JPS6028908B2 - Chromate treatment device and chromate treatment method using the treatment device - Google Patents
Chromate treatment device and chromate treatment method using the treatment deviceInfo
- Publication number
- JPS6028908B2 JPS6028908B2 JP54081052A JP8105279A JPS6028908B2 JP S6028908 B2 JPS6028908 B2 JP S6028908B2 JP 54081052 A JP54081052 A JP 54081052A JP 8105279 A JP8105279 A JP 8105279A JP S6028908 B2 JPS6028908 B2 JP S6028908B2
- Authority
- JP
- Japan
- Prior art keywords
- tank
- cleaning
- container
- liquid
- treatment
- 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
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C22/00—Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals
Landscapes
- Chemical & Material Sciences (AREA)
- General Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Chemical Treatment Of Metals (AREA)
Description
【発明の詳細な説明】
本発明はクロメート処理装置および該処理装置を用いる
クロメート処理方法に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a chromate treatment apparatus and a chromate treatment method using the treatment apparatus.
従来、この種のクロメート処理を行うには硝酸処理液、
クロメート処理液もしくは洗浄水を夫夫充填した処理槽
に所定の順序で被処理物を浸潰していくものであった。Traditionally, this type of chromate treatment requires a nitric acid treatment solution,
The objects to be treated were immersed in a predetermined order into a treatment tank filled with a chromate treatment solution or washing water.
例えばクロメート処理の場合は、メッキ→水洗→硝酸処
理→水洗→クロメート処理→水洗→脱水→乾燥という工
程があり、被処理物はメッキ槽→水洗槽→硝酸処理槽→
水洗槽→クロメート処理槽→水洗槽→脱水機→乾燥機と
順次搬送、浸潰されていた。このような方法によれば一
工程に対して一つの処理槽ないいま処理機が必要であり
、これら処理槽ないいま処理機を収納する広い空間を必
要とすること、処理槽ないいま処理機の間を被処理物が
搬送されることが必要であり、搬送に人手もしくは装置
が必要であり、かつ搬送中に被処理物が損傷する恐れが
あること、処理槽ないいま処理機間で処理液相互の混合
もしくは処理液と洗浄水との混合が起ること一特にクロ
メート処理の場合は洗浄水に6価クロムがかなりの量混
合するから、これを除去してから排水しなければならな
いが、この方法では6価クロム除去処理量が大きなもの
となる一等の欠点がある。For example, in the case of chromate treatment, the steps are plating → water washing → nitric acid treatment → water washing → chromate treatment → water washing → dehydration → drying, and the object to be treated is plating tank → water washing tank → nitric acid treatment tank →
They were transported in the order of washing tank → chromate treatment tank → washing tank → dehydrator → dryer, and were submerged. According to this method, one processing tank or one processing machine is required for one process, and a large space is required to accommodate these processing tanks or one processing machine. It is necessary for the material to be processed to be transported between the processing tank and the processing machine, and the transport requires manpower or equipment, and there is a risk of damage to the material during transport. Mixing with each other or between the treatment solution and the cleaning water - Particularly in the case of chromate treatment, a considerable amount of hexavalent chromium is mixed into the cleaning water, which must be removed before it is drained. This method has the first drawback that the amount of hexavalent chromium removed is large.
本発明は上記従釆技術の欠点を改良し、空間効率を高め
、かつ被処理物の搬送を最少限にとどめるとともに液切
りをよくして処理液相互の混合もしくは処理液と洗浄水
との混合を防止し、かつ洗浄廃水を有効に再利用して排
出量を最少限にとどめることを目的とするものであり、
処理槽を多孔とし、かつ回転自在とすることを特徴とす
るものである。The present invention improves the shortcomings of the above-mentioned conventional techniques, improves space efficiency, minimizes the transportation of objects to be treated, improves drainage, and allows mixing of treatment liquids with each other or mixing of treatment liquid and cleaning water. The purpose of this system is to prevent waste water from washing, and to effectively reuse cleaning wastewater to minimize emissions.
The processing tank is characterized by being porous and rotatable.
本発明を図に示す一実施例によって説明すれば、Aは表
面処理装置であり、Bは硝酸タンクであり、Cはクロメ
ート液タンクであり、Dは洗浄貯槽装置であり、Eは洗
浄液撒布装置であり、Fは熱風乾燥装置である。The present invention will be described with reference to an embodiment shown in the drawings. A is a surface treatment device, B is a nitric acid tank, C is a chromate liquid tank, D is a cleaning storage tank device, and E is a cleaning liquid spraying device. , and F is a hot air drying device.
