JPH09314142A - Oil separator in pretreatment degreasing process of plating - Google Patents
Oil separator in pretreatment degreasing process of platingInfo
- Publication number
- JPH09314142A JPH09314142A JP15315296A JP15315296A JPH09314142A JP H09314142 A JPH09314142 A JP H09314142A JP 15315296 A JP15315296 A JP 15315296A JP 15315296 A JP15315296 A JP 15315296A JP H09314142 A JPH09314142 A JP H09314142A
- Authority
- JP
- Japan
- Prior art keywords
- degreasing
- tank
- plating
- aqueous solution
- component
- 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
- 238000005238 degreasing Methods 0.000 title claims abstract description 152
- 238000000034 method Methods 0.000 title claims abstract description 56
- 238000007747 plating Methods 0.000 title claims abstract description 49
- 230000008569 process Effects 0.000 title claims abstract description 37
- 238000001914 filtration Methods 0.000 claims abstract description 60
- 239000007788 liquid Substances 0.000 claims abstract description 60
- 238000005192 partition Methods 0.000 claims abstract description 30
- 239000007864 aqueous solution Substances 0.000 claims abstract description 29
- 239000000243 solution Substances 0.000 claims abstract description 17
- 238000000926 separation method Methods 0.000 claims description 26
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 14
- 238000005237 degreasing agent Methods 0.000 claims description 6
- 239000013527 degreasing agent Substances 0.000 claims description 5
- 238000007667 floating Methods 0.000 claims description 5
- 230000006872 improvement Effects 0.000 abstract description 6
- 239000003921 oil Substances 0.000 description 46
- 235000019198 oils Nutrition 0.000 description 45
- 239000003925 fat Substances 0.000 description 21
- 235000019197 fats Nutrition 0.000 description 21
- 229910052751 metal Inorganic materials 0.000 description 17
- 239000002184 metal Substances 0.000 description 17
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 15
- 239000002904 solvent Substances 0.000 description 12
- 238000005498 polishing Methods 0.000 description 11
- 238000005406 washing Methods 0.000 description 8
- 230000000694 effects Effects 0.000 description 7
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 6
- 230000007797 corrosion Effects 0.000 description 5
- 238000005260 corrosion Methods 0.000 description 5
- 239000010410 layer Substances 0.000 description 5
- 235000011121 sodium hydroxide Nutrition 0.000 description 5
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 4
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 4
- 238000007796 conventional method Methods 0.000 description 4
- 230000006866 deterioration Effects 0.000 description 4
- 239000011133 lead Substances 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- 229910052725 zinc Inorganic materials 0.000 description 4
- 239000011701 zinc Substances 0.000 description 4
- 229910052782 aluminium Inorganic materials 0.000 description 3
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 3
- 239000011248 coating agent Substances 0.000 description 3
- 238000000576 coating method Methods 0.000 description 3
- 239000000839 emulsion Substances 0.000 description 3
- 229910052742 iron Inorganic materials 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 238000012545 processing Methods 0.000 description 3
- 239000005028 tinplate Substances 0.000 description 3
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 2
- 235000019737 Animal fat Nutrition 0.000 description 2
- 229910001369 Brass Inorganic materials 0.000 description 2
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 2
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 description 2
