JPS6261692A - Method for treating hot washing water in soldering line - Google Patents
Method for treating hot washing water in soldering lineInfo
- Publication number
- JPS6261692A JPS6261692A JP20274785A JP20274785A JPS6261692A JP S6261692 A JPS6261692 A JP S6261692A JP 20274785 A JP20274785 A JP 20274785A JP 20274785 A JP20274785 A JP 20274785A JP S6261692 A JPS6261692 A JP S6261692A
- Authority
- JP
- Japan
- Prior art keywords
- hot water
- water
- tank
- reverse osmosis
- cleaning
- 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
Links
Abstract
Description
【発明の詳細な説明】
(産業上の利用分野)
本発明は、はんだ付けラインで使用される洗浄用温水の
処理方法に関するものである。DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) The present invention relates to a method for treating hot water for cleaning used in a soldering line.
従来、フラクサ、プリヒータ、はんだ槽および温水洗浄
槽に沿って移動する搬送体により被はんだ付け物を搬送
しながらはんだ付けするはんだ付けラインにおいて、前
記温水洗浄槽で使用された温水は、その全部につき凝集
沈澱、生物処理等の排水処理を行っている。Conventionally, in a soldering line where objects to be soldered are soldered while being conveyed by a conveyor that moves along a fluxer, a preheater, a soldering bath, and a hot water cleaning bath, all of the hot water used in the hot water cleaning bath is We carry out wastewater treatment such as coagulation sedimentation and biological treatment.
したがって、従来は、使用汎みの温水の排水口が多く、
排水処理IIA設が大形化したり、温水の熱量が無駄に
外部に放出されていて、熱エネルギの損失が多い。Therefore, in the past, there were many hot water drains for general use.
Wastewater treatment IIA facilities are becoming larger, and the heat of hot water is being wasted outside, resulting in a large loss of thermal energy.
本発明の目的は、はんだ付けラインの渇水洗浄槽で使用
された温水の大部分を回収して再使用できるように工夫
することにより、排水量を減らし、熱エネルギの有効利
用を図ることにある。An object of the present invention is to reduce the amount of water discharged and make effective use of thermal energy by recovering and reusing most of the hot water used in the drought cleaning tank of the soldering line.
本発明は、フラクサ11、ブリヒータ12、はんだ槽1
3および温水洗浄槽14に沿って移動する搬送体15に
より被はんだ付け物を搬送しながらはんだ付けするはん
だ付けラインにおいて、このはんだ付けラインの始動時
は温水ヒータ49により冷水を加熱して温水にし、前記
プリヒータ12およびはんだ槽13により加熱され前記
温水洗浄槽14上に位置する前記搬送体15および被は
んだ付け物に前記温水を供給して洗浄し、この洗浄後の
温水をできるだけ温度低下させることなく比較的高温に
耐えられる逆浸透膜27.28に供給し、この逆浸透膜
により前記温水を比較的受石の濃縮水と比較的多盪の純
水とに分離し、濃縮水は排水処理し、純水は比較的高温
のまま前記温水ヒータ49を経て前記温水洗浄槽14上
の搬送体15等に循環するはんだ付けラインにおける洗
浄用温水処理方法である。The present invention includes a fluxer 11, a pre-heater 12, and a solder bath 1.
3 and a soldering line in which objects to be soldered are soldered while being conveyed by a conveyor 15 that moves along a hot water cleaning tank 14. When starting this soldering line, cold water is heated by a hot water heater 49 to turn it into hot water. , supplying the warm water to the carrier 15 and the objects to be soldered which are heated by the preheater 12 and the soldering bath 13 and located on the hot water cleaning bath 14 for cleaning, and lowering the temperature of the hot water after cleaning as much as possible. The hot water is supplied to reverse osmosis membranes 27 and 28, which can withstand relatively high temperatures, and this reverse osmosis membrane separates the hot water into relatively concentrated water and relatively highly purified water, and the concentrated water is sent to wastewater treatment. However, in this hot water treatment method for cleaning in a soldering line, pure water is circulated at a relatively high temperature through the hot water heater 49 to the carrier 15 on the hot water cleaning tank 14, etc.
