JPS58124195A - Method for recovering thermal energy by heat exchange - Google Patents

Method for recovering thermal energy by heat exchange

Info

Publication number
JPS58124195A
JPS58124195A JP57007787A JP778782A JPS58124195A JP S58124195 A JPS58124195 A JP S58124195A JP 57007787 A JP57007787 A JP 57007787A JP 778782 A JP778782 A JP 778782A JP S58124195 A JPS58124195 A JP S58124195A
Authority
JP
Japan
Prior art keywords
hot water
water
heat
thermal energy
tank
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP57007787A
Other languages
Japanese (ja)
Inventor
Hiroyuki Ide
裕之 井出
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to JP57007787A priority Critical patent/JPS58124195A/en
Publication of JPS58124195A publication Critical patent/JPS58124195A/en
Pending legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D21/00Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
    • F28D21/0001Recuperative heat exchangers
    • F28D21/0012Recuperative heat exchangers the heat being recuperated from waste water or from condensates
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02BCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
    • Y02B30/00Energy efficient heating, ventilation or air conditioning [HVAC]
    • Y02B30/56Heat recovery units

Landscapes

  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Abstract

PURPOSE:To enable to enhance heat-exchanging efficiency, by a method wherein a heat exchanger is floated up to a position in proximity to the surface of hot water in a storing tank and is brought into heat exchange with water fed into the tank, in recovering thermal energy from residual hot water contained in a bathtub or the like. CONSTITUTION:Water is poured into a hot water storing tank 2, while an appropriate quantity of hot water such as residual hot water is poured into the storing tank 1, in which the heat exchanger 3 is floated up to a position in proximity to the surface of hot water by a float 4. When the hot water temperature at the surface level is higher than the water temperature at a bottom part of the tank 2, a water-feeding pump 8 is operated to feed the water at the bottom part of the tank 2 into the heat exchanger 3, thereby bringing the water into heat exchange with hot water. In this case, since the heat exchanger 3 is located in proximity to the surface of hot water which is on the high-temperature side, heat is exchanged at the maximum efficiency. When the temperatures of hot water and water are equalized, the pump 8 is stopped to finish the heat exchange. Accordingly, even thermal energy at a relatively low level and intermittent thermal energy can be recovered efficiently.

Description

【発明の詳細な説明】 本発明は温水からこれに含まれる熱エネルギーを熱交換
によって補集する方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for collecting the thermal energy contained in hot water by heat exchange.

近年、太陽の輻射熱や風力エネルギー等を熱エネルギー
として補集しようとする試みがなされている。これは、
この熱エネルギーを燃料の一部に代替して燃料の消費量
を節減し、以って燃料費の低減を図るためであって、最
近は更に進んで工場から排出される温水や焼却炉の排ガ
ス等の従来は見棄てられていたものに含まれる熱エネル
ギーを補集してエネルギーの有効利用を図ろうとする機
運が高まって来た。
In recent years, attempts have been made to collect solar radiant heat, wind energy, and the like as thermal energy. this is,
The aim is to reduce fuel consumption by substituting a portion of this thermal energy for fuel, thereby reducing fuel costs. There has been a growing momentum to try to capture the thermal energy contained in things that have been abandoned in the past, and to make effective use of energy.

