JPS6222883A - Rapid heating device - Google Patents

Rapid heating device

Info

Publication number
JPS6222883A
JPS6222883A JP60162236A JP16223685A JPS6222883A JP S6222883 A JPS6222883 A JP S6222883A JP 60162236 A JP60162236 A JP 60162236A JP 16223685 A JP16223685 A JP 16223685A JP S6222883 A JPS6222883 A JP S6222883A
Authority
JP
Japan
Prior art keywords
hydrogen
heater
storage container
heating
heated
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
JP60162236A
Other languages
Japanese (ja)
Inventor
Katsuhiko Yamaji
克彦 山路
Shigemasa Kawai
河合 重征
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.)
Sekisui Chemical Co Ltd
Original Assignee
Sekisui Chemical Co Ltd
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 Sekisui Chemical Co Ltd filed Critical Sekisui Chemical Co Ltd
Priority to JP60162236A priority Critical patent/JPS6222883A/en
Publication of JPS6222883A publication Critical patent/JPS6222883A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To rapidly heat a material to be heated, by providing a heater contg. a first metal hydride,an electric heater provided so as to exchange heat with the heater, a hydrogen storage container and a communicating tube which connects the heater to the hydrogen storage container. CONSTITUTION:The titled device comprises a heater 1 (a) contg. a first metal hydride MH1 and capable of exchanging heat with a material to be heated, an electric heater 7 (b) provided so as to exchange heat with the heater 1, a hydrogen storage container 6 (c) contg. hydrogen or a second metal hydride MH2 and a communicating tube 5 which communicates the heater 1 with the hydrogen storage container 6 with a hydrogen flowing valve 4. The titled heating device is responsible for a heating step of transferring hydrogen from the hydrogen storage container 6 to the heater 1, where hydrogen is occluded in MH1 to generate heat, thereby rapidly heating the material to be heated as well as heating the electric heater 7 and a preparation step of lowering the hydrogen equilibrium pressure of MH2 or heating the heater 1 with the electric heater 7, thereby releasing hydrogen and transferring hydrogen to the hydrogen storage container.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は急速加熱装置に関し詳しくは、金属水素化物が
水素を吸蔵する際の発熱反応を利用して、被加熱物質を
急速加熱するための装置に関する。
Detailed Description of the Invention (Field of Industrial Application) The present invention relates to a rapid heating device, and more particularly, to a rapid heating device for rapidly heating a substance to be heated by utilizing an exothermic reaction when a metal hydride absorbs hydrogen. Regarding equipment.

(従来の技術) 例えば、種々の計測機や記録計は、その使用に際しては
、通常、電源を投入して後、機器内の所定の機構がある
温度まで昇温しではじめて使用することができる。しか
し、一般に、寒冷地においては、又は冬期早朝において
は、気温が低いので、上記機器類が所定の温度の恒温室
に配設されていない限りは、上記のように、使用し得る
温度まで暖まるには、通常、数分から十数分程度の待ち
時間を必要とする。また、家庭用の暖房器、例えば、電
気ストーブや電気ファンヒータは、電源を投入しても昇
温速度が遅く、正常に作動するまでに、やはり待ち時間
が生じる。しかし、急速加熱のために、例えば、加熱装
置に極端に大電流を通電すれば、昇温速度を大きくする
ことはできるが、そのために設備費用が高価となり、ま
た、かかる急速加熱以外に用途がないときは過剰設備と
なる。
(Prior art) For example, various measuring instruments and recorders can usually be used only after turning on the power and raising the temperature to a certain temperature by a predetermined mechanism inside the device. . However, in general, in cold regions or early in the morning in winter, the temperature is low, so unless the above equipment is placed in a constant temperature room at a predetermined temperature, it will warm up to a usable temperature as described above. Usually requires a waiting time of several minutes to more than ten minutes. Furthermore, household heaters, such as electric stoves and electric fan heaters, have a slow rate of temperature rise even when the power is turned on, and there is still a waiting time before they operate properly. However, for rapid heating, for example, if an extremely large current is applied to the heating device, the temperature increase rate can be increased, but this increases the equipment cost and there are no uses other than such rapid heating. If there is no such equipment, it will be excess equipment.

