JPH0410529Y2 - - Google Patents
Info
- Publication number
- JPH0410529Y2 JPH0410529Y2 JP1986149914U JP14991486U JPH0410529Y2 JP H0410529 Y2 JPH0410529 Y2 JP H0410529Y2 JP 1986149914 U JP1986149914 U JP 1986149914U JP 14991486 U JP14991486 U JP 14991486U JP H0410529 Y2 JPH0410529 Y2 JP H0410529Y2
- Authority
- JP
- Japan
- Prior art keywords
- heavy oil
- heater
- hot water
- regenerator
- heating
- 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
Landscapes
- Feeding And Controlling Fuel (AREA)
- 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、吸収式冷温水機に係り、燃料である
重油の予熱に要する電気ヒータの消費電力の減少
および電気ヒータの寿命を延ばすのに好適な吸収
式冷温水機の燃料予熱装置に関する。[Detailed description of the invention] [Field of industrial application] The present invention relates to an absorption type water chiller/heater, and is used to reduce the power consumption of the electric heater required for preheating heavy oil, which is the fuel, and to extend the life of the electric heater. The present invention relates to a fuel preheating device for a suitable absorption type water chiller/heater.
第2図は従来の吸収式冷温水機の燃料予熱装置
21の一例を示したもので、オイルタンク22に
供給された燃料の重油は、オイルタンク22下部
より燃焼装置23内に供給される。この燃焼装置
23内には、重油圧送用のオイルポンプ25と、
重油を加熱する予熱器26と、燃焼をON−OFF
するON−OFF電磁弁28と、重油を噴霧する噴
霧ノズル29とが直列に配置されている。バーナ
30には、ブロア31からダンパ32で調整され
た燃焼用空気が供給される。予熱器26内には、
重油を加熱する電気ヒータ33が設けられ、予熱
器26内の重油温度を温度センサ35で検知し、
ON−OFFスイツチ36で電気ヒータ33への通
電の制御を行なう。またON−OFF電磁弁28お
よびブロア31は、ON−OFFスイツチ36に電
気的に接続された制御器38により制御される。
FIG. 2 shows an example of a fuel preheating device 21 of a conventional absorption type water chiller/heater. Heavy oil, which is the fuel supplied to an oil tank 22, is supplied into a combustion device 23 from the lower part of the oil tank 22. Inside this combustion device 23, there is an oil pump 25 for feeding heavy hydraulic pressure,
Preheater 26 that heats heavy oil and turns combustion on and off
An ON-OFF solenoid valve 28 and a spray nozzle 29 that spray heavy oil are arranged in series. Combustion air regulated by a damper 32 is supplied to the burner 30 from a blower 31 . Inside the preheater 26,
An electric heater 33 for heating heavy oil is provided, and a temperature sensor 35 detects the temperature of the heavy oil in the preheater 26.
The ON-OFF switch 36 controls power supply to the electric heater 33. Further, the ON-OFF solenoid valve 28 and the blower 31 are controlled by a controller 38 electrically connected to the ON-OFF switch 36.
ところで吸収式冷温水機において、冬期、外気
温が0℃以下になると、重油の粘度が高くなり噴
霧ノズル29で重油を霧化しにくい状態となる。
したがつて、燃焼状態も悪くなり、不完全燃焼と
なり、効率の低下や不着火等の欠点が生じる。そ
こで、上記従来技術にあつては、冬期、重油を適
温に加熱し粘度を低くするために、電気ヒータ3
3を設け、バーナ30へ供給する重油を予熱し昇
温している。この電気ヒータ33は、前述の如
く、ON−OFFスイツチ36により制御されてお
り、重油温度が通常20〜40℃まで上つたことを温
度センサ35により検知するとON−OFFスイツ
チ36が開状態となり、電気ヒータ33への通電
が停止する。 By the way, in the absorption type water cooler/heater, when the outside temperature drops to 0° C. or lower in winter, the viscosity of the heavy oil increases, making it difficult to atomize the heavy oil with the spray nozzle 29.
Therefore, the combustion condition deteriorates, resulting in incomplete combustion, resulting in drawbacks such as reduced efficiency and non-ignition. Therefore, in the above conventional technology, in order to heat heavy oil to an appropriate temperature and lower its viscosity in winter, an electric heater 3 is used.
