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JPH11300341A - Distillation device - Google Patents

Distillation device

Info

Publication number
JPH11300341A
JPH11300341A JP11560498A JP11560498A JPH11300341A JP H11300341 A JPH11300341 A JP H11300341A JP 11560498 A JP11560498 A JP 11560498A JP 11560498 A JP11560498 A JP 11560498A JP H11300341 A JPH11300341 A JP H11300341A
Authority
JP
Japan
Prior art keywords
water
treated
storage tank
treated water
boiler
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
Application number
JP11560498A
Other languages
Japanese (ja)
Other versions
JP4034421B2 (en
Inventor
Ichiro Sato
佐藤  一郎
Shinichi Ikeda
真一 池田
Hiroshi Fujita
浩志 藤田
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.)
Yamato Scientific Co Ltd
Original Assignee
Yamato Scientific 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 Yamato Scientific Co Ltd filed Critical Yamato Scientific Co Ltd
Priority to JP11560498A priority Critical patent/JP4034421B2/en
Publication of JPH11300341A publication Critical patent/JPH11300341A/en
Application granted granted Critical
Publication of JP4034421B2 publication Critical patent/JP4034421B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Heat Treatment Of Water, Waste Water Or Sewage (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)
  • Treatment Of Water By Ion Exchange (AREA)

Abstract

PROBLEM TO BE SOLVED: To start a distillating operation quick in starting up by quickly feeding a new treated water till a fixed water level after discharging all water in a tank. SOLUTION: An electrical regenerative continuous ion exchanger 1 connecting a water feeding plug 5 and having a reverse osmotic membrane 13, a treated water storage tank 7 temporarily storing the treated water treated with the electrical regenerative continuous ion exchanger 1, a boiler 33 boiling the treated water sent from the treated water storage tank 7 with a heater 41, a condenser 19 condensing a steam generated at an inside of the boiler 33 by boiling and discharging as a distilled water and a distilled water storage tank 57 temporarily storing the distilled water from the condenser 19 are provided, and the treated water in a fixed water level is always stored in the treated water storage tank 7 so as to rapidly correspond to the boiler 33.

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、蒸溜装置に関す
る。
[0001] The present invention relates to a distillation apparatus.

【0002】[0002]

【従来の技術】一般に、蒸溜装置の概要は、蒸溜工程の
前段において、プレフィルタ、イオン交換樹脂により処
理し、その処理水と、ボイラ内において沸騰させ、その
発生した蒸気を凝縮器で凝縮し、蒸溜水として取出すよ
うになっている。
2. Description of the Related Art In general, a distillation apparatus is generally described as follows. Prior to a distillation step, a pre-filter and an ion-exchange resin are used for the treatment, the treated water is boiled in a boiler, and the generated steam is condensed in a condenser. , And is taken out as distilled water.

【0003】[0003]

【発明が解決しようとする課題】蒸溜工程の前段処理
は、プレフィルタ、イオン交換樹脂により行われるが、
イオン交換樹脂等には寿命があり、常に監視していない
と水質が低下し、必要な純度が確保できなくなる。その
外に、ボイラ内の缶石の付着を助長する等の弊害があっ
た。
The pretreatment of the distillation step is performed by a prefilter and an ion exchange resin.
Ion exchange resins and the like have a lifetime, and if not monitored constantly, the water quality will decrease, and the required purity cannot be ensured. In addition, there were other problems such as promoting adhesion of scales in the boiler.

【0004】そこで、この発明は、メンテナンスを不要
とし、長期に亘り処理水が安定して得られると共に、し
かも、一定水質の処理水の供給が迅速に対応出来るよう
にした蒸溜装置を提供することを目的としている。
Accordingly, the present invention provides a distillation apparatus which does not require maintenance, can obtain treated water stably over a long period of time, and can promptly supply treated water of a constant quality. It is an object.