更に、エネルギー効率も悪い。Furthermore, it is not energy efficient.

(発明の目的) 本発明は上記した諸点に窓みてなされたものであって、
被加熱物質を急速加熱するための装置を提供することを
目的とし、例えば、通常の電気ヒーターを利用した加熱
装置によっては、被加熱物質の昇温速度が不足するよう
な場合でも、十分に急速に加熱し得る急速加熱装置を提
供することを目的とする。
(Object of the invention) The present invention has been made in view of the above-mentioned points,
The objective is to provide a device for rapidly heating a substance to be heated. The object of the present invention is to provide a rapid heating device capable of heating the temperature.

(発明の構成) 本発明は、被加熱物質を急速加熱するための装置であっ
て、 (al  第1の金属水素化物を内蔵し、且つ、被加熱
物質と熱交換可能である加熱器と、 (b)  上記加熱器と熱交換可能に配設された電気ヒ
ーターと、 (c)  水素又は第2の金属水素化物を内蔵した水素
貯蔵容器と、 (e)  前記加熱器と前記水素貯蔵容器とを水素流通
弁により連通可能に接続する連通管とを有し、前記水素
流通弁を開けて、前記水素貯蔵容器から前記加熱器へ水
素を移動させ、前記第1の金属水素化物にこの水素を吸
蔵させて発熱させ、被加熱物質を急速加熱すると共に、
前記電気ヒーターを加熱する加熱工程と、前記第2の金
属水素化物の水素平衡圧を低くするか、又は前記電気ヒ
ーターにて前記加熱器を加熱することによって、前記第
1の金属水素化物から水素を放出させ、前記水素貯蔵容
器に移動させる準備工程とを行なうことを特徴とする。
(Structure of the Invention) The present invention is an apparatus for rapidly heating a substance to be heated, comprising: (a heater containing a first metal hydride and capable of exchanging heat with the substance to be heated; (b) an electric heater arranged to be able to exchange heat with the heater; (c) a hydrogen storage container containing hydrogen or a second metal hydride; (e) the heater and the hydrogen storage container. and a communication pipe which is connected to the first metal hydride by a hydrogen flow valve, and the hydrogen flow valve is opened to transfer hydrogen from the hydrogen storage container to the heater, and the hydrogen is transferred to the first metal hydride. In addition to occluding and generating heat to rapidly heat the substance to be heated,
Hydrogen is removed from the first metal hydride by heating the electric heater and lowering the hydrogen equilibrium pressure of the second metal hydride, or by heating the heater with the electric heater. and a preparation step of releasing the hydrogen and transferring it to the hydrogen storage container.

以下に実施例を示す図面に基づいて本発明を説明する。The present invention will be described below based on drawings showing examples.

第1図は本発明による急速加熱装置を示す概念図であり
、第2図は第1図においてA−A線に沿う断面図である
FIG. 1 is a conceptual diagram showing a rapid heating device according to the present invention, and FIG. 2 is a sectional view taken along line A-A in FIG. 1.

加熱器1は、外壁面にその半径方向に延びる複数のフィ
ン2を有する密閉された管状に形成されて、内部に第1
の金属水素化物(以下、M H+ と称する。)を内蔵
しており、適宜のハウジング3内に複数本収容されてい
る。急速加熱を必要とする加熱媒体、例えば、気体、液
体等や、その他の被加熱物質は、このハウジングと加熱
器との間の空間に流通されて、加熱器及び後述する電気
ヒータと熱交換される。
The heater 1 is formed into a sealed tubular shape having a plurality of radially extending fins 2 on its outer wall surface, and has a first tube inside.
A plurality of metal hydrides (hereinafter referred to as M H+ ) are housed in a suitable housing 3. A heating medium that requires rapid heating, such as gas, liquid, etc., and other substances to be heated, are passed through the space between the housing and the heater, and heat exchanged with the heater and an electric heater to be described later. Ru.

