JPH0252902A - Reduced pressure steam generator - Google Patents
Reduced pressure steam generatorInfo
- Publication number
- JPH0252902A JPH0252902A JP20251188A JP20251188A JPH0252902A JP H0252902 A JPH0252902 A JP H0252902A JP 20251188 A JP20251188 A JP 20251188A JP 20251188 A JP20251188 A JP 20251188A JP H0252902 A JPH0252902 A JP H0252902A
- Authority
- JP
- Japan
- Prior art keywords
- steam
- liquid
- steam generator
- pressure
- reduced pressure
- 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.)
- Granted
Links
- 239000007788 liquid Substances 0.000 claims abstract description 38
- 230000003247 decreasing effect Effects 0.000 abstract description 2
- 238000010438 heat treatment Methods 0.000 description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 12
- 230000007797 corrosion Effects 0.000 description 4
- 238000005260 corrosion Methods 0.000 description 4
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 239000000498 cooling water Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 230000000379 polymerizing effect Effects 0.000 description 1
- 230000002194 synthesizing effect Effects 0.000 description 1
Landscapes
- Jet Pumps And Other Pumps (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
Abstract
Description
【発明の詳細な説明】
産業上の利用分野
本発明は、被hu熱物を通常100℃以下の比較的低温
蒸気の凝縮熱伝達により加熱するための減圧蒸気を供給
する減圧蒸気発生装置に関する。DETAILED DESCRIPTION OF THE INVENTION Field of the Invention The present invention relates to a reduced pressure steam generator that supplies reduced pressure steam for heating an object to be heated by condensation heat transfer of relatively low temperature steam, usually below 100°C.
各種食品の乾燥や蒸溜、あるいは、化学工場にあける各
種物質の分解、合成、重合、縮合等を行う反応釜装置等
においては、被加熱物を100°C以下の低温で加熱し
ているケースが多くある。そしてこの低温加熱を行う場
合、最も製品品質や生産性に大きな影響を及ぼす要素が
hO熱温度の不均一、すなわち温度ムラでおる。In reaction kettle equipment used for drying and distilling various foods, or for decomposing, synthesizing, polymerizing, and condensing various substances in chemical factories, there are cases in which the objects to be heated are heated at low temperatures of 100°C or less. There are many. When this low-temperature heating is performed, the factor that has the greatest effect on product quality and productivity is non-uniformity of the hO heating temperature, that is, temperature unevenness.
従来技術
従来の低温加熱は、100’C以下の温水を温水ボイラ
ーで発生させ被加熱物と熱交換することによって行なわ
れていた。また、蒸気ボイラーで高温の蒸気を発生させ
、その蒸気によって温水を作って熱交換すること等も行
なわれていた。Prior Art Conventional low-temperature heating was performed by generating hot water of 100'C or less in a hot water boiler and exchanging heat with the object to be heated. In addition, a steam boiler was used to generate high-temperature steam, and the steam was used to create hot water for heat exchange.
本発明が解決しようとする課題
温水は同じ温度の蒸気と比べて保有している熱容量が小
さく、また、その境膜伝熱係数もはるかに小ざい。従っ
て、被加熱物全体を均一に加熱することができず、被加
熱物に部分的な低温部が発生して加熱温度ムラを生じる
問題がおった。加熱温度が均一に維持されないと、被加
熱物の製品品質が一定に維持できなくなったり、生産性
の低下を来たす等の弊害が生じる。Problems to be Solved by the Invention Hot water has a smaller heat capacity than steam at the same temperature, and its film heat transfer coefficient is also much smaller. Therefore, the entire object to be heated cannot be heated uniformly, and there is a problem in that the object to be heated has local low-temperature parts, resulting in uneven heating temperature. If the heating temperature is not maintained uniformly, there will be problems such as the inability to maintain a constant product quality of the heated object and a decrease in productivity.
また、従来の温水加熱では、温水中に含まれる不純物や
溶存酸素により、ボイラーや温水配管及び温水使用装置
等に腐蝕が発生しやすく、伝熱効率の低下や耐久性に乏
しいという問題がおった。In addition, in conventional hot water heating, impurities and dissolved oxygen contained in the hot water tend to cause corrosion in boilers, hot water piping, hot water usage equipment, etc., leading to problems such as reduced heat transfer efficiency and poor durability.
従って本発明は、温水に代って減圧された低温の蒸気を
供給することにより温度ムラのない、且つ、腐蝕の発生
しない加熱ができるようにすることを課題とする。Therefore, it is an object of the present invention to supply low-temperature steam under reduced pressure instead of hot water, thereby enabling heating without temperature unevenness and corrosion.
