Fuel cell device
US-9225047-B2 · Dec 29, 2015 · US
US9917317B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9917317-B2 |
| Application number | US-201314405154-A |
| Country | US |
| Kind code | B2 |
| Filing date | Mar 28, 2013 |
| Priority date | Jun 4, 2012 |
| Publication date | Mar 13, 2018 |
| Grant date | Mar 13, 2018 |
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The present invention relates to a combined fuel cell and boiler system, and comprising: a fuel cell portion for receiving supplied outside air and raw material gas and generating electricity through a catalyst reaction; and a boiler portion comprising a latent heat exchanger, which is connected to an exhaust gas pipe of the fuel cell portion, for collecting the latent heat of self-generated exhaust gas with the latent heat of exhaust gas from the fuel cell portion. The present invention can effectively increase the efficiency of a boiler by supplying the exhaust gas from the fuel cell to the latent heat exchanger in the boiler, so as to be heat-exchanged in the latent heat exchanger with the exhaust gas from the boiler and then discharged, and can simplify the composition by unifying exhaust gas pipes.
Opening claim text (preview).
The invention claimed is: 1. A combined fuel cell and boiler system, comprising: a fuel cell portion configured for receiving outside air and raw material gas and generating electricity through a catalytic reaction, the fuel cell portion comprising: a hot box accommodating a fuel cell and a reformer; a start burner for heating the hot box so that the temperature of the hot box is raised to a reaction temperature in an initial operation; a first heat exchange portion which heats inhaled outside air by using heat of the start burner or heat of exhaust gas from the hot box and supplies the heated air into the hot box; a second heat exchange portion generating steam using heat of the exhaust gas, supplying the steam to the reformer, and maintaining the reaction temperature by cooling the fuel cell using the exhaust gas having a lowered temperature; and a combustion gas line provided to surround the fuel cell inside of the hot box, connected to the first heat exchange portion, and is configured to maintain the reaction temperature by heating the hot box using heat of the start burner and by cooling the hot box using the exhaust gas from the second heat exchange portion, and a condensing boiler portion configured such that exhaust gas of the condensing boiler portion and the exhaust gas of the fuel cell portion are completely discharged through an exhaust hood for unifying discharge holes, the condensing boiler portion comprising: a sensible heat exchanger collecting sensible heat emitted by combustion of gas inside a burner; a latent heat exchanger connected to an exhaust gas pipe of the fuel cell portion, and collecting the latent heat of self-generated exhaust gas passing from the sensible heat exchanger to the latent heat exchanger together with the latent heat of exhaust gas from the fuel cell portion; and a connection pipe connected to the exhaust gas pipe and having a shape of a bent structure surrounding a side portion of the latent heat exchanger for further enhancing the thermal efficiency, the connection pipe being configured for supplying the exhaust gas of the fuel cell portion to the latent heat exchanger, the exhaust gas of the fuel cell portion being supplied to the entire periphery of the latent heat exchanger so that the latent heat exchanger is prevented from being locally overheated, wherein the first heat exchange portion and the second heat exchange portion are equipped outside of the hot box, wherein the exhaust gas from the hot box passes through sequentially the second heat exchange portion, the combustion gas line, and the first heat exchange portion. 2. The system of claim 1 , wherein the connection pipe guides the exhaust gas of the fuel cell portion to contact a side surface of the latent heat exchanger. 3. The system of claim 1 , wherein the reformer comprises: a reforming portion receiving the raw material gas and steam, and reforming the gas and the steam into hydrogen gas; and a burner for heating the reforming portion. 4. The system of claim 3 , wherein the burner heats the reforming portion by an exothermic reaction in which unreacted oxygen and hydrogen after reaction in the fuel cell are reacted. 5. The system of claim 4 , wherein the burner comprises a primary burner and a secondary burner, and the unreacted oxygen and hydrogen are sequentially supplied to the primary and secondary burners.
characterised by their heat exchangers · CPC title
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