초록 ▼

Solar-powered reactor for processing of slightly absorbing and transparent gases. An obvious path to providing storable, renewable energy is through solar dissociation of gas molecules. These dissociation products are the precursors of modern liquid and gaseous fuels such as hydrogen and methanol/et

Solar-powered reactor for processing of slightly absorbing and transparent gases. An obvious path to providing storable, renewable energy is through solar dissociation of gas molecules. These dissociation products are the precursors of modern liquid and gaseous fuels such as hydrogen and methanol/ethanol. An apparatus and method using a solar concentrator (such as a focusing trough or dish) directed at the receiving end of a reactor are disclosed. A range of designs of reactors for the dissociation of gases, both those that absorb slightly in the visible spectrum and those that are transparent in the visible and only absorb in the infrared, is described. For slightly-absorbing gases, a funnel-shaped reactor that preheats the gas and concentrates sunlight is the indicated embodiment. A system for dissociating CO2 using the invention is described. For transparent gases, a holraum embodiment is more appropriate for coupling solar energy into the gas. In both cases, heat from the hot stream of dissociated gas may also be used to produce electricity with a standard steam or Stirling cycle generator.

대표청구항 ▼

What is claimed is: 1. A method for solar powered processing of a slightly-absorbing or transparent gas, comprising the steps of: passing the process gas through a reaction zone; concentrating incoming solar radiation in the reaction zone to drive an endothermic dissociation reaction in the process

What is claimed is: 1. A method for solar powered processing of a slightly-absorbing or transparent gas, comprising the steps of: passing the process gas through a reaction zone; concentrating incoming solar radiation in the reaction zone to drive an endothermic dissociation reaction in the process gas; and quenching undesirable back reactions by rapidly cooling the process gas immediately downstream from the reaction zone, the quenching step further comprising contacting the process gas with a cooling surface. 2. The method of claim 1 wherein the step of quenching undesirable back reactions comprises quenching the reactions: CO+O+ M→CO2+M and CO+O2→CO2+O. 3. The method of claim 1 comprising the additional step of gathering heat from a reactor structure to suppress re-radiation and to drive a heat engine. 4. The method of claim 3 wherein the step of gathering comprises gathering heat from the cooling surface. 5. The method of claim 1 wherein the process gas is CO2 and the step of rapidly cooling comprises dropping the process gas temperature to a quench temperature of less than approximately 800 C. 6. A method for solar powered processing of a gas that absorbs only infrared light, the method comprising: directing solar energy, in the form of light rays, through an intake aperture into a holraum reactor chamber; pumping the gas into the holraum reactor chamber; allowing the light rays to repeatedly strike interior walls of the holraum reactor chamber; heating the process gas by infrared radiation from the interior walls to drive an endothermic dissociation reaction in the gas; and quenching undesirable back reactions by rapidly cooling the gas immediately downstream from the chamber, the quenching step further comprising contacting the gas with a cooling surface. 7. The method of claim 1 wherein the step of concentrating incoming solar radiation in the reaction zone comprises: admitting solar energy into the mouth of a highly reflective funnel while providing the funnel with a longitudinal centerline axis and a wall having an optically smooth inner surface; and defining with the funnel a radial cross-sectional area, wherein the cross-sectional area monotonically decreases along the axis from the mouth toward said reaction zone. 8. The method of claim 7 wherein the step of providing the funnel with a wall comprises defining with the wall a cone of revolution around the axis. 9. The method of claim 7 wherein the step of providing the funnel with a wall comprises defining with the wall a paraboloid of revolution around the axis. 10. The method of claim 7 further comprising preheating the process gas, the preheating step comprising the steps of: directing sunlight energy to the centerline axis; disposing a ceramic rod on the axis and extending at least partially into the reaction zone; and heating the ceramic rod with sunlight energy. 11. The method of claim 10 further comprising contact heating the process gas with the ceramic rod to induce molecular dissociation of the gas along and in the immediate vicinity of the rod. 12. The method of claim 1 wherein the step of passing the process gas through a reaction zone comprises: providing a holraum reactor chamber with black interior walls and an intake aperture; and pumping the process gas into the reactor chamber through the intake aperture in the chamber. 13. The method of claim 12 wherein the step of concentrating incoming solar radiation in the reaction zone comprises the step of focusing a beam of sunlight into the intake aperture. 14. The method of claim 12 wherein the step of providing a holraum reactor comprises providing a ratio of the area of the intake aperture to the area of the interior walls of less than approximately 0.5. 15. The method of claim 14 wherein the step of concentrating incoming solar radiation further comprises the steps of: attaching a reflective cone to a front of the aperture to reduce the cross sectional area of the beam of sunlight; and generally corresponding the cross sectional area of the beam to the area of the intake aperture. 16. The method of claim 13 further comprising the step of heating the process gas by infrared radiation from the interior walls. 17. The method of claim 1 wherein contacting the process gas with a cooling surface comprises the steps of defining a process gas flow area and defining a cooling surface area, wherein the ratio of the cooling surface area to the gas flow area is at least 5.0. 18. The method of claim 1 wherein the step of passing the process gas through a reaction zone comprises the steps of: passing the process gas through an array of a plurality of small fore-funnels to supply increased contact area for heating the gas; and fashioning from high-temperature ceramic a throat end portion of each of the fore-funnels. 19. The method of claim 18 wherein the step of concentrating incoming solar radiation in the reaction zone comprises intensifying solar energy near the throat end portion of each fore-funnel to create hot walls in each fore-funnel for heating and dissociating the passing gas. 20. The method of claim 19 wherein contacting the process gas with a cooling surface comprises flowing the gas through a cooling channel corresponding to and leading from each fore-funnel. 21. The method of claim 6 further comprising the step of providing a ratio of the area of the intake aperture to the area of the interior walls of less than approximately 0.5.