JPH041277B2 - - Google Patents

Info

Publication number
JPH041277B2
JPH041277B2 JP59020399A JP2039984A JPH041277B2 JP H041277 B2 JPH041277 B2 JP H041277B2 JP 59020399 A JP59020399 A JP 59020399A JP 2039984 A JP2039984 A JP 2039984A JP H041277 B2 JPH041277 B2 JP H041277B2
Authority
JP
Japan
Prior art keywords
heat
heat transfer
heat storage
tube
tubes
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.)
Expired - Lifetime
Application number
JP59020399A
Other languages
Japanese (ja)
Other versions
JPS60164196A (en
Inventor
Nobuyuki Abe
Takeo Ozawa
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.)
National Institute of Advanced Industrial Science and Technology AIST
Original Assignee
Agency of Industrial Science and Technology
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 Agency of Industrial Science and Technology filed Critical Agency of Industrial Science and Technology
Priority to JP59020399A priority Critical patent/JPS60164196A/en
Publication of JPS60164196A publication Critical patent/JPS60164196A/en
Publication of JPH041277B2 publication Critical patent/JPH041277B2/ja
Granted 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
    • F28D7/00Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D7/06Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits having a single U-bend
    • 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
    • F28D20/00Heat storage plants or apparatus in general; Regenerative heat-exchange apparatus not covered by groups F28D17/00 or F28D19/00
    • F28D20/0034Heat storage plants or apparatus in general; Regenerative heat-exchange apparatus not covered by groups F28D17/00 or F28D19/00 using liquid heat storage material
    • 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
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/14Thermal energy storage

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)

Description

【発明の詳細な説明】 この発明は、例えば溶融塩のように相変化を伴
い、且つ腐食性に留意する必要のある潜熱蓄熱材
料を用いた蓄熱器であつて、例えば原子力発電
所、工場等の廃熱を蓄熱するのに用いる蓄熱器に
関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention is a heat storage device using a latent heat storage material that undergoes a phase change, such as molten salt, and requires attention to corrosivity. This relates to a heat storage device used to store waste heat.

省エネルギー、エネルギー有効利用の観点から
蓄熱技術は極めて重要で、この場合物質の融解凝
固等の相変化を利用した潜熱蓄熱は、蓄熱密度が
高く、しかも一定温度で熱を貯えることができる
利点があり、比較的短期間(例えば、2〜3日)
の蓄熱方法としては最も有望な方法と考えられて
いる。
Heat storage technology is extremely important from the perspective of energy conservation and effective energy use. In this case, latent heat storage that utilizes phase changes such as melting and solidification of substances has the advantage of having a high heat storage density and being able to store heat at a constant temperature. , for a relatively short period of time (e.g. 2-3 days)
It is considered the most promising method for storing heat.

しかし、潜熱蓄熱技術の配慮すべき問題点は、
潜熱蓄熱材料によつてその性格が可成り変わつて
くる。産業上重要と考えられる200℃以上での蓄
熱には、各種溶融塩が最も適切な蓄熱材料として
利用されているが、この溶融塩を蓄熱材料として
利用する場合には次の点に留意しなければならな
い。
However, the issues that should be considered with latent heat storage technology are:
Its characteristics vary considerably depending on the latent heat storage material. Various molten salts are used as the most suitable heat storage materials for heat storage at temperatures above 200°C, which is considered important in industry. However, when using molten salts as heat storage materials, the following points must be kept in mind. Must be.

(1) 融解時の体積膨張が15〜25%と大きいこと。(1) The volumetric expansion upon melting is as high as 15-25%.

(2) 腐食性の高いこと。特に蓄熱材料の界面にお
いて蓄熱器材料の腐食が激しいこと。
(2) Highly corrosive. Severe corrosion of the heat storage material, especially at the interface of the heat storage material.

(3) 一般に熱伝導率が低いこと。(3) Generally low thermal conductivity.

