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    • 2. 发明专利
    • FI951380A0
    • 1995-03-23
    • FI951380
    • 1995-03-23
    • CHEVRON CHEM CO
    • HOPE KENNETH DCUPPLES BARRETT LHO TING C
    • B01J31/02C07B61/00C07C2/20C07C2/26C07C11/02C10G50/00C10M107/10C07C
    • A process for making an oligomer comprises contacting an olefinic monomer with boron trifluoride and a cpd. selected from hydroxyalkyl ketone and hydroxyalkyl aldehyde. The process is carried out at 0-200[deg]C and a pressure of from atmospheric up to 1000 psig. The olefinic monomer is a straight-chain, alpha-olefinic monomer contg. 6-20C, pref. 6-12C, more pref. 8-10C. The promoter cpd. is a hydroxyalkyl ketone, pref. contg. 1-6C, where the ketone gp. is pref. methyl ketone or ethyl ketone; suitable cpds. are hydroxy acetone, 1-hydroxy-2-butanone, 3-hydroxy-2-butanone, 3-hydroxy-3-methyl-2-butanone and 4-hydroxy-4-methyl-2-pentanone. More pref., the hydroxyl gp. is attached to a tert. carbon, and the most preferred ketone is 4-hydroxy-4-methyl-2-pentanone. The oligomer prod. has a kinematic viscosity at 100[deg]C of less than 3.6 cSt, pref. less than 2.0 cSt, more pref. less than 1.7 cSt. The ratio of dimer to the sum of trimer and higher oligomer is at least 0.5:1, pref. at least 1:1 and the prod. contains at least 70 wt.%, pref. at least 80 wt.%, more pref. at least 90 wt.% dimer and trimer before removal of unreacted monomer. A second promoter can be used in conjunction with the BF3 and the hydroxy carbonyl promoter. The second promoter is an aldehyde, alcohol, alcohol alkoxylate, carboxylic acid, ether, ketone or mixt. of these, pref. an alcohol such as methanol.
    • 3. 发明专利
    • DE69506935T2
    • 1999-05-27
    • DE69506935
    • 1995-03-14
    • CHEVRON CHEM CO
    • HOPE KENNETH DCUPPLES BARRETT LHO TING C
    • B01J31/02C07B61/00C07C2/20C07C2/26C07C11/02C10G50/00C10M107/10C07C2/08
    • A process for making an oligomer comprises contacting an olefinic monomer with boron trifluoride and a cpd. selected from hydroxyalkyl ketone and hydroxyalkyl aldehyde. The process is carried out at 0-200[deg]C and a pressure of from atmospheric up to 1000 psig. The olefinic monomer is a straight-chain, alpha-olefinic monomer contg. 6-20C, pref. 6-12C, more pref. 8-10C. The promoter cpd. is a hydroxyalkyl ketone, pref. contg. 1-6C, where the ketone gp. is pref. methyl ketone or ethyl ketone; suitable cpds. are hydroxy acetone, 1-hydroxy-2-butanone, 3-hydroxy-2-butanone, 3-hydroxy-3-methyl-2-butanone and 4-hydroxy-4-methyl-2-pentanone. More pref., the hydroxyl gp. is attached to a tert. carbon, and the most preferred ketone is 4-hydroxy-4-methyl-2-pentanone. The oligomer prod. has a kinematic viscosity at 100[deg]C of less than 3.6 cSt, pref. less than 2.0 cSt, more pref. less than 1.7 cSt. The ratio of dimer to the sum of trimer and higher oligomer is at least 0.5:1, pref. at least 1:1 and the prod. contains at least 70 wt.%, pref. at least 80 wt.%, more pref. at least 90 wt.% dimer and trimer before removal of unreacted monomer. A second promoter can be used in conjunction with the BF3 and the hydroxy carbonyl promoter. The second promoter is an aldehyde, alcohol, alcohol alkoxylate, carboxylic acid, ether, ketone or mixt. of these, pref. an alcohol such as methanol.