3 is provided to preheat and raise the temperature of heavy oil supplied to the burner 30. As mentioned above, this electric heater 33 is controlled by the ON-OFF switch 36, and when the temperature sensor 35 detects that the heavy oil temperature has risen to 20 to 40°C, the ON-OFF switch 36 is opened. The power supply to the electric heater 33 is stopped.
しかし、上記従来技術によれば、冬期の運転時
においては、外気温が低いため、電気ヒータ33
に通電する必要があり不経済であるという問題が
あつた。また重油温度調節のため、電気ヒータ3
3は絶えずON−OFF制御されるので、電気ヒー
タ33の寿命が短かくなるという問題があつた。
However, according to the above-mentioned conventional technology, during winter operation, the electric heater 33
There was a problem that it was uneconomical because it required electricity to be applied to the terminal. In addition, electric heater 3 is installed to adjust the temperature of heavy oil.
Since the electric heater 33 is constantly controlled to be turned on and off, there is a problem in that the life of the electric heater 33 is shortened.
本考案の目的は、上記のような問題点を解決
し、燃料である重油の予熱を暖房サイクルにより
発生する温水の熱によつてできるようにした吸収
式冷温水機の燃料予熱装置を提供することであ
る。 The purpose of the present invention is to solve the above-mentioned problems and provide a fuel preheating device for an absorption type water chiller/heater in which heavy oil, which is a fuel, can be preheated using the heat of hot water generated in a heating cycle. That's true.
かかる目的達成のため、本考案は、重油を燃料
として吸収溶液を加熱する再生器と、該再生器か
らの冷媒蒸気の凝縮潜熱で負荷循環水を加熱する
蒸発器と、該蒸発器へ前記再生器からの冷媒蒸気
および吸収溶液を導びく冷暖切換弁と、前記吸収
溶液および凝縮冷媒を前記再生器へ圧送する溶液
ポンプとにより暖房サイクルを形成し、該暖房サ
イクル中で加熱された負荷循環水の一部を導入
し、その温水の熱を重油の加熱源とした温水加熱
器を備えたものである。
To achieve this objective, the present invention includes a regenerator that heats an absorption solution using heavy oil as fuel, an evaporator that heats load circulating water with the latent heat of condensation of refrigerant vapor from the regenerator, and a A heating cycle is formed by a cooling/heating switching valve that guides refrigerant vapor and absorption solution from the regenerator, and a solution pump that pumps the absorption solution and condensed refrigerant to the regenerator, and the load circulating water heated in the heating cycle is The system is equipped with a hot water heater that uses the heat from the hot water as a heating source for heavy oil.
上述の構成によれば、再生器内の吸収溶液は、
重油を燃料として加熱され冷媒蒸気を発生する。
この冷媒蒸気は吸収溶液を伴なつて冷暖切換弁を
通過し蒸発器に導びかれる。すると、蒸発器内を
流れる負荷水は、冷媒蒸気の凝縮潜熱により昇温
し、室内負荷へと導びかれる。ここで凝縮した冷
媒は吸収溶液とともに溶液ポンプにより再度再生
器へ流入し暖房サイクルを形成する。この暖房サ
イクルにより発生した温水は温水加熱器内を循環
し、これによつて温水加熱器内を通過する重油が
加熱される。
According to the above configuration, the absorption solution in the regenerator is
It is heated using heavy oil as fuel and generates refrigerant vapor.
This refrigerant vapor, accompanied by the absorption solution, passes through the cooling/heating switching valve and is led to the evaporator. Then, the load water flowing in the evaporator is heated by the latent heat of condensation of the refrigerant vapor, and is led to the indoor load. The condensed refrigerant flows together with the absorption solution into the regenerator again by the solution pump to form a heating cycle. The hot water generated by this heating cycle circulates within the hot water heater, thereby heating the heavy oil passing through the hot water heater.
以下、本考案を図面に示す実施例に基づいて説
明する。
Hereinafter, the present invention will be explained based on embodiments shown in the drawings.
第1図は本考案に係る吸収式冷温水機の燃料予
熱装置1を示したもので、第2図に示すものと同
一の部品には、同一の符号を付して説明する。 FIG. 1 shows a fuel preheating device 1 for an absorption type water chiller/heater according to the present invention, and the same parts as those shown in FIG. 2 will be described with the same reference numerals.