〔作用〕
本発明は、はんだ付けラインの始動時は、温水ヒータ4
9により冷水を加熱して温水にし、この温水を、ブリヒ
ータ12およびはんだ槽13により加熱され温水洗浄槽
14上に位置する搬送体15および被はんだ付け物に供
給して、これらを洗浄する。[Function] In the present invention, when starting the soldering line, the hot water heater 4
9 heats the cold water to make it hot water, and this hot water is supplied to the carrier 15 and the objects to be soldered which are heated by the pre-heater 12 and the solder bath 13 and are located on the hot water cleaning bath 14 to clean them.
この洗浄優の温水は、できるだけ温度低下させることな
く比較的高温に耐えられる逆浸透g 27゜28に供給
し、この逆浸透膜により、前記温水を比較的少量の濃縮
水と、比較的多量の純水とに分離する。This hot water for cleaning is supplied to a reverse osmosis membrane that can withstand relatively high temperatures without reducing the temperature as much as possible, and this reverse osmosis membrane converts the hot water into a relatively small amount of concentrated water and a relatively large amount of concentrated water. Separate into pure water.
そして、濃縮水は排水処理し、純水は、比較的高−のま
ま前記温水ヒータ49を経て前記温水洗浄槽14上の搬
送体15等に循環し、再使用する。したがって、節水に
なるとともに、排水量が少ないから、大形の排水処理施
設を必要としない。Then, the concentrated water is treated as wastewater, and the pure water, which remains at a relatively high temperature, is circulated through the hot water heater 49 to the carrier 15 on the hot water cleaning tank 14, etc., and is reused. Therefore, it saves water and since the amount of wastewater is small, there is no need for large-scale wastewater treatment facilities.
前記温水ヒータ49は、はんだ付けラインの始動時に、
冷水の温度立上がり用ヒータとして使用し、その後は、
はんだ付けラインで加熱された搬送体15等に接触して
高温状態で循環される温水の温度制御に使用する。した
がって、この温水ヒータ49は、エネルギの消費が少な
い。The hot water heater 49 is used when starting the soldering line.
Used as a heater to raise the temperature of cold water, and then
It is used to control the temperature of hot water that is circulated at high temperature in contact with the heated carrier 15 etc. in the soldering line. Therefore, this hot water heater 49 consumes less energy.
以下、本発明を図面に示す実施例を参照して詳細に説明
する。Hereinafter, the present invention will be explained in detail with reference to embodiments shown in the drawings.
第1図に示すように、発泡式フラクサ11、プリヒータ
12、はんだ槽13および温水洗浄槽14に沿って移動
する搬送体くキャリヤまたはホルダ)15により被はん
だ付け物(例えばプリント配線基板)を搬送しながらは
んだ付けするはんだ付けラインがある。As shown in FIG. 1, objects to be soldered (for example, printed wiring boards) are conveyed by a carrier (carrier or holder) 15 that moves along a foam fluxer 11, a preheater 12, a solder bath 13, and a hot water cleaning bath 14. There is a soldering line where you solder while doing so.
前記温水洗浄槽14から使用済み温水の流動経路に沿っ
て、水素イオンa1度(以下PHという)の調整を行う
PH調整槽21、ポンプ用貯1t?22、濾過ポンプ2
3、第1および第2の濾過機24.25、逆浸透圧用ポ
ンプ26、第1および第2の逆浸透膜27゜28を順次
設ける。Along the flow path of the used hot water from the hot water washing tank 14, there is a PH adjustment tank 21 for adjusting the hydrogen ion a1 degree (hereinafter referred to as PH), and a 1 ton storage tank for the pump. 22, filtration pump 2
3. First and second filters 24, 25, reverse osmosis pressure pump 26, and first and second reverse osmosis membranes 27 and 28 are provided in this order.
さらに、前記逆浸透1127.28から濃縮水の排水管
路31と、純水の循環管路32とを分岐する。前記濃縮
水の排水管路31には、ソレノイド弁33および流a計
34を設け、さらに、この排水管路31から分岐した管
路35にソレノイド弁3Gと流量計37とを並列に設け
、そして、この管路35を前記PH調整槽21に戻す。Further, the reverse osmosis 1127.28 is branched into a concentrated water drainage pipe 31 and a pure water circulation pipe 32. A solenoid valve 33 and a flow meter 34 are provided in the concentrated water drain line 31, and a solenoid valve 3G and a flow meter 37 are provided in parallel in a line 35 branched from the drain line 31, and , this pipe line 35 is returned to the PH adjustment tank 21 .
