JPH0424372Y2 - - Google Patents
Info
- Publication number
- JPH0424372Y2 JPH0424372Y2 JP6791885U JP6791885U JPH0424372Y2 JP H0424372 Y2 JPH0424372 Y2 JP H0424372Y2 JP 6791885 U JP6791885 U JP 6791885U JP 6791885 U JP6791885 U JP 6791885U JP H0424372 Y2 JPH0424372 Y2 JP H0424372Y2
- Authority
- JP
- Japan
- Prior art keywords
- heat
- absorbent
- absorber
- condenser
- generator
- 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
- 230000002745 absorbent Effects 0.000 claims description 40
- 239000002250 absorbent Substances 0.000 claims description 40
- 238000010438 heat treatment Methods 0.000 claims description 30
- 239000007788 liquid Substances 0.000 claims description 30
- 239000006096 absorbing agent Substances 0.000 claims description 29
- 238000011084 recovery Methods 0.000 claims description 7
- 239000000126 substance Substances 0.000 claims description 5
- 239000012466 permeate Substances 0.000 claims description 3
- 238000001704 evaporation Methods 0.000 claims 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 19
- 239000013529 heat transfer fluid Substances 0.000 description 12
- 238000009413 insulation Methods 0.000 description 6
- 230000005494 condensation Effects 0.000 description 5
- 238000009833 condensation Methods 0.000 description 5
- 238000005338 heat storage Methods 0.000 description 5
- 238000001816 cooling Methods 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 239000012530 fluid Substances 0.000 description 3
- 238000010521 absorption reaction Methods 0.000 description 2
- 238000004090 dissolution Methods 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 239000011358 absorbing material Substances 0.000 description 1
- 230000037237 body shape Effects 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- -1 solar heat Substances 0.000 description 1
- 239000002918 waste heat Substances 0.000 description 1
Landscapes
- Sorption Type Refrigeration Machines (AREA)
Description
【考案の詳細な説明】
〔産業上の利用分野〕
本考案は、加熱による蒸気放出に伴つて吸熱す
ると共に、蒸気吸収に伴つて発熱する吸収剤を吸
収兼発生器に設け、その吸収兼発生器に対して、
蒸気放出のための加熱装置、熱を受取る熱回収
部、及び、蒸気を受渡す蒸発兼凝縮器を設け、そ
の蒸発兼凝縮器内の凝縮液を蒸発する伝熱管を設
けたケミカルヒートポンプに関する。[Detailed description of the invention] [Industrial field of application] The present invention provides an absorbent that absorbs heat as vapor is released by heating and generates heat as it absorbs vapor in an absorber/generator. For the vessel,
The present invention relates to a chemical heat pump that is provided with a heating device for releasing steam, a heat recovery section that receives heat, an evaporator/condenser that transfers steam, and a heat transfer tube that evaporates condensed liquid in the evaporator/condenser.
従来、第3図に示すように、保温ケース3内
に、吸収剤1Aを上方に配置して、かつ、伝熱管
2Aを下方に配置して収容し、凝縮液Wを保温ケ
ース3の底部に貯留するように構成していた。
Conventionally, as shown in FIG. 3, an absorbent 1A is placed above and a heat transfer tube 2A is placed below in a heat insulation case 3, and the condensate W is placed at the bottom of the heat insulation case 3. It was configured to be stored.
