Polymerization apparatus
    1.
    发明授权
    Polymerization apparatus 失效
    聚合装置

    公开(公告)号:US3704100A

    公开(公告)日:1972-11-28

    申请号:US3704100D

    申请日:1970-07-06

    Applicant: ALLIED CHEM

    CPC classification number: C08G69/04 C08G69/16

    Abstract: APPARATUS FOR POLYMERIZATION OF E-CAPROLACTAM TO PRODUCE A POLYCAPROAMIDE POLYMER MORE RAPIDLY AND WITH THE EXTENT OF POLYMERIZATION FAR GREATER THAN HERETOFORE BY UTILIZING A VACUUM DEMOISTURIZING COLUMN WITHIN THE POLYMERIZATION TRAIN THAT UPON EXTRUSION OF SAID POLYMER THE VOLATILES ARE SUBSTANTIALLY ALL REMOVED BY AN ENTRAIN-

    MENT SEPARATOR MEANS WHEREBY AN IMPROVED POLYCAPROAMIDE POLYMER IS OBTAINED.

    Process for the preparation of linear condensation polyesters
    4.
    发明授权
    Process for the preparation of linear condensation polyesters 失效
    制备线性聚合聚酯的方法

    公开(公告)号:US3689461A

    公开(公告)日:1972-09-05

    申请号:US3689461D

    申请日:1969-09-18

    Applicant: ALLIED CHEM

    CPC classification number: C08G63/78 C08G63/785

    Abstract: A HIGH MOLEUCULAR WEIGHT LINEAR CONDENSATION POLYESTER IS PREPARED FROM A POLYCARBOXYLIC ACID AND A POLYOL BY (A) ESTERIFYING SAID POLYCARBOXYLIC ACID WITH SAID POLYOL BY SUBJECTING TO CONDITIONS OF DIRECT ESTERIFICATION A FLOWABLE, UNIFORM DISPERSION COMPRISED OF (1) A PASTE OF THE SAID POLYCARBOXYLIC ACID AND THE SAID POLYOL, AND (2) AT LEAST 3 PARTS BY WEIGHT PER PART PASTE OF A PARTIALLY ESTERIFIED PRODUCT OF SAID POLYCARBOXYLIC ACID WITH SAID POLYOL, AND THENCE (B) FURTHER ESTERIFYING AND POLYCONDENSING THE ESTERIFICATION PRODUCT OF STEP (A) UNTIL THERE IS OBTAINED AN IMPROVED POLYESTER OF THE DESIRED MOLECULAR WEIGHT.

    Epsilon-caprolactam continuous polymerization process
    5.
    发明授权
    Epsilon-caprolactam continuous polymerization process 失效
    EPSILON-CAPROLACTAM连续聚合方法

    公开(公告)号:US3579483A

    公开(公告)日:1971-05-18

    申请号:US3579483D

    申请日:1969-04-15

    Applicant: ALLIED CHEM

    CPC classification number: C08G69/16 C08G69/04

    Abstract: APPARATUS AND PROCESS FOR CONTINUOUS POLYMERIZATION OF POLYAMIDEDS TO PRODUCE A POLYMER WHEREIN THE REQUIRED VISCOSITY CAN BE OBTAINED MUCH MORE RAPIDLY AND THE EXTENT OF POLYMERIZATION FAR GREATER THAN HERETOFORE POSSIBLE BY USE OF A VACUUM DEMOISTURIZING COLUMN WITHIN THE POLYMERIZATION TRAIN WHEREIN THE PRE-POLYMER IS CONVERTED TO POLYAMIDE OF HIGHER MOLECULAR WEIGHT IN A SHORT PERIOD OF TIME BY EXPOSING AT LEAST ABOUT 0.2 SQUARE FOOT OF PRE-POLYMER PER POUND THEREOF TO A TEMPERATURE OF BETWEEN ABOUT 230*C. AND ABOUT 300*C. AT PRESSURES OF LESS THAN ABOUT 500 MM. HG. THE APPARATUS AND PROCESS YIELDS EVEN GREATER EFFICIENCIES WHEN USED IN CONJUNCTION WITH POLYAMIDATION CATALYSTS.

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