公开(公告)号：US3796661A

公开(公告)日：1974-03-12

申请号：US3796661D

申请日：1971-07-19

Applicant: TEXACO INC

Inventor： SURATWALA J ,  MAY J ,  ALLEN B

IPC: C07D339/04 ,  C07G99/00 ,  C10M135/04 ,  C10M169/00 ,  C10M1/38

CPC classification number: C10M135/04 ,  C07C325/02 ,  C07D339/04 ,  C07G17/004 ,  C10M2207/121 ,  C10M2207/122 ,  C10M2207/125 ,  C10M2207/129 ,  C10M2209/084 ,  C10M2215/04 ,  C10M2215/086 ,  C10M2215/26 ,  C10M2215/28 ,  C10M2217/024 ,  C10M2217/044 ,  C10M2217/045 ,  C10M2217/046 ,  C10M2217/06 ,  C10M2219/022 ,  C10M2219/082 ,  C10M2219/10 ,  C10M2219/102 ,  C10M2219/104 ,  C10M2219/106 ,  C10M2221/041 ,  C10M2223/04 ,  C10M2223/042 ,  C10M2229/02 ,  C10M2229/05 ,  C10N2240/02 ,  C10N2240/04 ,  C10N2240/042 ,  C10N2240/044 ,  C10N2240/046 ,  C10N2240/401

Abstract: SULFURIZED TRIISOBUTYLENE, LUBRICATING OIL COMPOSITIONS THEREOF HAVING IMPROVED EXTREME PRESSURE PROPERTIES AND REDUCED COPPER CORROSIVITY, AND METHOD OF MANUFACTURE OF SAID SULFURIZED TRIISOBUTYLENE COMPRISING THE SEQUENTIAL STEPS: (1) FORMING A MIXTURE OF TRIISOBUTYLENE AND SULFUR UTILIZING A MOLE RATIO OF TRIISOBUTYLENE TO SULFUR OF BETWEEN ABOUT 1:2.5 AND 1:5 AT BETWEEN ABOUT 50 AND 100* 100*F., (2) CONTINUOUSLY BLOWING THE RESULTANT MIXTURE WITH AN INERT GAS AT A RATE OF BETWEEN ABOUT 0.1 AND 1 S.C.F.G./GALLON MIXTURE AT A TEMPERATURE BETWEEN ABOUT 375 AND 465*F. UNDER A CONTINUOUS PRESSURE OF BETWEEN ABOUT 20 AND 100 P.S.I.G. UNTIL THE FREE SULFUR CONTENT IN SAID RESULTANT REACTION MIXTURE IS LESS THAN 0.3 WT. PERCENT; (3) STRIPPING THE BLOWN MIXTURE WITH INERT GAS AT A RATE OF BETWEEN ABOUT 0.1 AND 1 S.C.F.G./GALLON AT A TEMPERATURE OF BETWEEN ABOUT 320 AND 360*F. AT SUBATMOSPHERIC PRESSURE; AND (4) FILTERING THE STRIPPED PRODUCT.

公开(公告)号：US3816297A

公开(公告)日：1974-06-11

申请号：US73964668

申请日：1968-06-25

Applicant: TEXACO INC

Inventor： LIDEN T ,  MAY J

IPC: B01J29/12 ,  B01J29/16 ,  C10G47/18 ,  C10G13/02

CPC classification number: B01J29/126 ,  B01J29/166 ,  C10G47/18

Abstract: A hydrocracking process for the conversion of heavy hydrocarbon oils using a catalyst containing a hydrogenating component and a cracking component which latter is composed of a modified crystalline zeolite and at least one amorphous inorganic oxide. The process is particularly adapted to hydrocrack charge stocks which are traditionally difficult to hydrocrack such as those having a high nitrogen content, a high polycyclic aromatic content or a Conradson Carbon Residue of at least 1 percent.

公开(公告)号：US3733473A

公开(公告)日：1973-05-15

申请号：US3733473D

申请日：1971-08-05

Applicant: TEXACO INC

Inventor： CHILD E ,  MAY J ,  STEPANEK W

IPC: B01J19/00 ,  C07C1/00 ,  C07C2/62 ,  C07C9/16 ,  C07C67/00 ,  G01N33/00 ,  G01N33/22 ,  G05B13/00 ,  G05B13/02 ,  C07C3/14

CPC classification number: C07C2/62 ,  B01J19/0006 ,  Y10T436/12

Abstract: The strength of acid in an alkylation unit is controlled by a system using a signal corresponding to the anticipated demand on the acid by the reaction of olefin and isoparaffin in the presence of the acid. The reaction weakens the acid so that it is necessary to replace some of the weakened acid with fresh acid to maintain a desired acid strength. The control system includes apparatus sampling the olefin and isoparaffin entering the alkylation unit which provides a signal corresponding to the percent volume of acid degrading constituents formed during alkylation. A water analyzer samples the olefin and isoparaffin and provides a signal corresponding to their water content. Signals corresponding to sensed flow rates of fresh and discharged acid entering and leaving, respectively, the alkylation unit and of the olefin and isoparaffin are provided by sensors. A control circuit using analog computers develop the control signal in accordance with the signals from the sensors, the volume signal and the signal from the analyzer and equations hereinafter disclosed. The control signal is applied to a flow recorder controller which controls the flow rate of the fresh acid entering the alkylation unit so as to maintain the desired acid strength.

Abstract translation: 烷基化单元中的酸的强度由在酸存在下通过烯烃和异链烷烃的反应使用对应于酸的预期需求的信号的系统来控制。 反应会使酸变弱，因此需要用新鲜的酸代替一些弱酸，以保持所需的酸强度。 控制系统包括对进入烷基化单元的烯烃和异构烷烃进行采样，其提供对应于在烷基化期间形成的酸降解成分的百分比体积的信号。 水分析仪对烯烃和异链烷烃进行采样，并提供对应于其含水量的信号。 分别由烷基化单元和烯烃和异链烷烃分别进入和离开的新鲜和排出的酸的感测流量的信号由传感器提供。 使用模拟计算机的控制电路根据来自传感器的信号，体积信号和来自分析仪的信号和下面公开的方程式来开发控制信号。 控制信号被施加到流量记录器控制器，其控制进入烷基化单元的新鲜酸的流量，以保持所需的酸强度。