JP2012057936A - Atmosphere open type heat storage tank - Google Patents

Atmosphere open type heat storage tank Download PDF

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JP2012057936A
JP2012057936A JP2011243895A JP2011243895A JP2012057936A JP 2012057936 A JP2012057936 A JP 2012057936A JP 2011243895 A JP2011243895 A JP 2011243895A JP 2011243895 A JP2011243895 A JP 2011243895A JP 2012057936 A JP2012057936 A JP 2012057936A
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heat
storage tank
heat storage
storage material
water
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JP5325281B2 (en
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Akishi Kegasa
明志 毛笠
Yoshinori Hisakado
喜徳 久角
Yoshimichi Kiuchi
義通 木内
Hideki Yamaguchi
秀樹 山口
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Osaka Gas Co Ltd
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Abstract

PROBLEM TO BE SOLVED: To obtain a heat storage tank having a high flexibility in selecting a shape and allowing free shape selection according to the clearance shape of a device to include the storage tank.SOLUTION: This storage tank stores a heat storage material, has an opening 3o leading to the atmosphere at a position higher than the upper face of the stored heat storage material, and a heat exchanger 2 submerged in the heat storage material to exchange heat between the heat storage material and a heat medium. An inner face of the storage tank molded with a heat insulating material is covered with a bag-like sheet-like material 3 having heat resistance or corrosion resistance, or both properties and fixed to the storage tank on the liquid level of the heat storage material or self-standing or shape-retained in the storage tank. The storage tank stores the heat storage material with the heat storage material in contact with the sheet-like material 3, and a pipe connecting to at least the heat exchanger 2 connects to the opening 3o of the sheet-like material 3 via an atmosphere open face.

Description

本発明は、熱を一時的に貯留する蓄熱槽に関するものであり、容量が比較的小さな家庭用、小規模業務用分野に適合し、ヒートポンプ給湯器の貯湯槽や小規模コジェネレーション機器の排熱回収蓄熱槽としての応用に好適なものである。   The present invention relates to a heat storage tank that temporarily stores heat, and is suitable for household and small-scale business fields with relatively small capacities, and exhaust heat from a hot-pump hot water storage tank and small-scale cogeneration equipment. It is suitable for application as a recovery heat storage tank.

家庭用等の給湯分野における蓄熱槽は、水を蓄熱材とする貯湯槽であり、形式は密閉型で給水の圧力を利用して、蓄熱材でもある貯留温水を押し出して、給湯を行うものが殆どであった。暖房に用いる場合は、密閉型蓄熱槽に貯留された温水を循環使用するもの、あるいは、密閉型蓄熱槽内部もしくは外部に熱交換器を設置して、貯留温水と熱交換して利用するものが一般的である。特許文献1、特許文献2、特許文献3には、この種の密閉型貯湯槽の応用技術が示されている。   Heat storage tanks in the field of hot water supply for home use, etc. are hot water storage tanks that use water as a heat storage material, and the type is a sealed type that uses hot water pressure to push out the stored hot water, which is also a heat storage material, to supply hot water. It was almost. When using for heating, there are those that circulate and use hot water stored in a sealed heat storage tank, or those that install heat exchangers inside or outside the sealed heat storage tank and exchange heat with the stored hot water. It is common. Patent Document 1, Patent Document 2, and Patent Document 3 show application techniques of this type of sealed hot water storage tank.

密閉型貯湯槽は、給水の圧力を利用して給湯を行うことができるため、ポンプが不要であり、蓄熱材である水の比重差を利用した温度成層蓄熱が行えるので貯槽容積の利用率が高く、さらには、安定して高温水を出湯することができる特長がある。   Since a closed water storage tank can supply hot water using the pressure of the water supply, a pump is not required, and thermal stratification heat storage using the specific gravity difference of water, which is a heat storage material, can be performed. In addition, it has a feature that hot water can be discharged stably.

特開2005−195185号公報JP 2005-195185 A 特開2005−214517号公報JP 2005-214517 A 特開2005−133984号公報JP 2005-133984 A

しかしながら、密閉型貯湯槽は、給水圧力を利用するため必然的に耐圧容器(上水道を利用する場合の必要耐圧性能は1.65MPa)となり、耐食性(応力腐食割れを含む)をも考慮すると特殊ステンレス鋼(例えばLSUS444)の球形もしくは円筒形形状とならざるを得なかった。従って、例えば貯湯槽外形に薄型が要求される場合には、細径とした缶体の複数設置等を行う必要があり、円筒形状間の隙間等を有効利用できなかったため、外形、質量が大きく、コストの高いものとならざるを得なかった。   However, the sealed hot water storage tank is inevitably a pressure vessel (necessary pressure resistance is 1.65 MPa when using waterworks) because it uses the water supply pressure, and special stainless steel is also considered in consideration of corrosion resistance (including stress corrosion cracking). It had to be a spherical or cylindrical shape of steel (for example LSUS444). Therefore, for example, when the hot water tank outer shape is required to be thin, it is necessary to install a plurality of cans having a small diameter, and the gap between the cylindrical shapes could not be effectively used. The cost was unavoidable.

また、密閉型貯湯槽を上水道に接続する場合、貯湯槽上流(成層型貯槽の場合には貯槽下部)に減圧逆止弁を、下流(成層型貯槽の場合、エア抜きも兼ねて貯槽上部)に過圧逃し弁を設置する必要がある。貯留水の上水道への逆流を防止すると共に、例えば2MPa未満に減圧し、さらに過圧となる場合には圧力を一部開放して、圧力容器としての規制に適合させるためである。   In addition, when connecting a closed water storage tank to the water supply, a pressure reducing check valve is provided upstream of the hot water tank (in the case of a stratified storage tank, the lower part of the storage tank), and downstream (in the case of a stratified storage tank, the upper part of the storage tank also serves as an air vent). It is necessary to install an overpressure relief valve. This is to prevent backflow of the stored water to the water supply, and to reduce the pressure to, for example, less than 2 MPa, and to release some of the pressure when it becomes overpressure, so as to comply with the regulation as a pressure vessel.

水は加熱すると体膨張を起こして圧力が上昇するので、膨張分は過圧逃し弁から排水として捨てられることになるが、捨てられる水は貯湯槽上部の最も温度の高い水であり、体積膨張相当分(例えば4%)の温水の熱が無駄に捨てられることになる。   When water is heated, it causes body expansion and the pressure rises, so the expansion is discarded as wastewater from the overpressure relief valve, but the discarded water is the hottest water at the top of the hot water tank, and volume expansion A considerable amount (for example, 4%) of hot water is wasted.

なお、過圧逃し弁は、体積膨張相当水量を逃すだけであれば貯湯槽下部の低温部に設置することも理屈上は可能であるが、上水の加熱による溶存空気(溶存酸素、窒素)の解離(温度上昇による溶解度の減少)によって貯湯槽上部に空気だまりのできる不都合を回避するため、空気抜きを兼ねて、通常(空気抜き弁を設置しない場合)は上部に設置される。   Although it is theoretically possible to install the overpressure relief valve in the low temperature part at the bottom of the hot water tank as long as the volume of water equivalent to volume expansion is released, dissolved air (dissolved oxygen, nitrogen) by heating the water In order to avoid the inconvenience that air can be trapped in the upper part of the hot water tank due to the dissociation (decrease in solubility due to temperature rise), it is usually installed at the upper part (when an air vent valve is not installed) also serving as an air vent.

更には、減圧弁で上水の圧力が減殺されるため、二階への給湯では水量が低下したり、シャワーの勢いが弱くなったりする不便も密閉型貯湯槽の短所として指摘されている。   Furthermore, since the pressure of clean water is reduced by the pressure reducing valve, the inconvenience that the amount of water in the hot water supply to the second floor decreases and the momentum of the shower becomes weak has been pointed out as a disadvantage of the sealed hot water storage tank.

従って、本願の目的は、上記のような様々な問題点を比較的簡単な構造で解決することが可能であり、特に、形状選択において自由度が高く、貯槽を内蔵すべき装置の隙間形状に合わせた自由な形状選択が可能な蓄熱槽を得ることにある。   Therefore, the object of the present application is to solve the above-mentioned various problems with a relatively simple structure, and in particular, it has a high degree of freedom in shape selection, and it has a gap shape of a device in which a storage tank should be built. The object is to obtain a heat storage tank that can be freely selected in combination.

本構成による大気開放型蓄熱槽は、請求項1に記載したように、蓄熱材を貯留する貯槽であって、貯留した蓄熱材の上面より高い位置に大気に通じる開口を有するとともに、前記蓄熱材と熱媒体との熱交換を行う熱交換器を当該蓄熱材に浸漬して備え、前記熱交換器で前記蓄熱材から受熱した前記熱媒体を貯槽外に取り出して、温水若しくは給湯水として供給可能に構成され〔構成1〕、
前記貯槽の蓄熱材接触部分が断熱材の一体成形品にて形成され〔構成2〕、
前記断熱材で成型された貯槽の内面を、耐熱性又は耐食性或はそれらの両方の性質を有し、前記蓄熱材の液面上で貯槽に固定或は貯槽内において自立或は保形される袋状のシート状材料にて覆い、前記シート状材料に蓄熱材が接触する状態で前記蓄熱材の貯留を行うと共に、少なくとも前記熱交換器に接続する配管が、前記シート状材料の開口で前記蓄熱材の大気開放面を介して配管接続され〔構成3〕、
前記貯槽の上面全体を気密に覆う蓋を設けると共に、前記蓄熱材の大気開放面から当該大気開放面より下方の大気に通じる配管スペースを設け、前記熱交換器に接続する配管が、当該配管スペースを通して配管接続されている〔構成4〕ことを特徴とする。
〔構成1〕
〔構成1〕のごとく、大気開放して蓄熱槽を形成すれば、温水や給湯水を得るのに、貯槽は蓄熱材自体を貯留する強度のみを保有すれば良く、例えば家庭用等で用いる容量500リットル未満程度の貯槽であれば、自体で断熱性を有する発泡性樹脂(例えば硬質な発泡ポリエチレン、発泡ポリスチレン、発泡ポリウレタン)等で形成することが可能である。この場合、貯槽の形状は比較的自由に選定することができ、円筒形や立方体形状の他、貯槽を内蔵すべき装置の隙間形状に合わせた自在な形状に、継ぎ目無く形成することができる。製法は発泡性樹脂の成型に一般的に用いられている成型法(射出成型、ブロー成型等)が使用できる。当然、金属製貯槽を使用し、その外面において断熱を行う構造を採用してもよい。
The open air type heat storage tank according to this configuration is a storage tank for storing a heat storage material as described in claim 1, and has an opening leading to the atmosphere at a position higher than the upper surface of the stored heat storage material, and the heat storage material A heat exchanger that exchanges heat with the heat medium is immersed in the heat storage material, and the heat medium received from the heat storage material by the heat exchanger can be taken out of the storage tank and supplied as hot water or hot water. [Configuration 1],
The heat storage material contact portion of the storage tank is formed of an integrally molded product of heat insulating material [Configuration 2],
The inner surface of the storage tank formed of the heat insulating material has heat resistance and / or corrosion resistance, and is fixed to the storage tank on the liquid surface of the heat storage material, or is self-supporting or retaining in the storage tank. Covering with a bag-shaped sheet material, storing the heat storage material in a state where the heat storage material is in contact with the sheet material, and at least a pipe connected to the heat exchanger is an opening of the sheet material Piping is connected through the air release surface of the heat storage material [Configuration 3],
A lid that covers the entire upper surface of the storage tank in an airtight manner is provided, and a piping space that leads from the atmosphere opening surface of the heat storage material to the atmosphere below the atmosphere opening surface is provided, and a pipe connected to the heat exchanger is the piping space. It is characterized by being connected by piping through [Configuration 4].
[Configuration 1]
If the heat storage tank is formed by opening to the atmosphere as in [Configuration 1], the storage tank only needs to have the strength to store the heat storage material itself to obtain hot water or hot water supply. If it is a storage tank of less than about 500 liters, it can be formed of a foamable resin (eg, hard foamed polyethylene, foamed polystyrene, foamed polyurethane) or the like that has heat insulating properties. In this case, the shape of the storage tank can be selected relatively freely, and in addition to a cylindrical shape or a cubic shape, the storage tank can be seamlessly formed into a shape that matches the gap shape of the device in which the storage tank is to be built. As the production method, a molding method (injection molding, blow molding, etc.) generally used for molding of foamable resin can be used. Of course, a structure in which a metal storage tank is used and heat insulation is performed on the outer surface thereof may be employed.

熱交換器は、銅やステンレス等の金属管をコイル状や蛇管に成型して利用することが簡便である。蓄熱材が水等の液体の顕熱を利用する場合には裸管でも良いが、パラフィン等の相変化を伴う潜熱蓄熱材である場合には固相での熱伝達率が小さいので、蓄熱材側にフィンを取付けて伝熱面積を増加させたプレートフィン熱交を選定することが有利である。   It is easy to use a heat exchanger by molding a metal tube such as copper or stainless steel into a coil shape or a serpentine tube. When the heat storage material uses sensible heat of liquid such as water, a bare tube may be used, but when the heat storage material is a latent heat storage material with phase change such as paraffin, the heat transfer coefficient in the solid phase is small, so the heat storage material It is advantageous to select a plate fin heat exchange with fins attached to the side to increase the heat transfer area.

上水の供給を受けて温水もしくは給湯水として利用する場合には、上水道の圧力を減圧することなく熱交換器に通じることができるため、給水圧力に近い高給湯圧力が実現でき、家屋の二階、三階への給湯や高圧シャワーに有利である。   When water is supplied and used as hot water or hot water, it can be connected to the heat exchanger without reducing the pressure of the water supply, so a high hot water pressure close to the water pressure can be realized, and the second floor of the house It is advantageous for hot water supply to the third floor and high pressure shower.

〔構成2〕
〔構成2〕のごとく、前記貯槽の蓄熱材接触部分が断熱材の一体成型品にて形成されているものとしておくと、任意の形状の貯槽を得、貯槽の外面に、鋼材等を配置して強度を補強したり、鋼板等で被覆して耐候性を向上させたりすることも可能である。また、内面を蓄熱材に対して耐食性、耐熱性、及び封液性のある材料とすること(自らの発泡倍率の低減、ライニング、コーティング、内張、塗装等を含む。)も必要に応じて選択することができる。
[Configuration 2]
As in [Configuration 2], if the heat storage material contact portion of the storage tank is formed of an integrally molded product of heat insulating material, a storage tank of an arbitrary shape is obtained, and steel or the like is disposed on the outer surface of the storage tank. It is also possible to reinforce the strength and improve the weather resistance by coating with a steel plate or the like. In addition, the inner surface should be made of a material that has corrosion resistance, heat resistance, and sealability against the heat storage material (including reduction of its own foaming ratio, lining, coating, lining, painting, etc.) as necessary. You can choose.