また、上記加熱器は、水素流通弁4を備えた連通管5を
介して水素貯蔵容器6に接続されていると共に、外壁面
を伝熱面とする電気ヒーター7が複数本の加熱器の中央
にフィンと熱交換可能に配設されている。但し、加熱器
は、上記電気ヒーターと熱交換可能であれば、何らフィ
ンを有する必要はなく、例えば、電気ヒーターがその壁
面にて管状の加熱器の外壁面と直接に熱交換し得るよう
に配設されていてもよい。
Further, the heater is connected to a hydrogen storage container 6 via a communication pipe 5 equipped with a hydrogen flow valve 4, and an electric heater 7 having an outer wall surface as a heat transfer surface is installed in the center of the plurality of heaters. It is arranged so that heat can be exchanged with the fins. However, the heater does not need to have any fins as long as it can exchange heat with the electric heater, for example, the electric heater can directly exchange heat with the outer wall of the tubular heater on its wall. It may be arranged.

第3図は本発明による急速加熱装置の別の実施例の第2
図に対応する断面図を示し、前記したように、密閉され
た管状の加熱器1は外壁面からその半径方向に延びる複
数のフィン2を有し、このフィンと熱交換可能に円筒状
の電気ヒーター7が加熱器を収容するように加熱器と共
軸的に配設されている。従って、この実施例においては
、電気ヒーターがハウジングを兼ねることができる。
FIG. 3 shows a second embodiment of the rapid heating device according to the invention.
As mentioned above, the sealed tubular heater 1 has a plurality of fins 2 extending in the radial direction from the outer wall surface, and a cylindrical electric heater 1 that can exchange heat with the fins. A heater 7 is arranged coaxially with the heater to accommodate the heater. Therefore, in this embodiment, the electric heater can also serve as the housing.

前記水素貯蔵容器6には水素が充填され、又は作動温度
領域で水素平衡圧がMH,よりも高い第2の金属水素化
物(以下、M H2と称する。)が内蔵されており、前
記連通管5の有する水素流通弁4によって、後述するよ
うに加熱工程及び準備工程番行なう間、加熱器1に連通
される。水素貯蔵容器6は環境、例えば、外気と熱交換
され、又は適宜の熱媒と熱交換される。
The hydrogen storage container 6 is filled with hydrogen or contains a second metal hydride (hereinafter referred to as MH2) whose hydrogen equilibrium pressure is higher than MH in the operating temperature range, and the communication pipe The hydrogen flow valve 4 of 5 communicates with the heater 1 during the heating process and preparatory process, which will be described later. The hydrogen storage container 6 is heat exchanged with the environment, for example with the outside air, or with a suitable heat medium.

次に、本発明による急速加熱装置の作動を説明する。Next, the operation of the rapid heating device according to the present invention will be explained.

第4図は、水素貯蔵容器として水素を充填した容器を用
いた装置の作動を示すサイクル線図であリ、横軸は絶対
温度Tの逆数を、縦軸は金属水素化物の水素平衡圧Pの
対数を示す。加熱器が内蔵するMH,は、加熱器による
被加熱物質の加熱温度Tbにおいては、その水素平衡圧
が水素貯蔵容器内の水素圧Pよりも低く、後述する準備
工程における所定の温度Taにおいては、水素貯蔵容器
内の水素圧Pよりも高くなるように選ばれる。
FIG. 4 is a cycle diagram showing the operation of an apparatus using a container filled with hydrogen as a hydrogen storage container, where the horizontal axis represents the reciprocal of the absolute temperature T, and the vertical axis represents the hydrogen equilibrium pressure P of the metal hydride. indicates the logarithm of The hydrogen equilibrium pressure of MH built in the heater is lower than the hydrogen pressure P in the hydrogen storage container at the heating temperature Tb of the substance to be heated by the heater, and at a predetermined temperature Ta in the preparation step described later. , is chosen to be higher than the hydrogen pressure P in the hydrogen storage vessel.

