초록 ▼

Synthesis gas is produced though a cyclic method where the first step of the cycle includes reforming a hydrocarbon feed over a catalyst to synthesis gas in a first zone of a bed and the second step reheats this first zone. A hydrocarbon feed is introduced to a bed along with CO2 and optionally stea

Synthesis gas is produced though a cyclic method where the first step of the cycle includes reforming a hydrocarbon feed over a catalyst to synthesis gas in a first zone of a bed and the second step reheats this first zone. A hydrocarbon feed is introduced to a bed along with CO2 and optionally steam where it is reformed into synthesis gas. The synthesis gas is collected at a second zone of the bed and an oxygen-containing gas is then introduced to this second zone of the bed and combusted with a fuel, thereby reheating the first zone to sufficient reforming temperatures. Additionally, a non-combusting gas can also be introduced to the second zone to move heat from the second zone to the first zone.

대표청구항 ▼

What is claimed is: 1. A cyclic reforming and re-heating process comprising: (a) reforming a hydrocarbon by introducing at least a portion of said hydrocarbon along with steam and optionally CO2, through a first end of a first zone having a first volume containing bed packing materials and catalyst

What is claimed is: 1. A cyclic reforming and re-heating process comprising: (a) reforming a hydrocarbon by introducing at least a portion of said hydrocarbon along with steam and optionally CO2, through a first end of a first zone having a first volume containing bed packing materials and catalyst to produce a synthesis gas product; (b) passing at least a portion of the product of step (a) to a second zone having a second volume containing bed packing materials, and transferring sensible heat from the product to the packing materials; (c) removing substantially all of the product from said second zone; (d) introducing an oxygen-containing gas into a first end of said second zone; and (e) contacting said oxygen-containing gas with a fuel and combusting said gas and fuel within said zones, thereby re-heating said first zone to reforming temperatures and creating a fluegas which exits through the first end of said first zone, where each of steps (a) and (b) are done at a space velocity C1GHSV of at least 500 hr-1 as calculated using a combined volume of the first and second zones. 2. The process of claim 1, wherein the combustion of said fuel with said oxygen-containing gas occurs at or substantially at an interface between said first and second zones. 3. The process of claim 1, wherein a non-combusting gas is introduced into the first end of said second zone either directly before step (d) or directly after step (e) and flows across said second zone, thereby transferring heat from said second zone to said first zone. 4. The process of claim 1 or 2, wherein the reforming of a hydrocarbon is carried out at a higher pressure than regenerating the heat of said first zone. 5. The process of claim 4, wherein the process has a characteristic ΔTHT in the range of from about 0.1�� C. to about 500�� C. 6. The process of claim 1, wherein the catalyst is selected from the group consisting of noble metal components, Group VIII metal components, Ag, Ce, Cu, La, Mo, Mg, Sn, Ti, Y, and Zn. 7. The process of claim 1, wherein the packing materials of said first zone or said second zone or both are composed of a material selected from the group consisting of magnesium aluminum silicates, aluminum silicate clays, mullite, alumina, silica-alumina, zirconia, and mixtures thereof. 8. The process of claim 1, wherein the inlet temperature of the hydrocarbon, steam and optional CO2 feed is in the range of about 20�� C. to 600�� C. 9. The process of claim 1, wherein the reforming temperature is in the range of about 700�� C. to 2000�� C. 10. The process of claim 1, wherein the inlet temperature of the oxygen-containing gas is in the range of about 20�� C. to 600�� C. 11. The process of claim 1, wherein the hydrocarbon, steam and optional CO2 feed is heat exchanged with reforming products. 12. The process of claim 1, wherein the oxygen-containing gas is heat exchanged against the exiting fluegas. 13. The process of claim 1, including: measuring the temperature at or substantially at the interface between said first and second zones and, upon reaching a pre-determined first temperature, the oxygen-containing gas is introduced to said second zone; and measuring the temperature at or substantially at the first end of said first zone and, upon reaching a pre-determined second temperature, the hydrocarbon, steam and optional CO2 feed is introduced to said first end of said first zone. 14. The process of claim 1, including: measuring the composition of the reforming product in step (c) and, upon reaching a pre-determined composition, the steps (a,b,c) are ended; and measuring the temperature at or substantially at the first end of said first zone and, upon reaching a pre-determined second temperature, the reforming and recovery steps (a,b,c) are begun. 15. The process of claim 1, wherein the second zone does not contain reforming catalyst.