IP Library Granted Patent US 11,448,460
Granted Patent B2
US 11,448,460 · App. 17/113,640 · Granted Sep 20, 2022

Process for separating hydrogen from an olefin hydrocarbon effluent vapor stream

Inventors: James Zhao (Houston, TX); Shukui Zhao (Katy, TX)
Assignee: Enflex, Inc.
F25J3/0252F25J3/0219F25J3/062F25J3/0645F25J3/0655F25J2200/02F25J2205/04F25J2210/04F25J2210/12F25J2210/62F25J2215/02F25J2215/04F25J2215/10F25J2215/64F25J2230/08F25J2230/20F25J2230/30F25J2230/32F25J2230/60F25J2235/60F25J2240/04F25J2240/40F25J2245/02F25J2270/06F25J2270/904
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Quick Facts
Patent No.
US 11,448,460
App. No.
17/113,640
Granted
Sep 20, 2022
Kind
B2
Abstract

One or more specific embodiments disclosed herein includes a method for separating hydrogen from an olefin hydrocarbon rich compressed effluent vapor stream, employing a single heat exchanger, multiple gas-liquid separators, multiple expander/compressor sets, and a rectifier attached to a liquid product drum.

Claims (38)

1. A process for the separation of hydrogen from an olefin hydrocarbon rich compressed effluent vapor stream from a dehydrogenation unit, which process comprises:

a. introducing a compressed effluent vapor stream into a processing unit;

b. cooling a compressed effluent vapor stream in a heat exchanger, wherein the heat exchanger comprises a warm section and a cold section;

c. separating hydrogen from olefin and heavy paraffinic components in the cooled compressed effluent vapor stream in a first separator to provide a first vapor stream and a first liquid stream;

d. cooling the first vapor stream in the heat exchanger;

e. separating hydrogen from olefin and heavy paraffinic components in the cooled first vapor stream in a second separator to provide a second vapor stream and a second liquid stream;

f. warming the second vapor stream in the heat exchanger;

g. isentropically expanding, in a first expander, the warmed second vapor stream, wherein the pressure and temperature of the warmed second vapor stream are lowered;

h. warming the isentropically expanded second vapor stream in the heat exchanger;

i. compressing, in a first compressor, the warmed, isentropically expanded second vapor stream;

j. cooling the compressed second vapor stream in a first discharge cooler;

k. dividing the cooled second vapor stream into a gas product and a split stream;

l. withdrawing a gas product from the processing unit;

m. compressing, in a second compressor, the split stream;

n. cooling the compressed split stream in a second discharge cooler and further cooling the cooled split stream in the heat exchanger;

o. isentropically expanding, in a second expander, the further cooled split stream, wherein the pressure and temperature of the further cooled split stream are lowered;

p. cooling a liquid paraffinic stream in the heat exchanger;

q. combining the cooled liquid paraffinic stream with the isentropically expanded split stream to provide a combined feed;

r. vaporizing the combined feed in the heat exchanger;

s. withdrawing the vaporized combined feed from the processing unit;

t. lowering the pressure of the first liquid stream in a control valve;

u. partially vaporizing the lowered-pressure first liquid stream in the heat exchanger;

v. flashing the partially vaporized first liquid stream in a liquid product drum to provide a hydrogen-rich gas, wherein the hydrogen-rich gas travels to a rectifier connected to the liquid product drum;

w. combining the hydrogen-rich gas and the second liquid stream in the rectifier, further purifying the hydrogen-rich gas;

x. warming the purified hydrogen-rich gas from the rectifier in the heat exchanger to provide a flashed vapor stream;

y. pumping a third liquid stream from the liquid product drum to the heat exchanger, wherein the third liquid stream is warmed; and

z. providing a liquid product.

2. The process of claim 1 , wherein the warm section and the cold section each comprise one or more brazed aluminum heat exchanger cores.

3. The process of claim 1 , which further comprises combining one or more liquid paraffinic side streams with the combined feed.

4. The process of claim 3 , which includes employing a booster compressor to provide additional pressure to the compressed second vapor stream from the first compressor.

5. The process of claim 3 , which includes mounting the first expander, the second expander, the first compressor, and the second expander to a bull gear.

6. The process of claim 5 , which includes employing a motor to drive the bull gear.

7. The process of claim 3 , which includes driving one or more electric generators by the power produced in the first expander, second expander, or both expanders.

8. The process of claim 3 , wherein the one or more liquid paraffinic side streams comprises two liquid paraffinic side streams.

9. The process of claim 8 , which includes employing a booster compressor to provide additional pressure to the compressed second vapor stream from the first compressor.

10. The process of claim 8 , which includes mounting the first expander, the second expander, the first compressor, and the second expander to a bull gear.

11. The process of claim 10 , which includes employing a motor to drive the bull gear.

12. The process of claim 8 , which includes driving one or more electric generators by the power produced in the first expander, second expander, or both expanders.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Dec 8, 2020
From: ZHAO, JAMES; ZHAO, SHUKUI
To: ENFLEX, INC.
Reel/Frame 054573/0152 →
Continuity (3)
Division 15988601 · May 24, 2018
Continuation In Part 15600758 · May 21, 2017
Related Publication 20210088278A1 · Mar 25, 2021