Process for producing a natural gas substitute

Claim 2

A process for producing a natural gas substitute at least partly from a hydrocarbon feedstock of higher molecular weight than methane which comprises: a. a first stage comprising reacting a hydrocarbon feedstock that is methane or is partly or wholly of a higher molecular weight than methane at a pressure in the range of 5-40 ata with steam in an externally heated tubular catalytic steam reforming process at an outlet temperature in the range 600°-900°C to give a first gas containing carbon oxides and hydrogen but under 30% of methane by volume on a dry basis and cooling the flue gases from the furnace of said externally heated tubular catalytic steam reforming process in a waste-heat boiler producing steam at over 1000 psig and letting down the steam in expansion engines; b. a second stage comprising reacting together the first gas, steam and hydrocarbon feedstock of higher molecular weight than methane at an outlet temperature of 600°-700°C over a catalyst having steam reforming and methanation activity to give a second gas, the second gas containing carbon oxides and hydrogen and having a methane content greater than that of the first gas and in the range 20-40% by volume on a dry basis and cooling the second gas in a waste-heat boiler producing steam at over 1000 psig and letting down the steam in expansion engines; and c. a third stage comprising reacting said second gas catalytically under methanating conditions at an outlet temperature in the range 250°-450°C in heat exchange with boiling water generating steam in which the steam generated by the said heat exchange with boiling water is at a pressure over 1000 psig and is therafter let down in expansion engines, whereby heat is continuously removed.

Claim 3

A process according to claim 1 in which the hydrogen content of the second gas is over 15%.

Claim 4

A process according to claim 1 comprising compressing the second gas and subjecting the compressed second gas to steam and carbon dioxide removal before passing it to the third stage.

Claim 5

A process according to claim 3 in which the second gas after removal of steam and carbon dioxide contains 0.3 to 4.0 volume % of steam, 2-6 volume % of of carbon dioxide and over 15 volume % of hydrogen.

Claim 6

A process according to claim 3 in which the pressure of the second gas is under 40 ata before compression and at least 68 ata after compression.

Claim 7

A process for producing a natural gas substitute at least partly from a hydrocarbon feedstock of higher molecular weight than methane which comprises: a. a first stage comprising reacting a hydrocarbon feedstock that is methane or is partly or wholly of a higher molecular weight than methane at a pressure in the range of 5- 40 ata with steam in an externally heated tubular catalytic steam reforming process at an outlet temperature in the range 600°-900°C to give a first gas containing carbon oxides and hydrogen but under 30% of methane by volume on a dry basis and cooling the flue gases from the furnace of said externally heated tubular catalytic steam reforming process in a waste-heat boiler producing steam at over 1000 psig and letting down the steam in expansion engines; b. a second stage comprising reacting together the first gas, steam and hydrocarbon feedstock of higher molecular weight than methane at an outlet temperature of 600°-700°C over a catalyst having steam reforming and methanation activity to give a second gas, the second gas containing carbon oxides and hydrogen and having a methane content greater than that of the first gas and in the range 20- 40% by volume on a dry basis and cooling the second gas in a waste-heat boiler producing steam at over 1000 psig and letting down the steam in expansion engines; c. a cooling stage in which the second gas is cooled; and then d. a third stage comprising catalytically reacting under methanating conditions the second gas at an outlet temperature in the range 250°-450°C in co-current heat exchange with feed gas from stage c) and cooling the gas product exiting the third stage in a waste-heat boiler producing steam at over 1000 psig and letting down the steam in expansion engines, whereby heat is continuously removed from the reacting gas and the feed gas to the third stage is warmed preparatory to entering the catalyst bed.

Claim 8

A process for producing a natural gas substitute at least partly from a hydrocarbon feedstock of higher molecular weight than methane which comprises: a. a first stage comprising reacting a hydrocarbon feedstock that is methane or is partly or wholly of a higher molecular weight than methane at a pressure in the range of 5- 40 ata with steam in an externally heated tubular catalytic steam reforming process at an outlet temperature in the range 600°-900°C to give a first gas containing carbon oxides and hydrogen but under 30% of methane by volume on a dry basis and cooling the flue gases from the furnace of said externally heated tubular catalytic steam reforming process in a waste-heat boiler producing steam at over 1000 psig and letting down the steam in expansion engines; b. a second stage comprising reacting together the first gas, steam and hydrocarbon feedstock of higher molecular weight than methane at an outlet temperature of 600°-700°C over a catalyst having steam reforming and methanation activity to give a second gas, the second gas containing carbon oxides and hydrogen and having a methane content greater than that of the first gas and in the range 20- 40% by volume on a dry basis and cooling the second gas in a waste-heat boiler producing steam at over 1000 psig and letting down the steam in expansion engines; c. a cooling stage in which the second gas is cooled; and then d. a third stage comprising catalytically reacting under methanating conditions the second gas at an outlet temperature in the range 250°-450°C in co-current heat exchange with feed gas from stage c) and cooling the gas product exiting the third stage in a waste-heat boiler producing steam at over 1000 psig and letting down the steam in expansion engines, whereby heat is continuously removed from the reacting gas and the feed gas to the third stage is warmed preparatory to entering the catalyst bed.

Claim 9

A process according to claim 6 in which the hydrogen content of the second gas is between 8 and 20%.

Claim 10

A process according to claim 6 further comprising compressing the second gas and subjecting it to steam and carbon dioxide removal before passing it to the third stage.

