JPS631148Y2 - - Google Patents
Info
- Publication number
- JPS631148Y2 JPS631148Y2 JP1980045755U JP4575580U JPS631148Y2 JP S631148 Y2 JPS631148 Y2 JP S631148Y2 JP 1980045755 U JP1980045755 U JP 1980045755U JP 4575580 U JP4575580 U JP 4575580U JP S631148 Y2 JPS631148 Y2 JP S631148Y2
- Authority
- JP
- Japan
- Prior art keywords
- heat exchanger
- heat exchange
- heat
- exchange container
- 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.)
- Expired
Links
- 238000001035 drying Methods 0.000 claims description 28
- 229910052987 metal hydride Inorganic materials 0.000 claims description 26
- 150000004681 metal hydrides Chemical class 0.000 claims description 26
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 10
- 238000010438 heat treatment Methods 0.000 claims description 9
- 238000009833 condensation Methods 0.000 claims description 6
- 230000005494 condensation Effects 0.000 claims description 6
- 239000007789 gas Substances 0.000 description 22
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 16
- -1 iron titanium hydride Chemical compound 0.000 description 8
- 239000001257 hydrogen Substances 0.000 description 7
- 229910052739 hydrogen Inorganic materials 0.000 description 7
- 238000010586 diagram Methods 0.000 description 6
- 229910052751 metal Inorganic materials 0.000 description 6
- 239000002184 metal Substances 0.000 description 6
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 description 2
- ICSGJQQEJPFDRH-UHFFFAOYSA-N cobalt dihydride neodymium Chemical compound [CoH2].[Nd] ICSGJQQEJPFDRH-UHFFFAOYSA-N 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 229910018007 MmNi Inorganic materials 0.000 description 1
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 1
- VKZIPTRJHUDLAF-UHFFFAOYSA-N [NiH2].[Ca] Chemical compound [NiH2].[Ca] VKZIPTRJHUDLAF-UHFFFAOYSA-N 0.000 description 1
- DLBCVDYPUSWERR-UHFFFAOYSA-N [NiH2].[La] Chemical compound [NiH2].[La] DLBCVDYPUSWERR-UHFFFAOYSA-N 0.000 description 1
- WIIBPQPFQUYUGZ-UHFFFAOYSA-N [NiH2].[Mg] Chemical compound [NiH2].[Mg] WIIBPQPFQUYUGZ-UHFFFAOYSA-N 0.000 description 1
- 229910045601 alloy Inorganic materials 0.000 description 1
- 239000000956 alloy Substances 0.000 description 1
- 238000007791 dehumidification Methods 0.000 description 1
- 239000002440 industrial waste Substances 0.000 description 1
- 239000011777 magnesium Substances 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 229910001120 nichrome Inorganic materials 0.000 description 1
- 229910000652 nickel hydride Inorganic materials 0.000 description 1
Landscapes
- Drying Of Solid Materials (AREA)
- Hydrogen, Water And Hydrids (AREA)
Description
【考案の詳細な説明】
本考案は金属水素化物を利用した加熱乾燥気体
の発生装置に関するものである。[Detailed Description of the Invention] The present invention relates to a heating and drying gas generating device using a metal hydride.
従来、乾燥はニクロム線ヒーター等で空気を加
熱し、得られた加熱空気により行われていたが、
空気は加熱されるだけで除湿は行われないので乾
燥効率が悪く、乾燥に長時間を要し、消費電力が
高くなるという欠点を有しており、又装置に除湿
装置を設置するには装置が複雑になり、高価であ
つた。 Traditionally, drying was done by heating air with a nichrome wire heater, etc., and using the heated air obtained.
Since the air is only heated but not dehumidified, the drying efficiency is poor, it takes a long time to dry, and the power consumption is high. was complicated and expensive.
