• 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:
    The invention relates to catalytic synthesis and, in particular, to an improvement in the method of deactivating a catalyst at the stage of its use during polymerization of polyisocyanates (PPI). The invention makes it possible to increase the stability of the polyisocyanate. In the preparation of PICs by cyclotrimerizing 1,6-diisocyanathexane in the presence of S, ethylaminotrimethylsilane or hexamethyldisilazane, at the moment when a given amount of isocyanurate groups is reached, 0.25-1 mol per 1 mol of the aminosilyl group of the catalyst is introduced into the reaction mixture. Water is introduced at 10-95 s. After storage of the obtained SC for a month, the content of NCO-rpynn practically does not change. ABOUT)
    公开号:SU1426456A3
    申请号:SU864027078
    申请日:1986-03-14
    公开日:1988-09-23
    发明作者:Робэн Жан
    申请人:Рон-Пуленк Спесьялитэ Шимик (Фирма)；
    IPC主号:
    专利说明:

    4 O5 4 SP
    but
    The invention relates to an improvement in the method of deactivating a catalyst at the stage of its use, in particular at the stage of catalytic partial cyclotrimerization of polyisocyanates.
    The purpose of the invention is to increase the stability of the polyisocyanate. The cyclotrimerization method can be carried out by simply heating the reagents at 50–180 ° C, preferably at 80–130 ° C and usually at
    . :
    Reaction cyclotrimerization can be carried out in a solvent, which can be an aliphatic or aromatic hydrocarbon, esters or ethers, low polarity. The catalyst can be introduced into the solvent and this solution is introduced into the isocyanate. Preferably, the process is carried out without a solvent. N, N-cyethylaminotrimethylsilane or hexamethyldistazan is used as the catalyst. When the iso-cyanurate content reaches the desired value, water is added.
    Example: In a flask with a 3L container, equipped with a stirrer and thermometer, 1600 g of 1,6-diizocytane hexane (9.5 mol) are charged. The mixture is heated on an oil bath until 16 g (0.1 mol) of hexamethyldisilazane is added and the temperature is raised to 120 ° C and held at this temperature for 2.5 hours. After this time, cool until approx. They contain NCO-groups, (which is 0.973 groups / 100 g. Then, with stirring, add-ft 0.9 g of water (0.5 mol per 1 mol of the catalyst) and hold such oxygen for 10-15 minutes.
    A part of the resulting mixture is taken and held for 20 h at 100 ° C. After this time, the con tent is that the content of NCO groups has not changed (the trimerization reaction has stopped).
    The remaining reaction mass is evaporated in vacuo using a thin layer evaporator with stirring until the residual content of free diisocyanate below 0.1% is obtained. After fakeni for 1 month. this content has remained virtually unchanged (below 0.2%).
    o
    five
    0
    five"
    50
    0
    Example 2. Carried out analogously to example 1. The mixture was cooled to 50 ° C and divided into two equal parts: ft - 0.05 mol of water (1 mol per 1 mol of aminosilyl catalyst group) was added to the first half and stirred for 15 minutes; o - the second half is added with O, 125 mol of water (0.25 mol of water per 1 mol of catalyst) and stirred for 15 minutes, one part is taken from each of these mixtures and kept for 20 hours. The NCO groups remain constant in both cases.
    The residue of these two reaction mixtures are vacuum-dried using a thin-film evaporator with stirring until a residual free diisocyanate content is less than or equal to 0.1% by weight.
    After storage for 1 month at 60 ° C, the content of HCO groups does not change for the product and exceeds 0.2% for product G.
    Example 3 Into a flask with a capacity of 3 liters, 1600 g of 1,6-diisocyanate-hexane (9.5 mol) was charged, heated on an oil bath at a SO with and 14.5 g (O, 1 mol) N, N- diethylamino5
    0
    five
    trimethylsilane stand
    3 hours
    about..
    at
    100 ° C, then cooled to 50 ° C. The content of NCO-rpynn is 0.9% by weight. While stirring, 0.9 g of water (0.05 mol) is added and held for 20 minutes.
    Analogously to Example 1, the stability of the NCO-rpynn content was ascertained after 20 hours at 100 ° C (the content was unchanged).
    The reaction mixture was spiked and after storage for 1 month at 60 ° C. The diisocyanate content remains almost unchanged.
    PrymeR 4. 1600 g of 1,6-diisodianate-hexane (9.5 mol) is charged into a 3 l container. Heat on an oil tank to 100 ° C and add 14.5 g (0.1 mol) K, 11-diethylamino-trimethylsilane. The mixture was incubated for 3 hours at and then cooled until. The content of NCO-rpynn is 0.9 wt.%.
    With vigorous stirring, 1.8 g of water (0.10 mol) is added and the mixture is maintained for 30 minutes. Ana-
    It is logical to Example 1 to note the stability of the NCO content after 20 h at (constant amount). Also, the reaction mixture is extruded and after 1 month of preservation at 60 ° C. The content of free diisocyanate remains almost unchanged.
    Example 5. In a capacity of 3 l load 1600 g of 1,6-diisocyanathexane (9.5 mol). DO is heated on an oil bath and 14.5 g (0.1 mol) of N, N-diethypamine-metmethylsilane are added. The mixture is held for 3 hours at 100 seconds and cooled slightly until. The content of NCO-rpynn is 0.9% by weight.