構成2の構造を採用すると、以下の利点を得ることができる。
1)蓄熱槽を樹脂等の低強度材料にて、安価に製造できる。
2)蓄熱槽を断熱材そのもので形成でき、断熱性に優れる。
3)比較的自由な形状に成型でき、外寸に対して貯留容積を大きくできる。
4)一体成型により蓄熱材の漏洩等を抑制できる。
5)熱交換器として、比較的安価なコイルやフィンチューブを利用できる。
6)熱媒体は管内を通すため、(管の耐圧内で)減圧の必要がない。
When the structure of the configuration 2 is adopted, the following advantages can be obtained.
1) The heat storage tank can be manufactured at low cost using a low-strength material such as resin.
2) The heat storage tank can be formed of the heat insulating material itself and has excellent heat insulating properties.
3) It can be molded into a relatively free shape, and the storage volume can be increased with respect to the outer dimensions.
4) Leakage of the heat storage material can be suppressed by integral molding.
5) A relatively inexpensive coil or fin tube can be used as a heat exchanger.
6) Since the heat medium passes through the pipe, there is no need for pressure reduction (within the pressure resistance of the pipe).

〔構成3〕
〔構成3〕のごとく、断熱材で成型された貯槽の内面を袋状のシート状材料にて覆い、前記シート状材料に蓄熱材が接触する状態で前記蓄熱材の貯留を行うと共に、少なくとも前記熱交換器に接続する配管が、前記シート状材料の開口で前記蓄熱材の大気開放面を介して配管接続されていることを特徴とする。この構成において、熱交換器とは関係しない蓄熱槽に関連する配管や、運転制御等に関連する検出配線、或いは制御機器との配線を前記シート状材料の開口で前記蓄熱材の大気開放面を介して行う。
[Configuration 3]
As [Configuration 3], the inner surface of the storage tank molded with the heat insulating material is covered with a bag-like sheet material, and the heat storage material is stored in a state where the heat storage material is in contact with the sheet material, and at least the The pipe connected to the heat exchanger is connected to the pipe through the air release surface of the heat storage material at the opening of the sheet-like material. In this configuration, piping related to the heat storage tank not related to the heat exchanger, detection wiring related to operation control, etc., or wiring to the control device is used to open the air release surface of the heat storage material at the opening of the sheet-like material. Do through.

〔作用効果〕
発泡性樹脂にて蓄熱槽を形成した場合、貯留する蓄熱材によっては発泡性樹脂を浸食する場合が発生する。例えば、蓄熱材として油脂状物質(溶剤を含む)を用いた場合である。そこで、蓄熱槽内面に、耐熱性・耐食性に優れたシート状材料(例えば、フッ素樹脂(テフロン(登録商標)等)、ナイロン樹脂等の耐熱性合成樹脂シート、ステンレス等の耐食性金属薄板・箔)の「袋」を挿入し、その内部に蓄熱材を充填する。
[Function and effect]
When the heat storage tank is formed of the foamable resin, the foamable resin may be eroded depending on the stored heat storage material. For example, it is a case where an oily substance (including a solvent) is used as the heat storage material. Therefore, on the inner surface of the heat storage tank, a sheet-like material excellent in heat resistance and corrosion resistance (for example, fluororesin (Teflon (registered trademark), etc.), heat resistant synthetic resin sheet such as nylon resin, corrosion resistant metal thin plate and foil such as stainless steel, etc. ) And insert the heat storage material inside.

「袋」は、液状の蓄熱材を漏洩させることの無いように一体的に成型されたもの、もしくは溶接・溶着にて封液性良くに加工されたものであることが望ましいが、液面上部で蓄熱槽に固定、又は(骨組みを用いてあるいは自らの強度にて)自立・保形していればよく、蓄熱槽内面には必ずしも密着もしくは接着してある必要はない。   It is desirable that the “bag” is molded integrally so as not to leak the liquid heat storage material or processed with good sealing properties by welding / welding. It is only necessary to be fixed to the heat storage tank, or to be self-supporting and shape-retaining (using a framework or with its own strength), and does not necessarily need to be in close contact with or adhered to the inner surface of the heat storage tank.

また、貯槽の上面全体を覆う蓋を設ける場合は、この蓋の部分にもシート状材料被覆を施すことも可能である。   Moreover, when providing the lid | cover which covers the whole upper surface of a storage tank, it is also possible to give a sheet-like material coating | cover also to the part of this lid | cover.

熱媒体に蓄熱された熱を回収する熱交換器や、熱媒体温度を検知するサーミスタや蓄熱材液面を検知する液面計(水位計)等の制御機器は、シート状材料の「袋」に孔を開けることなく固定し、それらの配管・配線も「袋」に別途開口する必要のない経路を選定して配置し、かつ「袋」に孔を開けることなく固定すべきである。熱媒体の漏洩を避止する効果の信頼性を向上させることができるからである。具体的には、機器は蓄熱槽の液面上部の構造物もしくは「蓋」から懸垂し、蓄熱材液面を通して配管・配線を行う構造を取ればよい。   Control devices such as heat exchangers that collect the heat stored in the heat medium, thermistors that detect the temperature of the heat medium, and liquid level gauges (water level gauges) that detect the liquid level of the heat storage material are “bags” of sheet-like material It should be fixed without opening a hole, and the piping and wiring should be selected and arranged so that it does not need to be opened separately in the “bag”, and fixed without making a hole in the “bag”. This is because the reliability of the effect of preventing leakage of the heat medium can be improved. Specifically, the device may be suspended from the structure or “lid” above the liquid level of the heat storage tank, and the piping / wiring may be taken through the heat storage material liquid level.

本構成により、蓄熱材の物性に応じた発泡樹脂製蓄熱槽を作成することが可能になると共に、蓄熱材の漏洩避止に関する信頼性を向上させることができる。   With this configuration, it is possible to create a foamed resin heat storage tank corresponding to the physical properties of the heat storage material, and it is possible to improve the reliability related to leakage prevention of the heat storage material.

〔構成4〕
上述の大気開放型蓄熱槽において、請求項2に記載したように、〔構成4〕のごとく、貯槽の上面全体(槽の大気開放面(気液界面もしくは気固界面)の上面全体)を気密に覆う蓋を設けると共に、蓄熱材の大気開放面から当該開放面より下方の大気に通じる配管スペースを設け、当該配管スペースを通して、前記熱交換器に接続する配管が、当該配管スペースを通して配管接続されていることを特徴とする。
この構成において、当然、配管スペースを配線スペースとしても使用することが好ましい。
[Configuration 4]
In the above-described atmospheric open type heat storage tank, as described in claim 2, as in [Configuration 4], the entire upper surface of the storage tank (the entire upper surface of the atmosphere open surface (gas-liquid interface or gas-solid interface) of the tank) is airtight. And a piping space that leads from the air opening surface of the heat storage material to the atmosphere below the opening surface, and the piping connected to the heat exchanger is connected through the piping space through the piping space. It is characterized by.
In this configuration, it is naturally preferable to use the piping space as the wiring space.

〔作用効果〕
上述のように大気開放型蓄熱槽への少なくとも配管(配線を含んでいてもよい)は、通常蓋に開口して行う必要が生じるが、開口と配管の隙間から熱損失を生じる可能性がある。また、蓋上部の取出し配管は、槽に比べて保温性能が低く熱容量も小さいのが通常であるため、静置時に放熱器となり、内部の熱媒体が冷やされて、温度の高い蓄熱槽内の熱媒体との間で自然循環が発生して、想定以上に放熱損失が生じる問題があった。
[Function and effect]
As described above, at least piping (which may include wiring) to the open air heat storage tank usually needs to be opened in the lid, but heat loss may occur from the gap between the opening and the piping. . Also, the extraction pipe at the top of the lid usually has a low heat retention performance and a small heat capacity compared to the tank, so it becomes a radiator when standing still, the internal heat medium is cooled, and the inside of the high-temperature heat storage tank There was a problem that natural circulation occurred with the heat medium, resulting in heat dissipation loss more than expected.

また、上述のシートを蓋内面に施工する場合にも、少なくとも配管(配線を含んでいてもよい)を通すために穿孔が必要となり、蒸気等を完全に封止することは困難であった。   Further, when the above-described sheet is applied to the inner surface of the lid, it is necessary to perforate to pass at least piping (which may include wiring), and it is difficult to completely seal the vapor and the like.

本構成では、槽の大気開放面から、槽の下方に向かって配管スペースを設けることで、上記の問題を解決している。配管スペースは、型の工夫により発泡性樹脂等で一体的に成型することも可能である。更には、配管スペースを蓄熱材下方まで延長すれば、配管接続を全て槽下方で行うことが可能になり、能率良く、また美観良く配線、配管を行うことができる。   In the present configuration, the above-described problem is solved by providing a piping space from the air release surface of the tank toward the bottom of the tank. The piping space can be integrally molded with a foamable resin or the like by devising the mold. Furthermore, if the piping space is extended to the lower side of the heat storage material, it is possible to connect all the piping under the tank, and the wiring and piping can be performed efficiently and aesthetically.

この構成では、少なくとも配管(配線を含んでいてもよい)の取り出しが下方になることにより、自然対流による放熱が抑制され、少なくとも配管と配管スペースとの間の隙間封止が精緻に行われなくても、高い断熱性能の期待できるメリットも生じる。   In this configuration, at least the piping (which may include wiring) is taken downward, so that heat dissipation due to natural convection is suppressed, and at least the gap between the piping and the piping space is not precisely sealed. However, the merit which can expect high heat insulation performance also arises.

〔構成5〕
本構成による大気開放型蓄熱槽は、請求項3に記載したように、〔構成1〕ないし〔構成4〕に記載した構成に加えて、〔構成5〕のごとく、熱交換器を流れる前記熱媒体の流れと蓄熱槽内の蓄熱材の流れとが、全体として対向流接触となるように熱交換器及び貯槽が配置若しくは配管接続されていることを特徴とする。
[Configuration 5]
In addition to the configurations described in [Configuration 1] to [Configuration 4], the open air heat storage tank according to the present configuration has the heat flowing through the heat exchanger as described in [Configuration 5]. The heat exchanger and the storage tank are arranged or connected by piping so that the flow of the medium and the flow of the heat storage material in the heat storage tank are in counterflow contact as a whole.

〔作用効果〕
蓄熱材が、温度上昇により比重が低下する液状物質(例えば水)である場合には、低温の熱媒体を蓄熱槽下部から抜き出してボイラ等で加熱の後蓄熱槽上部に戻すと、蓄熱槽内に上部から下部に向かう流れが形成されると共に上部が高温で下部が低温の温度成層が形成される。
[Function and effect]
When the heat storage material is a liquid substance (for example, water) whose specific gravity decreases as the temperature rises, if a low-temperature heat medium is extracted from the lower part of the heat storage tank and heated with a boiler or the like, it is returned to the upper part of the heat storage tank. In addition, a flow from the upper part to the lower part is formed, and a temperature stratification is formed in which the upper part is hot and the lower part is low.

また、比重の小さな潜熱蓄熱材と比重の大きな顕熱蓄熱材の組合せ(例えば、約70℃に融点を持つパラフィンと水)において、上述の加熱(例えば80℃)を行えば、昇温して蓄熱槽上部に戻された温水は上部のパラフィンを加熱して溶融させると共に、最上部に約80℃の溶融パラフィン、その下層に80℃から蓄熱材の初期温度(例えば20℃)に至る傾斜した温度分布を持つ温水層、さらに下部に(冷)水層が形成されると共に、やはり、上部から下部に向かう流れが形成される。   Further, in the combination of a latent heat storage material having a small specific gravity and a sensible heat storage material having a large specific gravity (for example, paraffin and water having a melting point of about 70 ° C.), if the above heating (for example, 80 ° C.) is performed, the temperature is increased. The hot water returned to the upper part of the heat storage tank heats and melts the paraffin in the upper part, and the uppermost part is about 80 ° C molten paraffin, and the lower layer is inclined from 80 ° C to the initial temperature of the heat storage material (for example, 20 ° C). A hot water layer having a temperature distribution and a (cold) water layer in the lower part are formed, and a flow from the upper part to the lower part is also formed.

このような温度成層を持つ蓄熱材中にコイル状熱交換器を設置し、コイル下部から上部に向かって熱媒体(例えば上水)を流せば、コイルを流れる熱媒体はマクロに見れば下部から上部に向かう流れとなり、全体として対向流的接触による熱交換が実現する。蓄熱材は上部が高温で、下部が低温であるため、対向流的流れにより、熱媒体(例えば上水)は、下部から上部に向かって温度が上昇し、加熱(熱回収)が実現する。蓄熱材は熱媒体によって冷却されるものの、上部が高温で下部が低温であるという温度分布は維持される。   If a coil-shaped heat exchanger is installed in a heat storage material having such a temperature stratification and a heat medium (for example, clean water) flows from the lower part of the coil to the upper part, the heat medium flowing through the coil starts from the lower part when viewed macroscopically. It becomes a flow toward the upper part, and heat exchange by countercurrent contact is realized as a whole. Since the upper part of the heat storage material has a high temperature and the lower part has a low temperature, the temperature of the heat medium (for example, clean water) rises from the lower part toward the upper part due to the counterflow, and heating (heat recovery) is realized. Although the heat storage material is cooled by the heat medium, the temperature distribution in which the upper part is high temperature and the lower part is low temperature is maintained.

ただし、蓄熱材が水の場合のように、初期には高温低温二層の成層が明瞭な場合にも、層の界面は不明瞭になり、傾斜的な温度分布に移行した後、その分布形状が維持される。このような作用により、温度分布が維持される結果、対向流接触的熱交換が実現し、効率的な熱回収が可能になる。   However, even when the stratification of the high-temperature and low-temperature bilayer is clear at the beginning, as in the case where the heat storage material is water, the layer interface becomes unclear, and after the transition to a gradient temperature distribution, the distribution shape Is maintained. As a result of this action, the temperature distribution is maintained, so that counter-flow contact heat exchange is realized and efficient heat recovery becomes possible.

