US2004244279A1PendingUtilityA1
Fuel compositions comprising natural gas and dimethyl ether and methods for preparation of the same
Priority: Mar 27, 2003Filed: Mar 22, 2004Published: Dec 9, 2004
Est. expiryMar 27, 2023(expired)· nominal 20-yr term from priority
C10L 3/003C10L 3/10
48
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Claims
Abstract
The invention is directed to compositions comprising mixtures of natural gas and dimethyl ether suitable for use as fuel compositions, and particularly to blends of dimethyl ether and a natural gas derived from LNG produced in an LNG process. The dimethyl ether can be added, for example, to a lean natural gas to improve the heat value thereof, and in embodiments, the dimethyl ether is conveniently derived from low value CO 2 contaminants present in a raw natural gas stream used to prepare LNG. Also disclosed are methods to prepare the mixtures.
Claims
exact text as granted — not AI-modifiedWe claim:
1 . A composition comprising natural gas and dimethyl ether.
2 . The composition of claim 1 wherein the natural gas is a lean natural gas.
3 . The composition of claim 2 wherein the lean natural gas comprises less than about 3 mol % of C 2 to C 5 hydrocarbons with the balance of the hydrocarbons in the lean natural gas being essentially methane, based on the total composition.
4 . The composition of claim 1 wherein dimethyl ether is present in an amount of less than 25 mol % based on the total composition.
5 . The composition of claim 1 wherein dimethyl ether is present in an amount of less than 20 mol % based on the total composition.
6 . The composition of claim 1 wherein dimethyl ether is present in an amount of from 10 mol % to 15 mol % based on the total composition.
7 . The composition of claim 1 wherein the natural gas is derived from a regasified LNG product produced in an LNG process.
8 . The composition of claim 1 having a heating value of from about 1000 BTU/scf to about 1200 BTU/scf.
9 . The composition of claim 1 having a heating value of from about 1030 BTU/scf to about 1170 BTU/scf.
10 . The composition of claim 1 having a heating value of from about 1050 BTU/scf to about 1150 BTU/scf.
11 . A method for preparing a fuel blend comprising natural gas and dimethyl ether, the method comprising mixing a natural gas component and dimethyl ether.
12 . The method of claim 11 wherein the natural gas component is derived from a regasified LNG product prepared in a LNG process.
13 . The method of claim 12 further comprising:
pre-treating a natural gas stream comprising acid gases, water and other contaminants therein to remove at least a portion of the contaminants therefrom and provide a natural gas feed;
cooling the natural gas feed in the LNG process to liquefy at least a portion of the natural gas component and thereby produce a LNG product; and
re-gasifying the LNG product to obtain the natural gas component.
14 . The method of claim 13 further comprising:
providing dimethyl ether; and
mixing the dimethyl ether with the natural gas component to obtain the fuel blend.
15 . The method of claim 14 wherein mixing of the natural gas component and dimethyl ether occurs at a site remote from the location where the natural gas stream originates.
16 . The method of claim 12 wherein the dimethyl ether is blended in an amount such that the concentration of dimethyl ether in the fuel blend is less than 25 mol % based on the total fuel blend.
17 . The method of claim 12 wherein the dimethyl ether is blended in an amount such that the concentration of dimethyl ether in the fuel blend is less than 20 mol % based on the total fuel blend.
18 . The method of claim 12 wherein the dimethyl ether is blended in an amount such that the concentration of dimethyl ether in the fuel blend is from 10 mol % to 15 mol % based on the total fuel blend.
19 . The method of claim 12 wherein the fuel blend has a heating value of from about 1000 BTU/scf to about 1200 BTU/scf.
20 . The method of claim 12 wherein the fuel blend has a heating value of from about 1030 BTU/scf to about 1170 BTU/scf.
21 . The method of claim 12 wherein the fuel blend has a heating value of from about 1050 BTU/scf to about 1150 BTU/scf.
22 . The method of claim 11 further comprising:
pre-treating a natural gas stream comprising acid gases, water and other contaminants therein to remove at least a portion of the contaminants therefrom and provide a natural gas feed for a LNG process;
mixing the dimethyl ether into the natural gas feed within a LNG process at a temperature above −220° F. (−140° C.) and in an amount such that the dimethyl ether does not solidify and form a separate solid phase during liquefaction of the natural gas feed in the LNG process; and
cooling the resulting natural gas and dimethyl ether mixture within the LNG process to a temperature of from about −240° F. (−151° C.) to about −260° F. (−162° C.) or less so as to liquefy at least a portion of the mixture and thereby produce a blended liquid product at substantially atmospheric pressure; and
re-gasifying the blended liquid product to produce the fuel blend.
23 . The method of claim 22 wherein the fuel blend comprises dimethyl ether in an amount of 5 mole % or less based on the total fuel blend.
24 . A method for preparing a fuel blend comprising natural gas and dimethyl ether, the method comprising:
pre-treating a natural gas stream comprising acid gases, water and other contaminants therein to remove at least a portion of the contaminants therefrom and provide a natural gas feed; cooling the natural gas feed in a LNG process to liquefy at least a portion of the natural gas component and thereby produce a LNG product; providing dimethyl ether; re-gasifying the LNG product to obtain the natural gas component; and mixing the dimethyl ether with the natural gas component to obtain the fuel blend.Join the waitlist — get patent alerts
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