IP Library › Granted Patent US 10,364,199
Granted Patent B2
US 10,364,199 · App. 15/523,910 · Granted Jul 30, 2019

Propane production method and propane production apparatus

Inventors: Akihiro Kuwana (Hyogo, JP); Junichi Kawakami (Hyogo, JP); Shuji Tsuno (Hyogo, JP)
Assignee: SUMITOMO SEIKA CHEMICALS CO., LTD.
C07C5/03C07C7/04C07C7/09C07C7/13C07C7/163C07C9/08
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Quick Facts
Patent No.
US 10,364,199
App. No.
15/523,910
Granted
Jul 30, 2019
Kind
B2
Abstract

A propane production method includes a hydrogenation reaction step of hydrogenation-reacting crude propylene and hydrogen in a presence of a catalyst to obtain gaseous crude propane containing impurities; and an impurity removal step of removing the impurities contained in the gaseous crude propane obtained in the hydrogenation reaction step to obtain purified propane. The impurity removal step includes an adsorptive removal stage of adsorbing and removing water, ethane and propylene contained as impurities in the gaseous crude propane by adsorption treatment in which the gaseous crude propane is brought into contact with an adsorbent, and a separation removal stage of separating and removing hydrogen, oxygen, nitrogen and methane contained as impurities in the crude propane after the adsorption treatment by partial condensation or distillation of crude propane after the adsorption treatment in the adsorptive removal stage.

Claims (13)

1. A propane production method, comprising:

a hydrogenation reaction step of hydrogenation-reacting crude propylene having a propylene purity of 95 mol % or more and comprising less than 1.0 vol·ppm isobutene, less than 1.0 vol·ppm normal butene, and less than 1.0 vol·ppm pentane, and hydrogen in a presence of a catalyst under conditions comprising a pressure of 0.0 MPaG to 1.0 MPaG and a temperature of 50° C. to 200° C. to obtain gaseous crude propane containing impurities; and

an impurity removal step of removing the impurities contained in the gaseous crude propane obtained in the hydrogenation reaction step to obtain a purified propane,

wherein the impurities include hydrogen, oxygen, nitrogen, water, methane, ethane, and propylene,

wherein the impurity removal step includes

an adsorptive removal stage of adsorbing and removing water, ethane and propylene contained as impurities in the gaseous crude propane by adsorption treatment in which the gaseous crude propane is brought into contact with an adsorbent, and

a separation removal stage of separating and removing hydrogen, oxygen, nitrogen and methane contained as impurities in the crude propane after the adsorption treatment by partial condensation or distillation of crude propane after the adsorption treatment in the adsorptive removal stage, and

wherein the adsorption treatment in the adsorptive removal stage is performed under conditions comprising a pressure of 0.1 to 0.3 MPaG.

2. The propane production method according to claim 1 ,

wherein the adsorbent is molecular sieve zeolite and molecular sieve activated carbon.

3. The propane production method according to claim 2 ,

wherein the molecular sieve zeolite and the molecular sieve activated carbon are porous bodies having pores with a pore diameter of 4 angstroms.

4. The propane production method according to claim 1 , wherein the adsorption treatment in the adsorptive removal stage is performed under a temperature range of 5 to 50° C.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded May 9, 2017
From: KUWANA, AKIHIRO; KAWAKAMI, JUNICHI; TSUNO, SHUJI
To: SUMITOMO SEIKA CHEMICALS CO., LTD.
Reel/Frame 042303/0842 →
Priority Claims (1)
JP 2015-016126 · Jan 29, 2015 · national
Continuity (1)
Related Publication 20170349506A1 · Dec 7, 2017
Cited By (1)
US 12,404,465