本考案は上記欠点に鑑み、除湿及び加熱が容易
に行え、効率よく乾燥することができる加熱乾燥
気体の発生装置を提供せんとしてなされたもので
あつて、その要旨は、金属水素化物がそれぞれ内
蔵された、２個の熱交換容器を、途中にバルブを
有する連通管によつて開閉制御可能に連結すると
共に、一方の熱交換容器内には熱交換器を設け、
他方の熱交換容器内には熱交換器とヒーターを設
け、前記一方の熱交換容器内の熱交換器には結露
水溜を配設し、さらに熱交換器入口には配管によ
りブロアーを連設し、熱交換器出口は前記他方の
熱交換容器内の熱交換器の入口と配管により連結
し、また前記他方の熱交換容器内の熱交換器の出
口には、加熱乾燥気体の出口である配管を連設し
たことを特徴とする加熱乾燥気体発生装置に存す
る。 In view of the above-mentioned drawbacks, the present invention was devised to provide a heating drying gas generator that can easily perform dehumidification and heating, and can dry efficiently. The two heat exchange containers are connected to each other so as to be able to be opened and closed by a communication pipe having a valve in the middle, and a heat exchanger is provided in one of the heat exchange containers,
A heat exchanger and a heater are provided in the other heat exchange container, a condensation water reservoir is provided in the heat exchanger in the one heat exchange container, and a blower is connected to the inlet of the heat exchanger via piping. , the heat exchanger outlet is connected to the inlet of the heat exchanger in the other heat exchange container by piping, and the outlet of the heat exchanger in the other heat exchange container is connected to piping that is an outlet for heated drying gas. The present invention relates to a heating and drying gas generating apparatus characterized in that the heating and drying gas generating apparatus is provided in series.
次に本考案の加熱乾燥気体発生装置を図面を参
照して説明する。第１図は本考案の加熱乾燥気体
発生装置の一例を示す説明図である。図中１及び
２は熱交換容器であり、途中にバルブ４を有する
連通管３によつて開閉制御可能に連結されてい
る。そして熱交換容器１は金属水素化物M1が内
蔵されており、熱交換容器２には金属水素化物
M2が内蔵されている。５及び５′は熱交換容器１
及び２内に設置された熱交換器であり、熱交換器
５′の出口と熱交換器５の入口は配管６により連
結されている。７はブロアーであり、配管６′に
より熱交換器５′の入口と連設されている。８は
結露水溜であり、熱交換容器５′に配設されて、
気体が冷却されて結露した水が貯えられるように
なされている。９は熱交換容器１に内設されたヒ
ーターであり、金属水素化物M1を加熱するよう
になされている。又は熱交換容器１に内設された
熱交換器５の出口には加熱乾燥気体の出口である
配管６″が連設されており、配管６″は乾燥室１０
に連結されている。従つて、ブロアー７から送ら
れた気体は配管６′、熱交換器５′、配管６、熱交
換器５及び配管６″を通つて乾燥室１０に送られ
るようになつている。 Next, the heated drying gas generator of the present invention will be explained with reference to the drawings. FIG. 1 is an explanatory diagram showing an example of the heating drying gas generating device of the present invention. In the figure, 1 and 2 are heat exchange containers, which are connected by a communication pipe 3 having a valve 4 in the middle so that they can be opened and closed. The heat exchange container 1 contains a metal hydride M1 , and the heat exchange container 2 contains a metal hydride M1.
Built-in M2 . 5 and 5' are heat exchange containers 1
and 2, and the outlet of heat exchanger 5' and the inlet of heat exchanger 5 are connected by piping 6. Reference numeral 7 denotes a blower, which is connected to the inlet of the heat exchanger 5' through a pipe 6'. 8 is a condensation water reservoir, which is arranged in the heat exchange container 5',
The gas is cooled and the condensed water is stored. A heater 9 is installed inside the heat exchange container 1 and is designed to heat the metal hydride M1 . Alternatively, the outlet of the heat exchanger 5 installed inside the heat exchange container 1 is connected to a pipe 6'' which is an outlet for heated drying gas, and the pipe 6'' is connected to the drying chamber 10.
is connected to. Therefore, the gas sent from the blower 7 is sent to the drying chamber 10 through the pipe 6', the heat exchanger 5', the pipe 6, the heat exchanger 5, and the pipe 6''.