- 230000009471 action Effects 0.000 description 2
- 239000012190 activator Substances 0.000 description 2
- 239000000956 alloy Substances 0.000 description 2
- 229910045601 alloy Inorganic materials 0.000 description 2
- 239000010951 brass Substances 0.000 description 2
- 229910052793 cadmium Inorganic materials 0.000 description 2
- BDOSMKKIYDKNTQ-UHFFFAOYSA-N cadmium atom Chemical compound [Cd] BDOSMKKIYDKNTQ-UHFFFAOYSA-N 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 2
- 230000002950 deficient Effects 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 238000005868 electrolysis reaction Methods 0.000 description 2
- 238000009713 electroplating Methods 0.000 description 2
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 description 2
- 229910052737 gold Inorganic materials 0.000 description 2
- 239000010931 gold Substances 0.000 description 2
- 229910052500 inorganic mineral Inorganic materials 0.000 description 2
- 238000007689 inspection Methods 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 238000005259 measurement Methods 0.000 description 2
- 150000002739 metals Chemical class 0.000 description 2
- 239000011707 mineral Substances 0.000 description 2
- 235000010755 mineral Nutrition 0.000 description 2
- 229910052759 nickel Inorganic materials 0.000 description 2
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 2
- 238000007517 polishing process Methods 0.000 description 2
- 238000005507 spraying Methods 0.000 description 2
- 238000004544 sputter deposition Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 239000004094 surface-active agent Substances 0.000 description 2
- VZGDMQKNWNREIO-UHFFFAOYSA-N tetrachloromethane Chemical compound ClC(Cl)(Cl)Cl VZGDMQKNWNREIO-UHFFFAOYSA-N 0.000 description 2
- 239000011135 tin Substances 0.000 description 2
- 229910052718 tin Inorganic materials 0.000 description 2
- 238000007740 vapor deposition Methods 0.000 description 2
- 235000015112 vegetable and seed oil Nutrition 0.000 description 2
- 235000019871 vegetable fat Nutrition 0.000 description 2
- AELGQPHXHKVUQK-UHFFFAOYSA-N 1,1,1,2,2,3,3,5-octachloropentane Chemical compound C(CC(C(C(Cl)(Cl)Cl)(Cl)Cl)(Cl)Cl)Cl AELGQPHXHKVUQK-UHFFFAOYSA-N 0.000 description 1
- 229910000906 Bronze Inorganic materials 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 description 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- ZOKXTWBITQBERF-UHFFFAOYSA-N Molybdenum Chemical compound [Mo] ZOKXTWBITQBERF-UHFFFAOYSA-N 0.000 description 1
- BQCADISMDOOEFD-UHFFFAOYSA-N Silver Chemical compound [Ag] BQCADISMDOOEFD-UHFFFAOYSA-N 0.000 description 1
- 239000004115 Sodium Silicate Substances 0.000 description 1
- XSTXAVWGXDQKEL-UHFFFAOYSA-N Trichloroethylene Chemical compound ClC=C(Cl)Cl XSTXAVWGXDQKEL-UHFFFAOYSA-N 0.000 description 1
- 230000004913 activation Effects 0.000 description 1
- 238000001994 activation Methods 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 235000021168 barbecue Nutrition 0.000 description 1
- 239000002585 base Substances 0.000 description 1
- 230000003796 beauty Effects 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 239000010974 bronze Substances 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 150000001768 cations Chemical class 0.000 description 1
- 239000003610 charcoal Substances 0.000 description 1
- 229910052804 chromium Inorganic materials 0.000 description 1
- 239000011651 chromium Substances 0.000 description 1
- 230000003749 cleanliness Effects 0.000 description 1
- 239000011247 coating layer Substances 0.000 description 1
- 229910017052 cobalt Inorganic materials 0.000 description 1
- 239000010941 cobalt Substances 0.000 description 1
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 description 1
