JP3241749B2 - Evacuation method for vacuum deaerator - Google Patents
Evacuation method for vacuum deaeratorInfo
- Publication number
- JP3241749B2 JP3241749B2 JP11569291A JP11569291A JP3241749B2 JP 3241749 B2 JP3241749 B2 JP 3241749B2 JP 11569291 A JP11569291 A JP 11569291A JP 11569291 A JP11569291 A JP 11569291A JP 3241749 B2 JP3241749 B2 JP 3241749B2
- Authority
- JP
- Japan
- Prior art keywords
- tank
- exhaust
- liquid
- water supply
- flow path
- 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 - Lifetime
Links
Landscapes
- Details Of Reciprocating Pumps (AREA)
- Degasification And Air Bubble Elimination (AREA)
Description
【0001】[0001]
【産業上の利用分野】本発明は、マンション・ビル等の
脱気による防錆やボイラー等の脱酸素処理等の多処理能
力と寿命性、運転費、維持の低減を要求される真空脱気
装置の減圧排気方法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to vacuum degassing, which requires multi-processing capability such as rust prevention by degassing condominiums and buildings and deoxygenation treatment of boilers, etc. and reduced life, operation cost and maintenance. The present invention relates to a method for evacuation of a device.
【0002】[0002]
【従来の技術】従来、真空を利用した脱気装置には大気
吸い込み排気型の一般の真空ポンプで脱気槽内を減圧し
気液分離を行い、かつ発生した気体を連続的に真空ポン
プによって排気させ減圧度を維持する脱気装置と、特殊
な膜を使用し内面に液体を通過させる際に外面を減圧さ
せ気体のみ液体から膜外部へと分離する膜脱気装置など
がある。2. Description of the Related Art Conventionally, a deaerator using vacuum has been decompressed in a deaeration tank by a general vacuum pump of an air suction and exhaust type to perform gas-liquid separation, and the generated gas is continuously discharged by a vacuum pump. There are a deaerator that exhausts gas and maintains the degree of decompression, and a membrane deaerator that uses a special membrane and depressurizes the outer surface when passing liquid through the inner surface and separates only gas from the liquid to the outside of the membrane.
【0003】[0003]
【発明が解決しようとする課題】大気吸い込み排気型の
真空装置を使用した脱気装置は液体送水用のポンプ・槽
内を減圧する真空ポンプと2種のポンプが必要となり当
初費用や運転費が大となってしまう。又真空ポンプは定
期的に部品交換、保守等を実施しないとポンプの能力は
低下してしまい、その結果真空下における液体送水のバ
ランスが崩れたり、減圧度自体上がらない等の不具合な
どがある。また膜を使用した脱気装置も液体送水ポンプ
と真空ポンプを使用しなくてはならなく膜自体も高価な
ものであり膜の寿命性、能力性の低下防止に前処理と定
期保守を必要とし当初費用と運転費が大幅にかかる等、
長期運転にあたっては寿命性、運転費、維持等に問題が
あるものである。A deaerator using a vacuum device of an air suction and exhaust type requires two pumps, a pump for liquid supply and a vacuum pump for depressurizing the inside of the tank. It will be big. If the vacuum pump is not replaced or maintained periodically, the performance of the pump is reduced. As a result, there is a problem in that the balance of water supply under vacuum is lost, and the degree of pressure reduction is not increased. Deaerators using membranes also require the use of liquid water pumps and vacuum pumps, and the membranes themselves are expensive, and require pretreatment and periodic maintenance to prevent deterioration in membrane life and performance. Initial costs and operating costs are significantly higher,
In long-term operation, there are problems in life, operation cost, maintenance, and the like.