尚、金属水素化物M1及びM2の水素平衡圧は第
２図に示した通りである。第２図は縦軸に水素平
衡圧を対数目盛で示してあり、横軸は絶対温度の
逆数を1000／Ｔ（Ｔは絶対温度）の目盛で示して
ある。又、説明に便利なように温度をｔで示して
ある。 Note that the hydrogen equilibrium pressures of metal hydrides M 1 and M 2 are as shown in FIG. In FIG. 2, the vertical axis shows hydrogen equilibrium pressure on a logarithmic scale, and the horizontal axis shows the reciprocal of absolute temperature on a scale of 1000/T (T is absolute temperature). Further, the temperature is indicated by t for convenience of explanation.
次に第２図を参照して上記発生装置の使用態様
を説明する。まずバルブ４を開放し、ヒーター９
に通電し金属水素化物M1を加熱する。金属水素
化物M1をtaまで加熱すると金属水素化物M1の水
素平衡圧はpaになり（点Ａ）、金属水素化物M2の
水素平衡圧pc（点Ｃ）より大となり（tpは外気
温）、水素ガスは熱交換容器１から熱交換容器２
へ流れ、金属水素化物M2は水素ガスを吸収する
と共に加熱され、温度tb水素平衡圧pb（点Ｂ）と
なり平衡になる。こうしてＡ→Ｂの反応の終了後
バルブ４を閉止し、放冷しておくと金属水素化物
M1及びM2の温度はtpになり水素平衡圧はそれぞ
れpc、peとなる。この時pc＞peなのでバルブ４を
開放すると金属水素化物M2は水素ガスを放出し、
金属水素化物M1は水素ガスを吸収し、金属水素
化物M2は点Ｃ→点Ｄ（温度tp→td）に冷却され、
金属水素化物M1は点Ｅ→点Ｆ（温度tp→tf）に加
熱されＤ→Ｆの反応が進行する。この時ブロアー
７により空気を送ると、熱交換容器２中の熱交換
器５′で冷却され、空気中の水分が結露して除去
され、ついで熱交換容器１中の熱交換器５で加熱
され、加熱乾燥気体となり乾燥室１０に供給され
る。尚、結露した水は結露水溜８にためられる。
そしてＤ→Ｆの反応終了後空気の供給を中止し、
再びヒーター９により加熱すればＡ→Ｂの反応が
進行し、乾燥に供しえるようになる。 Next, with reference to FIG. 2, the mode of use of the above generator will be explained. First, open valve 4, and then
energize to heat the metal hydride M1 . When metal hydride M 1 is heated to t a , the hydrogen equilibrium pressure of metal hydride M 1 becomes p a (point A), which is greater than the hydrogen equilibrium pressure of metal hydride M 2 p c (point C) (t p is outside temperature), hydrogen gas is transferred from heat exchange container 1 to heat exchange container 2
The metal hydride M 2 absorbs hydrogen gas and is heated, reaching equilibrium at a temperature t b and a hydrogen equilibrium pressure p b (point B). After the reaction from A to B is completed, valve 4 is closed and the metal hydride is left to cool.
The temperatures of M 1 and M 2 become t p , and the hydrogen equilibrium pressures become p c and pe, respectively. At this time, p c > p e , so when valve 4 is opened, metal hydride M 2 releases hydrogen gas,
Metal hydride M 1 absorbs hydrogen gas, metal hydride M 2 is cooled from point C to point D (temperature t p → t d ),
The metal hydride M 1 is heated from point E to point F (temperature t p →t f ), and the reaction D→F proceeds. At this time, when air is sent by the blower 7, it is cooled by the heat exchanger 5' in the heat exchange container 2, moisture in the air is condensed and removed, and then heated by the heat exchanger 5 in the heat exchange container 1. , and is supplied to the drying chamber 10 as a heated drying gas. Note that the condensed water is stored in a condensation water reservoir 8.
