JPS635675B2 - - Google Patents
Info
- Publication number
- JPS635675B2 JPS635675B2 JP58030120A JP3012083A JPS635675B2 JP S635675 B2 JPS635675 B2 JP S635675B2 JP 58030120 A JP58030120 A JP 58030120A JP 3012083 A JP3012083 A JP 3012083A JP S635675 B2 JPS635675 B2 JP S635675B2
- Authority
- JP
- Japan
- Prior art keywords
- heat
- heat exchanger
- heat storage
- shell tank
- storage material
- 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
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D20/00—Heat storage plants or apparatus in general; Regenerative heat-exchange apparatus not covered by groups F28D17/00 or F28D19/00
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/14—Thermal 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】
本発明は化学反応を用いて蓄熱を行なうことの
できる蓄熱装置に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a heat storage device that can store heat using chemical reactions.
省エネルギー技術の一環として、各種の蓄エネ
ルギー、蓄熱技術が研究開発され、各種の方法が
提案されている。蓄熱技術には
(a) 顕熱蓄熱
(b) 潜熱蓄熱
(c) 化学反応蓄熱
などに分類され、常温においても蓄熱状態を維持
し得る特徴をもつ(c)についての蓄熱物質による熱
輸送が可能な蓄熱装置が考えられている。 As part of energy saving technology, various energy storage and heat storage technologies have been researched and developed, and various methods have been proposed. Heat storage technology is classified into (a) sensible heat storage, (b) latent heat storage, (c) chemical reaction heat storage, etc., and (c) can transport heat using heat storage materials that have the characteristic of maintaining heat storage even at room temperature. A heat storage device is being considered.
すなわち、次のような可逆反応 A・B+QA+B (1) なる反応系があつたとする。 That is, the following reversible reaction A・B+QA+B (1) Suppose we have a reaction system like this.
蓄熱工程では、物質A・BにエネルギーQを加
え、AとBの物質に分解して分離・貯蔵する。Q
は通常熱エネルギーが考えられるが、光、電気な
ど他のエネルギーも利用される。 In the heat storage process, energy Q is added to substances A and B to decompose them into substances A and B, which are then separated and stored. Q
Usually, thermal energy is considered, but other energies such as light and electricity can also be used.
放熱工程では、熱が必要な時にAとBの物質を
反応させることによつて反応熱Qを発生させ、熱
を取り出す。 In the heat dissipation step, when heat is required, reaction heat Q is generated by reacting substances A and B, and the heat is extracted.
この時、物質AとBをそれぞれ化学変化を生じ
ない状態で貯蔵すれば、蓄熱工程と放熱工程の間
に時間的あるいは場所的な隔りがあつても、蓄・
放熱サイクルは成立するので、熱輪送が可能であ
る。 At this time, if substances A and B are stored in a state where no chemical changes occur, even if there is a time or place gap between the heat storage process and the heat release process, the storage and
Since the heat dissipation cycle is established, heat transfer is possible.
なお、AとBの物質は例えばAが固体、Bが液
体または気体のようにA〜B間が分離し易い状
態、すなわち相の異なつた状態が利用される。例
えばAとして硫化ナトリウム、Bとして水(水蒸
気)が考えられる。 Note that the substances A and B are used in a state in which A and B are easily separated, ie, in a state in which they have different phases, such that A is a solid and B is a liquid or gas. For example, A may be sodium sulfide, and B may be water (steam).
本発明は、このような一般的な化学反応熱を利
用した蓄熱技術のうち、次のような限定された条
件下で実施される蓄熱装置に関する。 The present invention relates to a heat storage device that is implemented under the following limited conditions among such general heat storage techniques that utilize the heat of chemical reaction.
(1) 蓄熱工程は、発熱など余剰熱源が存在する場
所Xで実施され、放熱工程はAとBを反応させ
て発生する熱を利用熱源とする場所Yで実施さ
れる。場所Xで蓄熱された物質をYまで輸送、
放熱し、放熱後再蓄熱のために蓄熱物質をXに
再輸送する。(1) The heat storage process is carried out at a location X where there is a surplus heat source such as heat generation, and the heat dissipation process is carried out at a location Y where the heat generated by reacting A and B is utilized as a heat source. Transport the material stored in heat at location X to Y,
Heat is released, and after heat release, the heat storage material is transported back to X for restorage.
