IP Library Granted Patent US 8,802,909
Granted Patent B2
US 8,802,909 · App. 12/982,272 · Granted Aug 12, 2014

Method for improving productivity and process stability in styrene manufacturing system having multiple reactors connected in series

Inventors: Jong-Kuk Won (Daejeon, KR); Hee-Heon Jang (Chungcheongnam-do, KR)
Assignee: Samsung Total Petrochemicals Co., Ltd.
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Quick Facts
Patent No.
US 8,802,909
App. No.
12/982,272
Granted
Aug 12, 2014
Kind
B2
Abstract

A method for improving productivity and process stability in styrene monomer manufacturing system using a reaction system having multiple reactors connected in series, which can prevent destruction of the embedded catalyst and bending of a screen which supports catalyst and achieve homogeneous catalyst inactivation during the reaction by divergence of some portions of the feed containing steam and ethylbenzene and injection thereof into a certain point of the system.

Claims (9)

1. A method for improving productivity and process stability in a styrene preparation process system comprising:

Providing first (R- 1 ), second (R- 2 ), and third (R- 3 ) adiabatic reactors connected in series, the first adiabatic reactor (R- 1 ) having a first heat exchanger (HX- 1 ) located downstream and a first furnace (F-1) located upstream, the second adiabatic reactor (R- 2 ) having a second heat exchanger (HX- 2 ) located downstream and a second furnace (F-2) located upstream, and the third adiabatic reactor (R- 3 ) having a third heat exchanger (HX- 3 ) located downstream and a third furnace (F-3) located upstream;

diverging a portion of a raw material containing steam and ethylbenzene downstream from the third heat exchanger (HX- 3 ) to produce a diverged raw material;

diverging a portion of a steam having a temperature in the range of 800-900° C. discharged from the first furnace (F-1) to produce a diverged steam;

mixing the diverged raw material and the diverged steam to produce a first mixture; and

injecting the first mixture at a point (P) downstream from the second adiabatic reactor (R- 2 ) and upstream from the second heat exchanger (HX- 2 ) or injecting the first mixture at a point (Q) downstream from the second heat exchanger (HX- 2 ) and upstream from the third adiabatic reactor (R- 3 ).

2. The method according to claim 1 , wherein the third adiabatic reactor (R- 3 ) has a volume 2-5 times greater than each of the first (R- 1 ) and second (R- 2 ) adiabatic reactors.

3. The method according to claim 1 , wherein the diverged raw material is 15-20 vol % of a total amount of the raw material containing the ethylbenzene and the steam.

4. The method according to claim 1 , wherein the diverged steam is 15-20 vol % of a total amount of the steam feed.

Assignments (5)
CHANGE OF NAME Recorded Dec 1, 2022
From: HANWHA TOTAL PETROCHEMICAL CO., LTD.
To: HANWHA TOTALENERGIES PETROCHEMICAL CO., LTD.
Reel/Frame 062034/0926 →
CORRECTIVE ASSIGNMENT TO CORRECT THE RECEIVING PARTY ADDRESS PREVIOUSLY RECORDED AT REEL: 036548 FRAME: 0271. ASSIGNOR(S) HEREBY CONFIRMS THE ASSIGNMENT. Recorded Nov 9, 2015
From: SAMSUNG ATOFINA CO., LTD.; SAMSUNG TOTAL PETROCHEMICALS CO., LTD.
To: HANWHA TOTAL PETROCHEMICAL CO., LTD.
Reel/Frame 037071/0433 →
CHANGE OF NAME Recorded Sep 3, 2015
From: SAMSUNG ATOFINA CO., LTD.; SAMSUNG TOTAL PETROCHEMICALS CO., LTD.
To: HANWHA TOTAL PETROCHEMICAL CO., LTD.
Reel/Frame 036548/0271 →
CHANGE OF ADDRESS OF ASSIGNEE Recorded Jul 14, 2014
From: SAMSUNG TOTAL PETROCHEMICALS CO., LTD.
To: SAMSUNG TOTAL PETROCHEMICALS CO., LTD.
Reel/Frame 033312/0388 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jan 26, 2011
From: WON, JONG-KUK; JANG, HEE-HEON
To: SAMSUNG TOTAL PETROCHEMICALS CO., LTD.
Reel/Frame 025699/0706 →
Priority Claims (1)
KR 10-2010-0000921 · Jan 6, 2010 · national
Continuity (1)
Related Publication 20110166399A1 · Jul 7, 2011