JPH065302A - Heat insulation construction method for fuel cell power generation facility - Google Patents
Heat insulation construction method for fuel cell power generation facilityInfo
- Publication number
- JPH065302A JPH065302A JP4160489A JP16048992A JPH065302A JP H065302 A JPH065302 A JP H065302A JP 4160489 A JP4160489 A JP 4160489A JP 16048992 A JP16048992 A JP 16048992A JP H065302 A JPH065302 A JP H065302A
- Authority
- JP
- Japan
- Prior art keywords
- fuel cell
- heat
- devices
- gas
- reformer
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 239000000446 fuel Substances 0.000 title claims abstract description 38
- 238000010248 power generation Methods 0.000 title claims abstract description 21
- 238000010276 construction Methods 0.000 title claims abstract description 12
- 238000009413 insulation Methods 0.000 title claims description 8
- 239000011810 insulating material Substances 0.000 claims abstract description 18
- 239000002245 particle Substances 0.000 claims abstract description 18
- 239000007789 gas Substances 0.000 claims description 42
- 239000002737 fuel gas Substances 0.000 claims description 11
- 230000003197 catalytic effect Effects 0.000 claims description 10
- 238000000034 method Methods 0.000 claims description 10
- 238000002407 reforming Methods 0.000 claims description 7
- 229910052739 hydrogen Inorganic materials 0.000 claims description 6
- 239000001257 hydrogen Substances 0.000 claims description 6
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 claims description 5
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 5
- 229910052760 oxygen Inorganic materials 0.000 claims description 5
- 239000001301 oxygen Substances 0.000 claims description 5
- 239000000919 ceramic Substances 0.000 claims description 4
- 239000011362 coarse particle Substances 0.000 claims description 4
- 239000010419 fine particle Substances 0.000 claims description 4
- 239000000203 mixture Substances 0.000 claims description 4
- 125000004435 hydrogen atom Chemical class [H]* 0.000 claims 1
- 230000017525 heat dissipation Effects 0.000 abstract description 5
- 238000002485 combustion reaction Methods 0.000 description 9
- 239000007788 liquid Substances 0.000 description 6
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 6
- 239000000567 combustion gas Substances 0.000 description 5
- 238000012360 testing method Methods 0.000 description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 4
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 4
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 3
- 239000003054 catalyst Substances 0.000 description 3
- 150000002431 hydrogen Chemical class 0.000 description 3
- 239000003345 natural gas Substances 0.000 description 3
- 230000005855 radiation Effects 0.000 description 3
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 2
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 2
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 2
- 229910002092 carbon dioxide Inorganic materials 0.000 description 2
- 239000001569 carbon dioxide Substances 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 230000005611 electricity Effects 0.000 description 2
- 239000003546 flue gas Substances 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 239000000377 silicon dioxide Substances 0.000 description 2
- 229910052717 sulfur Inorganic materials 0.000 description 2
- 239000011593 sulfur Substances 0.000 description 2
- 239000000378 calcium silicate Substances 0.000 description 1
- 229910052918 calcium silicate Inorganic materials 0.000 description 1
- OYACROKNLOSFPA-UHFFFAOYSA-N calcium;dioxido(oxo)silane Chemical compound [Ca+2].[O-][Si]([O-])=O OYACROKNLOSFPA-UHFFFAOYSA-N 0.000 description 1
- 229910002091 carbon monoxide Inorganic materials 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- SHFGJEQAOUMGJM-UHFFFAOYSA-N dialuminum dipotassium disodium dioxosilane iron(3+) oxocalcium oxomagnesium oxygen(2-) Chemical compound [O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[Na+].[Na+].[Al+3].[Al+3].[K+].[K+].[Fe+3].[Fe+3].O=[Mg].O=[Ca].O=[Si]=O SHFGJEQAOUMGJM-UHFFFAOYSA-N 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 239000010451 perlite Substances 0.000 description 1