本発明による急速加熱装置は、加熱工程及び準備工程を
行なう。先ず、加熱工程を行なうには、水素流通弁4を
開き、水素貯蔵容器内6の水素を加熱器Iに流入させる
ことにより、加熱器内のMH,にこの水素を吸蔵させて
発熱させ、加熱器を温度Tbに昇温させる。この加熱器
の高められた温度を利用して、被加熱物質を加熱する。
The rapid heating device according to the invention performs a heating step and a preparatory step. First, in order to carry out the heating process, the hydrogen flow valve 4 is opened and the hydrogen in the hydrogen storage container 6 is allowed to flow into the heater I, so that the MH in the heater absorbs the hydrogen and generates heat. Heat the vessel to temperature Tb. The increased temperature of this heater is used to heat the substance to be heated.

この加熱工程において、水素貯蔵容器内の水素圧はある
程度低下する。
During this heating step, the hydrogen pressure within the hydrogen storage container decreases to some extent.

更に、この加熱工程においては、好ましくは、加熱器の
作動の開始とほぼ同時に、即ち、水素流通弁を開くのと
ほぼ同時に、電気ヒーター7に通電される。従って、電
気ヒーターは、自身が発熱すると共に、加熱器によって
も加熱されるので、急速に温度が上昇し、かくして、加
熱器と共に所定の温度にて被加熱物質を加熱する。電気
ヒーターへの通電は、少なくとも後述する準備工程が完
了するまで継続される。また、被加熱物質を引き続いて
加熱する必要があるときは、この電気ヒーターにて被加
熱物質の加熱を1m続する。
Furthermore, in this heating step, the electric heater 7 is preferably energized almost simultaneously with the start of operation of the heater, that is, almost simultaneously with the opening of the hydrogen flow valve. Therefore, since the electric heater itself generates heat and is also heated by the heater, the temperature rises rapidly, and thus, together with the heater, the substance to be heated is heated to a predetermined temperature. The electricity supply to the electric heater is continued at least until the preparation process described below is completed. Further, when it is necessary to continue heating the substance to be heated, the electric heater continues to heat the substance for 1 m.

準備工程は、上記のようにして加熱器内のMH。The preparation process is to prepare the MH in the heater as described above.

に吸蔵された水素をMH,から放出させて、再び水素貯
蔵容器に戻し、次の加熱工程に備えるための工程である
。前述したように、加熱器の作動とほぼ同時に電気ヒー
ターに通電されるので、被加熱物質の加熱を止めるか、
又は電気ヒーターにて加熱器を温度Taに加熱すれば、
加熱器内のM H+は温度Taで吸熱的に水素を放出し
、この温度Taでは、前記したように、MH,の水素平
衡圧は水素貯蔵容器内の水素圧Pよりも高いので、この
水素は連通管を経て再び水素貯蔵容器に戻り、水素貯蔵
容器内の水素圧力は当初の圧力に復帰する。
In this step, the hydrogen stored in the MH is released from the MH and returned to the hydrogen storage container in preparation for the next heating step. As mentioned above, the electric heater is energized almost at the same time as the heater is activated, so it is necessary to either stop heating the substance to be heated or
Or, if you heat the heater to temperature Ta with an electric heater,
MH+ in the heater endothermically releases hydrogen at a temperature Ta, and at this temperature Ta, as mentioned above, the hydrogen equilibrium pressure of MH, is higher than the hydrogen pressure P in the hydrogen storage container, so this hydrogen The hydrogen returns to the hydrogen storage container via the communication pipe, and the hydrogen pressure in the hydrogen storage container returns to its original pressure.

この後、水素流通弁を閉じて、次回の作動に備える。尚
、この準備工程における電気ヒーターによる加熱器の加
熱に際しては、被加熱物質の加熱がm続されているとき
は、電気ヒーターへの通電量を増すのが好ましい。
After this, close the hydrogen flow valve and prepare for the next operation. When heating the heater with the electric heater in this preparatory step, it is preferable to increase the amount of current applied to the electric heater when the substance to be heated is continuously heated.