吸収式冷温水機の燃料予熱装置1には、重油を
燃料として加熱される再生器2と、この再生器2
と揚液管3により連通接続され再生器2で発生し
た冷媒蒸気と吸収溶液とを分離する分離器5と、
この冷媒蒸気と吸収溶液とを蒸発器6へ導びく冷
暖切換弁8とが設けられている。また燃焼装置2
3内には、オイルポンプ25、温水加熱器9、予
熱器26、ON−OFF電磁弁28および噴霧ノズ
ル29が直列に配置されている。蒸発器6のコイ
ル6a内は、負荷、例えば室内負荷へ熱を移動す
るための負荷水が循環し、その一部は温水導入管
10により接続された温水加熱器9に導入され、
該温水加熱器9内を循環する。 The fuel preheating device 1 of the absorption type water chiller/heater includes a regenerator 2 that is heated using heavy oil as fuel;
and a separator 5 that is connected in communication with the liquid lift pipe 3 and separates the refrigerant vapor generated in the regenerator 2 from the absorption solution;
A cooling/heating switching valve 8 is provided to guide this refrigerant vapor and absorption solution to the evaporator 6. Also, combustion device 2
3, an oil pump 25, a hot water heater 9, a preheater 26, an ON-OFF solenoid valve 28, and a spray nozzle 29 are arranged in series. Inside the coil 6a of the evaporator 6, load water for transferring heat to a load, for example, an indoor load, is circulated, and a part of it is introduced into a hot water heater 9 connected by a hot water introduction pipe 10.
The water is circulated within the hot water heater 9.
また第1図において、11は分離器5に接続さ
れた凝縮器、12は該凝縮器11に接続され、か
つ蒸発器6に対向して配置された吸収器、13は
制御器38に接続され、蒸発器6のコイル6a内
の負荷水の温度により吸収式冷温水機の燃焼を制
御する温水サーモ、15は再生器2と蒸発器6と
を連結する管路16に配置された溶液ポンプであ
る。 Further, in FIG. 1, 11 is a condenser connected to the separator 5, 12 is an absorber connected to the condenser 11 and placed opposite the evaporator 6, and 13 is connected to the controller 38. , a hot water thermostat that controls the combustion of the absorption type water chiller/heater based on the temperature of the load water in the coil 6a of the evaporator 6; 15 is a solution pump disposed in the pipe 16 connecting the regenerator 2 and the evaporator 6; be.
つぎに、本考案の実施例の作用を説明する。 Next, the operation of the embodiment of the present invention will be explained.
外気温が0℃以下を示すような冬期に暖房運転
を行なう場合、温度センサ35で低い重油の温度
を検知すると、ON−OFFスイツチ36が閉状態
となり、電気ヒータ33に通電が行なわれる。そ
して、設定された温度(一般的には20〜40℃)ま
で重油温度が上がると、制御器38からの信号に
より燃焼動作が開始され、ブロア31でプレパー
ジが行なわれ、オイルポンプ25の起動、ON−
OFF電磁弁28の開動作により、燃焼が始まる。 When heating is performed in winter when the outside temperature is below 0° C., when the temperature sensor 35 detects a low temperature of heavy oil, the ON-OFF switch 36 is closed and the electric heater 33 is energized. When the heavy oil temperature rises to a set temperature (generally 20 to 40°C), combustion operation is started by a signal from the controller 38, pre-purging is performed by the blower 31, and the oil pump 25 is started. ON−
Combustion begins by opening the OFF solenoid valve 28.
すると、再生器2内の吸収希溶液が噴霧ノズル
29から噴射した噴霧状の重油により加熱され、
冷媒蒸気を発生し、やがて加熱された吸収溶液と
冷媒蒸気は、揚液管3を上昇し、分離器5に達す
るが、吸収器12および凝縮器11に冷却水が循
環されていないので、一度分離された冷媒蒸気
は、吸収溶液を伴つて冷暖切換弁8を通過して蒸
発器6へと導びかれる。 Then, the absorbed dilute solution in the regenerator 2 is heated by the heavy oil spray sprayed from the spray nozzle 29,
Refrigerant vapor is generated, and the heated absorption solution and refrigerant vapor eventually ascend the liquid lift pipe 3 and reach the separator 5, but since cooling water is not circulated to the absorber 12 and condenser 11, The separated refrigerant vapor passes through the cooling/heating switching valve 8 and is guided to the evaporator 6 together with the absorption solution.
