Direct water vaporization for fuel processor startup and transients
View Patent ↗A fuel cell system including a fuel reforming processor having a catalyst therein constructed and arranged to produce a reformate stream including hydrogen and carbon monoxide, a water gas shift reactor downstream of the fuel reforming processor and wherein the water gas shift reactor includes a catalyst therein constructed and arranged to reduce the amount of carbon monoxide in the reformate stream, a preferential oxidation reactor downstream of the water gas shift reactor and wherein the preferential oxidation reactor includes a catalyst therein constructed and arranged to preferentially oxidize carbon monoxide into carbon dioxide and to produce a hydrogen-rich stream, and a fuel cell stack downstream of the preferential oxidation reactor constructed and arranged to produce electricity from the hydrogen-rich stream, a first direct water vaporizing combustor constructed and arranged to combust fuel producing a high-temperature fuel combustion byproducts exhaust and to produce steam from water sprayed into the combustion byproduct exhaust and wherein the first direct water vaporizing combustor is plumbed to the fuel reforming reactor to charge steam therein, and a second direct water vaporizing combustor constructed and arranged to combust fuel to produce a high-temperature fuel combustion byproduct exhaust and to produce steam from water sprayed into the fuel combustion byproduct exhaust and wherein the second direct water vaporizing combustor is plumbed to the water gas shift reactor to charge steam therein.
1. A process comprising:
starting up a fuel cell comprising instantaneously vaporizing sprayed water to produce steam; and
charging the steam into a fuel reforming reactor having a catalyst therein having a light off temperature substantially above ambient temperature, and wherein the charging of the steam into the fuel reforming reactor is continued until the temperature of the fuel reforming reactor catalyst is above the light off temperature, and only when the catalyst is above the light off temperature then delivering fuel to the fuel reforming reactor.
2. A process as set forth in claim 1 wherein the fuel reforming reactor is an autothermal reforming reactor.
3. A process as set forth in claim 1 wherein the vaporizing of sprayed water comprises burning a combustible fuel in the presence of oxygen to produce a flame and a high-temperature exhaust and spraying water into the high-temperature exhaust to produce the steam.
4. A process comprising:
starting up a fuel cell comprising instantaneously vaporizing sprayed water to produce steam; and
charging the steam into a reformate purification component having a catalyst therein having a light off temperature substantially above ambient temperature, to heat the catalyst above the light off temperature and only when the catalyst is above the light off temperature then delivering a reformate stream to the reformate purification component.
5. A process as set forth in claim 4 wherein the reformate purification component includes a water gas shift reactor.
6. A process as set forth in claim 4 wherein the vaporizing of sprayed water comprises injecting fuel and air into a combustor to provide a combustible mixture and igniting the combustible mixture to produce a flame and a combustor high-temperature exhaust, and spraying water into the combustor high-temperature exhaust to vaporize the water and produce the steam.
7. A process comprising instantaneously vaporizing sprayed water to produce steam;
charging the steam to a fuel reforming reactor having a first catalyst therein having a first light off temperature substantially above ambient temperature, wherein the charging of the steam into the fuel reforming reactor is continued until the temperature of the fuel reforming reactor catalyst is above the first light off temperature;
charging the steam into a water gas shift reactor having a second catalyst therein having a second light off temperature substantially above ambient temperature, and wherein the charging of the steam into the water gas shift reactor is continued until the temperature of the second catalyst is above the second light off temperature, and only when the first catalyst is above the first light off temperature and the second catalyst is above the second light off temperature then delivering fuel to the fuel reforming reactor.