〔構成6〕
本構成による大気開放型蓄熱槽は、請求項4に記載したように、〔構成1〕ないし〔構成5〕に記載した構成に加えて、〔構成6〕のごとくコジェネレーション機器(熱電併供給機器)の排熱を水の顕熱として貯留するものであることを特徴とする。
[Configuration 6]
In addition to the configurations described in [Configuration 1] to [Configuration 5], the open-air heat storage tank according to the present configuration is configured as described in [Configuration 6]. ) Is stored as sensible heat of water.

〔作用効果〕
コジェネレーション機器を住宅に設置する場合、構成機器の設置スペースと質量の低減が重要である。本構成にて蓄熱槽を構成する場合、蓄熱槽の形状を、円筒形や立方体形状のみならず、例えば、発電機器の余剰スペースの形状に合わせた不定型な形状も容易に形成することが可能である。現在の家庭用コージェネ機器は発電ユニット(主要機器はエンジン、燃料電池等)と排熱回収ユニット(主要機器は蓄熱槽とバックアップボイラ)の二分割形式が多いが、蓄熱槽の形状を適当に選択することによって、コジェネレーション機器を比較的コンパクトかつ軽量な一体形状にまとめたり、排熱回収ユニットを薄型に構成したりすることも容易になり、設置性が向上する。
[Function and effect]
When installing cogeneration equipment in a house, it is important to reduce the installation space and mass of the component equipment. When configuring a heat storage tank with this configuration, the shape of the heat storage tank can be easily formed not only in a cylindrical shape or a cubic shape, but also in an irregular shape that matches, for example, the shape of the surplus space of the power generation equipment. It is. Current home cogeneration equipment is divided into two types: a power generation unit (main equipment is an engine, fuel cell, etc.) and an exhaust heat recovery unit (main equipment is a heat storage tank and a backup boiler), but the shape of the heat storage tank is selected appropriately. By doing so, it becomes easy to combine the cogeneration equipment into a relatively compact and lightweight integrated shape, and to make the exhaust heat recovery unit thin, and the installation is improved.

〔構成7〕
本構成による大気開放型蓄熱槽は、請求項5に記載したように、〔構成1〕ないし〔構成5〕に記載した構成に加えて、〔構成7〕のごとくコジェネレーション機器の排熱を、水と水より比重と蒸気圧が小さくかつ固相−液相間の相変化潜熱を利用する潜熱蓄熱材の組合せにて貯留するものであることを特徴とする。
[Configuration 7]
In addition to the configurations described in [Configuration 1] to [Configuration 5], the open-air heat storage tank according to the present configuration, as described in claim 5, can exhaust heat from the cogeneration equipment as described in [Configuration 7]. It is characterized by being stored in a combination of water and a latent heat storage material having a specific gravity and vapor pressure smaller than water and utilizing phase change latent heat between a solid phase and a liquid phase.

〔作用効果〕
開放型蓄熱槽の蓄熱材として水を選択した場合、80℃程度に加熱すると蒸発が著しくなって蓄熱槽から湯気が発生する。この場合、蒸発潜熱に相当する熱量と水量を損失するだけでなく、槽を出た水蒸気が機体や家屋の表面に凝縮して腐食やカビを誘発するという不都合を生じる場合がある。水面からの蒸発を抑制するために、水面に多数の小球や、蒸気圧の低い油状物質を浮かべる対策の成されることが多いが、ここでは油脂状物質に替えて、あるいはその特殊例として、例えば水を80℃程度に加熱して蓄熱する場合には、70℃程度に融点を持ち、かつ水より比重と蒸気圧が小さな物質を採用する。そのような物質の例として分子量を適当に選択したパラフィンを挙げることができるが、パラフィンは潜熱蓄熱材としてもよく用いられるものであり、水面に浮かべることで、水の蒸発を抑えると共に、パラフィンの凝固−融解に伴う相変化潜熱をも蓄熱に利用することができる。
[Function and effect]
When water is selected as the heat storage material of the open-type heat storage tank, when it is heated to about 80 ° C., evaporation becomes remarkable and steam is generated from the heat storage tank. In this case, not only the amount of heat and the amount of water corresponding to the latent heat of vaporization are lost, but also the inconvenience that the water vapor exiting the tank condenses on the surface of the body and the house and induces corrosion and mold may occur. In order to suppress evaporation from the surface of the water, measures are often taken to float many small spheres or oily substances with low vapor pressure on the surface of the water, but here, instead of oily substances or as a special example thereof For example, when heat is stored by heating water to about 80 ° C., a substance having a melting point of about 70 ° C. and a specific gravity and vapor pressure smaller than that of water is adopted. Examples of such substances include paraffin with an appropriately selected molecular weight, but paraffin is also often used as a latent heat storage material. Phase change latent heat accompanying solidification-melting can also be used for heat storage.

本構成の場合、水の蒸発が盛んになる70℃以上になるとパラフィンが溶解して水面に広がるため、蒸発を有効に抑制することができる。また、低温(常温)から液体である油脂状物質を採用した場合に比べて、蓄熱量が増大するという特長が付加される。   In the case of this configuration, paraffin dissolves and spreads on the water surface at 70 ° C. or higher at which water evaporates, so that evaporation can be effectively suppressed. Moreover, compared with the case where the oily substance which is liquid from low temperature (normal temperature) is employ | adopted, the feature that heat storage amount increases is added.

水と潜熱蓄熱材の比率は適宜選択すればよく、例えば、潜熱蓄熱材の割合を多くすれば蓄熱量を増大させることができるが、固相での熱伝達率が小さくなるので、熱交換器に必要な伝熱面積も同時に増大させる必要が生じる。   The ratio between the water and the latent heat storage material may be appropriately selected. For example, if the ratio of the latent heat storage material is increased, the heat storage amount can be increased, but the heat transfer coefficient in the solid phase is reduced, so the heat exchanger It is also necessary to increase the heat transfer area required for the process.

〔構成12〕
本構成による大気開放型蓄熱槽は、請求項6に記載したように、これまで説明した構成に加えて、或いは〔構成1〕、〔構成2〕、〔構成3〕、〔構成4〕に、〔構成12〕のごとく熱交換器を、貯槽上部に配設される上部熱交換器と、貯槽下部に設けられる下部熱交換器と、前記両熱交換器内に形成された両熱媒体流路を貯槽上下方向に短絡する短絡流路を形成する短絡配管とを組み合わせて構成することを特徴とする。
[Configuration 12]
In addition to the configuration described so far, or the [configuration 1], [configuration 2], [configuration 3], and [configuration 4], the open air heat storage tank according to the present configuration is described in claim 6. As in [Configuration 12], the heat exchanger includes an upper heat exchanger disposed in the upper part of the storage tank, a lower heat exchanger provided in the lower part of the storage tank, and both heat medium flow paths formed in the two heat exchangers. And a short-circuit pipe that forms a short-circuit channel that short-circuits the storage tank in the vertical direction.

〔作用効果〕
このように、熱交換器を少なくとも2つに分割し、上部熱交換器と下部熱交換器とすることで、上部熱交換器においては、その近傍にある比較的高温の蓄熱材から受熱して、例えば、高温給湯を確実に行える。一方、下部熱交換器においては、その近傍にある比較的低温の蓄熱材への熱源温水からの授熱を、熱交換効率を高く保つことにより両者間の温度差によって確保することができ、熱の有効利用を図ることが可能となる。
[Function and effect]
In this way, by dividing the heat exchanger into at least two parts, an upper heat exchanger and a lower heat exchanger, the upper heat exchanger receives heat from a relatively high-temperature heat storage material in the vicinity thereof. For example, hot water can be reliably supplied. On the other hand, in the lower heat exchanger, heat transfer from the heat source hot water to the relatively low temperature heat storage material in the vicinity thereof can be ensured by the temperature difference between the two by keeping the heat exchange efficiency high. Can be used effectively.

さらに、この構成では所要の機能を果すことができる適正部位(上部及び下部)にのみ熱交換器を配設する構成となるため、各熱交換器は小型のものでよい。さらに、上部と下部で同一構造の熱交換器を2つ使用することとしておくと、更なるコストの低減を図ることができる。   Further, in this configuration, the heat exchangers are arranged only at appropriate portions (upper and lower portions) that can perform a required function, and thus each heat exchanger may be small. Furthermore, if two heat exchangers having the same structure are used in the upper part and the lower part, the cost can be further reduced.

〔構成13〕
本構成による大気開放型蓄熱槽は、請求項7に記載したように、これまで説明した構成に加えて、或いは〔構成1〕、〔構成2〕、〔構成3〕、〔構成4〕、〔構成12〕に、〔構成13〕のごとく蓄熱材が前記熱媒体に授熱する第1熱交換部を貯槽上部に設け、前記授熱により温度低下した前記蓄熱材を前記貯槽上部から貯槽下側に導く蓄熱材下降路を形成する下降路形成部材を設けるとともに、前記下降路形成部材の下側に蓄熱材開放口を設け、
前記蓄熱材開放口から流出する蓄熱材に授熱する第2熱交換部を設けたことを特徴とする。
〔作用効果〕
この構成にあっては、槽内上部に第1熱交換部が設けられ、この部位で蓄熱材が第1熱交換部内を流れる熱媒体に授熱することにより、その温度は低下する。このようにして温度低下した蓄熱材は、蓄熱材下降路を介して、貯槽上部から貯槽下側に導かれる。この蓄熱材下降路の下側には蓄熱材開放口が設けられていることにより、この開放口からその周部に蓄熱材が開放され、当該開放部位において第2熱交換部により、蓄熱材は加熱される。この蓄熱材は温度上昇に伴って上昇流動を起こす。
[Configuration 13]
As described in claim 7, the open air type heat storage tank according to the present configuration is in addition to the configuration described so far, or [Configuration 1], [Configuration 2], [Configuration 3], [Configuration 4], [ In the configuration 12], as in [configuration 13], a first heat exchanging part that heats the heat medium to the heat medium is provided in the upper part of the storage tank, and the heat storage material that has fallen in temperature due to the heat transfer is transferred from the upper part of the storage tank to the lower side of the storage tank Providing a descending path forming member that forms a heat storage material descending path leading to the thermal storage material, and providing a heat storage material opening on the lower side of the descending path forming member,
A second heat exchanging portion for providing heat to the heat storage material flowing out from the heat storage material opening is provided.
[Function and effect]
In this configuration, the first heat exchange part is provided in the upper part of the tank, and the temperature is lowered by the heat storage material transferring heat to the heat medium flowing in the first heat exchange part at this part. The heat storage material whose temperature has been lowered in this manner is guided from the upper part of the storage tank to the lower side of the storage tank via the heat storage material descending path. By providing a heat storage material opening on the lower side of the heat storage material descending path, the heat storage material is opened from the opening to the peripheral portion thereof, and the heat storage material is Heated. This heat storage material causes upward flow as the temperature rises.

結果、蓄熱材下降路の内側にあっては、低温となった蓄熱材の下降流が、外側では高温の蓄熱材の上昇流が形成でき、効率的に蓄熱槽内に蓄熱材の対流流動を実現でき、良好な熱利用を図ることができる。
以上より、本構成にて、排熱を有効利用して省エネルギーを図りながらも利便性を損なうことなく、高性能な給湯を実現することが可能になる。
蓄熱材における熱媒体との熱の授受の関係において、以下の構成を採ることも好ましい。
第1熱媒体から蓄熱材が受熱する前記熱交換器を、貯槽上部に配設される上部熱交換器と、貯槽下部に設けられる下部熱交換器と、前記両熱交換器内に形成された両熱媒体流路を蓄熱槽上下方向に短絡する短絡流路を形成する短絡配管とを組み合わせて構成し、
前記蓄熱材が第2熱媒体に授熱する第1熱交換部を貯槽上部に設け、
前記授熱により温度低下した前記蓄熱材を前記貯槽上部から貯槽下側に導く蓄熱材下降路を形成する下降路形成部材を設けるとともに、前記下降路形成部材の下側に蓄熱材開放口を設け、
前記第1熱媒体が、前記蓄熱材開放口から流出する蓄熱材に授熱する第2熱交換部を設ける。
As a result, on the inside of the heat storage material descending path, the downward flow of the heat storage material having a low temperature can form an upward flow of the high temperature heat storage material on the outside, and the convection flow of the heat storage material can be efficiently performed in the heat storage tank. It can be realized and good heat utilization can be achieved.
As described above, with this configuration, it is possible to realize high-performance hot water supply without impairing convenience while effectively using waste heat to save energy.
It is also preferable to adopt the following configuration in relation to the transfer of heat with the heat medium in the heat storage material.
The heat exchanger that receives the heat storage material from the first heat medium is formed in the upper heat exchanger disposed in the upper part of the storage tank, the lower heat exchanger provided in the lower part of the storage tank, and both the heat exchangers. Composed of a combination of short-circuit piping that forms a short-circuit channel that short-circuits both heat medium channels in the vertical direction of the heat storage tank,
A first heat exchanging part that heats the heat storage material to the second heat medium is provided in the upper part of the storage tank;
Provided is a descending path forming member that forms a thermal storage material descending path that guides the thermal storage material that has fallen in temperature due to the heat transfer from the upper part of the storage tank to the lower side of the storage tank, and a thermal storage material opening is provided below the descending path forming member. ,
The 1st heat carrier provides the 2nd heat exchange part which heats to the heat storage material which flows out of the heat storage material opening.

