Exhaust treatment and filtration system for molten carbonate fuel cells
원문보기
IPC분류정보
국가/구분
United States(US) Patent
등록
국제특허분류(IPC7판)
H01M-008/14
H01M-008/00
H01M-002/00
B01D-039/00
출원번호
US-0025662
(2001-12-19)
발명자
/ 주소
Huang, Yinyan
Mackenzie, Scott
Bar-Ilan, Amiram
출원인 / 주소
Sud-Chemie Inc.
인용정보
피인용 횟수 :
3인용 특허 :
23
초록▼
A filter system for adsorbing contaminants from an exhaust stream from a molten carbonate fuel cell including a filter substrate, a high surface area inorganic adsorbent secured to the filter substrate by an inorganic binder and an inorganic acid secured to the filter substrate. Also disclosed is a
A filter system for adsorbing contaminants from an exhaust stream from a molten carbonate fuel cell including a filter substrate, a high surface area inorganic adsorbent secured to the filter substrate by an inorganic binder and an inorganic acid secured to the filter substrate. Also disclosed is a process for preparing the filter system for filtering exhaust gas from the molten carbonate fuel cell and a process for using the filtering system in a molten carbonate fuel cell system.
대표청구항▼
1. A filter system for adsorbing contaminants from a molten carbonate fuel cell exhaust stream comprisinga filter substrate coated with a material, wherein the material comprises an inorganic adsorbent secured to the filter substrate by an inorganic binder, and an acidic material coated onto the fil
1. A filter system for adsorbing contaminants from a molten carbonate fuel cell exhaust stream comprisinga filter substrate coated with a material, wherein the material comprises an inorganic adsorbent secured to the filter substrate by an inorganic binder, and an acidic material coated onto the filter substrate, wherein the acidic material comprises a non-water soluble inorganic acid. 2. The filter system of claim 1 wherein the composition of the filter substrate is selected from a group of materials consisting of ceramic, alumina, titania, zirconia, boria, corundum, silica, magnesia, silica-zirconia, titania-zirconia, titania-silica, silica-alumina, silicon carbides, cordierite, mullite, and metallic filters, such as stainless steel, iron chromium alloy and other metallic alloy filters and mixtures and combinations thereof.3. The filter system of claim 1 wherein the filter substrate comprises a metallic filter.4. The filter system of claim 1 wherein the inorganic adsorbent is selected from the group consisting of alumina, silica, titania, titania-silica, silica-alumina, zirconia silica-zirconia, ceria, and zeolites, either modified or unmodified.5. The filter system of claim 1 wherein the inorganic adsorbent comprises a high surface area material selected from the group consisting of alumina, silica, titania, zirconia, ceria, titania-silica, silica-alumina, silica-zirconia and zeolites.6. The filter system of claim 1 wherein the inorganic adsorbent comprises a high surface area alumina with a surface area greater than about 100 m2/g.7. The filter system of claim 1 wherein the inorganic binder for binding the inorganic adsorbent to the filter substrate is selected from the group consisting of sols of alumina, silica, zirconia, ceria, titania, boehmite and aluminum nitrate, and blends of two or more different binders.8. The filter system of claim 1 wherein the filter substrate comprises a stainless steel screen and the inorganic binder comprises ceria.9. The filter system of claim 1 wherein the acidic material comprises a non-water soluble inorganic acid.10. A filter system for adsorbing contaminants from a molten carbonate fuel cell exhaust stream comprisinga filter substrate coated with a material, wherein the material comprises an inorganic adsorbent secured to the filter substrate by an inorganic binder, and an acidic material coated onto the filter substrate, wherein the acidic material comprises heteropolyphosphoric acid. 11. The filter system of claim 1 wherein the inorganic adsorbent comprises about 60 to about 95 percent, the inorganic binder comprises about 5 to about 40 percent and the acidic material comprises about 0.1 to about 20 percent of the material coated on the filter substrate.12. The filter system of claim 1 wherein the inorganic adsorbent comprises about 80 to about 95 percent, the binder comprises about 1 to about 20 percent and the acidic material comprises about 0.1 to about 5 percent of the material coated on the filter substrate.13. A filter system for adsorbing contaminants from an exhaust system from a molten carbonate fuel cell prior to passage of the exhaust stream through an oxidation catalyst comprisinga