課題を解決するための手段
上記の課題を解決するために講じた本発明の技術的手段
は、液体を加熱して蒸気に換える蒸気発生手段と、真空
吸引手段とを加熱器を介して連結管で連結し、上記真空
吸引手段と蒸気発生手段の間に、蒸気発生手段に液体を
供給する給液手段と、装置全体の減圧度を調整するため
の減圧弁を設けてなるものでおる。Means for Solving the Problems The technical means of the present invention taken to solve the above problems is to connect a steam generation means for heating a liquid to steam and a vacuum suction means through a heater. A liquid supply means for supplying liquid to the steam generation means and a pressure reduction valve for adjusting the degree of pressure reduction of the entire apparatus are provided between the vacuum suction means and the steam generation means.
作用
真空吸引手段により、蒸気発生手段と加熱器の内部は減
圧状態となる。蒸気発生手段に給液手段から液体が供給
されると液体は加熱されただちに減圧蒸気が発生する。The vacuum suction means creates a reduced pressure inside the steam generation means and the heater. When liquid is supplied from the liquid supply means to the steam generation means, the liquid is heated and immediately generates reduced pressure steam.
減圧蒸気は系内が大気圧以下の真空状態でおれば100
’C以下となる。発生した減圧蒸気は連結管を通って加
熱器に達し、被加熱物を均一に加熱する。加熱したこと
によって熱を奪われた減圧蒸気は一部がドレン化し、残
った減圧蒸気と共に真空吸引手段により加熱器から吸引
される。蒸気発生手段と加熱器内の減圧度は減圧弁によ
り任意に調整される。Reduced pressure steam is 100% if the system is in a vacuum state below atmospheric pressure.
'C or below. The generated reduced pressure steam passes through the connecting pipe and reaches the heater, uniformly heating the object to be heated. Part of the reduced pressure steam that has been deprived of heat by heating is converted into drain, and is sucked together with the remaining reduced pressure steam from the heater by the vacuum suction means. The degree of pressure reduction within the steam generation means and heater is arbitrarily adjusted by a pressure reduction valve.
発明の効果
本発明によれば、被加熱物を低温で加熱する場合に、温
水を用いることなく減圧蒸気で加熱することができ、温
度ムラが発生せず、製品品質を一定に維持したり、高生
産性を確保することができる
また、減圧蒸気を用いることにより、含まれる不純物は
少なく、また、蒸気発生手段と連結管及び加熱器内は減
圧された真空状態でおり、酸素による腐蝕が発生しにく
い。Effects of the Invention According to the present invention, when heating an object to be heated at a low temperature, it can be heated with reduced pressure steam without using hot water, temperature unevenness does not occur, product quality can be maintained constant, High productivity can be ensured.In addition, by using reduced pressure steam, there are fewer impurities, and the steam generation means, connecting pipes, and heater are in a vacuum state, which prevents corrosion due to oxygen. It's hard to do.
実施例
上記の技術的手段の具体例を示す実施例を説明する。(
第1図参照)
本発明の減圧蒸気発生装置は、液体を加熱して蒸気に換
える蒸気発生手段1と、被加熱物を加熱する加熱器2と
、真空吸引手段3と、蒸気発生手段1と加熱器2と真空
吸引手段3を連結する連結管4と、蒸気発生手段1に液
体を供給する給液手段5と、装置の減圧度を調整するた
めの減圧弁13とから成る。Embodiment An embodiment illustrating a specific example of the above technical means will be described. (
(See Figure 1) The reduced-pressure steam generation device of the present invention includes a steam generation means 1 that heats a liquid and converts it into steam, a heater 2 that heats an object to be heated, a vacuum suction means 3, and a steam generation means 1. It consists of a connecting pipe 4 that connects the heater 2 and the vacuum suction means 3, a liquid supply means 5 that supplies liquid to the steam generation means 1, and a pressure reducing valve 13 that adjusts the degree of pressure reduction of the device.
真空吸引手段3で、蒸気発生手段1と加熱器2と連結管
4の内部を減圧状態にする。The vacuum suction means 3 brings the insides of the steam generation means 1, the heater 2, and the connecting pipe 4 into a reduced pressure state.
