Method for removing hydrogen sulfide from an acid gas
A method for removing hydrogen sulfide (H 2 S) from an acid gas comprises feeding the gas to a membrane separation unit, collecting the product gas from the membrane unit, heating the permeate stream to the necessary inlet temperature for catalytic oxidation of H 2 S and feeding the heated permeate stream to a catalytic oxidation unit, where H 2 S is oxidized to SO 2 . The heating of the permeate stream is accomplished by using a fraction of the feed gas to heat the permeate stream in a separate heater or by using a steam-fired heater. The method is especially suited for use on an off-shore facility.
1. A method for removing hydrogen sulfide (H 2 S) from an acid gas, said method comprising the steps of:
feeding the acid gas to a membrane separation unit, optionally after membrane pre-treatment, drying and/or extraction of higher hydrocarbons, and separating the acid gas into a product gas and a permeate stream,
collecting the product gas from the membrane unit,
heating the permeate stream to an inlet temperature for catalytic oxidation of H 2 S over a monolithic metal oxide catalyst consisting of one or more metal oxides, and
feeding the heated permeate stream to a catalytic oxidation unit and oxidizing the H 2 S to SO 2 , wherein the catalytic oxidation unit comprises the monolithic metal oxide catalyst, and wherein the monolithic metal oxide catalyst oxidizes the H 2 S to SO 2 according to the equation
H 2 S+1.5O 2 →SO 2 +H 2 O
wherein the heating of the permeate stream is accomplished by using a fraction of the acid gas to heat the permeate stream in a separate heater, or
wherein the heating of the permeate stream is accomplished by using a steam heater, wherein the membrane separation unit and the catalytic oxidation unit are located on an off-shore facility.
2. The method according to claim 1 , wherein the acid gas is natural gas.
3. The method according to claim 1 , wherein the acid gas is biogas.
4. The method according to claim 1 , wherein the acid gas is associated gas.
5. The method according to claim 1 , wherein the monolithic metal oxide catalyst comprises a metal oxide and a support, wherein the metal of the metal oxide in the catalyst is selected from the group consisting of V, Cr, W, Ce, Mo, Nb, Fe, Si, Ti, Al, Ca and Mg, and wherein the support is selected from the group consisting of Al 2 O 3 , SiO 2 , and TiO 2 .
6. The method according to claim 1 , wherein the heating of the permeate stream is accomplished by using a fraction of the acid gas to heat the permeate stream in a separate heater.
7. The method according to claim 1 , wherein the heating of the permeate stream is accomplished by using a steam heater.
8. The method according to claim 1 , wherein the permeate pre-heating stream is heated to a temperature is within the temperature range 180-400° C.
9. The method according to claim 8 , wherein the permeate stream is heated to a temperature within the temperature range 220-350° C.