METHOD FOR SELECTIVE HYDROGENATION OF BUTADIENE EXTRACTION TAIL GAS AND SELECTIVE HYDROGENATION APPARATUS THEREOF
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United States of America Patent
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N/A
Issued Date -
Mar 7, 2024
app pub date -
Oct 19, 2021
filing date -
Oct 26, 2020
priority date (Note) -
Published
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Abstract
The present invention belongs to the field of petrochemical industry, and discloses a method for selective hydrogenation of butadiene extraction tail gas and a selective hydrogenation apparatus thereof. The method for selective hydrogenation of butadiene extraction tail gas comprises: (1) an alkyne-containing tail gas from a butadiene extraction unit is fed into a raw material tank, optionally impurities entrained in the alkyne-containing tail gas are removed before being fed into the raw material tank; (2) a C4 raw material in the raw material tank is pressurized by a feed pump to a pressure required for reaction, then merged with a circulated C4 stream from a first-stage reactor outlet buffer tank and fed into a first-stage mixer, wherein it is mixed with hydrogen gas, and fed into the first-stage reactor to undergo a first-stage hydrogenation reaction, and a first-stage reaction stream obtained by the reaction is fed into the first-stage reactor outlet buffer tank; the hydrogen gas required for the reaction in the first-stage reactor is fed through a first feeding mode or a second feeding mode: the first feeding mode comprises: all the hydrogen gas required for the reaction is fed through the first-stage reactor outlet buffer tank, and then fed into the first-stage reactor through a first route at an outlet of the first-stage reactor outlet buffer tank; the second feeding mode comprises: a part of the hydrogen gas required for the reaction is fed through the first-stage reactor outlet buffer tank, and then fed into the first-stage reactor through the first route at an outlet of the first-stage reactor outlet buffer tank; and the other part of the hydrogen gas is fed through the first-stage mixer, and then fed into the first-stage reactor; (3) there is no gas-phase discharge from the first-stage reactor outlet buffer tank, and a liquid-phase product is divided into at least two streams, the first stream is returned to the first-stage reactor as the circulated C4 stream, and the second stream is used as a feed to a stabilization tower or subjected to further hydrotreatment prior to being fed into the stabilization tower; (4) a C4 hydrogenation product is recovered after separation in the stabilization tower.

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Patent Owner(s)
Patent Owner | Address | |
---|---|---|
BEIJING RESEARCH INSTITUTE OF CHEMICAL INDUSTRY CHINA PETROLEUM & CHEMICAL CORPORATION | NO 14 BEISANHUAN EAST ROAD CHAOYANG DISTRICT BEIJING 100013 | |
CHINA PETROLEUM & CHEMICAL CORPORATION | NO 22 CHAOYANGMEN NORTH STREET CHAOYANG DISTRICT BEIJING 100728 100728 |
International Classification(s)
Inventor(s)
Inventor Name | Address | # of filed Patents | Total Citations |
---|---|---|---|
CUI, Ting | Beijing, CN | 11 | 12 |
DU, Zhou | Beijing, CN | 5 | 0 |
GUO, Liang | Beijing, CN | 173 | 1804 |
LI, Chunfang | Beijing, CN | 5 | 16 |
LI, Dongfeng | Beijing, CN | 21 | 185 |
LI, Yan | Beijing, CN | 1447 | 20982 |
LUO, Shujuan | Beijing, CN | 3 | 1 |
SHU, Zhan | Beijing, CN | 17 | 44 |
TIAN, Jun | Beijing, CN | 339 | 2974 |
YE, Jieming | Beijing, CN | 2 | 0 |
YUE, Yi | Beijing, CN | 10 | 13 |
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