蒸気発生手段1は、バーナー7と燃焼室8で蒸発熱源を
成し、給液手段5から供給されてきた液体で減圧蒸気を
生成する。給液手段5は、給液タンク9と、給液タンク
9と蒸気発生手段1の間に配した給ti、mを制御する
制御弁10とから成る。The steam generating means 1 uses a burner 7 and a combustion chamber 8 to form an evaporative heat source, and generates reduced pressure steam using the liquid supplied from the liquid supply means 5. The liquid supply means 5 includes a liquid supply tank 9 and a control valve 10 arranged between the liquid supply tank 9 and the steam generating means 1 to control the supply ti, m.
制御弁10は、蒸気発生手段1内に取り付けた液位セン
サー11.12からの信号により給液量を制御する。蒸
気発生手段1の給液手段5側に減圧弁13を取り付ける
。減圧弁13は、真空吸引手段3で吸引される蒸気発生
手段1と連結管4と加熱器2の内部が設定圧力よりも低
くなれば、今まで閉弁していたものが開弁じて給液量を
より多く供給し、蒸気量を増やして減圧圧力を設定圧力
まで高め、反対に設定圧力よりも高く成れば閉弁方向に
作用して蒸気量°を減少させ、設定圧力を維持するもの
である。The control valve 10 controls the amount of liquid supplied by a signal from a liquid level sensor 11.12 installed in the steam generating means 1. A pressure reducing valve 13 is attached to the liquid supply means 5 side of the steam generation means 1. When the internal pressure of the steam generating means 1, the connecting pipe 4, and the heater 2 sucked by the vacuum suction means 3 becomes lower than the set pressure, the pressure reducing valve 13, which was previously closed, opens and starts supplying liquid. A device that supplies a larger amount of steam, increases the amount of steam, and raises the reduced pressure to the set pressure. Conversely, if the pressure becomes higher than the set pressure, it acts in the direction of closing the valve, decreasing the amount of steam and maintaining the set pressure. It is.
真空吸引手段3は、エゼクタ−式の真空ポンプであり、
給液タンク9と渦巻きポンプ16の吸込口17を連結し
、渦巻きポンプ16の吐出口18とエセクター14の吸
込管15を連結し、吸込管15の一端のノズル19を経
てデイフユーザ部208再び給液タンク9に連結したも
のである。ノズル19を通過する高速流体により真空吸
引力が発生する。また、エゼクタ−14で発生する真空
吸引力は、エゼクタ−14を通過する流体の温度におけ
る飽和圧力と等しくなるために、飽和圧力すなわち真空
吸引力を、より精度良く保つために、給液タンク9内の
液温を制御する温度制御弁21を介して冷却水を注入す
る。符号22は、温度制御弁21へ給液タンク9内の液
温信号を送る温度センサーでおる。The vacuum suction means 3 is an ejector-type vacuum pump,
The liquid supply tank 9 and the suction port 17 of the centrifugal pump 16 are connected, the discharge port 18 of the centrifugal pump 16 and the suction pipe 15 of the esector 14 are connected, and the liquid is supplied to the differential user section 208 again through the nozzle 19 at one end of the suction pipe 15. It is connected to tank 9. The high velocity fluid passing through the nozzle 19 creates a vacuum suction force. In addition, since the vacuum suction force generated by the ejector 14 is equal to the saturation pressure at the temperature of the fluid passing through the ejector 14, in order to maintain the saturation pressure, that is, the vacuum suction force more accurately, the liquid supply tank 9 Cooling water is injected through a temperature control valve 21 that controls the temperature of the liquid inside. Reference numeral 22 denotes a temperature sensor that sends a liquid temperature signal in the liquid supply tank 9 to the temperature control valve 21.
エゼクタ−14に、加熱器2の出口側管23を連結する
。出口側管23には加熱器2で発生したドレンをエゼク
タ−14側に優先的に排出するスチームトラップ25を
設ける。The outlet side pipe 23 of the heater 2 is connected to the ejector 14. The outlet side pipe 23 is provided with a steam trap 25 for preferentially discharging the drain generated in the heater 2 to the ejector 14 side.
本実施例においては、真空吸引手段3としてエセクター
14と渦巻きポンプ16を組合せたエセクター式真空ポ
ンプを示したが、従来から用いられている真空ポンプを
単独で用いることもできるし、上記エセクター式真空ポ
ンプと組合せて用いることもできる。また、同様に、蒸
気発生手段1として、バーナー7を用いたボイラーを示
したが、従来の高温高圧蒸気ボイラーで発生した高温蒸
気あるいは高温水を用いて熱交換することにより減圧蒸
気を発生させることもできる。In this embodiment, an esector-type vacuum pump in which an esector 14 and a centrifugal pump 16 are combined is shown as the vacuum suction means 3, but a conventionally used vacuum pump can also be used alone, or the esector-type vacuum pump described above can be used alone. It can also be used in combination with a pump. Similarly, although a boiler using a burner 7 is shown as the steam generation means 1, it is also possible to generate reduced pressure steam by exchanging heat with high temperature steam or high temperature water generated in a conventional high temperature high pressure steam boiler. You can also do it.
