JPH115002A - Degasifier - Google Patents

Degasifier

Info

Publication number
JPH115002A
JPH115002A JP17761297A JP17761297A JPH115002A JP H115002 A JPH115002 A JP H115002A JP 17761297 A JP17761297 A JP 17761297A JP 17761297 A JP17761297 A JP 17761297A JP H115002 A JPH115002 A JP H115002A
Authority
JP
Japan
Prior art keywords
liquid
degassing
towers
line
degasifying
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.)
Pending
Application number
JP17761297A
Other languages
Japanese (ja)
Inventor
Seiji Tai
誠二 田井
Taizo Matsukawa
泰三 松川
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Miura Co Ltd
Original Assignee
Miura Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Miura Co Ltd filed Critical Miura Co Ltd
Priority to JP17761297A priority Critical patent/JPH115002A/en
Publication of JPH115002A publication Critical patent/JPH115002A/en
Pending legal-status Critical Current

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  • Degasification And Air Bubble Elimination (AREA)

Abstract

PROBLEM TO BE SOLVED: To make the weight of a structural member of degasifying tower light in weight and to save energy by connecting a supply line of a liquid to be degasified, a take-out line of degasified liquid and a vacuum suction line respectively to a plurality of degasifying towers and providing a pump in the take-out line. SOLUTION: The 1st degasifying tower 2 and the 2nd degasifying tower 3 are arranged in parallel under a tank 1 storing the liquid to be degasified and the supply line 4 for supplying the liquid to be degasified, the take-out line 8 provided with the taking out pump 7 for taking out the degasified liquid and the vacuum suction line 11 provided with a vacuum pump 10 are connected to respective degasifying towers 2, 3. In the degasifier so structured, since a plurality of degasifying towers 2, 3 are provided as a means to increase the throughput of the liquid to be degasified, a low strength structural member can be used to make the cost low. And since the plurality of degasifying towers are provided, only the required numbers of the degasifying towers in the plurality of degasifying towers are operated to enable the efficient operation and to save energy when the supply quantity of the liquid to be degasified to the loading side is decreased.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】この発明は、被脱気液に含ま
れている溶存気体を除去する脱気装置に関するものであ
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a deaerator for removing dissolved gas contained in a liquid to be degassed.

【0002】[0002]

【従来の技術】一般に、被脱気液(たとえば、溶剤等)
に含まれている溶存気体を除去する脱気装置として、図
4に示すものが知られている。図4において、被脱気液
を貯留するタンク32と真空脱気を行なう脱気塔33の
上部を被脱気液を供給する供給ライン31で接続し、前
記脱気塔33内を真空脱気する手段として真空ポンプ3
4を設け、この真空ポンプ34と前記脱気塔33の上部
とを真空吸引ライン35で接続している。一方、真空脱
気した脱気液の取出しライン36を前記脱気塔33の下
部に接続し、途中に脱気液の取出し用ポンプ37を設け
ている。
2. Description of the Related Art Generally, a liquid to be degassed (eg, a solvent, etc.)
FIG. 4 shows a known degassing device for removing dissolved gas contained in a gas. In FIG. 4, a tank 32 for storing the degassed liquid and an upper part of a degassing tower 33 for vacuum degassing are connected by a supply line 31 for supplying the degassed liquid, and the inside of the degassing tower 33 is vacuum degassed. Vacuum pump 3
The vacuum pump 34 is connected to the upper part of the degassing tower 33 by a vacuum suction line 35. On the other hand, a line 36 for taking out the degassed liquid that has been degassed under vacuum is connected to the lower part of the degassing tower 33, and a pump 37 for taking out the degassed liquid is provided on the way.

【0003】前記構成の脱気装置においては、被脱気液
の処理量を大きくするためには、脱気塔33内に噴霧す
る被脱気液の表面積と滞留時間を溶存気体が放出される
だけの十分な内容積を有する脱気塔が必要である。した
がって、前記脱気塔33を大型化するためには、その構
成部材を重厚なものとする必要からコスト的にも高くな
る。また、脱気塔33を大型化すると、負荷側の変動
(負荷減少時)に対して対応がむずかしく、省エネルギ
ー上からも問題がある。
In the degassing apparatus having the above-described structure, in order to increase the throughput of the degassed liquid, the dissolved gas is released from the surface area and residence time of the degassed liquid sprayed into the degassing tower 33. A deaeration tower having a sufficient internal volume is required. Therefore, in order to increase the size of the degassing tower 33, it is necessary to make its constituent members heavy, which increases the cost. In addition, when the size of the degassing tower 33 is increased, it is difficult to cope with fluctuations on the load side (when the load is reduced), and there is a problem in terms of energy saving.