(2) 輸送される蓄熱物質はAとB、もしくはAと
考える。すなわち、反応物Bが水蒸気のような
通常容易に入手あるいは廃棄できる物質で、X
において分離したBをYまで輸送しなくてもY
で入手できれば放熱反応は可能となるので、こ
の場合Aのみを輸送すれば良いことになる。本
発明では、Bの輸送の有無にかかわらず、蓄熱
物質Aのみの輸送に関する。(2) The heat storage materials to be transported are considered to be A and B, or A. That is, reactant B is a substance such as water vapor that is normally easily available or discarded, and X
Even if B separated at is not transported to Y, Y
If A is available, a heat dissipation reaction will be possible, so in this case it is only necessary to transport A. The present invention relates to the transportation of only the heat storage material A, regardless of whether or not B is transported.
(3) 反応条件下においては、物質A・BおよびA
は固体粒子、Bは気体である。すなわち、蓄熱
物質Aは、空気と長期間接触すると空気中の酸
素、炭酸ガス、水分などと反応し、変質もしく
は放熱するものである。本発明では、特に人体
と接触すると有害な物質に対して有効である。(3) Under the reaction conditions, substances A, B and A
is a solid particle and B is a gas. That is, when the heat storage material A comes into contact with air for a long period of time, it reacts with oxygen, carbon dioxide, moisture, etc. in the air, and changes in quality or releases heat. The present invention is particularly effective against substances that are harmful when they come into contact with the human body.
上記のような条件下で蓄熱システムを構成する
場合、通常蓄熱槽を輸送することになるが、これ
を第1図を例にとつて説明する。第1図は蓄熱槽
の断面図であり、1は蓄熱槽本体、2は多極式熱
交換器の場合は伝熱管、プレート式熱交換器の場
合は伝熱プレートを表わす。3は蓄熱槽への熱交
換流体流入部、4は熱交換流体流出部、5は伝熱
管または伝熱プレート2により熱交換流体と隔絶
された蓄熱物質充填部、6は蓄熱物質充填部5へ
の蒸気出入部である。 When constructing a heat storage system under the above conditions, the heat storage tank is normally transported, and this will be explained using FIG. 1 as an example. FIG. 1 is a sectional view of a heat storage tank, where 1 represents the heat storage tank body, 2 represents heat transfer tubes in the case of a multipolar heat exchanger, and heat transfer plates in the case of a plate heat exchanger. 3 is a heat exchange fluid inflow part to the heat storage tank, 4 is a heat exchange fluid outlet part, 5 is a heat storage material filling part isolated from the heat exchange fluid by a heat transfer tube or heat transfer plate 2, and 6 is a heat storage material filling part 5 This is the steam inlet and outlet section.
蓄熱工程は次の通りである。すなわち、上記条
件(1)から場所Xには余剰熱源が存在するので、こ
の熱を流体熱媒体を介して流入部3から蓄熱槽へ
導入する。熱媒体は伝熱管または伝熱プレート2
内を通過する間に伝熱壁面を通して充填部5の粒
子層に熱を与えた後、流出部4から排出される。
この与えられた熱によつて反応式(1)の左から右へ
の反応が生じ、Aなる固体とBなる気体が生成す
る。発生した気体Bは蒸気出入部6に取付けられ
たバルブ7を通つて蓄熱槽外に排出され、冷却に
よる凝縮、圧縮による液化、吸収剤による吸収な
どの操作によつて貯蔵部(図示せず)を貯蔵され
る。反応が終了したならば、バルブ7を閉鎖して
充填部5を外気と遮断するとともに、熱交換流体
流入部3、流出部4、バルブ7をこれに接続する
配管部(図示せず)から切り離す。 The heat storage process is as follows. That is, since a surplus heat source exists at the location X based on the above condition (1), this heat is introduced from the inflow portion 3 to the heat storage tank via the fluid heat medium. The heat medium is a heat transfer tube or heat transfer plate 2
After imparting heat to the particle layer in the filling part 5 through the heat transfer wall surface while passing through the inside, the particles are discharged from the outflow part 4.
