公开(公告)号：US11673975B2

公开(公告)日：2023-06-13

申请号：US17409958

申请日：2021-08-24

Applicant: Chevron Phillips Chemical Company LP

Inventor： Bradley T. Price ,  Jamie N. Sutherland ,  Joseph A Curren ,  James E. Hein

IPC: C08F2/00 ,  C08F10/02 ,  C08F2/01 ,  B01J19/24 ,  B01J8/00 ,  B01J4/00 ,  C08F6/10 ,  C08F2/14

CPC classification number: C08F2/008 ,  B01J4/008 ,  B01J8/006 ,  B01J8/0015 ,  B01J19/2435 ,  C08F2/01 ,  C08F2/14 ,  C08F6/10 ,  C08F10/02 ,  B01J2219/0004 ,  B01J2219/00042 ,  B01J2219/00162

Abstract: A system including a dump tank to receive a reactor product comprising a polymer and hydrocarbons, including liquid hydrocarbons, the dump tank including a vessel with a reactor product inlet, a motive gas inlet, a purge gas inlet, gas outlet(s), and a fluid outlet, the motive gas inlet for introducing a motive gas into the vessel, the purge gas inlet for introducing a purge gas into the vessel, the one or more gas outlets located at a top of the vessel and the fluid outlet located at a bottom of the vessel and fluidly connected with a dump tank fluid outlet line having a dump tank outlet valve to control flow of fluid out of the dump tank via the fluid outlet; and a strainer fluidly connected with the dump tank fluid outlet line to allow passage of liquid hydrocarbons therethrough into a hydrocarbon outlet line.

公开(公告)号：US12146106B2

公开(公告)日：2024-11-19

申请号：US17658921

申请日：2022-04-12

Applicant: CHEVRON PHILLIPS CHEMICAL COMPANY LP

Inventor： Ronald G. Abbott ,  Bruce D. Murray ,  Scott G. Morrison ,  Bradley T. Price

IPC: C10G1/00 ,  C07C4/04 ,  C08F10/02 ,  C10B53/07 ,  C10B57/06 ,  C10G1/10 ,  C10G9/36 ,  C10G11/18 ,  C10L1/06 ,  C10L1/08 ,  C10L3/06

Abstract: Processes for using pyrolysis gas as a feedstock or a co-feedstock for making a variety of chemicals, for example, circular ethylene, circular ethylene polymers and copolymers, and other circular products. In these processes, pyrolysis reactor conditions can be selected to increase or optimized the production of pyrolysis gas over pyrolysis oil, and the pyrolysis gas which is usually used as fuel or flared can be fed downstream of the steam cracker furnace for economic use to form circular chemicals. Operating parameters of the pyrolysis unit may be adjusted to increase or decrease the proportion of pyrolysis gas relative to pyrolysis liquid as a function of their relative economic values.