また、前記純水の循環管路32にソレノイド弁41およ
び流量計42を設け、さらに、この循環管路32から分
岐した管路43にソレノイド弁44を設け、そして、こ
の管路43を前記P H調整槽21に戻す。Further, a solenoid valve 41 and a flow meter 42 are provided in the pure water circulation line 32, and a solenoid valve 44 is further provided in a line 43 branched from this circulation line 32, and this line 43 is connected to the Return to H adjustment tank 21.
前記循環管路32の先端部は、温水槽45上に間放し、
さらに、処理槽46、循環ポンプ47およびソレノイド
弁48を経て前記温水洗浄槽14上に開放する。The tip of the circulation pipe 32 is left above the hot water tank 45,
Furthermore, it is opened onto the hot water cleaning tank 14 via a processing tank 46, a circulation pump 47, and a solenoid valve 48.
前記温水槽45の内部には温水ヒータ49を設け、はん
だ付けラインの始動時は、この温水ヒータ49がら十分
な熱エネルギを放出して冷水を急激に温度上昇させ、所
定温度の温水を得るようにするとともに、はんだ付け運
転中は、この温水ヒータ49を補助的に作動させて温水
の温度制御を行うようにする。A hot water heater 49 is provided inside the hot water tank 45, and when starting the soldering line, this hot water heater 49 releases sufficient thermal energy to rapidly raise the temperature of the cold water to obtain hot water at a predetermined temperature. At the same time, during the soldering operation, the hot water heater 49 is operated auxiliary to control the temperature of the hot water.
また前記PH調整槽21に対し、薬液タンク51゜52
からポンプ53.54により水素イオン濃度を調整する
ための薬液を供給するようにし、さらに、水道55から
ソレノイド弁56を介し水を補給づるようにし、ぞして
、このPH調整槽21の内部に設置ノだ攪拌機57によ
りこの調整槽内を攪拌する。In addition, with respect to the PH adjustment tank 21, a chemical tank 51° 52
A chemical solution for adjusting the hydrogen ion concentration is supplied from the pumps 53 and 54, and water is also supplied from the water supply 55 through the solenoid valve 56, and then into the PH adjustment tank 21. The inside of this adjustment tank is stirred by an installed agitator 57.
第1図中、1つ]」(よ水素イオン温度センサであり、
LSは一定の水面レベルを検出して作動するスイッチで
あり、PIは圧力計であり、PSは圧力スイッチであり
、特に前記ポンプ26と逆浸透膜27との間に設けたP
Sは、逆浸透膜27.28を保護するための圧力スイッ
チであり、CMは導電率センサであり、THは温度セン
サである。One in Figure 1 is a hydrogen ion temperature sensor,
LS is a switch that is activated by detecting a certain water surface level, PI is a pressure gauge, and PS is a pressure switch.
S is a pressure switch for protecting the reverse osmosis membranes 27, 28, CM is a conductivity sensor, and TH is a temperature sensor.
第2図、第3図および第4図は、第1図で説明した回路
を一体的にユニット構成したものを示すが、その説明は
、同一符号を付して省略する。2, 3, and 4 show an integral unit configuration of the circuit described in FIG. 1, but the description thereof will be omitted by giving the same reference numerals.
次に、この実施例の作用を説明する。Next, the operation of this embodiment will be explained.
まず、第1図に示す回路を始動させるときは、運転休止
中に、加圧されていなかった逆浸透膜21゜28を経て
濃縮水の排水管路31中に濃縮水でない汚水が、また純
水の循環管路32中に汚水が移動しているので、ソレノ
イド弁33.41を閉じるとともにソレノイド弁36.
44を開き、管路35.43を経て前記汚水をPHI整
槽21に戻す。そして、逆浸透圧ポンプ26の加圧作用
により逆浸透膜27.28が11常に作用して、IJI
水管路31と循環管路32とに濃縮水と純水とを分離で
きるようになったら、ソレノイド弁36.44を閉じる
とともにソレノイド弁33.41を開き、循環管路32
を杼で純水を温水槽45に拝送する。First, when starting the circuit shown in Fig. 1, during the suspension of operation, sewage that is not concentrated water passes through the unpressurized reverse osmosis membranes 21 and 28 and enters the concentrated water drainage pipe 31. Since waste water is moving into the water circulation line 32, the solenoid valves 33, 41 are closed and the solenoid valves 36, 41 are closed.