This applied heat causes a reaction from left to right in reaction formula (1), producing a solid A and a gas B. The generated gas B is discharged to the outside of the heat storage tank through the valve 7 attached to the steam inlet/outlet part 6, and is transferred to a storage part (not shown) through operations such as condensation by cooling, liquefaction by compression, and absorption by an absorbent. is stored. When the reaction is completed, the valve 7 is closed to isolate the filling section 5 from the outside air, and the heat exchange fluid inflow section 3, outflow section 4, and valve 7 are separated from the piping section (not shown) that connects them. .
輸送工程では、第1図に示した蓄熱槽部分と、
必要ならばBの貯蔵部とを何らかの輸送手段例え
ばトラツク、鉄道などによつてXからYまで輸送
する。 In the transportation process, the heat storage tank part shown in Figure 1,
If necessary, the storage portion of B is transported from X to Y by some means of transportation, such as a truck or a railway.
放熱工程は次の通りである。すなわち、場所Y
において、熱を回収するための熱媒体の流入配管
部に流入部3を、排出配管部に流出部4を接続す
るとともに、バルブ7を気体Bの導入部(もしく
は同時に輸送してきたBの貯蔵部)に接続する。
そして熱回収媒体を流入部3から流出部4へ流し
ながらバルブ7を開放すると、気体Bが蓄熱物質
充填部5に流入し、反応式1の右から左に進む反
応によつて反応熱を発生する。この熱は伝熱管ま
たは伝熱プレート2を通して熱回収媒体に移動し
て回収される。反応終了後は、蓄熱工程終了と同
様、バルブ7を閉鎖し、流入部3、流出部4、バ
ルブ7をこれに接続する配管部から切り離す。 The heat dissipation process is as follows. That is, location Y
, the inflow part 3 is connected to the inflow pipe part of the heat medium for recovering heat, and the outflow part 4 is connected to the discharge pipe part, and the valve 7 is connected to the introduction part of gas B (or to the storage part of B transported at the same time). ).
Then, when the valve 7 is opened while the heat recovery medium is flowing from the inflow part 3 to the outflow part 4, the gas B flows into the heat storage material filling part 5, and reaction heat is generated by the reaction proceeding from right to left in reaction formula 1. do. This heat is transferred to a heat recovery medium through heat transfer tubes or heat transfer plates 2 and is recovered. After the reaction is completed, the valve 7 is closed, and the inflow section 3, the outflow section 4, and the valve 7 are separated from the piping section connected thereto, similarly to the end of the heat storage step.
次の輸送工程では、第1図に示した蓄熱槽部分
と、必要ならばB貯蔵部の空容器とをYからXに
輸送する。そして、流入部3、流出部4、バルブ
7をそれぞれ必要部分に接続し、再び蓄熱工程を
実施する。 In the next transportation step, the heat storage tank portion shown in FIG. 1 and, if necessary, the empty container of the B storage section are transported from Y to X. Then, the inflow part 3, the outflow part 4, and the valve 7 are connected to necessary parts, respectively, and the heat storage process is performed again.
以上が上記条件下における通常の熱輸送可能な
蓄熱装置であるが、この場合の長所および短所を
述べると次のようになる。 The above is a typical heat storage device capable of transporting heat under the above conditions, and the advantages and disadvantages of this case are as follows.
長 所
(イ) 熱交換部から蓄熱物質粒子を分離しなくて良
い。もし、蓄熱物質粒子のみを輸送するとする
と、蓄・放熱工程1サイクル当り、熱交換部へ
の粒子の充填、分離作業をそれぞれ2回ずつ行
なわなければならないが、この方法によれば、
その手間が省け、そのための設備も不要であ
る。Advantages (a) There is no need to separate heat storage material particles from the heat exchange section. If only the heat storage material particles were to be transported, each cycle of the heat storage/radiation process would require the filling and separation of the particles into the heat exchange section twice, but with this method,
This saves time and requires no equipment.