Then, after the reaction of D → F is completed, the supply of air is stopped,
If it is heated again by the heater 9, the reaction A→B will proceed, and it will be ready for drying.
上記金属水素化物とは水素ガスと可逆的に反応
し、水素ガスを吸収する過程においては発熱し、
水素ガスを放出する過程においては吸熱する性質
を有する金属又は合金であつて、たとえばランタ
ンニツケル水素化物（LaNi5Hx）、カルシウムニ
ツケル水素化物（CaNi5Hx）、ミツシユメタルニ
ツケル水素化物（MmNi5Hx）、ミツシユメタル
コバルト水素化物（MmCoHx）、ネオジウムコ
バルト水素化物（NdCoHx）、鉄チタン水素化物
（FeTiHx）、バナジウム水素化物（VHx）、バナ
ジウムニオブ水素化物（VNbHx）、マグネシウ
ムニツケル水素化物（Mg2NiHx）等があげられ
る。そして２個の熱交換容器に内蔵された金属水
素化物は同種のものであつてもよいし異種のもの
であつてもよく、異種の金属水素化物の組み合せ
としては、たとえばランタンニツケル水素化物−
カルシウムニツケル水素化物、ミツシユメタルニ
ツケル水素化物−ランタンニツケル水素化物、ミ
ツシユメタルコバルト水素化物−ランタンニツケ
ル水素化物、バナジウムニオブ水素化物−ミツシ
ユメタルコバルト水素化物、鉄チタン水素化物−
ネオジウムコバルト水素化物等の組み合せがあげ
られる。 The metal hydride mentioned above reacts reversibly with hydrogen gas and generates heat in the process of absorbing hydrogen gas.
Metals or alloys that have the property of absorbing heat in the process of releasing hydrogen gas, such as lanthanum nickel hydride (LaNi 5 Hx), calcium nickel hydride (CaNi 5 Hx), and Mitsushi metal nickel hydride (MmNi 5 Hx), Mitsushi metal cobalt hydride (MmCoHx), neodymium cobalt hydride (NdCoHx), iron titanium hydride (FeTiHx), vanadium hydride (VHx), vanadium niobium hydride (VNbHx), magnesium nickel hydride (Mg 2 NiHx) etc. The metal hydrides contained in the two heat exchange vessels may be of the same type or different types, and a combination of different types of metal hydrides is, for example, lanthanum nickel hydride-
Calcium nickel hydride, Mitsushi metal nickel hydride - lanthanum nickel hydride, Mitsushi metal cobalt hydride - lanthanum nickel hydride, vanadium niobium hydride - Mitsushi metal cobalt hydride, iron titanium hydride -
Examples include combinations of neodymium cobalt hydride and the like.
本考案で使用されるヒーターは、電気ヒーター
の他、工場廃温水や太陽熱集熱温水を利用したヒ
ーターが利用できる。 The heater used in this invention can be an electric heater, or a heater that uses industrial waste hot water or solar heat collection hot water.