- 235000019362 perlite Nutrition 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- 210000002268 wool Anatomy 0.000 description 1
Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/04—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
- H01M8/04007—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids related to heat exchange
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/06—Combination of fuel cells with means for production of reactants or for treatment of residues
- H01M8/0606—Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants
- H01M8/0612—Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants from carbon-containing material
- H01M8/0625—Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants from carbon-containing material in a modular combined reactor/fuel cell structure
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/24—Grouping of fuel cells, e.g. stacking of fuel cells
- H01M8/2465—Details of groupings of fuel cells
- H01M8/247—Arrangements for tightening a stack, for accommodation of a stack in a tank or for assembling different tanks
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/50—Fuel cells
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Fuel Cell (AREA)
- Hydrogen, Water And Hydrids (AREA)
Abstract
(57)【要約】
【目的】 発電設備を小型にし、かつ放熱損出を低減さ
せてプラント効率を高めることができる燃料電池発電設
備の保温施工方法を提供する。
【構成】 保温施工した底部56の上面に保温が必要な
複数の機器10、20、30、40等を少なくとも保温
に必要な間隔を隔てて据え付け、複数の機器を配管で連
結し、複数の機器及び配管をまとめて囲む外枠50を底
部の上面に取り付け、次いで、複数の機器及び配管と外
枠との間に保温材の粒子を充填する。
(57) [Abstract] [Purpose] To provide a heat insulating construction method for a fuel cell power generation facility, which is capable of downsizing the power generation facility and reducing heat dissipation loss to improve plant efficiency. [Structure] A plurality of devices 10, 20, 30, 40, etc., which need to be kept warm, are installed on the upper surface of a heat-insulated bottom portion 56 at least at intervals necessary for keeping warm, and the plurality of devices are connected by pipes to form a plurality of devices. And the outer frame 50 that encloses the pipes together is attached to the upper surface of the bottom, and then particles of the heat insulating material are filled between the plurality of devices / pipes and the outer frame.
Description
【0001】[0001]
【産業上の利用分野】本発明は、燃料電池発電設備の保
温施工方法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a heat insulating construction method for fuel cell power generation equipment.
【0002】[0002]
【従来の技術】溶融炭酸塩型燃料電池は、高効率、かつ
環境への影響が少ないなど、従来の発電装置にはない特
徴を有しており、水力・火力・原子力に続く発電システ
ムとして注目を集め、現在世界各国で鋭意研究開発が行
われている。特に天然ガスを燃料とする溶融炭酸塩型燃
料電池を用いた発電設備は、都市部のビルやマンション
等に分散して設置し、都市ガスを燃料として発電と冷暖
房を行うことにより、従来の送電に伴うロスが大幅に低
減でき、かつ80%以上の熱効率を発揮できるシステム
として脚光を浴びている。2. Description of the Related Art Molten carbonate fuel cells have characteristics that conventional power generators do not have, such as high efficiency and little impact on the environment, and they are attracting attention as a power generation system following hydropower, thermal power, and nuclear power. Is currently being researched and developed all over the world. In particular, power generation facilities that use molten carbonate fuel cells that use natural gas as fuel are distributed and installed in buildings and condominiums in urban areas. It is in the limelight as a system that can significantly reduce the loss associated with the above and can exhibit a thermal efficiency of 80% or more.
【0003】かかる発電設備は、改質器と燃料電池を備
え、改質器により天然ガスを水素を含むアノードガスに
改質し、このアノードガスと空気とから燃料電池により
発電し、その余熱により温水を製造するものである。Such power generation equipment is equipped with a reformer and a fuel cell. The reformer reforms natural gas into an anode gas containing hydrogen, and the anode gas and air are used to generate electricity by the fuel cell. It produces hot water.
【0004】[0004]
【発明が解決しようとする課題】しかし、かかる発電設
備は、その特徴を十分に発揮するには、改質器と燃料電
池の他に、種々の機器、例えば脱硫器、燃料予熱器、空
気予熱器、触媒燃焼器、凝縮器、気液分離器等を必要と
する。このため、発電設備全体が大型になる問題があっ
た。However, in order to fully utilize the characteristics of such power generation equipment, in addition to the reformer and the fuel cell, various equipment such as a desulfurizer, a fuel preheater, and an air preheater are required. Reactor, catalytic combustor, condenser, gas-liquid separator, etc. are required. Therefore, there is a problem that the entire power generation facility becomes large.