(ロ) また、蓄・放熱工程から輸送工程に移る際に
も、バルブ7を閉鎖するだけでよく、蓄熱物質
が人体に接触することもなく、外気と遮断され
た状態下で作業が行なえる。(b) Also, when moving from the heat storage/dissipation process to the transportation process, it is only necessary to close the valve 7, so the heat storage material does not come into contact with the human body, and the work can be carried out in a state where it is isolated from the outside air. .
短 所
(イ) 一般に、固体粒子の熱伝導度は小さく、単位
時間当りの熱移動量を大きくしようとすると、
伝熱面積が増加し、熱交換部重量が増加する。
また、蓄・放熱反応を加圧もしくは減圧で行な
わせる場合が多いがこの時は蓄熱槽を耐圧構造
にする必要から蓄熱槽の外殻部重量も増加す
る。それ故蓄熱物質粒子のみの輸送に比べると
はるかに輸送重量が増加する。Disadvantages (a) Generally, the thermal conductivity of solid particles is low, and if you try to increase the amount of heat transfer per unit time,
The heat transfer area increases and the weight of the heat exchange section increases.
Furthermore, heat storage and heat dissipation reactions are often carried out under increased pressure or reduced pressure, but in this case, the heat storage tank must have a pressure-resistant structure, which increases the weight of the outer shell of the heat storage tank. Therefore, compared to transporting only heat storage material particles, the transport weight increases significantly.
(ロ) 輸送工程から蓄・放熱工程に移る際には、少
なくとも熱源あるいは熱回収のための熱媒体の
流出入部の配管部への接続と、反応気体の流出
入部の配管部への接続が必要であり、この接続
に手間がかかる。現在ワンタツチ式接手と呼ば
れるものが入手可能であるが、大口径の配管用
のものは現実には入手困難である。(b) When moving from the transportation process to the heat storage/radiation process, it is necessary to connect at least the inflow/outflow part of the heat source or heat medium for heat recovery to the piping part, and the connection of the inflow/outflow part of the reaction gas to the piping part. This connection takes time and effort. Currently, what is called a one-touch type joint is available, but it is actually difficult to obtain one for large diameter piping.
本発明は、以上のような事柄を考え、効率的な
熱輸送を行なうことのできる蓄熱装置を提供する
ことを目的とするものである。 The present invention has been made in consideration of the above-mentioned problems, and an object of the present invention is to provide a heat storage device that can efficiently transport heat.
本発明は上記目的を達成するために、挿抜可能
な内殻槽を持つた外殻槽と、前記外殻槽に取り外
し自在に連結されるとともに、伝熱管または伝熱
プレートとその先端に着脱自在に取り付けられる
同一直径の伝熱管ダミーとを上下方向に有し、こ
れらが前記内殻槽内部空間に収められた熱交換部
とを具備し、前記内殻槽の上下方向中間部に前記
伝熱管ダミーが貫通可能な隔壁を設け、前記隔壁
上の内殻槽内に充填された蓄熱物質は前記熱交換
部の伝熱管または伝熱プレートと接触可能である
とともに、前記熱交換部を上方に抜き出して前記
伝熱管ダミーを前記伝熱管または伝熱プレートよ
り離脱させた時に前記蓄熱物質は前記伝熱管ダミ
ーに接触して隔壁上に保持されるように構成し、
前記熱交換部に前記内殻槽内の蓄熱物質充填空間
に連通する気体出入口を設けたものであり、熱交
換部を引き上げ、伝熱管ダミーを蓄熱物質の中に
残して伝熱管または伝熱プレートを取り外し、そ
の後に前記伝熱管ダミーの接続部に係合可能な嵌
め合い部をもつた上蓋を内殻槽に取付ければ、内
殻槽は輸送できて、別の場所で熱交換が可能とな
る。このとき、輸送工程では熱交換部と外殻槽を
輸送しなくても良いので、輸送重量が大巾に軽減
できるとともに、熱交換部の反応気体の出入口
や、熱交換流体の流入口、流出口はフレキシブル
ホースなどを利用して接続しておくだけでよいの
で、輸送の度に配管部と着脱する必要がなく、さ
らに、蓄熱物質粒子の分離作業は人体を直接接触
することがなく、また長時間空気と接触すること
もない状態で行なえるので、都合がよい。 In order to achieve the above object, the present invention includes an outer shell tank having an insertable and removable inner shell tank, which is removably connected to the outer shell tank, and is detachably connected to a heat exchanger tube or a heat exchanger plate and its tip. and heat exchanger tube dummies of the same diameter that are attached to the inner shell tank in the vertical direction, and a heat exchange section that is housed in the inner space of the inner shell tank, and the heat exchanger tube dummy is installed in the vertical middle part of the inner shell tank. A partition wall that can be penetrated by the dummy is provided, and the heat storage material filled in the inner shell tank on the partition wall can come into contact with the heat exchanger tube or heat transfer plate of the heat exchanger, and the heat exchanger can be extracted upwardly. when the heat exchanger tube dummy is separated from the heat exchanger tube or the heat exchanger plate, the heat storage material contacts the heat exchanger tube dummy and is held on the partition wall,
