公开(公告)号：WO2021099850A1

公开(公告)日：2021-05-27

申请号：PCT/IB2020/055160

申请日：2020-06-01

Applicant: CHEVRON U.S.A. INC.

Inventor： ELOMARI, Saleh Ali ,  LUO, Huping ,  TIMKEN, Hye-Kyung Cho ,  JOHNS, Jeff William

IPC: C10G21/06 ,  C07C7/12 ,  C10G25/12 ,  C10G21/18 ,  C10G67/04 ,  C10G67/06 ,  B01D11/04

Abstract: A process is provided for removing a heavy polynuclear aromatic (HPNA) compound from a hydrocarbon oil. The process includes contacting the hydrocarbon oil containing the HPNA compound with a lean hydrocarbon-immiscible liquid stream to produce a mixture comprising the hydrocarbon oil and a rich hydrocarbon-immiscible liquid containing the HPNA compound; and separating the mixture to produce a hydrocarbon oil effluent having a reduced level of the HPNA compound and a hydrocarbon-immiscible liquid effluent containing the HPNA compound. The hydrocarbon-immiscible liquid can be a halometallate ionic liquid, a liquid coordination complex, or a combination thereof.

公开(公告)号：WO2016190976A1

公开(公告)日：2016-12-01

申请号：PCT/US2016/027430

申请日：2016-04-14

Applicant: CHEVRON U.S.A. INC.

Inventor： TIMKEN, Hye Kyung Cho ,  JOHNS, Jeff William ,  HARRIS, Thomas Van

IPC: B01J19/00 ,  G21C19/32

CPC classification number: A62D3/30 ,  C22B7/009 ,  C22B11/046 ,  C22B11/048 ,  Y02P10/214

Abstract: Processes for shutting down a regeneration reactor and for removing spent solid from the regeneration reactor may comprise shutting off a feed comprising an ionic liquid to the regeneration reactor, cooling the regeneration reactor, removing at least a portion of the ionic liquid from the regeneration reactor, purging the regeneration reactor with N 2 191 gas, introducing water into the regeneration reactor to form an acidic liquid in the regeneration reactor, and dumping the acidic liquid and the spent solid from the regeneration reactor. The acidic liquid may be neutralized with a basic liquid to provide a neutralized liquid. The spent solid may be separated from the neutralized liquid. In an embodiment, noble metal(s) may be recovered from the spent solid.

Abstract translation: 用于关闭再生反应器和从再生反应器中除去废固体的方法可以包括将包含离子液体的进料关闭到再生反应器，冷却再生反应器，从再生反应器中除去至少一部分离子液体， 用N 2 191气体吹扫再生反应器，将水引入再生反应器中以在再生反应器中形成酸性液体，并从再生反应器中倾倒酸性液体和废固体。 酸性液体可以用碱性液体中和以提供中和的液体。 废固体可以与中和的液体分离。 在一个实施方案中，贵金属可以从废固体中回收。

公开(公告)号：WO2016190977A1

公开(公告)日：2016-12-01

申请号：PCT/US2016/027434

申请日：2016-04-14

Applicant: CHEVRON U.S.A. INC.

Inventor： JOHNS, Jeff William ,  SOUERS, Steven Alden ,  MCDANIEL, Douglas Gayle ,  COOKE, David Lawrence ,  BOSI, David Michael

IPC: B01J8/00 ,  C10G49/00 ,  B01J19/00 ,  B01J8/02

CPC classification number: B08B9/08 ,  B01J8/003 ,  B01J8/0035 ,  B01J8/0285 ,  B01J19/0013 ,  B01J38/10 ,  B01J2208/00256 ,  B01J2208/00761 ,  B01J2208/00769 ,  B08B5/04 ,  B08B9/093 ,  B08B9/283 ,  B08B9/34 ,  C10G49/00 ,  C10G2300/4031 ,  C10G2300/701

Abstract: Processes for shutting down a hydroprocessing reactor and for removing catalyst from the reactor may comprise shutting off hydrocarbon feed to the reactor, stripping hydrocarbons from the catalyst, cooling the reactor to a first threshold reactor temperature, purging the reactor with N 2 gas, introducing water into the reactor, and dumping the catalyst from the reactor, wherein the first threshold reactor temperature may be substantially greater than 200°F. In an embodiment, the water may be introduced into the reactor via a quench gas distribution system when the reactor is at a second threshold reactor temperature not greater than 200°F to cool the reactor to a third threshold reactor temperature not greater than 120°F.

Abstract translation: 关闭加氢处理反应器和从反应器中除去催化剂的方法可包括：将烃进料切断至反应器，从催化剂中汽提烃，将反应器冷却至第一阈值反应器温度，用N 2气体吹扫反应器，将水引入 反应器，并从反应器中倾倒催化剂，其中第一阈值反应器温度可以基本上大于200°F。 在一个实施方案中，当反应器处于不大于200°F的第二阈值反应器温度时，可以通过骤冷气体分配系统将水引入反应器，以将反应器冷却至不超过120°F的第三阈值反应器温度 。