【0005】また、従来の保温施工方法では、保温を必
要とする機器や配管等をそれぞれ成形した保温材と繊維
状の保温材で囲み、そのまわりを薄い外装板で覆い、更
にバンド等で外装板を固定していた。しかし、かかる方
法では、各機器のまわりに保温施工するための作業スペ
ースを必要とするため、発電設備全体が更に大型になる
問題があった。In the conventional heat insulating construction method, the heat insulating material and the fibrous heat insulating material are used to enclose the equipment and pipes, etc., which require heat insulation. The board was fixed. However, such a method requires a work space around each device for heat insulating work, and thus has a problem that the entire power generation facility becomes larger.
【0006】一方、上述した分散型の発電設備は、ビル
等に設置するために小型であることが強く要望されるた
め、各機器をできるだけ密接に配置することが不可欠と
なる。このため、高温(例えば700°C以上)に達す
る機器であっても十分な保温ができず、放熱損失が大き
くなり、プラント効率が低下する問題があった。On the other hand, since the distributed power generation equipment described above is strongly required to be small in size for installation in a building or the like, it is indispensable to arrange each equipment as closely as possible. For this reason, there is a problem in that even a device that reaches a high temperature (for example, 700 ° C. or higher) cannot sufficiently retain heat, heat dissipation increases, and plant efficiency decreases.
【0007】本発明は、かかる問題を解決するために創
案されたものである。すなわち、本発明は、発電設備を
小型にし、かつ放熱損出を低減させてプラント効率を高
めることができる燃料電池発電設備の保温施工方法を提
供することを目的とする。The present invention was created to solve such a problem. That is, an object of the present invention is to provide a heat insulating construction method for a fuel cell power generation facility, which is capable of downsizing the power generation facility and reducing heat dissipation loss to improve plant efficiency.
【0008】[0008]
【課題を解決するための手段】本発明による燃料電池発
電設備の保温施工方法は、保温施工した底部の上面に保
温が必要な複数の機器を少なくとも保温に必要な間隔を
隔てて据え付け、前記複数の機器を配管で連結し、前記
複数の機器及び配管をまとめて囲む外枠を前記底部の上
面に取り付け、次いで、前記複数の機器及び配管と前記
外枠との間に保温材の粒子を充填する、ことからなる。According to the present invention, there is provided a method for keeping heat of a fuel cell power generation facility, wherein a plurality of devices which need to be kept warm are installed on the upper surface of the bottom which is kept warm at least at intervals necessary for keeping warm. The equipment is connected by piping, an outer frame surrounding the plurality of equipment and piping together is attached to the upper surface of the bottom portion, and then particles of a heat insulating material are filled between the plurality of equipment and piping and the outer frame. Yes, it consists of things.
【0009】本発明の好ましい実施例によれば、前記保
温材の粒子は、セラミック粒子であり、かつ粗い粒子と
微細な粒子との混合物である。また、前記外枠は取り付
け前に保温施工されているのが好ましい。更に、前記複
数の機器は、燃料ガスを水素を含むアノードガスに改質
する改質器と、前記アノードガスと酸素を含むカソード
ガスとから発電する燃料電池と、燃料電池を出たアノー
ド排ガスを燃焼させる触媒燃焼器と、改質器を出た高温
のアノードガスと改質器に供給する低温の燃料ガスとの
間で熱を交換する熱交換器とからなることが好ましい。
また、前記燃料電池は溶融炭酸塩型燃料電池であり、前
記改質器はプレート型改質器であることが好ましい。According to a preferred embodiment of the present invention, the particles of the heat insulating material are ceramic particles and are a mixture of coarse particles and fine particles. Further, it is preferable that the outer frame is heat-insulated before mounting. Further, the plurality of devices include a reformer for reforming a fuel gas into an anode gas containing hydrogen, a fuel cell for generating power from the anode gas and a cathode gas containing oxygen, and an anode exhaust gas discharged from the fuel cell. It is preferably composed of a catalytic combustor for combusting and a heat exchanger for exchanging heat between the high temperature anode gas leaving the reformer and the low temperature fuel gas supplied to the reformer.
Further, it is preferable that the fuel cell is a molten carbonate fuel cell and the reformer is a plate reformer.