The heat exchange section is provided with a gas inlet/outlet communicating with the heat storage material filling space in the inner shell tank, and the heat exchange section is pulled up and the heat exchanger tube dummy is left in the heat storage material and the heat exchanger tube or heat exchanger plate is removed. If the inner shell tank is removed and then a top cover with a fitting part that can be engaged with the connection part of the heat transfer tube dummy is attached to the inner shell tank, the inner shell tank can be transported and heat exchanged at another location. Become. At this time, there is no need to transport the heat exchange section and the outer shell tank during the transportation process, so the transportation weight can be greatly reduced. The outlet only needs to be connected using a flexible hose, etc., so there is no need to connect and disconnect the piping each time it is transported.Furthermore, separation of heat storage material particles does not involve direct contact with the human body. This is convenient because it can be carried out without coming into contact with air for a long period of time.
以下本発明の一実施例を図面に基づいて説明す
る。第2図はその断面図である。11は鉄、ステ
ンレス鋼などの金属製の熱交換部、12は必要な
らば耐圧のための厚さを持つ金属製の外殻槽で、
フランジ部11a,12aを介して取り外し自在
に連結されている。熱交換部11は複数の伝熱管
13を有し、その先端に同一直径の伝熱管ダミー
14が着脱自在に取り付けられており、熱交換部
11と外殻槽12がフランジ部11a,12aを
介して連結されたときに、前記伝熱管13及び伝
熱管ダミー14の全長は外殻槽12に挿抜可能に
内装された内殻槽15の内部空間に収まる程度の
長さを有している。前記伝熱管13は2重管構造
に構成され、先端部で円筒部と外筒部は互いに連
通するとともに基部で円筒部は熱交換流体流入口
16に接続され、外筒部は熱交換流体流出口17
に接続されている。また、内殻槽15の上下方向
中間部に、例えば前記伝熱管13と伝熱管ダミー
14との接続点相当位置の高さに、前記伝熱管1
3およびび伝熱管ダミー14が貫通可能でかつ、
内殻槽15の内部空間を上下に2分する隔壁18
が設けられ、上部の伝熱管間空間が蓄熱物質19
を収納するための蓄熱物質充填部20に構成さ
れ、その中に蓄熱物質19が外殻槽12のフラン
ジ部12aを越えない程度に充填され、熱交換部
11の伝熱管13と接触するようになつている。
21は熱交換部11に設けられた気体出入口で、
内殻槽15の蓄熱物質充填部20に連通するよう
に構成されており、バルブ22が設けられてい
る。23はフランジ部11a,12aに介装され
るOリング、24は後述するボルト用のネジ穴、
25は吊り下げ具である。前記内殻槽15と伝熱
管ダミー14はプラスチツクなどの非金属材料も
しくは比重4.6以下の軽量金属材料からなる。 An embodiment of the present invention will be described below based on the drawings. FIG. 2 is a sectional view thereof. 11 is a heat exchanger made of metal such as iron or stainless steel; 12 is a metal outer shell tank having a thickness for pressure resistance if necessary;
They are removably connected via flange portions 11a and 12a. The heat exchange part 11 has a plurality of heat exchanger tubes 13, and a heat exchanger tube dummy 14 of the same diameter is detachably attached to the tip of each heat exchanger tube dummy 14, and the heat exchange part 11 and the outer shell tank 12 are connected to each other via flange parts 11a and 12a. When connected together, the total length of the heat exchanger tubes 13 and the heat exchanger tube dummy 14 is long enough to fit into the internal space of the inner shell tank 15 that is removably inserted into the outer shell tank 12. The heat exchanger tube 13 has a double tube structure, and the cylindrical part and the outer cylindrical part communicate with each other at the tip, and the cylindrical part is connected to the heat exchange fluid inlet 16 at the base, and the outer cylindrical part communicates with the heat exchange fluid flow. Exit 17
It is connected to the. Further, the heat exchanger tube 1 is placed in the middle part of the inner shell tank 15 in the vertical direction, for example, at a height corresponding to the connection point between the heat exchanger tube 13 and the heat exchanger tube dummy 14.