このうち、(3)の欠点を補うためには何らかの伝
熱促進手段を用いることも考えられるが(例え
ば、特願昭57−109046号(特開昭59−1995号公
報)、特願昭57−197356号)(特開昭59−86894号
公報)、高温の溶融塩に対しては伝熱面積を大き
くすることが最も手つ取り早く、確実な方法であ
る。しかし、伝熱面積を増やせば、それだけ蓄熱
器のコストが上昇してしまうため、蓄熱器の構造
を極力単純化して製作費を抑える必要が生ずる。
Among these, in order to compensate for the shortcoming (3), it is possible to use some kind of heat transfer promoting means (for example, Japanese Patent Application No. 57-109046 (Japanese Unexamined Patent Publication No. 59-1995), Japanese Patent Application No. 57 -197356) (Japanese Unexamined Patent Publication No. 59-86894), increasing the heat transfer area is the quickest and surest method for high-temperature molten salt. However, if the heat transfer area is increased, the cost of the heat storage device increases accordingly, so it is necessary to simplify the structure of the heat storage device as much as possible to reduce manufacturing costs.

このため、従来の蓄熱器としてはシエル・チユ
ーブ型蓄熱器とカプセル型蓄熱器が知られてい
る。シエル・チユーブ型蓄熱器は、第1図にその
概略を示すように蓄熱器1内に蓄熱材料aの収容
室2を形成し、該収容室2には垂直方向に複数本
の伝熱管3,……を配設するとともに、熱媒体は
伝熱管3,……の下端に設けられた出入口部4か
ら伝熱管3,……内に送入排出された伝熱管3,
……の上端に設けられた出入口部5に送入排出さ
れ、この間に熱媒体により収容室2内に収容され
た蓄熱材料aを蓄放熱させるものである。
For this reason, shell-tube type heat storage devices and capsule type heat storage devices are known as conventional heat storage devices. The shell tube type heat storage device, as schematically shown in FIG. ... are arranged, and the heat medium is fed into and discharged from the heat transfer tube 3, ... from the inlet/outlet portion 4 provided at the lower end of the heat transfer tube 3,...
It is fed into and discharged from the entrance/exit portion 5 provided at the upper end of the .

これに対してカプセル型蓄熱器は、第2図にそ
の概略を示すように蓄熱器1内に蓄熱材料aを密
封した複数個のカプセル6,……を収容し、熱媒
体は前記同様、蓄熱器1の下端に設けられた出入
口部4から器内に送入排出され、蓄熱器1の上端
に設けられた出入口部5に送入排出され、この間
に熱媒体によりカプセル6,……内に密封された
蓄熱材料aを蓄放熱させるものである。
On the other hand, a capsule type heat storage device, as schematically shown in FIG. 2, houses a plurality of capsules 6, . The heat is introduced into and discharged from the inlet/outlet section 4 provided at the lower end of the heat storage device 1, and is introduced into and discharged from the inlet/outlet section 5 provided at the upper end of the heat accumulator 1. The sealed heat storage material a is used to store and release heat.

第1図と第2図の蓄熱器を比べると、第2図の
カプセル型蓄熱器は経済的に著しく不利であり、
基本構造としては第1図のシエル・チユーブ型蓄
熱器が望ましい形式である。
Comparing the heat storage devices shown in Figures 1 and 2, the capsule type heat storage device shown in Figure 2 is economically disadvantageous;
As for the basic structure, the shell-tube type heat storage device shown in FIG. 1 is desirable.

しかし、このシエル・チユーブ型蓄熱器につい
ても前記(1)に述べたように蓄熱材料aの融触時の
体積膨張が極めて大きい。
However, even in this shell tube type heat storage device, as mentioned in (1) above, the volumetric expansion of the heat storage material a during melting is extremely large.

そこで、融解時における蓄熱材料aの体積膨張
による応力を吸収するために、収容室2の上部に
スペースを設けると、伝熱管3,……の表面が蓄
熱材料aの界面に晒され、しかもこの界面が蓄熱
材料aの融解と凝固により激しく変動するため、
伝熱管3,……の表面が腐食を受けることにな
る。更に、蓄熱材料aの界面が伝熱管3,……の
表面と接触するため、蓄熱材料aが伝熱管3を這
い上る、所謂クリーピング現象を起こし易い。
Therefore, if a space is provided above the storage chamber 2 in order to absorb the stress due to the volumetric expansion of the heat storage material a during melting, the surfaces of the heat transfer tubes 3, etc. will be exposed to the interface of the heat storage material a, and this Since the interface changes drastically due to melting and solidification of heat storage material a,
The surfaces of the heat exchanger tubes 3, . . . will be subject to corrosion. Furthermore, since the interface of the heat storage material a comes into contact with the surfaces of the heat transfer tubes 3, . . . , the heat storage material a tends to creep up the heat transfer tubes 3, which is a so-called creeping phenomenon.