【0010】[0010]
【作用】本発明によれば、保温施工した底部の上面に保
温が必要な複数の機器を据え付け、この複数の機器を配
管で連結した後、所定の試験、例えば耐圧・気密試験、
作動試験、等を行う。複数の機器は、互いに少なくとも
保温に必要な間隔を隔てている。次いで、複数の機器及
び配管をまとめて囲む外枠を前記底部の上面に取り付け
る。この外枠は取り付け前に保温施工されているのが良
い。次いで、前記複数の機器及び配管と前記外枠との間
に保温材の粒子を充填する。この保温材の粒子は、セラ
ミック粒子であり、かつ粗い粒子と微細な粒子との混合
物であるのが良い。According to the present invention, a plurality of devices that need to be kept warm are installed on the upper surface of the bottom that has been kept warm, and after connecting the plurality of devices by piping, a predetermined test, for example, pressure resistance / airtightness test,
Perform an operation test, etc. The plurality of devices are separated from each other by at least an interval required for heat retention. Next, an outer frame that encloses a plurality of devices and piping together is attached to the upper surface of the bottom portion. This outer frame should be heat-insulated before installation. Next, particles of the heat insulating material are filled between the plurality of devices and piping and the outer frame. The particles of the heat insulating material are preferably ceramic particles and a mixture of coarse particles and fine particles.
【0011】この方法により、従来の施工方法のよう
に、各機器のまわりに保温施工するための作業スペース
を必要とせず、できる限り密接して配置することがで
き、設備全体を小型にすることができる。また、外枠と
各機器の間には保温材が充填されるため、従来以上に厚
く完全な保温性能を得ることができ、放熱損失が少なく
なり、プラント効率を高めることができる。By this method, unlike the conventional construction method, it is possible to arrange the equipment as close to each other as possible without requiring a work space for heat insulation construction around each equipment, and to make the entire equipment compact. You can Further, since the heat insulating material is filled between the outer frame and each device, it is possible to obtain a thicker and more complete heat insulating performance than ever before, the heat dissipation loss is reduced, and the plant efficiency can be improved.
【0012】[0012]
【実施例】以下に本発明の好ましい実施例を図面を参照
して説明する。図1は、本発明による方法を実施するた
めの発電設備を示す全体構成図である。この図におい
て、発電設備は、燃料ガスを水素を含むアノードガスに
改質する改質器10と、前記アノードガスと酸素を含む
カソードガスとから発電する燃料電池20と、アノード
排ガスを燃焼させる触媒燃焼器30と、改質器10を出
た高温のアノードガスと改質器10に供給する低温の燃
料ガスとの間で熱を交換する熱交換器すなわち燃料予熱
器40とを備える。更に、本発電設備は、燃料ガス中に
含まれる硫黄分を除去する脱硫器12と、空気を予熱す
る空気予熱器14と、排ガス中の水分を凝縮する凝縮器
16と、凝縮した水分を分離する気液分離器18とを備
えている。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENT A preferred embodiment of the present invention will be described below with reference to the drawings. FIG. 1 is an overall configuration diagram showing a power generation facility for carrying out the method according to the present invention. In this figure, a power generation facility includes a reformer 10 for reforming a fuel gas into an anode gas containing hydrogen, a fuel cell 20 for generating power from the anode gas and a cathode gas containing oxygen, and a catalyst for burning the anode exhaust gas. A combustor 30 and a heat exchanger or fuel preheater 40 for exchanging heat between the high temperature anode gas that has exited the reformer 10 and the low temperature fuel gas that is supplied to the reformer 10 are provided. Further, the present power generation facility has a desulfurizer 12 for removing sulfur contained in the fuel gas, an air preheater 14 for preheating air, a condenser 16 for condensing water in exhaust gas, and a condensed water for separation. And a gas-liquid separator 18 that operates.
【0013】硫黄分を含む天然ガス等の燃料ガスは脱硫
器12により脱硫された後、ライン1を通って燃料加熱
器40に供給され、この燃料予熱器40で加熱されて改
質器10に供給される。A fuel gas such as natural gas containing sulfur is desulfurized by a desulfurizer 12 and is then supplied to a fuel heater 40 through a line 1 and heated by the fuel preheater 40 to be supplied to a reformer 10. Supplied.