クロメート液タンクCはクロメート液の種類、例えば有
色クロメート液、光沢クロメート液、黒クロメート液等
に対応して2個以上設けてもよい。また、洗浄液貯槽D
も各洗浄工程の洗浄廃水が混合しないように各洗浄工程
に対応して2個以上設けることが望ましい。表面処理装
置Aにおいて1は基礎11から脚12およびスプリング
13を介して支持せられる容体であり、容体1の上部に
は菱30が蝶番31で枢着され、更に容体1の外周には
容体1内部と連絡孔10によって連絡する配液槽9が設
けられ、底部には自動弁MV,が介在する排液管28A
、自動弁MN2が介在する排液管28B、自動弁MV4
が介在する排出管29が夫々連絡し、排液管28Aは硝
酸タンクBに、排液管28Bはクロメート液タンクCに
、排出管29Aは洗浄液貯槽Dに夫々連絡する。ここに
自動弁とは、電磁弁・電動弁等をいう。容体1の底部中
心からは回転軸受2が垂下せられ、回転軸受2内部には
ベアリング4で支持され、かつメカニカルシール5にて
シールせられる垂直方向の回転軸3が貫通し、回転軸3
の上端には多数の細孔23を有する処理槽6が固定ナッ
ト8によって固定せられている。回転軸3の下端部には
プーリ−16,17が鼓着せられ、プーリー16,17
はベルト16A,17Aを介してブレーキモーターM,
,M2のプーリ−14,15に連絡する。処理槽6の回
転を低速・高速の二段に切換えるには、本実施例のよう
に二個のブレーキモーターM,,M2を備える他、一個
の駆動源でギァ−による切換え、プーリーによる切換え
等の公知の切換え方法が適用せられる。硝酸タンクB、
クロメート液タンクC、洗浄液貯槽Dからは夫々ポンプ
P,,P2,P3が介在する配液管24,25,26が
差出され、配液槽9に連絡する。配液槽9には、レベル
ゲージLが配置せられる。洗浄液噴射装置Eは容体1内
の処理槽6直上に配置せられ、孔20を多数設けたノズ
ル管21からなり、該ノズル管21は自動弁MV3が介
在する洗浄液供給管22に連絡する。熱風乾燥装置Fは
表面処理装置Aの容体1の上部に配され、先端に噴出管
27Aを設け、内部に熱線27Bを設け、後部に送風機
27Cを取付けた筒体27からなり、熱線27Bと送風
機27Cは作動装置日によって制御せられる。上記表面
処理装置系によってクロメート処理を施すには、亜鉛メ
ッキされたボルト等の彼処理物18は一対の把手19を
上縁両側に設けた金網のカゴ7に充填され、該カゴ7は
容体1の蓋30を開いて処理槽6に挿填される。Two or more chromate liquid tanks C may be provided depending on the type of chromate liquid, for example, colored chromate liquid, glossy chromate liquid, black chromate liquid, etc. In addition, the cleaning liquid storage tank D
It is desirable to provide two or more filters corresponding to each cleaning process so that the cleaning wastewater from each cleaning process does not mix. In the surface treatment apparatus A, a container 1 is supported from a base 11 via legs 12 and a spring 13. A rhombus 30 is pivotally attached to the upper part of the container 1 with a hinge 31, and a container 1 is attached to the outer periphery of the container 1. A liquid distribution tank 9 is provided which communicates with the interior through a communication hole 10, and a liquid drain pipe 28A is provided with an automatic valve MV interposed at the bottom.
, drain pipe 28B with automatic valve MN2 interposed, automatic valve MV4
The drain pipe 28A is connected to the nitric acid tank B, the drain pipe 28B is connected to the chromate liquid tank C, and the discharge pipe 29A is connected to the cleaning liquid storage tank D. Automatic valves here refer to solenoid valves, electric valves, etc. A rotary bearing 2 is suspended from the center of the bottom of the container 1, and a vertical rotary shaft 3 supported by a bearing 4 and sealed with a mechanical seal 5 passes through the rotary bearing 2.
A processing tank 6 having a large number of pores 23 is fixed by a fixing nut 8 at the upper end of the tank. Pulleys 16 and 17 are mounted on the lower end of the rotating shaft 3.
is the brake motor M via the belts 16A and 17A,
, M2 pulleys 14 and 15. In order to switch the rotation of the processing tank 6 into two stages of low speed and high speed, in addition to providing two brake motors M, M2 as in this embodiment, switching by gears or pulleys using a single drive source is also possible. The known switching method is applied. Nitric acid tank B,
From the chromate liquid tank C and the cleaning liquid storage tank D, liquid distribution pipes 24, 25, and 26 with pumps P, , P2, and P3 interposed, respectively, are extended and communicated with the liquid distribution tank 9. A level gauge L is arranged in the liquid distribution tank 9. The cleaning liquid injection device E is placed directly above the processing tank 6 in the container 1, and consists of a nozzle pipe 21 provided with a large number of holes 20, and the nozzle pipe 21 communicates with a cleaning liquid supply pipe 22 in which an automatic valve MV3 is interposed. The hot air drying device F is arranged on the top of the container 1 of the surface treatment device A, and consists of a cylinder body 27 with a jet pipe 27A at the tip, a hot wire 27B inside, and a blower 27C attached to the rear. 27C is controlled by the actuator. To perform chromate treatment using the above-mentioned surface treatment system, the object to be treated 18, such as a galvanized bolt, is filled into a wire mesh basket 7 having a pair of handles 19 on both sides of the upper edge. The lid 30 of the container is opened and the container is inserted into the processing tank 6.