又、２個の連結された熱交換容器は２組以上組
み合わされると連続的に加熱乾燥気体が得られる
ので好ましい。第３図は２組組み合わされた装置
の一例を示す説明図である。図中１１、１２，１
３，１４は熱交換容器であり、熱交換容器１１及
び１３には金属水素化物M1が内蔵され、熱交換
容器１２及び１４には金属水素化物M2が内蔵さ
れている。熱交換容器１１と熱交換容器１２はバ
ルブ４１を介して連通管３１によつて開閉制御可
能に連結されており、熱交換容器１３と熱交換容
器１４はバルブ４２を介して連通管３２によつて
開閉制御可能に連結されている。５１，５２，５
３及び５４は熱交換容器１１，１２，１３及び１
４内にそれぞれ設置された熱交換器であり、熱交
換器５１と熱交換器５２はバルブ４３を介して配
管６５，６４で連結され、熱交換器５１と熱交換
器５３は配管６７で連結され、熱交換器５３と熱
交換器５４はバルブ４４を介して配管６６，６３
で連結されている。熱交換器５２の入口には配管
６１によりブロアー７１が連結され、熱交換器５
４の入口には配管６２によりブロアー７１が連結
されている。又、配管６５は分岐されバルブ４５
を介して配管６８に連結されており、配管６６は
分岐されて配管６９に連結されており、配管６８
と６９は配管７０に連結され乾燥室２０に連結さ
れている。９１及び９２はヒーターであり、それ
ぞれ熱交換容器１１及び１３内に設けられてい
る。又、８１及び８２は結露水溜であり、それぞ
れ熱交換器５２及び５２に配設されている。 Further, it is preferable to combine two or more sets of two connected heat exchange vessels because heated and dry gas can be obtained continuously. FIG. 3 is an explanatory diagram showing an example of two combined devices. 11, 12, 1 in the diagram
3 and 14 are heat exchange vessels; heat exchange vessels 11 and 13 contain a metal hydride M1 , and heat exchange vessels 12 and 14 contain a metal hydride M2 . The heat exchange container 11 and the heat exchange container 12 are connected via a valve 41 to a communication pipe 31 so that opening and closing can be controlled, and the heat exchange container 13 and the heat exchange container 14 are connected to each other by a communication pipe 32 via a valve 42. They are connected so that they can be opened and closed. 51, 52, 5
3 and 54 are heat exchange containers 11, 12, 13 and 1
Heat exchanger 51 and heat exchanger 52 are connected by pipes 65 and 64 via valve 43, and heat exchanger 51 and heat exchanger 53 are connected by pipe 67. The heat exchanger 53 and the heat exchanger 54 are connected to the pipes 66 and 63 via the valve 44.
are connected. A blower 71 is connected to the inlet of the heat exchanger 52 through a pipe 61, and a blower 71 is connected to the inlet of the heat exchanger 52.
A blower 71 is connected to the inlet of 4 through a pipe 62. Further, the pipe 65 is branched to the valve 45.
The pipe 66 is branched and connected to the pipe 69 via the pipe 68.
and 69 are connected to a pipe 70 and connected to the drying chamber 20. 91 and 92 are heaters, which are provided in the heat exchange containers 11 and 13, respectively. Further, 81 and 82 are dew condensation water reservoirs, which are arranged in the heat exchangers 52 and 52, respectively.
次に上記発生装置の使用態様を説明する。まず
バルブ４１を開放し、ヒーター９１で金属水素化
物M1を加熱し、Ａ→Ｂの反応を行い、反応終了
後バルブ４１を閉止する。次いでバルブ４３及び
４６を開放し、バルブ４４及び４５を閉止し、バ
ルブ４１及び４２を開放し、ヒーター９２で熱交
換容器１３内の金属水素化物M1を加熱すると共
にブロアー７１で空気を供給する。熱交換容器１
１と１２の間ではＤ→Ｆの反応が進行し、ブロア
ー７１で供給された空気は熱交換器５２で冷却除
湿され、熱交換器５１で加熱される。又、熱交換
容器１３はヒーター９２により加熱されているの
で、熱交換容器１３と１４の間ではＡ→Ｂの反応
が進行すると共に熱交換器５１から供給された空
気は熱交換器５３でも加熱される。 Next, the manner of use of the above generator will be explained. First, the valve 41 is opened, and the metal hydride M 1 is heated with the heater 91 to carry out the reaction A→B. After the reaction is completed, the valve 41 is closed. Then, the valves 43 and 46 are opened, the valves 44 and 45 are closed, and the valves 41 and 42 are opened, and the metal hydride M 1 in the heat exchange container 13 is heated by the heater 92, and air is supplied by the blower 71. . Heat exchange container 1
The reaction D→F progresses between 1 and 12, and the air supplied by the blower 71 is cooled and dehumidified by the heat exchanger 52, and then heated by the heat exchanger 51. Furthermore, since the heat exchange container 13 is heated by the heater 92, the reaction A→B progresses between the heat exchange containers 13 and 14, and the air supplied from the heat exchanger 51 is also heated in the heat exchanger 53. be done.