Claim 11

A process according to claim 8 in which the second gas after removal of steam and carbon dioxide contains 0.3 to 4.0 volume % of steam, 2-6 volume % of carbon dioxide and between 8 and 20 volume % of hydrogen.

Claim 12

A process according to claim 8 in which the pressure of the second gas is under 40 ata before compression and at least 68 ata after compression.

Claim 13

A process for producing a natural gas substitute at least partly from a hydrocarbon feedstock of higher molecular weight than methane which comprises a. a first stage comprising reacting a hydrocarbon feedstock that is methane or is partly or wholly of a higher molecular weight than methane at a pressure in the range of 5-40 ata with steam in an externally heated tubular catalytic reforming process at an outlet temperature in the range 600°-900°C to give a first gas containing carbon oxides and hydrogen but under 12% of methane by volume and cooling the flue gases from the furnace of the externally heated tubular catalytic steam reforming process in a waste-heat boiler producing steam at over 1000 psig and letting down the steam in expansion engines; b. a second stage comprising reacting together the feed gas, steam and hydrocarbon feedstock of higher molecular weight than methane at an outlet temperature in the range 250°-450°C over a catalyst having steam reforming and methanation activity in heat exchange with boiling water generating steam in which the steam generated by the said heat exchange with boiling water is at a pressure over 1000 psig and is thereafter let down in expansion engines to produce a second gas, the second gas having a methane content of over 90% by volume on a dry CO 2 -free basis.

Claim 14

A process for producing a natural gas substitute at least partly from a hydrocarbon feedstock of higher molecular weight than methane which comprises a. a first stage comprising reacting a hydrocarbon feedstock that is methane or is partly or wholly of a higher molecular weight than methane at a pressure in the range of 5-40 ata with steam in an externally heated tubular catalytic reforming process at an outlet temperature in the range 600°-900°C to give a first gas containing carbon oxides and hydrogen but under 12% of methane by volume and cooling the flue gases from the furnace of the externally heated tubular catalytic steam reforming process in a waste-heat boiler producing steam at over 1000 psig and letting down the steam in expansion engines; b. a second stage comprising reacting together the feed gas, steam and hydrocarbon feedstock of higher molecular weight than methane at an outlet temperature in the range 250°-450°C over a catalyst having steam reforming and methanation activity in heat exchange with boiling water generating steam in which the steam generated by the said heat exchange with boiling water is at a pressure over 1000 psig and is thereafter let down in expansion engines to produce a second gas, the second gas having a methane content of over 90% by volume on a dry CO 2 -free basis.

Claim 15

A process according to claim 11 including further methanating the second gas in a third stage.

Claim 16

A process according to claim 11 in which the temperature at the outlet of the second stage is less than that at the inlet by between 20° and 100°C.

Claim 17

A process according to claim 11 in which the feedstock fed to the second stage is between 75 and 95% of the total hydrocarbon fed to the process.

Claim 18

A process for producing a natural gas substitute at least partly from a hydrocarbon feedstock of higher molecular weight than methane which comprises a. a first stage comprising reacting a hydrocarbon feedstock that is methane or is partly or wholly of a higher molecular weight than methane at a pressure in the range of 5-40 ata with steam in an eternally heated tubular catalytic reforming process at an outlet temperature in the range 600°-900°C to give a first gas containing carbon oxides and hydrogen but under 12% of methane by volume and cooling the flue gases from the furnace of the externally heated tubular catalytic steam reforming process in a waste-heat boiler producing steam at over 1000 psig and letting down the steam in expansion engines; b. a cooling stage in which the first gas is cooled; and then c. a second stage comprising reacting together the first gas, steam and hydrocarbon feedstock at an outlet temperature in the range 250°-450°C over a catalyst having steam reforming and methanation activity to produce a second gas having a methane content of over 90% by volume on a dry CO 2 -free basis, the second stage reaction being performed in co-current heat exchange with cool gas from stage b), whereby heat is continuously removed from the reacting gas and the first gas from said cooling stage is warmed preparatory to entering the catalyst bed and cooling the second gas in a waste heat boiler producing steam at over 1000 psig and letting down the steam in expansion engines.

Claim 19

A process for producing a natural gas substitute at least partly from a hydrocarbon feedstock of higher molecular weight than methane which comprises a. a first stage comprising reacting a hydrocarbon feedstock that is methane or is partly or wholly of a higher molecular weight than methane at a pressure in the range of 5-40 ata with steam in an eternally heated tubular catalytic reforming process at an outlet temperature in the range 600°-900°C to give a first gas containing carbon oxides and hydrogen but under 12% of methane by volume and cooling the flue gases from the furnace of the externally heated tubular catalytic steam reforming process in a waste-heat boiler producing steam at over 1000 psig and letting down the steam in expansion engines; b. a cooling stage in which the first gas is cooled; and then c. a second stage comprising reacting together the first gas, steam and hydrocarbon feedstock at an outlet temperature in the range 250°-450°C over a catalyst having steam reforming and methanation activity to produce a second gas having a methane content of over 90% by volume on a dry CO 2 -free basis, the second stage reaction being performed in co-current heat exchange with cool gas from stage b), whereby heat is continuously removed from the reacting gas and the first gas from said cooling stage is warmed preparatory to entering the catalyst bed and cooling the second gas in a waste heat boiler producing steam at over 1000 psig and letting down the steam in expansion engines.