【0004】[0004]

【発明が解決しようとする課題】この発明は、前記問題
点に鑑み、脱気塔の構成部材の軽量化と省エネルギー化
ができる脱気装置を提供することを目的とするものであ
る。
SUMMARY OF THE INVENTION In view of the above problems, an object of the present invention is to provide a deaerator capable of reducing the weight of components of a deaerator and saving energy.

【0005】[0005]

【課題を解決するための手段】この発明は、前記課題を
解決するためになされたものであって、請求項1に記載
の発明は、複数の脱気塔に被脱気液の供給ラインと脱気
液の取出しラインをそれぞれ接続し、真空ポンプを備え
た真空吸引ラインを前記各脱気塔にそれぞれ接続すると
ともに、前記取出しラインにポンプを設けたことを特徴
としており、また請求項2に記載の発明は、密閉容器内
に隔壁を設け、この隔壁を介して第一,第二脱気室を形
成し、この各脱気室に被脱気液の供給ラインと脱気液の
取出しラインをそれぞれ接続し、真空ポンプを備えた真
空吸引ラインを前記各脱気室にそれぞれ接続するととも
に、前記取出しラインにポンプを設けたことを特徴とし
ており、さらに請求項3に記載の発明は、前記両脱気室
の気相部および液相部にそれぞれ連通部を設けたことを
特徴としている。
Means for Solving the Problems The present invention has been made to solve the above problems, and the invention according to claim 1 has a plurality of degassing towers having a supply line for a liquid to be degassed. The degassing liquid extraction lines are connected to each other, and a vacuum suction line equipped with a vacuum pump is connected to each of the deaeration towers, and a pump is provided on the extraction line. According to the described invention, a partition is provided in a closed container, first and second deaeration chambers are formed through the partition, and a supply line for a liquid to be degassed and a line for taking out a deaeration liquid are provided in each of the deaeration chambers. And a vacuum suction line equipped with a vacuum pump is connected to each of the deaeration chambers, and a pump is provided in the extraction line. Further, the invention according to claim 3, wherein Gas phase and liquid in both degassing chambers It is characterized in that each provided with communicating portion parts.

【0006】[0006]

【発明の実施の形態】つぎに、この発明の実施の形態に
ついて説明すると、この発明は、複数の脱気塔に被脱気
液の供給ラインと脱気液の取出しラインをそれぞれ接続
し、前記各脱気塔内を真空吸引する真空ポンプを備えた
真空吸引ラインを前記各脱気塔の上部にそれぞれ接続す
るとともに、前記取出しラインに脱気液の取出し用ポン
プを設けた構成の脱気装置において実現される。この発
明の脱気装置は、前記脱気塔を複数設けることにより被
脱気液の処理量の増加に対応することができる。したが
って、従来の大容量の単体型脱気塔に比し、小容量の独
立多塔型としたので、個々の脱気塔の構成部材は低強度
のものでよく、軽量化と低コスト化を実現することがで
きる。また、負荷側への脱気液の供給量が低下した場合
は、前記複数の脱気塔を必要台数のみ稼動させる省エネ
ルギー運転とすることもできる。
DESCRIPTION OF THE PREFERRED EMBODIMENTS Next, an embodiment of the present invention will be described. In the present invention, a supply line for a degassed liquid and a line for taking out a degassed liquid are connected to a plurality of degassing towers, respectively. A deaerator having a configuration in which vacuum suction lines provided with vacuum pumps for vacuum suction in the respective deaeration towers are respectively connected to upper portions of the respective deaeration towers, and a pump for removing a deaeration liquid is provided on the extraction line. It is realized in. The degassing device of the present invention can cope with an increase in the amount of liquid to be degassed by providing a plurality of the degassing towers. Therefore, as compared with the conventional large-capacity single-type degassing tower, it is a small-capacity independent multi-tower type, so the components of each degassing tower may be of low strength, reducing weight and cost. Can be realized. Further, when the supply amount of the deaeration liquid to the load side decreases, the energy saving operation may be performed in which only the required number of the plurality of deaeration towers are operated.