44 is opened and the wastewater is returned to the PHI tank 21 via pipes 35 and 43. Then, the reverse osmosis membranes 27 and 28 are constantly operated by the pressurizing action of the reverse osmosis pump 26, and the IJI
When concentrated water and pure water can be separated into the water pipe 31 and the circulation pipe 32, the solenoid valve 36.44 is closed and the solenoid valve 33.41 is opened.
Pure water is sent to the hot water tank 45 using a shuttle.
そして、はんだ付けラインの始!Jl萌t、(、温水ヒ
ータ49に最大限の通電を行って、冷水を最大の熱エネ
ルギにより急速加熱して温水にする。この温水を、ブリ
ヒータ12およびはんだ槽13にJ、り加熱され温水洗
浄槽14上に位置する搬送体15およびこの搬送体によ
り保持された被はんだ付け物に供給して、これらを洗浄
する。And the beginning of the soldering line! (The hot water heater 49 is energized to the maximum extent, and the cold water is rapidly heated with the maximum thermal energy to become hot water. This hot water is heated by the pre-heater 12 and the solder bath 13, and becomes hot water. It is supplied to the carrier 15 located on the cleaning tank 14 and the objects to be soldered held by this carrier to clean them.
この洗浄後の温水は、PH調′l!槽21でP HA整
した後に濾過機24.25により濾過し、そして、前記
ポンプ26により、できるだけ温度低下させることなく
、比較的高温(例えば60℃)に耐えられる逆浸透膜2
7.28に60Kg10i稈の圧で加圧供給し、この逆
浸透膜27.2111により、前記温水を比較的生のの
濃縮水と、比較的多量の純水とに分離する。The PH of the hot water after washing is adjusted! After the PHA is adjusted in the tank 21, the filter is filtered by the filter 24, 25, and then the reverse osmosis membrane 2, which can withstand relatively high temperatures (for example, 60° C.), is filtered by the pump 26 without reducing the temperature as much as possible.
7.28 is pressurized and supplied at a pressure of 60 kg 10 i culm, and this reverse osmosis membrane 27.2111 separates the hot water into relatively raw concentrated water and a relatively large amount of pure water.
そして、ill縮水は排水管路31を経て、凝集沈澱方
式、生物処理方式または蒸発処理方式等の排水処理施設
に送って排水処理し、純水は、比較的高温のまま前記循
環管路32を経て温水槽45に送り、この槽45内の温
水ヒータ49の補助的通電により前記純水を例えば70
℃程度に温度制御しながら、前記温水洗浄lf!14上
の搬送体15等に循環し、再使用する。前記はんだ付け
ラインで加熱された搬送体15等に接触した純水はその
搬送体15等から熱を19で高温状態でPHJ整槽21
に循環される。The ill condensed water is then sent through the drainage pipe 31 to a wastewater treatment facility such as a coagulation-sedimentation method, biological treatment method, or evaporation treatment method for wastewater treatment, and the purified water is passed through the circulation pipe 32 at a relatively high temperature. The purified water is then sent to a hot water tank 45, and by supplementary energization of the hot water heater 49 in this tank 45, the pure water is heated to a temperature of, for example, 70%.
While controlling the temperature to about ℃, the hot water washing lf! It is circulated to the carrier 15 on top of the carrier 14 and reused. The pure water that has come into contact with the carrier 15 etc. heated in the soldering line transfers heat from the carrier 15 etc. to the PHJ tank 21 in a high temperature state.
is circulated.
