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US 10,870,810 B2Granted
Method and system for converting associated gas
AssigneeProteum Energy, LLC
InventorsJason S. Steill, Adam Smith, Dean C. Hoaglan, Scott V. Johnson, David L. Grottenthaler, Robert Terry Kennon, Michael R. Johnson, Steven K. Eddy, Kenneth Losch, Charles Robert Rapier, Jay K. Neutzler
Life of this patent
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Abstract
A volume of natural gas including a volume of methane and a volume of other alkanes may be cleaned of the other alkanes using a steam reformer system to create synthesis gas.
Claims51
A gas conversion system configured to form a second product gas from an associated gas stream, the gas conversion system comprising:
- a steam generator configured to receive system water and to output steam;
- a Joule-Thomson (J-T) apparatus configured (i) to receive at least a portion of an associated gas stream containing methane and non-methane hydrocarbons and (ii) to separate the at least a portion of the associated gas stream into:
- (a) a J-T liquid in gaseous form containing primarily non-methane hydrocarbons, and
- (b) a J-T gas containing primarily methane and lesser amounts of non-methane hydrocarbons;
- a mixing valve system configured to flow control at least a portion of the J-T liquid and the steam, and to output a feed gas which is a mixture of the steam and the at least a portion of the J-T liquid;
- a super heater configured to receive the feed gas and to superheat the feed gas to a predetermined temperature range to form a superheated feed gas;
- a heavy hydrocarbon reactor containing a first catalyst having a leading edge and configured to receive the superheated feed gas onto the leading edge and to crack a portion of the non-methane hydrocarbons of the superheated feed gas into carbon oxides and hydrogen to form a heavy hydrocarbon reactor reformate comprising methane in the J-T liquid from the associated gas stream, the carbon oxides, and the hydrogen;
- and
- a synthetic natural gas generator containing a second catalyst configured to receive the heavy hydrocarbon reactor reformate to convert a portion of the carbon oxides and the hydrogen into converted methane to form a synthetic natural wet processed gas containing the methane in the J-T liquid from the associated gas stream and the converted methane, wherein the synthetic natural wet processed gas has an overall higher methane mole fraction than the J-T liquid;
- wherein the gas conversion system is configured to blend (i) at least a portion of the synthetic natural wet processed gas as a product gas with (ii) the J-T gas to form the second product gas.
7 more elements
Dependencies are inferred from the claim text.