【0007】また、前記実施の形態では、脱気塔を複数
台設けたものについて説明したが、これに代わる実施の
形態について説明すると、所定容量の密閉容器内に隔壁
を設け、この隔壁によって複数の脱気室を形成し、この
各脱気室に被脱気液の供給ラインと脱気液の取出しライ
ンをそれぞれ接続し、前記各脱気室内を真空吸引する真
空ポンプを備えた真空吸引ラインを前記各脱気室の上部
にそれぞれ接続するとともに、前記取出しラインに脱気
液の取出し用ポンプを設けた構成とすることもできる。
この実施の形態で説明した密閉容器内を隔壁で分割し、
複数の脱気室を形成した連結多塔型のものは、前記隔壁
が密閉容器の補強部材となるので、全体としては強度ア
ップとなり、軽量部材で構成することができ、同等の効
果を実現することができる。また、前記隔壁によって仕
切られた各脱気室の気相部および液相部に連通部を設け
た構成とすることもできる。
In the above embodiment, a plurality of degassing towers have been described. However, an alternative embodiment will be described. A partition is provided in an airtight container having a predetermined capacity. A vacuum suction line having a vacuum pump for connecting the supply line of the liquid to be degassed and the line for taking out the degassed liquid to each of the degassing chambers, and vacuuming each of the degassing chambers May be connected to the upper part of each of the degassing chambers, and a pump for taking out degassed liquid may be provided in the takeout line.
The inside of the closed container described in this embodiment is divided by a partition wall,
In the connected multi-tower type in which a plurality of degassing chambers are formed, the partition walls serve as a reinforcing member for the closed vessel, so that the strength is increased as a whole, and a lightweight member can be used, and the same effect is realized. be able to. In addition, it is also possible to adopt a configuration in which a communication part is provided in a gas phase part and a liquid phase part of each deaeration chamber partitioned by the partition.

【0008】[0008]

【実施例】以下、この発明の具体的実施例を図面に基づ
いて詳細に説明する。図1は、この発明の第一実施例を
示すものであって、ここに説明する実施例は、溶剤等に
含まれている溶存気体を除去する脱気装置として説明す
る。図1は、前記脱気装置の構成を概略的に示す説明図
である。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Hereinafter, specific embodiments of the present invention will be described in detail with reference to the drawings. FIG. 1 shows a first embodiment of the present invention. The embodiment described here will be described as a deaerator for removing a dissolved gas contained in a solvent or the like. FIG. 1 is an explanatory view schematically showing a configuration of the deaerator.

【0009】図1において、前記脱気装置の構成は、被
脱気液(この実施例では溶剤)を貯留したタンク1の下
方に第一脱気塔2と第二脱気塔3とを並列に配置し、前
記タンク1から前記第一脱気塔2および前記第二脱気塔
3へそれぞれ被脱気液を供給する供給ライン4を設け、
前記第一脱気塔2に接続した供給ライン4に第一電磁弁
5を設けるとともに、前記第二脱気塔3に接続した供給
ライン4に第二電磁弁6を設けている。また、前記第一
脱気塔2および前記第二脱気塔3の下部から脱気液をそ
れぞれ取り出す取出し用のポンプ7を備えた取出しライ
ン8を設け、前記第一脱気塔2に接続した取出しライン
8に第三電磁弁9を設けている。一方、前記第一脱気塔
2および前記第二脱気塔3内を真空吸引する真空ポンプ
10を備えた真空吸引ライン11を設け、この真空吸引
ライン11を前記第一,第二脱気塔2,3の上部にそれ
ぞれ接続し、前記第一脱気塔2に接続した真空吸引ライ
ン11に第四電磁弁12を設けている。そして、前記ポ
ンプ7,真空ポンプ10および各電磁弁5,6,9,1
2は、それぞれ信号線(図示省略)を介して制御器(図
示省略)に接続している。また、前記第一,第二脱気塔
2,3の被脱気液の入口部には、それぞれノズル13が
装着してある。
In FIG. 1, the structure of the degassing apparatus is such that a first degassing tower 2 and a second degassing tower 3 are arranged in parallel below a tank 1 storing a liquid to be degassed (a solvent in this embodiment). And a supply line 4 for supplying a liquid to be degassed from the tank 1 to the first degassing tower 2 and the second degassing tower 3, respectively.
The supply line 4 connected to the first degassing tower 2 is provided with a first solenoid valve 5, and the supply line 4 connected to the second degassing tower 3 is provided with a second solenoid valve 6. Further, an extraction line 8 having an extraction pump 7 for extracting the degassed liquid from the lower part of the first degassing tower 2 and the second degassing tower 3 was provided and connected to the first degassing tower 2. A third solenoid valve 9 is provided on the extraction line 8. On the other hand, a vacuum suction line 11 provided with a vacuum pump 10 for vacuum-evacuating the inside of the first deaeration tower 2 and the second deaeration tower 3 is provided, and this vacuum suction line 11 is connected to the first and second deaeration towers. A fourth solenoid valve 12 is provided in a vacuum suction line 11 connected to the upper portions of the first and second degassing towers 2 and 3, respectively. Then, the pump 7, the vacuum pump 10, and the respective solenoid valves 5, 6, 9, 1
2 are connected to a controller (not shown) via signal lines (not shown). In addition, nozzles 13 are respectively mounted on the inlets of the liquids to be degassed in the first and second degassing towers 2 and 3.

