative). The reaction is carried out under conditions similar to example 8 ,. except that the catalyst of example 4 is replaced by 5% palladium-alumina (released by the Japanese company Engelhard Co.). 0.2 g of propionic aldehyde, 3.7 g of propionic acid and 8.8 g of propylpropane are obtained. Large amounts of gases are produced as by-products, and ethane and carbon dioxide are each obtained in an amount of 60 mmol or more. PRI me R 9. Analogously to the example of 1.10 g of isobutanol and 100 mp of methanol interact in the presence of 10 g of the catalyst of example 1 at 40 ° C for 2 h, while the air passes through the reaction system at a speed of 10 l / h. Methyl. Isobutyrate is obtained with a yield of 18, Example 10. Under conditions analogous to Example 9, 10 g of 1,3-pro pandiol is reacted by preparing dimethyl malonate from the 17.1% house. Sample 11. In a tubular reactor with a jacket, internal diameter. 10 mm is packed with 10 g of the catalyst of example 4, heated at 60 ° C with warm water transported in the jacket. When air is introduced at a rate of 2 l / h and a 7% solution of methacrolein in methanol at a rate of 30 ml / h through the top of the reactor. the reaction is carried out with an irrigation flow, and the conversion of methacrr-lein is 82%, the yield of methyl methacrylate is 74.2% (90.5% selectivity) Small amounts of methacrylic acid (2.9% selectivity), propylene are obtained as by-products. (0.5% selectivity), carbon dioxide and methyl formate. Example 12. In a jacketed jacketed reactor with an inner diameter of 7 mm, 7.5 g of the catalyst prepared according to reference example 2 is packed and a 4% methacrolein in methanol solution is introduced into it at a rate of 10 ml / h at 60 ° C; t at a rate of 1 l / h at 60 ° C to conduct a reaction with an irrigation flow. The conversion of methacrolein is 28.0%, the yield of methyl methacrylate is 26.3% (93.9% selectivity), propylene was not detected as a by-product. Example 13. The reaction is carried out under conditions analogous to example 11, however, the solution obtained by adding magnesium acetate to a solution of methacrolein in methanol so that the concentration of magnesium acetate in solution is 1 g / l is introduced into the reactor. After 200.h, methacrolein conversion is equal to 83.4%, methyl methacrylate is obtained as the main product with a yield of 72.8% (87.3% selectivity). Methacrylic acid is obtained as by-products in a yield of 1.9% (2.3% selectivity), propylene in a yield of 1.2% (1.4% selectivity), methyl formate (3.5 MOL.% / MMA) and dioxide carbon. After 2000 parts of methacrolein it is equal to 79.3%, the total weight of methyl methacrylate is 72.3% (91.2% selectivity), methacrylic acid - 1.9% (2.3% selectivity), propylene - 0, 5% (0.6% selectivity). Additionally, methyl formate (3.0 mol.% / MMA) and carbon dioxide (1.7 ml.% / MMA) are obtained from the beginning of the reaction and after 2000 hours the amount of methyl methacrylate obtained is almost constant. Example 14. The reaction was carried out similarly to Example 13, however, magnesium acetate (1 g / l) was replaced with calcium acetate (1 g / l). After 50 h, the conversion of methacrolein is 78.6%, methyl methacrylate is obtained in a yield of 70.1% (89.1% selectivity). After 200 hours, almost constant results were obtained: methacrolein conversion. 75, 3%, 69 (4) methyl methacrylate yield (92.2% selectivity). The amount of by-products is small as in Example 10.
    Example 15. A catalyst (Example 1) is charged to the reactor with 3.5 g of methacrolein and 100 ml of ethanol and air is blown into it at a rate of. 10 l / h at 40 ° C. The reaction is carried out for 2 hours. Methacrolein conversion is 75.5%, the yield of ethyl methacrylate is 65.3% (86.5% selectivity) ..
