JPH0331490A - Rinsing method for surface treating stage - Google Patents
Rinsing method for surface treating stageInfo
- Publication number
- JPH0331490A JPH0331490A JP16731389A JP16731389A JPH0331490A JP H0331490 A JPH0331490 A JP H0331490A JP 16731389 A JP16731389 A JP 16731389A JP 16731389 A JP16731389 A JP 16731389A JP H0331490 A JPH0331490 A JP H0331490A
- Authority
- JP
- Japan
- Prior art keywords
- washing
- water
- cleaning
- materials
- zones
- 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
- 238000000034 method Methods 0.000 title claims abstract description 17
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 36
- 239000013505 freshwater Substances 0.000 claims abstract description 19
- 239000000463 material Substances 0.000 claims abstract description 18
- 239000000126 substance Substances 0.000 claims abstract description 18
- 239000007921 spray Substances 0.000 claims abstract description 17
- 238000004381 surface treatment Methods 0.000 claims abstract description 11
- 238000004140 cleaning Methods 0.000 claims description 42
- 238000005406 washing Methods 0.000 abstract description 25
- 238000011109 contamination Methods 0.000 abstract description 17
- 239000007788 liquid Substances 0.000 abstract description 9
- 239000003595 mist Substances 0.000 abstract description 4
- 230000003247 decreasing effect Effects 0.000 abstract description 2
- 238000009825 accumulation Methods 0.000 abstract 1
- 238000005238 degreasing Methods 0.000 description 7
- 239000002184 metal Substances 0.000 description 6
- 229910052751 metal Inorganic materials 0.000 description 6
- 239000003513 alkali Substances 0.000 description 5
- 230000000694 effects Effects 0.000 description 4
- 238000005507 spraying Methods 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 3
- 230000000052 comparative effect Effects 0.000 description 3
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 2
- 238000010422 painting Methods 0.000 description 2
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 1
- 239000002585 base Substances 0.000 description 1
- 239000013043 chemical agent Substances 0.000 description 1
- KRVSOGSZCMJSLX-UHFFFAOYSA-L chromic acid Substances O[Cr](O)(=O)=O KRVSOGSZCMJSLX-UHFFFAOYSA-L 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 239000013527 degreasing agent Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- AWJWCTOOIBYHON-UHFFFAOYSA-N furo[3,4-b]pyrazine-5,7-dione Chemical compound C1=CN=C2C(=O)OC(=O)C2=N1 AWJWCTOOIBYHON-UHFFFAOYSA-N 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 238000005192 partition Methods 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
- LRXTYHSAJDENHV-UHFFFAOYSA-H zinc phosphate Chemical compound [Zn+2].[Zn+2].[Zn+2].[O-]P([O-])([O-])=O.[O-]P([O-])([O-])=O LRXTYHSAJDENHV-UHFFFAOYSA-H 0.000 description 1
- 229910000165 zinc phosphate Inorganic materials 0.000 description 1
Landscapes
- Cleaning And De-Greasing Of Metallic Materials By Chemical Methods (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は金属表面の前処理方法とりわけ節水式の表面処
理方法に関する。DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] The present invention relates to a method for pre-treating metal surfaces, and in particular to a water-saving surface treatment method.
金属製品等に塗装などを行うに際しては、素地面を化学
的に脱脂、化成あるいはクロム酸、りん酸等で処理する
ことが行われる。When painting metal products, etc., the base surface is chemically degreased, chemically converted, or treated with chromic acid, phosphoric acid, etc.
この金属表面処理は、処理物を薬液処理部で処理し、次
いで次段以降の洗浄部で薬液を洗い落とす手段が汎用さ
れている。In this metal surface treatment, a method is commonly used in which the object to be treated is treated in a chemical treatment section, and then the chemical solution is washed off in a subsequent cleaning section.
しかしながら、従来の表面処理方法では、各水洗槽への
薬液の持込みが増加して洗浄効果が低下するのを防止す
る方法として、各水洗槽の最終槽に新鮮水を単に給水し
て順次前送りするか、処理物にスプレーして付着水の洗
浄を兼ねながら給水を行い、順次前送りする方法がとら
れている。However, in conventional surface treatment methods, as a way to prevent the cleaning effect from decreasing due to an increase in the amount of chemicals brought into each washing tank, fresh water is simply supplied to the final tank of each washing tank and the water is sent forward one by one. Alternatively, a method is used in which water is supplied by spraying the material to be treated while also cleaning the adhering water, and the method is carried out sequentially.