しかし、吸収剤1Aから蒸気を発生させ、その
蒸気を伝熱管2Aによる冷却で凝縮させる蓄熱状
態において、保温ケース3の蒸気に対する接触面
積が大になり、多量の蒸気がケース壁面で凝縮す
るために、保温ケース3からの外部放熱量が多く
なつて、熱エネルギーのロスが多くなり、また、
保温ケース3の上部内面3Aがほぼ水平面である
ために、その上部内面3Aから吸収剤1Aに凝縮
液が滴下して、吸収剤1Aが溶解しやすく、一層
の改良が望まれていた。
However, in a heat storage state in which steam is generated from the absorbent 1A and the steam is condensed by cooling by the heat transfer tube 2A, the contact area of the heat insulation case 3 with the steam becomes large, and a large amount of steam condenses on the case wall. , the amount of external heat dissipated from the thermal insulation case 3 increases, and the loss of thermal energy increases, and
Since the upper inner surface 3A of the heat-retaining case 3 is a substantially horizontal surface, condensed liquid drips onto the absorbent 1A from the upper inner surface 3A, and the absorbent 1A is easily dissolved, and further improvements have been desired.
本考案の目的は、簡単な改造でもつて、吸収兼
発生器からの蒸気が保温ケースの壁面で凝縮する
ことを十分に抑制でき、凝縮液による吸収剤の溶
解を十分に防止できるようにする点にある。 The purpose of this invention is to make it possible to sufficiently suppress the condensation of steam from the absorber/generator on the wall of the heat insulation case, even with simple modifications, and to sufficiently prevent the absorbent from dissolving due to condensate. It is in.
本考案の特徴構成は、吸収剤を有する吸収兼発
生器との間で蒸気を受渡す蒸発兼凝縮器に、凝縮
液を浸透させる多孔状吸液体を設け、その吸液体
を前記吸収剤の横側方全周又はほぼ全周にわたつ
て配置し、前記伝熱管を前記吸液体の内部に配置
し、前記吸収剤の上部に臨む上部内面を、その吸
収剤の横側方側ほど低くなるように傾斜させたこ
とにあり、その作用効果は次の通りである。
The characteristic configuration of the present invention is that an evaporator/condenser that transfers vapor between an absorber/generator having an absorbent is provided with a porous liquid absorber that allows the condensate to permeate, and the absorbent liquid is transferred to the side of the absorbent. The heat transfer tube is arranged over the entire lateral circumference or almost the entire lateral circumference, and the heat transfer tube is arranged inside the liquid absorbent, and the upper inner surface facing the upper part of the absorbent is inclined so that it becomes lower as the lateral side of the absorbent increases. The functions and effects are as follows.
つまり、吸収兼発生器で発生した蒸気は、吸収
剤の横側方を囲む吸液体の孔に流入して、伝熱管
の冷却で凝縮し、凝縮液は吸液体の孔内に貯留さ
れる。したがつて、吸収兼発生器から蒸発兼凝縮
器に送られる蒸気が保温ケースと接触する割合は
極めて少なくなり、保温ケースとの接触による凝
縮に起因する熱エネルギーロスを大巾に減少でき
る。
In other words, the vapor generated in the absorber/generator flows into the liquid absorbing holes surrounding the absorbent, is condensed by cooling the heat transfer tube, and the condensed liquid is stored in the liquid absorbing holes. Therefore, the proportion of steam sent from the absorber-generator to the evaporator-condenser that comes into contact with the heat-insulating case is extremely small, and thermal energy loss caused by condensation due to contact with the heat-insulating case can be greatly reduced.
また、例えば保温ケースに加熱手段を備えさせ
て、保温ケースと蒸気の接触による凝縮を防止す
るに比して、単に多孔状吸液体を付加するだけで
済むから構成の簡略化を図れる。 Furthermore, compared to, for example, providing the heat insulating case with a heating means to prevent condensation due to contact between the heat insulating case and steam, the structure can be simplified because it is sufficient to simply add porous liquid absorbing material.
そして、凝縮液を吸液体の孔内に貯留させて、
凝縮液と吸収剤の接触を無くし、かつ、吸収剤の
上部に臨む上部内面を、たとえそこで凝縮が生じ
ても、凝縮液が、その上部内面を伝つて流化し
て、吸収剤に滴下しないようにしてあるから、吸
収剤が凝縮液に溶解するといつた不都合な事態を
確実に防止できる。 Then, the condensed liquid is stored in the holes of the liquid absorber,
Eliminate contact between the condensate and the absorbent, and make sure that even if condensation occurs there, the condensate will not flow down the upper inner surface and drip onto the absorbent. This ensures that undesirable situations such as dissolution of the absorbent into the condensate can be prevented.
