IP Library Granted Patent US 10,816,262
Granted Patent B2
US 10,816,262 · App. 16/077,484 · Granted Oct 27, 2020

Production equipment and production method of liquefied hydrogen and liquefied natural gas

Inventors: Yoshiyuki Watanabe (Kanagawa, JP); Hidefumi Omori (Kanagawa, JP); Toru Matsuhara (Kanagawa, JP); Shintaro Watanabe (Kanagawa, JP); Toru Nakayama (Kanagawa, JP)
Assignee: JGC CORPORATION
F25J1/001C01B3/38C01B3/506F25B9/00F25J1/004F25J1/005F25J1/0022F25J1/0052F25J1/0065F25J1/0067F25J1/0072F25J1/0087F25J1/021F25J1/0211F25J1/0217F25J1/0229F25J1/0236C01B2203/0227C01B2203/043C01B2203/046C01B2203/048C01B2203/0415C01B2203/0495C01B2203/127F25J2210/60F25J2215/10F25J2220/02F25J2220/60F25J2220/66F25J2260/60F25J2260/80F25J2270/16
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Quick Facts
Patent No.
US 10,816,262
App. No.
16/077,484
Granted
Oct 27, 2020
Kind
B2
Abstract

Provided is a production facility for liquefied hydrogen and a liquefied natural gas from a natural gas, including: a first heat exchanger configured to cool a hydrogen gas through heat exchange between the hydrogen gas and a mixed refrigerant for liquefying a natural gas containing a plurality of kinds of refrigerants selected from the group consisting of methane, ethane, propane, and nitrogen; a second heat exchanger configured to cool the mixed refrigerant through heat exchange between the mixed refrigerant and propane; and a third heat exchanger configured to cool the hydrogen gas through heat exchange between the hydrogen gas and a refrigerant containing hydrogen or helium, wherein the first heat exchanger has a precooling temperature of from −100° C. to −160° C.

Claims (29)

1. A production facility for liquefied hydrogen and a liquefied natural gas from a natural gas, comprising:

a first heat exchanger configured to cool a hydrogen gas through heat exchange between the hydrogen gas and a mixed refrigerant used for liquefying a natural gas containing a plurality of kinds of refrigerants selected from the group consisting of methane, ethane, propane, and nitrogen;

a second heat exchanger configured to cool the mixed refrigerant through heat exchange between the mixed refrigerant and propane; and

a third heat exchanger configured to cool the hydrogen gas through heat exchange between the hydrogen gas and a refrigerant containing hydrogen or helium,

wherein the first heat exchanger provides precooling at a precooling temperature of from −100° C. to −160° C.;

the production facility further comprises:

a liquefied hydrogen production line comprising at least one acid gas removal unit;

a liquefied natural gas production line comprising an acid gas removal unit; and

a single acid gas stripping unit shared between the liquefied hydrogen production line and the liquefied natural gas production line, and configured to collectively strip an acid gas absorbed in the acid gas removal units of the liquefied hydrogen production line and the liquefied natural gas production line,

wherein the liquefied natural gas production line is used for producing the liquefied natural gas and the liquefied hydrogen production line is used for producing a raw material hydrogen that is supplied as the hydrogen gas to the first heat exchanger.

2. The production facility for liquefied hydrogen and a liquefied natural gas according to claim 1 ,

wherein the liquefied hydrogen production line and the liquefied natural gas production line further comprises at least one natural gas pretreatment unit selected from the group consisting of a condensate separation unit, and a mercury removal unit,

so that a natural gas having been subjected to the pretreatment unit is divided into the liquefied hydrogen production line for producing the raw material hydrogen and the liquefied natural gas production line for producing the liquefied natural gas.

3. The production facility for liquefied hydrogen and a liquefied natural gas according to claim 1 ,

wherein the production facility comprises a plurality of the acid gas removal units in the liquefied hydrogen production line, and

wherein the single acid gas stripping unit is configured to collectively strip the acid gas absorbed in the acid gas removal unit in the liquefied natural gas production line and acid gases absorbed in the plurality of the acid gas removal units in the liquefied hydrogen production line.

4. A production method for liquefied hydrogen and a liquefied natural gas from a natural gas, comprising:

dividing a natural gas into a liquefied hydrogen production line for producing a hydrogen gas and a liquefied natural gas production line for producing a liquefied natural gas;

removing an acid gas from the natural gas in the liquefied natural gas production line and an acid gas from the natural gas in the liquefied hydrogen production line;

collectively stripping the acid gas removed from the natural gas in the liquefied natural gas production line and the acid gas removed from the natural gas in the liquefied hydrogen production line;

using a refrigerant for producing the liquefied natural gas in a precooling step for producing liquefied hydrogen,

the precooling step for producing liquefied hydrogen having a precooling temperature of from −100° C. to −160° C.,

the refrigerant for liquefying the natural gas comprising a mixed refrigerant containing a plurality of kinds of refrigerants selected from the group consisting of methane, ethane, propane, and nitrogen;

precooling the mixed refrigerant through heat exchange between the mixed refrigerant and propane; and

cooling the hydrogen gas supplied from the liquefied hydrogen production line through heat exchange between the hydrogen gas and a refrigerant containing hydrogen or helium.

5. The production method for liquefied hydrogen and a liquefied natural gas according to claim 4 , wherein the production method further comprises subjecting the natural gas in each of the liquefied hydrogen production line and the liquefied natural gas production line to at least one pretreatment selected from the group consisting of condensate separation treatment and mercury removal treatment.

6. The production method for liquefied hydrogen and a liquefied natural gas according to claim 4 , wherein the production method further comprises:

removing another acid gas from a process gas which is produced after a shift reaction of a reformed gas containing hydrogen as a main component in the liquefied hydrogen production line; and

collectively stripping the another acid gas produced after the shift reaction together with the acid gas removed from the natural gas in the liquefied natural gas production line and the acid gas removed from the natural gas in the liquefied hydrogen production line.

Assignments (3)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Feb 5, 2020
From: JGC HOLDINGS CORPORATION
To: JGC CORPORATION
Reel/Frame 051718/0796 →
CHANGE OF NAME Recorded Dec 24, 2019
From: JGC CORPORATION
To: JGC HOLDINGS CORPORATION
Reel/Frame 051415/0734 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Aug 24, 2018
From: WATANABE, YOSHIYUKI; OMORI, HIDEFUMI; MATSUHARA, TORU; WATANABE, SHINTARO; NAKAYAMA, TORU
To: JGC CORPORATION
Reel/Frame 046690/0898 →
Continuity (1)
Related Publication 20190063824A1 · Feb 28, 2019
Cited By (2)
US 12,287,144 US 12,535,268