かくしてから容体1の蓋30を閉じ、ブレーキモーター
M,を駆動して処理槽6を低速回転あるいは断続もしく
は反転回転せしめつつ自動弁MV4を閉じ、ポンプP3
を作動して洗浄液貯槽から洗浄水を容体1内に充填する
。洗浄水は、処理槽6内の被処理物18が完全に浸債す
るまで供給せられ、その時の水位はしベルゲージLによ
って検出され、レベルゲージLからの信号によってポン
プP3が停止して洗浄水の供給を断つ。断続回転とは例
えば正回転もしくは逆回転を0.5〜3秒間行ってのち
0.5〜3秒間停止するサイクルを繰返すものであり、
反転回転とは例えば正回転を0.5〜3秒間行ってのち
0.5〜3秒間停止し、次いで逆回転を0.5〜3秒間
行ってのち0.5〜3秒間停止する断続反転回転、正回
転と逆回転を停止期間を設けずして例えば0.5〜3秒
間ずつ繰返す連続反転回転のいずれも意味するものであ
る。上記低速回転および反転回転の間、被処理物18は
遠心力によって処理槽6の外壁方向に押圧され、殆んど
固定状態となり被処理物18相互の衝突は殆んと起らず
、被処理物が損傷することなく、只洗浄水のみが遠心力
により処理槽内に放射状に移動し、かくして被処理物に
洗浄水が充分行きわたるのである。反転回転では処理槽
内の洗浄水より騒乱されるが故に洗浄効果は一層向上す
る。ポンプP3が停止すると処理槽6が断続もしくは反
転回転せしめられている場合は低速回転に切換えられ「
かつ自動弁MV,が開き容体1内の洗浄廃水は排出管
29を介して洗浄液貯槽Dに回収する洗浄法1、および
/または自動弁MN3が開いて洗浄液供給管22からノ
ズル管21に洗浄水を供給し、ノズル管21から処理槽
6に挿填されたカゴ7内の被処理物18に対して洗浄水
が撒布される洗浄法2が適用される。かくして被処理物
18は効果的に洗浄され、洗浄廃水は排出管29から洗
浄液貯槽Dに回収せられる。洗浄が終了したら自動弁M
V3を閉じて洗浄液の供給を停止し、所望なればいまら
くそのままの状態を続けることによって洗浄廃水を振り
切る。この際、洗浄廃水の量はノズル管21から供給さ
れた洗浄水の量だけ増加することになるが、洗浄廃水の
上記増加分相当量は洗浄液貯槽Dからオーバーフローさ
れる。上記ノズル管21から供給された洗浄水は洗浄廃
水を希釈し、一定の清浄度に保つものである。以上が第
1洗浄工程である。次いで、処理槽6の低速回転をその
まま維持するかあるいは断続もしくは反転回転に切換え
、ポンプP,を作動して硝酸液を配液管24および配液
槽9を介して容体1内に充填する。After this, the lid 30 of the container 1 is closed, the automatic valve MV4 is closed while the brake motor M is driven to cause the processing tank 6 to rotate at low speed, intermittently or in reverse, and the pump P3 is turned on.
is operated to fill the container 1 with cleaning water from the cleaning liquid storage tank. The cleaning water is supplied until the object 18 in the treatment tank 6 is completely immersed, and the water level at that time is detected by the bell gauge L, and the pump P3 is stopped by a signal from the level gauge L to supply the cleaning water. cut off the supply of Intermittent rotation is, for example, repeating a cycle of forward or reverse rotation for 0.5 to 3 seconds and then stopping for 0.5 to 3 seconds.
Reverse rotation is, for example, intermittent reverse rotation in which forward rotation is performed for 0.5 to 3 seconds, then stopped for 0.5 to 3 seconds, then reverse rotation is performed for 0.5 to 3 seconds, and then stopped for 0.5 to 3 seconds. , refers to continuous reversal rotation in which forward rotation and reverse rotation are repeated, for example, for 0.5 to 3 seconds each without providing a stop period. During the above-mentioned low-speed rotation and reverse rotation, the objects 18 to be processed are pressed toward the outer wall of the processing tank 6 by centrifugal force, and are almost fixed, with almost no collision between the objects 18 and the objects 18 being processed. Only the washing water moves radially into the processing tank due to centrifugal force without damaging the objects, and thus the washing water is sufficiently distributed over the objects to be processed. Since the reverse rotation causes more disturbance than the cleaning water in the processing tank, the cleaning effect is further improved. When the pump P3 stops, if the processing tank 6 is being rotated intermittently or in reverse, it is switched to low speed rotation.
Then, the automatic valve MV is opened and the cleaning waste water in the container 1 is collected into the cleaning liquid storage tank D via the discharge pipe 29 (cleaning method 1), and/or the automatic valve MN3 is opened and the cleaning water is discharged from the cleaning liquid supply pipe 22 to the nozzle pipe 21. A cleaning method 2 is applied in which cleaning water is supplied and sprayed from the nozzle pipe 21 onto the objects 18 to be processed in the basket 7 inserted into the processing tank 6. In this way, the object to be treated 18 is effectively cleaned, and the cleaning waste water is collected from the discharge pipe 29 into the cleaning liquid storage tank D. Automatic valve M when cleaning is completed
Close V3 to stop the supply of cleaning fluid and, if desired, continue to do so for now to shake off the cleaning waste water. At this time, the amount of cleaning wastewater increases by the amount of cleaning water supplied from the nozzle pipe 21, but the amount corresponding to the increase in cleaning wastewater overflows from the cleaning liquid storage tank D. The cleaning water supplied from the nozzle pipe 21 dilutes the cleaning waste water and maintains it at a constant level of cleanliness. The above is the first cleaning step. Next, the low-speed rotation of the processing tank 6 is maintained as it is, or is switched to intermittent or reverse rotation, and the pump P is operated to fill the container 1 with the nitric acid solution via the liquid distribution pipe 24 and the liquid distribution tank 9.
硝酸液は処理槽6内の彼処理物18が完全に浸債するま
で供給せられ、その時の液位はしベルゲージLによって
検出され、レベルゲージLからの信号によってポンプP
,が停止して硝酸液の供給を断つ。約3〜5秒そのまま
の状態を維持したのち処理槽6が断続もしくは反転回転
せしめられている場合は低速回転に切換えてから自動弁
MN,を開いて容体1内の硝酸液を排液管28Aから硝
酸タンクBに回収する。容体1内の硝酸液が殆ど排出さ
れてから約5秒間そのままの状態を維持して被処理物に
付着した硝酸を振り切る。この場合、第1洗浄工程後の
被処理物18が硝酸液に浸潰するまでの間処理槽6が高
速回転していないから表面は完全に乾いておらず単分子
膜程度の水は残着しており、したがってこの状態で硝酸
処理が行われることになり、処理が円滑に進む。以上が
硝酸処理工程である。次いで、処理槽6の低速回転を維
持するかあるいは断続もしくは反転回転せしめ、前述の
洗浄法1および/または洗浄法2を適用する。この際は
、第1洗浄工程によって回収せられた洗浄廃水と混合し
ないように別の洗浄液貯槽Dに洗浄廃水を回収すること
が望ましい。かくして前回と同様に被処理物18は効果
的に洗浄され、洗浄廃水は排出管29から洗浄液貯槽D
に回収せられる。The nitric acid solution is supplied until the material to be processed 18 in the processing tank 6 is completely immersed, and the liquid level at that time is detected by the level gauge L, and the pump P is activated based on the signal from the level gauge L.