蒸発器6のコイル6a内を流れる負荷水は冷媒
蒸気の凝縮潜熱により昇温し、矢印Aの方向から
室内負荷へと導びかれる。ここで、凝縮した冷媒
は、吸収溶液とともに、溶液ポンプ15により再
度再生器2へと流入し、暖房サイクルを継続す
る。したがつて、時間経過に伴ない蒸発器6のコ
イル6a内を流れる負荷水は、一般的な暖房温度
の50〜55℃の温水となる。この温水の温度上昇に
伴つて、温水導入管10を通して温水を循環して
いる温水加熱器9の温水の温度も上昇し、該温水
加熱器9内を通過する燃料の重油を加熱する働き
を始める。この温水加熱器9における加熱度は、
温水サーモ13により吸収式冷温水機の燃料が停
止する温度(約55℃)で重油が30℃程度となるよ
う、伝熱面積、温水循環量によつて調整されてい
る。したがつて、この温水加熱器9を通過した重
油は十分昇温されているため、予熱器26におけ
る再加熱は不要となり、電気ヒータ33は非通電
の状態となる。かりに、吸収式冷温水機がON−
OFFしても蒸発器6内を流れる負荷水の温水加
熱器9への循環は継続されるため、重油は加熱さ
れつづけた状態となり、つぎの燃焼再開時には、
電気ヒータ33による予熱は不要となる。また吸
収式冷温水機の燃焼停止状態であつても、温水
は、温水サーモ13により50゜〜55℃に調整され
るため、重油の引火点である60℃以上を越えて昇
温することはない。つまり、吸収式冷凍機が暖房
運転を継続する限り、電気ヒータ33への通電は
不要となる。また想定した外気温以下で運転され
る場合には、温水加熱器9と予熱器26との両者
が作動することになり、重油が設定された温度ま
で上がると、予熱器26の電気ヒータ33への通
電が停止される。すなわち、2段階の加熱システ
ムとなり、適正な重油温度が得られる。 The load water flowing through the coil 6a of the evaporator 6 is heated by the latent heat of condensation of the refrigerant vapor, and is led to the indoor load in the direction of arrow A. Here, the condensed refrigerant flows together with the absorption solution into the regenerator 2 again by the solution pump 15 to continue the heating cycle. Therefore, over time, the load water flowing through the coil 6a of the evaporator 6 becomes hot water at a typical heating temperature of 50 to 55°C. As the temperature of this hot water rises, the temperature of the hot water in the hot water heater 9 that circulates hot water through the hot water introduction pipe 10 also rises, and begins to heat the heavy oil that is the fuel that passes through the hot water heater 9. . The heating degree in this hot water heater 9 is
The heat transfer area and the amount of hot water circulation are adjusted so that the temperature of the heavy oil is approximately 30°C at which the hot water thermometer 13 stops the fuel of the absorption chiller/heater (approximately 55°C). Therefore, since the heavy oil that has passed through the hot water heater 9 has been sufficiently heated, reheating in the preheater 26 is unnecessary, and the electric heater 33 is in a non-energized state. Suddenly, the absorption type water cooler/heater is turned on.
Even if it is turned off, the load water flowing through the evaporator 6 continues to be circulated to the hot water heater 9, so the heavy oil continues to be heated, and when the next combustion restarts,
Preheating by the electric heater 33 becomes unnecessary. In addition, even when the absorption type water cooler/heater is in a state where combustion is stopped, the hot water is adjusted to 50° to 55°C by the hot water thermometer 13, so the temperature does not rise above 60°C, which is the flash point of heavy oil. do not have. That is, as long as the absorption refrigerating machine continues heating operation, it is not necessary to energize the electric heater 33. In addition, when operating at a temperature below the assumed outside temperature, both the hot water heater 9 and the preheater 26 will operate, and when the heavy oil reaches the set temperature, it will be transferred to the electric heater 33 of the preheater 26. energization is stopped. That is, it becomes a two-stage heating system, and an appropriate heavy oil temperature can be obtained.
