초록 ▼

A method for generating hydrogen in a production facility having a catalytic steam reformer, a boiler downstream of the catalytic steam reformer, optionally having a prereformer, and optionally having a shift reactor, wherein the reformer feed gas mixture is formed using a steam-containing recycle g

A method for generating hydrogen in a production facility having a catalytic steam reformer, a boiler downstream of the catalytic steam reformer, optionally having a prereformer, and optionally having a shift reactor, wherein the reformer feed gas mixture is formed using a steam-containing recycle gas mixture which was formed from boiler effluent. The boiler generates steam which may be used to form the reformer feed gas mixture, used elsewhere in the production facility, and/or used for export steam.

대표청구항 ▼

The invention claimed is: 1. A method for generating hydrogen in a production facility comprising: (a) forming a reformer feed gas mixture from a steam-containing gas, a sulfur-depleted reformer feedstock, and a separate steam-containing recycle gas mixture; (b) introducing the reformer feed gas mi

The invention claimed is: 1. A method for generating hydrogen in a production facility comprising: (a) forming a reformer feed gas mixture from a steam-containing gas, a sulfur-depleted reformer feedstock, and a separate steam-containing recycle gas mixture; (b) introducing the reformer feed gas mixture into a plurality of catalyst-containing reformer tubes of a catalytic steam reformer to form a reformed gas mixture comprising hydrogen; (c) combusting a fuel external to the plurality of catalyst-containing reformer tubes to supply energy for reforming the reformer feed gas mixture; (d) passing the reformed gas mixture or a portion of the reformed gas mixture from the plurality of catalyst-containing reformer tubes into a boiler to form a boiler effluent from the reformed gas mixture or the portion of the reformed gas mixture and to generate steam from a liquid water-containing feed; and (e) forming the separate steam-containing recycle gas mixture from a first portion of the boiler effluent, the separate steam-containing recycle gas mixture containing steam from the reformer effluent. 2. The method of claim 1 wherein the steam-containing gas comprises greater than 99 volume % steam. 3. The method of claim 1 wherein the sulfur-depleted reformer feedstock comprises less than 1 volume % steam. 4. The method of claim 1 wherein the separate steam-containing recycle gas mixture comprises greater than 10 volume % steam. 5. The method of claim 1 wherein the separate steam-containing recycle gas mixture comprises between 25 volume % and 95 volume % steam. 6. The method of claim 1 wherein the step of forming the separate steam-containing recycle gas mixture comprises: cooling the first portion of the boiler effluent to form a cooled portion of the boiler effluent; and compressing the cooled portion of the boiler effluent to form a compressed portion of the boiler effluent for forming the separate steam-containing recycle gas mixture. 7. The method of claim 6 wherein the step of forming the separate steam-containing recycle gas mixture further comprises: heating the compressed portion of the boiler effluent for forming the separate steam-containing recycle gas mixture. 8. The method of claim 1 further comprising: passing a second portion of the boiler effluent into at least one heat exchanger to heat at least one of a reformer feedstock and the liquid water-containing feed. 9. The method of claim 8 further comprising: passing the reformer feedstock into a desulfurization unit to form the sulfur-depleted reformer feedstock from the reformer feedstock. 10. The method of claim 1 wherein the step of forming the reformer feed gas mixture comprises: forming a first gas mixture from the separate steam-containing recycle gas mixture and the sulfur-depleted reformer feedstock; and combining the first gas mixture with the steam-containing gas. 11. The method of claim 1 wherein the step of forming the reformer feed gas mixture comprises: forming a steam-enriched recycle gas mixture from the separate steam-containing recycle gas mixture and the steam-containing gas; and combining the steam-enriched recycle gas mixture with the sulfur-depleted reformer feedstock. 12. The method of claim 11 wherein the step of forming a steam-enriched recycle gas mixture comprises: combining the separate steam-containing recycle gas mixture and the steam-containing gas in a compressor ejector. 13. The method of claim 1 wherein the step of forming the reformer feed gas mixture comprises: forming a sulfur-depleted feedstock mixture from the sulfur-depleted reformer feedstock and the steam-containing gas; and combining the sulfur-depleted feedstock mixture with the separate steam-containing recycle gas mixture. 