OPTIMIZED NATURAL GAS/SALES GAS/SOUR GAS REFORMING EMPLOYING A NOVEL CATALYTIC PROCESS AT THE INDUSTRIAL SCALE
A system for hydrogen production including a first separation system, a first purification unit, a second purification unit, an oxygen scavenger, a catalytic reactor, a second separation system, and a liquefier. A method for hydrogen production including separating oxygen-containing components from a feed also containing hydrogen sulfide and methane. The method further includes separating the hydrogen sulfide from the methane and feeding the hydrogen sulfide to a first purification unit. The method includes feeding the methane to a second purification unit. The method further includes feeding the purified hydrogen sulfide and methane to an oxygen scavenger unit to remove residual oxygen before reacting the two streams in a catalytic reactor. The method includes separating the gaseous hydrogen and liquid carbon disulfide exiting the catalytic reactor and then purifying and liquefying the gaseous hydrogen stream to produce a purified liquid hydrogen stream.
1 . A system for hydrogen production, comprising:
a first separation system configured to remove a plurality of oxygen-containing components from a natural gas feed stream, and produce a hydrogen sulfide containing stream and a methane containing stream;
a first purification unit configured to receive the hydrogen sulfide containing stream and produce a purified hydrogen sulfide stream;
a second purification unit configured to receive the methane containing stream and produce a purified methane stream;
an oxygen scavenger unit configured to treat the purified hydrogen sulfide stream and the purified methane stream;
a catalytic reactor configured to react the purified hydrogen sulfide stream and the purified methane stream in the absence of oxygen, producing an effluent containing hydrogen and carbon disulfide;
a second separation system configured to separate the effluent into a gaseous hydrogen stream and a liquid carbon disulfide stream; and
a liquefier configured to transition the gaseous hydrogen stream to a liquid hydrogen stream.
2 . The system of claim 1 , wherein the first separation system is selected from the group consisting of a catalyst, a membrane, or a combination thereof.
3 . The system of claim 1 , wherein the first purification unit and the second purification are combined into a single purification unit.
4 . The system of claim 1 , wherein the first purification unit and the second purification unit are separate units.
5 . The system of claim 1 , wherein the oxygen scavenger unit is a stripping packed apparatus.
6 . The system of claim 1 , wherein the catalytic reactor contains a heterogeneous site-isolated catalyst in an inorganic-organic hybrid structure.
7 . The system of claim 1 , wherein the heterogeneous site-isolated catalyst further comprises a crosslinked organic shell and site-isolated catalyst in the core.
8 . The system of claim 1 , wherein the reactor is a glass-lined reactor.
9 . The system of claim 1 , wherein the second separation system is a decanter.
10 . A method for hydrogen production, comprising:
separating a plurality of oxygen-containing components from a feed mixture containing the plurality of oxygen containing components, hydrogen sulfide, and methane;
separating the hydrogen sulfide from the methane;
feeding the hydrogen sulfide to a first purification unit, producing a purified hydrogen sulfide stream;
feeding the methane to a second purification unit, producing a purified methane stream;
removing an amount of residual oxygen containing components from the hydrogen sulfide stream and the methane stream using an oxygen scavenger unit;
reacting the hydrogen sulfide stream and the methane stream in a catalytic reactor, producing an effluent containing a mixture of gaseous hydrogen and liquid carbon disulfide;
separating the mixture of gaseous hydrogen and liquid carbon disulfide to form a gaseous hydrogen stream and a liquid carbon disulfide stream; and
purifying and liquefying the gaseous hydrogen stream producing a purified liquid hydrogen stream.
11 . The method of claim 10 , wherein a molar ratio of the hydrogen sulfide stream to methane stream fed to the catalytic reactor is from 5:1 to 1:5.
12 . The method of claim 10 , wherein the hydrogen sulfide stream and the methane stream contain less than 1 ppm of oxygen.
13 . The method of claim 10 , wherein the reacting of the hydrogen sulfide stream and the methane stream occurs between 600 and 1200° C.
14 . The method of claim 10 , wherein the effluent containing a mixture of gaseous hydrogen and liquid carbon disulfide contains less than 4 ppm hydrogen sulfide.
15 . The method of claim 10 , wherein the purified liquid hydrogen stream comprises less than 4 ppm hydrogen sulfide.
16 . The method of claim 10 , further comprising feeding the liquid carbon disulfide stream to a process for the production of an additive, a pharmaceutical, a polymer, a pesticide, a fungicide, or a solvent.