公开(公告)号：US4033857A

公开(公告)日：1977-07-05

申请号：US643050

申请日：1975-12-22

Applicant: Dale Williams ,  James H. Colvert ,  Frederick C. Jahnke

Inventor： Dale Williams ,  James H. Colvert ,  Frederick C. Jahnke

IPC: C10G7/00 ,  C10G37/00

CPC classification number: C10G7/00

Abstract: The present application discloses a fluidized catalytic cracking process wherein light cycle gas oil is stripped of heavy naphtha components employing reboiled light cycle gas oil as stripping vapor. Heavy naphtha vapors stripped from the light cycle gas oil are returned to the reaction vapor as primary stripping vapor. This process results in increased naphtha octanes, and reduced sour water production from a fluidized catalytic cracking unit.

Abstract translation: 本申请公开了一种流化催化裂化方法，其中轻循环瓦斯油用重沸石循环瓦斯油作为汽提蒸汽汽提重质石脑油成分。 从轻质循环瓦斯油中汽提的重质石脑油蒸气作为一次汽提蒸汽返回到反应蒸气。 该方法导致石脑油辛烷值增加，并且从流化催化裂化装置减少酸水产生。

公开(公告)号：US4003822A

公开(公告)日：1977-01-18

申请号：US652276

申请日：1976-01-26

Applicant: Hong-Kyu Jo

Inventor： Hong-Kyu Jo

IPC: C10G11/18 ,  C10G37/00

CPC classification number: C10G11/18

Abstract: Separation of the catalyst-containing product effluent from a fluid catalytic cracking unit is effected in the main column by a technique which involves removing a light naphtha fraction as the single overhead stream and separately withdrawing a heavy naphtha fraction as a lower side-cut. The latter is stripped of light naphtha (for recycle to the main column) and recovered as a product stream. Preferably a portion of the heavy naphtha fraction (as withdrawn) is cooled and combined with the light naphtha overhead reflux stream.

Abstract translation: 含有催化剂的产物流出物与流化催化裂化装置的分离是通过一种技术来实现的，该技术包括除去作为单一塔顶馏出物流的轻质石脑油馏分，并单独地将重质石脑油馏分作为下馏分馏出。 后者被汽提轻石脑油（用于再循环到主塔）并作为产物流回收。 优选地，将一部分重质石脑油馏分（取出的）冷却并与轻石脑油塔顶回流物流组合。

公开(公告)号：US3844932A

公开(公告)日：1974-10-29

申请号：US25498272

申请日：1972-05-19

Applicant: GOMI S ,  UEMOTO K ,  OKAGAMI A ,  ISHIGURO T ,  TAKAHASHI M ,  KURIBAYASHI H

Inventor： UEMOTO K ,  KURIBAYASHI H ,  GOMI S ,  TAKAHASHI M ,  ISHIGURO T ,  OKAGAMI A

IPC: C10G45/36 ,  C10G65/08 ,  C10G69/12 ,  C10G37/00

CPC classification number: C10G69/123 ,  C10G45/36 ,  C10G65/08

Abstract: A process for obtaining improved hydrocarbon oil products by treating by-product heavy fractions, formed in the production of olefins and having initial boiling point of above 160*C and a 75 percent distill-off point of below 450*C, with hydrogen at a temperature of from 40* to 200*C and a pressure of from 5 to 300 kg/cm2 G using a nickel-containing catalyst which has been pretreated with organic sulfur compounds, to thereby impart thermal stability to the oil, then subjecting the resulting oil to a hydrorefining followed by hydrogenation is disclosed.

Abstract translation: 一种通过处理在烯烃生产中形成的初始沸点高于160℃和75％馏出点低于450℃的副产物重馏分获得改进的烃油产物的方法，在 温度为40〜200℃，压力为5〜300kg / cm2，使用已经用有机硫化合物预处理的含镍催化剂，从而赋予油热稳定性， 公开了产生加氢精制氢化的油。

