• 专利附录
  • 专利说明
  • 权利要求
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  • 优先权
    • 专利摘要:
    A catalyst for the production of hydrocarbon consists essentially of crystalline aluminum silicate, at least one compound of the metal zinc and/or cadmium and additionally silica. The catalyst is produced by heating a crystalline aluminum silicate, in a given case partially or completely converted to the hydrogen form, with a zinc and/or cadmium compound and molding with a silica containing binder.
    公开号:SU1217246A3
    申请号:SU833618701
    申请日:1983-07-18
    公开日:1986-03-07
    发明作者:Бааке Михаэль；Деллер Клаус；Кляйншмит Петер；Коберштайн Эдгар
    申请人:Дегусса Аг (Фирма)；
    IPC主号:
    专利说明:

    Ci H s-CH-CH -SlCHj)
    he
    at the temperature under its own pressure in the autoclave with subsequent separation of the precipitate of the formed pentasil, washing it
    one
    The invention relates to catalysts for the conversion of synthesis gas to hydrocarbons and methods for their preparation with a higher selectivity towards ethane.
    The aim of the invention is to increase the selectivity of the catalyst for ethane and to obtain a catalyst with increased selectivity for ethane by containing and using a certain type of zeolite and a binder.
    In addition, a catalyst with increased selectivity is obtained by forming a specific structure of the zeolite in the presence of a hydroxy compound in a certain mode of interaction between the components forming it.
    Example 1. Obtaining a catalyst. 5 g of sodium aluminate and 25 g of sodium hydroxide are dissolved in 50 m of water and the prepared solution is added to a suspension of 20D g of precipitated silicic acid and 75 g of CHOHC S (CH-), 1 in 2 × 00 ml of water. Mixture of ne
    rotates for 80 hours at 160 ° C in an autoclave at its own pressure, then filtered and washed the product with water to pH 9. The wet filter mass is suspended in 2 liters of ethyl alcohol, the product is filtered, rinsed with ethyl alcohol and dried at 120 C. 100 g dried silicate is stirred in 1 l 2 n. hydrochloric acid solution for 2 h at 80 ° C, the product is filtered off, washed with water until neutral reaction with industrial water and dried at 120 C.
    Analysis data: 0.06% by mass of sodium oxide; 1.74 May,% oxide al.yum1217246
    and drying or using pentasil, obtained by the method described above and treated with acid for conversion into the hydrogen form, the resulting pentasil is treated with an aqueous solution of zinc salt, dried and molded with a binder containing silica.
    neither; 91.1% silica; 3.2% pp pp
    On the x-ray diffraction diagram, aluminum silicate has the following characteristic inter- actions;
    0
    five
    0
    five
    five
    0
    d-value
    11.17 + 0.1 10.05 + 0.1 6.34 + 0.1 4.98 + 0.03 4.35 ± 0.03 4.27 + 0.03 3.85 + 0.03. 3.74 + 0.03 3.66 + 0.03 3.45 + 0.03 3.34 + 0.02 2.98 + 0.02 2.49 + 0.02 2.00 + 0.02 p and measure 2,
    Interferential
    52 35
    five
    four
    18 23,100 54 22
    7
    eight
    12 12
    P
    50 g of aluminosilicate in accordance with Example 1 is mixed in a solution containing 136.3 g of zinc chloride in 500 ml of water for one hour at 80 ° C, the product is filtered, washed with water and dried. The resulting aluminum silicate containing zinc, has the following composition, May.%:
    Zinc Oxide 0.74
    Sodium oxide 0.01 Aluminum oxide 1.63 Silicon dioxide Else Example 3.50g of aluminosilicate, obtained in accordance with Example 1, without acid treatment (O, 75 May,% sodium oxide, 1.52 May,% alumina, 89.6 May.% silica) mix in solution.
    3 .12
    containing 50 g of zinc chloride 50J ml of water, during two hours at 80 ° С and immediately after, by analogy with example 2, it is processed in the same way.
    The resulting aluminosilicate containing zinc has the following composition
    ae.%:
    Zinc Oxide 1 1 7
    Sodium oxide 0.18 Aluminum oxide 1 15 Silicon dioxide Rest Example 4. 50 g of the aluminosilicate obtained in accordance with Example 1 is suspended in a solution containing 1.25 g of zinc chloride in 100 ml of water and the suspension is stirred for two hours at 80 ° C. The resulting mixture is dried at 50 ° C and a pressure of 50 mbar.