上述のとおり、本考案によれば、暖房出力のご
く一部を加熱源として用いるが、燃料とする重油
は電気料金と比べて大幅に廉価であり、また電気
ヒータによる重油の加熱は運転開始時だけてよい
ので、消費電力を大幅に減少させることができ
る。また、電気ヒータの通電時間、ON−OFF回
数が減少するので、電気ヒータの寿命が延びると
いう効果がある。さらに、吸収式冷温水機が想定
した外気温以下で運転される場合であつても、2
段階の加熱システムとなるので、適正な重油温度
が得られる。また、本考案の装置は重油により腐
食しやすい予熱器系のメンテナンスを非常に容易
にする。
As mentioned above, according to the present invention, a small portion of the heating output is used as a heating source, but the heavy oil used as fuel is significantly cheaper than the electricity bill, and the heating of the heavy oil by the electric heater is required at the start of operation. Since the power consumption can be reduced significantly, power consumption can be significantly reduced. Furthermore, since the energization time and the number of ON/OFF times of the electric heater are reduced, the life of the electric heater is extended. Furthermore, even if the absorption type water chiller/heater is operated at a temperature below the assumed outside temperature, 2.
Since it is a staged heating system, appropriate heavy oil temperature can be obtained. Additionally, the device of the present invention greatly facilitates maintenance of the preheater system, which is prone to corrosion due to heavy oil.
第1図は本考案に係る吸収式冷温水機の燃料予
熱装置のシステム図、第2図は従来例に係る吸収
式冷温水機の燃料予熱装置のシステム図である。
1……吸収式冷温水機の燃料予熱装置、2……
再生器、6……蒸発器、8……冷暖切換弁、9…
…温水加熱器、15……溶液ポンプ。
FIG. 1 is a system diagram of a fuel preheating device for an absorption type water chiller/heater according to the present invention, and FIG. 2 is a system diagram of a fuel preheating device for an absorption type chiller/heater according to a conventional example. 1...Fuel preheating device for absorption type water chiller/heater, 2...
Regenerator, 6... Evaporator, 8... Cooling/heating switching valve, 9...
...Hot water heater, 15...Solution pump.
Claims (1)
と、該再生器からの冷媒蒸気の凝縮潜熱で負荷循
環水を加熱する蒸発器と、該蒸発器へ前記再生器
からの冷媒蒸気および吸収溶液を導びく冷暖切換
弁と、前記吸収溶液および凝縮冷媒を前記再生器
へ圧送する溶液ポンプとにより暖房サイクルを形
成し、該暖房サイクル中で加熱された負荷循環水
の一部を導入し、その温水の熱を重油の加熱源と
した温水加熱器を備えた吸収式冷温水機の燃料余
熱装置。 a regenerator that heats an absorption solution using heavy oil as fuel; an evaporator that heats load circulation water with latent heat of condensation of refrigerant vapor from the regenerator; and a refrigerant vapor and absorption solution from the regenerator that are introduced to the evaporator. A heating cycle is formed by a cooling/heating switching valve and a solution pump that pumps the absorption solution and condensed refrigerant to the regenerator, and a part of the load circulating water heated in the heating cycle is introduced, and the hot water is A fuel residual heat device for an absorption type water chiller/heater equipped with a hot water heater that uses heat as the heating source for heavy oil.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1986149914U JPH0410529Y2 (en) | 1986-09-30 | 1986-09-30 |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1986149914U JPH0410529Y2 (en) | 1986-09-30 | 1986-09-30 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6357469U JPS6357469U (en) | 1988-04-16 |
| JPH0410529Y2 true JPH0410529Y2 (en) | 1992-03-16 |
Family
ID=31065563
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1986149914U Expired JPH0410529Y2 (en) | 1986-09-30 | 1986-09-30 |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0410529Y2 (en) |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS4214704Y1 (en) * | 1966-07-04 | 1967-08-22 | ||
| JPS4527695Y1 (en) * | 1968-01-18 | 1970-10-26 | ||
| JPS5728963A (en) * | 1980-07-29 | 1982-02-16 | Sanyo Electric Co | Absorption refrigerating machine |
| JPS57192758A (en) * | 1981-05-25 | 1982-11-26 | Ebara Mfg | Absorption air conditioner |
-
1986
- 1986-09-30 JP JP1986149914U patent/JPH0410529Y2/ja not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6357469U (en) | 1988-04-16 |
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