公开(公告)号：US3806445A

公开(公告)日：1974-04-23

申请号：US28520872

申请日：1972-08-31

Applicant: EXXON RESEARCH ENGINEERING CO

Inventor： HENRY H ,  GILBERT J

IPC: C10G67/04 ,  C10G13/00 ,  C10G37/00

CPC classification number: C10G67/0445 ,  C10G2400/10

Abstract: HIGH QUALITY UV STABLE LUBRICATING OIL STOCKS ARE PREPARED BY SOLVENT EXTRACTING A HYDROCARBON FEEDSTOCK WITH A SOLVENT HAVING PREFERENTIAL SOLUBILITY FOR AROMATICS, THEREBY REDUCING THE AROMATIC CONTENT THEREOF AND RECOVERING A RAFFINATE PHASE THEREFROM. THE RAFFINATE IS STRIPPED OF SOLVENT AND SUBSEQUENTLY HYDROCRACKED MILD CONDITIONS TO INCREASE THE VISCOSITY INDEX OF THE RAFFINATE. THE HYDROCRACKATE PRODUCT IS THEN SOLVENT EXTRACTED WITH A SOLVENT HAVING PREFERENTIAL SOLUBILITY FOR AROMATICS, WHICH SOLVENT MAY BE THE SAME OR DIFFERENT THAN THE SOLVENT USED IN THE FIRST EXTRACTION, THEREBY FORMING A SECOND EXTRACT

PHASE AND A SECOND RAFFINATE PHASE. THE EXTACT AND RAFFINATE PHAESE ARE SEPARATED AND THE EXTRACT PHASE STRIPPED OF SOLVENT AND RECYCLED TO THE HYDROCRACKER .

公开(公告)号：US3781197A

公开(公告)日：1973-12-25

申请号：US3781197D

申请日：1972-01-10

Applicant: GULF RESEARCH DEVELOPMENT CO

Inventor： BRYSON M ,  MCKINNEY J ,  TITMUS R ,  WHITE F

IPC: C10G11/04 ,  C10G11/18 ,  C10G37/00 ,  C10L1/04

CPC classification number: C10G11/04 ,  C10G11/18

Abstract: In fluid catalytic riser cracking of a gas oil with a zeolite catalyst the inclusion of controlled amounts of residual oil in the feed results in an improvement in octane value and/or improvement in the distribution of octane value of the gasoline product. The octane number improvement is further enhanced by hydrodesulfurizing the residual oil prior to charging to the FCC unit. However, residual oil is relatively difficult to vaporize and the extent of its vaporization will depend on the equilibrium flash vaporization temperature at the bottom or inlet of the riser. Therefore, the quantity of residual oil in the feed must be controlled in relation to the equilibrium temperature in order to, on the one hand, vaporize and crack a sufficient quantity of residual oil to obtain the octane improvement effect, while, on the other hand, keeping the quantity of residual oil which remains unvaporized below a specified level.

公开(公告)号：US3764519A

公开(公告)日：1973-10-09

申请号：US3764519D

申请日：1972-12-11

Applicant: CHEVRON RES

Inventor： MEYER J

IPC: B01J29/16 ,  C10G47/20 ,  C10G13/02 ,  C01B33/28 ,  C10G37/00

CPC classification number: B01J29/16 ,  C10G47/20

Abstract: A hydrocarbon hydroconversion process comprising contacting a hydrocarbon feedstock and hydrogen with a catalyst comprising an alumina-silica-magnesia matrix containing a hydrogenation component, and a crystalline zeolitic molecular sieve substantially free of hydrogenation components, said catalyst having a specific gravity less than about 1.8, preferably 1.1 to 1.8, in a reaction zone at hydrocarbon hydroconversion conditions; also, said catalyst.

Abstract translation: 一种烃加氢转化方法，包括使烃原料和氢与包含含有氢化组分的氧化铝 - 二氧化硅 - 氧化镁基质和基本上不含氢化组分的结晶沸石分子筛的催化剂接触，所述催化剂的比重小于约1.8， 优选1.1至1.8，在烃加氢转化条件下在反应区中; 也称催化剂。

公开(公告)号：US3758401A

公开(公告)日：1973-09-11

申请号：US3758401D

申请日：1971-05-21

Applicant: PHILLIPS PETROLEUM CO

Inventor： BRIDGEFORD R ,  CAWI V

IPC: C10G61/06 ,  C10G63/00 ,  C10L1/06 ,  C10G37/04 ,  C10G37/00

CPC classification number: C10G61/06 ,  C10G63/00 ,  C10L1/06

Abstract: COMPOSITE MOTOR FUELS OR GASOLINE, SUITABLE FOR USE AS A LEAD-FREE OR LOW-LEAD-CONTENT FUEL, ARE PROVIDED BY VARIOUS COMBINATIONS OF STEPS COMPRISING, IN DIFFERENT EMBODIMENTS, VARIOUS NOVEL COMBINATIONS OF STEPS COMPRISING CATALYTIC CRACKING, CATALYTIC REFORMING, AND SOLVENT EXTRACTION. IN SOME EMBODIMENTS, THE COMBINATION(S) INCLUDE ONE OR MORE ADDITIONAL STEPS SUCH AS HYDROCRACKING, ALKYLATION, AND DISPROPORTIONATION.