【0005】[0005]

【課題を解決するための手段】前記目的を達成するため
に、この発明は、給水栓と接続し、逆浸透膜を有する電
気再生式連続イオン交換器と、電気再生式連続イオン交
換器で処理された処理水を一時貯留する処理水貯留タン
クと、処理水貯留タンクから送り出される処理水をヒー
タによって沸騰させるボイラと、ボイラ内で沸騰し発生
した蒸気を凝縮し蒸溜水として取出す凝縮器と、凝縮器
からの蒸溜水を一時貯留する蒸溜水貯留タンクとを備え
ている。
In order to achieve the above object, the present invention relates to an electric regeneration type continuous ion exchanger connected to a water faucet and having a reverse osmosis membrane, and treated with an electric regeneration type continuous ion exchanger. A treated water storage tank for temporarily storing the treated water, a boiler for boiling the treated water sent from the treated water storage tank by a heater, and a condenser for condensing steam generated by boiling in the boiler and extracting the distilled water, A distilled water storage tank for temporarily storing distilled water from the condenser.

【0006】かかる蒸溜装置によれば、電気再生式連続
イオン交換器で処理された処理水は、処理水貯留タンク
内に一時貯留された後、ボイラ内へ供給される。
According to such a distillation apparatus, the treated water treated by the electric regeneration type continuous ion exchanger is temporarily stored in the treated water storage tank and then supplied to the boiler.

【0007】ボイラ内に送り込まれた処理水はヒータに
より沸騰し、発生した蒸気は凝縮器により凝縮され、蒸
溜水貯留タンク内へ一時貯留された後、必要に応じて取
出される。
[0007] The treated water sent into the boiler is boiled by a heater, and the generated steam is condensed by a condenser, temporarily stored in a distilled water storage tank, and then taken out as needed.

【0008】この場合、ボイラ内の処理水は、水質を一
定に保つために定期的に全部排水される。排水完了後、
貯留された処理水貯留タンクからタンク内へ処理水を一
定水位まで供給する。これにより、タンク内への処理水
の迅速な対応が可能となり、立上りの早い蒸溜運転が行
える。
In this case, all the treated water in the boiler is periodically drained in order to keep the water quality constant. After drainage is completed,
The treated water is supplied from the stored treated water storage tank to the tank to a certain level. As a result, prompt treatment of the treated water into the tank becomes possible, and a distillation operation with a quick rise can be performed.

【0009】また、この発明にあっては、凝縮器冷却用
の冷却水の節約を図るために、電気再生式連続イオン交
換器で不純物を含む水を外部に排除するための排水を、
凝縮器冷却用の補助冷却水として使用する。
Further, in the present invention, in order to save the cooling water for cooling the condenser, the waste water for removing the water containing impurities to the outside by the electric regeneration type continuous ion exchanger is provided.
Used as auxiliary cooling water for cooling the condenser.

【0010】[0010]

【発明の実施の形態】以下、図1の図面を参照しながら
この発明の実施形態について具体的に説明する。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be specifically described below with reference to the drawing of FIG.

【0011】図1において、1は電気再生式連続イオン
交換器を示しており、取入口3は給水栓5と、取出口7
は処理水貯留タンク7とそれぞれ連通している。電気再
生式連続イオン交換器1は、前処理フィルタ9とポンプ
11と逆浸透膜13とイオン交換膜15及び少量のイオ
ン交換樹脂17より構成されている。
In FIG. 1, reference numeral 1 denotes an electric regeneration type continuous ion exchanger, and an inlet 3 has a water tap 5 and an outlet 7.
Are in communication with the treated water storage tank 7, respectively. The electric regeneration type continuous ion exchanger 1 includes a pretreatment filter 9, a pump 11, a reverse osmosis membrane 13, an ion exchange membrane 15, and a small amount of ion exchange resin 17.

【0012】前処理フィルタ9は、給水栓5から供給さ
れる水道水の残留塩素等を除去するよう機能する。
The pretreatment filter 9 functions to remove residual chlorine and the like from tap water supplied from the water tap 5.

【0013】ポンプ11は一定の水圧として逆浸透膜1
3へ送り込むよう機能する。
The pump 11 operates at a constant water pressure so that the reverse osmosis membrane 1
Function to send to 3.