3 and the heat exchanger tube dummy 14 can be penetrated, and
A partition wall 18 that divides the internal space of the inner shell tank 15 into upper and lower halves.
is provided, and the space between the upper heat transfer tubes is a heat storage material 19
The heat storage material 19 is filled in the heat storage material filling part 20 to accommodate the heat storage material 19 to the extent that it does not exceed the flange part 12a of the outer shell tank 12, and is in contact with the heat exchanger tube 13 of the heat exchange part 11. It's summery.
21 is a gas inlet/outlet provided in the heat exchange section 11;
It is configured to communicate with the heat storage material filling section 20 of the inner shell tank 15, and is provided with a valve 22. 23 is an O-ring interposed in the flange portions 11a and 12a, 24 is a screw hole for a bolt to be described later,
25 is a hanging tool. The inner shell tank 15 and the heat exchanger tube dummy 14 are made of a non-metallic material such as plastic or a lightweight metallic material with a specific gravity of 4.6 or less.
蓄熱工程では、熱源流体が流入口16から流入
し、伝熱管13を通過する間に蓄熱物質19の粒
子層に熱を与え、流出口17から流出する。一
方、従来例と同じく熱の授受によつて気体Bが粒
子層から発生し、この気体Bの移動は気体出入口
21を通して行なわれる。放熱工程では、逆に気
体出入口21から気体Bが供給され、蓄熱物質1
9の粒子層に吸収され、熱を発生し、この熱は流
入口16から流入する熱回収用流体に伝熱され、
流出口17から回収される。 In the heat storage step, the heat source fluid flows in from the inlet 16 , gives heat to the particle layer of the heat storage material 19 while passing through the heat transfer tube 13 , and flows out from the outlet 17 . On the other hand, as in the conventional example, gas B is generated from the particle layer by exchange of heat, and movement of this gas B is performed through the gas inlet/outlet 21. In the heat dissipation process, gas B is supplied from the gas inlet/outlet 21 and the heat storage material 1
It is absorbed by the particle layer 9 and generates heat, and this heat is transferred to the heat recovery fluid flowing in from the inlet 16.
It is collected from the outlet 17.