以上、説明を加えてきたように、本発明は蓄熱槽を大気開放型とすることにより以下の効果を発揮する。
1)蓄熱槽を発泡性樹脂等の低強度材料にて、安価に製造できる。
2)蓄熱槽を発泡性樹脂等の断熱材そのもので形成でき、断熱性に優れる。
3)比較的自由な形状に成型でき、外寸に対して貯留容積を大きくできる。
4)発泡性樹脂等の一体成型により蓄熱材の漏洩等を抑制できる。
5)槽内面を耐熱・耐食性のフィルムで覆うことで、信頼性を一層向上できる。
6)蓄熱材が水である場合、その蒸発損失(水と熱)を抑えることができる。
7)熱交換器として、比較的安価なコイルやフィンチューブを利用できる。
8)熱媒体は管内を通すため、(管の耐圧内で)減圧の必要がない。
9)補助熱源にて温度制御が確実にできる。
10)コージェネ排熱等、特に凝縮水の顕熱をも有効に利用できる。
これらにより、本発明利用機器のコストダウン、省エネルギー及び省スペースが実現できる。
As described above, the present invention exhibits the following effects by making the heat storage tank open to the atmosphere.
1) The heat storage tank can be manufactured at low cost using a low-strength material such as foamable resin.
2) The heat storage tank can be formed of a heat insulating material such as a foamable resin itself, and has excellent heat insulating properties.
3) It can be molded into a relatively free shape, and the storage volume can be increased with respect to the outer dimensions.
4) Leakage of the heat storage material can be suppressed by integral molding of foamable resin or the like.
5) Reliability can be further improved by covering the inner surface of the tank with a heat and corrosion resistant film.
6) When the heat storage material is water, the evaporation loss (water and heat) can be suppressed.
7) A relatively inexpensive coil or fin tube can be used as a heat exchanger.
8) Since the heat medium passes through the pipe, there is no need for pressure reduction (within the pressure resistance of the pipe).
9) The temperature can be reliably controlled by the auxiliary heat source.
10) The sensible heat of condensed water, such as cogeneration exhaust heat, can be used effectively.
As a result, cost reduction, energy saving, and space saving of the device using the present invention can be realized.

〔構成1・2〕の発明に係わる大気開放型蓄熱槽の斜視透視模式図Perspective perspective schematic view of the open air heat storage tank according to the invention of [Configuration 1 and 2] 〔構成1・2〕の発明に係わる他の実施形態を示す斜視透視模式図Perspective perspective schematic view showing another embodiment according to the invention of [Configuration 1 and 2] 〔構成3〕の発明に係わる発明の実施形態を示す斜視透視模式図Perspective perspective schematic view showing an embodiment of the invention according to the invention of [Configuration 3] 本発明をコジェネレーション機器等の蓄熱槽として利用した場合〔構成6〕の実施形態を示す斜視透視模式図A perspective perspective schematic diagram showing an embodiment of [Configuration 6] when the present invention is used as a heat storage tank for a cogeneration device or the like. 配線・配管を専用スペースを通じて下部に取出すことのできるように構成した蓄熱槽の例を示す中心部断面模式図Central cross-sectional schematic diagram showing an example of a heat storage tank configured so that wiring and piping can be taken out to the bottom through a dedicated space 小型SOFCに本発明の蓄熱槽を適用した場合の実施形態を示す流れ図Flow chart showing an embodiment when the heat storage tank of the present invention is applied to a small SOFC 図6に示す小型SOFCに本発明の蓄熱槽を適用した場合の別実施形態を示す流れ図The flowchart which shows another embodiment at the time of applying the thermal storage tank of this invention to the small-sized SOFC shown in FIG. 小型SOFCに本発明の蓄熱槽を適用した場合の他の実施形態を示す流れ図The flowchart which shows other embodiment at the time of applying the thermal storage tank of this invention to small SOFC. 隣組コジェネシステムに本発明の蓄熱槽を適用した場合の実施形態を示す流れ図Flow chart showing an embodiment when the heat storage tank of the present invention is applied to the adjacent cogeneration system 隣組コジェネシステムに本発明の蓄熱槽を適用した場合の別実施形態を示す流れ図The flowchart which shows another embodiment at the time of applying the thermal storage tank of this invention to an adjacent assembly cogeneration system 循環流動付与手段を備えた実施形態を示す図The figure which shows embodiment provided with the circulation flow provision means 貯槽の別実施形態を示す図The figure which shows another embodiment of a storage tank 密閉槽と、当該密閉槽に接続された膨張タンクからなる別実施形態を示す図The figure which shows another embodiment which consists of a closed tank and the expansion tank connected to the said closed tank

本発明の実施の形態について、図面に基づいて説明する。
〔構成1・2〕
図1は〔構成1・2〕の発明に係わる大気開放型蓄熱槽の概念図(斜視透視模式図)である。蓄熱槽1は発泡スチロール等の断熱性が良く液と蒸気の封止可能な発泡性樹脂にて有底円筒形状に一体的に成型されている。具体的には、一例として、ブタン等の炭化水素ガスを吸収させたポリスチレン樹脂を高温蒸気に当てて発泡させることにより、所定の有底円柱形状を得る成型法を採用している。そして、金型を切替える多段階成型手法を採用することにより、筒材内部1m及び外面1oにあっては、スチロールの発泡度の高いものとされ断熱性を確保し、蓄熱材hs(具体的には水w)が直接接触する内面1iにあっては、スチロールの発泡度を低下させ、蓄熱材hsとの接触面積を低下させている。結果、内面1iでは、スチロールが蓄熱材hsの影響を受け難く、蓄熱材hsの洩れ等が発生し難い構造としている。
この蓄熱槽1の構成材料としては、発泡スチロールの他、発泡ポリウレタン、発泡ポリエチレン等を採用してもよい。
Embodiments of the present invention will be described with reference to the drawings.
[Configuration 1 and 2]
FIG. 1 is a conceptual diagram (perspective perspective schematic diagram) of an open-air heat storage tank according to the invention of [Configuration 1 and 2]. The heat storage tank 1 is integrally formed into a bottomed cylindrical shape with a foamable resin having good heat insulation such as polystyrene foam and capable of sealing liquid and steam. Specifically, as an example, a molding method is adopted in which a polystyrene resin having absorbed hydrocarbon gas such as butane is foamed by applying high temperature steam to foam. Then, by adopting a multi-stage molding method for switching the mold, the inside of the cylindrical material 1m and the outer surface 1o are assumed to have a high degree of foaming of styrene, ensuring heat insulation, and the heat storage material hs (specifically In the inner surface 1i where water w) is in direct contact, the degree of foaming of styrene is reduced, and the contact area with the heat storage material hs is reduced. As a result, the inner surface 1i has a structure in which styrene is hardly affected by the heat storage material hs and leakage of the heat storage material hs is difficult to occur.
As a constituent material of the heat storage tank 1, foamed polyurethane, foamed polyethylene, or the like may be adopted in addition to foamed polystyrene.

熱交換器2は、銅管を螺旋状に巻いたいわゆるコイルであり、水w等の液体の蓄熱材hsもしくはパラフィン等の低温時固体−高温時液体の潜熱蓄熱材(図示せず。)に浸漬して使用する。潜熱蓄熱材を用いるときには、銅管外面にフィンを取付け、伝熱面積を増やして熱伝達性能を補うことが可能である。   The heat exchanger 2 is a so-called coil in which a copper tube is spirally wound, and is a liquid heat storage material hs such as water w or a low temperature solid-high temperature liquid latent heat storage material (not shown) such as paraffin. Immerse and use. When using a latent heat storage material, it is possible to supplement the heat transfer performance by attaching fins to the outer surface of the copper tube to increase the heat transfer area.

蓄熱槽外面1oは耐候性向上のため鋼板等で被覆し(図示せず。)、内面1iは蓄熱材hsの熱と浸食に耐えるべく樹脂の発泡率を低下させる等の適当な処置を採ることも任意である。また、機械的強度を補うため、鋼材等で適宜補強することも自由である。
この熱交換器2には、蓄熱材hsとの熱交換の対象となる熱媒体hrが流れる内部流路が形成されており、例えば熱媒体hrとして、常温の上水swが供給されて蓄熱材hsから受熱し、予熱水hwとして槽外に送り出される。
The outer surface 1o of the heat storage tank is covered with a steel plate or the like for improving the weather resistance (not shown), and the inner surface 1i is subjected to appropriate measures such as lowering the foaming rate of the resin to withstand the heat and erosion of the heat storage material hs. Is also optional. Moreover, in order to supplement mechanical strength, it is also possible to reinforce appropriately with steel materials or the like.
The heat exchanger 2 is formed with an internal flow path through which a heat medium hr to be heat exchanged with the heat storage material hs flows. For example, normal temperature clean water sw is supplied as the heat medium hr to the heat storage material. It receives heat from hs and is sent out of the tank as preheated water hw.

〔構成1・2〕
図2は〔構成1・2〕の発明に係わる発明の他の実施形態を示す概念図(斜視透視模式図)である。本構成では、蓄熱槽1を立方体形状にし、熱交換器2を蛇管状に形成している。これにより、蓄熱槽1の外形を「角形」とすることができ、「丸形」槽の外部を鋼板にて「角形」に被覆する場合に比べて、蓄熱量を増大させることが可能になる。
更には、「丸形」、「角形」に拘泥する必要はなく、蓄熱槽1を利用する装置全体の形状を考慮して、余剰空間等の活用を含めた自在な形状に成型することも可能である。
[Configuration 1 and 2]
FIG. 2 is a conceptual diagram (perspective perspective schematic diagram) showing another embodiment of the invention relating to the invention of [Configuration 1 and 2]. In this configuration, the heat storage tank 1 has a cubic shape, and the heat exchanger 2 has a serpentine shape. Thereby, the external shape of the heat storage tank 1 can be made into a "square", and it becomes possible to increase heat storage compared with the case where the outside of a "round" tank is covered with a "square" with a steel plate. .
Furthermore, there is no need to be concerned with “round” or “square”, and it can be molded into any shape including the use of surplus space in consideration of the overall shape of the device using the heat storage tank 1. It is.

〔構成3〕
図3は〔構成3〕に係わる発明の実施形態を示す概念図(斜視透視模式図)である。
耐熱性、封液性に優れた樹脂シート(例えばフッ素樹脂シート)3を袋状に成型したもので、先述の蓄熱槽1の内面を覆っている。この樹脂シート3は,先に説明したシート状材料に該当し、上部に開口3oを有する袋状に形成されており、内部に蓄熱材hsを収納して、蓄熱材hsの大気開放面が形成される。本シート3は槽内面に化学的に一体として製膜してもよいし、適当な接着剤で接着してもよい。更には、厚めのシートの場合機械的に固定しても良いし、金属薄板(箔)等の保形成のあるシートの場合には、全く接合しなくてもよい。
[Configuration 3]
FIG. 3 is a conceptual diagram (perspective perspective schematic diagram) showing an embodiment of the invention relating to [Configuration 3].
A resin sheet (for example, a fluororesin sheet) 3 excellent in heat resistance and sealing property is molded into a bag shape, and covers the inner surface of the heat storage tank 1 described above. The resin sheet 3 corresponds to the sheet-like material described above, and is formed in a bag shape having an opening 3o at the top, and the heat storage material hs is accommodated therein to form an air release surface of the heat storage material hs. Is done. The sheet 3 may be formed as a film integrally with the tank inner surface or may be bonded with an appropriate adhesive. Furthermore, in the case of a thick sheet, it may be fixed mechanically, or in the case of a sheet having a preserving shape such as a metal thin plate (foil), it may not be joined at all.

〔構成5・6・7〕
図4は、本発明を熱源機であるコジェネレーション機器等の蓄熱槽として利用した場合〔構成6〕の実施形態を示す概念図である。
蓄熱槽1に開口5を穿孔した蓋4をかぶせ、コージェネレーション機器50である熱源機と結ぶ配管51,52を取付けたものである。蓄熱材hsは水wであるが、蒸発を抑えるためと潜熱を利用するために、パラフィン層6を水面に浮かべている〔構成7〕。
[Configuration 5, 6, 7]
FIG. 4 is a conceptual diagram showing an embodiment of [Configuration 6] when the present invention is used as a heat storage tank of a cogeneration device or the like that is a heat source device.
The heat storage tank 1 is covered with a lid 4 having a perforated opening 5, and pipes 51 and 52 connected to a heat source machine that is a cogeneration device 50 are attached. Although the heat storage material hs is water w, the paraffin layer 6 is floated on the water surface in order to suppress evaporation and use latent heat [Configuration 7].

熱源機50に向かう水wは蓄熱槽下部の低温層1Lから抜き出され、コージェネレーション機器50を冷却することで熱を得て昇温され、蓄熱槽上部1Uに返される。水wの流量は制御され、層上部1Uに高温の一定温度(例えば80℃)で返されるのが通常である。図4の場合、熱媒体hrは上水swであり、熱交換器を成すコイル下部CLから導入されて、上部CUから取出され予熱水hwとなり給湯に使用される。   The water w toward the heat source unit 50 is extracted from the low temperature layer 1L at the lower part of the heat storage tank, is cooled by the cogeneration device 50, is heated, and is returned to the upper part 1U of the heat storage tank. The flow rate of the water w is controlled, and is usually returned to the upper layer 1U at a constant temperature (for example, 80 ° C.). In the case of FIG. 4, the heat medium hr is clean water sw, which is introduced from the coil lower part CL constituting the heat exchanger, is taken out from the upper part CU, becomes preheated water hw, and is used for hot water supply.

蓄熱材hsである水wは全体として蓄熱槽1の上部1Uから下部1Lへと下降して流れ、熱媒体hrである上水swはコイル下部CLから上部CUへと旋回しながら上昇して流れ、両者は全体として対向流的に接触し、能率良く熱交換が成される〔構成5〕。また、熱交換の結果、蓄熱槽1内の水wには、下方から上方に向かって温度が上昇する傾斜的な温度分布が形成・維持される。   The water w as the heat storage material hs flows downward from the upper part 1U of the heat storage tank 1 to the lower part 1L as a whole, and the upper water sw as the heat medium hr flows upward while swirling from the coil lower part CL to the upper part CU. As a whole, they are in counterflow contact with each other, and heat exchange is efficiently performed [Configuration 5]. Further, as a result of the heat exchange, an inclined temperature distribution in which the temperature rises from below to above is formed and maintained in the water w in the heat storage tank 1.

上記の蓄熱槽1では、熱源機50で加熱された蓄熱材は蓄熱槽上部にもどされ、熱交換器内を流れる熱媒体と熱交換を行い、冷却された蓄熱材が蓄熱槽下部から、熱源機50に送られる。従って、蓄熱材は蓄熱槽ないで温度成層を成す。 In the heat storage tank 1, the heat storage material heated by the heat source unit 50 is returned to the upper part of the heat storage tank, heat exchange is performed with the heat medium flowing in the heat exchanger, and the cooled heat storage material is supplied from the lower part of the heat storage tank to the heat source. Sent to machine 50. Therefore, the heat storage material forms a temperature stratification without a heat storage tank.