    Example 16.4 g of catalyst (Example 4) 3.5 g of methacrolein and 100 MP of methanol are introduced into the reactor and oxygen is blown at a rate of 3 l / h at 40 ° C to carry out the reaction for 1 h. Conversion of methacrolein is 99%, methyl methacrylate yield - 94.3% (95.3% selectivity).
    Example17. 4 g of catalyst (Example 4), 5.6 g of acrolein and 100 ml of ethanol are charged to the reactor, air is blown into the reactor at a rate of 10 l / h at 50 ° C and reacted for 2 hours. The conversion of acrolein is equal to 87.5%, the yield of ethyl acrylate is 81.2% (92.8% selectivity).
    Example 18 Into 100 ml of dimethylformamide (DMF), 2.36 g of a brown precipitate (which is a Pd-Pb complex, does not absorb IR rays due to nitrile and absorbs IR rays due to the acetic acid radical) dissolved in acetone. -. Tata of lead and bis (benzonitrile) palladium chloride, obtained in the same way as in reference example 1, is added with 10 g of 2% magnesium on alumina, impregnated with a solution, separated by filtration and then
    washed with water. To the washed carrier, 100 ml of water are added, followed by the addition of 4 ml of an aqueous formaldehyde solution and 20 ml of 1N. an aqueous solution of sodium hydroxide at 60 ° C. The support thus treated is separated by filtration, washed with water, then dried to obtain a catalyst. When the reaction is carried out under conditions similar to Example T, using 4 g of catalyst, methacrolein conversion is 55%, the yield of methyl methacrylate is 52.2% (95.0% selectivity). As byproducts, methyl formate and small amounts of propylene (0.4% selectivity) and carbon dioxide are obtained.
    PRI eriy.19-28. The reaction is carried out analogously to example 1, except that the catalyst is replaced by a catalyst, is given in table. 2. The results are shown in Table. 2, where the numbers at the top of the symbols, the metal atoms in the Isho column of the catalytic composition indicate the initial amounts (% by weight of metals on the substrate calculated on the carrier, and the compounds after the right bracket are the carriers. As a result of x-ray diffraction in the catalyst of the example 19, an intermetallic compound was formed: PdjHgj (20 38.5, 42.2, 68.0, 74.7), and the catalyst used in Example 20 was such an intermetallic compound that diffraction peaks appeared at diffraction angles ( 20) 38.9, 45.2, 65.8 and 79.
    (I
    and St; you l i
    According to diffraction peaks, it was confirmed that the catalyst of Example 21 is Pd-TJ. interme tallic compound with 2Q 38.5, 44.7, 65 and 78.1. In all cases, no diffraction peaks were detected for metallic palladium. Diffraction experiments were carried out at angles of 30–, however, in the case of an alumina carrier, the determinations were carried out at large angles, because the diffraction peaks of alumina overlap those
    refer to intermetallic compounds,
    Examples 29-33. The reaction is carried out analogously to example 1, except that the catalyst of example 1 has been replaced by the catalyst shown in table. 3. The reaction is carried out at 50 ° C, as a result of which the data given in Table 1 are obtained. 3. Using X-ray diffraction, it was determined that an intermetallic compound was obtained.