その結果、単に、吸収兼発生器と蒸発兼凝縮器
の配置、上部内面の形状に改良を施すと共に多孔
状吸液体を付加するだけの簡単な改造でもつて、
無駄な凝縮を十分に少なくして、熱効率良好に運
転でき、かつ、吸収剤の溶解による性能低下を確
実に防止して、長期にわたつて良好な運転を行え
るようになり、全体として性能、耐久性、コスト
面の全てにおいて優れたケミカルヒートポンプを
提供できるようになつた。
As a result, even with simple modifications such as simply improving the arrangement of the absorber/generator and evaporator/condenser, the shape of the upper inner surface, and adding porous liquid absorbers,
By sufficiently reducing unnecessary condensation, it is possible to operate with good thermal efficiency, and by reliably preventing performance deterioration due to absorbent dissolution, it is possible to maintain good operation over a long period of time, improving overall performance and durability. It is now possible to provide chemical heat pumps that are superior in terms of performance and cost.
次に、第1図及び第2図により実施例を示す。 Next, an example will be shown with reference to FIGS. 1 and 2.
加熱による蒸気放出に伴つて吸熱すると共に蒸
気吸収に伴つて発熱する吸収剤1Aを有する吸収
兼発生器1、及び、その吸収兼発生器1との間で
蒸気を受渡す蒸気兼凝縮器2を保温ケース3に内
装し、他方、給水管路4及び出湯管路5を接続し
た貯湯槽6に、その中の貯留水を加熱する熱交換
器7A,7Bを設けてある。 An absorber/generator 1 having an absorbent 1A that absorbs heat as vapor is released by heating and generates heat as it absorbs the vapor, and a steam condenser 2 that transfers steam between the absorber/generator 1 and the absorber/generator 1. Heat exchangers 7A and 7B are provided in a hot water storage tank 6, which is housed inside the heat insulating case 3 and connected to the water supply pipe 4 and the hot water outlet pipe 5, for heating the water stored therein.
蒸発兼凝縮器2において、凝縮液の全量を浸透
させる多孔状吸液体2Bを設け、その吸液体2B
を、下側のみが開口した中空体形状に形成して、
吸収剤1Aの横側方全周にわたつてかつ上方に配
置し、伝熱管2Aを吸液体2Bの内部に配置し、
吸液体2Bの上部内面Sをアーチ型やドーム型等
の傾斜面に形成してある。 In the evaporator/condenser 2, a porous liquid absorber 2B is provided to allow the entire amount of condensate to permeate.
is formed into a hollow body shape with only the lower side open,
The heat transfer tube 2A is placed over the entire lateral circumference of the absorbent 1A, and the heat transfer tube 2A is placed inside the liquid absorbent 2B.
The upper inner surface S of the liquid absorbent 2B is formed into an arch-shaped, dome-shaped, or other inclined surface.
つまり、吸収剤1Aからの蒸気が、ほとんど保
温ケース3に接触しないで吸液体2Bの孔内に送
られ、伝熱管2Aによる冷却で凝縮されるように
構成し、凝縮液が吸液体2B内に貯留されて、吸
収剤1Aが溶解しないように構成してある。ま
た、吸液体2Bの上部内面Sで凝縮しても、凝縮
液が、傾斜した上部内面Sを伝つて流下して、吸
収剤1A上に滴下しないように構成してある。 In other words, the vapor from the absorbent 1A is sent into the holes of the liquid absorber 2B without almost contacting the heat insulating case 3, and is condensed by cooling by the heat transfer tube 2A, so that the condensed liquid flows into the liquid absorber 2B. It is configured so that the absorbent 1A is stored and does not dissolve. Further, even if the liquid is condensed on the upper inner surface S of the liquid absorbent 2B, the condensed liquid is configured so as not to flow down along the inclined upper inner surface S and drip onto the absorbent 1A.