ところでこのエネルギーは新たな水を加熱するエネルギ
ーとして補集されるのであるが、エネルギー補集の対象
とされる熱源は比較的温度が高く、しかも連続的に供給
されるものであって、少な(とも水を数十度にまで加熱
することのできる虻のに限られており、例えば温水では
温度は高くても断続的に、又は一時に排出されるものは
対象とされないし、又連続的に排出されるものであって
も50℃以下の比較的温度の低いものも対象とされるこ
とはなかった。しかしながら、浴湯の残り湯の様に温度
が 40℃程度の温水であっても、この温水中には20
kcal/L程度の利用可能な熱エネルギーが含まれて
いるから、この熱エネルギーを補集すれば燃料費の節減
が一段と図られるのであるが、上に述べた様に従来の熱
エネルギーの補集は、新たな水を数十度にまで加熱する
ことによって行なわれるから、それよりも温度の低い熱
源からは熱エネルギーを取り出すことは不可能であると
考えられたこと、及び温水が一時的に排出され、しかも
排出量が一定しないものではこのものから有効に熱エネ
ルギーを補集する手段がなかったことからこの種の温水
は何ら利用されることなくそのま\棄てられたのである
。しかしながらこの温水を15〜20℃の水と熱交換し
て1tに)4の熱エネルギーを補集することができれば
温水に対する熱エネルギーの補集率は40〜50%とな
るし、特に、加温された新たな水は浴用水として利用す
れば、浴用水は40〜50℃程度に加温すれば足りるか
ら、結局燃料費を20〜30%程度節減することができ
るのである。
By the way, this energy is collected as energy to heat new water, but the heat source targeted for energy collection has a relatively high temperature and is continuously supplied, so it is small ( Both species are limited to flies that can heat water up to several tens of degrees.For example, even if the temperature is high in hot water, it does not cover those that are discharged intermittently or all at once; Even if it is discharged, relatively low temperature water below 50 degrees Celsius was not targeted. However, even hot water with a temperature of about 40 degrees Celsius, such as leftover hot water from a bathtub, 20 in this warm water
Since it contains about kcal/L of usable thermal energy, collecting this thermal energy can further reduce fuel costs, but as mentioned above, conventional thermal energy collection This is done by heating new water to a temperature of several tens of degrees, so it was thought that it would be impossible to extract thermal energy from a heat source with a lower temperature. Since there was no way to effectively collect thermal energy from the water that was discharged and the amount of discharge was not constant, this type of hot water was simply discarded without being used in any way. However, if this hot water can be heat-exchanged with water at 15 to 20°C and 1 ton of thermal energy can be collected, the collection rate of thermal energy for hot water will be 40 to 50%. If the new water is used as bathing water, it is sufficient to heat the bathing water to about 40 to 50 degrees Celsius, resulting in a fuel cost savings of about 20 to 30%.

本発明は上記した点に鑑みてなされたものであって、熱
源である温水の温度が例えば浴場の残り湯の様に比較的
低いものであっても、或いはその排出が連続的でなく、
断続的又は一時的であってもこれに含まれる熱エネルギ
ーを効率よ(補集することができる様にしたものである
The present invention has been made in view of the above-mentioned points, and even if the temperature of hot water as a heat source is relatively low, such as leftover hot water in a bath, or its discharge is not continuous,
The thermal energy contained therein can be collected efficiently even if it is intermittent or temporary.

以下、本発明を図面に基づいて具体的に説明する。図中
、符号1は貯溜槽、2は貯湯槽、3は熱交換器である。
Hereinafter, the present invention will be specifically explained based on the drawings. In the figure, numeral 1 is a storage tank, 2 is a hot water storage tank, and 3 is a heat exchanger.

貯溜槽1は浴場等から排出された温水を貯湯flF2に
充満された水と熱交換させるために一時的に貯溜する槽
であって、排出された温水は先ずこの貯溜槽1に注ぎ込
まれる。そしてこの貯溜槽1は温水が浴場の残り湯の様
に一時に排出されるものであるときは、これを貯溜する
に充分な容積であることは勿論熱交換中に出来るだけ熱
の放散を抑える様に形成されているものであり、例えば
許容される範囲内で、表面積を狭くすやことは云うまで
もない。
The storage tank 1 is a tank that temporarily stores hot water discharged from a bathhouse or the like in order to exchange heat with the water filled in the hot water storage flF2, and the discharged hot water is first poured into this storage tank 1. When hot water is to be discharged all at once, such as leftover hot water in a bath, this storage tank 1 must not only have a sufficient volume to store it, but also suppress heat dissipation as much as possible during heat exchange. It goes without saying that the surface area can be reduced within an allowable range, for example.

