CA2205678C

CA2205678C - Gas storage method and product

Info

Publication number: CA2205678C
Application number: CA002205678A
Authority: CA
Inventors: Ian Morris; Glen Perry
Original assignee: JL Energy Transportation Inc
Current assignee: JL Energy Transportation Inc
Priority date: 1996-11-18
Filing date: 1997-05-16
Publication date: 1999-10-05
Anticipated expiration: 2017-05-16
Also published as: CA2205678A1

Abstract

For storage of natural gas at pressures over 1,000 psia, it is advantageous to add to natural gas an additive which is a C2 or C3 hydrocarbon compound, or a mixture of such hydrocarbon compounds. Above a lower limit (which varies with the additive being added and the pressure), a decrease in the amount of power needed to compress the mixture.
For storage or pipeline transportation of natural gas at pressures over 800 psia, it is advantageous to add ammonia to the natural gas, in an amount such that the ammonia does not create a liquid phase at the temperature and pressure used.
The ammonia-natural gas mixture can be compressed or pumped with a lower energy expenditure than would be needed for an equivalent volume of natural gas alone. When more than 4% by volume of ammonia is present, the pumping through pipelines is also aided by the refrigerant effect of the ammonia, which reduces the temperature of the gas being transported.

Instead of ammonia, hydrogen fluoride or carbon monoxide can be added to the natural gas, but these are less preferred than ammonia.

Claims

We claim as our invention:
A method of storing natural gas, which comprises (a) admixing the natural gas with one or more hydrocarbons selected from the group of saturated and unsaturated C2 and C3 hydrocarbons, to form a resulting mixture, the amount of said one or more hydrocarbons being sufficient so that the product of the z factor and the molecular weight of the resulting mixture is lower than the product of the z factor and the molecular weight for natural gas alone at the pressure at which the mixture will be stored, and (b) storing said resulting mixture at a temperature not exceeding 110°F. and a pressure or at least 1000 psia.
2. A method as claimed in claim 1, where the hydrocarbon comprises one or more hydrocarbons, in an amount which depends on the pressure at which the storage takes place, said amount being sufficient to give the mixture a total C2 hydrocarbon content which ranges smoothly from a minimum percentage by volume of not less than 26% when the storage is at a pressure of 1000psia, to a minimum percentage of 15% when the pressure is 2200 psia.
3. A method as claimed in claim 1 or 2 , in which the hydrocarbon is ethane.
4. A method as claimed in claim 1, where the hydrocarbon is one or more C3 hydrocarbons in an amount which depends on the pressure at which the storage takes place, said amount being sufficient to give the mixture a total C3 hydrocarbon content which ranges smoothly from a minimum percentage by volume of not less than about 5% when the storage is at a pressure of 1000 psia, to a minimum percentage of 3% when the pressure is 2200 psia.
5. A method as claimed in claim 1, in which the hydrocarbon is a mixture of propane and ethane.
6. A method as claimed in any of claims 1-5, in which the hydrocarbon is present in insufficient quantity for the formation of a coherent liquid phase at the temperature and pressure of storage.
7. A method of storing or transporting natural gas, which comprises, (a) admixing the natural gas with at least one compound selected from the group of ammonia, carbon monoxide and hydrogen fluoride to form a resulting mixture, and (b) storing said resulting mixture or transmitting it by pipeline at a temperature not exceeding 110°F. and a pressure of at least 800 psia.
8. A method as claimed in claim 7, in which the resulting mixture is stored, and said compound is present in (a) a minimum percentage by volume of at least:
(i) 0.5 % if the compound is ammonia;
(ii) 0.5% if the compound is hydrogen fluoride, or (iii) 1% if the compound is carbon monoxide;
(b) a maximum percentage by volume insufficient to form a coherent liquid phase at the temperature and pressure of storage.
9. A method as claimed in claim 7, in which the resulting mixture is transmitted by pipeline, and said compound is present in an amount of at least 4% by volume, but an amount insufficient to form a coherent liquid phase at the temperature and pressure of such transmission.
10. A method as claimed in any of claims 7, 8 or 9, in which said compound is ammonia.
11. A method as claimed in any of claims 7, 8 or 9, in which said compound is hydrogen fluoride.
12. A method as claimed in any of claims 7, 8 or 9, in which said compound is carbon monoxide.
13. A gas mixture, for use in a storage facility at a pressure greater than 1,150 psia and a temperature of from -40 degrees F. to +120 dgrees F., which comprises:
(a) from 68 to 92% by volume of methane (b) from 6 to 35% by volume of ethane (c) from 0% to 12% by volume of propane (d) from 0% to 1% by volume of butane (e) from 0% to 1% by volume of carbon dioxide (f ) From 0% to 2% by volume of nitrogen the total being 100%, and such mixture being gaseous with no coherent liquid phase at the temperature and pressure of intended operation.
14. A gas mixture as claimed in claim 13, said gas mixture being at a pressure of 1150-2160 psia and a temperature of from -20 degrees F. to +120 degrees F.
15. A gas mixture as claimed in claim 13, said gas mixture being at a pressure of 1350-1750 psia and a temperature of from 35 degrees F to +120 degrees F.
16. A gas mixture for use in a pipeline or storage at a pressure greater than 800 psia and a temperature of from -40 degrees F, to +100 degrees F. which comprises:
(a) natural gas (b) from 0.5% to 10% by volume of ammonia (c) 0 to 35% by volume of ethane in addition to the ethane forming part of the natural gas, the total being 100%, and such mixture being gaseous with no coherent liquid phase at the temperature and pressure of intended operation.
17. A gas mixture as claimed in claim 16, in which the amount of ammonia present is at least 4% by volume.
18. A gas mixture, for use in a pipeline or storage facility at a pressure greater than 1,000 psia and a temperature of -40 degrees F. to +100 degrees F., which comprises:
(a) from 68 to 92% by volume of methane (b) from 6 to 35% by volume of ethane (c) from 0 to 12% by volume of propane (d) from 0 to 1 % by volume of butane (e) not more than 1% each of carbon dioxide or nitrogen (f) at least 0.5% of ammonia or hyrogen fluoride the total being 100%, and such mixture being gaseous with no coherent liquid phase at the temperature and pressure of intended operation.
19. A gas mixture, for use in a pipeline or storage facility at a pressure greater than 1,000 psia and a temperature of -40 degrees F. to +100 degrees F., which comprises:
(a) from 68 to 92% by volume of methane (b) from 6 to 35% by volume of ethane (c) from 0 to 12% by volume of propane (d) from 0 to 1% by volume of butane (e) not more than 1% each of carbon dioxide or nitrogen (f) at least 1% carbon monoxide the total being 100%, and such mixture being gaseous with no coherent liquid phase at the temperature and pressure of intended operation.
20. A method of transporting natural gas which comprises:
adding to said natural gas at least 0.5% (based on volume of the total mixture) of ammonia to form an ammonia-natural gas mixture which is gaseous with no coherent liquid phase at a chosen pressure and temperature of pipeline transport transporting said ammonia-natural gas mixture to a desired destination by a pipeline pressurized to at least 800 psia and at a temperature of between -40°F
and 100°F, and separating said ammonia from said natural gas.
21. A method as claimed in claim 20, in which the amount of ammonia is a least 4% by volume.