【0004】[0004]
【課題を解決するための手段】本発明は上記従来の問題
点に鑑みなされたものであり、本発明の真空脱気装置の
減圧排気方法は、脱気槽と、排気槽と、排気槽の上部に
設けた逆止機構を有する排気弁と、脱気槽に連結した給
水路と、脱気槽の頂部と排気槽の底部を連絡する一方の
流路と、脱気槽の底部を送水ポンプの給水側に連結する
とともに送水ポンプの排水側より液体を導く排水路と、
排水路の送水ポンプ排出側より分岐し排気槽下部に連絡
する他方の流路とを有する真空脱気装置の減圧排気方法
において、他方の流路を閉塞し、一方の流路を開いた状
態で送水ポンプにより液体を吐出しつつ脱気層に液体を
供給し脱気槽と排気槽とを液体で満たす工程と、脱気槽
内への新たな液体の供給を停止し、脱気槽内の液体を排
水路を介して送水ポンプにより吐出することにより気液
分離を脱気槽内において行なう工程と、脱気槽内の気体
が所定の減圧度になった際に一方の流路を閉塞し、他方
の流路を開いた状態で脱気槽内の液体を排水路を介して
送水ポンプにより吐出させながら、吐出された液体の一
部を他方の流路を介して排気槽内に供給し排気槽内の気
体を排気弁を通じて外部に押し出す工程とを備えたこと
を特徴とするものである。SUMMARY OF THE INVENTION The present invention has been made in view of the above-mentioned conventional problems, and a method for depressurizing and exhausting a vacuum deaerator according to the present invention comprises a deaeration tank, an exhaust tank, and an exhaust tank. An exhaust valve having a check mechanism provided at the top, a water supply passage connected to the deaeration tank, one flow path connecting the top of the deaeration tank and the bottom of the exhaust tank, and a water supply pump at the bottom of the deaeration tank A drainage channel that connects to the water supply side of the pump and guides liquid from the drainage side of the water supply pump;
In the depressurizing / evacuating method of the vacuum deaerator having the other flow path branched from the water supply pump discharge side of the drainage passage and connected to the lower part of the exhaust tank, the other flow path is closed and one of the flow paths is opened. A step of supplying liquid to the degassing layer while discharging liquid by the water pump and filling the degassing tank and the exhaust tank with liquid, and stopping supply of new liquid into the degassing tank, A step of performing gas-liquid separation in a degassing tank by discharging a liquid by a water pump through a drainage channel, and closing one of the flow paths when the gas in the degassing tank reaches a predetermined pressure reduction degree. While discharging the liquid in the deaeration tank by the water supply pump through the drainage channel with the other flow path opened, a part of the discharged liquid is supplied into the exhaust tank through the other flow path. Extruding the gas in the exhaust tank to the outside through an exhaust valve. A.
【0005】また、本発明の真空脱気装置の減圧排気方
法の他の構成では、脱気槽と、排気槽と、脱気槽及び排
気槽上部にそれぞれ設けた逆止機構を有する排気弁と、
脱気槽に連結した給水路と、脱気槽の上部と排気槽の上
部を連絡する上部流路と、脱気槽の底部を送水ポンプの
給水側に連結するとともに送水ポンプの排水側より液体
を導く排水路と、排水路の送水ポンプ給水側と排気槽の
底部を連絡する第1底部流路と、排水路の送水ポンプ排
水側より分岐し排気槽底部に連絡する第2底部流路とを
有する真空脱気装置の減圧排気方法において、排水路の
送水ポンプ給水側における脱気槽側流路と第2底部流路
を閉塞し、上部流路を開き、第1底部流路を排水路の送
水ポンプ給水側における送水ポンプ側流路を経て送水ポ
ンプへと連通させた状態で送水ポンプにより液体を吐出
しつつ脱気層に液体を供給し脱気槽と排気槽とを液体で
満たす工程と、脱気槽内への新たな液体の供給を停止
し、脱気槽内の液体を上部流路、排気槽、第1底部流
路、及び排水路を介して送水ポンプにより吐出させるこ
とにより、気液分離を脱気槽内において行なう工程と、
脱気槽内の気体が所定の減圧度になった際に上部流路と
第1底部流路を閉塞し、排水路の送水ポンプ給水側にお
ける脱気槽側流路と第2底部流路を開いた状態で脱気槽
内の液体を排水路を介して送水ポンプにより吐出させな
がら、吐出された液体の一部を第2底部流路を介して排
気槽内に供給し排気槽内の気体を排気弁を通じて外部に
押し出す工程とを備えたことを特徴とするものである。In another configuration of the method for depressurizing and exhausting a vacuum deaerator according to the present invention, a deaeration tank, an exhaust tank, and an exhaust valve having a check mechanism provided on the deaeration tank and the exhaust tank are provided. ,
