• 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:
    A process for olefin bond isomerization by means of a gamma alumina-based catalyst containing SiO2 and oxides of a metal chosen from those of Group II A and/or VIII and/or III B and/or Lanthanides, with particular molar ratios between the various oxides. The catalyst is thermally stable, and in the conversion of butene-2 to butene-1 enables butene-1 to be obtained with an isobutene content below the allowable limits for butene-1 grade polymerization.
    公开号:SU1333231A3
    申请号:SU833598342
    申请日:1983-05-26
    公开日:1987-08-23
    发明作者:Форлани Орфео；Анциллотти Франческо；Нотари Бруно
    申请人:Снампрогетти С.П.А. (Фирма)；
    IPC主号:
    专利说明:

    113
    The invention relates to petrochemistry, namely to the production of butane-1 by isomerization of butene-2.
    . The purpose of the invention is to prevent the formation of by-products.
    PRI me R 1. (comparative). 20 g of Y-alumina (with a specific surface area of 200) are impregnated with 15 cm of an aqueous solution containing 1.8 g of lanthanum nitrate. The material is then dried and calcined at 500 ° C for 4 hours. The resulting material contains 3.5% by weight on alumina and has the formula
     , 0.01Q-La O ,.
    The catalyst thus obtained is placed in a flow reactor. the type in which butene-2 isomerization is carried out.
    When this process is carried out beyond the limits, butane-1 cannot be obtained when the content of isobutene is below the maximum permissible limit (0.1% by weight relative to butene-1).
    Example 2 A catalyst is prepared similarly to that described, containing 5 wt.% Ba, 0h on alumina, having the formula A1., 01 3.
    Example 3. The process is carried out as in Example 1, but a catalyst containing 7.5% by weight on alumina, having the formula X 0.023, is obtained.
    Example 4, the process is carried out as in example 1, but a catalyst containing 10.0 wt.% On alumina, having the formula AljO, is obtained 0.031.
    In tab. 1 shows the results of isomerization of butene-2 according to examples 1-4 and the values of the specific surface of the catalysts after heat treatment for 24 hours are indicated at.
    Example5. 20 g of J-alumina (specific surface 200) are treated with 15 cm of an alcohol solution containing 0.75 g of Dynasil A 40 (40% ethyl O-liquate). The mixture is kept at 50 ° C, then the solution is drained, the residue is treated with water vapor in order to hydrolyze the silanol groups, dried and calcined at 500 ° C for 4 hours.
    12
    The material thus obtained, containing 1.5% by weight of SiO, is impregnated with 5.14 g of lanthanum nitrate, as described in Example 1.
    A material consisting of J-alumina, stabilized by 1.5 wt.% Si02, and containing 10 wt.%, Is obtained. -.
    The catalyst has the formula
    , b-SiOj
    with ,
    where C is 0.664 + 0.014; L 0.0250;
    but
     0.0642.
    This catalyst is introduced into a reactor in which trans-butene-2 is isomerized.
    Primarb. 20 g of alumina are impregnated according to the method described in Example 5 with an alcoholic solution of o-silicate, resulting in a material that, after steaming and calcining, contains 3.8 wt.% SiO.
    This material is then impregnated with the required amount of solution of lanthanum nitrate so that a content of 10.0 May is obtained. % Thus, a catalyst is obtained by providing 3.8% by weight of SiO and 10% by weight on alumina. Catalyst Imamat formula specified in example 5, where
    C 0.233 L + 0.014; b 0.063;
    B + c
     Oh, 111.
    EXAMPLE 7 Analogously to Example 5, a catalyst is obtained containing 8% by weight SiO, j and 15% by weight La on alumina. The composition of the catalyst corresponds to the general formula given in Example 5, where
    C 0.241 b + 0.014; L 0.133;
    b + C
     0.2099.
    Example 8. Using silicified alumina containing 3.8% by weight of SiOj (according to Example 6) by impregnation with an aqueous solution of rare-acetate 3133231
    grinding metals REE. A catalyst containing 10 wt.% REE oxide is obtained, the coefficients in the general formula of which, specified in Example 5, are related by the relations
    C 0.174L + 0.016; b 0.133;
    a + b
     0.0739.
    PR and m-r 9 (comparative). Analogously to example 5, a catalyst is prepared containing 5.0 wt.% And 1.5 wt.% SiOj J-alumina. The coefficients Q, b, c in the formula are related by
    С 0.05Ь + Ь + С
    0.014; 0.0430.
    In tab. 2 is given in Examples 5-9, data relating to the tests carried out, and the values of specific gravity are shown (Noah, the surface of the catalysts after heat treatment for 24 hours at 1000 ° C.
    Example 10. Using the silica alumina obtained in Example 5, a catalyst is obtained by impregnating this silica alumina (wt.% SiOg) with an aqueous solution of calcium nitrate in such an amount that the final ready-to-use catalyst contains 2.5 wt.% calcium oxide. The catalyst has a composition of SiD to SSAO, where
    L 0.025; C 0.584 +
    0.030;
    B + c
     0.0739.