    While stirring vigorously, 0.45 g of water (0.025 mol) is then added and the mixture is kept for 5 minutes,
    Analogously to Example 1, the stability of the NCOrpynn content after 20 hours at 100 ° C (constant amount) is noted.
    Also, the reaction mixture is evaporated and after 1 month of preservation at 60 C. The content of free diisocyanate remains almost unchanged -.
    权利要求:
    Claims (1)
    [1]
    Invention Formula
    The method of producing polyisocyanates with isocyanurate groups by cyclo-trimer from the ation of 1,6-diisocyanate-hexane in the presence of H, to -diethyl-aminotrimethylsilane or hexamethyldisilazane, followed by introduction of hype into the deactivator reaction mixture at the moment when the specified amount of isocyanurate groups is reached, when a different amount of isocyanurate groups is reached, when a different amount of isocyanurate groups is reached, when a different amount of isocyanurate groups is reached, a different solution is obtained. By the fact that, in order to increase the stability of the polyisocyanate, water in an amount of 0.25-1 mol per 1 mol of the aminosilyl group of the catalyst is used as a deactivator, and water is introduced at 10-95 s.
    类似技术:
    公开号 | 公开日 | 专利标题
    SU1426456A3|1988-09-23|Method of producing polyisocyanates with isocyanurate groups
    CA1037640A|1978-08-29|Storage stable polyisocyanates and manufacture thereof
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    CA1257593A|1989-07-18|Process for the production of oligomericpolyisocyanates and their use in the production ofpolyurethane plastics
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    US4994541A|1991-02-19|Process for the preparation of polyisocyanates containing uretdione and isocyanurate groups, the polyisocyanates obtained by this process and their use in two-component polyurethane coatings
    US3248372A|1966-04-26|Glycol modified isocyanurate containing polyisocyanates
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    US4302351A|1981-11-24|Compounds containing isocyanuric groups and terminally blocked isocyanate groups
    US4490300A|1984-12-25|Liquid diphenylmethane diisocyanate compositions
    US4085140A|1978-04-18|Carbodiimides
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    US3394111A|1968-07-23|Process for the polymerization of uretdiones using aliphatic tertiary phosphine catalysts
    US3462470A|1969-08-19|Liquid polyisocyanate compositions and process for the manufacture thereof
    US4668780A|1987-05-26|Isocyanate-uretdiones and a method for their production
    US4490301A|1984-12-25|Liquid diphenylmethane diisocyanate compositions
    US2853518A|1958-09-23|Chemical process
    US4937339A|1990-06-26|Process for preparing isocyanurate ring-containing materials
    CN102442959A|2012-05-09|Process for preparation of polyisocyanates and use thereof
    US3970600A|1976-07-20|Stable, liquid solutions of isocyanurate-polyisocyanates containing amide and/or acylurea groups
    US2698845A|1955-01-04|Reaction products of lactams and cer-
    US5750629A|1998-05-12|Uretdione diisocyanates and a process for their production
    US2954365A|1960-09-27|Process for the production of isocyanate polymerization products
    同族专利:
    公开号 | 公开日
    DK134286A|1986-09-26|
    FI861248A|1986-09-26|
    PL145029B1|1988-07-30|
    FR2579205B1|1987-05-15|
    NO861114L|1986-09-26|
    JPS61227574A|1986-10-09|
    JPH0324471B2|1991-04-03|
    AT39249T|1988-12-15|
    EP0197864B1|1988-12-14|
    AR245114A1|1993-12-30|
    NO161265C|1989-07-26|
    US4697014A|1987-09-29|
    YU44986A|1987-10-31|
    NO161265B|1989-04-17|
    KR910009019B1|1991-10-28|
    FR2579205A1|1986-09-26|
    EP0197864A1|1986-10-15|
    DK134286D0|1986-03-24|
    DD246763A5|1987-06-17|
    KR860007270A|1986-10-10|
    KR900005283A|1990-04-13|
    ES8802432A1|1988-06-01|
    KR910009819B1|1991-11-30|
    ES553303A0|1988-06-01|
    HUT41055A|1987-03-30|
    BR8601229A|1986-11-25|
    FI861248A0|1986-03-24|
    DE3661416D1|1989-01-19|
    引用文献:
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    FR2522667B1|1982-03-04|1984-05-11|Rhone Poulenc Spec Chim|DE19526920A1|1995-07-24|1997-01-30|Bayer Ag|Process for the preparation of polyisocyanates containing isocyanurate groups from aliphatic and aromatic isocyanate compounds|
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    FR2818974B1|2000-12-29|2003-10-24|Rhodia Chimie Sa| CONDENSATION OF ISOCYANATE COMPOUNDS|
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    EP3401344B1|2017-05-09|2020-04-08|Evonik Operations GmbH|Method for the preparation of trimers and/or oligomers of diisocyanates|
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    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    FR8504608A|FR2579205B1|1985-03-25|1985-03-25|PROCESS FOR THE PREPARATION OF POLYISOCYANATES POLYISOCYANURATES BY CATALYTIC CYCLOTRIMERIZATION OF POLYISOCYANATES|
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