A water supply channel connected to the deaeration tank, an upper flow path connecting the upper part of the deaeration tank and the upper part of the exhaust tank, and a bottom part of the deaeration tank connected to the water supply side of the water supply pump and liquid from the water discharge side of the water supply pump A first bottom passage connecting the water supply pump water supply side of the drain passage to the bottom of the exhaust tank, and a second bottom passage branching from the water pump discharge side of the drain passage and communicating with the bottom of the exhaust tank. In the vacuum evacuation method of the vacuum deaerator having the above, the deaeration tank side flow path and the second bottom flow path on the water supply pump water supply side of the drainage path are closed, the upper flow path is opened, and the first bottom flow path is connected to the drainage path. Filling the deaeration layer with the liquid while discharging the liquid by the water supply pump in a state of being connected to the water supply pump through the water supply pump side flow path on the water supply pump water supply side, and filling the deaeration tank and the exhaust tank with the liquid. And the supply of new liquid into the degassing tank is stopped. Upper flow path, an exhaust tank, first bottom flow path, and by ejecting the water pump via the drain passage, and performing gas-liquid separation in the degassing tank,
When the gas in the deaeration tank reaches a predetermined degree of pressure reduction, the upper flow path and the first bottom flow path are closed, and the deaeration tank side flow path and the second bottom flow path on the water supply pump water supply side of the drainage channel are connected. While the liquid in the degassing tank is discharged by the water supply pump through the drainage channel in the open state, a part of the discharged liquid is supplied to the exhaust tank through the second bottom passage, and the gas in the exhaust tank is supplied. Extruding outside through an exhaust valve.
【0006】本発明のこのような構成により、1台のポ
ンプにて真空脱気装置の処理液の送水と脱気槽内の減圧
維持、多処理が可能となり、維持や維持費、運転費が大
幅に削減され、又長期使用に適応させることが可能にな
る。[0006] With such a configuration of the present invention, it is possible to supply the processing liquid of the vacuum deaerator and maintain the reduced pressure in the deaeration tank and perform multiple treatments with one pump, and the maintenance, maintenance costs, and operation costs are reduced. It is greatly reduced and can be adapted for long-term use.
【0007】[0007]
【実施例】以下、本発明の一実施例を第1,2図の図面
に基づき説明する。1は脱気槽で硬質塩化ビニール、ス
テンレス等から成り自動弁3を介して排気弁8を具備し
た排気槽2に連結され(第2図では上部に排気弁8を具
備した脱気槽1と送水ポンプ5間に自動弁3を介して連
結管3Cによって連結され、連結部と脱気槽1間には自
動弁3A、脱気槽1と排気槽2を繋ぐ自動弁3Bが設け
られる)脱気槽1下部より送水ポンプ5を介して吐出管
6を接続し、送水ポンプ5以降吐出管より連結管7から
自動弁4を介して排気槽2に連結する、10は給水管で
自動弁9を介して脱気槽1に貫通せしめたものから本発
明を実行する脱気装置が構成される。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be described below with reference to FIGS. Reference numeral 1 denotes a deaeration tank which is made of hard vinyl chloride, stainless steel or the like and is connected to an exhaust tank 2 having an exhaust valve 8 via an automatic valve 3 (in FIG. The water supply pump 5 is connected by a connection pipe 3C via an automatic valve 3 via an automatic valve 3, and an automatic valve 3A is provided between the connection portion and the deaeration tank 1, and an automatic valve 3B connecting the deaeration tank 1 and the exhaust tank 2 is provided. A discharge pipe 6 is connected from the lower part of the air tank 1 via a water supply pump 5, and a discharge pipe after the water supply pump 5 is connected from the connection pipe 7 to the exhaust tank 2 via the automatic valve 4. A degassing apparatus for executing the present invention is constructed from the gas that has been passed through the degassing tank 1 through the airbag.