また、以上のシエル・チユーブ型蓄熱器である
と熱媒体が伝熱管3,……の下方より上方へ移送
させる構造であるため、伝熱管3の長手方向の温
度差が大きく、したがつて温度差による質量移行
現象により伝熱管の腐食されることもある。
In addition, in the above-mentioned shell tube type heat storage device, the heat medium is transferred upward from the bottom of the heat transfer tubes 3, etc., so the temperature difference in the longitudinal direction of the heat transfer tubes 3 is large, and therefore the temperature The heat transfer tubes may be corroded due to the mass transfer phenomenon caused by the difference.

更に、通常の熱交換器では、管板に伝熱管を通
す穴を設け、この穴に伝熱管を挿入して溶接固定
するため、伝熱管と管板との間に〓間が生じ、特
に竪型熱交換器では伝熱管と管板との〓間に腐食
生成物が堆積し、伝熱管の根元を化学的、機械的
に腐食させる所謂デンデイングが生ずる可能性が
高い。
Furthermore, in normal heat exchangers, holes are provided in the tube sheet for the heat transfer tubes to pass through, and the heat transfer tubes are inserted into these holes and fixed by welding, so a gap is created between the heat transfer tubes and the tube sheet. In type heat exchangers, corrosion products are deposited between the heat exchanger tubes and the tube sheets, and there is a high possibility that so-called dending, which chemically and mechanically corrodes the bases of the heat exchanger tubes, will occur.

また、溶融塩のような蓄熱物質を利用した蓄熱
器においては、蓄熱物質の熱伝導率が一般に低い
ため、熱の出入りに長時間がかかり、しかも放熱
時には入力温度と出力温度との温度差が小さく、
緩慢な放熱特性を示す場合が多い。
In addition, in heat storage devices that use heat storage materials such as molten salt, the thermal conductivity of the heat storage materials is generally low, so it takes a long time for heat to enter and exit, and the temperature difference between the input temperature and output temperature is large during heat radiation. small,
Often exhibits slow heat dissipation characteristics.

溶融塩の相変化に伴う体積変化が大きいため、
溶融塩を上部より凝固させると、熱伝達を著しく
低下させる原因となる所謂“す”が生ずる。
Because the volume change associated with the phase change of the molten salt is large,
If the molten salt is solidified from the top, a so-called "slug" is created which causes a significant reduction in heat transfer.