〔構成4〕
図5は、上記の構成を更に改善し、蓄熱槽上方の全面を気密に覆う蓋4を取付けると共に、蓄熱槽1を断面ドーナツ状に形成して中心部に配線・配管スペース(配管スペースの一種)7を設け、全ての配管pcを配線・配管スペース7を通じて、蓄熱槽の下に取出すことのできるように構成した蓄熱槽1〔構成4〕の例を示す断面模式図である。図5(a)は上下方向の断面である縦断面図を示し、図5(b)は水平方向の断面である横断面図を示している。当然、このスペース7を介して外部に設けられた制御機器と蓄熱槽内に設けられた各機器との配線を行うこともできる(図示省略)。
[Configuration 4]
FIG. 5 shows a further improvement of the above configuration, and a lid 4 that covers the entire upper surface of the heat storage tank in an airtight manner is attached, and the heat storage tank 1 is formed in a cross-sectional donut shape so that wiring / pipe space (a type of pipe space) ) Is a schematic cross-sectional view showing an example of a heat storage tank 1 [Configuration 4] configured so that all the pipes pc can be taken out under the heat storage tank through the wiring / pipe space 7. 5A shows a vertical cross-sectional view that is a cross section in the vertical direction, and FIG. 5B shows a cross-sectional view that is a cross section in the horizontal direction. Of course, it is also possible to perform wiring between the control device provided outside via the space 7 and each device provided in the heat storage tank (not shown).

本図には、熱源温水の供給・排出を担う熱源機との接続配管51、52を示すとともに、給湯用コイル2だけでなく、暖房用コイル2´をも併設した例を示している。更に、追焚き用等のコイル(図示せず)を設けることも容易である。
蓄熱槽1の大気への開放は、配線・配管スペース7もしくはオーバーフロー管70を通じて行われる。本構成の場合、配管取出し部の断熱・気密が不完全でも、蓄熱槽1の大気開放面ASからの自然対流による放熱を抑止することができ、しかも蓄熱槽1と蓋4を配管pc(配線を行った場合は配線も含む)が貫通することがないため、封液性、気密性に関する信頼度が高い。
図示する例では、蓄熱槽1内の水wを適宜排水可能とすべく排水機構55を設けている。この排水機構55は、蓄熱槽1における熱の外部との授受に関しては、実質的な影響は少ない。
This figure shows an example in which not only the hot water supply coil 2 but also the heating coil 2 ′ is provided together with the connection pipes 51 and 52 connected to the heat source machine responsible for supplying and discharging the heat source hot water. Furthermore, it is easy to provide a coil (not shown) for chasing.
The heat storage tank 1 is opened to the atmosphere through the wiring / piping space 7 or the overflow pipe 70. In the case of this configuration, even if heat insulation and airtightness of the pipe take-out portion are incomplete, heat radiation due to natural convection from the atmosphere open surface AS of the heat storage tank 1 can be suppressed, and the heat storage tank 1 and the lid 4 are connected to the pipe pc (wiring). In the case of carrying out (including wiring), there is no penetration, so the reliability with respect to sealing and airtightness is high.
In the illustrated example, a drainage mechanism 55 is provided so that the water w in the heat storage tank 1 can be drained as appropriate. The drainage mechanism 55 has little substantial effect on the exchange of heat with the outside in the heat storage tank 1.

〔構成6〜11〕
図6は、小型SOFC(固体酸化物型燃料電池)に本発明の蓄熱槽1を適用した場合の実施形態を示す流れ図である。
[Configurations 6 to 11]
FIG. 6 is a flowchart showing an embodiment when the heat storage tank 1 of the present invention is applied to a small SOFC (solid oxide fuel cell).

小型SOFC10は、セルスタック11、予備改質器12、蒸発器13、インバーター14、空気予熱器15、排熱回収熱交換器16、純水装置17、純水貯槽18及び蓄熱槽1等から構成される。また、ガス湯沸器20が燃料電池故障時及び回収排熱の加温用に付随している。この純水装置17は、上水swから純水を製造する装置である。   The small SOFC 10 includes a cell stack 11, a pre-reformer 12, an evaporator 13, an inverter 14, an air preheater 15, an exhaust heat recovery heat exchanger 16, a pure water device 17, a pure water storage tank 18, a heat storage tank 1, and the like. Is done. In addition, the gas water heater 20 is attached when the fuel cell fails and for heating the recovered exhaust heat. The pure water device 17 is a device for producing pure water from the clean water sw.

蓄熱槽1に貯留された蓄熱材hs(水w)は、槽下部1Lから抜き出され、排熱回収熱交換器16で燃料電池燃焼排ガスから排熱回収を行って加熱され、蓄熱槽1の上部1Uに戻される。この循環は、ポンプ19´にて行われるが、蓄熱槽1に戻る温度が略80℃一定となるように制御される。なお、蓄熱槽1は、上部に通気口5を設けると共に、水蒸気が通気口5から漏れ出さないように、パラフィン6にて水面を覆っている。
さらにオーバフロー管70が設けられるとともに、図示する例では、蓄熱槽1内の水wを適宜排水可能とすべく排水機構55を設けている。
The heat storage material hs (water w) stored in the heat storage tank 1 is extracted from the tank lower part 1L, heated by exhaust heat recovery from the fuel cell combustion exhaust gas by the exhaust heat recovery heat exchanger 16, and stored in the heat storage tank 1. Returned to the upper 1U. This circulation is performed by the pump 19 ′, and is controlled so that the temperature returning to the heat storage tank 1 is constant at about 80 ° C. In addition, the heat storage tank 1 is provided with a vent hole 5 at the top and covers the water surface with paraffin 6 so that water vapor does not leak from the vent hole 5.
Further, an overflow pipe 70 is provided, and in the illustrated example, a drainage mechanism 55 is provided so that the water w in the heat storage tank 1 can be drained appropriately.

上水swは熱交換器2の下部1Lから上部1Uに向けて流通させることにより、上部1Uが高温である蓄熱材hsと対向流的に接触・熱交換して加熱される。この時、蓄熱槽下部1Uの蓄熱材hs(水w)は、冷却されて低温に維持される結果、排熱回収や熱源機冷却に冷却水として使用できる〔構成10〕。予熱水hwはガス湯沸器20にて温度調節をされて、給湯に使用される〔構成11〕。   By flowing the water sw from the lower part 1L of the heat exchanger 2 toward the upper part 1U, the upper part 1U is heated by contacting and exchanging heat with the heat storage material hs having a high temperature. At this time, the heat storage material hs (water w) in the lower part 1U of the heat storage tank is cooled and maintained at a low temperature, so that it can be used as cooling water for exhaust heat recovery and heat source cooling [Configuration 10]. The temperature of the preheated water hw is adjusted by the gas water heater 20 and used for hot water supply [Configuration 11].

なお、本湯沸器20は、PID制御にてガス量を調節すると共に自動ミキシングバルブ23にて湯水混合を行い、温度センサ24´で検知される出湯温度を設定温度となるように制御する。ただし、給湯器20への入り水温が温度センサ24にて設定温度より高いと検知された場合には、ミキシングバルブ23´にて上水swと混合し、熱交換器22をバイパスして設定温度の給湯を行うように構成されている。   The hot water heater 20 adjusts the amount of gas by PID control and mixes hot water with the automatic mixing valve 23 so as to control the hot water temperature detected by the temperature sensor 24 ′ to be a set temperature. However, when it is detected by the temperature sensor 24 that the temperature of water entering the water heater 20 is higher than the set temperature, it is mixed with the clean water sw by the mixing valve 23 ′, bypassing the heat exchanger 22, and the set temperature. It is configured to perform hot water supply.

図7には、先に図6を用いて説明した小型SOFCとほぼ同様な構成において、蓄熱槽1内に更なる熱交換器であるコイルCを設け、排熱回収及び回収された熱の蓄熱材hsへの供給を独立の熱媒体回路で行う例である。従って、この熱媒体回路R1は、排熱回収熱交換器16と蓄熱槽1内に設けられたコイルCとの間をポンプ19´を利用して熱媒体を循環させる構造としている。この構造を採用することで、排熱回収、回収された熱の蓄熱材への供給を熱授受の観点から独立に制御可能となる。換言すると、蓄熱槽1内の蓄熱材hs(水w)の量の調整に関係なく行える。更には、給湯水と熱媒体回路R1を流れる熱媒体とは管壁で二重に隔てられているため、いずれかに腐食による微小な孔あきがあった場合にも、両者が混合することがなく、給湯水は衛生的に保たれる。   In FIG. 7, a coil C, which is a further heat exchanger, is provided in the heat storage tank 1 in a configuration almost the same as that of the small SOFC described with reference to FIG. 6, and exhaust heat recovery and heat storage of the recovered heat are performed. In this example, the supply to the material hs is performed by an independent heat medium circuit. Accordingly, the heat medium circuit R1 has a structure in which the heat medium is circulated between the exhaust heat recovery heat exchanger 16 and the coil C provided in the heat storage tank 1 by using the pump 19 '. By adopting this structure, exhaust heat recovery and supply of recovered heat to the heat storage material can be controlled independently from the viewpoint of heat transfer. In other words, it can be performed regardless of the adjustment of the amount of the heat storage material hs (water w) in the heat storage tank 1. Furthermore, since the hot water and the heat medium flowing through the heat medium circuit R1 are doubly separated by the tube wall, even if there is a minute perforation due to corrosion, both can be mixed. No hot water is kept hygienic.

図8は、小型SOFCに本発明の蓄熱槽1を適用した場合の他の実施形態を示す流れ図である。この例では、排熱回収熱交換器16にて冷却され、生成した凝縮水〔構成10〕を蓄熱槽1の中程の位置に返して、純水装置17で製造された純水と併せて蓄熱材hs(水w)として使用している〔構成8〕。これにより、純水の貯槽(図6、図7における18)を省略するとともに、凝縮水の顕熱をも有効に回収できるようにしている。   FIG. 8 is a flowchart showing another embodiment when the heat storage tank 1 of the present invention is applied to a small SOFC. In this example, the condensed water [Configuration 10] cooled by the exhaust heat recovery heat exchanger 16 is returned to the middle position of the heat storage tank 1, and combined with the pure water produced by the pure water device 17. It is used as the heat storage material hs (water w) [Configuration 8]. Thus, the storage tank for pure water (18 in FIGS. 6 and 7) is omitted, and the sensible heat of the condensed water can be effectively recovered.

蓄熱槽1に蓄えられた純水は、その下部が上水swで冷却された後、排熱回収熱交換器16に送られて排熱回収に使用され、蓄熱槽上部1Uに高温水として蓄えられる。この時、燃料電池排ガスは冷却されて凝縮水を分離するため、上述のように、凝縮水を純水の一部として蓄熱槽1に蓄えて使用することとなる。   The pure water stored in the heat storage tank 1 is cooled at the lower part with clean water sw, then sent to the exhaust heat recovery heat exchanger 16 to be used for exhaust heat recovery, and stored as high temperature water in the upper part 1U of the heat storage tank. It is done. At this time, since the fuel cell exhaust gas is cooled to separate the condensed water, the condensed water is stored in the heat storage tank 1 as a part of pure water as described above.

蓄熱槽上部1Uには温度の高い(例えば80℃)純水が蓄えられるため、これを抜き出して蒸発器13に供給〔構成9〕すれば、純水の予熱に必要な分の伝熱面積が省略でき、コストダウンとコンパクト化に繋がる。
上水swの給湯利用、及び小型SOFCの他の構成は、図6、図7に基づいて説明した例と同様である。
Since high temperature (for example, 80 ° C.) pure water is stored in the upper part 1U of the heat storage tank, if this is extracted and supplied to the evaporator 13 [Configuration 9], the heat transfer area required for preheating pure water is increased. This can be omitted, leading to cost reduction and downsizing.
The use of the hot water sw for the hot water supply and the other configurations of the small SOFC are the same as those described with reference to FIGS.

〔構成12〕
図6から図8に示す例では、本願に係る大気開放型蓄熱槽1を小型SOFCに適用する例を示したが、以下の図9、図10に示す例は、複数の熱需要家110(給湯先)に対して、共有・単一若しくは複数のコジェネレーション機器111(例えば燃料電池)を共有敷地内に設け、共有のコジェネレーション機器111から発生する熱を利用し、例えば90℃の熱源温水HWを各熱需要家110を巡る形態で供給し、別途各熱需要家110に供給されている上水swを利用して給湯を行うことが可能なシステムに、本願に係る大気開放型蓄熱槽1を使用する例について説明する。無論、この構成の大気開放型蓄熱槽1を、図6〜8に示された小型SOFCに適用することもできる。
[Configuration 12]
In the example shown in FIGS. 6 to 8, an example in which the open air heat storage tank 1 according to the present application is applied to a small SOFC has been shown. However, the examples shown in FIGS. 9 and 10 below include a plurality of heat consumers 110 ( A common / single or a plurality of cogeneration devices 111 (for example, fuel cells) are provided in a common site for the hot water supply destination), and heat generated from the shared cogeneration device 111 is used, for example, 90 ° C. heat source hot water An open air heat storage tank according to the present application is provided in a system that can supply HW in a form that goes around each heat consumer 110 and can supply hot water using the water sw separately supplied to each heat consumer 110. An example using 1 will be described. Of course, the open air heat storage tank 1 having this configuration can also be applied to the small SOFC shown in FIGS.

図6から図8に示す例では、都市ガスg及び水(通常は上水swであり、この上水は常温で供給される)の供給を受けて、システムは電気e及び湯hwの供給が可能であったのに対して、図9及び図10に示す例では、コジェネレーション機器111側で行われる電気eの供給に関しては記載を省略し、各熱需要家110において、水(上水sw)の供給を受けるとともに、コジェネレーション機器111側で発生された熱源温水HWの供給を受け、給湯に加え、風呂の追い焚き及び暖房温水の再加熱を行うシステムとされている。   In the examples shown in FIG. 6 to FIG. 8, the system is supplied with electricity e and hot water hw upon receiving supply of city gas g and water (usually clean water sw, which is supplied at room temperature). In the example shown in FIG. 9 and FIG. 10, the description of the supply of electricity e performed on the cogeneration device 111 side is omitted, and in each heat consumer 110, water (clean water sw ) And the supply of heat source hot water HW generated on the cogeneration device 111 side, and in addition to hot water supply, the system reheats the bath and reheats the heated hot water.