これら給水された水洗水は余剰水となって、第1段の水
洗部でオーバーフローされ、排水となって工程外へ排出
される。The supplied washing water becomes surplus water, overflows in the first stage washing section, becomes waste water, and is discharged outside the process.
これら従来の方法では、余剰水が洗浄槽へ戻される為、
洗浄槽の汚染度が高くなり、汚染度を低く押さえる為に
給水量も多量に必要になっている。In these conventional methods, excess water is returned to the cleaning tank, so
The level of contamination in the cleaning tank is increasing, and a large amount of water is required to keep the level of contamination low.
本発明は、前記のような従来技術の欠点を解消しようと
するもので、その目的とするところは薬液の付着した処
理物を効率よく洗浄し、しかも洗浄部の洗浄水の汚染度
を充分に低(維持し、掻めて少量の新鮮水の補給で済む
様にすることにある。The present invention aims to eliminate the above-mentioned drawbacks of the prior art, and its purpose is to efficiently clean the processed material to which the chemical solution has adhered, and to sufficiently reduce the degree of contamination of the cleaning water in the cleaning section. The goal is to maintain low water levels so that only a small amount of fresh water is required.
上記目的を達成するなめ、本発明は薬液を含む処理部で
表面処理を行った処理物を処理部から次段の洗浄部に移
送する際に通過する液切り部にて、処理物に付着した薬
液を新鮮水または次段の洗浄槽から導入された洗浄水で
スプレー洗浄し、スプレー洗浄後の汚染水は薬液槽や洗
浄槽へ戻すことな(、液切ゆ部から排水するようにした
ものである。In order to achieve the above-mentioned object, the present invention has been developed to remove particles that have been surface-treated in a treatment section containing a chemical solution, and to prevent the surface treatment from adhering to the treatment article at a liquid drain section through which the treated article is transferred from the treatment section to the next cleaning section. The chemical solution is spray-washed with fresh water or washing water introduced from the next-stage washing tank, and the contaminated water after spray washing is not returned to the chemical solution tank or washing tank (it is drained from the liquid drain section). It is.
上記構成により、処理物は薬液部にて表面処理された後
、液切り部に移送されてスプレー洗浄され、スプレー洗
浄された洗浄水は排水される。処理物はスプレー洗浄さ
れた後、次段以降の洗浄部へ移送され更に充分に洗浄さ
れるが、洗浄部にて洗浄されろ時には処理物に付着して
いる汚染水は、液切り部でスプレー洗浄されて充分に薄
められているので、洗浄槽の汚染のMWIが極めて低く
なる。With the above configuration, the treated object is surface-treated in the chemical solution section, then transferred to the liquid drain section and spray-cleaned, and the spray-cleaned cleaning water is drained. After the treated material is spray-cleaned, it is transferred to the next washing section and thoroughly cleaned. However, when it is washed in the cleaning section, the contaminated water adhering to the treated material is sprayed in the liquid draining section. Since it has been cleaned and is sufficiently diluted, the MWI of cleaning tank contamination is extremely low.
これにより洗浄槽への給水を低減させ、効果的に節水し
ながら汚染度管理が維持できる。This reduces water supply to the cleaning tank, effectively saving water while maintaining contamination level control.
次に本発明を添付図面にもとずいて具体的に説明する。Next, the present invention will be specifically explained based on the accompanying drawings.
第1図は本発明を金属塗装前処理工程に適用した実施例
を示すもので、2Aは入口部、2Bは予備脱脂部、2D
は本脱脂部、2Fは洗浄部、2Hば化成処理部、2Jは
洗浄部、2には出口部、Qは処理物である。Figure 1 shows an embodiment in which the present invention is applied to a metal painting pretreatment process, where 2A is an inlet, 2B is a preliminary degreasing part, and 2D is a pre-degreasing part.
2F is the main degreasing section, 2F is the cleaning section, 2H is the chemical conversion treatment section, 2J is the cleaning section, 2 is the outlet section, and Q is the treated product.