この発明は、上記実情に鑑み溶融塩のように融
解時に大きな体積膨張を伴い、且つ腐食性に留意
する必要のある潜熱蓄熱材料を用いる場合におけ
るシエル・チユーブ型蓄熱器の改良を目的とし、
その特徴は器内を、多数の取付孔を有する管板で
垂直方向に区切り、その一側に相変化により蓄放
熱作用を行う蓄熱材料の収容室を形成し、他側に
水室を形成し、上記収容室には収容される蓄熱材
料の界面下に曲率の異なる複数本のU字状伝熱管
を水平方向に、且つその複数本を垂直方向に沿つ
て多段状に配設し、更に上記U字状伝熱管の入口
及び出口を一方向に向けて上記管板の取付孔に嵌
合し、一方上記水室には垂直方向の仕切壁で仕切
り入水部と出水部を形成し、入水部には隣接する
各段のU字状伝熱管の入口が連通するように水平
方向の仕切壁を設け、出水部には隣接する各段の
U字状伝熱管の出口が連通するように水平方向の
仕切壁を設け、且つ上記入水部と出水部の仕切壁
を互い違いに配置し、上記伝熱管内には蓄熱時に
は上位の伝熱管より下位の伝熱管に熱媒体を流
し、放熱時には下位の伝熱管より上位の伝熱管に
熱媒体を流すようにしたことある。
In view of the above-mentioned circumstances, the present invention aims to improve a shell-tube heat storage device when using a latent heat storage material such as molten salt, which undergoes large volumetric expansion when melted and requires consideration of corrosivity.
The feature is that the inside of the vessel is vertically divided by a tube plate with many mounting holes, and on one side of the chamber is formed a storage chamber for a heat storage material that stores and releases heat through phase change, and on the other side is a water chamber. , a plurality of U-shaped heat exchanger tubes with different curvatures are arranged in the horizontal direction under the interface of the heat storage material to be accommodated in the storage chamber, and the plurality of U-shaped heat transfer tubes are arranged in a multi-tiered manner along the vertical direction, and further the above-mentioned The inlet and outlet of the U-shaped heat transfer tube are fitted into the mounting holes of the tube plate with the inlet and outlet facing in one direction, and the water chamber is partitioned with a vertical partition wall to form a water inlet and a water outlet. A partition wall is provided in the horizontal direction so that the inlets of the U-shaped heat exchanger tubes in each adjacent stage are connected to each other, and a partition wall is installed in the horizontal direction so that the outlet of the U-shaped heat exchanger tubes in each adjacent stage is connected to each other. partition walls are provided, and the partition walls between the water inlet and water outlet are arranged alternately, and when heat is stored in the heat transfer tubes, the heat medium flows from the upper heat transfer tube to the lower heat transfer tube, and during heat dissipation, the heat transfer medium flows through the lower heat transfer tube. I have tried to make the heat medium flow through the heat exchanger tubes above the heat exchanger tubes.

即ち、この発明では伝熱管を横向きに設置する
構造とし、しかもU字状伝熱管を用い、伝熱管と
管板との接続箇所を片側だけにしてあるため、デ
ンディングが生じ難い。
That is, in this invention, the heat exchanger tubes are installed horizontally, U-shaped heat exchanger tubes are used, and the connection between the heat exchanger tubes and the tube sheet is made only on one side, so that dending is less likely to occur.

また、伝熱管を横向きにし、しかも常に蓄熱材
料の界面下にあるため、上述の界面腐食の問題も
生じない。
Furthermore, since the heat exchanger tubes are oriented horizontally and are always under the interface of the heat storage material, the above-mentioned problem of interfacial corrosion does not occur.

更に、この発明では水室を上述のように細かく
仕切り、且つ伝熱管内には蓄熱時には上位の伝熱
管より下位の伝熱管に熱媒体を流し、放熱時には
下位の伝熱管より上位の伝熱管に熱媒体を流すよ
うにしたことあるため、蓄熱器内が常に上部が高
温、下部が低温に保たれる。このため、この発明
では蓄熱時には十分に熱媒体の温度が下がり、放
熱時にはより高い温度で熱が得られ、上述の従来
例のように緩慢な温度変化を示すことがない。
Furthermore, in this invention, the water chamber is divided finely as described above, and when storing heat, the heat medium flows from the upper heat exchanger tube to the lower heat exchanger tube, and during heat dissipation, the heat medium flows from the lower heat exchanger tube to the upper heat exchanger tube. Because a heat medium is allowed to flow through the heat storage unit, the upper part of the heat storage unit is always kept at a high temperature and the lower part is kept at a low temperature. Therefore, in the present invention, the temperature of the heat medium is sufficiently lowered during heat storage, and heat is obtained at a higher temperature during heat dissipation, and the temperature does not change slowly as in the above-mentioned conventional example.

また、この発明では上述のように熱媒体を流す
ことにより、蓄熱材料を常に上部から融解し、ま
た下部から凝固されるために、熱伝達を著しく低
下させる原因となる所謂“す”が生ずることもな
く同時に、蓄熱材料の融解時、凝固時にも容器や
伝熱管に大きな応力が作用することがない。
In addition, in this invention, by flowing the heat medium as described above, the heat storage material is always melted from the upper part and solidified from the lower part, so that so-called "su" which causes a significant decrease in heat transfer is generated. At the same time, no large stress is applied to the container or heat exchanger tubes when the heat storage material melts or solidifies.

以下、図示の実施例に基いてこの発明を説明す
る。
The present invention will be explained below based on illustrated embodiments.