- 239000004020 conductor Substances 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- KUNSUQLRTQLHQQ-UHFFFAOYSA-N copper tin Chemical compound [Cu].[Sn] KUNSUQLRTQLHQQ-UHFFFAOYSA-N 0.000 description 1
- 238000005034 decoration Methods 0.000 description 1
- 238000007598 dipping method Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 239000008151 electrolyte solution Substances 0.000 description 1
- 238000004945 emulsification Methods 0.000 description 1
- 230000001804 emulsifying effect Effects 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 239000004519 grease Substances 0.000 description 1
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 1
- 239000003350 kerosene Substances 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 239000002923 metal particle Substances 0.000 description 1
- 239000002480 mineral oil Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 229910052750 molybdenum Inorganic materials 0.000 description 1
- 239000011733 molybdenum Substances 0.000 description 1
- -1 naphtha Substances 0.000 description 1
- 238000006386 neutralization reaction Methods 0.000 description 1
- MOFOBJHOKRNACT-UHFFFAOYSA-N nickel silver Chemical compound [Ni].[Ag] MOFOBJHOKRNACT-UHFFFAOYSA-N 0.000 description 1
- 239000010956 nickel silver Substances 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 238000005554 pickling Methods 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229910052697 platinum Inorganic materials 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 230000009290 primary effect Effects 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 239000012266 salt solution Substances 0.000 description 1
- 238000005488 sandblasting Methods 0.000 description 1
- 238000007127 saponification reaction Methods 0.000 description 1
- 230000009291 secondary effect Effects 0.000 description 1
- 238000005480 shot peening Methods 0.000 description 1
- 229910052709 silver Inorganic materials 0.000 description 1
- 239000004332 silver Substances 0.000 description 1
- 239000000344 soap Substances 0.000 description 1
- 229910000029 sodium carbonate Inorganic materials 0.000 description 1
- 229940023144 sodium glycolate Drugs 0.000 description 1
- NTHWMYGWWRZVTN-UHFFFAOYSA-N sodium silicate Chemical compound [Na+].[Na+].[O-][Si]([O-])=O NTHWMYGWWRZVTN-UHFFFAOYSA-N 0.000 description 1
- 229910052911 sodium silicate Inorganic materials 0.000 description 1
- 230000003068 static effect Effects 0.000 description 1
- 238000004381 surface treatment Methods 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 239000013077 target material Substances 0.000 description 1
- 229940035339 tri-chlor Drugs 0.000 description 1
- JEJAMASKDTUEBZ-UHFFFAOYSA-N tris(1,1,3-tribromo-2,2-dimethylpropyl) phosphate Chemical compound BrCC(C)(C)C(Br)(Br)OP(=O)(OC(Br)(Br)C(C)(C)CBr)OC(Br)(Br)C(C)(C)CBr JEJAMASKDTUEBZ-UHFFFAOYSA-N 0.000 description 1
- WFKWXMTUELFFGS-UHFFFAOYSA-N tungsten Chemical compound [W] WFKWXMTUELFFGS-UHFFFAOYSA-N 0.000 description 1
- 229910052721 tungsten Inorganic materials 0.000 description 1
- 239000010937 tungsten Substances 0.000 description 1
- 239000008158 vegetable oil Substances 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
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
- C23G—CLEANING OR DE-GREASING OF METALLIC MATERIAL BY CHEMICAL METHODS OTHER THAN ELECTROLYSIS
- C23G1/00—Cleaning or pickling metallic material with solutions or molten salts
- C23G1/36—Regeneration of waste pickling liquors
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Removal Of Floating Material (AREA)
- Cleaning And De-Greasing Of Metallic Materials By Chemical Methods (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】メッキ加工の前処理としてワ