熱交換器3は通常のこの種のものと同様であって、その
構造について特に限定はしないが貯溜槽1に注ぎ込まれ
る温水の量の多少に拘わらず常に液面附近に在って液面
附近の、従って貯溜槽1内では最も温度の高い部分の、
温水と熱交換する様に形成されているのである。第一図
に示したものはその一例であってこのものにはフロート
4が取付けられていてこれによって液面に浮かぶ様にな
っている。勿論この場合、熱交換器3に接続されている
通水パイプ5はフレキシブルパイプが用いられて熱交換
器3の昇降に対処することができる様に構成されている
。第二図に示したものは熱交換器3を貯溜槽1の内壁の
一点に取付けてその位置決めを図ったものであって、貯
溜槽1の内壁の適所にあらかじめフック12を取り付け
ておきこれに熱交換器3を枢着するのである。この方式
では、熱交換を終了して貯溜槽1内の温水を排棄したと
きに、熱交換器1がフック12に吊下がって槽底にまで
落ち込まない利点があるが、反面貯溜槽1には一定量以
上の温水を注入しなければ熱交換を開始することができ
ないものであり、貯溜槽1に液面調節機構14が備えら
れていて、温水は断続的又は連続的に注加されて液面が
一定に調節された状態で熱交を行なうのに適している。
The heat exchanger 3 is similar to a normal one of this type, and although there are no particular limitations on its structure, it is always located near the liquid level regardless of the amount of hot water poured into the storage tank 1. Therefore, in the storage tank 1, the part with the highest temperature is
It is designed to exchange heat with hot water. The one shown in Figure 1 is one example, and a float 4 is attached to this float so that it floats on the liquid surface. Of course, in this case, the water pipe 5 connected to the heat exchanger 3 is a flexible pipe, and is configured to cope with the raising and lowering of the heat exchanger 3. The heat exchanger 3 shown in FIG. 2 is installed at one point on the inner wall of the storage tank 1 for positioning. The heat exchanger 3 is pivotally mounted. This method has the advantage that when the heat exchange is finished and the hot water in the storage tank 1 is discharged, the heat exchanger 1 does not hang from the hook 12 and fall to the bottom of the tank. The tank cannot start heat exchange unless a certain amount or more of hot water is injected, and the storage tank 1 is equipped with a liquid level adjustment mechanism 14, and the hot water is intermittently or continuously injected. Suitable for heat exchange with a constant liquid level.

また熱交換を行なうのは云うまでもなく貯湯槽2内の水
の温度よりも貯溜槽1内の少なくとも液面附近の温水の
温度の方が高い時に限るのであって一例として熱交換器
3と貯湯11!2の底部に温度計6及び7を取付けてお
き、これによって貯溜槽1の液面附近の温水の温度と貯
湯槽2の槽底附近の水の温度を検知しこれが熱交換する
に適しているときは送水ポンプ8を作動させて熱交換器
3に水を送り、然して熱交換をするのである。尚、貯湯
槽2は通常のこの種の温水装置のそれと同様であって、
図示はしないが湯沸器や太陽熱集熱器等の加熱装置が付
設されていることは云うまでもない。
It goes without saying that heat exchange is performed only when the temperature of the hot water in the storage tank 1, at least near the liquid level, is higher than the temperature of the water in the hot water storage tank 2. Thermometers 6 and 7 are attached to the bottom of the hot water storage tank 11!2, and these detect the temperature of the hot water near the liquid level of the storage tank 1 and the temperature of the water near the bottom of the hot water storage tank 2, and these are used for heat exchange. When appropriate, the water pump 8 is operated to send water to the heat exchanger 3, thus exchanging heat. Incidentally, the hot water storage tank 2 is similar to that of a normal water heating device of this type,
Although not shown, it goes without saying that a heating device such as a water heater or a solar heat collector is attached.