filter substrate, a high surface area inorganic adsorbent secured to the filter substrate by an inorganic binder, and an inorganic acidic material coated onto the filter substrate, wherein the inorganic acidic material comprises a non-water soluble inorganic acid. 14. A process for filtering contaminants which are present in an exhaust stream of a molten carbonate fuel cell comprisingpassing a fuel stream through the molten carbonate fuel cell, passing at least a portion of an exhaust stream containing inorganic contaminants through a filter system, and filtering the inorganic contaminants from the exhaust stream by use of the filter system, wherein the filter system comprises a filter substrate, an inorganic adsorbent secured to the filter substrate by an inorganic binder and an acidic material coated onto the filter substrate. 15. The process of claim 14 further comprising passing at least a portion of the filtered exhaust stream after passage through the filter system through an oxidation catalyst system.16. An exhaust treatment system for adsorbing contaminants from a molten carbonate fuel cell comprising the filter system of claim 1 and an oxidation catalyst.17. An exhaust treatment system for adsorbing contaminants from a molten carbonate fuel cell comprising the filter system of claim 13 and an oxidation catalyst.18. A process for filtering contaminants which are present in an exhaust stream of a molten carbonate fuel cell comprisingpassing a fuel stream through the molten carbonate fuel cell which generates an exhaust stream containing inorganic contaminants, passing at least a portion of the exhaust stream containing inorganic contaminants through a filter system, filtering the inorganic contaminants from the exhaust stream by use of the filter system, wherein the filter system comprises a filter substrate, an inorganic adsorbent secured to the filter substrate by an inorganic binder and an acidic material coated onto the filter substrate and passing the filtered exhaust stream through an oxidation catalyst. 19. A process for preparing an exhaust treatment system for filtering exhaust gases from a molten carbonate fuel cell comprisingpreparing a filter system comprising a filter substrate coated with a material, wherein the material comprises an inorganic adsorbent secured to the filter substrate by an inorganic binder, and an acidic material coated onto the filter substrate, wherein the acidic material comprises an inorganic acid, preparing an oxidation catalyst for fuel cells, and placing the filter system and the oxidation catalyst on-line to filter the exhaust gases from the molten carbonate fuel cell. 20. A filter system for adsorbing contaminants from a molten carbonate fuel cell exhaust stream consisting essentially ofa filter substrate coated with a material, wherein the material comprises an inorganic adsorbent secured to the filter substrate by an inorganic binder, and an acidic material coated onto the filter substrate. 21. The process of claim 14 wherein the composition of the filter substrate is selected from a group of materials consisting of ceramic, alumina, titania, zirconia, boria, corundum, silica, magnesia, silica-zirconia, titania-zirconia, titania-silica, silica-alumina, silicon carbides, cordierite, mullite, and metallic filters, such as stainless steel, iron chromium alloy and other metallic alloy filters and mixtures and combinations thereof.22. The process of claim 14 wherein the filter substrate comprises a metallic filter.23. The process of claim 14 wherein the inorganic adsorbent is selected from the group consisting of alumina, silica, titania, titania-silica, silica-alumina, zirconia silica-zirconia, ceria, and zeolites, either modified or unmodified.24. The process of claim 14 wherein the inorganic adsorbent comprises a high surface area material selected from the group consisting of alumina, silica, titania, zirconia, ceria, titania-silica, silica-alumina, silica-zirconia and zeolites.25. The process of claim 14 wherein the inorganic adsorbent comprises a high surface area alumina with a surface area greater than about 100 m2/g.26. The process of claim 14 wherein the inorganic binder for binding the inorganic adsorbent to the filter substrate is selected from the group consisting of sols of alumina, silica, zirconia, ceria, titania, boehmite and aluminum nitrate and blends of two or more different binders.27. The process of claim 14 wherein the filter substrate comprises a stainless steel screen and the inorganic binder comprises ceria.
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