    Table 3
    29 30 31 32 33 Example 34. A four-neck flask with a capacity of 200 mp, equipped with: 4 g of a condenser based on dry ice methanol, a gas inlet with a stirrer and a thermometer; catalyst (Ilg / AlgO,), 100 ml of methanol and 7 g and -octylalde gTvda; , oxygen is blown at a rate of 3 l / h at 40 ° C, with the result that the reaction takes place over 2 hours. Methyl H-octanoate is obtained with a yield of 65.4%, the conversion degree of α-octylal dehydro is 75.3% (selectivity 86.8%). Example 35. The process is carried out similarly to example 34, however, instead of--octylaldehyde, 7 g of isovaler of new aldehyde is used, resulting in methyl isovalerate with a yield of 61.4%, the degree of conversion of isovaler of aldehyde is 72.1 % (selectivity 85.2%). EXAMPLE 36, The process is carried out analogously to example 34, however, instead of P-octylaldehyde, 7 g of P-toluolaldehyde are used, resulting in methyl-P-toluate with a yield of 52.4% The L-toluol aldehyde conversion rate is 59.0% (selectivity 88.8%). Example 37. 4 g of Pd catalyst (1.0) and 100 ml of methanol are introduced into the flask, oxygen is blown at a rate of 3 l / h at 55 ° C, as a result of which the reaction proceeds for 2 hours. 6.3 g of methyl formate are obtained . Example 38. Analogously to Example 1, catalysts are prepared, of which the first contains 2 wt.% Mg, 5 wt.% Pd and 2 wt.% Pb on the carrier, and the second contains 2 wt.% Mg, 0.5 wt.% Pd and 10 wt.% Pb on a carrier. In a four-necked 200 ml flask are placed 100 ml of methanol, 7 g of methacrolein and the catalyst. The reaction was carried out at 40 ° C for 2 hours, Og passes at a rate of 5 l / h. The following results are given in Table. four.
    Table 4
    Example 39: 0.8 g of potassium acetate and 0.92 g of lead acetate were dissolved in 40 cm of water and 10 g of silicate was added to the resulting solution. The resulting mixture is subjected to impregnation, then evaporated to dryness in a boiling water bath with stirring and then calcined for 3 hours in air at 500 ° C. For impregnation of the product thus treated with palladium, a diluted hydrochloric acid solution containing 0.83 g of hydrochloric palladium heated to 60 ° C is added to it with stirring. Thereafter, 2 ml of a formaldehyde aqueous solution and 1N are added to the mixture. aqueous sodium hydroxide solution. The supported catalyst thus obtained is filtered off, washed with water and dried.
    A 200-ml flask, cooled with a mixture of dry ice and methanol, equipped with a gas inlet tube, a stirrer and a thermometer, is charged with 100 ml of methanol, 4 g of the catalyst prepared in this way and 7 g of methacrolein. For 2 hours, a stream of oxygen is passed through the mixture at a rate of 5 l / h. The conversion ratio of methacrolein is 78%. Methacrylate formation occurs, with selectivity, 88, 5%.
    Example 40. The process is carried out analogously to example 39, however, in preparing a catalysts, 0.67 g of sodium acetate is used instead of potassium acetate. Using the obtained catalyst, the reaction is carried out analogously to example 39. The methacrolein conversion is 83.4%, methyl methacrylate is obtained with a selectivity of 86.2%,
    Example41.In a 300 ml reactor equipped with a stirrer, a condenser with a gas outlet gas tube at the end, tubes for supplying gas and liquid, a layer
    to separate the catalyst and tube to remove the reaction product, load 72 g of the catalyst having the composition Pd Pb Mg / AljOj and feed it with a 20% methanol solution
    methacrolein at a rate of 100 ml / h, as well as NaOH so that the pH of the system is in the range of 7.0 - 7.5, as well as the air required for the reaction at a rate of 60 nl / h with a total pressure of 8 kg / cm . The results are given in table. five.
    Table 5
    EXAMPLE 42. The process is carried out analogously to example 41, however, the reaction is carried out at 30 ° C for 4 hours using the catalyst of example 41. The methacrolein conversion is 71.0%, methyl methacrylate is obtained with a selectivity of 93, 7%.
    PRI me R 43. In a 300 ml autoclave equipped with a stirrer, 10 g of a catalyst of the same composition as in Example 41, 100 ml of methanol and 30 g of methacrolein are loaded and oxygen is passed through the mixture at 60 C and 50 kg pressure / cm for 4 hours. The methacrolein conversion rate is 73.5%, methyl metha-. Crilat is obtained with a selectivity of 87.1%.