図9は、所謂「隣組コジェネシステム」に、本発明の蓄熱槽1を適用した場合の各熱需要家110(給湯先)の実施形態を示す流れ図である。
同図下側に本願に係る大気開放型蓄熱槽1を、上側に、熱源温水HWの循環路112、給水路113、給湯路114、暖房温水回路115の入側115i及び出側115o、風呂追い焚き回路116の入側116i及び出側116oを示している。
FIG. 9 is a flowchart showing an embodiment of each heat consumer 110 (hot water supply destination) when the heat storage tank 1 of the present invention is applied to a so-called “neighboring assembly cogeneration system”.
In the lower part of the figure, the open-air heat storage tank 1 according to the present application is shown, and on the upper side, the circulation path 112 of the heat source hot water HW, the water supply path 113, the hot water supply path 114, the inlet side 115i and the outlet side 115o of the heating hot water circuit 115, The entry side 116i and the exit side 116o of the winding circuit 116 are shown.

熱源温水HWは、循環路112の上流側に設けられた共有の燃料電池設備であるコジェネレーション機器111から発生する排熱等により所定温度(例えば90℃)の温水として得られ、熱源温水HWが内部を循環する形態で、各需要家110に送られてくる。熱源温水HWの循環路112には、この循環路112の上流側部位から熱源温水HWを取り出してその供給を受ける供給部112aと、この供給部112aより循環路下流側部位に熱源温水HWを戻す戻り部112bが設けられている。そして、供給部112aと戻り部112bとの間の熱源温水流路RHWは、大気開放型蓄熱槽1内に設けられた熱交換器HC内を介する構成とされている。   The heat source hot water HW is obtained as hot water of a predetermined temperature (for example, 90 ° C.) by exhaust heat generated from the cogeneration device 111 that is a shared fuel cell facility provided on the upstream side of the circulation path 112. It is sent to each consumer 110 in a form that circulates inside. In the circulation path 112 of the heat source hot water HW, the heat source hot water HW is taken out from the upstream portion of the circulation passage 112 and supplied thereto, and the heat source hot water HW is returned from the supply portion 112a to the downstream portion of the circulation path. A return portion 112b is provided. And the heat-source hot water flow path RHW between the supply part 112a and the return part 112b is set as the structure via the heat exchanger HC provided in the air release type | formula heat storage tank 1. FIG.

この熱源温水用の熱交換は、図9に示すように、蓄熱槽上部1Uに配設される上部熱交換器HCUと、蓄熱槽下部1Lに設けられる下部熱交換器HCLと、両熱交換器HCU,HCL内に形成された両熱媒体流路を蓄熱槽上下方向に短絡する短絡流路を形成する短絡配管SPとを組み合わせて構成されている。   As shown in FIG. 9, the heat exchange for the heat source hot water is performed by using an upper heat exchanger HCU provided in the upper part 1U of the heat storage tank, a lower heat exchanger HCL provided in the lower part 1L of the heat storage tank, and both heat exchangers. It is configured by combining a short-circuit pipe SP that forms a short-circuit channel that short-circuits both heat medium channels formed in the HCU and HCL in the vertical direction of the heat storage tank.

そして、供給部112aから供給される熱源温水HWは上部熱交換器HCU、短絡流路SP、下部熱交換器HCLの順に内部を流れ、戻り部112bに戻る構成とされている。   The heat source hot water HW supplied from the supply unit 112a flows through the upper heat exchanger HCU, the short-circuit channel SP, and the lower heat exchanger HCL in this order, and returns to the return unit 112b.

給水路113及び給湯路114は、給水部113aから給湯部114aに直接給水が供給されるバイパス路brと、給水部113aから供給される上水swを蓄熱槽1内に導き、蓄熱槽1内に配設されている給湯タンクTにおいて所定の温度に昇温し、所定温度の給湯温水を給湯部114aに送る熱交換路RSWとを備えて構成されている。この構成を採用することにより、熱交換路RSWにあっては、蓄熱槽1内にある蓄熱材hs或いは熱源温水HWから受熱して、上水swから給湯温水が生成され、所定温の温水を供給することができる。   The water supply channel 113 and the hot water supply channel 114 lead the bypass water br supplied directly from the water supply unit 113a to the hot water supply unit 114a and the clean water sw supplied from the water supply unit 113a into the heat storage tank 1, In the hot water supply tank T provided in FIG. 2, the heat exchange path RSW is configured to be heated to a predetermined temperature and send hot water at a predetermined temperature to the hot water supply section 114a. By adopting this configuration, in the heat exchange path RSW, heat is received from the heat storage material hs or the heat source hot water HW in the heat storage tank 1, hot water supply hot water is generated from the tap water sw, and hot water having a predetermined temperature is supplied. Can be supplied.

熱源温水HWの回路RHWと熱媒体である上水swの回路RSWとの間にもバイパス路BRを設け、給湯温が充分でない場合は、熱源温水を給湯温水に直接混合することもできるように構成されている。   A bypass path BR is also provided between the circuit RHW of the heat source hot water HW and the circuit RSW of the hot water sw that is the heat medium so that the hot source hot water can be directly mixed with the hot water hot water when the hot water supply temperature is not sufficient. It is configured.

暖房温水回路115は、その入側115iにおいて暖房作動により温度低下した温水を受け入れ、その出側115oから蓄熱槽1で加熱された温水を暖房機器115a側に戻す。
この暖房用の温水の熱交換は、図9に示すように、蓄熱槽上部1Uに配設される少なくとも上部熱交換器hcuにより行われるように構成されている。この構成を採用することにより、蓄熱槽上部1Uにある蓄熱材hs或いは熱源温水HWから熱の供給を受けて、暖房用の温水は適切に昇温されて暖房機器115aに戻される。
The heating hot water circuit 115 accepts hot water whose temperature has decreased due to the heating operation on the entry side 115i, and returns the warm water heated in the heat storage tank 1 from the exit side 115o to the heating equipment 115a side.
As shown in FIG. 9, the heat exchange of the warm water for heating is configured to be performed by at least the upper heat exchanger hcu disposed in the heat storage tank upper portion 1U. By adopting this configuration, heat is supplied from the heat storage material hs or the heat source hot water HW in the heat storage tank upper part 1U, and the warm water for heating is appropriately heated and returned to the heating device 115a.

追い焚き回路116は、その入側116iにおいて温度低下した風呂水を受け入れ、その出側116oから蓄熱槽1で加熱された風呂水を浴槽116aに戻す。
この風呂水の熱交換は、図9に示すように、蓄熱槽上部1Uに配設される少なくとも上部熱交換器hcu及び蓄熱槽下部1Lに設けられる下部熱交換器hclと、両熱交換器hcu、hcl内に形成された両熱媒体流路を蓄熱槽上下方向に短絡する短絡流路を形成する短絡配管spとを組み合わせて構成されている。
この風呂水は、下部熱交換器hcl、短絡流路sp、上部熱交換器hcuの順に内部をながれ、予熱された後、上部熱交換器hcuで充分に昇温されて風呂に戻される。
The reheating circuit 116 accepts the bath water whose temperature has decreased on the entry side 116i, and returns the bath water heated in the heat storage tank 1 from the exit side 116o to the bathtub 116a.
As shown in FIG. 9, the heat exchange of the bath water is performed by at least the upper heat exchanger hcu provided in the heat storage tank upper part 1U and the lower heat exchanger hcl provided in the heat storage tank lower part 1L, and the both heat exchangers hcu. , Hcl is formed by combining a short-circuit pipe sp that forms a short-circuit channel that short-circuits both heat medium channels formed in hcl in the vertical direction of the heat storage tank.
The bath water flows through the lower heat exchanger hcl, the short-circuit channel sp, and the upper heat exchanger hcu in this order and is preheated, and then is sufficiently heated by the upper heat exchanger hcu and returned to the bath.

結果、熱源温水から受熱して効率的に各用途での熱利用を図ることができる。   As a result, it can receive heat from the heat source hot water and efficiently use heat in each application.

〔構成13〕
図10も、所謂「隣組コジェネシステム」に、本発明の蓄熱槽1を適用した場合の各熱需要家110(給湯先)の実施形態を示す流れ図である。
同図下側に本願に係る大気開放型蓄熱槽1を、上側に、熱源温水HWの循環路112、給水路113、給湯路114、暖房温水回路115の入側115i及び出側115o、風呂追い焚き回路116の入側116i及び出側116oを示している。
[Configuration 13]
FIG. 10 is also a flowchart showing an embodiment of each heat consumer 110 (hot water supply destination) when the heat storage tank 1 of the present invention is applied to a so-called “neighboring cogeneration system”.
In the lower part of the figure, the open-air heat storage tank 1 according to the present application is shown, and on the upper side, the circulation path 112 of the heat source hot water HW, the water supply path 113, the hot water supply path 114, the inlet side 115i and the outlet side 115o of the heating hot water circuit 115, The entry side 116i and the exit side 116o of the winding circuit 116 are shown.

熱源温水HW(本願における第1熱媒体に相当)の循環に関しては、先に図9で説明したと同様であるので、説明を省略する。   The circulation of the heat source hot water HW (corresponding to the first heat medium in the present application) is the same as that described above with reference to FIG.

給水路113、給湯路114は、給水部113aから給湯部114aに直接給水が供給されるバイパス路brと、給水部113aに供給される上水swを蓄熱槽1内に導き、蓄熱槽1内に配設されている下部熱交換器hcl、短絡路sp、上部熱交換器hcuを経て所定の温度に昇温し、得られた温水を給湯部114aに送る熱交換路RSWとを備えて構成されている。この構成を採用することにより、熱交換路RSWにあっては、蓄熱槽1内にある蓄熱材hs或いは熱源温水HWから受熱して、上水swから温水が生成され、所定温の温水を供給することができる。   The water supply passage 113 and the hot water supply passage 114 lead the bypass water br supplied directly from the water supply portion 113a to the hot water supply portion 114a and the water sw supplied to the water supply portion 113a into the heat storage tank 1, And a heat exchange path RSW that raises the temperature to a predetermined temperature via the lower heat exchanger hcl, the short circuit path sp, and the upper heat exchanger hcu, and sends the obtained hot water to the hot water supply unit 114a. Has been. By adopting this configuration, in the heat exchange path RSW, heat is received from the heat storage material hs or the heat source hot water HW in the heat storage tank 1, hot water is generated from the clean water sw, and hot water of a predetermined temperature is supplied. can do.

暖房温水回路115(この回路内を流れる温水が本願における第2熱媒体に相当する)及び追い焚き回路116は、先に図9において説明したと同様であるため、説明を省略する。   The heating / warming water circuit 115 (the warm water flowing in this circuit corresponds to the second heat medium in the present application) and the reheating circuit 116 are the same as those described above with reference to FIG.

さて、図10からも判明するように、蓄熱材hsが熱媒体に授熱する第1熱交換部HC1を蓄熱槽上部1Uに設け、授熱により温度低下した蓄熱材hsを蓄熱槽上部1Uから蓄熱槽下側1Lに導く蓄熱材下降路を形成する下降路形成部材117が設けられている。この下降路形成部材117の上側端は、大きな断面積を有し、蓄熱材hsが熱媒体に授熱する前記第1熱交換部HC1をその内部に形成するように構成されており、蓄熱材熱交換部下側端に蓄熱材開放口117bが設けられている。この蓄熱材開放口117bから流出する蓄熱材hsに授熱する第2熱交換部HC2が設けられている。
結果、この構成にあっては、下降路形成部材117を設けることで、図10に矢印で示すように、蓄熱槽1内に、中心側で下降流となり外径側で上昇流となる蓄熱材hsが効率的に循環する循環対流を良好に形成でき、熱源温水HWから受熱して効率的に各用途での熱利用を図ることができる。
Now, as can be seen from FIG. 10, the first heat exchange part HC1 that heats the heat storage material hs to the heat medium is provided in the upper part 1U of the heat storage tank, and the heat storage material hs whose temperature has decreased due to heat transfer is provided from the upper part 1U of the heat storage tank. A descending path forming member 117 is provided to form a heat storage material descending path leading to the heat storage tank lower side 1L. The upper end of the descending path forming member 117 has a large cross-sectional area, and is configured to form therein the first heat exchanging part HC1 that heats the heat medium to the heat medium. A heat storage material opening 117b is provided at the lower end of the heat exchange section. A second heat exchange part HC2 for providing heat to the heat storage material hs flowing out from the heat storage material opening 117b is provided.
As a result, in this configuration, by providing the descending path forming member 117, as shown by the arrow in FIG. 10, the heat storage material that becomes a downward flow on the center side and an upward flow on the outer diameter side in the heat storage tank 1. A circulation convection in which hs circulates efficiently can be formed satisfactorily, and heat can be received from the heat source hot water HW to efficiently use heat in each application.

〔構成14・15〕
図11は、本願に係る大気開放型蓄熱槽を備え、コジェネレーション機器150(例えば燃料電池)からの排熱を給湯に利用可能に構成したものである。
これまで説明したように、この例にあっても大気開放型蓄熱槽は、蓄熱材hsを貯留してその貯留した蓄熱材hsの上面より高い位置に大気に通じる開口145を有する貯槽141と、貯槽141内に貯留された蓄熱材hsと内部を流れる熱媒体との熱交換を行う熱交換器142とを備えて構成され、給水を加熱して給湯することが可能とされている。この例では熱交換器142はコイル熱交換器であり、貯槽内部に貯留された蓄熱材hsを循環させるための循環流動付与手段Vが備えられている。
[Configuration 14 and 15]
FIG. 11 includes an open air heat storage tank according to the present application, and is configured such that exhaust heat from a cogeneration device 150 (for example, a fuel cell) can be used for hot water supply.
As described above, even in this example, the open air heat storage tank has a storage tank 141 that stores the heat storage material hs and has an opening 145 that leads to the atmosphere at a position higher than the upper surface of the stored heat storage material hs; The heat storage material hs stored in the storage tank 141 and the heat exchanger 142 that performs heat exchange between the heat medium flowing inside the storage tank 141 are provided, and the water supply can be heated to supply hot water. In this example, the heat exchanger 142 is a coil heat exchanger, and is provided with a circulation flow imparting means V for circulating the heat storage material hs stored in the storage tank.

大気開放型蓄熱槽は、蓄熱材hsとして水wを用いており、高温の温水を上部に且つ低温の水を下部に貯留させて温度成層を形成する状態で水wを貯留する。この蓄熱材hsは、コジェネレーション機器150の冷却水としても使用され、コジェネレーション機器150から発生する排熱を利用可能に構成されている。貯槽141は、合成樹脂にて有底筒状に形成されている。合成樹脂としては、例えば、ポリプロピレン等を用いることができるが、銅イオンに対して変性劣化しにくい銅害防止グレードを用いることが好ましい。   The open air heat storage tank uses water w as the heat storage material hs, and stores the water w in a state where high temperature hot water is stored in the upper part and low temperature water is stored in the lower part to form a temperature stratification. The heat storage material hs is also used as cooling water for the cogeneration device 150, and is configured to be able to use exhaust heat generated from the cogeneration device 150. The storage tank 141 is formed of a synthetic resin in a bottomed cylindrical shape. As the synthetic resin, for example, polypropylene or the like can be used, but it is preferable to use a copper damage prevention grade that hardly changes and deteriorates with respect to copper ions.