第5図は作動温度領域で水素平衡圧がMH,よりも高い
MH,を水素貯蔵容器に充填した装置の作動を示すサイ
クル線図である。これらの金属水素化物は、加熱器の作
動時には、例えば大気温度Tcにおいては、M H2の
方が温度TdのMH。
FIG. 5 is a cycle diagram showing the operation of a device in which a hydrogen storage container is filled with MH whose hydrogen equilibrium pressure is higher than MH in the operating temperature range. When the heater is in operation, for example, at atmospheric temperature Tc, these metal hydrides are MH2 and MH2 is MH2 at temperature Td.

よりも水素平衡圧が高く一方、準備工程における加熱器
の温度Taにおいては、MH,の方が温度TbのMH!
よりも水素平衡圧が高いように選ばれる。ここに温度T
″bは、MH,が水素を吸蔵して発熱昇温する温度であ
り、環境との熱交換の態様に応じて定まる温度であり、
例えば、大気と熱交換する場合、温度Tcより幾分高い
温度となる。
On the other hand, at the temperature Ta of the heater in the preparation process, MH, has a higher hydrogen equilibrium pressure than MH! at temperature Tb.
The hydrogen equilibrium pressure is selected so that it is higher than the hydrogen equilibrium pressure. Here is the temperature T
``b'' is the temperature at which MH absorbs hydrogen and heats up, and is determined depending on the mode of heat exchange with the environment,
For example, when exchanging heat with the atmosphere, the temperature is somewhat higher than the temperature Tc.

従って、加熱工程において、水素流通弁を開くとき、水
素貯蔵容器内のMH,は、温度Tcで大気から吸熱しつ
つ水素を放出し、この水素を加熱器内のMH,が吸蔵し
、発熱して、加熱器を温度Tdに昇温させる。
Therefore, in the heating process, when the hydrogen flow valve is opened, the MH in the hydrogen storage container releases hydrogen while absorbing heat from the atmosphere at the temperature Tc, and the MH in the heater absorbs this hydrogen and generates heat. Then, the heater is heated to the temperature Td.

かかる作動による場合も、加熱器と熱交換可能に配設さ
れている電気ヒーターが、加熱器の作動とほぼ同時に通
電されるので、加熱工程においては、前述したように、
電気ヒーターは、自身が発熱すると共に、加熱器によっ
ても加熱されるので、急速に温度が上昇し、所定の温度
に達して、加熱器と共に被加熱物質を加熱する。
Even in the case of such an operation, the electric heater, which is disposed so as to be able to exchange heat with the heater, is energized almost simultaneously with the operation of the heater, so that in the heating process, as described above,
Since the electric heater itself generates heat and is also heated by the heater, the temperature rises rapidly, reaches a predetermined temperature, and heats the substance to be heated together with the heater.

準備工程においては、前述したと同様ように、加熱器の
作動とほぼ同時に電気ヒーターに通電されているので、
被加熱物質の加熱を止めるか、又は電気ヒーターにて加
熱器を温度Taに加熱すれば、加熱器内のMH,が吸熱
的に水素を放出し、この温度Taでは、前記したように
、MH,の水素平衡圧はM Hzの温度Tbの水素平衡
圧よりも高いので、この水素は連通管を経て再び水素貯
蔵容器に戻り、MH,に吸蔵される。この際のM H2
の発熱は、例えば、大気に放散される。この後、水素流
通弁を閉じて、次回の作動に備える。
In the preparation process, as mentioned above, the electric heater is energized almost at the same time as the heater is activated, so
If the heating of the substance to be heated is stopped or the heater is heated to a temperature Ta using an electric heater, the MH in the heater endothermically releases hydrogen, and at this temperature Ta, as mentioned above, the MH , is higher than the hydrogen equilibrium pressure at temperature Tb in MHz, this hydrogen returns to the hydrogen storage container via the communication pipe and is stored in MH,. M H2 at this time
The heat generated is, for example, dissipated into the atmosphere. After this, close the hydrogen flow valve and prepare for the next operation.

また、本発明においては、上記の準備工程に代えて、水
素貯蔵容器内のMH2の温度を下げて、。
Furthermore, in the present invention, instead of the above preparation step, the temperature of MH2 in the hydrogen storage container is lowered.