10は、この発明に係る蓄熱器で、蓄熱器10
は通常は、常圧で設計され、その内部には横長円
筒状の収容室11が設けられる。収容室11の上
端にはその長手方向に沿つて蓄熱材料aの充填座
12,……が設けられ、また収容室11の下端に
はその長手方向に沿つて蓄熱材料aのドレン座1
3,……が設けられ、蓄熱材料aは上部に空間1
4を残して収容室11内に収容される。
10 is a heat storage device according to the present invention, and the heat storage device 10
is usually designed at normal pressure, and a horizontally long cylindrical storage chamber 11 is provided inside. At the upper end of the storage chamber 11, a filling seat 12, .
3,... are provided, and the heat storage material a has a space 1 at the top.
All but 4 are housed in the housing chamber 11.

一方収容室11内には、伝熱管15が水平方向
に、且つその複数本を垂直方向に沿つて多段状に
配設するとともに、多段状に配設された伝熱管1
5a,15b,……のうち最上段の伝熱管15a
が常に蓄熱材料aの界面下にあるように配置す
る。
On the other hand, inside the storage chamber 11, a plurality of heat exchanger tubes 15 are arranged in a horizontal direction and a plurality of heat exchanger tubes 15 are arranged in a multi-tiered manner along a vertical direction.
The uppermost heat exchanger tube 15a among 5a, 15b, ...
is arranged so that it is always under the interface of the heat storage material a.

この実施例では、各段に使用する伝熱管として
は曲率の異なる複数本のU字管が使用され、各段
におけるその配列は各U字管の入口16及び出口
17を収容室11の一方向に向け、且つ最外郭に
そのうち最も曲率の大きなU字管を配置し、内方
にゆくにしたがつて順次曲率の小さなU字管を配
置するようにする。これ等の伝熱管15は、収容
室11の一側に設けられ、その内部には多数の取
付孔を有する管板18の取付孔にその入口部及び
出口部を嵌合し、且つ伝熱管15の長手方向に沿
つて設けられた支持板20,……で収容室11内
に支持されている。
In this embodiment, a plurality of U-shaped tubes with different curvatures are used as heat transfer tubes in each stage, and the arrangement in each stage is such that the inlet 16 and outlet 17 of each U-shaped tube are directed in one direction of the storage chamber 11. The U-shaped tube with the largest curvature is placed at the outermost edge of the tube, and the U-shaped tubes with smaller curvature are placed inward. These heat exchanger tubes 15 are provided on one side of the storage chamber 11, and have their inlet and outlet portions fitted into attachment holes of a tube plate 18, which has a large number of attachment holes therein. It is supported within the storage chamber 11 by support plates 20, . . . provided along the longitudinal direction.

一方、管板18の一側には水室21を設け、且
つ該水室21は上記のように各段に複数本設けら
れたU字管の入口16a,16b,……と出口1
7a,17b,……を仕切る壁22を設け、その
左右に入水部23と出水部24を形成する。
On the other hand, a water chamber 21 is provided on one side of the tube plate 18, and the water chamber 21 is connected to the inlets 16a, 16b, . . . and the outlet 1 of the U-shaped tubes provided in each stage as described above.
A wall 22 is provided to partition 7a, 17b, . . . , and a water inlet part 23 and a water outlet part 24 are formed on the left and right sides thereof.

更に、入水部23には隣接する各段のU字管の
入口16o-1,16oが連通するように水平方向の
仕切壁25,……を設け、出水部24には隣接す
る各段のU字管の出口17o,17o+1が連通する
ように水平方向の仕切壁26,……を設け、仕切
壁25,……と仕切壁26,……とは互い違いに
配置される。
Further, the water inlet 23 is provided with horizontal partition walls 25 , . Horizontal partition walls 26, . . . are provided so that the outlets 17o , 17o +1 of the U-shaped tubes communicate with each other, and the partition walls 25, . . . and the partition walls 26, . .