従つて、ブロアー７１から供給された空気は配
管６１−熱交換器５２−配管６４，６５−熱交換
器５１−配管６７−熱交換器５３−配管６６，６
９，７０を経由して乾燥室２０に送られる間に熱
交換器５２（熱交換容器１２）で冷却除湿され、
熱交換器５１（熱交換容器１１）及び熱交換器５
３（熱交換容器１３）で加熱され、乾燥した加熱
気体となつて乾燥室２０に供給される。そして熱
交換容器１１と１２の間でＤ→Ｆの反応が終了
し、熱交換容器１３と１４の間でＡ→Ｂの反応が
終了した後バルブ４３及び４６を閉止し、バルブ
４４及び４５を開放し、ヒーター９２を止め、ヒ
ーター９１で熱交換容器１１内の金属水素化物
M2を加熱すると、熱交換容器１１と１２の間で
はＡ→Ｂの反応が進行し、熱交換容器１３と１４
の間ではＤ→Ｆの反応が進行し、ブロアー７１に
より供給された空気は配管６２−熱交換器５４−
配管６３，６６−熱交換器５３−配管６７−熱交
換器５１−配管６５，６８，７０を経由して乾燥
室２０に送られる間に熱交換器５４（熱交換容器
１４）で冷却除湿され、熱交換器５３（熱交換容
器１３）及び熱交換器５１（熱交換容器１１）で
加熱され乾燥した加熱気体となつて乾燥室２０に
供給される。上記装置においては、上述の如くバ
ルブ及びヒーターを切り換えることにより連続的
に加熱乾燥気体を得ることができる。 Therefore, the air supplied from the blower 71 is routed through the pipe 61 - heat exchanger 52 - pipes 64, 65 - heat exchanger 51 - pipe 67 - heat exchanger 53 - pipes 66, 6.
9 and 70 to the drying chamber 20, it is cooled and dehumidified in the heat exchanger 52 (heat exchange container 12),
Heat exchanger 51 (heat exchange container 11) and heat exchanger 5
3 (heat exchange container 13), and is supplied to the drying chamber 20 as a dry heated gas. After the reaction D→F is completed between heat exchange vessels 11 and 12 and the reaction A→B is completed between heat exchange vessels 13 and 14, valves 43 and 46 are closed, and valves 44 and 45 are closed. The metal hydride in the heat exchange container 11 is removed by the heater 91.
When M 2 is heated, the reaction A→B progresses between heat exchange vessels 11 and 12, and heat exchange vessels 13 and 14
The reaction D→F progresses between, and the air supplied by the blower 71 is passed through the pipe 62 - heat exchanger 54 -
While being sent to the drying room 20 via piping 63, 66 - heat exchanger 53 - piping 67 - heat exchanger 51 - piping 65, 68, 70, it is cooled and dehumidified in heat exchanger 54 (heat exchange container 14). The heated gas is heated and dried by the heat exchanger 53 (heat exchange container 13) and the heat exchanger 51 (heat exchange container 11), and is supplied to the drying chamber 20. In the above device, heating and drying gas can be continuously obtained by switching the valve and heater as described above.