【0014】改質器10は、触媒燃焼器30から燃焼ガ
スライン6を介して供給される高温の燃焼ガスが完全燃
焼する燃焼室Coと、燃焼室からの伝熱により燃料ガス
を改質する改質室Reとからなる。改質器10は、燃焼
室Coと改質室Reを平面状にし、これを複数積層させ
たプレート型改質器であるのが良い。改質室Re内には
改質触媒が充填され、燃焼室Coで発生した高温の燃焼
ガスにより燃料ガスを水素を含む高温のアノードガスに
改質する。放熱により温度が下がった燃焼排ガスは、燃
焼排ガスライン7を介して空気予熱器14に供給されて
空気を加熱し、次いで、凝縮器16及び気液分離器18
により水分が除去される。一方、改質器10を出た高温
のアノードガスは、アノードガスライン2を介して燃料
予熱器40に供給され、この燃料予熱器40で冷却さ
れ、燃料電池20に供給される。The reformer 10 reforms the fuel gas by the combustion chamber Co in which the high temperature combustion gas supplied from the catalytic combustor 30 through the combustion gas line 6 is completely burned and the heat transfer from the combustion chamber. The reforming chamber Re. The reformer 10 is preferably a plate-type reformer in which the combustion chamber Co and the reforming chamber Re are made flat and a plurality of these are stacked. The reforming chamber Re is filled with a reforming catalyst, and the high temperature combustion gas generated in the combustion chamber Co reforms the fuel gas into a high temperature anode gas containing hydrogen. The flue gas whose temperature has dropped due to heat radiation is supplied to the air preheater 14 via the flue gas line 7 to heat the air, and then the condenser 16 and the gas-liquid separator 18
Removes water. On the other hand, the high temperature anode gas exiting the reformer 10 is supplied to the fuel preheater 40 via the anode gas line 2, cooled by the fuel preheater 40, and supplied to the fuel cell 20.
【0015】燃料電池20は、アノードガスが通過する
アノード側Aと、カソードガスが通過するカソード側C
とからなり、アノードガス中の水素、一酸化炭素と、カ
ソードガス中の酸素、二酸化炭素とから化学反応により
電気を発生するようになっている。燃料電池20は、溶
融炭酸塩型燃料電池であるのが良い。The fuel cell 20 has an anode side A through which the anode gas passes and a cathode side C through which the cathode gas passes.
And hydrogen is generated in the anode gas and carbon monoxide, and oxygen and carbon dioxide in the cathode gas generate electricity by a chemical reaction. The fuel cell 20 may be a molten carbonate fuel cell.
【0016】燃料電池20を出たアノード排ガスとカソ
ード排ガスはアノード排ガスライン4及びカソード排ガ
スライン5を介して触媒燃焼器30に供給される。この
触媒燃焼器30内には、ハニカム状のニッケルを主成分
とする燃焼触媒が充填されており、アノード排ガスに含
まれる未燃分をカソード排ガスに含まれる酸素により燃
焼させるようになっている。この触媒燃焼器30で発生
した高温の燃焼ガスはライン6を介して改質器10の燃
焼室Coに供給される。The anode exhaust gas and the cathode exhaust gas that have exited the fuel cell 20 are supplied to the catalytic combustor 30 via the anode exhaust gas line 4 and the cathode exhaust gas line 5. The catalytic combustor 30 is filled with a honeycomb-shaped combustion catalyst containing nickel as a main component, and the unburned components contained in the anode exhaust gas are burned by the oxygen contained in the cathode exhaust gas. The high temperature combustion gas generated in the catalytic combustor 30 is supplied to the combustion chamber Co of the reformer 10 via the line 6.
【0017】なお、触媒燃焼器30を用いずに、改質器
10の燃焼室でアノード排ガスを直接燃焼させる場合も
ある。In some cases, the anode exhaust gas is directly combusted in the combustion chamber of the reformer 10 without using the catalytic combustor 30.
【0018】燃料電池20のカソードガスライン3には
空気源(図示せず)から空気ライン8、空気予熱器14
を介して空気が供給される。この空気ライン8には凝縮
器16及び気液分離器18により水分が除去された燃焼
排ガスの一部が供給され、電池の反応に必要な二酸化炭
素を供給するようになっている。In the cathode gas line 3 of the fuel cell 20, an air source (not shown), an air line 8 and an air preheater 14 are provided.
Air is supplied through the. A part of the combustion exhaust gas from which water has been removed by the condenser 16 and the gas-liquid separator 18 is supplied to the air line 8 so that carbon dioxide necessary for the reaction of the battery is supplied.