【0014】逆浸透膜13は、圧力が加えられた濃厚液
側から希薄液側へ流れを変えることで、サブミクロンオ
ーダーの微生物、有機物及び無機イオンを90〜99%
除去する。半透膜には、ポリアミド系や酢酸セルロース
系等が使用され、水分子あるいはそれ以下の分子レベル
の物質を通過させる。原水は、すべて処理水として採取
できない。逆浸透膜13により取除かれた不純物は膜面
より流し、排水しないと原水側の濃度が上昇し、回収効
率が低下するからである。また、スケールができやすい
状態となり、逆浸透膜13の寿命を低下させる。なお、
排水量を多くするとスケールはできにくくなるが、回収
率が低下するため回収率は実測値で約40%程度とな
る。
The reverse osmosis membrane 13 changes the flow from the concentrated solution to which the pressure is applied from the concentrated solution to the dilute solution to reduce the submicron-order microorganisms, organic substances and inorganic ions by 90 to 99%.
Remove. For the semipermeable membrane, a polyamide system, a cellulose acetate system, or the like is used to allow water molecules or lower molecular substances to pass therethrough. All raw water cannot be collected as treated water. This is because the impurities removed by the reverse osmosis membrane 13 flow from the membrane surface, and if not drained, the concentration on the raw water side increases and the recovery efficiency decreases. Further, the scale is easily formed, and the life of the reverse osmosis membrane 13 is reduced. In addition,
Increasing the amount of drainage makes it difficult to scale, but the recovery rate decreases, so the recovery rate is about 40% as a measured value.

【0015】不純物を膜面より流す排水は、後述する凝
縮器19の冷却用補助冷却水として使用される。
The waste water from which impurities flow from the membrane surface is used as auxiliary cooling water for cooling the condenser 19 described later.

【0016】イオン交換膜15は電気的に連続して処理
し、イオン交換樹脂17とで無機イオンの除去を行うも
ので、メンテナンスが不要であり、回収率は実測値で約
60%程度となる。
The ion-exchange membrane 15 is electrically treated continuously to remove inorganic ions with the ion-exchange resin 17, requiring no maintenance, and the recovery rate is about 60% as a measured value. .

【0017】処理水貯留タンク7は、電気再生式連続イ
オン交換器1で処理された処理水を一時貯留しておくた
めのもので、エアーフィルタ21及び水抜き用の排水バ
ルブ23並びにオーバーフローさせることで常に一定の
水質を確保するオーバーフロー口25の外に、水位低下
検出フロートスイット27と蒸溜開始出力フロートスイ
ッチ29と水位異常検知フロートスイッチ31がそれぞ
れ設けられている。
The treated water storage tank 7 is for temporarily storing treated water treated by the electric regeneration type continuous ion exchanger 1. The treated water storage tank 7 has an air filter 21 and a drain valve 23 for draining water and overflows. In addition to the overflow port 25 for always ensuring a constant water quality, a water level drop detection float switch 27, a distillation start output float switch 29, and a water level abnormality detection float switch 31 are provided respectively.

【0018】水位低下検出フロートスイッチ27は、タ
ンク内の水位が異常に低下したことを検知し、その検知
信号により蒸溜運転を停止させる。
The water level drop detection float switch 27 detects that the water level in the tank has dropped abnormally, and stops the distillation operation based on the detection signal.

【0019】蒸溜開始出力フロートスイッチ29は、タ
ンク内が一定水位に達したことを検知し、その検知信号
によりボイラ33内へ給水するボイラ給水用電磁弁35
を開とする。
The distilling start output float switch 29 detects that the inside of the tank has reached a certain water level, and a boiler water supply solenoid valve 35 for supplying water into the boiler 33 based on the detection signal.
Open.

【0020】水位異常検知フロートスイッチ31は、オ
ーバーフロー口25を越えて上昇する異常液面を検知
し、その検知信号により電気再生式連続イオン交換器1
の運転を停止させる。
The water level abnormality detection float switch 31 detects an abnormal liquid level rising above the overflow port 25 and, based on the detection signal, detects the electric regeneration type continuous ion exchanger 1.
Stop the operation of.