加熱工程における加熱器の温度TdでのM H、の水素
平衡圧よりもM Hzの水素平衡圧が低いような温度T
eとすることによっても、第5図に破線で示すように、
M H+からMH,へ水素を移動させることができる。
A temperature T such that the hydrogen equilibrium pressure of MHz is lower than the hydrogen equilibrium pressure of MH at the temperature Td of the heater in the heating process.
By setting e, as shown by the broken line in Fig. 5,
Hydrogen can be transferred from M H+ to MH,.

以上においては、上記第1の金属水素化物と第2の金属
水素化物とが異なるとして、本発明による急速加熱器の
作動を説明したが、しかし、本発明においては、第1の
金属水素化物と第2の金属水素化物とは同じであっても
よい。この場合は、加熱工程においては、水素貯蔵容器
を高温に保持して水素流通弁を開くと、水素貯蔵容器内
のM Hzは水素を放出し、この水素を加熱器内のMH
,が吸蔵して、急速に発熱する。準備工程においては、
水素貯蔵容器内のMH2を低温に冷却すれば、加熱器内
のM HI は水素を放出し、MH,がこの水素を吸蔵
する。
In the above, the operation of the rapid heater according to the present invention has been explained assuming that the first metal hydride and the second metal hydride are different; however, in the present invention, the first metal hydride and the second metal hydride are different. The second metal hydride may be the same. In this case, in the heating process, when the hydrogen storage container is held at a high temperature and the hydrogen flow valve is opened, the hydrogen inside the hydrogen storage container is released, and this hydrogen is transferred to the MH in the heater.
, occludes and rapidly generates heat. In the preparation process,
When the MH2 in the hydrogen storage container is cooled to a low temperature, the MHI in the heater releases hydrogen, and the MH, absorbs this hydrogen.

(発明の効果) 以上のように、本発明の装置によれば、金属水素化物が
水素を吸蔵する際の発熱反応を利用するので、電気ヒー
ターによる加熱と併用することにより急速に被加熱物質
を加熱することができ、前述したように、種々の機器類
の電源の投入から使用までの待ち時間を短縮し、或いは
暖房器の使用に際しての待ち時間を短縮することができ
る。更に、また、本発明の装置によれば、急速加熱器の
使用の態様や環境にかかわらずに、加熱工程の後、電気
ヒーターによって加熱器を所定の温度まで加熱するので
、準備工程を確実に完了して、次回の作動に備えること
ができる。
(Effects of the Invention) As described above, according to the apparatus of the present invention, since the exothermic reaction when metal hydride absorbs hydrogen is used, the substance to be heated can be rapidly absorbed by using it in combination with heating by an electric heater. As mentioned above, it is possible to shorten the waiting time between turning on the power of various devices and using them, or shortening the waiting time when using a heater. Furthermore, according to the apparatus of the present invention, the heater is heated to a predetermined temperature by the electric heater after the heating process, regardless of the usage mode or environment of the rapid heater, so that the preparation process can be performed reliably. Complete and ready for next operation.

(実施例) 以下に本発明の装置の実施例について説明する。(Example) Examples of the apparatus of the present invention will be described below.

実施例1 第4図に示す作動を行なう装置によって、被加熱物質と
しての空気をハウジング内に供給しつつ、急速加熱した
。加熱器のMH,としてLaN1n、 aAlo、 z
を1.0 kg用い、水素貯蔵容器の容積を40Aとし
、Tb=50℃、Ta=130℃とする条件下では、P
b=6気圧、Pa=9気圧である。
Example 1 Using a device operating as shown in FIG. 4, rapid heating was carried out while supplying air as a material to be heated into the housing. As MH of the heater, LaN1n, aAlo, z
Using 1.0 kg of P
b=6 atm, Pa=9 atm.

加熱工程において、水素流通弁を開くとほぼ同時に、容
量IKWの電気ヒーターに通電を開始した。温度O″C
の空気は5秒後に40℃まで、また、10秒後には50
℃まで高められ、以後、空気は′m続して50°Cに加
熱された。
In the heating process, electricity was started to be applied to the electric heater with a capacity of IKW almost at the same time as the hydrogen flow valve was opened. Temperature O″C
The temperature of the air reaches 40℃ after 5 seconds, and 50℃ after 10 seconds.
The air was then heated continuously to 50°C.