前記貯槽141は、平面視が矩形状の下部貯槽141Lと上部に開口145が設けられて平面視が同じく矩形状の上部貯槽141Uとを連通する状態で備えて構成されている。具体的には、前記下部貯槽141Lの上部の一部(図において左側端)と上部貯槽141Uの下部の一部(図において右側端)とが連通され、内部に貯留される蓄熱材hsが流通可能に構成されている。また、平面視において上部貯槽141Uの断面積を下部貯槽141Lの断面積よりも小さくすることによって、貯槽141に貯留した蓄熱材hsと大気との界面部分の面積を界面部分以外の部分の断面積よりも小さくしている〔構成15〕。   The storage tank 141 is configured to include a lower storage tank 141L having a rectangular shape in plan view and an upper storage tank 141U having an opening 145 provided in the upper portion and also having a rectangular shape in plan view. Specifically, a part of the upper part of the lower storage tank 141L (left end in the figure) communicates with a part of the lower part of the upper storage tank 141U (right end in the figure), and the heat storage material hs stored inside flows. It is configured to be possible. In addition, by making the cross-sectional area of the upper storage tank 141U smaller than the cross-sectional area of the lower storage tank 141L in plan view, the area of the interface portion between the heat storage material hs stored in the storage tank 141 and the atmosphere is the cross-sectional area of the portion other than the interface portion. [Configuration 15].

前記上部貯槽141Uには、貯槽141における蓄熱材hsの水位が上限水位以上であることを検出する上限水位スイッチLSU、蓄熱材hsの水位が下限水位以下であることを検出する下限水位スイッチLSLが設けられている。そして、上部貯槽141Uには、蓄熱材hsの水位がオーバーフロー用水位になると、オーバーフローにより蓄熱材hsを排出するオーバーフロー路170が接続されている。
また、下部貯槽141Lの下部には、貯槽141に貯留されている蓄熱材hsを排出するための蓄熱材排出路145が接続され、その蓄熱材排出路145には蓄熱材排出弁146が設けられている。
The upper storage tank 141U includes an upper limit water level switch LSU for detecting that the water level of the heat storage material hs in the storage tank 141 is equal to or higher than the upper limit water level, and a lower limit water level switch LSL for detecting that the water level of the heat storage material hs is lower than the lower limit water level. Is provided. And the overflow path 170 which discharges | emits the heat storage material hs by overflow is connected to the upper storage tank 141U when the water level of the heat storage material hs becomes the overflow water level.
Further, a heat storage material discharge path 145 for discharging the heat storage material hs stored in the storage tank 141 is connected to a lower portion of the lower storage tank 141L, and a heat storage material discharge valve 146 is provided in the heat storage material discharge path 145. ing.

前記循環流動付与手段Vは、下部貯槽141Lの上側部位において蓄熱材hsを通流自在に連通する循環路Vaと、その循環路Vaを介して槽内141Lの蓄熱材hsを循環させる循環ポンプVbを備えて構成されている。そして、槽への戻しは槽壁の接線に沿った接線方向に行うように、槽からの蓄熱材の取り出しは前記接線方向とは槽壁に沿って逆方向となるように、循環路Vaが形成されている。また、図11に示すように、循環路Vaは、下部貯槽141Lの側部から取り出した蓄熱材hsを、下部貯槽141Lの側部で、取り出し部とほぼ同じ高さ位置に戻すように構成されている。結果、循環ポンプVpの働きにより、この下部貯槽141L内で蓄熱材hsを、ほぼ同一高さ位置で水平に循環流動させることができる〔構成14〕。   The circulation flow applying means V includes a circulation path Va that allows the heat storage material hs to flow freely in an upper portion of the lower storage tank 141L, and a circulation pump Vb that circulates the heat storage material hs in the tank 141L via the circulation path Va. It is configured with. The circulation path Va is set so that the return to the tank is performed in a tangential direction along the tangent line of the tank wall, and the heat storage material is removed from the tank in a direction opposite to the tangential direction along the tank wall. Is formed. Further, as shown in FIG. 11, the circulation path Va is configured to return the heat storage material hs taken out from the side portion of the lower storage tank 141 </ b> L to substantially the same height position as the extraction portion at the side portion of the lower storage tank 141 </ b> L. ing. As a result, by the action of the circulation pump Vp, the heat storage material hs can be circulated and flowed horizontally at substantially the same height position in the lower storage tank 141L [Configuration 14].

前記熱交換器142は、下部貯槽141L内に収納されるコイル熱交換器として構成されており、この熱交換器142には、給水路143から給水逆止弁OVを介して上水を供給可能に構成されている。熱交換器142の下流側はミキシングバルブMXVを介して給湯路144に接続される構成が採用されている。   The heat exchanger 142 is configured as a coil heat exchanger housed in the lower storage tank 141L, and can be supplied with clean water from the water supply path 143 via the water supply check valve OV. It is configured. A configuration is adopted in which the downstream side of the heat exchanger 142 is connected to the hot water supply path 144 via a mixing valve MXV.

前記給水路143には上水が供給され、給水路143には上水の給水圧が常時作用する。前記給水路143には、熱交換器142をバイパスする状態でバイパス路148が接続されている。給水路143において、バイパス路148の分岐箇所よりも上流側には、給水逆止弁OVが設けられている。   The supply water 143 is supplied with clean water, and the supply water pressure is always applied to the supply water 143. A bypass passage 148 is connected to the water supply passage 143 so as to bypass the heat exchanger 142. In the water supply path 143, a water supply check valve OV is provided on the upstream side of the branch point of the bypass path 148.

また、熱交換器142下流側のバイパス路148との合流箇所には、熱交換器142にて得られた温水とバイパス路148からの水とを混合して給湯路144に供給するとともに、給水路143からの温水とバイパス路148からの水との混合比を調整自在なミキシングバルブMXVが設けられている。   In addition, the hot water obtained by the heat exchanger 142 and the water from the bypass passage 148 are mixed and supplied to the hot water supply passage 144 at a junction with the bypass passage 148 on the downstream side of the heat exchanger 142, A mixing valve MXV capable of adjusting the mixing ratio of the hot water from the passage 143 and the water from the bypass passage 148 is provided.

前記給湯路144は、例えば、給湯栓等に接続されており、その上流側から、給湯路144を通流する給湯水の温度を検出する給湯温度センサT1、設定量以上の水量を検出するフロースイッチFSが設けられている。   The hot water supply path 144 is connected to, for example, a hot water tap or the like, and from the upstream side thereof, a hot water supply temperature sensor T1 that detects the temperature of hot water flowing through the hot water supply path 144, and a flow that detects a water amount greater than a set amount. A switch FS is provided.

前記上部貯槽141Uには、排熱往き路151によりコジェネレーション機器150等の排熱により加熱された高温の温水が供給されるように構成されている。従って、この貯槽141では、コジェネレーション機器150等の排熱を蓄熱することができる。
前記蓄熱材排出路145には、貯槽141にて排熱が回収された水をコジェネレーション機器150等に戻す排熱戻り路152が分岐接続されている。排熱戻り路152にて戻す水の温度が設定温度以上である状態では、その温水を排水路149を介して、温度の低い給水を導入するためのサーモバルブTMVが設けられている。尚、空冷熱交換器を用いて大気にて冷却することも可能である。このようにして、排熱戻り路152にてコジェネレーション機器150等に戻す水の温度を設定温度未満に保つことができ、貯槽141内の温度成層を良好に保つことができるようにしている。
The upper storage tank 141U is configured to be supplied with high-temperature hot water heated by exhaust heat from the cogeneration device 150 or the like through the exhaust heat outgoing path 151. Therefore, in the storage tank 141, exhaust heat from the cogeneration device 150 or the like can be stored.
The heat storage material discharge path 145 is branched and connected to an exhaust heat return path 152 that returns the water whose exhaust heat has been recovered in the storage tank 141 to the cogeneration device 150 or the like. In a state where the temperature of the water returned in the exhaust heat return path 152 is equal to or higher than the set temperature, a thermo valve TMV is provided for introducing the warm water through the drain path 149 into the low temperature water supply. In addition, it is also possible to cool in air | atmosphere using an air cooling heat exchanger. In this way, the temperature of the water returned to the cogeneration device 150 or the like in the exhaust heat return path 152 can be kept below the set temperature, and the temperature stratification in the storage tank 141 can be kept good.

前記バイパス路148には、貯槽141に蓄熱材hsとしての水を供給する蓄熱材供給路148aが分岐接続されている。そして、この蓄熱材供給路148aには、その上流側から、蓄熱材hsとしての水の供給を断続する蓄熱材供給用断続弁MV、蓄熱材供給用逆止弁OVが設けられている。蓄熱材供給用断続弁MVは、上部貯槽141Uに設けられた下限水位スイッチLSLに従って働くように構成されており、貯槽141内の蓄熱材hsの量が所定量を下回った状態で、給水を行うように構成されている。   A heat storage material supply path 148 a that supplies water as the heat storage material hs to the storage tank 141 is branched and connected to the bypass path 148. The heat storage material supply channel 148a is provided with a heat storage material supply intermittent valve MV and a heat storage material supply check valve OV for intermittently supplying water as the heat storage material hs from the upstream side. The heat storage material supply intermittent valve MV is configured to work in accordance with a lower limit water level switch LSL provided in the upper storage tank 141U, and supplies water in a state where the amount of the heat storage material hs in the storage tank 141 falls below a predetermined amount. It is configured as follows.

以下、このシステムの運転に関して説明する。
このシステムの運転は、貯槽141内に貯留される蓄熱材hsの量を適切に保つ蓄熱材供給運転と、給湯を適切に実行する給湯運転とに別れる。
The operation of this system will be described below.
The operation of this system is divided into a heat storage material supply operation that appropriately maintains the amount of the heat storage material hs stored in the storage tank 141 and a hot water supply operation that appropriately executes hot water supply.

蓄熱材供給運転
下限水位スイッチLSLにて蓄熱材hsの水位が下限水位以下であることを検出すると、蓄熱材供給用断続弁MVを開弁させて、給水路143、バイパス路148、蓄熱材供給路148aを通して、下部貯槽141Lに蓄熱材hsとしての水を供給して蓄熱材供給運転を行う。
上限水位スイッチLSUにて蓄熱材hsの水位が上限水位となったことを検出すると、蓄熱材供給用断続弁MVを閉弁させて、下部貯槽141Lへの蓄熱材hsの供給を停止して蓄熱材供給運転を停止する。
Heat storage material supply operation When the lower limit water level switch LSL detects that the water level of the heat storage material hs is equal to or lower than the lower limit water level, the heat storage material supply intermittent valve MV is opened, and the water supply path 143, the bypass path 148, and the heat storage material supply Water as the heat storage material hs is supplied to the lower storage tank 141L through the path 148a to perform the heat storage material supply operation.
When the upper water level switch LSU detects that the water level of the heat storage material hs has reached the upper limit water level, the heat storage material supply intermittent valve MV is closed to stop the supply of the heat storage material hs to the lower storage tank 141L to store heat. Stop the material supply operation.

給湯運転
給湯路144の下流側に設けられた給湯栓等が開かれてフロースイッチFSにて設定量以上の水量を検出すると、給水圧力を利用して、熱交換器142内を下部から上部に向かって上水を流し、温水を得る。前記熱交換器142では、下部貯槽141L内を下降する蓄熱材hsと、コイル内を上昇する水とが対向流形態で熱交換し蓄熱材hsにて温水を得ることとなる。さらにフロースイッチFSが設定量以上の水量を検出すると、循環流動付与手段Vを成す循環ポンプVpが作動され、槽内において蓄熱材hsは螺旋を描きながら下降され、熱伝達が促進される。
Hot-water supply operation When a hot-water tap or the like provided on the downstream side of the hot-water supply channel 144 is opened and the flow switch FS detects a water amount that exceeds a set amount, the water exchanger pressure is used to move the heat exchanger 142 from the lower part to the upper part. Run warm water to get warm water. In the heat exchanger 142, the heat storage material hs descending in the lower storage tank 141L and the water rising in the coil exchange heat in a counterflow manner to obtain hot water in the heat storage material hs. Further, when the flow switch FS detects an amount of water equal to or larger than the set amount, the circulation pump Vp constituting the circulation flow imparting means V is operated, and the heat storage material hs is lowered while drawing a spiral in the tank, thereby promoting heat transfer.

また、給湯温度制御に関しては、熱交換器142にて加熱された温水にバイパス路148からの水をミシングバルブMXVにて混合させるとともに、給湯温度センサT1の検出情報に基づいて給湯設定温度の温水を給湯路144にて給湯すべく、温水とバイパス路148からの水との混合比をミキングバルブMXVにて調整する。
そして、給湯栓等が閉じられてフロースイッチFSにて設定量以上の水量を検出しなくなると、作動が停止される。
As for the hot water supply temperature control, the hot water heated by the heat exchanger 142 is mixed with the water from the bypass 148 by the mixing valve MXV, and the hot water at the hot water supply set temperature is changed based on the detection information of the hot water supply temperature sensor T1. In order to supply hot water in the hot water supply path 144, the mixing ratio of warm water and water from the bypass path 148 is adjusted by the mixing valve MXV.
The operation is stopped when the hot water tap or the like is closed and the flow switch FS no longer detects the amount of water greater than the set amount.