    The resulting aluminosilicate, zinc content, has the following composition, May. %: Zinc Oxide1 5
    Sodium oxide 0.03 Alumina 1 54 Silicon dioxide Else Example 5, 50 g of aluminosilicate obtained in accordance with Example 1 in hydrogen form and 1.5 g of zinc oxide are suspended in 100 ml of water, after which the suspension is stirred for two hours at 80 C. The resulting mixture is dried at 50 ° C and a pressure of 50 mbar.
    The obtained aluminosilicate, pre-treated with salt, has the following composition, wt.%:
    Zinc Oxide 2.9 Sodium Oxide 0.04 Aluminum 1.7 Dioxide Silicon Rest PRI me R 6. Aluminosilicate, prepared as in Example 4, is treated in an analogous manner with an aqueous solution of zinc acetate. All other things being equal, 4.3 g of zinc acetate are used. Immediately thereafter, the resulting aluminum silicate, pre-treated. zinc salt, calcined at a temperature of 440 ° C, and the resulting product has the following composition, wt.%:
    Zinc Oxide. 3.1 Sodium oxide 0.02 Alumina 1.26. Silicon dioxide Rest Example. Molding 50 g pre-treated powder 7246
    The alumina silicate obtained in accordance with Examples 1-6 is transferred from 15 mp of 40% silica gel and 15 ml of water to obtain a pasty mass, after which it is molded on granulating plates. After drying (4 hours at) the granulated product is calcined at 440 ° C and then sieved.
    Get the catalyst following composition, wt.%:
    Zeolite type pentasil containing 0.74 wt.%. 5 zinc oxide85
    Silica 15
    Fraction e with a particle size of 0.3-1 mm is used to convert synthesis gas. 0 The transformation of CO / H2.
    PRI me R 8. A mixture of synthesis gas, which contains hydrogen and carbon monoxide in a molar ratio of 2: 1, at 400 ° C, a pressure of 5–80 bar and a space velocity of 500 is passed through a catalyst bed.
    The results obtained here are presented below.
    Conversion of synthesis gas takes place on aluminosilicate obtained in accordance with example 2 and molded in accordance with example 7. Temperature, ° С 400 Pressure, bar 80 Volume velocity, volume / volume h 500 Conversion of carbon monoxide to hydrocarbons,% 18 N / CO2
    Total conversion of synthesis gas,% 25 Distribution of hydrocarbons, May. % :.
    methane22
    ethane. 70
    five . 3
    five
    0
    five
    propane
    with;
    50 Example9. Synthesis gas conversion is carried out in a fixed bed reactor with a diameter of 10 mm and a reaction volume of 60 ml. 40 ml is placed in the reactor.
    55 of the catalyst obtained in accordance with example 2. The catalyst is activated by what is through it at 450 C and a pressure of 2 bar
    for 4 h pass nitrogen in the amount of 10 l / h
    Then, synthesis gas is passed through the reactor, and the composition, volume velocity, reaction temperature / ra, and pressure 5 at which the reaction is carried out are presented in Table 1.
    In tab. 1 also indicates the general conversion of synthesis gas, the conversion of carbon monoxide into hydrocarbons and the distribution of hydrocarbons.
    The gaseous mixture leaving the reactor is brought to atmospheric pressure and passed at -20 ° C through a low-temperature trap. In a low-temperature trap, products that cannot condense in it are separated. The gas mixture S leaving the low temperature trap is passed through a gas sampling tube for analysis.
    Example 10, The method is carried out by analogy with that described in Example 9, with the parameters and results used in the implementation of the method being presented in Table. 2
    When measure 11. The method is carried out by analogy with the description in Example 9, with the parameters used in the implementation of qnoco6a and the results obtained are presented in Table 3,
    Example 12. The method is carried out by analogy with that described in Example 9, wherein the parameters used in the process and the results obtained are presented in Table. four,
    Example 13, The transformation is carried out as KA, in example 8. Obtained: - The results are presented below,
    The synthesis gas conversion is carried out on an aluminosilicate catalyst prepared according to example 6 and formed according to example 7; the following | its composition, mas: zeolite of the pentasil type, containing 3.1 wt.% zinc oxide 82., silicon dioxide 18.
    Temperature, C
    Pressure bar Volume rate, volume / volume-h
    400 80
    500 2.2
    Conversion of carbon monoxide to hydrocarbons Total synthesis gas conversion Hydrocarbons distribution, May.%:
    methane
    ethane
    propane
    with:
    17.4 18 o
     four
    29.0 62.0 5.0 4.0
    Example 14. 50 g of conventional β-zeolite are treated by analogy with example 2 and molded in accordance with example 7. A catalyst of the following composition is prepared, wt.%: U type zeolite, containing 10.7 wt.% Zinc oxide 87, silica 13.
