Process and device for converting hydrogen sulfide into hydrogen gas and sulfur

1. A process for producing hydrogen from an input gas stream primarily comprising hydrogen sulfide, said process comprising:

a. passing the input gas stream into an optionally positively charged electrically conductive reactor chamber, wherein the reactor chamber has an outer wall defining an interior chamber, said interior chamber including a heating zone, a hydrogen-permeable inorganic, organic, or composite membrane with an optionally negatively charged conductor and a sulfur condenser, said reactor comprising:

i. an inlet for introducing the input gas stream into the reactor chamber;

ii. a heating element disposed inside the reactor chamber, such heating element creating a heating zone to heat said input gas stream;

iii. said membrane being positioned at the entrance to a first outlet from the reactor chamber and permeable to hydrogen but impermeable to hydrogen sulfide, sulfur vapor, and other gases that may be contained in the input gas stream, such membrane having a first side facing the first outlet and a second side facing the interior chamber;

iv. said membrane comprising a negatively charged material located at a flow passageway; and

v. an inner surface of the outer wall serving as a sulfur condenser inside the interior chamber, such inner surface directing condensed sulfur towards and into a second outlet;

b. reacting the hydrogen sulfide in the heating zone surrounding the heating element at temperature between about 100° Celsius and about 700° Celsius wherein a conversion of hydrogen sulfide to hydrogen gas and sulfur vapor is at least about 95%;

c. continuously and immediately removing the hydrogen gas through the membrane and withdrawing the hydrogen from the first outlet; and

d. continuously condensing the sulfur vapor on the inner surface of the outer wall and removing the sulfur through the second outlet.

2. The process of claim 1 , wherein the reactor chamber includes one or more reactor chambers in series.

3. The process of claim 1 , wherein the reactor chamber is operated at a pressure ranging from sub-atmospheric pressure up to 3,000 psi (20,684 kPa).

4. The process of claim 1 , wherein the membrane is a hydrogen-permeable organic polymer membrane wherein the membrane's second side is maintained at a pressure lower than the pressure on the membrane's first side.

5. The process of claim 4 , wherein the membrane is a hydrogen-permeable inorganic membrane.

6. The process of claim 4 , wherein the membrane is hydrogen-permeable and consists of both organic and inorganic components.

7. The process of claim 1 , comprising two or more membranes.

8. The process of claim 1 , wherein the negatively charged conductor is an electrically conductive thermocouple or an electrical conductor of other composition located within the low pressure second side of the hydrogen permeable membrane.

9. The process of claim 1 , wherein the reactor chamber is positively charged.

10. The process of claim 1 , wherein the conversion of hydrogen sulfide comprises at least about 99%.

11. The process of claim 1 , wherein the reactor contains effluent gas comprising less than about 10,000 ppm hydrogen sulfide.

12. The process of claim 1 , further comprising wherein the heating element is located adjacent to the membrane.

13. The process of claim 1 , further comprising wherein a magnetron or other electromagnetic field generator for heating the hydrogen sulfide gas is located in the heating zone adjacent to membrane or membranes.

14. The process of claim 1 , wherein the inner surface of the outer wall, or further comprising one or more heat exchange condensers collect sulfur vapor for removal from the reactor.

15. The process of claim 1 , wherein the inner surface of the outer wall or one or more sulfur condensers are positively charged.

16. The process of claim 1 , wherein each of the inner surface of the outer wall and the one or more sulfur condensers are positively charged.