, stops and cuts off the supply of nitric acid. After maintaining this state for about 3 to 5 seconds, if the processing tank 6 is being rotated intermittently or in reverse, switch to low speed rotation, open the automatic valve MN, and drain the nitric acid solution in the container 1 to the drain pipe 28A. from the nitric acid tank B. After most of the nitric acid solution in the container 1 has been discharged, the state is maintained for about 5 seconds to shake off the nitric acid adhering to the object to be treated. In this case, since the processing tank 6 is not rotating at high speed until the object to be processed 18 is immersed in the nitric acid solution after the first cleaning step, the surface is not completely dry and a monomolecular film of water remains. Therefore, the nitric acid treatment is performed in this state, and the treatment proceeds smoothly. The above is the nitric acid treatment step. Next, the processing tank 6 is kept rotating at a low speed, or is rotated intermittently or in reverse, and the above-mentioned cleaning method 1 and/or cleaning method 2 is applied. At this time, it is desirable to collect the washing wastewater in a separate washing liquid storage tank D so as not to mix it with the washing wastewater collected in the first washing step. In this way, the object to be treated 18 is effectively cleaned as in the previous case, and the cleaning waste water is discharged from the discharge pipe 29 to the cleaning liquid storage tank D.
will be collected.
洗浄が終了したら自動弁MV3を閉じて洗浄液の供給を
停止し、所望なればいまらくそのままの状態を続けるこ
とによって洗浄廃水を振り切ったのち自動弁MV4を閉
じる。この場合、硝酸処理工程後の被処理物18が洗浄
水と接触するまでの間処理槽6は高速回転していないか
ら被処理物18の表面に残着している硝酸液は乾燥濃縮
されず、したがって硝酸液による被処理物18の腐蝕は
起らないのである。以上が第2洗浄工程である。自動弁
MN5が閉じるとともにポンプP2が作動するように設
定すれば、ポンプP2によってクロメート液タンクC中
のクロメート液は配液管25を介して配液槽9、更に容
体1に充填せられ、液位はポンプP2と連動するレベル
ゲージLIこよって調節せられる。When the cleaning is completed, the automatic valve MV3 is closed to stop the supply of cleaning liquid, and if desired, the state is continued for a while to shake off the cleaning waste water, and then the automatic valve MV4 is closed. In this case, since the treatment tank 6 is not rotating at high speed until the object 18 comes into contact with the washing water after the nitric acid treatment step, the nitric acid solution remaining on the surface of the object 18 is not dried and concentrated. Therefore, the object to be treated 18 is not corroded by the nitric acid solution. The above is the second cleaning step. If the automatic valve MN5 is set to close and the pump P2 is activated, the chromate solution in the chromate solution tank C is filled by the pump P2 into the distribution tank 9 and further into the container 1 via the distribution pipe 25, and the liquid is The level is adjusted by a level gauge LI that is interlocked with pump P2.
容体1内のクロメート液が所定の液位L、即ち被処理物
が完全に浸潰するに至るとポンプP2が停止する。この
間処理槽6は低速回転をそのまま維持するか、あるいは
断続もしくは反転回転に切換える。そのままの状態をい
まらく維持したのち、処理槽6が断続もしくは反転回転
せしめられている場合には低速回転に切換え、自動弁M
N2を開いて容体1から排液管288を介してクロメー
ト液をクロメート液タンクCに回収する。容体1内のク
ロメート液が殆ど排出されてからそのままの状態を続け
、被処理物に付着したクロメート液を振切る。クロメー
ト処理に際して被処理物18の表面には単分子膜程度の
洗浄水が残着しており、クロメート処理はこのような状
態では円滑に進む。以上がクロメート処理工程である。
次いで、処理槽6の低速回転を維持するかあるいは断続
もしくは反転回転せしめ、前述の洗浄法1および/また
は洗浄法2を適用する。この際もまた第1洗浄工程およ
び第2洗浄工程によって回収せられた洗浄廃水と夫々混
合しないように別の洗浄液貯槽Dに洗浄廃水を回収する
ことが望ましい。洗浄が終了したら自動弁My3を閉じ
て洗浄法の供給を停止し、所望なればいまらくそのまま
の状態を続けることによって洗浄廃水を振り切ったのち
自動弁hW4を閉じる。When the chromate solution in the container 1 reaches a predetermined level L, that is, the object to be treated is completely immersed, the pump P2 stops. During this time, the processing tank 6 either maintains low speed rotation or switches to intermittent or reverse rotation. After maintaining this state for a while, if the processing tank 6 is being rotated intermittently or in reverse, it is switched to low speed rotation and the automatic valve M is turned on.
N2 is opened and the chromate solution is collected from the container 1 through the drain pipe 288 into the chromate solution tank C. After most of the chromate solution in the container 1 has been discharged, the container 1 is left in that state, and the chromate solution adhering to the object to be treated is shaken off. During the chromate treatment, a monomolecular film of cleaning water remains on the surface of the object to be treated 18, and the chromate treatment proceeds smoothly under such conditions. The above is the chromate treatment step.