公开(公告)号：US3698552A

公开(公告)日：1972-10-17

申请号：US3698552D

申请日：1970-12-21

Applicant: WITTMANN PAUL

Inventor： WITTMANN PAUL

IPC: B07B13/075 ,  C10G37/00

CPC classification number: B07B1/4636 ,  B07B13/075

Abstract: A sorting machine having a plurality of parallel rollers, all being supported by chain means, which form them into an endless belt and each supporting a plurality of spaced, double-conical sectional discs; guide rails for the discs for adjusting the positions of the discs along their rollers; slotted guide plate means connected with the rails for readjusting the positions of the rails, thereby to readjust the positions of the sectional discs. A plurality of sorting machines may be arranged in a row, each with means for providing a transition to the succeeding machine.

Abstract translation: 一种具有多个平行辊的分选机，全部由链条装置支撑，将其形成环形带，并分别支撑多个间隔开的双锥形分段盘; 用于盘的导轨，用于调节盘沿其辊的位置; 与轨道连接的开槽导板装置，用于重新调整轨道的位置，从而重新调整分段盘的位置。 多个分选机可以排列成一排，每个具有用于向后续机器提供过渡的装置。

公开(公告)号：US3686093A

公开(公告)日：1972-08-22

申请号：US3686093D

申请日：1971-02-25

Applicant: ROBERT LEARD IRVINE

Inventor： IRVINE ROBERT LEARD

IPC: C10G45/16 ,  C10G45/18 ,  C10G47/26 ,  C10G47/28 ,  C10G65/12 ,  C10G23/00 ,  C10G37/00

CPC classification number: C10G45/16 ,  C10G2300/107

Abstract: THE INVENTION RELATES TO A HYDROCRACKING ARRANGMENT. CRUDE OR RESIDUA FEEDBSTOCK IS IN A FIRST STAGE TREATED TO HYDROGENATE ITS NON-HYDROCARBON CONTENT USING A FLUIDISED CATALYST DESCENDING IN A MULTI-BED REACTOR IN COUNTERCURRENT TO FEED AND HYDROGEN. THE EFFLUENT FROMTHE FIRST REACTOR PASSES TO DISCARD HYDROCRACKER ALSO WITH DESCENDING FLUIDISED CATALYST AND ASCENDING FEED AND HYDROGEN, THE CATALYST BEING REGENERATED LOW ACTIVITY CATALYST FROM THE SUBSEQUENT MAIN HYDROCRACKING ZONE.

公开(公告)号：US3679574A

公开(公告)日：1972-07-25

申请号：US3679574D

申请日：1971-02-25

Applicant: ROBERT L IRVINE

Inventor： IRVINE ROBERT L

IPC: C10G45/16 ,  C10G45/18 ,  C10G47/26 ,  C10G47/28 ,  C10G65/12 ,  C10G23/00 ,  C10G37/00 ,  C10G37/10

CPC classification number: C10G45/16 ,  C10G2300/107

Abstract: THE INVENTION RELATES TO THE PREPARATION OF LUBE OIL AND WAX FROM LOW VANADIUM CONTENT CRUDE OR RESIDUA FEED. THE FEED IS FIRST TREATED IN A CATALYST DISCARD ZONE HYDROCRACKER USING CATALYST PROVIDED BY REGNERATION OF LOW ACTIVITY CATALYST FROM A SUBSEQUENT MAIN HYDROCRACKING ZONE. THE DISCARD HYDROCRACKER COMPRISING A PLURALITY OF BEDS CONTAINING FLUIDISED CATALYST DESCENDING IN COUNTERCURRENT TO ASCENDING FEED AND HYDROGEN. CATALYST TRANSFER BETWEEN BEDS IS EXTERNAL OF THE REACTOR.