ークに行われる脱脂工程に用いられる油分離装置に関す
る。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an oil separation device used in a degreasing process performed on a work as a pretreatment for plating.
【0002】[0002]
【従来の技術】メッキは金属表面の美しさ,耐食性,堅
さを増すなどのため他の金属で被覆する方法及び生成し
た金属被覆層をいう。装飾用のメッキには、金,銀,白
金,黄銅合金などがもっぱら使用されているが、耐食性
や堅さを増すための物にはクロム,ニッケルなどのメッ
キが施されるが、鉄板に錫をメッキしたブリキや亜鉛を
メッキしたトタンなどが知られている。メッキ加工方法
には、電気メッキ法,溶融メッキ法,金属溶射法,真空
メッキ法があるが、これらのメッキ加工方法について簡
単に説明する。電気メッキ法は電気分解の原理を応用し
て電導体にメッキを施す方法で、メッキされる金属を陰
極とし被覆金属を陽極とした電気回路を塩類溶液の電解
液に浸してメッキ処理を行うもので、鉛,炭素などの不
溶解性陽極を用いることもある。被覆金属としては、
金,鉛,銅,ニッケル,亜鉛,錫,コバルト,カドミウ
ム,タングステン,モリブデンなどの純金属の他に、真
鍮,青銅,洋白などの合金も用いられる。溶融メッキ法
は溶融した金属中に被メッキ金属を浸漬して行う方法で
あるが、溶融点の比較的低い亜鉛,錫,鉛,カドミウ
ム,アルミニウムなどが用いられる。トタン板やブリキ
板はこの方法で作られることが多い。金属溶射法は溶融
状態の金属を圧風によってふきつける方法である。真空
メッキ法は金属蒸着法とスパッタリングがあるが、金属
蒸着法は真空中で金属を加熱し、その蒸気を他の物体に
付着させるもので、プラスチック,ガラスにアルミニウ
ム,鉛などをメッキするのはその一例である。スパッタ
リングは真空中の電極間に電圧をかけると、残留気体が
電離して陽イオンが陰極に衝突し、陰極金属粒子を飛散
させるので、これを目的物に付着させる。非電導性の物
体メッキ下地として用いられる。2. Description of the Related Art Plating refers to a method of coating with another metal and a formed metal coating layer in order to enhance the beauty, corrosion resistance and hardness of the metal surface. Gold, silver, platinum, brass alloys, etc. are mainly used for decoration plating, but chromium, nickel, etc. are plated for corrosion resistance and hardness, but iron plates are tinned. Tinplate plated with zinc and galvanized galvanized galvanized iron are known. The plating method includes an electroplating method, a hot dip plating method, a metal spraying method, and a vacuum plating method. These plating processing methods will be briefly described. The electroplating method is a method of plating an electric conductor by applying the principle of electrolysis, in which an electric circuit in which the metal to be plated is the cathode and the coating metal is the anode is immersed in an electrolyte solution of a salt solution to perform the plating treatment. Therefore, an insoluble anode such as lead or carbon may be used. As the coating metal,
Besides pure metals such as gold, lead, copper, nickel, zinc, tin, cobalt, cadmium, tungsten and molybdenum, alloys such as brass, bronze and nickel silver are also used. The hot dipping method is a method of immersing a metal to be plated in a molten metal, and zinc, tin, lead, cadmium, aluminum or the like having a relatively low melting point is used. Tin plate and tin plate are often made by this method. The metal spraying method is a method in which a molten metal is wiped with pressurized air. The vacuum plating method includes a metal vapor deposition method and a sputtering method. The metal vapor deposition method heats a metal in a vacuum and causes the vapor to adhere to another object. Plating aluminum or lead on plastic or glass is not recommended. This is an example. In sputtering, when a voltage is applied between electrodes in a vacuum, the residual gas is ionized and the cations collide with the cathode, causing the metal particles of the cathode to scatter, and these are attached to the target. Used as a non-conductive object plating base.
【0003】メッキ作業の工程は工程順に分けると、研
磨,前処理,メッキ,後処理,乾燥の5工程が行われる
が、この内メッキ処理した製品のクオリティに大きく影
響する工程が研磨と前処理である。この工程は製品の材
質,表面状態,形状などにより異なるが、例えば、鉄製
品の場合だと素材,研磨,脱脂,水洗,酸洗,水洗,中
和,水洗,,活性化,水洗,メッキ,水洗,乾燥という
工程をとる。この内、研磨工程はメッキする製品の表面
を研磨材で磨いてメッキに適した表面に仕上げること
で、研磨法には、グラインダ掛け,炭トギ,ヘラ,ミガ
キ,ラッピング,バフ研磨,ベルト研磨,回転研磨,振
動研磨等が一般的であるが、一部ではサンドブラスト,
液体ホーニング,ショットピーニング,電解,化学研磨
等を用いた研磨も行われている。一方、前処理工程は製
品についた油脂,サビ,キズなどの汚れを除去して表面
をメッキに最も適した状態にする工程をいう。具体的に
は、メッキを施すワークの表面に付着した動物性油脂,
植物性油脂及び鉱物性油脂等の有機質の汚れや無機質な
汚れ或いは有機質・無機質混合物の汚れを溶剤脱脂,乳
化脱脂,アルカリ脱脂,電解脱脂,超音波脱脂,機械脱
脂等の方法で脱脂処理することであるが、これらについ
て簡単に説明する。 溶剤脱脂は有機溶剤を用いてメッキ素材の油性汚れを
溶解させ、除去する方法で、水洗いで完全に除去できな