準備工程においては、加熱器への空気の供給を停止した
ところ、加熱器は温度Ta=130℃となり、加熱工程
において加熱器に流れた水素と同量の水素を水素貯蔵容
器に戻すことができた。以上の加熱工程及び準備工程に
おける時間と空気温度との関係を第6図に示す。図中、
実線は本発明の急速加熱器を用いたときの空気の温度変
化を示し、破線は前記電気ヒーターを単独で用いて空気
を加熱したときの空気の温度変化を示す。明らかに本発
明の急速加熱装置によれば、空気の昇温速度が大きい。
In the preparation process, when the supply of air to the heater was stopped, the temperature of the heater reached Ta = 130°C, and the same amount of hydrogen as that flowing into the heater in the heating process could be returned to the hydrogen storage container. Ta. FIG. 6 shows the relationship between time and air temperature in the above heating step and preparation step. In the figure,
The solid line shows the temperature change of the air when the rapid heater of the present invention is used, and the broken line shows the temperature change of the air when the air is heated using the electric heater alone. Obviously, according to the rapid heating device of the present invention, the rate of temperature rise of air is high.

実施例2 第5図に示す作動を行なう装置によって、実施例1と同
様にして空気を急速加熱した。加熱器のMH,としてC
aNi5.oを1kg、水素貯蔵容器のM Htとして
MmNi41A1 +1.2 (Mmはミツシュメタル
を示す。)1kgを用い、Tc=20°c、Tb=20
℃、Td=100℃、Ta=150℃とする条件下では
、Pd=6気圧、Pa=10気圧である。
Example 2 Air was rapidly heated in the same manner as in Example 1 using an apparatus operating as shown in FIG. MH of the heater, as C
aNi5. o is 1 kg, M Ht of the hydrogen storage container is MmNi41A1 +1.2 (Mm indicates Mitshu metal) 1 kg, Tc = 20 ° C, Tb = 20
℃, Td=100°C, and Ta=150°C, Pd=6 atmospheres and Pa=10 atmospheres.

水素流通弁を開くとほぼ同時に電気ヒーターに通電した
ところ、温度30℃の空気は、10秒後に90℃まで高
められた。
When electricity was applied to the electric heater almost at the same time as the hydrogen flow valve was opened, the temperature of the air at 30°C was raised to 90°C in 10 seconds.

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

第1図は本発明による急速加熱装置を示す概念図、第2
図は第1図においてA−A線に沿う断面図、第3図は本
発明による急速加熱装置の別の実施例を示す断面図、第
4図及び第5図は本発明による装置の作動を示すサイク
ル線図、第6図は本発明による装置を用いて空気を加熱
したときの空気の昇温速度を示すグラフである。 1・・・加熱器、2・・・フィン、3・・・ハウジング
、4・・・水素流通弁、5・・・連通管、6・・・水素
貯蔵容器、7・・・電気ヒーター。 特許出願人 積水化学工業株式会社 代表者  廣  1)  馨 第1図 第4図 於
Fig. 1 is a conceptual diagram showing a rapid heating device according to the present invention;
The figures are a sectional view taken along the line A-A in FIG. 1, FIG. 3 is a sectional view showing another embodiment of the rapid heating device according to the present invention, and FIGS. 4 and 5 illustrate the operation of the device according to the present invention. The cycle diagram shown in FIG. 6 is a graph showing the temperature increase rate of air when air is heated using the apparatus according to the present invention. DESCRIPTION OF SYMBOLS 1... Heater, 2... Fin, 3... Housing, 4... Hydrogen distribution valve, 5... Communication pipe, 6... Hydrogen storage container, 7... Electric heater. Patent applicant Sekisui Chemical Co., Ltd. Representative Hiroshi 1) Kaoru Figure 1 Figure 4

Claims (1)