Next, the processing tank 6 is kept rotating at a low speed, or is rotated intermittently or in reverse, and the above-mentioned cleaning method 1 and/or cleaning method 2 is applied. At this time as well, it is desirable to collect the washing wastewater into a separate washing liquid storage tank D so as not to mix with the washing wastewater collected in the first washing step and the second washing step, respectively. When the cleaning is completed, the automatic valve My3 is closed to stop the supply of the cleaning method, and if desired, the cleaning method is continued for a while to shake off the cleaning waste water, and then the automatic valve hW4 is closed.
第3洗浄工程の際には被処理物に残着しているクロメー
ト液は乾燥濃縮されず、したがって被処理物はクロメー
ト液に腐蝕されない。以上が第3洗浄工程である。以上
、第1洗浄工程・第2洗浄工程‘第3洗浄工程から選ば
れた1つの工程、または2つ以上の工程に必ず洗浄法1
を適用して洗浄廃液の回収を図るべきである。During the third cleaning step, the chromate solution remaining on the object to be treated is not dried and concentrated, so that the object to be treated is not corroded by the chromate solution. The above is the third cleaning step. As mentioned above, cleaning method 1 must be applied to one or more processes selected from the first cleaning process, second cleaning process, and third cleaning process.
should be applied to recover cleaning waste liquid.
次いで、ブレーキモーターによって高速回転を行い、脱
水を完全に図ると同時に容体1の蓋30を開き作動装置
日を作動させて熱風乾燥機Fから熱風を3〜5分間被処
理物に吹付けて乾燥を完全にする。ブレーキモーター地
および熱風乾燥機Fの作動装置日を停止する。以上が乾
燥工程である。以上に述べた6つの工程によってクロメ
ート処理が完了するから、金網のカゴ7を処理槽6から
取出すことにより作業は完了する。Next, the brake motor rotates at high speed to ensure complete dehydration, and at the same time, the lid 30 of the container 1 is opened, the actuator is activated, and hot air is blown from the hot air dryer F onto the object for 3 to 5 minutes to dry it. complete. Stop the brake motor and hot air dryer F operating system. The above is the drying process. Since the chromate treatment is completed through the six steps described above, the work is completed by taking out the wire mesh basket 7 from the treatment tank 6.
本発明は上記実施例以外電解メッキ、無電解〆ッキ、亜
鉛−クロム処理その他如何なる表面処理にも適用されて
も有用である。The present invention is useful even when applied to any surface treatment other than the above embodiments, such as electrolytic plating, electroless finishing, zinc-chromium treatment, and others.
上記6つの工程はシーケンス制御され得、かくして入手
が全く必要でなくなる。The above six steps can be sequenced, thus eliminating the need for any acquisition.
本発明は上記の構成を有するから、被処理物の移動に要
する装置、人手等が省略される上に多孔処理槽中の被処
理物は処理液に浸潰されつつ多孔処理槽とともに遠心力
によって束縛されることにより殆んどお互いに衝突し、
損傷し合うことなく回転するから被処理物の細部にまで
被処理液が速かにいきわたり、処理効率が向上するとと
もに処理が均一に施される。Since the present invention has the above-mentioned configuration, the equipment, manpower, etc. required for moving the object to be treated can be omitted, and the object to be treated in the porous treatment tank is immersed in the treatment liquid and is caused by centrifugal force together with the porous treatment tank. By being constrained, they almost collide with each other,
Because they rotate without damaging each other, the liquid to be treated is quickly distributed to the smallest details of the object, improving treatment efficiency and uniformly processing the object.
また、被処理物に付着した処理液も遠心脱液されるから
残存量も少なくなり、処理液の回収率は向上し、かつ処
理液相互の混合も少なくなる。そして洗浄工程、硝酸工
程、クロメート処理工程の後は処理槽は高速回転されず
低速回転もしくは反転回転されて、その後につづく処理
を行うまで被処理物が完全に乾燥することを防止し、も
って処理の円滑化、処理液による腐蝕防止を図るもので
ある。更にまた洗浄廃水を洗浄液貯槽に回収し有効利用
するから、洗浄の際の洗浄水も極めて僅かですむから、
洗浄廃水量も少なくなり、処理が簡単かつ容易であり、
処理費用も低減される。Further, since the processing liquid adhering to the object to be processed is centrifugally removed, the remaining amount is reduced, the recovery rate of the processing liquid is improved, and mixing of the processing liquids with each other is reduced. After the cleaning process, nitric acid process, and chromate treatment process, the processing tank is not rotated at high speed but at low speed or rotated in reverse to prevent the workpiece from drying completely until the subsequent processing. This aims to smooth the process and prevent corrosion caused by the processing liquid. Furthermore, since the cleaning waste water is collected in the cleaning liquid storage tank and used effectively, the amount of cleaning water required for cleaning is extremely small.
The amount of washing waste water is also reduced, and treatment is simple and easy.
Processing costs are also reduced.
図は本発明の一実施例を示すものであり、第1図は正断
面図、第2図は表面処理装置本体の斜視図、第3図は多
孔処理槽の斜視図、第4図はカゴの斜視図である。
図中 1…・・・容体、3・・・・・・回転軸、6・・
・・・・多孔処理槽、18・・・・・・被処理物、21
・・・・・・ノズル管、22……洗浄液供給管、MV.
,MV2,MV3,MV4,MV5・・・…自動弁、L
……レベルゲージ、M,,M2・・・・・・ブレーキモ
ーター、日・・・・・・熱風乾燥機の作動装置。
才4図
才1賊
才2図
才3図The drawings show one embodiment of the present invention, in which Fig. 1 is a front sectional view, Fig. 2 is a perspective view of the main body of the surface treatment equipment, Fig. 3 is a perspective view of the porous treatment tank, and Fig. 4 is a cage. FIG. In the diagram: 1...Container, 3...Rotation axis, 6...
... Porous treatment tank, 18 ... Treated object, 21
... Nozzle pipe, 22 ... Cleaning liquid supply pipe, MV.