【0008】自動弁9、自動弁3(第2図では自動弁
9、自動弁3、自動弁3B)を開路し、又自動弁4(第
2図では自動弁4、自動弁3A)を閉路し給水管10か
ら液体を補給し脱気槽1内と排気槽2内を液体で満水に
した後、自動弁9を閉路し送水ポンプ5により排気槽2
内の液体を吐出させるのだが、図1では直接には脱気槽
1内の液体を吐出させその吸引力により液体を排気槽2
内より吐出させる。これと同時に脱気槽1内に残ってい
る、もしくは発生した気体類は比重が軽い為に自動弁3
を経て排気槽2内へ上昇する(第2図では直接排気槽2
内より液体を吐出せしめ、排気槽2内を減圧させ脱気槽
1内の気体を強制的に吸引し、脱気槽1内を減圧するも
のである。)脱気槽1内の減圧度が設定減圧度になると
自動弁3(第2図では自動弁3,3B)が閉路し、又自
動弁4(第2図では自動弁4,3Aが開路し、送水ポン
プ5によって吐出される処理水を吐出管6より分岐接続
された連結管7を経て、排気槽2内に補給し水位を上昇
させ排気槽2内に導かれた気体類を排気弁8から排気す
るものである。排気弁8は自動空気抜弁に逆止機構を施
されたもので、液体を通過させず気体のみを排気し、又
内部が不圧の状態では逆止機構により大気を吸い込まな
い仕組みになっているものである。この状態において
は、脱気槽1内で気液分離処理されている液体が吐出さ
れる。又処理中に当たって脱気槽1内の設定減圧度が崩
れた時点に於いて、各自動弁を制御し排気槽2内から液
体を直接、又は脱気槽1を介して間接的に吐出せしめ、
脱気槽1内で発生した気体を排気槽2内に上昇、又は吸
引し脱気槽1内の減圧度を取り戻す。上記作用は脱気槽
1内に具備された真空センサー、水位センサー等で感知
し制御器によって自動弁を自動制御し減圧排気を反復す
ることで、連続処理中において脱気槽1内減圧度を維持
するものであり、つまり脱気槽1内が設定減圧度間の時
は、脱気槽1内で処理された脱気水を吐出供給し、脱気
槽1内が設定減圧度以下になった時点において減圧する
ために要する液体を、排気槽2内に補給された処理水を
吐出供給することで、連続的に一定の濃度の処理水を供
給し、かつ脱気槽1内の減圧度を維持する、真空脱気装
置の減圧排気方法を提供せんとするものである。The automatic valves 9 and 3 (in FIG. 2, the automatic valves 9, 3 and 3B) are opened, and the automatic valves 4 (in FIG. 2 the automatic valves 4 and 3A) are closed. After the liquid is supplied from the water supply pipe 10 and the inside of the deaeration tank 1 and the exhaust tank 2 are filled with the liquid, the automatic valve 9 is closed and the water supply pump 5 closes the exhaust tank 2.
In FIG. 1, the liquid in the deaeration tank 1 is directly discharged and the liquid is discharged by the suction force.