【0019】更に、燃料電池のカソード側Cを通過した
カソード排ガスの一部はカソード循環ライン9を介して
カソードライン3に循環される。このカソード循環ライ
ン9には通常、熱交換器(図示せず)、ブロア22が設
けられ、循環するカソードガスの温度、流量を制御でき
るようになっている。Further, a part of the cathode exhaust gas passing through the cathode side C of the fuel cell is circulated to the cathode line 3 via the cathode circulation line 9. A heat exchanger (not shown) and a blower 22 are usually provided in the cathode circulation line 9 so that the temperature and flow rate of the circulating cathode gas can be controlled.
【0020】上記発電設備では、改質器10、燃料電池
20、触媒燃焼器30、燃料予熱器40、及びそれらの
間の配管が、特に高温であり十分な保温施工を必要とす
る。このため、これらの機器を共通の外枠内に格納する
のが良い。すなわち、例えば図1において、一点鎖線で
囲んだ機器及び配管のすべてを1つの外枠50内に格納
する。In the above-mentioned power generation equipment, the reformer 10, the fuel cell 20, the catalytic combustor 30, the fuel preheater 40, and the pipes between them are particularly high in temperature, and a sufficient heat insulating work is required. Therefore, it is preferable to store these devices in a common outer frame. That is, for example, in FIG. 1, all the equipment and piping surrounded by the one-dot chain line are stored in one outer frame 50.
【0021】その他の機器、例えば、図1における脱硫
器12、空気予熱器14、凝縮器16、及び気液分離器
18は、比較的運転温度が低いため外枠50内に格納し
なくても良い。Other devices, for example, the desulfurizer 12, the air preheater 14, the condenser 16 and the gas-liquid separator 18 in FIG. 1 do not have to be stored in the outer frame 50 because their operating temperatures are relatively low. good.
【0022】図2は図1で一点鎖線で囲んだ機器及び配
管を共通の外枠50に格納した状態を示す模式的断面図
である。この図に示すように、外枠50には保温材の粒
子を内部に充填するための投入口52と、保温材の粒子
を取り出すための取出口54とが設けられている。投入
口52は外枠50の上部に設けられ、取出口54は下部
に設けられるのがよい。粒子の充填は、空気輸送等を用
いてもよく、或いは単に内部にコンベア等で投入しても
良い。充填した粒子は、適当な方法、例えば振動や棒突
き等で適当な密度にする。また、図に示すように、制御
弁のアクチュエータ部や電動機等は制御と放熱のため
に、外枠の外側に出るように外枠を作っておく。FIG. 2 is a schematic cross-sectional view showing a state in which the equipment and piping surrounded by the one-dot chain line in FIG. 1 are stored in a common outer frame 50. As shown in this figure, the outer frame 50 is provided with an inlet 52 for filling the particles of the heat insulating material inside and an outlet 54 for taking out the particles of the heat insulating material. It is preferable that the inlet 52 is provided at the upper portion of the outer frame 50 and the outlet 54 is provided at the lower portion. The particles may be filled by pneumatic transportation or the like, or may be simply charged inside by a conveyor or the like. The packed particles are made to have an appropriate density by an appropriate method such as vibration or sticking. Further, as shown in the drawing, the actuator frame of the control valve, the electric motor, and the like are formed with an outer frame so as to extend outside the outer frame for control and heat dissipation.
【0023】本発電設備の保温施工は、以下の手順で行
う。まず、保温施工した底部56の上面に保温が必要な
複数の機器10、20、30、40等を少なくとも保温
に必要な間隔を隔てて据え付ける。この間隔は外枠内が
完全に保温材で充填された状態で必要な最小寸法にすれ
ばよく、特に保守や作業のための空間を必要としない。The heat insulating construction of the power generation equipment is carried out in the following procedure. First, a plurality of devices 10, 20, 30, 40, etc. that require heat insulation are installed on the upper surface of the bottom portion 56 that has been heat-insulated at least at intervals necessary for heat insulation. This space may be set to the minimum size required when the outer frame is completely filled with the heat insulating material, and does not require a space for maintenance or work.
