Unconditioned syngas composition and method of cleaning up same for fischer-tropsch processing

1. A method of producing Fischer-Tropsch products, comprising:

(a) providing an unconditioned syngas;

(b) after step (a), hydrocarbon reforming the unconditioned syngas with an oxidant source to generate additional hydrogen and carbon monoxide and produce a syngas of improved quality, wherein the oxidant source includes one or more selected from the group consisting of carbon dioxide, steam, air, and oxygen;

(c) after step (b), cooling the syngas of improved quality;

(d) after step (c), removing at least a portion of the steam from the syngas of improved quality;

(e) after step (d), compressing the syngas of improved quality;

(f) after step (e), removing from the syngas of improved quality, one or more volatile organic compounds from the group consisting of benzene, toluene, phenol, styrene, xylene, and cresol;

(g) after step (f), removing ammonia from the syngas of improved quality, thereby producing an ammonia-depleted syngas of improved quality;

(h) after step (g), removing carbon dioxide from the ammonia-depleted syngas of improved quality, thereby forming an ammonia-and-carbon-dioxide-depleted syngas of improved quality; and

(i) after step (h), introducing the ammonia-and-carbon-dioxide-depleted syngas of improved quality to a Fischer-Tropsch (FT) catalytic synthesis process and generating Fischer-Tropsch products including at least a Medium Fraction Fischer-Tropsch Liquid (MFFTL) and wax.

2. The method according to claim 1 , further comprising:

hydrocarbon reforming by partial oxidation and/or

hydrocarbon reforming by using a catalyst.

3. The method according to claim 1 , comprising:

(b1) in step (b) and before step (c), mixing the unconditioned syngas with a gaseous hydrocarbon and an oxidant; and

(b2) reacting the unconditioned syngas with said gaseous hydrocarbon and said oxidant to generate said additional hydrogen and carbon monoxide;

wherein:

said gaseous hydrocarbons are converted into said additional hydrogen and carbon monoxide at a conversion efficiency between 50% and 100%;

the gaseous hydrocarbon includes one or more selected from the group consisting of natural gas, syngas, refinery offgases, methanol, ethanol, petroleum, methane, ethane, propane, butane, hexane, benzene, toluene, xylene, wax, low melting solids, paraffin wax, and naphthalene;

the oxidant includes one or more selected from the group consisting of carbon dioxide, steam, air, and oxygen.

4. The method according to claim 3 , further comprising:

cooling the syngas of improved quality in a shell and tube heat exchanger, wherein the syngas of improved quality travels through the tube-side and indirectly contacts steam located on the shell-side.

5. The method according to claim 1 , further comprising:

in step (c), cooling the syngas of improved quality to between 250 degrees Fahrenheit and 650 degrees Fahrenheit.

6. The method according to claim 1 , further comprising:

in step (c), cooling the syngas of improved quality and generating superheated steam by using a heat recovery steam generator superheater (HRSG superheater) configured to receive steam from a steam drum;

further cooling the syngas of improved quality and generating steam using a heat recovery steam generator (HRSG) configured to receive water from the steam drum; and

transferring the steam generated by the HRSG back to the steam drum.

7. The method according to claim 1 , further comprising:

after step (c) and before step (d), generating superheated steam from steam, by cooling at least a portion of the said additional hydrogen and carbon monoxide generated by said hydrocarbon reforming.

8. The method according to claim 1 , further comprising:

in step (d), removing said steam from at least a portion of the syngas of improved quality by condensing said steam within a scrubber.

9. The method according to claim 1 , further comprising:

in step (e), compressing the syngas of improved quality with a compressor from a first pressure ranging from 15 PSIG to 50 PSIG to a second higher pressure ranging from 100 PSIG to 2,000 PSIG.

10. The method according to claim 1 , further comprising:

in step (f), removing said VOCs with an adsorbent.

11. The method according to claim 10 , further comprising:

desorbing said adsorbent via pressure swing desorption and/or temperature swing desorption.

12. The method according to claim 1 , further comprising:

in step (f), removing said VOCs with an adsorbent including one or more selected from the group consisting of styrene based polymeric adsorbents, molecular sieves, zeolites, catalyst materials, silica gel, alumina, and activated carbon materials.

13. The method according to claim 1 , further comprising:

in step (f), removing said VOCs with a capture efficiency greater than 95%.

14. The method according to claim 1 , further comprising:

in step (g), removing ammonia from the syngas of improved quality by use of a scrubber.