この給湯運転においては、下部貯槽141Lの下部に到る蓄熱材hsが設定温度以下となるように、貯槽141とコージェネレーション機器150との間の蓄熱材hsの循環流量を制御する。即ち、サーモバルブTMVの検出温度が設定温度になるように、このバルブにより検出される検出温度が上昇した場合、コージェネレーション機器150側に戻る水を棄て、低温の上水が槽内に供給される。よって、前記設定温度は、貯槽141に形成される温度成層を乱すことがないような温度に設定されており、例えば、給水温度よりも5℃高い温度が設定されている。
〔別実施形態〕
(1)本願に係る貯槽の構成は、貯槽に使用される材料、強度との関係で適宜変更が可能である。
例えば、図12に示すように、貯槽を、複数の貯槽ユニット121を少なくとも上部同士及び下部同士において蓄熱材hsを流通自在に連通接続して構成することができる〔構成16〕。図12では、第1槽121a、第2槽121b、第3槽121cの3つの槽121を水平方向に並べる状態で配置し、水平方向に隣接するもの同士において上部同士及び下部同士を連通管120にて蓄熱材hsを通流自在に連通接続している。この場合、少なくとも上部同士及び下部同士で連通していればよく、上部、下部以外の中間部、全面等に亘って連通接続する構成としてもよい。
この場合、設置する貯槽ユニットの数は適宜変更が可能である。そして、複数の貯槽ユニットを上下方向に並べる状態で設置することも可能であり、複数の貯槽ユニットをどのように配置して設けるかは適宜変更が可能である。
また、各貯槽ユニットの上部及び下部に連通用開口を設けてその連通用開口同士を溶接等により接着して、各貯槽ユニットの上部同士及び下部同士を蓄熱材hsを通流自在に連通接続することもできる。
一方、第1槽121aの上部には、上部貯槽121Uが設けられており、この上部貯槽121Uは、平面視における断面積が小さくするとともに、その上部に開口125が形成されている。この構成の場合、熱交換器122は、各貯槽ユニット内に設けてもよいし、その一部に設けてもよい。
In this hot water supply operation, the circulation flow rate of the heat storage material hs between the storage tank 141 and the cogeneration device 150 is controlled so that the heat storage material hs reaching the lower part of the lower storage tank 141L is equal to or lower than the set temperature. That is, when the detection temperature detected by this valve rises so that the detection temperature of the thermo valve TMV becomes the set temperature, the water returning to the cogeneration equipment 150 side is discarded and low temperature clean water is supplied into the tank. The Therefore, the set temperature is set to a temperature that does not disturb the temperature stratification formed in the storage tank 141. For example, a temperature that is 5 ° C. higher than the feed water temperature is set.
[Another embodiment]
(1) The configuration of the storage tank according to the present application can be appropriately changed in relation to the material used for the storage tank and the strength.
For example, as shown in FIG. 12, the storage tank can be configured by connecting a plurality of storage tank units 121 at least in the upper part and in the lower part so that the heat storage material hs is communicatively connected [Configuration 16]. In FIG. 12, three tanks 121 of a first tank 121a, a second tank 121b, and a third tank 121c are arranged in a state of being arranged in the horizontal direction, and the upper and lower parts are connected to each other in the horizontal direction. The heat storage material hs is connected in a freely communicating manner. In this case, it suffices that at least the upper part and the lower part communicate with each other, and the intermediate part other than the upper part and the lower part, the entire surface, and the like may be connected.
In this case, the number of storage tank units to be installed can be changed as appropriate. And it is also possible to install in a state where a plurality of storage tank units are arranged in the vertical direction, and how to arrange and provide the plurality of storage tank units can be appropriately changed.
Further, communication openings are provided in the upper and lower portions of each storage tank unit, the communication openings are bonded to each other by welding or the like, and the upper and lower portions of each storage tank unit are connected to each other so that the heat storage material hs can flow freely. You can also
On the other hand, an upper storage tank 121U is provided in the upper part of the first tank 121a. The upper storage tank 121U has a small cross-sectional area in plan view, and an opening 125 is formed in the upper part thereof. In the case of this configuration, the heat exchanger 122 may be provided in each storage tank unit, or may be provided in a part thereof.

また、図13に示すように、貯槽を、上部を貯槽131の最上部に空気抜き弁130を備えた密閉槽131Cと、上部が開放され且つ密閉槽131Cよりも高い位置に蓄熱材hsと大気との界面を形成させる大気開放型の膨張タンク131Oと、蓄熱材hsを流通自在に密閉槽131Cの下部と膨張タンク131Oとを連通する連通路136とを備えて構成することができる。そして、空気抜き弁130の空気排出路133を膨張タンク131Oに接続している。したがって、空気抜き弁130にて水を含む空気を空気排出路133に排出しても、その空気に含まれた水を膨張タンク131Oに戻すことができるので、その水が漏れることを防止することができる。この場合、大気開放型の膨張タンク131Oは、低温水の膨張タンクとなる。また、大気開放は、開口135により確保される。この構成の場合、熱交換器132は、密閉槽131内に設けることとなり、コジェネレーション機器からの排熱往き及び排熱戻りは、密閉槽131のみを対象として、内部に温度成層が形成されるように、排熱往き路を密閉槽131の上部に接続し、排熱戻り路を密閉槽131の下部に接続することとなる。   Further, as shown in FIG. 13, the storage tank is composed of a sealed tank 131C having an air vent valve 130 at the uppermost part of the storage tank 131, a heat storage material hs and the atmosphere at a position where the upper part is open and higher than the sealed tank 131C. The expansion tank 131O that is open to the atmosphere that forms the interface and the communication path 136 that allows the heat storage material hs to flow freely and communicate with the lower part of the sealed tank 131C and the expansion tank 131O can be configured. The air discharge path 133 of the air vent valve 130 is connected to the expansion tank 131O. Therefore, even if air containing water is discharged to the air discharge path 133 by the air vent valve 130, the water contained in the air can be returned to the expansion tank 131O, so that the water can be prevented from leaking. it can. In this case, the open-air expansion tank 131O serves as a low-temperature water expansion tank. Moreover, the opening to the atmosphere is ensured by the opening 135. In the case of this configuration, the heat exchanger 132 is provided in the sealed tank 131, and the heat stratification is formed inside only the sealed tank 131 for exhaust heat going back and exhaust heat return from the cogeneration equipment. As described above, the exhaust heat return path is connected to the upper part of the sealed tank 131, and the exhaust heat return path is connected to the lower part of the sealed tank 131.

形状選択において自由度が高く、貯槽を内蔵すべき装置の隙間形状に合わせた自由な形状選択が可能な蓄熱槽を得ることができた。   It was possible to obtain a heat storage tank having a high degree of freedom in shape selection and capable of selecting a shape freely according to the gap shape of the device in which the storage tank should be built.

1 …蓄熱槽
2 …熱交換器(コイル)
3 …シート状材料
4 …蓋
5 …通気管
6 …潜熱蓄熱材(パラフィン)
7 …配線、配管スペース
10 …小型SOCF本体
11 …SOFCセルスタック
12 …(予備)改質器
13 …蒸発器
14 …インバーター(パワーコンディショナー)
15 …空気予熱器
16 …排熱回収熱交換器
17 …純水装置
18 …純水貯槽
19 …ポンプ
20 …ガス湯沸器
21 …熱交換器
22 …バーナ
23 …ミキシングバルブ
24 …温度センサ
1 ... heat storage tank 2 ... heat exchanger (coil)
3 ... Sheet-like material 4 ... Lid 5 ... Vent pipe 6 ... Latent heat storage material (paraffin)
7 ... Wiring and piping space 10 ... Small SOCF main body 11 ... SOFC cell stack 12 ... (Preliminary) reformer 13 ... Evaporator 14 ... Inverter (power conditioner)
DESCRIPTION OF SYMBOLS 15 ... Air preheater 16 ... Waste heat recovery heat exchanger 17 ... Pure water apparatus 18 ... Pure water storage tank 19 ... Pump 20 ... Gas water heater 21 ... Heat exchanger 22 ... Burner 23 ... Mixing valve 24 ... Temperature sensor

Claims (8)

蓄熱材を貯留する貯槽であって、貯留した前記蓄熱材の上面より高い位置に大気に通じる開口を有するとともに、前記蓄熱材と熱媒体との熱交換を行う熱交換器を当該蓄熱材に浸漬して備え、前記蓄熱材から受熱した前記熱媒体を貯槽外に取り出して、温水若しくは給湯水として供給可能に構成され、
前記貯槽の蓄熱材接触部分が断熱材の一体成形品にて形成され、
前記断熱材で成型された貯槽の内面を、耐熱性又は耐食性或はそれらの両方の性質を有し、前記蓄熱材の液面上で貯槽に固定或は貯槽内において自立或は保形される袋状のシート状材料にて覆い、前記シート状材料に蓄熱材が接触する状態で前記蓄熱材の貯留を行うと共に、少なくとも前記熱交換器に接続する配管が、前記シート状材料の開口で前記蓄熱材の大気開放面を介して配管接続されている大気開放型蓄熱槽。
A storage tank for storing a heat storage material, having an opening leading to the atmosphere at a position higher than the upper surface of the stored heat storage material, and immersing a heat exchanger for exchanging heat between the heat storage material and the heat medium in the heat storage material The heat medium received from the heat storage material is taken out of the storage tank and configured to be supplied as hot water or hot water.
The heat storage material contact portion of the storage tank is formed of an integrally molded product of heat insulating material,
The inner surface of the storage tank formed of the heat insulating material has heat resistance and / or corrosion resistance, and is fixed to the storage tank on the liquid surface of the heat storage material, or is self-supporting or retaining in the storage tank. Covering with a bag-shaped sheet material, storing the heat storage material in a state where the heat storage material is in contact with the sheet material, and at least a pipe connected to the heat exchanger is an opening of the sheet material An open air heat storage tank that is piped through an open air surface of the heat storage material.
前記貯槽の上面全体を気密に覆う蓋を設けると共に、前記蓄熱材の大気開放面から当該大気開放面より下方の大気に通じる配管スペースを設け、前記熱交換器に接続する配管が、当該配管スペースを通して配管接続されている請求項1記載の大気開放型蓄熱槽。   A lid that covers the entire upper surface of the storage tank in an airtight manner is provided, and a piping space that leads from the atmosphere opening surface of the heat storage material to the atmosphere below the atmosphere opening surface is provided, and a pipe connected to the heat exchanger is the piping space. The open air heat storage tank according to claim 1, wherein the pipe is connected through a pipe. 前記熱交換器を流れる前記熱媒体の流れと貯槽内の前記蓄熱材の流れとが、全体として対向流接触となるように前記熱交換器及び前記貯槽が配置若しくは配管接続されている請求項1又は2記載の大気開放型蓄熱槽。   The heat exchanger and the storage tank are arranged or connected by piping so that the flow of the heat medium flowing through the heat exchanger and the flow of the heat storage material in the storage tank are in counterflow contact as a whole. Or the open air type | formula heat storage tank of 2 description. コジェネレーション機器の排熱を水の顕熱として貯留する請求項1〜3の何れか一項記載の大気開放型蓄熱槽。   The open air type | formula thermal storage tank as described in any one of Claims 1-3 which stores the waste heat of a cogeneration apparatus as sensible heat of water. コジェネレーション機器の排熱を、水と水より比重と蒸気圧が小さくかつ固相−液相間の相変化潜熱を利用する潜熱蓄熱材の組合せにて貯留する請求項1〜3の何れか一項記載の大気開放型蓄熱槽。   The waste heat of the cogeneration device is stored as a combination of latent heat storage materials that have a specific gravity and vapor pressure smaller than water and water and that utilize phase change latent heat between the solid phase and the liquid phase. The open air heat storage tank described in the item. 前記熱交換器を、貯槽上部に配設される上部熱交換器と、貯槽下部に設けられる下部熱交換器と、前記両熱交換器内に形成された両熱媒体流路を蓄熱槽上下方向に短絡する短絡流路を形成する短絡配管とを組み合わせて構成した請求項1〜5のいずれか一項記載の大気開放型蓄熱槽。   The heat exchanger includes an upper heat exchanger disposed in the upper part of the storage tank, a lower heat exchanger provided in the lower part of the storage tank, and both heat medium passages formed in the both heat exchangers in the vertical direction of the heat storage tank. The atmosphere open type heat storage tank according to any one of claims 1 to 5, comprising a combination of a short-circuit pipe that forms a short-circuit channel that is short-circuited with each other. 前記蓄熱材が前記熱媒体に授熱する第1熱交換部を貯槽上部に設け、
前記授熱により温度低下した前記蓄熱材を前記貯槽上部から貯槽下側に導く蓄熱材下降路を形成する下降路形成部材を設けるとともに、前記下降路形成部材の下側に蓄熱材開放口を設け、
前記蓄熱材開放口から流出する蓄熱材に授熱する第2熱交換部を設けた請求項1〜6のいずれか一項記載の大気開放型蓄熱槽。
A first heat exchanging portion that heats the heat storage material to the heat medium is provided in the upper portion of the storage tank;
Provided is a descending path forming member that forms a thermal storage material descending path that guides the thermal storage material that has fallen in temperature due to the heat transfer from the upper part of the storage tank to the lower side of the storage tank, and a thermal storage material opening is provided below the descending path forming member. ,
The open air type | formula heat storage tank as described in any one of Claims 1-6 which provided the 2nd heat exchange part which heat-sucks the heat storage material which flows out out of the said heat storage material opening | mouth.
第1熱媒体から蓄熱材が受熱する前記熱交換器を、貯槽上部に配設される上部熱交換器と、貯槽下部に設けられる下部熱交換器と、前記両熱交換器内に形成された両熱媒体流路を蓄熱槽上下方向に短絡する短絡流路を形成する短絡配管とを組み合わせて構成し、
前記蓄熱材が第2熱媒体に授熱する第1熱交換部を貯槽上部に設け、
前記授熱により温度低下した前記蓄熱材を前記貯槽上部から貯槽下側に導く蓄熱材下降路を形成する下降路形成部材を設けるとともに、前記下降路形成部材の下側に蓄熱材開放口を設け、
前記第1熱媒体が、前記蓄熱材開放口から流出する蓄熱材に授熱する第2熱交換部を設けた請求項1〜6のいずれか一項記載の大気開放型蓄熱槽。
The heat exchanger that receives the heat storage material from the first heat medium is formed in the upper heat exchanger disposed in the upper part of the storage tank, the lower heat exchanger provided in the lower part of the storage tank, and both the heat exchangers. Composed of a combination of short-circuit piping that forms a short-circuit channel that short-circuits both heat medium channels in the vertical direction of the heat storage tank,
A first heat exchanging part that heats the heat storage material to the second heat medium is provided in the upper part of the storage tank;
Provided is a descending path forming member that forms a thermal storage material descending path that guides the thermal storage material that has fallen in temperature due to the heat transfer from the upper part of the storage tank to the lower side of the storage tank, and a thermal storage material opening is provided below the descending path forming member. ,
The atmosphere-opening type heat storage tank according to any one of claims 1 to 6, wherein the first heat medium is provided with a second heat exchanging section that heats the heat storage material flowing out from the heat storage material opening.
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