, MV2, MV3, MV4, MV5... automatic valve, L
... Level gauge, M,, M2 ... Brake motor, Day ... Hot air dryer operating device. 4 figures, 1 figure, 2 figures, 3 figures
Claims (1)
容体に連通する配液槽と、該多孔処理槽内の内容物を洗
浄する洗浄液撒布装置と、該多孔処理槽内の内容物を乾
燥する熱風乾燥装置と、硝酸タンクと、クロメート液タ
ンクと、洗浄排液貯槽とからなり、しかして多孔処理槽
は垂直方向に回転軸を有し駆動装置Mによつて正逆両方
向に高速および低速回転せしめられ、硝酸タンク、クロ
メート液タンクおよび洗浄排液貯槽はポンプP_1,P
_2,P_3が介在する配液管により夫々配液槽に連絡
せられ、かつまた自動弁MV_1,MV_2,MV_4
が介在する排液管によつて容体と夫々連絡せられ、配液
槽にはレベルゲージLが配置せられ、洗浄液撒布装置は
自動弁MV_3が介在する供液管が連絡せられ、熱風乾
燥装置には作動装置Hが取付けられたことを特徴とする
クロメート処理装置。 2 容体と、該容体内に取付けられた多孔処理槽と、該
容体に連通する配液槽と、該多孔処理槽内の内容物を洗
浄する洗浄液撒布装置と、該多孔処理槽内の内容物を乾
燥する熱風乾燥装置と、硝酸タンクと、クロメート液タ
ンクと洗浄排液貯槽とからなり、しかして多孔処理槽は
垂直方向に回転軸を有し駆動装置Mによつて正逆両方向
に高速および低速回転せしめられ、硝酸タンク、クロメ
ート液タンクおよび洗浄排液貯槽はポンプP_1,P_
2,P_3が介在する配液管により夫々配液槽に連絡せ
られ、かつまた自動弁MV_1,MV_2,MV_4が
介在する排液管によつて容体と夫々連絡せられ、配液槽
にはレベルゲージLが配置せられ、洗浄液撒布装置は自
動弁MV_3が介在する供液管が連絡せられ、熱風乾燥
装置には作動装置Hが取付けられたクロメート処理装置
において、被処理物を多孔処理槽に収容し、該処理槽を
駆動装置Mによつて低速回転させつつ洗浄水を容体内に
充填し、更にMV_4を開いて洗浄排水を排出管から洗
浄液貯槽に回収する第1洗浄工程、MV_3を閉じてか
ら処理槽の低速回転を維持しつつMV_4を閉じP_1
を作動して硝酸液を配液槽を介して容体内に充填し、処
理槽内の被処理物が完全に浸漬する液位LでP_1を停
止し、しかるのちMV_1を開いて容体から硝酸タンク
に硝酸液を回収し、かつ振切る硝酸処理工程、MV_1
を閉じ処理槽の低速回転を維持させつつ洗浄水を容体内
に充填し、更にMV_4を開いて洗浄排水を排出管から
洗浄排液貯槽に回収する第2洗浄工程、Mを閉じてから
Mを停止して処理槽の低速回転を中断し、MV_4を閉
じP_2を作動してクロメート液を配液槽を介して容体
に充填し、処理槽内の被処理物が完全に浸漬する液位L
でP_2を停止し、しかるのち多孔処理槽をMによつて
断続もしくは反転回転せしめた後、処理槽を低速回転せ
しめつつMN_3を開いて容体からクロメート液タンク
にクロメート液を回収し、かつ振切るクロメート処理工
程、MV_2を閉じ処理槽の低速回転を維持しつつ洗浄
水を容体内に充填し、更にMV_4を開いて洗浄廃水を
排出管から洗浄液貯槽に回収する第3洗浄工程、MV_
3を閉じ処理槽をMによつて高速回転せしめつつHを作
動して残存洗浄水の振切りおよび乾燥を行う乾燥工程。 以上の工程からなり、しかして第1洗浄工程、第2洗
浄工程、第3洗浄工程は処理槽を駆動装置Mによつて低
速回転させつつP_3を作動して洗浄液貯槽から洗浄水
を容体内に充填し、処理槽内の被処理物が完全に浸漬す
る水位でP_3を停止しMV_4を開いて洗浄廃水を排
出管から洗浄液貯槽に回収する洗浄法1、および/また
はMV_3を開いて洗浄水を洗浄液撒布装置から被処理
物に噴射する洗浄法2によつて行なうが、第1洗浄工程
、第2洗浄工程、第3洗浄工程から選ばれた1つの工程
、または2つ以上の工程に必ず洗浄法1を適用すること
を特徴とするクロメート処理方法。3 容体と、該容体
内に取付けられた多孔処理槽と、該容体に連通する配液
槽と、該多孔処理槽内の内容物を洗浄する洗浄液撒布装
置と、該多孔処理槽内の内容物を乾燥する熱風乾燥装置
と、硝酸タンクと、クロメート液タンクと、洗浄排液貯
槽とからなり、しかして多孔処理槽は垂直方向に回転軸
を有し駆動装置Mによつて正逆両方向に高速および低速
回転せしめられ、硝酸タンク、クロメート液タンクおよ
び洗浄排液貯槽はポンプP_1,P_2,P_3が介在
する配液管により夫々配液槽に連絡せられ、かつまた自
動弁MV_1,MV_2,MV_4が介在する排液管に
よつて容体と夫々連絡せられ、配液槽にはレベルゲージ
Lが配置せられ、洗浄液撒布装置は自動弁MV_3が介
在する供液管が連絡せられ、熱風乾燥装置には作動装置
Hが取付けられたクロメート処理装置において、被処理
物を多孔処理槽に収容し、該処理槽を駆動装置Mによつ
て低速回転させつつ洗浄水を容体内に充填し、更にMV
_4を開いて洗浄排水を排出管から洗浄液貯槽に回収す
る第1洗浄工程、MV_3を閉じてからMによつて処理
槽を断続もしくは反転回転せしめつつMV_4を閉じP
_1を作動して硝酸液を配液槽を介して容体内に充填し
、処理槽内の被処理物が完全に浸漬する液位LでP_1
を停止し、しかるのちMによつて処理槽を低速回転させ
つつMV_1を開いて容体から硝酸タンクに硝酸液を回
収し、かつ振切る硝酸処理工程、MV_1を閉じ処理槽
を断続もしくは反転回転せしめつつ洗浄水を容体内に充
填し、更にMによつて処理槽を低速回転させMV_4を
開いて洗浄排水を排出管から洗浄液貯槽に回収する第2
洗浄工程、MV_3を閉じてからMを停止して所望なれ
ば処理槽の低速回転を中断し、あるいは処理槽の低速回
転を維持しつつMV_4を閉じP_2を作動してクロメ
ート液を配液槽を介して容体に充填し処理槽内の被処理
物が完全に浸漬する液位LでP_2を停止し、しかるの
ち多孔処理槽をMによつて断続もしくは反転回転せしめ
た後、処理槽を低速回転せしめつつMV_2を開いて容
体からクロメート液タンクにクロメート液を回収し、か
つ振切るクロメート処理工程、MV_2を閉じ処理槽を
断続もしくは反転回転せしめつつ洗浄水を容体内に充填
し、更にMによつて処理槽を低速回転させMV_4を開
いて洗浄排水を排出管から洗浄液貯槽に回収する第3洗
浄工程、MV_3を閉じ処理槽をMによつて高速回転せ
しめつつHを作動して残存洗浄水の振切りおよび乾燥を
行う乾燥工程。 以上の工程からなり、しかして第1洗浄工程、第2洗
浄工程、第3洗浄工程は処理槽を駆動装置Mによつて低
速回転させつつP_3を作動して洗浄液貯槽から洗浄水
を容体内に充填し、処理槽内の被処理物が完全に浸漬す
る水位でP_3を停止しMV_4を開いて洗浄排水を排
出管から洗浄液貯槽に回収する洗浄法1、および/また
はMV_3を開いて洗浄水を洗浄液撒布装置から被処理
物に噴射する洗浄法2によつて行なうが、第1洗浄工程
、第2洗浄工程、第3洗浄工程から選ばれた1つの工程
、または2つ以上の工程に必ず洗浄法1を適用すること