前記、入口部2Aから出口部2にはトンネル状のブース
として構成され、本実施例では処理物送入側から入口部
2A、予備脱脂ゾーン2B。A tunnel-shaped booth is constructed from the inlet section 2A to the outlet section 2, and in this embodiment, from the processing material inlet side to the inlet section 2A and the preliminary degreasing zone 2B.
ドレンゾーン2c、本税111ゾーン2D、ドレンゾー
ン2E、第1洗浄ゾーン2F、 ドレンゾーン2G、化
成ゾーン2H,ドレンゾーン21゜第2洗浄ゾーン2J
1処理物出口部2Kが分割形成され、予備脱脂ゾーン2
Bから第2洗浄ゾーン2Jまでの各ゾーンの間には、仕
切り板1υ〜IOUが設けられている。Drain zone 2c, main tax 111 zone 2D, drain zone 2E, first cleaning zone 2F, drain zone 2G, chemical conversion zone 2H, drain zone 21゜second cleaning zone 2J
1 Processed material outlet section 2K is divided and formed into a preliminary degreasing zone 2.
Partition plates 1υ to IOU are provided between each zone from B to the second cleaning zone 2J.
前記予備脱脂ゾーン2Bから第2洗浄ゾーン2Jの薬液
処理ゾーンならびに洗浄ゾーンには、それぞれスプレー
ノズル5B、5D、5F、5F’ 5H,5J、5
J’が配設されろと共に下部にはポンプ3B、3D、3
F、30.3Jと送り管4B、4D、4F、4H,4J
を介して前記スプレーノズル5B〜5Jと接続する液槽
IB〜IJが設けられている。Spray nozzles 5B, 5D, 5F, 5F' 5H, 5J, 5 are provided in the chemical treatment zones and cleaning zones from the preliminary degreasing zone 2B to the second cleaning zone 2J, respectively.
J' is arranged and pumps 3B, 3D, 3 are placed at the bottom.
F, 30.3J and feed pipe 4B, 4D, 4F, 4H, 4J
Liquid tanks IB to IJ are provided, which are connected to the spray nozzles 5B to 5J via.
又、ドレンゾーン2E、2G、21,2Kには新水送り
管6E、6G、61.6Kが配設されミストスプレーノ
ズル9E、9G、9 I、9Kに連結されている。Further, fresh water feed pipes 6E, 6G, 61.6K are arranged in the drain zones 2E, 2G, 21, 2K and connected to mist spray nozzles 9E, 9G, 9I, 9K.
ミストスプレーは流量調NI器?E、7G、717Kに
より流量を調整してスプレーされる。Is the mist spray a flow control NI device? E, 7G, and 717K are used to adjust the flow rate and spray.
ドレンゾーン2E、2Iには排水孔8E181が設けら
れている。Drain holes 8E181 are provided in the drain zones 2E and 2I.
Rは処理物搬送用のコンベアである。R is a conveyor for conveying the processed material.
(実施例1)
上記構成の金属塗装前処理工程により、金属製品の連続
脱脂〜化成処理を行った。(Example 1) Continuous degreasing to chemical conversion treatment of a metal product was performed by the metal coating pretreatment process having the above configuration.
処理物は表面414.38m’のロッカー 40台/時
間および表面積0.64m”の棚板100枚7時間の割
合で処理した。The treated items were treated at a rate of 40 lockers/hour with a surface area of 414.38 m'' and 100 shelf boards with a surface area of 0.64 m'' for 7 hours.
1B、10にはアルカリ脱脂剤(全アルカリ汚染度換算
で180m#)IHにはりん酸亜鉛系化成剤(全耐汚染
度換算で180mZ )を用い5F’、5J′のスプレ
ーを止めて9E、91への新鮮水のスプレー給水量をお
のおの24017時間としてそれぞれ8E、81より排
水し、9G、9にへの新鮮水のスプレー給水量をおのお
の4301ノ時間、1730I/時間として、それぞれ
前段へオーバーフローを行い8E、8Iより排水しなが
ら操業をおこなった。For 1B and 10, use an alkaline degreaser (180 m# in terms of total alkali contamination degree), and for IH, use a zinc phosphate-based chemical agent (180 mZ in terms of total contamination resistance degree), stop the spraying of 5F' and 5J', and apply 9E. The amount of fresh water sprayed to 91 is set to 24017 hours each, and the water is drained from 8E and 81, respectively.The amount of fresh water sprayed to 9G and 9 is set to 4301 hours and 1730 I/hour, respectively, and the overflow is sent to the previous stage. The operation was conducted while draining water from 8E and 8I.