い油性の汚れを水洗いの予備脱脂として行われている。
脱脂溶剤としては、ガソリン,ナフサ,石油,四塩化炭
素,アセトン,トリクロル,エチレン,パークロルエチ
レン,メチレンクロライド,等が使用されている。 乳化脱脂は、界面活性剤・溶剤・水からなるエマルジ
ョン脱脂剤を用いてメッキ素材の油性汚れを溶解・乳化
させて除去する方法で、これも水洗いの予備脱脂として
行われている。溶剤としては、ケロシンまたはトリクレ
ンに界面活性剤を少量添加して使用されている。 アルカリ脱脂は、ケン化性油脂が付着した製品をアル
カリ溶剤につけると、アルカリとケン化性油脂が結合し
て水溶性の石ケンができる。このケン化作用を利用して
製品に付着したケン化性油脂を製品から脱脂させる方法
で、使用されるアルカリ脱脂剤はカセイソーダ,炭酸ナ
トリウム,ケイ酸ソーダ,グリコール酸ソーダ等が用い
られている。 電解脱脂は予備洗浄でも製品の表面に僅かに残留した
汚れを除去する方法で、溶剤脱脂,乳剤脱脂及びアルカ
リ脱脂の後に行っている。 超音波脱脂は、溶剤脱脂,アルカリ脱脂,電解脱脂に
併用して洗浄効果を高めるために行われるもので、亜鉛
ダイキャスト,アルミニウム等の非鉄金属の脱脂に多く
用いられている。When the plating process is divided into process steps, five processes of polishing, pretreatment, plating, posttreatment, and drying are carried out. Of these, the processes that greatly affect the quality of the plated product are polishing and pretreatment. Is. This process varies depending on the product material, surface condition, shape, etc. For example, in the case of iron products, material, polishing, degreasing, washing, pickling, washing, neutralization, washing, activation, washing, plating, Take steps of washing with water and drying. Among these, in the polishing process, the surface of the product to be plated is polished with an abrasive to finish the surface suitable for plating. The polishing method includes grinder hanging, charcoal barbecue, spatula, brush, lapping, buff polishing, belt polishing, Rotational polishing, vibration polishing, etc. are common, but in some cases sandblasting,
Polishing using liquid honing, shot peening, electrolysis, chemical polishing, etc. is also performed. On the other hand, the pretreatment process is a process for removing stains such as grease, rust, and scratches on the product to make the surface most suitable for plating. Specifically, animal fats and oils attached to the surface of the work to be plated,
Degreasing organic and inorganic stains such as vegetable oils and mineral oils or stains of organic and inorganic mixtures by solvent degreasing, emulsion degreasing, alkaline degreasing, electrolytic degreasing, ultrasonic degreasing, mechanical degreasing, etc. However, these are briefly explained. Solvent degreasing is a method of dissolving and removing oily stains on a plating material using an organic solvent, and is performed as preliminary degreasing for washing oily stains that cannot be completely removed by washing with water.
As the degreasing solvent, gasoline, naphtha, petroleum, carbon tetrachloride, acetone, trichlor, ethylene, perchlorethylene, methylene chloride, etc. are used. Emulsification degreasing is a method of dissolving and emulsifying oily stains on a plating material by using an emulsion degreasing agent composed of a surfactant, a solvent and water, and this is also performed as preliminary degreasing for washing with water. As a solvent, kerosene or trichlene with a small amount of added surfactant is used. In alkaline degreasing, when a product to which a saponifying oil / fat is attached is dipped in an alkaline solvent, the alkali and the saponifying oil / fat are combined to form a water-soluble soap. In this method of saponifying fats and oils adhering to products by utilizing this saponification action, caustic soda, sodium carbonate, sodium silicate, sodium glycolate and the like are used as alkaline degreasing agents. Electrolytic degreasing is a method for removing a small amount of stains remaining on the surface of the product even in preliminary cleaning, and is performed after solvent degreasing, emulsion degreasing and alkaline degreasing. Ultrasonic degreasing is performed in combination with solvent degreasing, alkaline degreasing, and electrolytic degreasing to enhance the cleaning effect, and is often used for degreasing nonferrous metals such as zinc die cast and aluminum.