    8 pp. And m. 44. 8.3 g of palladium chloride and 12.3 g of thallium acetate (Pd: Tl 1g1 atomic ratio) are dissolved in 100 ml of a dilute aqueous solution of hydrochloric acid. Formalin and 1N are added to it. NaOH aqueous solution. The resulting mixture is subjected to a reduction treatment to obtain a black powder. Similarly, black powders, Pd-Hg and Pd-Bi, are obtained. The Pd-Bi powder is then subjected to reduction with Hj at 150 ° C for 2 hours. The powders obtained in this way show the same X-ray diffraction maxima as
    Pd - T1 (loaded
    with respect to 1: 1)
    Pd - Hg (same as
    and above)
    Pd - Bi (the same as
    above) NOTE Ma: metacrol EXAMPLE 45. The reaction is carried out analogously to example 44, except foro, that the catalyst was replaced with 4 g of one of the catalysts shown in Table. 7 which
    Responsibly In examples 21, 19 and 20, which are determined by X-ray diffraction test.
    In the autoclave with a capacity of 200 ml, equipped with a stirrer, cooling means, an inlet
    100 ml of methanol and 10 ml of methacrolein are charged with gas and an injection valve, after which 8 g of one of the resulting catalysts is added to this mixture. This reaction
    carried out by blowing a gas mixture consisting of 10% Oj-Nj at a rate of 10 nl / h.
    The conditions used and the results obtained are shown in Table. 6
    Table
    53
    88
    32
    91
    . 7
    47
    85, MMA: methyl methacrylate. " . were obtained in the same way as in example 2. As a result of the interaction, 10 g of the aldehyde indicated in Table. 7, with 10Q MP of methanol, the results shown in Table 1 are obtained. 7., Pd TlVAl Oj Pd IlgVC,
    . I 0.5 /
    Table 7 Octyl aldehyde Propyl aldehyde Isobutyraldehyde 80 Benzaldehyde 100 3 4 amine 5 5 5 3 3 4 20 3
    权利要求:
    Claims (1)
    [1]
    : METHOD FOR PRODUCING COMPOUND / ETHERS OF CARBONIC ACID OXIDE. lower C, - C 4 alcohol and SC-C (0- aldehyde by means of an oxygen-containing gas in the liquid phase under heating and pressure using a metal catalyst, characterized in that, in order to increase the selectivity of the process, the oxidation is carried out at 30-100 ° C and pressure
    1-50 kg / cm 2 , and as a metal catalyst use a catalyst containing an intermetallic compound of the general formula where A is Pb, T1, Hg or Bi, or a catalyst of the general formula ^ 0.5-10.0 ^ 4-20 Pc1 015 -U 10 / Carrier >
    where A is Pb, T1, Hg or Bi;
    B is Na, K, Li, Mg or Ca, and the numerical values represent the mass percent of metals with respect to the support, with a ratio of Pd: A 1: (0.4-20) and using Si0 2 , A1 2 O as the support 3 , activated carbon, Fe 2 0 3 , MgO or CaCO 0 .
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    同族专利:
    公开号 | 公开日
    AU518930B2|1981-10-29|
    NZ193742A|1982-03-23|
    BR8002986A|1980-12-23|
    IN151805B|1983-08-06|
    NL181356C|1987-08-03|
    MX153577A|1986-11-27|
    AR220625A1|1980-11-14|
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    引用文献:
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    WO2021102415A1|2019-11-22|2021-05-27|The Johns Hopkins University|Pulsed electrochemical deposition of ordered intermetallic carbon composites|
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    EP1994978A1|2007-05-25|2008-11-26|Evonik Röhm GmbH|Process for preparation of methyl methacrylate by esterification during oxidation|
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    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    JP54059631A|JPS627902B2|1979-05-17|1979-05-17|
    JP54059632A|JPS627903B2|1979-05-17|1979-05-17|
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