を特徴とするクロメート処理方法。[Scope of Claims] 1. A container, a porous treatment tank installed in the container, a liquid distribution tank communicating with the container, a cleaning liquid spraying device for cleaning the contents in the porous treatment tank, and a porous treatment tank. It consists of a hot air drying device for drying the contents in the treatment tank, a nitric acid tank, a chromate solution tank, and a washing waste liquid storage tank. The nitric acid tank, chromate liquid tank, and cleaning waste liquid storage tank are operated by pumps P_1 and P_1.
_2, P_3 are connected to the liquid distribution tank by intervening liquid distribution pipes, and automatic valves MV_1, MV_2, MV_4
A liquid distribution tank is connected to the container by a drain pipe with an intervening liquid tank, a level gauge L is arranged in the liquid distribution tank, a cleaning liquid spraying device is connected with a liquid supply pipe with an automatic valve MV_3, and a hot air drying device A chromate treatment device characterized in that an actuating device H is attached to the chromate treatment device. 2. A container, a porous treatment tank installed in the container, a liquid distribution tank communicating with the container, a cleaning liquid spraying device for cleaning the contents in the porous treatment tank, and the contents in the porous treatment tank. The porous treatment tank has a rotating shaft in the vertical direction and can be rotated at high speed and in both forward and reverse directions by a drive device M. The nitric acid tank, chromate liquid tank, and washing waste liquid storage tank are rotated at low speed, and
2, P_3 are connected to the liquid distribution tank through liquid distribution pipes, and are also connected to the container through liquid drainage pipes in which automatic valves MV_1, MV_2, and MV_4 are interposed, and the liquid distribution tank has a level. In the chromate treatment equipment, a gauge L is arranged, a cleaning liquid spraying device is connected to a liquid supply pipe with an automatic valve MV_3, and a hot air drying device is equipped with an actuating device H. The processing tank is rotated at low speed by the drive device M, and cleaning water is filled into the container, and MV_4 is opened to collect the cleaning waste water from the discharge pipe to the cleaning liquid storage tank. MV_3 is closed. After that, close MV_4 while maintaining the low speed rotation of the processing tank P_1
MV_1 is opened to fill the container with nitric acid solution through the liquid distribution tank, stop P_1 at the liquid level L where the objects to be processed in the processing tank are completely immersed, and then open MV_1 to remove the nitric acid from the container. Nitric acid treatment step of recovering and shaking off the nitric acid solution, MV_1
The second cleaning process involves closing M and filling the container with cleaning water while maintaining the low speed rotation of the processing tank, and then opening MV_4 to collect the cleaning wastewater from the discharge pipe into the cleaning wastewater storage tank. Stop and interrupt the low-speed rotation of the processing tank, close MV_4 and activate P_2 to fill the container with chromate solution through the liquid distribution tank until the liquid level L is reached at which the object to be processed in the processing tank is completely immersed.