以上の構成において、熱媒体は入水部23に設
けられた入口部27より入水部23に入水され
る。入水部23に入水された熱媒体は最上段のU
字管の入口16aに送入され、U字管内を通過し
てその出口17aより出水部25内に送入され、
出水部24では次段のU字管の出口17bよりU
字管内に送入されて管内を通過するようにして順
次下方に移行させ、最下段のU字管の出口より出
水部24内に排出された熱媒体は出水部24に設
けられた出口部28より系外に排出される。
In the above configuration, the heat medium enters the water inlet part 23 through the inlet part 27 provided in the water inlet part 23. The heat medium that has entered the water inlet section 23 is
The water is fed into the inlet 16a of the U-shaped tube, passes through the U-shaped tube, and is fed into the water outlet 25 from the outlet 17a,
In the water outlet 24, the U-shaped pipe is
The heat medium is introduced into the pipe, passed through the pipe, moved downward one by one, and discharged into the water outlet part 24 from the outlet of the lowest U-shaped pipe. is discharged from the system.

このようにして熱媒体が蓄熱器10内に多段状
に設けられたU字状の伝熱管15内を通過して順
次下方に移送される間に、熱媒体の含有する熱は
収容室11内に収容された蓄熱材料a内に蓄熱さ
れる。
In this way, while the heat medium passes through the U-shaped heat transfer tubes 15 provided in multiple stages in the heat storage device 10 and is sequentially transferred downward, the heat contained in the heat medium is transferred into the storage chamber 11. Heat is stored in the heat storage material a housed in the heat storage material a.

また、蓄熱材料a内に蓄熱された熱を放熱させ
る場合には反対に出口部28より熱媒体を出水部
24内に送入し、多段状に設けられたU字状の伝
熱管15を上方へ順次移送し、その間に蓄熱材料
aに蓄熱された熱を熱媒体へ放熱させる。
When the heat stored in the heat storage material a is to be radiated, on the contrary, the heat medium is fed into the water outlet part 24 from the outlet part 28, and the U-shaped heat transfer tubes 15 provided in multiple stages are directed upward. During this period, the heat stored in the heat storage material a is radiated to the heat medium.

以上のように、この発明によれば蓄熱器10内
に水平方向に、且つその複数本を垂直方向に多段
状に配設し、それぞれを連通した伝熱管15内
を、蓄熱時には上方より下方へ、放熱時には下方
より上方へ移送するものであり、したがつて蓄熱
時には蓄熱材料aを上方より順次融解させること
ができ、このため蓄熱材料aの融解時における体
積膨張を吸収することができる。
As described above, according to the present invention, a plurality of tubes are arranged horizontally in the heat storage device 10 and in a multi-tiered manner vertically, and the inside of the heat transfer tubes 15 in which the tubes are communicated with each other is arranged from the top to the bottom during heat storage. During heat dissipation, the heat is transferred from the bottom to the top. Therefore, during heat storage, the heat storage material a can be sequentially melted from the top, and therefore the volumetric expansion of the heat storage material a when it is melted can be absorbed.

また、この発明によれば多段状に配設された伝
熱管のうち最上位にあるものが常に蓄熱材料aの
界面下にあるため、蓄熱材料aの界面は収容室1
1の内壁としか接触せず、したがつて蓄熱、放熱
時に蓄熱材料aの界面が変動しても蓄熱器10内
の腐食を少くすることができる。
Furthermore, according to the present invention, the uppermost one among the heat exchanger tubes arranged in multiple stages is always under the interface of the heat storage material a, so that the interface of the heat storage material a is
Therefore, even if the interface of the heat storage material a fluctuates during heat storage and heat dissipation, corrosion within the heat storage device 10 can be reduced.

なお、収容室11の内壁については耐食材料の
ライニング等を施せば蓄熱材料aの界面変動によ
る腐食を完全に抑制することができる。
Note that if the inner wall of the storage chamber 11 is lined with a corrosion-resistant material, corrosion due to interface fluctuations of the heat storage material a can be completely suppressed.

また、この発明では伝熱管15は水平に設置さ
れ、且つ蓄熱材料aの界面下に常にあるため、ク
リーピング現象を防止することができる。
Further, in the present invention, the heat transfer tubes 15 are installed horizontally and are always under the interface of the heat storage material a, so that creeping phenomenon can be prevented.