以上の操業の結果IFにおける全アルカリ汚染度は2I
!1#で一定となり、IJにおける全齢汚染度は0.5
−で一定となった。As a result of the above operations, the total alkali contamination level at IF was 2I.
! It becomes constant at 1#, and the all-age contamination degree at IJ is 0.5
It became constant at −.
(実施例2)
次に9E、91への新鮮水のスプレー給水を止め5F’
5J’からの洗浄水のスプレー水量及び9G、9に
への新鮮水のスプレー給水量をそれぞれ、8B(17時
間、22901 /時間とした以外は実施例1と同一の
操業条件で処理をおこなった。(Example 2) Next, stop spraying fresh water to 9E and 91 and 5F'
The treatment was carried out under the same operating conditions as in Example 1, except that the amount of spray water from 5J' and the amount of fresh water sprayed to 9G and 9 were set to 8B (17 hours, 22901 / hour), respectively. .
以上の操業の結果1Fにおける全アルカリ汚染度は2d
で一定となり、IJにおげろ全齢汚染度は0.5−で一
定となった。As a result of the above operations, the total alkali contamination level on the 1st floor was 2d.
The contamination level of all ages in the IJ remained constant at 0.5-.
(実施例3)
9E、9Iへの新鮮水のスプレー給水量をおのおの24
01 /時間とし5F’、5J’からの洗浄水のスプレ
ー洗浄水量及び9G、9にへの新鮮水のスプレー給水量
をおのおの22017時間、88(1/時間として実施
例1と同一の操業条件で処理をおこなった。(Example 3) The amount of fresh water sprayed to 9E and 9I was adjusted to 24
Under the same operating conditions as Example 1, the amount of spray water from 5F' and 5J' and the amount of fresh water sprayed from 9G and 9 were set as 01/hour and 22,017 hours and 88 (1/hour, respectively). Processed.
以上の操業の結果IFにおける全アルカリ汚染度は2d
で一定となり、IJにおける全齢汚染度はO,S−で一
定となった。As a result of the above operations, the total alkali contamination level at IF was 2d.
The all-age contamination degree at IJ was constant at O and S-.
9E、9Iへの新鮮水のスプレー給水及び5F’5J’
からの洗浄水のスプレーを止めて969にへの新鮮水の
スプレー給水量をそれぞれ21001/時間、864(
17時間とした以外は同一の操業条件で処理を行った。Fresh water spray supply to 9E and 9I and 5F'5J'
Stop spraying washing water from 969 and increase the amount of fresh water sprayed from 969 to 21001/hour and 864/hour, respectively.
The treatment was carried out under the same operating conditions except for a 17 hour period.
以上の操業の結果、IFにおける全アルカリ汚染度は2
mjで一定となり、IJにおける全齢汚染度は0.5d
で一定となった。As a result of the above operations, the total alkali contamination level in the IF was 2.
It becomes constant at mj, and the all-age contamination degree at IJ is 0.5d.
It became constant.
実施例1〜3と比較例の新鮮水の給水量を第1表に示す
。Table 1 shows the amount of fresh water supplied in Examples 1 to 3 and Comparative Example.
第1表 単位(1I時間)
4B〜4J−・送り管、5B〜5J スプレーノズル、
6E〜6K・・新鮮水送り管、7E〜7に流量mvtm
、BE、81−・排水孔、9E〜9K・ミストスプレー
ノズル、Q 処理物、Rコンベア
〔発明の効果〕
実施例1〜3におけろ洗浄部IF、IJの洗浄水の汚染
度は比較例の新鮮水の給水量の約15〜30%であるに
も関わらず同等になり、良好な水量が維持できた。Table 1 Unit (1I hour) 4B~4J-・Feed pipe, 5B~5J Spray nozzle,
6E~6K...Fresh water feed pipe, flow rate mvtm to 7E~7
, BE, 81-・Drainage hole, 9E-9K・Mist spray nozzle, Q Processed material, R conveyor [Effect of the invention] The degree of contamination of the cleaning water of filter cleaning sections IF and IJ in Examples 1 to 3 is a comparative example Even though it was about 15 to 30% of the amount of fresh water supplied, it was the same, and a good amount of water could be maintained.