【0024】次いで、前記複数の機器10、20、3
0、40等を配管で連結する。各機器の作動試験や、耐
圧試験等はこの段階で行うのが良い。次いで、前記複数
の機器及び配管をまとめて囲む外枠50を前記底部56
の上面に取り付ける。この外枠50は取り付け前に例え
ば内面が保温性能の高い保温材、例えば、シリカウール
やカオール等で十分に保温施工されているのが良い。Next, the plurality of devices 10, 20, 3
0, 40, etc. are connected by piping. It is advisable to perform the operation test and pressure resistance test of each device at this stage. Then, the outer frame 50 that encloses the plurality of devices and piping together is attached to the bottom portion 56.
To the top of the. Before mounting the outer frame 50, it is preferable that the inner surface thereof is sufficiently heat-insulated with a heat-insulating material having high heat-insulating performance, for example, silica wool or cahor.
【0025】次いで、前記複数の機器及び配管と前記外
枠との間に保温材の粒子を充填する。この保温材の粒子
は、700〜800°Cの高温に耐える保温材、例え
ば、セラミック、シリカ、ケイ酸カルシウム、パーライ
ト等の粒子であり、かつ粗い粒子と微細な粒子との混合
物であるのが良い。これにより、粒子の充填率を調節
し、必要な保温性能を得ることができる。Next, particles of a heat insulating material are filled between the plurality of devices and piping and the outer frame. The particles of this heat insulating material are heat insulating materials that can withstand a high temperature of 700 to 800 ° C., for example, particles of ceramics, silica, calcium silicate, perlite, and the like, and are a mixture of coarse particles and fine particles. good. Thereby, the packing rate of particles can be adjusted and the required heat retention performance can be obtained.
【0026】[0026]
【発明の効果】本発明による保温施工方法により、従来
の施工方法のように、各機器のまわりに保温施工するた
めの作業スペースを必要とせず、できる限り密接して配
置することができ、設備全体を小型にすることができ
る。また、外枠と各機器の間には保温材が充填されるた
め、従来以上に厚く完全な保温性能を得ることができ、
放熱損失が少なくなり、プラント効率を高めることがで
きる。EFFECTS OF THE INVENTION According to the heat insulation construction method of the present invention, unlike the conventional construction method, a work space for heat insulation construction around each device is not required, and the equipment can be arranged as close to each other as possible. The whole can be made small. In addition, since a heat insulating material is filled between the outer frame and each device, it is possible to obtain a thicker and more complete heat insulating performance than before,
Radiation loss is reduced, and plant efficiency can be improved.
【0027】従って、本発明により発電設備を小型に
し、かつ放熱損出を低減させてプラント効率を高めるこ
とができるTherefore, according to the present invention, it is possible to reduce the size of the power generation equipment, reduce the radiation loss, and enhance the plant efficiency.
【図1】本発明による発電装置を示す全体構成図であ
る。FIG. 1 is an overall configuration diagram showing a power generator according to the present invention.
【図2】図1で一点鎖線で囲んだ機器及び配管を共通の
外枠に格納した状態を示す模式的断面図である。FIG. 2 is a schematic cross-sectional view showing a state in which a device and a pipe surrounded by a chain line in FIG. 1 are stored in a common outer frame.
1 燃料ガスライン 2 アノードガスライン 3 カソードガスライン 4 アノード排ガスライン 5 カソード排ガスライン 6 燃焼ガスライン 7 燃焼排ガスライン 8 カソードガスライン 9 カソード循環ライン 10 改質器 12 脱硫器 14 空気予熱器 16 凝縮器 18 気液分離器 20 燃料電池 30 触媒燃焼器 40 燃料予熱器 50 外枠 56 外枠の底部 1 fuel gas line 2 anode gas line 3 cathode gas line 4 anode exhaust gas line 5 cathode exhaust gas line 6 combustion gas line 7 combustion exhaust gas line 8 cathode gas line 9 cathode circulation line 10 reformer 12 air preheater 16 condenser 18 Gas-Liquid Separator 20 Fuel Cell 30 Catalytic Combustor 40 Fuel Preheater 50 Outer Frame 56 Bottom of Outer Frame
Claims (5)
複数の機器を少なくとも保温に必要な間隔を隔てて据え
付け、 前記複数の機器を配管で連結し、 前記複数の機器及び配管をまとめて囲む外枠を前記底部
の上面に取り付け、 次いで、前記複数の機器及び配管と前記外枠との間に保
温材の粒子を充填する、ことからなる燃料電池発電設備
の保温施工方法。1. A plurality of devices that need to be kept warm are installed on the upper surface of the bottom portion that has been subjected to heat insulation at least at intervals necessary for keeping the heat, the plurality of devices are connected by pipes, and the plurality of devices and the pipes are collected together. A heat insulating construction method for a fuel cell power generation facility, comprising mounting an enclosing outer frame on an upper surface of the bottom portion, and then filling particles of a heat insulating material between the plurality of devices and pipes and the outer frame.