【0004】次に、従来技術としての脱脂工程の一例に
ついて説明する。図1及び図2は従来から使用されてい
る溶剤脱脂装置の概要である。従来装置としての溶剤脱
脂装置は、図1に示した如く、一定の水位を超えると水
面から外部に溢れ出るオーバーフロー部1を側面に備え
た脱脂処理用タンク2とオーバーフロー部1直下に備え
た濾過タンク3から構成され、更に、濾過タンク3の液
槽内部には、上面開口部から液面に突設した上部仕切板
3aと液槽底面から上方に突設した下部仕切板3bとを
1濾過ユニットとして1組以上設けられている。この
内、濾過タンク3の底部からは、図2に示した如く、ポ
ンプ4及びリタンーバルブ5を介して溶液循環パイプ6
が備えられていて、溶液循環パイプ6の先端放出口6a
から脱脂処理用タンク2に蓄液されている脱脂処理水溶
液Aの液面に放出するようになっている。この構成によ
り、従来のアルカリ脱脂装置は、脱脂処理用タンク2と
濾過タンク3の内部にかせいソーダ(水酸化ナトリウ
ム)と活性剤を混合した脱脂剤を水に溶かした脱脂処理
水溶液Aを投入し、図1に示した様にプレス加工や研磨
工程で動物性油脂油,植物性油脂及び鉱物性油脂等の有
機質・無機質・或いは有機質無機質混合物等の油脂成分
が塗布されたワーク7を脱脂処理用タンク2の内部に投
入する。すると、ワーク7に付着した油脂成分Bは、脱
脂処理水溶液Aの脱脂効果によって浮遊し、図2に示し
た如く、液面に油脂層Cを作ることになる。そこで、こ
の脱脂処理水溶液Aの上面に浮遊した油脂層Cを、オー
バーフロー部1を介して濾過タンク3にかき出して排除
する。一方、オーバーフロー部1から濾過タンク3に排
出された脱脂処理排出液は、図2に示した如く、濾過タ
ンク3の内部に設けられた1濾過ユニットの上部仕切板
3aと下部仕切板3bとを通過することで、脱脂処理排
出液に含まれた油脂成分は、濾過タンク3の液面に突出
した上部仕切板3a,3cと濾過タンクの内壁面で仕切
られた液面D1,D2に堆積するとしている。Next, an example of a conventional degreasing process will be described. 1 and 2 show an outline of a solvent degreasing device which has been conventionally used. As shown in FIG. 1, a solvent degreasing apparatus as a conventional apparatus includes a degreasing treatment tank 2 having an overflow portion 1 on the side surface that overflows from the water surface to the outside when a certain water level is exceeded, and a filtration provided immediately below the overflow portion 1. The tank 3 is composed of an upper partition plate 3a projecting from the upper surface opening to the liquid surface and a lower partition plate 3b projecting upward from the liquid tank bottom into one inside the liquid tank of the filtration tank 3. One or more sets are provided as a unit. Among these, as shown in FIG. 2, from the bottom of the filtration tank 3, a solution circulation pipe 6 is provided via a pump 4 and a return valve 5.
Is provided and the tip discharge port 6a of the solution circulation pipe 6 is provided.
Is discharged to the liquid surface of the degreasing treatment aqueous solution A stored in the degreasing treatment tank 2. With this configuration, in the conventional alkaline degreasing device, the degreasing treatment aqueous solution A prepared by dissolving the degreasing agent obtained by mixing the caustic soda (sodium hydroxide) and the activator in water is introduced into the degreasing treatment tank 2 and the filtration tank 3. As shown in FIG. 1, a work 7 to which a fat component such as an organic / inorganic substance such as an animal fat / oil oil, a vegetable fat / oil and a mineral fat / oil or an organic / inorganic mixture is applied by depressurization or polishing is used for degreasing treatment. Put in the tank 2. Then, the fat and oil component B attached to the work 7 floats due to the degreasing effect of the degreasing treatment aqueous solution A, and as shown in FIG. 2, an oil and fat layer C is formed on the liquid surface. Therefore, the oil / fat layer C floating on the upper surface of the degreasing-treated aqueous solution A is scraped out to the filtration tank 3 via the overflow portion 1 and eliminated. On the other hand, the degreasing treatment discharge liquid discharged from the overflow section 1 to the filtration tank 3 is, as shown in FIG. 2, separated into the upper partition plate 3a and the lower partition plate 3b of one filtration unit provided inside the filtration tank 3. By passing, the fat and oil component contained in the degreasing treatment discharge liquid is accumulated on the upper partition plates 3a and 3c protruding to the liquid surface of the filtration tank 3 and the liquid surfaces D1 and D2 partitioned by the inner wall surface of the filtration tank. I am trying.
