公开(公告)号：WO0218316A3

公开(公告)日：2002-06-20

申请号：PCT/US0126765

申请日：2001-08-27

Applicant: STANDARD OIL CO

Inventor： HEPFER ROBERT P ,  MILLER CRAIG T ,  ATTIG THOMAS G ,  NORENBERG GREGORY A ,  BUDGE JOHN R

IPC: C07D307/33 ,  C07B61/00 ,  C07C29/149 ,  C07C31/20 ,  C07C51/36 ,  C07C55/10

CPC classification number: C07C29/149 ,  C07C31/207

Abstract: In the process for the conversion of maleic acid to gamma-butyrolactone. 1.4-butanediol and/or tetrahydrofuran, a feedstream comprising maleic acid is hydrogenated in a first hydrogenation zone to produce a reaction product comprising succinic acid and unreacted hydrogen which is then supplied to a second hydrogenation zone, where succinic acid is converted to 1,4-butanediol, the temper atures of the feedstream comprising maleic acid and the first hydrogenation zone are controlled such that the temperature of mal eic acid in the feedstream and the first hydrogenation zone does not exceed about 130 DEG C, thereby minimizing the corrosive effects of the maleic acid and prolonging reactor life and improving overall process economics.

Abstract translation: 在马来酸转化为γ-丁内酯的过程中。 在1,4-丁二醇和/或四氢呋喃中，包含马来酸的原料流在第一氢化区中氢化以产生包含琥珀酸和未反应的氢的反应产物，然后将其供应到第二氢化区，其中琥珀酸转化成1,4 - 丁二醇中，控制包含马来酸和第一加氢区的进料流的温度，使得进料流和第一加氢区中的丙二酸的温度不超过约130℃，由此使 马来酸和延长反应器寿命并改善整个过程的经济性。

公开(公告)号：AU8532001A

公开(公告)日：2002-03-13

申请号：AU8532001

申请日：2001-08-27

Applicant: STANDARD OIL CO

Inventor： HEPFER ROBERT P ,  MILLER CRAIG T ,  ATTIG THOMAS G ,  NORENBERG GREGORY A ,  BUDGE JOHN R

IPC: C07D307/33 ,  C07B61/00 ,  C07C29/149 ,  C07C31/20 ,  C07C51/36 ,  C07C55/10

Abstract: In the process for the conversion of maleic acid to gamma-butyrolactone, 1.4-butanediol and/or tetrahydrofuran, a feedstream comprising maleic acid is hydrogenated in a first hydrogenation zone to produce a reaction product comprising succinic acid and unreacted hydrogen which is then supplied to a second hydrogenation zone, where succinic acid is converted to 1,4-butanediol, the temperatures of the feedstream comprising maleic acid and the first hydrogenation zone are controlled such that the temperature of maleic acid in the feedstream and the first hydrogenation zone does not exceed about 130° C., thereby minimizing the corrosive effects of the maleic acid and prolonging reactor life and improving overall process economics.

公开(公告)号：CA2418280C

公开(公告)日：2009-08-25

申请号：CA2418280

申请日：2001-08-27

Applicant: STANDARD OIL CO

Inventor： BUDGE JOHN R ,  HEPFER ROBERT P ,  ATTIG THOMAS G ,  MILLER CRAIG T ,  NORENBERG GREGORY A

IPC: C07C51/36 ,  C07D307/33 ,  C07B61/00 ,  C07C27/04 ,  C07C29/149 ,  C07C31/20 ,  C07D307/08

Abstract: In the process for the conversion of maleic acid to gamma-butyrolactone. 1.4 - butanediol and/or tetrahydrofuran, a feedstream comprising maleic acid is hydrogenated in a first hydrogenation zone to produce a reaction product comprising succinic acid and unreacted hydrogen which is then supplied to a second hydrogenation zone, where succinic acid is converted to 1,4-butanedio l, the temper atures of the feedstream comprising maleic acid and the first hydrogenation zone are controlled such that the temperature of maleic acid i n the feedstream and the first hydrogenation zone does not exceed about 130 ~C , thereby minimizing the corrosive effects of the maleic acid and prolonging reactor life and improving overall process economics.

公开(公告)号：TR200200030T2

公开(公告)日：2002-11-21

申请号：TR200200030

申请日：2000-05-31

Applicant: STANDARD OIL CO

Inventor： TROTT LOUIS R ,  GUSTAFERRO ROBERT A ,  HEPFER ROBERT P ,  MILLER CRAIG T ,  CARLSSON STIG AXEL ,  CLOSE BENJAMIN W

IPC: B01J8/18 ,  B01J8/24 ,  B01J19/00 ,  C07C253/24 ,  C07C255/08

Abstract: A sparger includes a conduit for conducting an oxygen feed, a nozzle connected to the conduit for passage of the oxygen feed from the conduit to the outside of the sparger, the nozzle including an orifice and a shroud, and insulation surrounding the conduit and also the shroud substantially the full length of the shroud. A method is provided for producing acrylonitrile via propane ammoxidation, comprising introducing propane and ammonia feeds into a fluid bed of a fluid bed reactor, and introducing an oxygen feed into the fluid bed through at least one insulated and jacketed sparger nozzle for reacting with at least one of the propane feed and ammonia feed in the presence of a fluid bed catalyst.

公开(公告)号：CA2418280A1

公开(公告)日：2002-03-07

申请号：CA2418280

申请日：2001-08-27

Applicant: STANDARD OIL CO

Inventor： HEPFER ROBERT P ,  MILLER CRAIG T ,  ATTIG THOMAS G ,  NORENBERG GREGORY A ,  BUDGE JOHN R

IPC: C07D307/33 ,  C07B61/00 ,  C07C29/149 ,  C07C31/20 ,  C07C51/36 ,  C07C55/10

Abstract: In the process for the conversion of maleic acid to gamma-butyrolactone. 1.4 - butanediol and/or tetrahydrofuran, a feedstream comprising maleic acid is hydrogenated in a first hydrogenation zone to produce a reaction product comprising succinic acid and unreacted hydrogen which is then supplied to a second hydrogenation zone, where succinic acid is converted to 1,4-butanedio l, the temper atures of the feedstream comprising maleic acid and the first hydrogenation zone are controlled such that the temperature of maleic acid i n the feedstream and the first hydrogenation zone does not exceed about 130 ~C , thereby minimizing the corrosive effects of the maleic acid and prolonging reactor life and improving overall process economics.