あり、かつ粗い粒子と微細な粒子との混合物である、こ
とを特徴とする請求項1に記載の方法。2. The method according to claim 1, wherein the particles of the heat insulating material are ceramic particles and are a mixture of coarse particles and fine particles.
いる、ことを特徴とする請求項1に記載の方法。3. The method according to claim 1, wherein the outer frame is heat-insulated before mounting.
むアノードガスに改質する改質器と、前記アノードガス
と酸素を含むカソードガスとから発電する燃料電池と、
燃料電池を出たアノード排ガスを燃焼させる触媒燃焼器
と、改質器を出た高温のアノードガスと改質器に供給す
る低温の燃料ガスとの間で熱を交換する熱交換器とから
なる、ことを特徴とする請求項1に記載の方法。4. The plurality of devices comprises a reformer for reforming a fuel gas into an anode gas containing hydrogen, and a fuel cell for generating power from the anode gas and a cathode gas containing oxygen.
It consists of a catalytic combustor that burns the anode exhaust gas that exits the fuel cell, and a heat exchanger that exchanges heat between the high-temperature anode gas that exits the reformer and the low-temperature fuel gas that supplies the reformer. The method according to claim 1, wherein
あり、前記改質器はプレート型改質器である、ことを特
徴とする請求項4に記載の方法。5. The method according to claim 4, wherein the fuel cell is a molten carbonate fuel cell, and the reformer is a plate reformer.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP16048992A JP3147498B2 (en) | 1992-06-19 | 1992-06-19 | Thermal insulation construction method for fuel cell power generation equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP16048992A JP3147498B2 (en) | 1992-06-19 | 1992-06-19 | Thermal insulation construction method for fuel cell power generation equipment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH065302A true JPH065302A (en) | 1994-01-14 |
| JP3147498B2 JP3147498B2 (en) | 2001-03-19 |
Family
ID=15716047
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP16048992A Expired - Fee Related JP3147498B2 (en) | 1992-06-19 | 1992-06-19 | Thermal insulation construction method for fuel cell power generation equipment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3147498B2 (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2003089504A (en) * | 2001-07-09 | 2003-03-28 | Mitsubishi Heavy Ind Ltd | Apparatus for reforming fuel |
| JP2003221207A (en) * | 2002-01-31 | 2003-08-05 | Aisin Seiki Co Ltd | Fuel reformer |
| JP2004311443A (en) * | 2003-04-03 | 2004-11-04 | J Eberspaesher Gmbh & Co Kg | Fuel cell system and burner device for the system |
| JP2005524218A (en) * | 2002-05-01 | 2005-08-11 | ゼネラル・モーターズ・コーポレーション | Apparatus and method for extending the operating range of a fuel cell stack |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP2431656B1 (en) | 2010-09-16 | 2013-08-28 | LG Innotek Co., Ltd. | Lighting device |
-
1992
- 1992-06-19 JP JP16048992A patent/JP3147498B2/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2003089504A (en) * | 2001-07-09 | 2003-03-28 | Mitsubishi Heavy Ind Ltd | Apparatus for reforming fuel |
| JP2003221207A (en) * | 2002-01-31 | 2003-08-05 | Aisin Seiki Co Ltd | Fuel reformer |
| JP2005524218A (en) * | 2002-05-01 | 2005-08-11 | ゼネラル・モーターズ・コーポレーション | Apparatus and method for extending the operating range of a fuel cell stack |
| JP2004311443A (en) * | 2003-04-03 | 2004-11-04 | J Eberspaesher Gmbh & Co Kg | Fuel cell system and burner device for the system |
Also Published As
| Publication number | Publication date |
|---|---|
| JP3147498B2 (en) | 2001-03-19 |
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