【0010】前記構成の脱気装置によれば、被脱気液の
処理量を大きくする手段として複数の脱気塔2,3を設
けたので、従来の単体型構造の脱気塔に比し、構成部材
が低強度のものでよく、しかも低コスト化できる。さら
に、被脱気液の供給ライン4にそれぞれ第一,第二電磁
弁5,6を設けるとともに、脱気液の取出しライン8に
第三電磁弁9を設け、さらにまた前記第一脱気塔2に接
続した真空吸引ライン11に第四電磁弁12を設けたの
で、負荷側の都合により脱気液の供給量を減量(たとえ
ば、50%)する場合には、制御器(図示省略)からの
信号に基づいて、前記第一脱気塔2への被脱気液の供給
を停止する。すなわち、前記供給ライン4に設けた第一
電磁弁5を閉じるとともに、前記取出しライン8に設け
た第三電磁弁9を閉じ、つぎに前記真空吸引ライン11
に設けた第四電磁弁12を閉じ、前記第二脱気塔3のみ
を運転する。この際の前記第二脱気塔3への被脱気液の
供給量は、全供給量の50%の供給量となっている。ま
た、前記真空ポンプ10および前記ポンプ7の回転数
は、前記制御器に内蔵したインバータの作用により回転
数を通常回転数から50%減速した省エネルギー運転と
している。
According to the deaeration apparatus having the above-described structure, a plurality of deaeration towers 2 and 3 are provided as means for increasing the throughput of the liquid to be deaerated. In addition, the components may be of low strength, and the cost can be reduced. Further, first and second solenoid valves 5 and 6 are provided on the supply line 4 for the degassed liquid, and a third solenoid valve 9 is provided on the degassing liquid take-out line 8. Since the fourth electromagnetic valve 12 is provided on the vacuum suction line 11 connected to the second unit 2, when the supply amount of the deaerated liquid is reduced (for example, 50%) due to the load side, a controller (not shown) is used. The supply of the liquid to be degassed to the first degassing tower 2 is stopped based on the above signal. That is, the first solenoid valve 5 provided on the supply line 4 is closed, and the third solenoid valve 9 provided on the take-out line 8 is closed.
Is closed, and only the second degassing tower 3 is operated. At this time, the supply amount of the liquid to be degassed to the second degassing tower 3 is 50% of the total supply amount. The rotation speed of the vacuum pump 10 and the pump 7 is set to an energy-saving operation in which the rotation speed is reduced by 50% from the normal rotation speed by the action of an inverter built in the controller.

【0011】つぎに、この発明の第二実施例を図面に基
づいて説明する。この第二実施例は、前記第一実施例で
説明した被脱気液の処理量を大きくする手段として、所
定容量の密閉容器内に隔壁を設け、この隔壁を介して複
数の脱気室を形成したものであるから、前記第一実施例
と共通の部材には同一符号を付し、重複する説明は省略
する。
Next, a second embodiment of the present invention will be described with reference to the drawings. In the second embodiment, a partition is provided in a closed container having a predetermined capacity as a means for increasing the throughput of the liquid to be degassed described in the first embodiment, and a plurality of deaeration chambers are formed through the partition. Since they are formed, the same members as those in the first embodiment are denoted by the same reference numerals, and overlapping description will be omitted.