【特許請求の範囲】[Claims] (1)被加熱物質を急速加熱するための装置であって、 (a)第1の金属水素化物を内蔵し、且つ、被加熱物質
と熱交換可能である加熱器と、 (b)上記加熱器と熱交換可能に配設された電気ヒータ
ーと、 (c)水素又は第2の金属水素化物を内蔵した水素貯蔵
容器と、 (c)前記加熱器と前記水素貯蔵容器とを水素流通弁に
より連通可能に接続する連通管とを有し、前記水素流通
弁を開けて、前記水素貯蔵容器から前記加熱器へ水素を
移動させ、前記第1の金属水素化物にこの水素を吸蔵さ
せて発熱させ、被加熱物質を急速加熱すると共に、前記
電気ヒーターを加熱する加熱工程と、前記第2の金属水
素化物の水素平衡圧を低くするか、又は前記電気ヒータ
ーにて前記加熱器を加熱することによって、前記第1の
金属水素化物から水素を放出させ、前記水素貯蔵容器に
移動させる準備工程とを行なうことを特徴とする急速加
熱装置。
(1) An apparatus for rapidly heating a substance to be heated, comprising: (a) a heater containing a first metal hydride and capable of exchanging heat with the substance to be heated; (b) the above heating device; (c) a hydrogen storage container containing hydrogen or a second metal hydride; (c) the heater and the hydrogen storage container are connected by a hydrogen flow valve; and a communication pipe that is communicatively connected, the hydrogen flow valve is opened to transfer hydrogen from the hydrogen storage container to the heater, and the first metal hydride absorbs the hydrogen and generates heat. , a heating step of rapidly heating the substance to be heated and heating the electric heater, and lowering the hydrogen equilibrium pressure of the second metal hydride, or heating the heater with the electric heater. A rapid heating apparatus comprising: a preparatory step of releasing hydrogen from the first metal hydride and transferring it to the hydrogen storage container.
JP60162236A 1985-07-22 1985-07-22 Rapid heating device Pending JPS6222883A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60162236A JPS6222883A (en) 1985-07-22 1985-07-22 Rapid heating device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60162236A JPS6222883A (en) 1985-07-22 1985-07-22 Rapid heating device

Publications (1)

Publication Number Publication Date
JPS6222883A true JPS6222883A (en) 1987-01-31

Family

ID=15750562

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60162236A Pending JPS6222883A (en) 1985-07-22 1985-07-22 Rapid heating device

Country Status (1)

Country Link
JP (1) JPS6222883A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6434705A (en) * 1987-06-26 1989-02-06 Inax Corp Apparatus for stacking tile
JPH0516738U (en) * 1991-08-21 1993-03-02 レンゴー株式会社 Seat palletizer
JPH0516730U (en) * 1991-08-13 1993-03-02 株式会社アマダ Material alignment device
KR20170089344A (en) * 2016-01-26 2017-08-03 현대자동차주식회사 Solid state hydrogen storage device and solid state hydrogen storage system

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5380372A (en) * 1976-12-27 1978-07-15 Agency Of Ind Science & Technol Method and apparatus for acquiring heat energy by hydrogenation reaction of metal
JPS5889678A (en) * 1981-11-20 1983-05-28 Agency Of Ind Science & Technol Absorption of fluctuation in heat load in batch type operation

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5380372A (en) * 1976-12-27 1978-07-15 Agency Of Ind Science & Technol Method and apparatus for acquiring heat energy by hydrogenation reaction of metal
JPS5889678A (en) * 1981-11-20 1983-05-28 Agency Of Ind Science & Technol Absorption of fluctuation in heat load in batch type operation

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6434705A (en) * 1987-06-26 1989-02-06 Inax Corp Apparatus for stacking tile
JPH0516730U (en) * 1991-08-13 1993-03-02 株式会社アマダ Material alignment device
JPH0516738U (en) * 1991-08-21 1993-03-02 レンゴー株式会社 Seat palletizer
KR20170089344A (en) * 2016-01-26 2017-08-03 현대자동차주식회사 Solid state hydrogen storage device and solid state hydrogen storage system
US10511039B2 (en) 2016-01-26 2019-12-17 Hyundai Motor Company Solid state hydrogen storage device and solid state hydrogen storage system

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