【0021】ボイラ33は、フロート筒35の液面と常
に同一となるよう連通管37を介して連通しており、検
知センサ39を内蔵したセラミックヒータ41が複数本
取付けられている。
The boiler 33 communicates via a communication pipe 37 so as to be always at the same level as the liquid level of the float cylinder 35, and a plurality of ceramic heaters 41 having a built-in detection sensor 39 are attached.

【0022】フロート筒35には、ボイラ33内の水位
を規定の液面に維持するよう検知するボイラ水位制御用
フロートスイッチ43の外に、ヒータ制御用のフロート
スイッチ45とボイラ過熱検知用のフロートスイッチ4
7がそれぞれ設けられている。
The float cylinder 35 has a boiler water level control float switch 43 for detecting the water level in the boiler 33 at a specified liquid level, a heater control float switch 45 and a boiler overheat detection float. Switch 4
7 are provided.

【0023】ボイラ水位制御用のフロートスイッチ43
は、所定の液面になったことを検知すると、その検知信
号によってセラミックヒータ41をオンとするように機
能し、蒸溜運転に入るようになっている。
Float switch 43 for controlling boiler water level
Functions to turn on the ceramic heater 41 according to the detection signal when it detects that the liquid level has reached a predetermined level, so that the distillation operation is started.

【0024】ヒータ制御用のフロートスイッチ45は、
規定された水位より液面が下がり液面より露出すると、
その検知信号に基づきセラミックヒータ41をオフとす
るよう機能し、セラミックヒータ41の過度の加熱状態
となるのを防ぐようになる。
The float switch 45 for controlling the heater is
When the liquid level falls below the specified water level and is exposed from the liquid level,
The ceramic heater 41 functions to be turned off based on the detection signal, thereby preventing the ceramic heater 41 from being excessively heated.

【0025】ボイラ過熱検知用のフロートスイッチ47
は、ボイラ33内の圧力が、何等かの原因で異常に高ま
りフロート筒35内の液面を押上げてフロートスイッチ
47に接触すると、その検知信号に基づきセラミックヒ
ータ41をオフとするよう機能する。
Float switch 47 for detecting overheating of boiler
When the pressure in the boiler 33 rises abnormally for some reason and pushes up the liquid surface in the float cylinder 35 and comes into contact with the float switch 47, the ceramic heater 41 is turned off based on the detection signal. .

【0026】検知センサ39は、セラミックヒータ41
内に組込まれており、セラミックヒータ41のヒータ温
度情報としてヒータ温度を検知し、セラミックヒータ4
1を一定の温度に制御管理する。
The detection sensor 39 includes a ceramic heater 41
The heater temperature is detected as heater temperature information of the ceramic heater 41, and the ceramic heater 4
1 is controlled and managed at a constant temperature.

【0027】凝縮器19は、前記ボイラ33と接続し、
冷却水用電磁弁49を介して送り込まれる冷却水によっ
て蒸気を凝縮し蒸溜水とする主冷却管51と、前記電気
再生式イオン交換器1からの排水によって蒸気を凝縮し
蒸溜水とする補助冷却管53とを有し、主冷却管51及
び補助冷却管53を通った水は、排水管55から外部へ
排水されるようになっている。一方、凝縮器19で蒸溜
された蒸溜水は、蒸溜水貯留タンク57へ送り込まれる
ようになっている。
The condenser 19 is connected to the boiler 33,
A main cooling pipe 51 that condenses steam by using cooling water sent through a cooling water solenoid valve 49 to form distilled water, and an auxiliary cooling that condenses steam by using drainage from the electric regeneration type ion exchanger 1 to produce distilled water. A pipe 53 is provided, and water that has passed through the main cooling pipe 51 and the auxiliary cooling pipe 53 is drained to the outside from a drain pipe 55. On the other hand, the distilled water distilled in the condenser 19 is sent to the distilled water storage tank 57.