14. The method of claim 1 wherein the step of forming the reformer feed gas mixture comprises: forming a sulfur-depleted feedstock mixture from the sulfur-depleted reformer feedstock and the steam-containing gas; introducing the sulfur-depleted feedstock mixture into a prereformer to form a prereformed gas mixture; and combining the prereformed gas mixture with the separate steam-containing recycle gas mixture. 15. The method of claim 1 wherein the step of forming the reformer feed gas mixture comprises: forming a steam-enriched recycle gas mixture from the separate steam-containing recycle gas mixture and the steam-containing gas; combining the steam-enriched recycle gas mixture with the sulfur-depleted reformer feedstock to form a sulfur-depleted feedstock mixture containing recycle gas; and introducing the sulfur-depleted feedstock mixture containing recycle gas into a prereformer to prereform the sulfur-depleted feedstock mixture containing recycle gas for forming the reformer feed gas mixture. 16. The method of claim 1 wherein the step of forming the reformer feed gas mixture comprises: forming a sulfur-depleted feedstock mixture from the sulfur-depleted reformer feedstock and the steam-containing gas; combining the sulfur-depleted feedstock mixture with the separate steam-containing recycle gas mixture to form a sulfur-depleted feedstock mixture containing recycle gas; and introducing the sulfur-depleted feedstock mixture containing recycle gas into a prereformer to prereform the sulfur-depleted feedstock mixture containing recycle gas for forming the reformer feed gas mixture. 17. The method of claim 1 wherein the step of forming the reformer feed gas mixture comprises: forming a sulfur-depleted feedstock mixture from the sulfur-depleted reformer feedstock and the steam-containing gas; combining the sulfur-depleted feedstock mixture with the separate steam-containing recycle gas mixture in a compressor ejector to form a sulfur-depleted feedstock mixture containing recycle gas; and introducing the sulfur-depleted feedstock mixture containing recycle gas into a prereformer to prereform the sulfur-depleted feedstock mixture containing recycle gas for forming the reformer feed gas mixture. 18. The method of claim 1 wherein the step of forming the separate steam-containing recycle gas mixture comprises: passing the boiler effluent into a shift reactor to form a shift reactor effluent; and taking a first portion of the shift reactor effluent for forming the separate steam-containing recycle gas mixture. 19. The method of claim 18 wherein the step of forming the separate steam-containing recycle gas mixture further comprises: cooling the first portion of the shift reactor effluent to form a cooled portion of the shift reactor effluent; and compressing the cooled portion of the shift reactor effluent for forming the separate steam-containing recycle gas mixture. 20. The method of claim 18 further comprising: passing a second portion of the shift reactor effluent into at least one heat exchanger to heat at least one of a reformer feedstock and the liquid water-containing feed. 21. The method of claim 1 wherein the step of forming the separate steam-containing recycle gas mixture comprises: passing the boiler effluent into at least one heat exchanger to form a heat exchanger effluent and to heat at least one of a reformer feedstock and the liquid water-containing feed; and taking a portion of the heat exchanger effluent for forming the separate steam-containing recycle gas mixture. 22. The method of claim 21 wherein the step of forming the separate steam-containing recycle gas mixture further comprises: cooling the portion of the heat exchanger effluent to form a cooled portion of the heat exchanger effluent; and compressing the cooled portion of the heat exchanger effluent for forming the separate steam-containing recycle gas mixture. 23. The method of claim 1 wherein the step of forming the separate steam-containing recycle gas mixture comprises: passing the boiler effluent into a shift reactor to form a shift reactor effluent; passing at least a portion of the shift reactor effluent into at least one heat exchanger to form a heat exchanger effluent and to heat at least one of a reformer feedstock and the liquid water-containing feed; and taking a portion of the heat exchanger effluent for forming the separate steam-containing recycle gas mixture. 24. The method of claim 23 wherein the step of forming the separate steam-containing recycle gas mixture further comprises: cooling the portion of the heat exchanger effluent to form a cooled portion of the heat exchanger effluent; and compressing the cooled portion of the heat exchanger effluent for forming the separate steam-containing recycle gas mixture.