尚、図では熱交換器3の上面にフロート4を取付けた一
例を示したがこの方式には次の様な利点がある。即ちフ
ロート4が液面を覆うために放熱が少な(なり、従って
熱エネルギーの利用効率が高められるのであり、また一
般的に浴場の残り湯等には脂肪分の多い浮遊物が水面近
くに集まっているので、もし熱交換器3が水面に位置し
ていると、それら浮遊物が熱交換器の外部熱伝達面に耐
着し、熱伝達を著るしく阻宜することとなる。しかるに
フロート4を取付けることによって熱交換器は常に液面
下の適宜な位置に配されるため浮遊物による汚れを最少
限にくいとめることができる。
Although the figure shows an example in which the float 4 is attached to the upper surface of the heat exchanger 3, this system has the following advantages. In other words, because the float 4 covers the liquid surface, less heat is radiated (therefore, the efficiency of using thermal energy is increased).Also, in general, residual hot water in a bathtub, etc., has floating matter with a high fat content that collects near the water surface. Therefore, if the heat exchanger 3 is located on the water surface, these floating objects will adhere to the external heat transfer surface of the heat exchanger and significantly impede heat transfer. 4, the heat exchanger is always located at an appropriate position below the liquid surface, so that contamination by floating matter can be minimized.

ここで、貯溜槽1に注入された温水と貯湯槽2に充満さ
れた水との間で熱交換する方法について説明する。
Here, a method of exchanging heat between the hot water injected into the storage tank 1 and the water filling the hot water storage tank 2 will be described.

先ず、貯湯t!2には水を充満しておき、貯溜槽1に適
当量の温水を注入する。すると熱交換器3が温水の液面
附近に浮かぶから、この附近の温水の温度と貯湯槽2の
槽底附近の水の温度とを検知し、前者の温度の方が高い
ときは送水ポンプ8を作動させ、貯湯槽2内の水を熱交
換器3に送り込んで、これを温水と熱交換させるのであ
る。熱交換が進むに従がって貯溜槽1内の温水の温度が
下降すると共に貯湯槽2内の水の温度が上昇し、やがて
両者が同一になった時点で熱交換は終了する。ここにお
いて本発明の特徴は、熱交換器3を常に温水の液面附近
に位置させる点にある。
First of all, store hot water! 2 is filled with water, and an appropriate amount of hot water is poured into the storage tank 1. Then, since the heat exchanger 3 floats near the surface of the hot water, it detects the temperature of the hot water nearby and the temperature of the water near the bottom of the hot water storage tank 2, and when the former temperature is higher, the water pump 8 is activated to send the water in the hot water tank 2 to the heat exchanger 3, where it exchanges heat with hot water. As the heat exchange progresses, the temperature of the hot water in the storage tank 1 decreases and the temperature of the water in the hot water tank 2 increases, and when the two become the same, the heat exchange ends. Here, the feature of the present invention is that the heat exchanger 3 is always located near the surface of the hot water.

即ち、貯溜槽1内の温水は熱交換が進むに従かって全体
が一様に降温するのではなく、熱交換器に接触したもの
が降温して沈降するので、槽内には次第に温度勾配が生
じることとなる。
In other words, as the heat exchange progresses, the temperature of the hot water in the storage tank 1 does not drop uniformly all over, but the water that comes into contact with the heat exchanger cools and settles, so a temperature gradient gradually develops inside the tank. This will occur.

然して熱交換器3は常に液面附近に位置しているから、
常に最も温度の高い温水と接することとなり、最も効率
よく熱交換が行なわれるのである。
However, since the heat exchanger 3 is always located near the liquid level,
It is always in contact with the warm water that has the highest temperature, and heat exchange occurs most efficiently.

この点からすれば、既に熱交換の行なわれている温水中
に更に新たな温水を断続的にしろ連続的にしろ注油する
ときはこの新たな温水が槽内の温水の温度勾配を乱さな
い様にすることが肝要であり、同時に槽外へ排出させる
温水は槽底附近の最も温度の低いものを溢流させること
が肝要である。
From this point of view, when adding new hot water to hot water that has already undergone heat exchange, either intermittently or continuously, it is important to ensure that this new hot water does not disturb the temperature gradient of the hot water in the tank. At the same time, it is important that the warm water discharged outside the tank has the lowest temperature near the bottom of the tank.