本考案の加熱乾燥気体発生装置の構成は上述の
通りであり、金属水素化物が水素ガスを吸収する
際に発生する熱と、水素ガス放出する際に吸収す
る熱の両方を利用し、気体を冷却して水分を結露
させ除去した後加熱するのであるから気体は効率
よく加熱され、得られた気体は湿度が低く乾燥に
適している。 The structure of the heated drying gas generator of the present invention is as described above, and it utilizes both the heat generated when the metal hydride absorbs hydrogen gas and the heat absorbed when it releases hydrogen gas, to generate gas. Since the gas is heated after being cooled to condense and remove moisture, the gas is efficiently heated, and the resulting gas has low humidity and is suitable for drying.
第１図は本考案の加熱乾燥気体発生装置の一例
を示す説明図であり、第２図は金属水素化物の水
素平衡圧特性を示すグラフであり、第３図は本考
案の加熱乾燥気体発生装置の異なる例を示す説明
図である。
１，２…熱交換容器、３…連通管、４…バル
ブ、５，５′…熱交換器、６，６′，６″…配管、
７…ブロアー、８…結露水溜、９…ヒーター、１
０…乾燥室。
Fig. 1 is an explanatory diagram showing an example of the heat-drying gas generating device of the present invention, Fig. 2 is a graph showing hydrogen equilibrium pressure characteristics of metal hydrides, and Fig. 3 is a diagram showing an example of the heat-drying gas generating device of the present invention. It is an explanatory diagram showing a different example of a device. 1, 2... Heat exchange container, 3... Communication pipe, 4... Valve, 5, 5'... Heat exchanger, 6, 6', 6''... Piping,
7... Blower, 8... Condensation water reservoir, 9... Heater, 1
0...Drying room.
Claims (1)
交換容器を、途中にバルブを有する連通管によつ
て開閉制御可能に連結すると共に、一方の熱交換
容器内には熱交換器を設け、他方の熱交換容器内
には熱交換器とヒーターを設け、前記一方の熱交
換容器内の熱交換器には結露水溜を配設し、さら
に熱交換器入口には配管によりブロアーを連設
し、熱交換器出口は前記他方の熱交換容器内の熱
交換器の入口と配管により連結し、また前記他方
の熱交換容器内の熱交換器の出口には、加熱乾燥
気体の出口である配管を連設したことを特徴とす
る加熱乾燥気体発生装置。 Two heat exchange vessels, each containing a metal hydride, are connected to each other so that they can be opened and closed via a communication pipe with a valve in the middle, and a heat exchanger is provided in one heat exchange vessel, and a heat exchanger is provided in the other. A heat exchanger and a heater are provided in the heat exchange container, a condensation water reservoir is provided in the heat exchanger in the one heat exchange container, and a blower is connected to the inlet of the heat exchanger via piping, The outlet of the heat exchanger is connected to the inlet of the heat exchanger in the other heat exchange container by piping, and the outlet of the heat exchanger in the other heat exchange container is connected with piping which is an outlet for heated drying gas. A heating drying gas generator characterized by being installed in series.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1980045755U JPS631148Y2 (en) | 1980-04-03 | 1980-04-03 |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1980045755U JPS631148Y2 (en) | 1980-04-03 | 1980-04-03 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS56146857U JPS56146857U (en) | 1981-11-05 |
| JPS631148Y2 true JPS631148Y2 (en) | 1988-01-12 |
Family
ID=29640822
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1980045755U Expired JPS631148Y2 (en) | 1980-04-03 | 1980-04-03 |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS631148Y2 (en) |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5533588A (en) * | 1978-07-12 | 1980-03-08 | Standard Oil Co | Device for circulating hydride |
-
1980
- 1980-04-03 JP JP1980045755U patent/JPS631148Y2/ja not_active Expired
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5533588A (en) * | 1978-07-12 | 1980-03-08 | Standard Oil Co | Device for circulating hydride |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS56146857U (en) | 1981-11-05 |
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