    The value of 0.030 is the number of moles of CaO in the catalyst, the required dp to maintain the amount of isobutene within the specified limits when using alumina, which is not stabilized by silica.
    Example 11. Isomerization of butene-2 to butene-1 is carried out on a catalyst containing 1.5% by weight of SiO and 5.0% by weight. CaO on alumina. The catalyst corresponds to the general formula given in Example 10, where b
     0.025; C 0.372L + 0.030; (B + c):., 1214.
    Example 12. Analogously to example 10, get a catalyst containing 2.5 wt.% CaO and 3.8 wt.% SiO on 2-alumina. Ratio ratio
    WITH
    B
    0.2306 L + 0.063;
    0.030;
    but
    0.1170.
    E, the isomerization results of butane-2 to butene-1, according to examples 10-12, on this catalyst are given in table. 3
    All the catalysts used in Examples 10-12 are subjected to aging tests that include 40 reaction cycles (332 hours in total) and 40 regeneration cycles (152 hours in total) without loss of catalytic activity. Regeneration is carried out at.
    Example 13. The catalyst composition of 1.5 wt.% SiOj + 4.0 wt.% BaO on alumina prepared according to. Example 10 (barium is injected similarly to calcium in the form of a barium nitrate solution). For this catalyst, the coefficients in the general formula a, with BaO are related by the ratios
    C 0.240 L + 0.020; L 0.025;
    -C-.0.055 ,.
    The value of 0.020 is the number of moles of BaO in the catalyst, which is necessary in dp to maintain the amount of isobutene within the specified limits when using alumina not stabilized by silica.
    Example 14. A catalyst containing 3.8 wt.% SiO and 8.0 BaO% on alumina is prepared analogously to Example 9. The catalyst responds to the general formula given in Example 13, where C 0.5055 is L + 0.020;
    L 0.063; 0.12281.
    Example 15. Catalyst composition 3.8 wt.% SiO wt.% SrO and alumina prepared according to example 10. The catalyst has a total
    formula a b SiDj CSiO, the coefficients d, b, and C are related by the relations
    C 0,2l52b + 0,020; b + C
    q
     0.1080.
    The results of isomerization of butene-2. In butene-1- in examples 13-15 on this catalyst are given in table. four.
    Example 16 (comparative). The catalyst is obtained as described above,. containing 2.5 wt.% Fe ,, 0j and 1.5 wt.% SiOj on J-alumina. Ratio of coefficients (10 of the a, b, and C atoms of the general formula of the catalyst q Al, X bSiO C are related by ratios.
    C 0.092 + 0.018; B + c
    Q
     0.0432.
    Example 17. The catalyst composition of 1.5 wt.% SiOj and 5 wt.%. , on alumina is prepared similarly (iron is introduced in the form of an aqueous solution of nitrate of iron). The catalyst corresponds to l} in the general formula C | Al ,, b SiOj whose coefficients are related by the relations
    C 0.5376L + 0.018; b 0.025 |
      0.0615.
    Example .18 (comparative). Analogously to example 17, catalyst is carried out containing 2.5 wt.% And 3.8 wt.% SiO on J-alumina. The ratios of the coefficients a, b, and C are as follows:
    C 0.0363 - t - 0,018; . 0.0860.
    Example 19. Analogously to example 18, a catalyst is obtained containing wt.% SiO and 7.5 wt.% On V-alumina. The coefficients a b and C in the general formula are related by
    C 0.351L + 0.018; L 0.083;
    0 |
    0.1521.
    The results of the process of isomerization of butene-2 to butene-1 according to examples 16-19 on this catalyst are given in table. five.
    In so-called "1-5 isomerization is carried out under the following reaction conditions: temperature 470 ° C, pressure P 1 atm, amount of trans-butene-2 per unit of mass of catalyst per 1 hour is equal to 6. In the reaction products are linear butenes are always present in an amount corresponding to thermodynamic equilibrium at the specified reaction temperature.
    权利要求:
    Claims (5)
    [1]
    1. A method of producing butene-1 by isomerizing butene-2 in the presence of a catalyst based on activated alumina at 470 ° C at a mass feed rate of 6h, characterized in that, in order to prevent the formation of by-products, a catalyst of the general formula
    but
    Al OybSiD
    With Me.Ou,
    where is the oxide of a bivalent or trivalent metal selected from the group of lanthanum, calcium, strontium, barium, iron (III);
    C1, b, c is the number of molecules, SiD and respectively, interconnected by the relations
    C tb + B
    45 where
    B 05013-0-031; m 0,2192-0,664; B 0.0250-0.133;
      0,0551-0,209,
    X, y - correspond to the valence of the metal in the acid, or catalyst of the general formula
    (0.013-0., 031) La5.0z.
    [2]
    2 o The method according to p. 1, on.
    71333231
    analyzer where is the oxide lan
    tana and
    m 0,233-0,664; in 0.014}
     WITH
    but
     0.0642-0.209.