更に、この発明では水平に配置された伝熱管1
5内に熱媒体を通過させるため、伝熱管15の長
手方向の温度差が小さく、したがつて質量移行現
象が殆んど生じない。
Furthermore, in this invention, the heat exchanger tubes 1 arranged horizontally
Since the heat medium is passed through the heat exchanger tubes 15, the temperature difference in the longitudinal direction of the heat exchanger tubes 15 is small, and therefore the mass transfer phenomenon hardly occurs.

また、この実施例では各段に使用する伝熱管1
5としては曲率の異なる複数本のU字管が使用さ
れ、各段におけるその配列は最外郭に最も曲率の
大きなU字管を配置し、内方にゆくにしたがつて
順次曲率の小さなU字管を配置するようにしてあ
るため、これ等のU字管内を蓄熱時には熱媒体を
上方から移送し、放熱時には下方から移送するこ
とにより、蓄熱材料aの融解と凝固とを円滑に行
わせることができる。
In addition, in this embodiment, the heat exchanger tubes 1 used in each stage are
5, a plurality of U-shaped tubes with different curvatures are used, and the arrangement in each stage is such that the U-shaped tube with the largest curvature is placed on the outermost part, and the U-shaped tubes with smaller curvature are placed inward. Since the tubes are arranged, the heat medium is transferred from above when storing heat in these U-shaped tubes, and from below when dissipating heat, thereby melting and solidifying the heat storage material a smoothly. I can do it.

また、U字管を伝熱管として使用するため、伝
熱管の熱膨張に対する対策を特に必要としない。
Furthermore, since the U-shaped tube is used as the heat transfer tube, no special measures are required against thermal expansion of the heat transfer tube.

更に、この方式では従来のU字管式シエル・チ
ユーブ型熱交換器と同型であるため、従来の技術
を十分に適用でき、コストを安くすることができ
る。
Furthermore, since this system is of the same type as the conventional U-tube type shell tube heat exchanger, conventional techniques can be fully applied and costs can be reduced.

なお、以上の実施例ではU字管を使用する実施
例について説明したが、伝熱管として直管を使用
することもできる。
Although the above embodiments have been described using U-shaped tubes, straight tubes may also be used as the heat transfer tubes.

この場合は、当然水室及び熱媒体の折り返し側
の仕切室又は遊動頭内では第3図のように熱媒体
の流路を変える必要がある。
In this case, it is of course necessary to change the flow path of the heat medium in the water chamber and the partition on the folded side of the heat medium or in the floating head as shown in FIG.

更に、遊動頭式は別として固定管板式では伝熱
管の胴部に膨張継手を設ける必要がある。
Furthermore, apart from the floating head type, in the fixed tube sheet type, it is necessary to provide an expansion joint in the body of the heat transfer tube.

以上要するに、この発明によれば特に高温潜熱
蓄熱材を用いる蓄熱器における技術的問題点の大
半を解決でき、したがつてこれ等の問題点のため
に今までなかなか推進することができなかつた高
温潜熱蓄熱技術を、強力に推進させ、エネルギー
の有効利用を図ることができる。
In summary, according to the present invention, it is possible to solve most of the technical problems particularly in heat storage devices using high-temperature latent heat storage materials, and therefore, it is possible to solve high temperature It is possible to strongly promote latent heat storage technology and aim for effective use of energy.

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

第1図は、従来のシエル・チユーブ型蓄熱器の
概略を示す縦断側面図、第2図は、従来のカプセ
ル型蓄熱器の概略を示す縦断側面図、第3図は、
この発明の一実施例を示す縦断側面図、第4図
は、同上の−線断面図、第5図は、第3図の
−線断面図、第6図は、第3図の−線断
面図である。 図中、10は蓄熱器、15は伝熱管。
FIG. 1 is a vertical side view schematically showing a conventional shell tube type heat storage device, FIG. 2 is a vertical side view schematically showing a conventional capsule type heat storage device, and FIG.
FIG. 4 is a sectional view taken along the line ``-'' in FIG. 3, and FIG. 6 is a sectional view taken along the line ``-'' in FIG. 3. It is a diagram. In the figure, 10 is a heat storage device, and 15 is a heat exchanger tube.