蓄熱物質19の取出し工程では、蓄熱もしくは
放熱工程終了後、外殻槽12から熱交換部11を
分離するために、吊り下げ具25によつて上方に
引き抜く操作を行なう。この時伝熱管13の先端
部に接続した伝熱管ダミー14も上方に移動し、
前に蓄熱物質19の粒子層内の伝熱管13の存在
した部分に粒子層の崩れのない状態ではまり込
む。この状態を示したものが第4図である。な
お、第3図は伝熱管13と伝熱管ダミー14の接
続部の例を示したもので、互いに嵌め合い・取り
外しが自在になつており、伝熱管13の軸方向の
引張りもしくは押し出し動作に対しては分離せ
ず、伝熱管軸に対して直角もしくはその他の方向
の動作に対してはワンタツチ式に着脱できる構造
になつていれば、第3図以外の構造でも良い。例
えば第4図の状態から熱交換部11を矢印A方向
に移動させれば、伝熱管とダミーが分離できる。 In the step of taking out the heat storage material 19, after the heat storage or heat radiation step is completed, an operation of pulling the heat exchanger 11 upwardly using the hanging tool 25 is performed in order to separate the heat exchanger 11 from the outer shell tank 12. At this time, the heat exchanger tube dummy 14 connected to the tip of the heat exchanger tube 13 also moves upward,
The heat exchanger tube 13 is fitted into the part of the particle layer of the heat storage material 19 where the heat transfer tube 13 was previously present without the particle layer being collapsed. FIG. 4 shows this state. In addition, FIG. 3 shows an example of the connection part between the heat exchanger tube 13 and the heat exchanger tube dummy 14, which can be fitted into and removed from each other freely, and is resistant to axial tension or extrusion of the heat exchanger tube 13. A structure other than that shown in FIG. 3 may be used as long as it does not separate and can be attached and detached in a one-touch manner for operation perpendicular to the axis of the heat exchanger tube or in other directions. For example, by moving the heat exchanger 11 in the direction of arrow A from the state shown in FIG. 4, the heat exchanger tube and the dummy can be separated.
次に、第5図のように、伝熱管13と同じ位置
で、同じ構造の嵌め合い部26をもつた上蓋27
を外殻槽12上で第4図の矢印A方向と逆の方向
からかぶせて嵌め合い部26を伝熱管ダミー14
の接続部に係合させるとともに、ネジ穴24に合
うボルト28をもつて上蓋27を内殻槽15に固
定する。そして吊り下げ具29を利用して内殻槽
15ごと上方に引き抜く操作を行ない、外殻槽1
2と分離する。 Next, as shown in FIG.
over the outer shell tank 12 from the direction opposite to the direction of arrow A in FIG.
At the same time, the upper cover 27 is fixed to the inner shell tank 15 with bolts 28 that fit into the screw holes 24. Then, using the hanging tool 29, pull out the entire inner shell tank 15 upward, and then pull out the outer shell tank 1.
Separate from 2.
輸送工程は、蓄熱物質が充填された内殻槽15
のみを場所XからYもしくはYからXへ適当な輸
送手段によつて輸送する。 In the transportation process, the inner shell tank 15 filled with heat storage material is
Transport only from location X to location Y or from location Y to location X by appropriate means of transportation.
充填工程は、蓄・放熱を行なう場所XとYに同
一構造の大きさを持つ外殻槽と熱交換部を準備し
ておき、抜き出し工程と逆の工程で第2図に示し
た状態にセツトする。 In the filling process, prepare outer shell tanks and heat exchange parts with the same structure and size at locations X and Y where heat is stored and dissipated, and set them to the state shown in Figure 2 by performing the reverse process of the extraction process. do.
なお、伝熱管13は伝熱プレートであつてもよ
い。 Note that the heat transfer tube 13 may be a heat transfer plate.
以上本発明によれば、蓄・放熱を別の場所で行
なう場合、次のような効果を得ることができる。 As described above, according to the present invention, the following effects can be obtained when heat storage and radiation are performed at different locations.
(イ) 蓄熱物質の粒子の充填された内殻槽への熱交
換部の装脱作業は必要であるが、熱交換部と外
殻槽を輸送しなくて良いので、大巾に輸送重量
が軽減できる。(b) Although it is necessary to load and unload the heat exchange unit into the inner shell tank filled with heat storage material particles, there is no need to transport the heat exchange unit and the outer shell tank, so the transport weight can be reduced over a large area. It can be reduced.
(ロ) 蓄熱物質の粒子を直接取り出したり、充填し
たりする必要がないので、蓄熱物質が人体と接
触することはなく、また空気との長時間の接触
も避けられ、操作も簡単である。(b) Since there is no need to directly take out or fill the heat storage material particles, the heat storage material does not come into contact with the human body, long-term contact with air can be avoided, and operation is simple.