【0012】図2は、第二実施例の脱気装置の構成を概
略的に示す説明図である。図2において、所定容量の密
閉容器14内に隔壁20を設け、この隔壁20を介して
第一,第二脱気室15,16を形成している。この各脱
気室15,16には、前記第一実施例と同様の被脱気液
の供給ライン4,脱気液の取出ライン8および真空吸引
ライン11が接続されている。この第二実施例において
は、前記隔壁20が前記密閉容器14の補強部材となる
ので、全体としては強度アップとなり、軽量部材で構成
することができる。
FIG. 2 is an explanatory view schematically showing the configuration of the deaerator of the second embodiment. In FIG. 2, a partition 20 is provided in a sealed container 14 having a predetermined capacity, and first and second deaeration chambers 15 and 16 are formed through the partition 20. The degassing chambers 15 and 16 are connected to the supply line 4, the degassing liquid extraction line 8, and the vacuum suction line 11 as in the first embodiment. In the second embodiment, since the partition wall 20 serves as a reinforcing member for the closed container 14, the strength is increased as a whole, and it can be constituted by a lightweight member.

【0013】つぎに、この発明の第三実施例を図面に基
づいて説明する。この第三実施例は、前記第二実施例で
説明した密閉容器14内を隔壁20によって仕切られた
第一,第二脱気室15,16の各気相部17および各液
相部18に連通部19を設けたものであるから、前記連
通部19以外の説明は省略する。
Next, a third embodiment of the present invention will be described with reference to the drawings. In the third embodiment, the gas-phase portions 17 and the liquid-phase portions 18 of the first and second deaeration chambers 15 and 16 partitioned by the partition wall 20 in the closed container 14 described in the second embodiment are provided. Since the communication part 19 is provided, the description other than the communication part 19 is omitted.

【0014】図3において、密閉容器14内に隔壁20
を設け、この隔壁20によって仕切られた第一,第二脱
気室15,16の各液相部18と各気相部17に適宜の
連通部19をそれぞれ設けている。この連通部19は、
前記隔壁20の所定位置に適宜の手段で所定の穴また切
欠部を形成している。この連通部19は、被脱気液中の
溶存気体を除去するときに有効であり、また液相部18
の下部に連通部19を形成しているので脱気液の貯留と
取出しが便利である。
In FIG. 3, a partition 20 is placed in a closed container 14.
The first and second degassing chambers 15 and 16 separated by the partition wall 20 are provided with appropriate communication portions 19 in the respective liquid phase portions 18 and the respective gas phase portions 17. This communication part 19
A predetermined hole or notch is formed at a predetermined position of the partition wall 20 by an appropriate means. The communication portion 19 is effective when removing dissolved gas in the liquid to be degassed, and is connected to the liquid phase portion 18.
Since the communication portion 19 is formed in the lower part of the storage space, storage and removal of the degassed liquid are convenient.

【0015】[0015]

【発明の効果】以上説明したように、この発明によれ
ば、複数の脱気塔に被脱気液の供給ラインと脱気液の取
出しラインをそれぞれ接続し、真空ポンプを備えた真空
吸引ラインを前記各脱気塔にそれぞれ接続するととも
に、前記取出しラインにポンプを設けた構成としたの
で、従来の被脱気液の処理量を大きくするための大容量
で単体型脱気塔方式に比し、前記各脱気塔を構成する構
成部材を低強度の材料とすることができる。したがっ
て、前記各脱気塔の軽量化と低コスト化を図ることがで
きる。また、複数の脱気塔としたので、負荷側への脱気
液の供給量が低下した場合は、複数の脱気塔を必要台数
のみ稼動させる省エネルギー運転とすることもできるの
で効率的である。
As described above, according to the present invention, the supply line for the liquid to be degassed and the line for taking out the deaeration liquid are connected to the plurality of deaeration towers, respectively, and the vacuum suction line provided with the vacuum pump. Is connected to each of the deaeration towers, and a pump is provided in the extraction line.Therefore, compared to the conventional large-capacity single deaeration tower system for increasing the throughput of the liquid to be deaerated. Then, the constituent members constituting each of the degassing towers can be made of low-strength materials. Therefore, the weight and cost of each degassing tower can be reduced. Further, since a plurality of deaeration towers are used, when the supply amount of the deaeration liquid to the load side decreases, the energy saving operation in which only the required number of the plurality of deaeration towers are operated can be performed, which is efficient. .

【図面の簡単な説明】[Brief description of the drawings]

【図1】この発明に係る脱気装置の第一実施例の構成を
概略的に示す説明図である。
FIG. 1 is an explanatory view schematically showing a configuration of a first embodiment of a deaerator according to the present invention.

【図2】この発明に係る脱気装置の第二実施例の構成を
概略的に示す説明図である。
FIG. 2 is an explanatory view schematically showing a configuration of a second embodiment of the deaerator according to the present invention.