    • 5. 发明专利
    • FI120624B
    • 2009-12-31
    • FI951380
    • 1995-03-23
    • CHEVRON CHEM CO
    • HOPE KENNETH DCUPPLES BARRETT LHO TING C
    • B01J31/02C07C2/26C07B61/00C07C2/20C07C11/02C10G50/00C10M107/10
    • A process for making an oligomer comprises contacting an olefinic monomer with boron trifluoride and a cpd. selected from hydroxyalkyl ketone and hydroxyalkyl aldehyde. The process is carried out at 0-200[deg]C and a pressure of from atmospheric up to 1000 psig. The olefinic monomer is a straight-chain, alpha-olefinic monomer contg. 6-20C, pref. 6-12C, more pref. 8-10C. The promoter cpd. is a hydroxyalkyl ketone, pref. contg. 1-6C, where the ketone gp. is pref. methyl ketone or ethyl ketone; suitable cpds. are hydroxy acetone, 1-hydroxy-2-butanone, 3-hydroxy-2-butanone, 3-hydroxy-3-methyl-2-butanone and 4-hydroxy-4-methyl-2-pentanone. More pref., the hydroxyl gp. is attached to a tert. carbon, and the most preferred ketone is 4-hydroxy-4-methyl-2-pentanone. The oligomer prod. has a kinematic viscosity at 100[deg]C of less than 3.6 cSt, pref. less than 2.0 cSt, more pref. less than 1.7 cSt. The ratio of dimer to the sum of trimer and higher oligomer is at least 0.5:1, pref. at least 1:1 and the prod. contains at least 70 wt.%, pref. at least 80 wt.%, more pref. at least 90 wt.% dimer and trimer before removal of unreacted monomer. A second promoter can be used in conjunction with the BF3 and the hydroxy carbonyl promoter. The second promoter is an aldehyde, alcohol, alcohol alkoxylate, carboxylic acid, ether, ketone or mixt. of these, pref. an alcohol such as methanol.
    • 7. 发明专利
    • FI951380A
    • 1995-09-25
    • FI951380
    • 1995-03-23
    • CHEVRON CHEM CO
    • HOPE KENNETH DCUPPLES BARRETT LHO TING C
    • B01J31/02C07B61/00C07C2/20C07C2/26C07C11/02C10G50/00C10M107/10C07C
    • A process for making an oligomer comprises contacting an olefinic monomer with boron trifluoride and a cpd. selected from hydroxyalkyl ketone and hydroxyalkyl aldehyde. The process is carried out at 0-200[deg]C and a pressure of from atmospheric up to 1000 psig. The olefinic monomer is a straight-chain, alpha-olefinic monomer contg. 6-20C, pref. 6-12C, more pref. 8-10C. The promoter cpd. is a hydroxyalkyl ketone, pref. contg. 1-6C, where the ketone gp. is pref. methyl ketone or ethyl ketone; suitable cpds. are hydroxy acetone, 1-hydroxy-2-butanone, 3-hydroxy-2-butanone, 3-hydroxy-3-methyl-2-butanone and 4-hydroxy-4-methyl-2-pentanone. More pref., the hydroxyl gp. is attached to a tert. carbon, and the most preferred ketone is 4-hydroxy-4-methyl-2-pentanone. The oligomer prod. has a kinematic viscosity at 100[deg]C of less than 3.6 cSt, pref. less than 2.0 cSt, more pref. less than 1.7 cSt. The ratio of dimer to the sum of trimer and higher oligomer is at least 0.5:1, pref. at least 1:1 and the prod. contains at least 70 wt.%, pref. at least 80 wt.%, more pref. at least 90 wt.% dimer and trimer before removal of unreacted monomer. A second promoter can be used in conjunction with the BF3 and the hydroxy carbonyl promoter. The second promoter is an aldehyde, alcohol, alcohol alkoxylate, carboxylic acid, ether, ketone or mixt. of these, pref. an alcohol such as methanol.
    • 8. 发明专利
    • DE69506935D1
    • 1999-02-11
    • DE69506935
    • 1995-03-14
    • CHEVRON CHEM CO
    • HOPE KENNETH DCUPPLES BARRETT LHO TING C
    • B01J31/02C07B61/00C07C2/20C07C2/26C07C11/02C10G50/00C10M107/10C07C2/08
    • A process for making an oligomer comprises contacting an olefinic monomer with boron trifluoride and a cpd. selected from hydroxyalkyl ketone and hydroxyalkyl aldehyde. The process is carried out at 0-200[deg]C and a pressure of from atmospheric up to 1000 psig. The olefinic monomer is a straight-chain, alpha-olefinic monomer contg. 6-20C, pref. 6-12C, more pref. 8-10C. The promoter cpd. is a hydroxyalkyl ketone, pref. contg. 1-6C, where the ketone gp. is pref. methyl ketone or ethyl ketone; suitable cpds. are hydroxy acetone, 1-hydroxy-2-butanone, 3-hydroxy-2-butanone, 3-hydroxy-3-methyl-2-butanone and 4-hydroxy-4-methyl-2-pentanone. More pref., the hydroxyl gp. is attached to a tert. carbon, and the most preferred ketone is 4-hydroxy-4-methyl-2-pentanone. The oligomer prod. has a kinematic viscosity at 100[deg]C of less than 3.6 cSt, pref. less than 2.0 cSt, more pref. less than 1.7 cSt. The ratio of dimer to the sum of trimer and higher oligomer is at least 0.5:1, pref. at least 1:1 and the prod. contains at least 70 wt.%, pref. at least 80 wt.%, more pref. at least 90 wt.% dimer and trimer before removal of unreacted monomer. A second promoter can be used in conjunction with the BF3 and the hydroxy carbonyl promoter. The second promoter is an aldehyde, alcohol, alcohol alkoxylate, carboxylic acid, ether, ketone or mixt. of these, pref. an alcohol such as methanol.