又、新鮮水の給水量を約15〜30%に減らす乙とがで
きたため、排水処理の負担軽減にもなるという優れた効
果が得られろ。Moreover, since the amount of fresh water supplied can be reduced by about 15-30%, an excellent effect can be obtained in that the burden of wastewater treatment is reduced.
Claims (4)
処理液で表面処理を行った後、処理物を順次次段の洗浄
ゾーン以降へ移送して洗浄等を行う表面処理方法におい
て、処理物を薬液ゾーンから次段の洗浄ゾーンの中間位
置にて洗浄水によるスプレー洗浄を行い、スプレー洗浄
した洗浄水を循環使用せずに排水することを特徴とする
表面処理工程における洗浄方法。1. In a surface treatment method in which the treated material is introduced into a tunnel-shaped booth and subjected to surface treatment with a treatment solution containing a chemical solution, the treated material is sequentially transferred to the next cleaning zone and subsequent stages for cleaning, etc. A cleaning method in a surface treatment process, characterized in that spray cleaning with cleaning water is performed at an intermediate position between a chemical zone and the next cleaning zone, and the sprayed cleaning water is drained without being recycled.
範囲第1項記載の表面処理工程における洗浄方法。2. A cleaning method in a surface treatment step according to claim 1, wherein the cleaning water for spray cleaning is fresh water.
導入された洗浄水である特許請求の範囲第1項記載の表
面処理工程における洗浄方法。3. 2. A cleaning method in a surface treatment step according to claim 1, wherein the cleaning water for spray cleaning is cleaning water introduced from a cleaning tank in a cleaning zone.
の洗浄槽から導入された洗浄水の両方である特許請求の
範囲第1項記載の表面処理工程における洗浄方法。4. A cleaning method in a surface treatment step according to claim 1, wherein the cleaning water to be spray cleaned is both fresh water and cleaning water introduced from a cleaning tank in a cleaning zone.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1167313A JP2711902B2 (en) | 1989-06-29 | 1989-06-29 | Cleaning method in surface treatment process |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1167313A JP2711902B2 (en) | 1989-06-29 | 1989-06-29 | Cleaning method in surface treatment process |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0331490A true JPH0331490A (en) | 1991-02-12 |
| JP2711902B2 JP2711902B2 (en) | 1998-02-10 |
Family
ID=15847435
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1167313A Expired - Fee Related JP2711902B2 (en) | 1989-06-29 | 1989-06-29 | Cleaning method in surface treatment process |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2711902B2 (en) |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5841355A (en) * | 1981-08-07 | 1983-03-10 | ビー・ブラウン―エスエスシー・アクチエンゲゼルシャフト | Collector for liquefied secretion |
| JPS5961272U (en) * | 1982-10-19 | 1984-04-21 | 日産自動車株式会社 | Pretreatment device |
| JPS6116367U (en) * | 1984-06-29 | 1986-01-30 | 日産自動車株式会社 | Pretreatment device |
| JPS6150762U (en) * | 1984-09-03 | 1986-04-05 |
-
1989
- 1989-06-29 JP JP1167313A patent/JP2711902B2/en not_active Expired - Fee Related
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5841355A (en) * | 1981-08-07 | 1983-03-10 | ビー・ブラウン―エスエスシー・アクチエンゲゼルシャフト | Collector for liquefied secretion |
| JPS5961272U (en) * | 1982-10-19 | 1984-04-21 | 日産自動車株式会社 | Pretreatment device |
| JPS6116367U (en) * | 1984-06-29 | 1986-01-30 | 日産自動車株式会社 | Pretreatment device |
| JPS6150762U (en) * | 1984-09-03 | 1986-04-05 |
Also Published As
| Publication number | Publication date |
|---|---|
| JP2711902B2 (en) | 1998-02-10 |
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