(ハ) 熱交換部は輸送しないので、気体出入口、熱
交換流体流入口および流出口にフレキシブルホ
ースなどを利用して接続すれば、取り外しする
必要はない。(c) Since the heat exchange part is not transported, there is no need to remove it if it is connected to the gas inlet/outlet, heat exchange fluid inlet, and outlet using flexible hoses.
第1図は通常の蓄熱槽の一例を示す断面図、第
2図は本発明の一実施例を示す断面図、第3図〜
第5図は輸送工程を説明するための断面図であ
る。
11……熱交換部、12……外殻槽、13……
伝熱管、14……伝熱管ダミー、15……内殻
槽、16……熱交換流体流入口、17……熱交換
流体流出口、18……隔壁、19……蓄熱物質、
20……蓄熱物質充填部、21……気体出入口、
24……ネジ穴、25……吊り下げ具、26……
嵌め合い部、27……上蓋、28……ボルト、2
9……吊り下げ具。
Fig. 1 is a sectional view showing an example of a normal heat storage tank, Fig. 2 is a sectional view showing an embodiment of the present invention, and Figs.
FIG. 5 is a sectional view for explaining the transportation process. 11... Heat exchange section, 12... Outer shell tank, 13...
Heat exchanger tube, 14... Heat exchanger tube dummy, 15... Inner shell tank, 16... Heat exchange fluid inlet, 17... Heat exchange fluid outlet, 18... Partition wall, 19... Heat storage material,
20... Heat storage material filling section, 21... Gas inlet/outlet,
24...Screw hole, 25...Hanging tool, 26...
Fitting part, 27...Top lid, 28...Bolt, 2
9...Hanging tool.
Claims (1)
殻槽に取り外し自在に連結されるとともに、伝熱
管または伝熱プレートとその先端に着脱自在に取
り付けられる同一直径の伝熱管ダミーとを上下方
向に有し、これらが前記内殻槽内部空間に収めら
れる熱交換部とを具備し、前記内殻槽の上下方向
中間部に前記伝熱管ダミーが貫通可能な隔壁を設
け、前記隔壁上の内殻槽内に充填された蓄熱物質
は前記熱交換部の伝熱管または伝熱プレートと接
触可能であるとともに、前記熱交換部を上方に抜
き出して前記伝熱管ダミーを前記伝熱管または伝
熱プレートより離脱させた時に前記蓄熱物質は前
記伝熱管ダミーに接触して隔壁上に保持されるよ
うにし、前記熱交換部に、前記内殻槽内の蓄熱物
質充填空間に連通する気体出入口を設けたことを
特徴とする蓄熱装置。1. An outer shell tank having an insertable and removable inner shell tank, and a heat transfer tube dummy of the same diameter that is removably connected to the outer shell tank and that is detachably attached to a heat transfer tube or a heat transfer plate and its tip. and a heat exchange section which is housed in the internal space of the inner shell tank, and a partition wall through which the heat transfer tube dummy can pass is provided in the middle part of the inner shell tank in the vertical direction, and the partition wall The heat storage material filled in the upper inner shell tank can be brought into contact with the heat exchanger tubes or heat exchanger plates of the heat exchanger, and the heat exchanger is pulled out upward and the heat exchanger tube dummy is inserted into the heat exchanger tube or the heat exchanger plate. When the heat storage material is removed from the heat plate, the heat storage material comes into contact with the heat transfer tube dummy and is held on the partition wall, and the heat exchange part is provided with a gas inlet/outlet communicating with the heat storage material filling space in the inner shell tank. A heat storage device characterized by being provided with.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58030120A JPS59157483A (en) | 1983-02-23 | 1983-02-23 | Heat storage material transportation device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58030120A JPS59157483A (en) | 1983-02-23 | 1983-02-23 | Heat storage material transportation device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS59157483A JPS59157483A (en) | 1984-09-06 |
| JPS635675B2 true JPS635675B2 (en) | 1988-02-04 |
Family
ID=12294917
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP58030120A Granted JPS59157483A (en) | 1983-02-23 | 1983-02-23 | Heat storage material transportation device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS59157483A (en) |
-
1983
- 1983-02-23 JP JP58030120A patent/JPS59157483A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS59157483A (en) | 1984-09-06 |
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