    The results of using the catalyst in the conversion of synthesis gas are lower,
    (Temperature, C
    Pressure, bar Volume velocity volume / volume-N ,, / WITH
    Conversion of carbon monoxide to hydrocarbons Total conversion of synthesis gas Distribution of hydrocarbons, wt.%:
    methane
    ethane
    propane +
    WITH.;
    t
    500 80
    500 2 2
     , xL
    21.0 24.7
    51 41 6 2
    Example 15 50 g of conventional mordenite type zeolite in a hydrogen form are impregnated, according to examples, 6.9 g of zinc acetate and the product obtained is formed according to example 7 and used to convert synthesis gas.
    The obtained results are presented in Table. five.
    The synthesis gas conversion is carried out on the catalyst composition, wt.%: Mordenite type zeolite containing 7 May,% oxide of cyan oxide 85, silica 15. Pressure 100 bar, H., / CO 1.72.
    Table 1
    propane
    butane and higher molecular weight hydrocarbons
    500 500 500
    400 400 400
    100 100 100
    Total conversion of synthesis gas,% 24.9
    20, 1 12.5 16.0

    37.5 29.6 48.0 45.0 60.6 36.5
    10.2 6.8 8.6
    7, 3 3.1 6.9
    Volumetric speed, volume / volume h
    Continued that bl. 2
    6.8
    5.9
    7.2 3.1 2.5 4.2
    14.5 17.9
    125
    125
    eleven
    121724612
    Continuation of table 4
     to borrow nieta bl. five
    ParametersResults
    , 8 12.1 8.65.9.

    , 3,6 2,40,9
    Ct 0.2 1.1 0.90.3
    权利要求:
    Claims (4)
    [1]
    1. The catalyst for the conversion of synthesis gas to hydrocarbons - containing c ^ rlit, including zinc oxide, and a binder, characterized in that, in order to increase the selectivity of the catalyst for ethane, the zeolite contains zeolite selected from pentasil groups in sodium or hydrogen form, type U zeolite and mordenite in hydrogen form and comprising 0.74-10.7 wt. X zinc oxide, and as a binder - silicon dioxide with the following components, wt.%:
    One of these zeolites, including 0.74-10.7 wt.% Zinc oxide. 82-87
    Silica 13-18
    [2]
    2. The catalyst on π '. 1, characterized in that the pentasil has a structure corresponding to x-ray diffraction pattern with the following characteristic β-interference:
    d-value interference
    11.17 + 0.1 52 10.05 + 0.1 35 6.34 ± 0.1 5 4.98 ± 0.03 four 4.35 + 0.03 eighteen 4.27 ± 0.03 23 3.85 + 0.03 one hundred 3.74 + 0.03 54 3.66 + 0.03 22 3.45 + 0.03 7 3.34 + 0.03 8 2.98 + 0.02 12 2.49 ± 0.02 • 12 2.00 + 0.02 8
    [3]
    3. A method of producing a catalyst for the conversion of synthesis gas to hydrocarbons by treating zeolite with an aqueous solution of zinc salt, drying, molding with a binder and calcining, characterized in that, in order to obtain a catalyst with increased selectivity for Ethane, zeolite is used pentasil in sodium or hydrogen forms, or type U zeolite, or mordenite in hydrogen form, and silicon dioxide is used as a binder.
    [4]
    4. The method according to p. 3, characterized in that they use pentasil obtained by interaction.
    water in sodium aluminate, sodium hydroxide, precipitated silicic acid and the compound of the following formula with 12 n 25 -sn-sn 7 - s (sn ^ it at a temperature of 160 ° C under its own pressure in an autoclave, followed by separation of the precipitate of the resulting pentasil, its washing and drying or using pentasil (obtained by the method described above and treated with acid to convert to the hydrogen form, the obtained pentasil is treated with an aqueous solution of zinc salt, dried and formed with a binder containing silicon dioxide.
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    同族专利:
    公开号 | 公开日
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    DE3228270A1|1984-02-02|
    引用文献:
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    US4096163A|1975-04-08|1978-06-20|Mobil Oil Corporation|Conversion of synthesis gas to hydrocarbon mixtures|
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    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    DE3228270A|DE3228270C2|1982-07-29|1982-07-29|
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