【図3】この発明に係る脱気装置の第三実施例の構成を
概略的に示す説明図である。
FIG. 3 is an explanatory view schematically showing a configuration of a third embodiment of a deaerator according to the present invention.

【図4】従来の脱気装置の構成を概略的に示す説明図で
ある。
FIG. 4 is an explanatory view schematically showing a configuration of a conventional deaerator.

【符号の説明】[Explanation of symbols]

2 第一脱気塔 3 第二脱気塔 4 供給ライン 7 ポンプ 8 取出しライン 10 真空ポンプ 11 真空吸引ライン 14 密閉容器 15 第一脱気室 16 第二脱気室 17 気相部 18 液相部 19 連通部 20 隔壁 2 First degassing tower 3 Second degassing tower 4 Supply line 7 Pump 8 Extraction line 10 Vacuum pump 11 Vacuum suction line 14 Closed vessel 15 First degassing chamber 16 Second degassing chamber 17 Gas phase 18 Liquid phase 19 communication part 20 partition

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 複数の脱気塔2,3に被脱気液の供給ラ
イン4と脱気液の取出しライン8をそれぞれ接続し、真
空ポンプ10を備えた真空吸引ライン11を前記各脱気
塔2,3にそれぞれ接続するとともに、前記取出しライ
ン8にポンプ7を設けたことを特徴とする脱気装置。
1. A degassing liquid supply line 4 and a degassing liquid takeout line 8 are connected to a plurality of degassing towers 2 and 3, respectively, and a vacuum suction line 11 equipped with a vacuum pump 10 is connected to each of the degassing towers. A degassing device which is connected to the towers 2 and 3, respectively, and is provided with a pump 7 in the extraction line 8.
【請求項2】 密閉容器14内に隔壁20を設け、この
隔壁20を介して第一,第二脱気室15,16を形成
し、この各脱気室15,16に被脱気液の供給ライン4
と脱気液の取出しライン8をそれぞれ接続し、真空ポン
プ10を備えた真空吸引ライン11を前記各脱気室1
5,16にそれぞれ接続するとともに、前記取出しライ
ン8にポンプ7を設けたことを特徴とする脱気装置。
2. A partition wall 20 is provided in a sealed container 14, and first and second degassing chambers 15 and 16 are formed through the partition wall 20. Supply line 4
And a degassing liquid extraction line 8 are connected to each other, and a vacuum suction line 11 equipped with a vacuum pump 10 is connected to each of the degassing chambers 1.
A degassing device, wherein the degassing device is connected to each of the extraction lines 5 and 16 and a pump 7 is provided in the extraction line 8.
【請求項3】 前記両脱気室15,16の気相部17お
よび液相部18にそれぞれ連通部19を設けたことを特
徴とする請求項2に記載の脱気装置。
3. The degassing device according to claim 2, wherein a communicating portion is provided in each of the gas phase portion and the liquid phase portion of the degassing chambers.
JP17761297A 1997-06-17 1997-06-17 Degasifier Pending JPH115002A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP17761297A JPH115002A (en) 1997-06-17 1997-06-17 Degasifier

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP17761297A JPH115002A (en) 1997-06-17 1997-06-17 Degasifier

Publications (1)

Publication Number Publication Date
JPH115002A true JPH115002A (en) 1999-01-12

Family

ID=16034058

Family Applications (1)

Application Number Title Priority Date Filing Date
JP17761297A Pending JPH115002A (en) 1997-06-17 1997-06-17 Degasifier

Country Status (1)

Country Link
JP (1) JPH115002A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2011136079A1 (en) * 2010-04-28 2011-11-03 株式会社ミマキエンジニアリング Degassing system
JP2015040647A (en) * 2013-08-20 2015-03-02 三浦工業株式会社 Boiler system
JPWO2018100970A1 (en) * 2016-11-29 2019-10-17 田村 稔 Degassing device for removing gaseous components dissolved in liquid

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2011136079A1 (en) * 2010-04-28 2011-11-03 株式会社ミマキエンジニアリング Degassing system
JPWO2011136079A1 (en) * 2010-04-28 2013-07-18 株式会社ミマキエンジニアリング Deaeration system
JP2015040647A (en) * 2013-08-20 2015-03-02 三浦工業株式会社 Boiler system
JPWO2018100970A1 (en) * 2016-11-29 2019-10-17 田村 稔 Degassing device for removing gaseous components dissolved in liquid

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