Gas Treatment Unit, Redox System and Method for Desulfurization of Gases Including Biogas

1 . A gas treatment system configured to treat an influent gas stream including hydrocarbon gas and a hydrogen sulfide gas, the system comprising:

a reduction unit configured to contact the influent gas stream with a primary stream including an aqueous metal chelant and release a hydrocarbon gas stream separate from a contacted primary stream including elemental sulfur and a contacted aqueous metal chelant; and

an oxidation unit including at least one oxidation eductor configured to contact an oxidizing gas stream and the contacted primary stream and output an oxidized stream including regenerated aqueous metal chelant.

2 . The system of claim 1 , wherein the reduction unit further comprises:

at least one reduction eductor configured to contact the influent gas stream and the primary stream and output an eductor effluent stream including hydrocarbon gas, the contacted aqueous metal chelant and elemental sulfur; and

a chamber downstream of the at least one reduction eductor, the chamber configured to receive the eductor effluent stream and release the hydrocarbon gas stream separate from the contacted primary stream including elemental sulfur and aqueous metal chelant.

3 . The system of claim 1 , further comprising:

a tank configured to hold the primary stream, receive the hydrocarbon gas stream from the reduction unit and release the hydrocarbon stream from the system.

4 . The system of claim 2 , further comprising:

a pump providing a motive force to the primary stream for operation of the oxidation eductor and reduction eductor.

5 . The system of claim 1 , wherein the aqueous metal chelant further comprises:

metal chelants, ferric salts, ferrous salts, ferric chelants, ferrous chelants, nano-iron, colloidal iron, Fe-MGDA, HEME, organisms containing HEME, or a combination thereof.

6 . The system of claim 1 , further comprising:

a sulfur removal unit configured to separate the elemental sulfur from the primary stream.

7 . The system of claim 1 , wherein the hydrocarbon gas includes methane, CO 2 or any combination thereof.

8 . The system of claim 1 , wherein the hydrocarbon gas is a biogas, a landfill generated gas, industrial waste gas, a petroleum or a gas refining waste gas, or any combination thereof.

9 . The system of claim 1 , further comprising:

a hydrocarbon gas generating unit connected upstream of the reduction unit, the hydrocarbon generator including a biogas generator, an anaerobic digestor, a landfill, a bio generator or any combination thereof.

10 - 14 . (canceled)

15 . The system of claim 1 , further comprising:

a polishing tank downstream of the chamber, the polishing tank including:

a treated gas inlet comprising a downcomer including a slotted end, the slotted end extending into the polishing tank; and

a polished gas outlet through which a polished gas stream is released from the polishing tank.

16 . (canceled)

17 . A method for continually removing hydrogen sulfide from an influent gas stream, the method comprising steps of:

contacting, via a reduction unit, the influent gas stream with a primary stream including an aqueous metal chelant and releasing a hydrocarbon gas stream separate from a contacted primary stream including elemental sulfur and contacted aqueous metal chelant; and

contacting, via an oxidation eductor, an oxidizing gas stream and the contacted primary stream and releasing an oxidized stream including regenerated aqueous metal chelant.

18 . The method of claim 17 , wherein the step of contacting the influent gas stream further comprises steps of:

contacting, via at least one reduction eductor, the influent gas stream and the primary stream and releasing an eductor effluent stream including hydrocarbon gas, contacted aqueous metal chelant and elemental sulfur;

receiving, via a chamber downstream of the at least one reduction eductor, the eductor effluent stream; and

releasing the hydrocarbon gas stream separate from the contacted primary stream including elemental sulfur and aqueous metal chelant.

19 . The method of claim 18 , further comprising a step of:

providing, via a pump, a motive force to the primary stream for operation of the oxidation eductor and the reduction eductor.

20 . The method of claim 17 , wherein the step of contacting the influent gas stream with a primary stream including an aqueous metal chelant further comprises the steps of:

using metal chelants, ferric salts, ferrous salts, ferric chelants, ferrous chelants, nano-iron, colloidal iron, Fe-MGDA, HEME, organisms containing HEME, or any combination thereof.

21 . The method of claim 17 , further comprising a step of:

removing sulfur from the primary stream using a sulfur removal unit.

22 . The method of claim 17 , wherein the influent gas stream includes hydrogen sulfide and methane, CO 2 , or any combination thereof.

23 . The method of claim 17 , wherein the hydrocarbon gas is a biogas, a landfill generated gas, industrial waste gas, a petroleum or a gas refining waste gas, or any combination thereof.

24 . The method of claim 17 , further comprising:

connecting, upstream of the reduction unit, a hydrocarbon generator including a biogas generator, an anaerobic digestor, a landfill, a bio generator or any combination thereof.

25 . The method of claim 17 , wherein the primary stream includes a metal chelant, metal chelants, ferric salts, ferrous salts, ferric chelants, ferrous chelants, nano-iron, colloidal iron Fe-MGDA, HEME, organisms containing HEME, or any combination thereof.