Claims (1)

【特許請求の範囲】[Claims] 1 器内を、多数の取付孔を有する管板で垂直方
向に区切り、その一側に相変化により蓄放熱作用
を行う蓄熱材料の収容室を形成し、他側に水室を
形成し、上記収容室には収容される蓄熱材料の界
面下に曲率の異なる複数本のU字状伝熱管を水平
方向に、且つその複数本を垂直方向に沿つて多段
状に配設し、更に上記U字状伝熱管の入口及び出
口を一方向に向けて上記管板の取付孔に嵌合し、
一方上記水室には垂直方向の仕切壁で仕切り入水
部と出水部を形成し、入水部には隣接する各段の
U字状伝熱管の入口が連通するように水平方向の
仕切壁を設け、出水部には隣接する各段のU字状
伝熱管の出口が連通するように水平方向の仕切壁
を設け、且つ上記入水部と出水部の仕切壁を互い
違いに配置し、上記伝熱管内には蓄熱時には上位
の伝熱管より下位の伝熱管に熱媒体を流し、放熱
時には下位の伝熱管より上位の伝熱管に熱媒体を
流すようにしたことを特徴とする蓄熱器。
1. The inside of the vessel is vertically divided by a tube plate having a large number of mounting holes, and on one side thereof a storage chamber for a heat storage material that stores and releases heat through phase change is formed, and on the other side a water chamber is formed, and the above-mentioned In the storage chamber, a plurality of U-shaped heat exchanger tubes with different curvatures are arranged horizontally below the interface of the heat storage material to be accommodated, and the plurality of U-shaped heat transfer tubes are arranged in multi-tiered form along the vertical direction, and the U-shaped Fitting the shaped heat transfer tube into the mounting hole of the tube plate with the inlet and outlet facing in one direction,
On the other hand, in the water chamber, a vertical partition wall is used to form a partitioned water inlet and a water outlet, and a horizontal partition wall is provided in the water inlet so that the inlets of the U-shaped heat transfer tubes of each adjacent stage communicate with each other. , horizontal partition walls are provided in the water outlet section so that the outlets of the U-shaped heat transfer tubes of adjacent stages communicate with each other, and the partition walls of the water input section and the water outlet section are arranged alternately, so that the heat transfer A heat storage device characterized in that during heat storage, a heat medium is allowed to flow from an upper heat transfer tube to a lower heat transfer tube, and during heat dissipation, a heat medium is made to flow from a lower order heat transfer tube to an upper heat transfer tube.
JP59020399A 1984-02-07 1984-02-07 Heat accumulator Granted JPS60164196A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59020399A JPS60164196A (en) 1984-02-07 1984-02-07 Heat accumulator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59020399A JPS60164196A (en) 1984-02-07 1984-02-07 Heat accumulator

Publications (2)

Publication Number Publication Date
JPS60164196A JPS60164196A (en) 1985-08-27
JPH041277B2 true JPH041277B2 (en) 1992-01-10

Family

ID=12025939

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59020399A Granted JPS60164196A (en) 1984-02-07 1984-02-07 Heat accumulator

Country Status (1)

Country Link
JP (1) JPS60164196A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2025128379A (en) * 2022-03-14 2025-09-02 国立大学法人東京科学大学 Chemical heat storage block, chemical heat storage device, and chemical heat storage and heat release method

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106766490A (en) * 2017-01-04 2017-05-31 合肥华凌股份有限公司 An energy storage tube and a refrigerator
CN109282511A (en) * 2018-08-20 2019-01-29 昆明理工大学 A low temperature solar energy efficient heat storage device
WO2020250970A1 (en) * 2019-06-12 2020-12-17 パナソニック株式会社 Heat storage device

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5924799B2 (en) * 1977-01-31 1984-06-12 日立造船株式会社 Regenerative heat exchanger
JPS5712256A (en) * 1980-06-25 1982-01-22 Nippon Tokkyo Kanri Kk Heat storage device for solar heat utilization equipment

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2025128379A (en) * 2022-03-14 2025-09-02 国立大学法人東京科学大学 Chemical heat storage block, chemical heat storage device, and chemical heat storage and heat release method

Also Published As

Publication number Publication date
JPS60164196A (en) 1985-08-27

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