15. The method according to claim 1 , further comprising:

in step (h), removing carbon dioxide from the ammonia-depleted syngas of improved quality with one or more selected from the group consisting of a membrane, an adsorber, and an absorber;

wherein the carbon dioxide capture efficiency of step (h) is greater than 20%.

16. The method according to claim 1 , wherein the unconditioned syngas has a component composition comprising:

(a) a carbon monoxide concentration ranging from between 5 volume percent to 35 volume percent on a dry basis;

(b) a hydrogen concentration ranging from between 20 volume percent to 60 volume percent on a dry basis;

(c) one or more volatile organic compounds (VOC) selected from the group consisting of benzene, toluene, phenol, styrene, xylene, cresol, and combinations thereof, the VOC concentration ranges from between 500 parts per million by volume to 10,000 parts per million by volume on a dry basis;

(d) one or more semi-volatile organic compounds (SVOC) selected from the group consisting of indene, indan, napthalene, methylnapthalene, acenapthylene, acenapthalene, anthracene, phenanthrene, (methyl-) anthracenes/phenanthrenes, pyrene/fluoranthene, methylpyrenes/benzofluorenes, chrysene, benz[a]anthracene, methylchrysenes, methylbenz[a]anthracenes, perylene, benzo[a]pyrene, dibenz[a,kl]anthracene, dibenz[a,h]anthracene, and combinations thereof, the SVOC concentration ranges from between 10 parts per million by volume to 1,000 parts per million by volume on a dry basis;

(e) a hydrogen chloride concentration ranging from between greater than 0 parts per million by volume to 1,000 parts per million by volume on a dry basis; and

(f) a hydrogen sulfide concentration ranging from between greater than 0 parts per million by volume to 1,000 parts per million by volume on a dry basis.

17. A method of producing Fischer-Tropsch products, comprising:

(a) providing a source of unconditioned syngas;

(b) after step (a), hydrocarbon reforming the unconditioned syngas with an oxidant source to generate additional hydrogen and carbon monoxide and produce a syngas of improved quality, wherein the oxidant source includes one or more selected from the group consisting of carbon dioxide, steam, air, and oxygen;

(c) after step (b), cooling the syngas of improved quality;

(d) after step (c), removing at least a portion of the steam from the syngas of improved quality;

(e) after step (d), compressing the syngas of improved quality;

(f) after step (e), removing one or more volatile organic compounds from the syngas of improved quality;

(g) after step (f), removing ammonia from the syngas of improved quality, thereby producing an ammonia-depleted syngas of improved quality;

(h) after step (g), removing carbon dioxide from the ammonia-depleted syngas of improved quality, thereby forming an ammonia-and-carbon-dioxide-depleted syngas of improved quality; and

(i) after step (h), introducing the ammonia-and-carbon-dioxide-depleted syngas of improved quality to a Fischer-Tropsch (FT) catalytic synthesis process and generating Fischer-Tropsch products including at least a Medium Fraction Fischer-Tropsch Liquid (MFFTL) and wax;

wherein:

the unconditioned syngas in step (a) includes:

(I) a carbon monoxide concentration ranging from between 5 volume percent to 35 volume percent on a dry basis;

(II) a hydrogen concentration ranging from between 20 volume percent to 60 volume percent on a dry basis;

(III) one or more volatile organic compounds (VOC) selected from the group consisting of benzene, toluene, phenol, styrene, xylene, cresol, and combinations thereof, the VOC concentration ranges from between 500 parts per million by volume to 10,000 parts per million by volume on a dry basis; and

(IV) one or more semi-volatile organic compounds (SVOC) selected from the group consisting of indene, indan, napthalene, methylnapthalene, acenapthylene, acenapthalene, anthracene, phenanthrene, (methyl-) anthracenes/phenanthrenes, pyrene/fluoranthene, methylpyrenes/benzofluorenes, chrysene, benz[a]anthracene, methylchrysenes, methylbenz[a]anthracenes, perylene, benzo[a]pyrene, dibenz[a,kl]anthracene, dibenz[a,h]anthracene, and combinations thereof, the SVOC concentration ranges from between 10 parts per million by volume to 1,000 parts per million by volume on a dry basis.

18. The method according to claim 17 , comprising, in step (f),

removing one or more volatile organic compounds from the syngas of improved quality with an adsorbent, the adsorbent being one or more selected from the group consisting of styrene based polymeric adsorbents, molecular sieves, zeolites, catalyst materials, silica gel, alumina, and activated carbon materials.