Discharge from inside. At the same time, the gas remaining in the degassing tank 1 or generated gas has a low specific gravity, so the automatic valve 3
Through the exhaust tank 2 (in FIG. 2, the exhaust tank 2
A liquid is discharged from the inside, the inside of the exhaust tank 2 is depressurized, and the gas in the deaeration tank 1 is forcibly sucked, thereby depressurizing the inside of the deaeration tank 1. When the degree of pressure reduction in the deaeration tank 1 reaches the set pressure reduction degree, the automatic valve 3 (the automatic valves 3 and 3B in FIG. 2) closes, and the automatic valve 4 (the automatic valves 4 and 3A in FIG. 2) opens. The treated water discharged by the water supply pump 5 is supplied to the exhaust tank 2 through the connecting pipe 7 branched from the discharge pipe 6 to increase the water level, and the gas introduced into the exhaust tank 2 is exhausted by the exhaust valve 8. The exhaust valve 8 is an automatic air bleed valve provided with a check mechanism to exhaust only gas without allowing liquid to pass therethrough. In this state, the liquid subjected to the gas-liquid separation processing is discharged in the deaeration tank 1. During the processing, the set pressure reduction degree in the deaeration tank 1 is broken. At this point, each automatic valve is controlled to supply liquid directly from the exhaust tank 2 or through the degassing tank 1. Indirectly caused to discharge,
The gas generated in the degassing tank 1 is raised or sucked into the exhaust tank 2 to recover the degree of pressure reduction in the degassing tank 1. The above-described operation is performed by automatically controlling the automatic valve by the controller and repeating the depressurization and exhaustion by detecting with a vacuum sensor, a water level sensor and the like provided in the deaeration tank 1 so that the degree of decompression in the deaeration tank 1 can be reduced during continuous processing. That is, when the inside of the degassing tank 1 is between the set decompression degrees, the deaerated water treated in the deaeration tank 1 is discharged and supplied, and the inside of the degassing tank 1 becomes equal to or less than the set decompression degree. At this point, the processing liquid supplied to the exhaust tank 2 is discharged and supplied with the liquid required to reduce the pressure, thereby continuously supplying the processing water having a constant concentration and the degree of pressure reduction in the degassing tank 1. And a method for depressurizing and exhausting the vacuum deaerator.
【0009】[0009]
【発明の効果】上気したように本発明は通常運転中には
脱気槽で気液分離を行いその処理水を吐出し同時に処理
水を排気槽に補給し導いた気体類を排気せしめ、減圧度
が低下した時点において排気槽に補給された処理水を吐
出させ減圧を維持し連続的に処理水を供給することを、
ポンプを送水ポンプに限定し行なうものである。従って
従来の真空ポンプを使用せずとも設定の減圧度を維持す
ることができ、常に一定濃度の処理液を供給することが
できる。実験では硬質塩化ビニール樹脂の17リットル
の排気槽と50リットルの脱気槽に真空槽を30リット
ル、液体槽を20リットル取り、送水ポンプに単相10
0V,50Hz吸込全揚程−4m,出力0.4KWと各
自動弁に不圧に対応する電磁弁を使用し、脱気装置の給
水・吐出管の径を30Aにしマンションの入水槽に給水
・吐出管を連結し液体を3t/hの流量で循環させたと
ころ、脱気槽減圧度を−740〜−720mmHg間で
維持することを可能としており、脱酸素能力でみると液
温4〜6℃溶存酸素量約12ppmが処理後4ppm前
後と約70%の脱気能力を実測した。又上気したように
主となる動力は液体送水ポンプ1台のみで液体吐出、排
気減圧を可能としているものなので、当初コストや維持
や維持費、運転費が大幅に削減され、寿命性等にも優れ
るものであり、多処理や長期使用に当たって絶大な効果
を果たすものである。As described above, according to the present invention, during normal operation, gas-liquid separation is performed in a deaeration tank, the treated water is discharged, and at the same time, the treated water is supplied to an exhaust tank to exhaust the introduced gases. At the time when the degree of decompression has decreased, discharging the treated water supplied to the exhaust tank and maintaining the reduced pressure to continuously supply the treated water,
The pump is limited to a water supply pump. Therefore, the set degree of reduced pressure can be maintained without using a conventional vacuum pump, and a processing solution having a constant concentration can always be supplied. In the experiment, a 30-liter vacuum tank and a 20-liter liquid tank were placed in a 17-liter exhaust tank and a 50-liter deaeration tank of hard vinyl chloride resin, and a single-phase 10 pump was supplied to the water pump.
