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-modified
We 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.

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