第二図はその様にした一例を示したもので貯溜槽1に補
助槽9を付設し、この補助49と貯溜槽1との間には高
さの異なる数個所に通水孔10を穿設し、新たな温水は
一旦補助漕9に注入し然るのち通水孔10を通して貯溜
槽に入り込む様にするのである。この様にすると補助槽
9に注入された新たな温水は貯溜槽1内のこれと同じ温
度の温水に最も近い位置にある通水孔10を通って槽内
に入り込むのである。勿論多くの場合は貯溜11内の水
面附近の温水よりも新たに注油される温水の方が温度が
高いから、この温水は液面に最も近い通水孔10aを通
って槽内に入るのであるが、仮にこの温水の温度が槽底
附近の温水の温度と同程度若しくはそれより低いもので
あった場合には最下位の通水孔10aより入り込み、何
ら熱交換されることなく排水口11を通って槽外に排出
されるのである。尚、第三図は補助槽9に代えて貯溜槽
1内に多孔性の隔壁12を設けて貯溜槽の一部を仕切っ
た一例を示したものであり、この仕切りの内側に新たな
温水を注入すれば上記したものと効果において殆んど変
るところはない。
Figure 2 shows an example of such a structure, in which an auxiliary tank 9 is attached to the storage tank 1, and water holes 10 are bored at several locations at different heights between the auxiliary tank 49 and the storage tank 1. The new hot water is once injected into the auxiliary tank 9 and then flows into the storage tank through the water passage hole 10. In this way, new hot water injected into the auxiliary tank 9 enters the tank through the water passage hole 10 located closest to the hot water of the same temperature in the storage tank 1. Of course, in most cases, the temperature of newly added hot water is higher than the warm water near the water surface in the reservoir 11, so this hot water enters the tank through the water passage hole 10a closest to the liquid surface. However, if the temperature of this hot water is the same as or lower than the temperature of the hot water near the bottom of the tank, it will enter through the lowest water passage hole 10a and drain through the drain port 11 without any heat exchange. It passes through the tank and is discharged outside the tank. Incidentally, Figure 3 shows an example in which a porous partition wall 12 is provided in the storage tank 1 instead of the auxiliary tank 9 to partition a part of the storage tank, and new hot water can be added to the inside of this partition. When injected, there is almost no difference in effect from the one described above.

以上詳述した様に本発明は、連続的に、或いは一時に排
出される温水から、熱交換によってこれに含まれる熱エ
ネルギーを補集するに当り温水を貯溜槽1に注入して同
じく貯溜11に備えられた熱交換器3によって熱交換す
るものであり、特に熱交換器3は常に温水の液面附近に
在る様にしたから、常に最も温度の高いものと熱交換す
ることとなり、熱交換効率の高いものである。
As described in detail above, the present invention is capable of injecting hot water into the storage tank 1 to collect the thermal energy contained in the hot water continuously or all at once by heat exchange. The heat exchanger 3 is installed in the hot water, and since the heat exchanger 3 is always located near the surface of the hot water, it always exchanges heat with the object with the highest temperature. It has high exchange efficiency.

【図面の簡単な説明】[Brief explanation of the drawing]