0V, 50Hz suction total head -4m, output 0.4KW, using solenoid valves corresponding to non-pressure for each automatic valve, water supply / discharge pipe diameter of deaerator 30A, water supply / discharge to apartment water tank By connecting the pipes and circulating the liquid at a flow rate of 3 t / h, it is possible to maintain the degassing tank depressurization degree between -740 and -720 mmHg, and the liquid temperature is 4-6 ° C in terms of the deoxygenation capacity. The dissolved oxygen amount was about 12 ppm after the treatment, and the degassing ability of about 70% was actually measured. Also, as mentioned above, the main motive power is that only one liquid water pump can discharge and depressurize the liquid, so initial costs, maintenance, maintenance costs, operation costs are greatly reduced, and life is improved. Is also excellent, and has a tremendous effect in multiprocessing and long-term use.
【図1】本発明の実施例である。FIG. 1 is an embodiment of the present invention.
【図2】本発明の実施例である。FIG. 2 is an embodiment of the present invention.
1 脱気槽 2 排気槽 3,3A,3B,4,9 自動弁 5 送水ポンプ 6 吐出管 7,3C 連結管 8 排気弁 10 給水管 DESCRIPTION OF SYMBOLS 1 Deaeration tank 2 Exhaust tank 3, 3A, 3B, 4, 9 Automatic valve 5 Water supply pump 6 Discharge pipe 7, 3C Connecting pipe 8 Exhaust valve 10 Water supply pipe
Claims (2)
けた逆止機構を有する排気弁と、脱気槽に連結した給水
路と、脱気槽の頂部と排気槽の底部を連絡する一方の流
路と、脱気槽の底部を送水ポンプの給水側に連結すると
ともに送水ポンプの排水側より液体を導く排水路と、排
水路の送水ポンプ排出側より分岐し排気槽下部に連絡す
る他方の流路とを有する真空脱気装置の減圧排気方法に
おいて、他方の流路を閉塞し、一方の流路を開いた状態
で送水ポンプにより液体を吐出しつつ脱気層に液体を供
給し脱気槽と排気槽とを液体で満たす工程と、脱気槽内
への新たな液体の供給を停止し、脱気槽内の液体を排水
路を介して送水ポンプにより吐出することにより気液分
離を脱気槽内において行なう工程と、脱気槽内の気体が
所定の減圧度になった際に一方の流路を閉塞し、他方の
流路を開いた状態で脱気槽内の液体を排水路を介して送
水ポンプにより吐出させながら、吐出された液体の一部
を他方の流路を介して排気槽内に供給し排気槽内の気体
を排気弁を通じて外部に押し出す工程とを備えたことを
特徴とする真空脱気装置の減圧排気方法。1. A deaeration tank, an exhaust tank, an exhaust valve having a check mechanism provided on an upper part of the exhaust tank, a water supply passage connected to the deaeration tank, a top of the deaeration tank and a bottom of the exhaust tank. And a drain that connects the bottom of the deaeration tank to the water supply side of the water pump and guides the liquid from the drain side of the water pump. In the vacuum evacuation method of the vacuum deaerator having the other flow path and the other flow path, the other flow path is closed, and while the one flow path is opened, the liquid is discharged to the deaeration layer by the water supply pump. Supplying water and filling the degassing tank and exhaust tank with liquid, stopping the supply of new liquid into the degassing tank, and discharging the liquid in the degassing tank by a water pump through a drainage channel. Performing the gas-liquid separation in the degassing tank, and when the gas in the degassing tank reaches a predetermined pressure reduction degree. When one of the flow paths is closed and the other flow path is opened, a part of the discharged liquid is discharged to the other flow path while discharging the liquid in the deaeration tank by a water supply pump through a drainage path. Supplying the gas into the exhaust tank via a path and pushing the gas in the exhaust tank to the outside through an exhaust valve.