【0028】排水管55には、排水温度を検知する温度
検知センサ59が設けられ、温度検知センサ59からの
検知信号は、制御部61へ入力される。
The drain pipe 55 is provided with a temperature detection sensor 59 for detecting a drain temperature, and a detection signal from the temperature detection sensor 59 is input to the control unit 61.

【0029】制御部61は、電気再生式連続イオン交換
器1のオン・オフ制御を行う外に、前記温度検知センサ
59からの温度情報に基づき冷却水用電磁弁49の開閉
制御を行う。
The control unit 61 controls the opening and closing of the cooling water solenoid valve 49 based on the temperature information from the temperature detection sensor 59 in addition to the on / off control of the electric regeneration type continuous ion exchanger 1.

【0030】ここでは、排水温度が約45℃を基準とし
て、以下の場合は、冷却用電磁弁49を閉として主冷却
管51に流れる冷却水の節水を図る一方、以上になると
冷却水用電磁弁49を開として主冷却管51に冷却水を
流すことで、凝縮器19冷却用の冷却水となる一方、排
水温度を低下させ、排水設備の配管耐熱温度を下げて、
配管のダメージを少なくするようになっている。
Here, based on the drainage temperature of about 45 ° C., in the following cases, the cooling electromagnetic valve 49 is closed to save the cooling water flowing through the main cooling pipe 51. By opening the valve 49 and allowing the cooling water to flow through the main cooling pipe 51, the cooling water for cooling the condenser 19 is obtained.
Piping damage is reduced.

【0031】蒸溜水貯留タンク57は、内部に複数の水
位検知スイッチS1〜S5が設けられ、蒸溜水貯留タン
ク57内の蒸溜水は、ポンプ61を駆動することで採取
口63から取出せるようになっている。
A plurality of water level detection switches S1 to S5 are provided in the distilled water storage tank 57, and the distilled water in the distilled water storage tank 57 can be taken out from the sampling port 63 by driving the pump 61. Has become.

【0032】水位検知スイッチS1〜S5は、上下方向
に沿って配置されている。最上位の水位検知S1はオン
になることで蒸溜水貯留タンク57内が満水になったこ
とを検知するスイッチとなっていて、その検知信号に基
づきセラミックヒータ41をオフとして蒸溜運転を停止
する。最下位の水位検知スイッチS5は、オンになるこ
とで、蒸溜水が残り少ないことを検知するスイッチとな
っていて、このスイッチ信号が働いている時に、蒸溜水
取出し用のポンプ61を操作しても駆動しないようにな
っている。
The water level detection switches S1 to S5 are arranged vertically. The uppermost water level detection S1 is a switch for detecting that the inside of the distilled water storage tank 57 is full by turning on, and based on the detection signal, the ceramic heater 41 is turned off to stop the distillation operation. The lowest water level detection switch S5 is a switch for detecting that the amount of distilled water is low when it is turned on. When the switch signal is activated, even if the pump 61 for extracting distilled water is operated. It is not driven.

【0033】なお、65は二次凝縮器、67はポンプ6
9の駆動によって処理水を処理水貯留タンク7から取出
す取出口となっている。
Incidentally, 65 is a secondary condenser, 67 is a pump 6
9 is an outlet for taking out treated water from the treated water storage tank 7 by driving the 9.