本減圧蒸気発生装置は、蒸気発生手段1で減圧蒸気を発
生し、加熱器2へ供給することにより、被加熱物を温水
でなく減圧蒸気で加熱することができ、腐蝕の発生しに
くい、耐久性に優れた装置で、温度ムラのない加熱を行
うことができる。This reduced-pressure steam generator generates reduced-pressure steam with the steam generation means 1 and supplies it to the heater 2, so that the object to be heated can be heated with reduced-pressure steam instead of hot water, and is corrosion-resistant and durable. The device has excellent properties and can heat evenly.
第1図は本発明の1実施例の概略の構成を示す構成図で
おる。
1:蒸気発生手段 2:加熱器
3:真空吸引手段 4:連結管
5:給液手段 7:バーナー
9:給液タンク 13:減圧弁FIG. 1 is a block diagram showing a schematic structure of an embodiment of the present invention. 1: Steam generation means 2: Heater 3: Vacuum suction means 4: Connecting pipe 5: Liquid supply means 7: Burner 9: Liquid supply tank 13: Pressure reducing valve
Claims (1)
吸引手段とを加熱器を介して連結管で連結し、上記真空
吸引手段と蒸気発生手段の間に、蒸気発生手段に液体を
供給する給液手段と、装置全体の減圧度を調整する減圧
弁を設けた減圧蒸気発生装置。1. A steam generating means that heats a liquid to convert it into steam and a vacuum suction means are connected by a connecting pipe through a heater, and liquid is supplied to the steam generating means between the vacuum suction means and the steam generating means. A reduced-pressure steam generator equipped with a liquid supply means to provide liquid and a pressure-reducing valve to adjust the degree of pressure reduction of the entire device.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP63202511A JPH0788932B2 (en) | 1988-08-12 | 1988-08-12 | Reduced pressure steam generator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP63202511A JPH0788932B2 (en) | 1988-08-12 | 1988-08-12 | Reduced pressure steam generator |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0252902A true JPH0252902A (en) | 1990-02-22 |
| JPH0788932B2 JPH0788932B2 (en) | 1995-09-27 |
Family
ID=16458696
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP63202511A Expired - Fee Related JPH0788932B2 (en) | 1988-08-12 | 1988-08-12 | Reduced pressure steam generator |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0788932B2 (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2002147400A (en) * | 2000-11-15 | 2002-05-22 | Tlv Co Ltd | Ejector vacuum pump |
| JP2011137073A (en) * | 2009-12-28 | 2011-07-14 | Tosoh Corp | Method for recovering polyethylene particle and apparatus for producing polyethylene particle |
| JP2018109474A (en) * | 2017-01-05 | 2018-07-12 | 株式会社テイエルブイ | Drain collection system |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5723703A (en) * | 1980-07-19 | 1982-02-08 | Babcock Hitachi Kk | Boiler controller |
| JPS5751559A (en) * | 1980-09-12 | 1982-03-26 | Aisin Seiki Co Ltd | Brake booster |
| JPS5765503A (en) * | 1980-10-09 | 1982-04-21 | Mitsubishi Heavy Ind Ltd | Boiler feed water controller |
-
1988
- 1988-08-12 JP JP63202511A patent/JPH0788932B2/en not_active Expired - Fee Related
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5723703A (en) * | 1980-07-19 | 1982-02-08 | Babcock Hitachi Kk | Boiler controller |
| JPS5751559A (en) * | 1980-09-12 | 1982-03-26 | Aisin Seiki Co Ltd | Brake booster |
| JPS5765503A (en) * | 1980-10-09 | 1982-04-21 | Mitsubishi Heavy Ind Ltd | Boiler feed water controller |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2002147400A (en) * | 2000-11-15 | 2002-05-22 | Tlv Co Ltd | Ejector vacuum pump |
| JP2011137073A (en) * | 2009-12-28 | 2011-07-14 | Tosoh Corp | Method for recovering polyethylene particle and apparatus for producing polyethylene particle |
| JP2018109474A (en) * | 2017-01-05 | 2018-07-12 | 株式会社テイエルブイ | Drain collection system |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0788932B2 (en) | 1995-09-27 |
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