上部にそれぞれ設けた逆止機構を有する排気弁と、脱気
槽に連結した給水路と、脱気槽の上部と排気槽の上部を
連絡する上部流路と、脱気槽の底部を送水ポンプの給水
側に連結するとともに送水ポンプの排水側より液体を導
く排水路と、排水路の送水ポンプ給水側と排気槽の底部
を連絡する第1底部流路と、排水路の送水ポンプ排水側
より分岐し排気槽底部に連絡する第2底部流路とを有す
る真空脱気装置の減圧排気方法において、排水路の送水
ポンプ給水側における脱気槽側流路と第2底部流路を閉
塞し、上部流路を開き、第1底部流路を排水路の送水ポ
ンプ給水側における送水ポンプ側流路を経て送水ポンプ
へと連通させた状態で送水ポンプにより液体を吐出しつ
つ脱気層に液体を供給し脱気槽と排気槽とを液体で満た
す工程と、脱気槽内への新たな液体の供給を停止し、脱
気槽内の液体を上部流路、排気槽、第1底部流路、及び
排水路を介して送水ポンプにより吐出させることによ
り、気液分離を脱気槽内において行なう工程と、脱気槽
内の気体が所定の減圧度になった際に上部流路と第1底
部流路を閉塞し、排水路の送水ポンプ給水側における脱
気槽側流路と第2底部流路を開いた状態で脱気槽内の液
体を排水路を介して送水ポンプにより吐出させながら、
吐出された液体の一部を第2底部流路を介して排気槽内
に供給し排気槽内の気体を排気弁を通じて外部に押し出
す工程とを備えたことを特徴とする真空脱気装置の減圧
排気方法。2. A deaeration tank, an exhaust tank, an exhaust valve having a check mechanism provided on each of the deaeration tank and the exhaust tank, a water supply passage connected to the deaeration tank, and an upper part of the deaeration tank. An upper passage connecting the upper part of the exhaust tank, a drain connecting the bottom of the deaeration tank to the water supply side of the water pump and guiding the liquid from the discharge side of the water pump, a water pump water supply side of the drain and the exhaust tank. A first bottom passage connecting the bottom of the drainage passage, and a second bottom passage branching from the water pump drain side of the drainage passage and communicating with the bottom of the exhaust tank. The deaeration tank side flow path and the second bottom flow path on the pump water supply side are closed, the upper flow path is opened, and the first bottom flow path is connected to the water supply pump via the water supply pump side flow path on the water supply pump water supply side of the drainage passage. While supplying the liquid to the degassing layer while discharging Supplying the deaeration tank and the exhaust tank with a liquid, stopping the supply of new liquid into the deaeration tank, and allowing the liquid in the deaeration tank to flow through the upper flow path, the exhaust tank, and the first bottom flow path And a step of performing gas-liquid separation in the deaeration tank by discharging the water by a water supply pump through a drainage path, and when the gas in the deaeration tank has a predetermined degree of pressure reduction, the upper flow path and the first With the bottom flow path closed and the deaeration tank side flow path on the water supply pump water supply side of the drainage path and the second bottom flow path opened, the liquid in the deaeration tank is discharged by the water supply pump through the drainage path. ,
Depressurizing the vacuum degassing device, comprising: supplying a part of the discharged liquid to the exhaust tank via the second bottom passage, and pushing out the gas in the exhaust tank to the outside through the exhaust valve. Exhaust method.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP11569291A JP3241749B2 (en) | 1991-02-25 | 1991-02-25 | Evacuation method for vacuum deaerator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP11569291A JP3241749B2 (en) | 1991-02-25 | 1991-02-25 | Evacuation method for vacuum deaerator |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH08266810A JPH08266810A (en) | 1996-10-15 |
JP3241749B2 true JP3241749B2 (en) | 2001-12-25 |
Family
ID=14668883
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP11569291A Expired - Lifetime JP3241749B2 (en) | 1991-02-25 | 1991-02-25 | Evacuation method for vacuum deaerator |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP3241749B2 (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR101225278B1 (en) * | 2010-08-30 | 2013-01-22 | 현대제철 주식회사 | Apparatus for reducing dissolved oxygen |
-
1991
- 1991-02-25 JP JP11569291A patent/JP3241749B2/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
JPH08266810A (en) | 1996-10-15 |
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