第一図乃至第三図は本発明方法の一実施例を骨格的に示
す説明図である。 1・・・貯 溜 槽    2・・・貯 湯 漕3・・
・熱交換器    4・・・フロート5・・・通水パイ
プ     6・・・温 度 計7・・・温 度 計 
    8・・・送水ポンプ9・・・補助槽  10・
・・通水孔 11・・・排水孔  12・・・隔 壁13・・・フ 
ッ り    14・・・液面調節機構特許出願人 井
 出 裕 之 手続補正書 (自発) 1.事件の表示  昭和57年特許願第007787号
2、発明の名称   熱交換による熱エネルギーの補集
方法3、補正をする者 事件との関係   特許出願人 4、補正命令の日付   自発補正 5、補正の対象   ■看書車発明の名称の欄■ 明細
書中特許請求の範囲の欄 ■ 発明の詳細な説明の欄 6、補正の内容 ■ 発明の名称を「熱交換による熱エネルギーの捕集2
、特許請求の範囲 熱交換器を備えた貯溜槽に温水を注入すると共薔ζ熱交
換器番ζは水を送り込んで、この水と温水との間で熱交
換を行なう熱エネルギーの捕集方法において熱交換器は
温水の液面附近に浮び上がらせて、常に液面附近の温水
と接触させ、この温水との間で熱交換を行なわせること
を特徴とする熱交換による熱エネルギーの捕集方法3、
明細書中          − 第2ページ第5行目、同第6行目、同第17行目、同第
19行目 第3ページ第5行目、同第9行目、同第10行目、同第
20行目 第9ページ第19行目 「補集」とあるを「捕集」と訂正する。
Figures 1 to 3 are explanatory diagrams schematically showing one embodiment of the method of the present invention. 1... Storage tank 2... Hot water storage tank 3...
・Heat exchanger 4...Float 5...Water pipe 6...Temperature meter 7...Temperature meter
8... Water pump 9... Auxiliary tank 10.
... Water hole 11 ... Drain hole 12 ... Partition wall 13 ... F
14...Liquid Level Adjustment Mechanism Patent Applicant Hiroshi Ide's Procedural Amendment (Voluntary) 1. Display of the case Patent Application No. 007787 of 1982 2, Title of the invention Method of collecting thermal energy by heat exchange 3, Person making the amendment Relationship to the case Patent applicant 4, Date of amendment order Voluntary amendment 5, Amendment Subject ■ Column for the name of the billboard wheel invention ■ Column for claims in the specification ■ Column 6 for detailed explanation of the invention, contents of amendment ■ Change the title of the invention to “Collection of thermal energy by heat exchange 2”
, Claims A method for collecting thermal energy in which when hot water is injected into a storage tank equipped with a heat exchanger, the heat exchanger number ζ sends water and performs heat exchange between the water and the hot water. In this method, the heat exchanger is floated near the liquid surface of the hot water, and is always in contact with the hot water near the liquid surface, and heat exchange is performed between the heat exchanger and the hot water.Collection of thermal energy by heat exchange Method 3,
In the specification - 2nd page, 5th line, 6th line, 17th line, 19th line, 3rd page, 5th line, 9th line, 10th line, In line 20, page 9, line 19, the words ``supplement'' are corrected to ``collection''.

Claims (1)

【特許請求の範囲】[Claims] 熱交換器を備えた貯溜槽に温水を注入すると共に熱交換
器には水を送り込んで、この水と温水との間で熱交換を
行なう熱エネルギーの補集方法において熱交換器は温水
の液面附近に浮び上がらせて、常に液面附近の温水と接
触させ、この温水との間で熱交換を行なわせることを特
徴とする熱交換による熱エネルギーの補集方法
In this thermal energy collection method, hot water is injected into a storage tank equipped with a heat exchanger, and the water is also sent to the heat exchanger to exchange heat between the water and the hot water. A method for collecting thermal energy by heat exchange, which is characterized by floating the liquid near the liquid surface, constantly bringing it into contact with hot water near the liquid surface, and exchanging heat with this hot water.
JP57007787A 1982-01-20 1982-01-20 Method for recovering thermal energy by heat exchange Pending JPS58124195A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57007787A JPS58124195A (en) 1982-01-20 1982-01-20 Method for recovering thermal energy by heat exchange

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57007787A JPS58124195A (en) 1982-01-20 1982-01-20 Method for recovering thermal energy by heat exchange

Publications (1)

Publication Number Publication Date
JPS58124195A true JPS58124195A (en) 1983-07-23

Family

ID=11675371

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57007787A Pending JPS58124195A (en) 1982-01-20 1982-01-20 Method for recovering thermal energy by heat exchange

Country Status (1)

Country Link
JP (1) JPS58124195A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPWO2020166653A1 (en) * 2019-02-14 2021-12-09 三菱製紙株式会社 Total heat exchange element Paper and total heat exchange element

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPWO2020166653A1 (en) * 2019-02-14 2021-12-09 三菱製紙株式会社 Total heat exchange element Paper and total heat exchange element

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