After stopping P_2, the porous treatment tank is rotated intermittently or in reverse by M, and then MN_3 is opened while rotating the treatment tank at low speed to collect the chromate solution from the container into the chromate solution tank and shake it out. Chromate treatment step, MV_2 is closed and cleaning water is filled into the container while maintaining the low speed rotation of the treatment tank, and MV_4 is further opened to collect the cleaning waste water from the discharge pipe into the cleaning liquid storage tank. Third cleaning step, MV_
3 is closed, the processing tank is rotated at high speed by M, and H is operated to shake off the remaining washing water and dry it. Consisting of the above steps, the first, second, and third cleaning steps operate P_3 while rotating the treatment tank at low speed by the drive device M to supply cleaning water from the cleaning liquid storage tank into the container. Cleaning method 1, in which P_3 is stopped at a water level where the objects to be treated in the treatment tank are completely immersed, and MV_4 is opened to collect the cleaning waste water from the discharge pipe into the cleaning liquid storage tank, and/or MV_3 is opened to drain the cleaning water. This is carried out by cleaning method 2, in which the cleaning liquid is sprayed onto the workpiece from a cleaning liquid spraying device, but cleaning is always performed in one or more steps selected from the first cleaning step, second cleaning step, and third cleaning step. A chromate treatment method characterized by applying Method 1. 3. A container, a porous treatment tank installed in the container, a liquid distribution tank communicating with the container, a cleaning liquid spraying device for cleaning the contents in the porous treatment tank, and the contents in the porous treatment tank. The porous treatment tank has a rotating shaft in the vertical direction and can be rotated at high speed in both forward and reverse directions by a drive device M. The nitric acid tank, chromate liquid tank, and cleaning waste liquid storage tank are connected to the liquid distribution tank through liquid distribution pipes with pumps P_1, P_2, and P_3, respectively, and automatic valves MV_1, MV_2, and MV_4 are connected to the liquid distribution tank. Each of them is connected to the container by an intervening drain pipe, a level gauge L is placed in the liquid distribution tank, and the cleaning liquid spraying device is connected to a liquid supply pipe with an automatic valve MV_3, and connected to a hot air drying device. is a chromate treatment apparatus equipped with an actuating device H, in which the object to be treated is accommodated in a porous treatment tank, the treatment tank is rotated at low speed by a drive device M, cleaning water is filled into the container, and the MV
The first cleaning step is to open _4 and collect the cleaning wastewater from the discharge pipe to the cleaning liquid storage tank, then close MV_3, and then close MV_4 while intermittent or reverse rotation of the treatment tank by M.
_1 is activated to fill the container with nitric acid solution through the liquid distribution tank, and at the liquid level L at which the object to be processed in the processing tank is completely immersed, P_1 is reached.
Then, while rotating the processing tank at low speed using M, MV_1 is opened to collect the nitric acid solution from the container into the nitric acid tank, and the nitric acid solution is shaken off. MV_1 is closed and the processing tank is rotated intermittently or in reverse. In the second step, cleaning water is filled into the container, and the treatment tank is rotated at low speed by M, and MV_4 is opened to collect the cleaning waste water from the discharge pipe to the cleaning liquid storage tank.
In the cleaning process, close MV_3 and then stop M to interrupt the low-speed rotation of the treatment tank if desired, or close MV_4 while maintaining the low-speed rotation of the treatment tank and operate P_2 to supply the chromate solution to the distribution tank. P_2 is stopped at a liquid level L at which the object to be processed in the processing tank is completely immersed in the container, and then the porous processing tank is rotated intermittently or in reverse by M, and then the processing tank is rotated at low speed. Chromate treatment process in which MV_2 is opened to collect the chromate solution from the container into the chromate solution tank and shaken out. MV_3 is closed, the treatment tank is rotated at high speed by M, and H is activated to remove the remaining cleaning water. A drying process that involves shaking off and drying. Consisting of the above steps, the first, second, and third cleaning steps operate P_3 while rotating the treatment tank at low speed by the drive device M to supply cleaning water from the cleaning liquid storage tank into the container. Cleaning method 1, in which P_3 is stopped at a water level where the objects to be treated in the treatment tank are completely immersed, and MV_4 is opened to collect the cleaning waste water from the discharge pipe into the cleaning liquid storage tank, and/or MV_3 is opened to drain the cleaning water. This is carried out by cleaning method 2 in which the cleaning liquid is sprayed onto the workpiece from a cleaning liquid spraying device, but cleaning is always performed in one or more steps selected from the first cleaning step, second cleaning step, and third cleaning step. A chromate treatment method characterized by applying Method 1.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP54081052A JPS6028908B2 (en) | 1979-06-26 | 1979-06-26 | Chromate treatment device and chromate treatment method using the treatment device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP54081052A JPS6028908B2 (en) | 1979-06-26 | 1979-06-26 | Chromate treatment device and chromate treatment method using the treatment device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS565983A JPS565983A (en) | 1981-01-22 |
| JPS6028908B2 true JPS6028908B2 (en) | 1985-07-08 |
Family
ID=13735634
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP54081052A Expired JPS6028908B2 (en) | 1979-06-26 | 1979-06-26 | Chromate treatment device and chromate treatment method using the treatment device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6028908B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105506664A (en) * | 2015-12-08 | 2016-04-20 | 松阳上上德盛不锈钢有限公司 | Stainless steel tube acid pickling process making acid solutions self-circulated and washing water recyclable |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS4221694Y1 (en) * | 1966-02-12 | 1967-12-13 | ||
| CH603832A5 (en) * | 1975-08-21 | 1978-08-31 | Siemens Ag | |
| JPS5340172A (en) * | 1976-09-27 | 1978-04-12 | Ebara Corp | Synchronizing circuit for hydraulic actuators |
| FR2398124A1 (en) * | 1977-07-20 | 1979-02-16 | Neiman Sa | ELECTROLYTIC TREATMENT PROCESS AND DEVICE |
-
1979
- 1979-06-26 JP JP54081052A patent/JPS6028908B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS565983A (en) | 1981-01-22 |
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