    [3]
    3. The method according to p. 1,, o tl and h aa yu and with the fact that they use a catalyst, where is calcium oxide and
    m 0,2306-0,584; B 0.030;
    but
    0.0739-0.1214.
     In the form of oxides of rare earth metals.
    eight
    [4]
    4, the method according to p. 1v on tl and h a - y i and with the fact that they use a cationator, where is barium oxide
    and
    WITH
    0.240-0.5055; 0.020;
    0.0551-0.1281.
    [5]
    5. The method according to claim 1, wherein the catalyst is used, where is iron oxide and
    55 0.351-0.5376;
    And - 0,018;
    but
    0.0613-0.1521 Table 1
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    同族专利:
    公开号 | 公开日
    ZM3683A1|1984-01-23|
    NL8301872A|1983-12-16|
    HUT34419A|1985-03-28|
    RO86409A|1985-03-15|
    PL141424B1|1987-07-31|
    CS244933B2|1986-08-14|
    SE8302849L|1983-11-28|
    ATA192583A|1986-09-15|
    MW2283A1|1985-02-13|
    DE3319171A1|1983-12-01|
    NO831847L|1983-11-28|
    IT1190839B|1988-02-24|
    FR2527596A1|1983-12-02|
    BE896849A|1983-11-28|
    IN159131B|1987-03-28|
    PT76764A|1983-06-01|
    LU84823A1|1984-03-07|
    FR2527596B1|1985-04-19|
    GR81339B|1984-12-11|
    NZ204340A|1986-01-24|
    IN158661B|1987-01-03|
    GB2121430B|1986-09-24|
    KR870000055B1|1987-02-09|
    IT8221511D0|1982-05-27|
    ES8500201A1|1984-10-01|
    US4814542A|1989-03-21|
    AU552806B2|1986-06-19|
    CA1199041A|1986-01-07|
    ZW11283A1|1983-07-27|
    DD209801A5|1984-05-23|
    DK234583A|1983-11-28|
    DE3319171C2|1989-01-26|
    GB2121430A|1983-12-21|
    PT76764B|1986-03-27|
    JPS58219128A|1983-12-20|
    AU1453583A|1983-12-01|
    PL242214A1|1984-07-02|
    KR840004702A|1984-10-24|
    AT382864B|1987-04-27|
    GB8313561D0|1983-06-22|
    YU113083A|1986-02-28|
    PH17965A|1985-02-22|
    RO86409B|1985-04-01|
    DK234583D0|1983-05-25|
    ES523076A0|1984-10-01|
    ZA833396B|1984-05-30|
    SE8302849D0|1983-05-19|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    US3313858A|1965-02-12|1967-04-11|Phillips Petroleum Co|Isomerization of non-terminal olefins|
    US3467727A|1966-10-10|1969-09-16|Universal Oil Prod Co|Isomerization of 2,3-dimethylbutenes|
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    US4217244A|1978-05-11|1980-08-12|Phillips Petroleum Company|Regeneration of isomerization catalysts containing magnesium oxide|
    US4229610A|1978-11-03|1980-10-21|Phillips Petroleum Company|Olefin double bond isomerization|
    FR2506297B1|1981-05-21|1986-05-02|Inst Francais Du Petrole|PROCESS FOR ISOMERIZING OLEFINS|
    IT1190839B|1982-05-27|1988-02-24|Anic Spa|PROCEDURE FOR THE ISOMERIZATION OF BOND OF THE OLEFINS|IT1190839B|1982-05-27|1988-02-24|Anic Spa|PROCEDURE FOR THE ISOMERIZATION OF BOND OF THE OLEFINS|
    EP0225407A1|1985-01-25|1987-06-16|Council of Scientific and Industrial Research|Lanthanum silicate materials, their production and use|
    FR2584388B1|1985-07-03|1991-02-15|Rhone Poulenc Spec Chim|COMPOSITION BASED ON CERIC OXIDE, ITS PREPARATION AND USES THEREOF|
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    DE102015200702A1|2015-01-19|2016-07-21|Evonik Degussa Gmbh|Preparation of butadiene from ethene|
    JP6571392B2|2015-05-29|2019-09-04|Ｊｘｔｇエネルギー株式会社|Isomerization catalyst, linear olefin production method and compound production method|
    JP6736017B2|2015-11-05|2020-08-05|Ｅｎｅｏｓ株式会社|Isomerization catalyst, method for producing linear olefin and method for producing compound|
    EP3490967B1|2016-07-28|2021-05-05|Lyondell Chemical Technology, L.P.|Paraffin removal from c4 containing streams|
    JP2020097544A|2018-12-18|2020-06-25|Ｊｘｔｇエネルギー株式会社|Manufacturing method of straight chain monoolefin and manufacturing method of compound|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    IT21511/82A|IT1190839B|1982-05-27|1982-05-27|PROCEDURE FOR THE ISOMERIZATION OF BOND OF THE OLEFINS|
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