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公开(公告)号:JP2731426B2
公开(公告)日:1998-03-25
申请号:JP21840789
申请日:1989-08-24
Applicant: SHELL INT RESEARCH
Inventor: CHADWICK JOHN CLEMENT , VILLENA ALAN , GAALEN RONALD PETRUS C VAN
IPC: C08F4/658 , C08F4/60 , C08F4/654 , C08F4/6592 , C08F10/00
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42.
公开(公告)号:JPH1036421A
公开(公告)日:1998-02-10
申请号:JP9239497
申请日:1997-04-10
Applicant: SHELL INT RESEARCH
Inventor: DE BOER ERIC JOHANNES MARIA , HESSEN BART , VAN DER HUIZEN ADRIAAN ALBERT , DE JONG WOUTER , VAN DER LINDEN ADRIANUS JOHANN , RUISCH BART JOHAN , SCHOON LODEWIJK , DE SMET HELEEN JOHANNA AUGUSTA , VAN DER STEEN FREDERIK HENDRIK , VAN STRIEN HUBERTUS CORNELIS T , VILLENA ALAN , WALHOF JUDITH JOHANNA BERENDIN
Abstract: PROBLEM TO BE SOLVED: To provide a catalyst which is more effective than a known catalysts, is stable, is active even when used in sufficiently low concentrations and is suitable for use in the hydrogenation of a polymer having ethylenic unsaturations by using a plurality of specified compounds. SOLUTION: This composition comprises a titanium compound represented by formula I, an alkali metal hydride which is initially added or produced in situ from an alkali-metal-terminated living polymer and/or an added alkyl alkali metal and hydrogen in the polymer solution, the molar ratio of the alkali metal to the titanium being at least 2:1, and a boron compound represented by formula II (wherein A1 and A2 are each cyclopentadienyl or indenyl; X1 and X2 are each H, a halogen, a lower alkyl, a lower alkoxyl or the like; and R1 , R2 and R3 are each a halogen, a lower alkyl, a lower alkoxyl or the like).
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公开(公告)号:JPH09309937A
公开(公告)日:1997-12-02
申请号:JP2575397
申请日:1997-01-27
Applicant: SHELL INT RESEARCH
Inventor: BERUTOUSU YAN BURIYUUKERU , ERUSU UAN ERUDEEREN , GUREGORII JIYON HITSUCHINGUSU , MARUCHINUSU ENGERUBERUTO MAACH , YOHANNESU GOUERUTO RUTSUTEN
IPC: C08L25/04 , C08F2/12 , C08F2/44 , C08F12/08 , C08F285/00 , C08G18/28 , C08G18/48 , C08G18/63 , C08G71/02 , C08L51/00 , C08L71/02 , C08L75/04
Abstract: Process for the preparation of a stable polymer polyol having a narrow polymer particle size distribution comprising the steps of: (a) preparing a polymer seed dispersion wherein the liquid polyol medium comprises at least 30% by weight of a coupled polyol; (b) admixing a base polyol and one or more ethylenically unsaturated monomers, at least 80% by weight of which is styrene, with at least part of the polymer seed dispersion obtained in step (a) at a temperature below the polymerization temperature; and subsequently (c) heating the resulting mixture to a temperature at which polymerization occurs and allowing the polymerization to proceed until completion, thus yielding the polymer polyol. Polymer polyol comprising a liquid polyol phase and from 10 to 55% by weight based on total weight of polymer polyol of solid polymer particles stably dispersed therein, wherein the polymer particles consist essentially of polystyrene and have a mean particle size in the range of from 0.5 to 2.5 micron with a particle size span of at most 1.3. The above polymer polyols are very useful in the production of polyurethane articles, particularly polyurethane foams.
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公开(公告)号:JPH09241375A
公开(公告)日:1997-09-16
申请号:JP5712997
申请日:1997-02-26
Applicant: SHELL INT RESEARCH
Inventor: YOANNESU ADORIANUSU MARIA UAN
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公开(公告)号:JP2631534B2
公开(公告)日:1997-07-16
申请号:JP25962488
申请日:1988-10-17
Applicant: SHELL INT RESEARCH
Inventor: LI SIMON MING-KUNG
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公开(公告)号:JPH09176302A
公开(公告)日:1997-07-08
申请号:JP33913596
申请日:1996-12-05
Applicant: SHELL INT RESEARCH
Inventor: BROENNUM THOMAS , SANGHA PARMINDER SINGH , STEINMETZ JOHANNES CORNELIS
IPC: C08G65/02 , C08G18/28 , C08G18/32 , C08G18/48 , C08G65/26 , C08G101/00 , C08J9/02 , C08L71/02 , C08L75/04
Abstract: Polyether polyol having an aromaticity in the range of from 2% to 35%, an average nominal functionality (Fn) in the range of from 2.0 to 4.5 and a hydroxyl value in the range of from 390 to 650 mg KOH/g, whereby the aromatic carbon atoms are contained in structural moieties of the general formula wherein both R1 groups independently represent hydrogen or a C1-C3 alkyl group; both R2 groups independently represent a C1-C3 alkyl group; and n is an integer of from 0 to 3. Process for the preparation of the above polyether polyol, which process comprises reacting an alkylene oxide with a polyhydric alcohol blend comprising a diphenylol alkane precursor of the above indicated structural moiety and at least one aliphatic or alicyclic polyhydric alcohol having a functionality of at least 2.0. Polyether polyol blend having an aromaticity in the range of from 2 to 10% and a Fn in the range of from 2.5 to 5.0 eq/mole, which blend comprises the above polyether polyol and one or more aliphatic or alicyclic polyether polyols having a Fn of at least 2.5. Rigid polyurethane foam having a total aromaticity in the range of from 35% to 50%, obtainable by foaming a composition comprising the above polyol or polyol blend having an aromaticity from 2 to 10% and a Fn from 2.5 to 5.0 eq/mole, and an aromatic polyisocyanate in such amount that the isocyanate index is from 100 to 150, whereby the polyol reactant accounts for from 1 and 10% of the total aromaticity of the rigid polyurethane foam.
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公开(公告)号:JPH08323186A
公开(公告)日:1996-12-10
申请号:JP12564095
申请日:1995-04-27
Applicant: SHELL INT RESEARCH
Abstract: PURPOSE: To provide a vessel easy for operation and replace of catalyst and suitable for hydrotreatment of hydrocarbon oils by setting a bed of solid material upon a support layer fixed horizontally in the vessel and closing the support layer by a breakplate during normal operation. CONSTITUTION: A reactor comprises an inlet 2 and an outlet 9, a layer 3 distributing an inflow liquid into a catalyst bed 8, and a pipe 4 supported by the layer 3, and a new catalyst is filled through this pipe 4. Further, the reactor 1 comprises a support layer 7 having an opening 5 closed by a breakplate 6 during operation. During the operation, the catalyst bed 8 is located upon the support layer 7 and this support layer 7 distributes gases and liquids. The reactor 1 is used in the hydrotreatment, and the like, of hydrocarbons, in which, during normal operation, the opening 5 in the support layer 7 is closed completely by the breakplate 6.
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