本発明によれば、洗浄後の温水を、できるだけ温度低下
させることなく比較的高温に耐えられる逆浸透膜に供給
し、この逆浸透膜により、前記温水を比較的少量の濃縮
水と、比較的多量の純水とに分離し、そして、濃縮水は
排水処理し、純水は、比較的iE’X′fAのまま前記
温水ヒータを経て前記温水洗浄槽上の搬送体等に循環し
、再使用するようにしたから、節水になるとともに、排
水量が少ないから、大形の排水処理IM設を必要としな
い。また、前記温水ヒータは、はんだ付けラインの始動
時に、冷水の温度立上がり用ヒータとして使用し、その
後は、はんだ付けラインで加熱された搬送体等に接触し
て高温状態で循環される温水の温度制御llに使用する
から、運転中は、この温水ヒータの消費熱エネルギが少
なく、省エネルギの温水処理方法である。According to the present invention, hot water after cleaning is supplied to a reverse osmosis membrane that can withstand relatively high temperatures without reducing the temperature as much as possible, and the reverse osmosis membrane converts the hot water into a relatively small amount of concentrated water and a relatively small amount of concentrated water. The concentrated water is separated into a large amount of pure water, and the concentrated water is treated as wastewater, and the pure water is circulated in a relatively iE'X'fA state through the hot water heater to the carrier on the hot water washing tank, and then recycled. Since it is used, it saves water, and since the amount of wastewater is small, there is no need for large-scale wastewater treatment IM equipment. In addition, the hot water heater is used as a heater to raise the temperature of cold water at the time of starting the soldering line, and after that, the temperature of the hot water that is circulated at high temperature when it comes into contact with the heated carrier etc. in the soldering line. Since it is used for control, the heat energy consumed by this hot water heater is small during operation, making it an energy-saving hot water treatment method.
第1図は本発明のはんだ付けラインにおける洗浄用温水
処理方法の一実施例を承り流体回路図、第2図はその回
路をユニット化した波防の正面図、第3図はその平面図
、第4図はその側面図である。
11・・フラクサ、12・・ブリヒータ、13・・はん
だ槽、14・・温水洗浄槽、15・・w1送体、27゜
28・・逆浸透膜、49・・渇水ヒータ。FIG. 1 is a fluid circuit diagram of an embodiment of the hot water treatment method for cleaning in a soldering line of the present invention, FIG. 2 is a front view of a wave block that unitizes the circuit, and FIG. 3 is a plan view thereof. FIG. 4 is a side view thereof. 11...Fluxer, 12...Buri heater, 13...Solder bath, 14...Hot water cleaning tank, 15...W1 feeder, 27° 28...Reverse osmosis membrane, 49...Drought water heater.
Claims (1)
槽に沿って移動する搬送体により被はんだ付け物を搬送
しながらはんだ付けするはんだ付けラインにおいて、こ
のはんだ付けラインの始動時は温水ヒータにより冷水を
加熱して温水にし、前記プリヒータおよびはんだ槽によ
り加熱され前記温水洗浄槽上に位置する前記搬送体およ
び被はんだ付け物に前記温水を供給して洗浄し、この洗
浄後の温水をできるだけ温度低下させることなく比較的
高温に耐えられる逆浸透膜に供給し、この逆浸透膜によ
り前記温水を比較的少量の濃縮水と比較的多量の純水と
に分離し、濃縮水は排水処理し、純水は比較的高温のま
ま前記温水ヒータを経て前記温水洗浄槽上の搬送体等に
循環することを特徴とするはんだ付けラインにおける洗
浄用温水処理方法。(1) In a soldering line where objects to be soldered are soldered while being conveyed by a conveyor that moves along a fluxer, preheater, soldering bath, and hot water cleaning bath, cold water is supplied by a hot water heater when starting the soldering line. Heating the water to make it hot, supplying the hot water to the carrier and the objects to be soldered that are heated by the preheater and the soldering tank and located on the hot water cleaning tank for cleaning, and lowering the temperature of the hot water after cleaning as much as possible. This reverse osmosis membrane separates the hot water into a relatively small amount of concentrated water and a relatively large amount of pure water, and the concentrated water is treated as waste water and purified water is A method of treating hot water for cleaning in a soldering line, characterized in that the hot water is circulated at a relatively high temperature through the hot water heater to a carrier on the hot water cleaning tank.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP20274785A JPS6261692A (en) | 1985-09-13 | 1985-09-13 | Method for treating hot washing water in soldering line |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP20274785A JPS6261692A (en) | 1985-09-13 | 1985-09-13 | Method for treating hot washing water in soldering line |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS6261692A true JPS6261692A (en) | 1987-03-18 |
Family
ID=16462490
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP20274785A Pending JPS6261692A (en) | 1985-09-13 | 1985-09-13 | Method for treating hot washing water in soldering line |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6261692A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2017087161A (en) * | 2015-11-12 | 2017-05-25 | 岩井ファルマテック株式会社 | Hot water recovery system |
-
1985
- 1985-09-13 JP JP20274785A patent/JPS6261692A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2017087161A (en) * | 2015-11-12 | 2017-05-25 | 岩井ファルマテック株式会社 | Hot water recovery system |
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