そして、吸収兼発生器1と加熱装置8あるいは
前記貯留水加熱用熱交換器7Bとにわたつて熱運
搬流体を循環するポンプP1付き流路9を設け、
かつ、蒸発兼凝縮器2と入熱用交換器10又は前
記貯留水加熱用熱交換器7Aとにわたつて熱運搬
流体を循環するポンプP2付き流路11を設けて
ある。また、吸収兼発生器1を作動状態の加熱装
置8に対してのみ、かつ、蒸発兼凝縮器2を貯留
水加熱用熱交換器7Aに夫々接続する蓄熱状態
と、吸収兼発生器1を貯留水加熱用熱交換器7B
に、かつ、蒸発兼凝縮器2を入熱用熱交換器10
に対してのみ夫々接続する加熱状態とに前記両流
路9,11の接続状態を選択的に切換える弁装置
12a,12bを各流路9,11に介装し、もつ
て、下記の蓄熱状態及び加熱状態を択一的に現出
し、かつ、両状態を交互に繰返すことにより貯湯
槽6内の水を加熱するケミカルヒートポンプを構
成してある。 Then, a flow path 9 with a pump P1 is provided for circulating the heat transport fluid between the absorber/generator 1 and the heating device 8 or the heat exchanger 7B for heating the stored water,
In addition, a flow path 11 with a pump P2 is provided for circulating the heat transfer fluid between the evaporator/condenser 2 and the heat input exchanger 10 or the stored water heating heat exchanger 7A. In addition, there is a heat storage state in which the absorber/generator 1 is connected only to the heating device 8 in the operating state, and the evaporator/condenser 2 is connected to the heat exchanger 7A for heating the stored water, and the absorber/generator 1 is connected only to the heating device 8 in the operating state. Water heating heat exchanger 7B
, and the evaporator/condenser 2 is connected to the heat exchanger 10 for heat input.
Valve devices 12a and 12b are interposed in each of the flow channels 9 and 11 to selectively switch the connection state of both flow channels 9 and 11 to a heating state in which they are connected only to the heat storage state described below. This constitutes a chemical heat pump that heats the water in the hot water tank 6 by selectively displaying the and heating states and alternately repeating both states.
(イ) 蓄熱状態〔第1図イ参照〕
加熱装置8からの高温の熱運搬流体を吸収兼発
生器1に供給し、吸収兼発生器1の吸収剤1Aを
伝熱管2Bの熱運搬流体により加熱して、吸収剤
1Aから蒸気を放出させ、その蒸気を吸液体2B
の孔内に流入させる。同時に、貯留水加熱用熱交
換器7Aからの低温の熱運搬流体を蒸発兼凝縮器
2の伝熱管2Aに供給し、吸液体2B内の蒸気を
熱運搬流体により冷却して凝縮すると共に、凝縮
熱により熱運搬流体を加熱する。そして、その加
熱された熱運搬流体を貯留水加熱用熱交換器7A
に供給し、貯湯槽6内の水を熱運搬流体により加
熱する。(B) Heat storage state [See Figure 1A] The high temperature heat transport fluid from the heating device 8 is supplied to the absorber/generator 1, and the absorbent 1A of the absorber/generator 1 is absorbed by the heat transport fluid of the heat transfer tube 2B. The absorbent 1A releases vapor by heating, and the vapor is transferred to the absorbent 2B.
flow into the hole. At the same time, the low-temperature heat transfer fluid from the heat exchanger 7A for heating the stored water is supplied to the heat transfer tube 2A of the evaporator/condenser 2, and the vapor in the liquid absorption liquid 2B is cooled and condensed by the heat transfer fluid. The heat heats the heat transfer fluid. Then, the heated heat transfer fluid is transferred to the stored water heating heat exchanger 7A.