【0034】このように構成された蒸溜装置によれば、
電気再生式連続イオン交換器1のオンにより、処理水は
処理水貯留タンク内に貯留され、蒸溜開始出力フロート
スイッチ29のオンによって給水用電磁弁35は開とな
る。これにより、ボイラ33内は所定の水位が確保され
ると共に、フロート筒35内のボイラ水位制御用フロー
トスイッチ43によりオンとなるセラミックヒータ41
によって蒸溜運転に入る。この時、セラミックヒータ4
1は、検知センサ39によりヒータ温度が監視される。
同時に、ボイラ33内の水は、セラミックヒータ41に
よって加熱され、発生した蒸気は凝縮器19において補
助冷却管53を流れる冷却水によって凝縮され蒸溜水と
なる。この時、温度検知センサ59によって管理される
冷却水用電磁弁49は閉のため、主冷却管51には給水
栓5からの冷却水は流れず、節水が図れる。
According to the distillation apparatus configured as described above,
When the electric regeneration type continuous ion exchanger 1 is turned on, the treated water is stored in the treated water storage tank, and when the distillation start output float switch 29 is turned on, the water supply solenoid valve 35 is opened. As a result, a predetermined water level is secured in the boiler 33 and the ceramic heater 41 turned on by the boiler water level control float switch 43 in the float cylinder 35.
Starts the distillation operation. At this time, the ceramic heater 4
In 1, the heater temperature is monitored by the detection sensor 39.
At the same time, the water in the boiler 33 is heated by the ceramic heater 41, and the generated steam is condensed by the cooling water flowing through the auxiliary cooling pipe 53 in the condenser 19 to become distilled water. At this time, the cooling water solenoid valve 49 managed by the temperature detection sensor 59 is closed, so that the cooling water from the water tap 5 does not flow through the main cooling pipe 51, thereby saving water.

【0035】一方、排水管55を流れる排水温度が所定
温度を越えると、冷却水用電磁弁49は開となり、主冷
却管51に冷却水が流れる。これにより、主冷却管51
と補助冷却管53を流れる冷却水によって蒸気の凝縮が
行なわれると同時に、排水温度を下げる。凝縮器19で
凝縮された蒸溜水は蒸溜水貯留タンク57内へ送り込ま
れた後、必要に応じて採取口63から取出される。
On the other hand, when the temperature of the drain water flowing through the drain pipe 55 exceeds a predetermined temperature, the cooling water solenoid valve 49 is opened, and the cooling water flows through the main cooling pipe 51. Thereby, the main cooling pipe 51
The steam is condensed by the cooling water flowing through the auxiliary cooling pipe 53 and at the same time, the drainage temperature is lowered. The distilled water condensed in the condenser 19 is sent into the distilled water storage tank 57, and then is taken out from the sampling port 63 as needed.

【0036】次に、タンク33内の水質を一定を保つた
めに、一定時間ごとに内部の処理水は全部排水するよう
になるが、排水完了後、処理水貯留タンク7内の処理水
をボイラ33内へ供給する。この結果迅速に一定の水位
まで供給が可能になると共に、立上りの早い蒸溜運転が
行えるようになる。
Next, in order to keep the water quality in the tank 33 constant, all of the internal treated water is drained at regular intervals, but after the drainage is completed, the treated water in the treated water storage tank 7 is removed from the boiler. 33. As a result, it is possible to quickly supply water to a certain water level, and to perform a distillation operation with a fast rise.

【0037】[0037]

【発明の効果】以上、説明したように、この発明の蒸溜
装置によれば、水質を一定に保つために一定時間ごとに
タンク内の水を全部抜いた後、新たな処理水を一定の水
位まで迅速に供給することができる。この結果、立上り
の早い蒸溜運転が行えるようになる。
As described above, according to the distilling apparatus of the present invention, in order to keep the water quality constant, after all the water in the tank is drained at regular time intervals, fresh treated water is kept at a constant water level. Can be supplied quickly. As a result, a distillation operation with a fast rise can be performed.

【0038】また、電気再生式連続イオン交換器を通過
した排水を、凝縮器冷却用の冷却水として使用できるた
め、主冷却管を流れる冷却水の節水を図ることができ
る。
Further, since the waste water that has passed through the electric regeneration type continuous ion exchanger can be used as cooling water for cooling the condenser, it is possible to save water flowing through the main cooling pipe.

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

【図1】この発明にかかる蒸溜装置全体の配管系統図。FIG. 1 is a piping diagram of the entire distillation apparatus according to the present invention.