The water in the hot water storage tank 6 is heated by the heat transfer fluid.
(ロ) 加熱状態〔第1図(ロ)参照〕
入熱用熱交換器10において外部からの熱を取
入れた熱運搬流体を蒸発兼凝縮器2の伝熱管2A
に供給し、吸液体2Bに貯えられている凝縮液を
熱運搬流体により加熱して、蒸気を発生させ、そ
の蒸気を吸収兼発生器1に流入させる。同時に、
貯留水加熱用熱交換器7Bからの低温の熱運搬流
体を吸収兼発生器1に供給し、吸収兼発生器1に
おいて、蒸発兼凝縮器2からの蒸気を吸収剤1A
に吸収させると共に、吸収熱により熱運搬流体を
加熱する。そして、その加熱された熱運搬流体を
貯留水加熱用熱交換器7Bに供給し、貯湯槽6内
の水を熱運搬流体により加熱する。(B) Heating state [See Figure 1 (B)] The heat transfer fluid that has taken in heat from the outside in the heat input heat exchanger 10 is transferred to the heat transfer tube 2A of the evaporator/condenser 2.
The condensate stored in the liquid absorber 2B is heated by the heat transfer fluid to generate steam, and the steam is caused to flow into the absorber/generator 1. at the same time,
The low temperature heat transfer fluid from the heat exchanger 7B for heating the stored water is supplied to the absorber/generator 1, and in the absorber/generator 1, the steam from the evaporator/condenser 2 is transferred to the absorbent 1A.
The absorbed heat heats the heat transfer fluid. Then, the heated heat transfer fluid is supplied to the stored water heating heat exchanger 7B, and the water in the hot water storage tank 6 is heated by the heat transfer fluid.
次に別の実施例を説明する。 Next, another embodiment will be described.
貯湯槽6に代えて例えば暖房用等の加熱用熱交
換器を設けてもよく、それらを熱回収部6と総称
する。 In place of the hot water storage tank 6, for example, a heat exchanger for heating or the like may be provided, and these are collectively referred to as a heat recovery section 6.
加熱装置8の加熱型式は種々の構成変更が可能
であり、又、加熱装置8に供給するエネルギーの
形態も都市ガスや液体燃料、あるいは、太陽熱を
利用するものや、廃熱を利用するもの等、種々の
ものを適用できる。 The heating type of the heating device 8 can be changed in various configurations, and the form of energy supplied to the heating device 8 can be city gas, liquid fuel, solar heat, waste heat, etc. , various methods can be applied.
吸収兼発生器1と加熱装置8あるいは熱回収部
6との間で熱を運搬する構成、及び、伝熱管2A
と入熱用熱交換器10あるいは熱回収部6との間
で熱を運搬する構成は各種変更自在である。 A configuration for transporting heat between the absorber/generator 1 and the heating device 8 or the heat recovery section 6, and the heat transfer tube 2A
The configuration for transporting heat between the heat input heat exchanger 10 or the heat recovery section 6 can be modified in various ways.
多孔状吸液体2Bは、形状において筒形状等に
変更でき、材質において焼結金属、金網等の適当
なものから選択でき、要するに、凝縮液の全量又
はほぼ全量を浸透させる吸液能力を有し、かつ、
吸収剤1Aの横側方全周又はほぼ全周にわたつて
配置してあればよい。 The porous liquid absorbent 2B can be changed in shape to a cylindrical shape, etc., and can be selected from suitable materials such as sintered metal or wire mesh, and has the ability to absorb all or almost all of the condensate. ,and,
It is sufficient if they are arranged over the entire lateral circumference or almost the entire lateral circumference of the absorbent 1A.
吸収剤1Aの上方に吸液体2Bが無い時、吸収
剤1Aの上部に臨む保温ケース3の上部内面を傾
斜させる等、吸収剤1Aの横側方側ほど低くなる
ように傾斜した上部内面Sを形成するに、具体構
造において適当に変更できる。 When there is no absorbent liquid 2B above the absorbent 1A, the upper inner surface S is sloped so that it becomes lower toward the lateral side of the absorbent 1A, such as by slanting the upper inner surface of the heat insulation case 3 facing the upper part of the absorbent 1A. Any suitable changes may be made in the specific construction.
第1図及び第2図は、本考案の実施例を示し、
第1図イは蓄熱状態をかつ第1図ロは加熱状態を
夫々示す概念図、第2図は要部断面図である。第
3図は従来例の要部図である。
1……吸収兼発生器、1A……吸収剤、2……
蒸発兼凝縮器、2A……伝熱管、2B……吸液
体、6……熱回収部、8……加熱装置、S……上
部内面。
1 and 2 show an embodiment of the present invention,
FIG. 1A is a conceptual diagram showing a heat storage state, FIG. 1B is a conceptual diagram showing a heating state, and FIG. 2 is a sectional view of a main part. FIG. 3 is a diagram of main parts of a conventional example. 1...Absorber and generator, 1A...Absorbent, 2...
Evaporator/condenser, 2A...heat transfer tube, 2B...liquid absorption, 6...heat recovery section, 8...heating device, S...upper inner surface.
Claims (1)
蒸気吸収に伴つて発熱する吸収剤1Aを吸収兼発
生器1に設け、その吸収兼発生器1に対して、蒸
気放出のための加熱装置8、熱を受取る熱回収部
6、及び、蒸気を受渡す蒸発兼凝縮器2を設け、
その蒸発兼凝縮器2内の凝縮液を蒸発する伝熱管
2Aを設けたケミカルヒートポンプであつて、前
記蒸発兼凝縮器2に、凝縮液を浸透させる多孔状
吸液体2Bを設け、その吸液体2Bを前記吸収剤
1Aの横側方全周又はほぼ全周にわたつて配置
し、前記伝熱管2Aを前記吸液体2Bの内部に配
置し、前記吸収剤1Aの上部に臨む上部内面S
を、その吸収剤1Aの横側方側ほど低くなるよう
に傾斜させてあるケミカルヒートポンプ。 Along with absorbing heat as steam is released due to heating,
An absorbent 1A that generates heat as it absorbs steam is provided in an absorber/generator 1, and the absorber/generator 1 is equipped with a heating device 8 for releasing steam, a heat recovery section 6 for receiving heat, and a heat recovery unit 6 for receiving heat. Provides an evaporator and condenser 2 for delivery,
The chemical heat pump is equipped with a heat exchanger tube 2A for evaporating the condensate in the evaporator/condenser 2, and the evaporator/condenser 2 is provided with a porous liquid absorber 2B that allows the condensate to permeate. are arranged over the entire lateral or almost entire circumference of the absorbent 1A, the heat transfer tube 2A is arranged inside the liquid absorber 2B, and an upper inner surface S facing the upper part of the absorbent 1A is arranged.
The chemical heat pump is inclined so that it becomes lower toward the lateral side of the absorbent 1A.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP6791885U JPH0424372Y2 (en) | 1985-05-07 | 1985-05-07 |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP6791885U JPH0424372Y2 (en) | 1985-05-07 | 1985-05-07 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS61185961U JPS61185961U (en) | 1986-11-20 |
| JPH0424372Y2 true JPH0424372Y2 (en) | 1992-06-09 |
Family
ID=30602188
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP6791885U Expired JPH0424372Y2 (en) | 1985-05-07 | 1985-05-07 |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0424372Y2 (en) |
-
1985
- 1985-05-07 JP JP6791885U patent/JPH0424372Y2/ja not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS61185961U (en) | 1986-11-20 |
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