【符号の説明】[Explanation of symbols]

1 電気再生式イオン交換器 5 給水栓 7 処理水貯留タンク 13 逆浸透膜 19 凝縮器 33 ボイラ 57 蒸溜水貯留タンク DESCRIPTION OF SYMBOLS 1 Electric regeneration type ion exchanger 5 Water tap 7 Treated water storage tank 13 Reverse osmosis membrane 19 Condenser 33 Boiler 57 Distilled water storage tank

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 給水栓と接続し、逆浸透膜を有する電気
再生式連続イオン交換器と、電気再生式連続イオン交換
器で処理された処理水を一時貯留する処理水貯留タンク
と、処理水貯留タンクから送り出される処理水をヒータ
によって沸騰させるボイラと、ボイラ内で沸騰し発生し
た蒸気を凝縮し蒸溜水として取出す凝縮器と、凝縮器か
らの蒸溜水を一時貯留する蒸溜水貯留タンクとを備えて
いることを特徴とする蒸溜装置。
1. An electric regeneration continuous ion exchanger connected to a water tap and having a reverse osmosis membrane, a treated water storage tank for temporarily storing treated water treated by the electric regeneration continuous ion exchanger, and a treated water A boiler in which the treated water sent from the storage tank is boiled by a heater, a condenser that condenses steam generated by boiling in the boiler and extracts the distilled water, and a distilled water storage tank that temporarily stores distilled water from the condenser. A distillation apparatus, comprising:
【請求項2】 電気再生式連続イオン交換器で不純物を
含む水を外部に排除するための排水を、凝縮器冷却用の
補助冷却水として使用することを特徴とする請求項1記
載の蒸溜装置。
2. The distilling apparatus according to claim 1, wherein waste water for removing water containing impurities to the outside by the electric regeneration type continuous ion exchanger is used as auxiliary cooling water for cooling the condenser. .
JP11560498A 1998-04-24 1998-04-24 Distillation equipment Expired - Fee Related JP4034421B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11560498A JP4034421B2 (en) 1998-04-24 1998-04-24 Distillation equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11560498A JP4034421B2 (en) 1998-04-24 1998-04-24 Distillation equipment

Publications (2)

Publication Number Publication Date
JPH11300341A true JPH11300341A (en) 1999-11-02
JP4034421B2 JP4034421B2 (en) 2008-01-16

Family

ID=14666754

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11560498A Expired - Fee Related JP4034421B2 (en) 1998-04-24 1998-04-24 Distillation equipment

Country Status (1)

Country Link
JP (1) JP4034421B2 (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20020085686A (en) * 2001-05-09 2002-11-16 주식회사 라우 Water cooling distiller having high thermal energy efficiency
KR100419342B1 (en) * 2002-01-02 2004-02-21 최종훈 The utilization waste water of membrane filt water purifing system
US7066452B2 (en) 2002-10-11 2006-06-27 Honeywell International Inc. Humidifier with reverse osmosis filter
US9822990B2 (en) 2013-07-19 2017-11-21 Honeywell International Inc. Methods, systems, and devices for humidifying
US10900680B2 (en) 2013-07-19 2021-01-26 Ademco Inc. Humidifier system
US11085656B2 (en) 2017-02-24 2021-08-10 Ademco Inc. Configurable electrode humidifier allowing for various injects

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20020085686A (en) * 2001-05-09 2002-11-16 주식회사 라우 Water cooling distiller having high thermal energy efficiency
KR100419342B1 (en) * 2002-01-02 2004-02-21 최종훈 The utilization waste water of membrane filt water purifing system
US7066452B2 (en) 2002-10-11 2006-06-27 Honeywell International Inc. Humidifier with reverse osmosis filter
US9822990B2 (en) 2013-07-19 2017-11-21 Honeywell International Inc. Methods, systems, and devices for humidifying
US10808957B2 (en) 2013-07-19 2020-10-20 Ademco Inc. Methods, systems, and devices for humidifying
US10900680B2 (en) 2013-07-19 2021-01-26 Ademco Inc. Humidifier system
US11639801B2 (en) 2013-07-19 2023-05-02 Ademco Inc. Methods, systems, and devices for humidifying
US11085656B2 (en) 2017-02-24 2021-08-10 Ademco Inc. Configurable electrode humidifier allowing for various injects

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