【0005】[0005]
【発明が解決しようとする課題】ところが、上記従来の
技術では、オーバーフロー部1から濾過タンク3に投下
された脱脂処理排出液は、液体の落下する衝撃によって
上部仕切板3aの板面で形成される液面D1に大量のフ
クレを発生させるため、脱脂処理水排出液から濾過すべ
き油脂成分が液面に分離することなく濾過タンク3の内
部を流れてしまい最初の濾過ユニットの液面D1には実
質上油脂成分が濾過されない。更に、上部仕切板3aの
板面に沿って流入した脱脂処理排出液も、濾過タンク3
の底板に当たって横方向の流れとなり、矢印aに示した
様に下部仕切板3bの板面に当たってせき止められるこ
とになるため、濾過タンク3内に投入されている脱脂処
理排出液は、矢印bに示した様に上層流から下部仕切板
3bの上端辺を蛇行して次の濾過ユニットを形成する上
部仕切板3c側に溢れ出ることになる。しかも、この上
部仕切板3cの板面で形成される液面D2には下流側か
らポンプ4による強制的な循環流が作られるため、一
旦、上部仕切板3cの板面で形成される液面D2に堆積
した油脂成分が、ポンプ4による急激な吸い込み流によ
って液面D2の静止状態が妨げられ、再度脱脂処理排出
液の流れに吸収されてしまうといった濾過効率の極めて
悪い致命的な問題があった。そこで、本発明はこれらの
従来技術の問題点を解決するために成されたものであ
り、メッキ工程における前処理工程の脱脂処理水溶液の
濾過処理効率を飛躍的に向上させるのみならず脱脂処理
水溶液の消費量の節約,装置全体のクリーン度の向上,
作業性の向上を達成することを第1の目的し、更には、
メッキ処理後のメッキ皮膜のハガレ,ワークとメッキ皮
膜との間のフクレの発生,艶の低下,メッキの不均一等
と言った製品のクオリティを低下させる要因を排除する
と共に、ピンホールの発生を抑制して耐食性を向上させ
ることを第2の目的としている。However, in the above-mentioned conventional technique, the degreasing treatment discharge liquid dropped from the overflow portion 1 to the filtration tank 3 is formed on the plate surface of the upper partition plate 3a by the impact of dropping the liquid. Since a large amount of blisters are generated on the liquid surface D1 that flows, the oil and fat components to be filtered from the degreased water discharge liquid flow through the inside of the filtration tank 3 without separating into the liquid surface, and then on the liquid surface D1 of the first filtration unit. Substantially no oil and fat components are filtered. Furthermore, the degreasing treatment discharge liquid that has flown along the plate surface of the upper partition plate 3a is also filtered by
Since it will flow laterally when hitting the bottom plate, and will be stopped by hitting the plate surface of the lower partition plate 3b as indicated by arrow a, the degreasing treatment discharge liquid that has been put into the filtration tank 3 is indicated by arrow b. As described above, the upper flow of the lower partition plate 3b meanders from the upper layer flow and overflows to the upper partition plate 3c side forming the next filtration unit. Moreover, since a forced circulating flow is generated by the pump 4 from the downstream side on the liquid surface D2 formed by the plate surface of the upper partition plate 3c, the liquid surface formed by the plate surface of the upper partition plate 3c once There is a fatal problem that the filtration efficiency is extremely poor, because the oil and fat components accumulated on D2 are absorbed by the flow of the degreasing process discharge liquid again because the static state of the liquid surface D2 is hindered by the rapid suction flow by the pump 4. It was Therefore, the present invention has been made to solve the problems of these conventional techniques, and not only dramatically improves the filtration treatment efficiency of the degreasing aqueous solution in the pretreatment step in the plating step, but also the degreasing aqueous solution. Saving of consumption, improvement of cleanliness of the whole equipment,
The first purpose is to achieve improvement in workability, and further,
It eliminates the factors that deteriorate the product quality, such as peeling of the plated film after plating, blistering between the work and the plated film, loss of gloss, uneven plating, and the occurrence of pinholes. The second purpose is to suppress and improve the corrosion resistance.
【0006】[0006]
【課題を解決するための手段】上記目的を達成するため
に成された本発明は、メッキ加工の前処理工程として行
われる脱脂工程で用いられれ装置であって、脱脂剤を一
定の濃度で溶融させた脱脂処理水溶液を満たし、被脱脂
部材を投入して脱脂処理をおこなう脱脂処理槽と、当該
脱脂処理槽の内壁部所定の位置に設けた脱脂処理水溶液
放出部と、上記脱脂処理槽の胴部上面所定の位置に開口
を設け、脱脂処理水溶液の水面に浮遊した脱脂成分と溢
れた脱脂処理水溶液を外部に排除するオーバーフロー部
と、当該オーバーフロー部下部近傍に設け、オーバーフ
ロー部から排出された脱脂成分が混合した脱脂処理水溶
液を濾過する脱脂成分濾過槽と、当該脱脂成分濾過槽で
濾過処理されて排出された脱脂処理水溶液を上記脱脂処
理槽の脱脂処理水溶液放出部に循環させる循環経路と、
当該循環経路に介装されたポンプと、当該ポンプに並装
されたリターンバルブとから成るメッキ加工の前処理脱
脂工程における油分離装置において、脱脂成分濾過槽に
は、当該脱脂成分濾過槽の上面部から底部にかけて突設
し、その下端辺は液槽底部より所定の液体流入開口部が
形成されるように形成した仕切板を、当該脱脂成分濾過
槽の長手方向に所定の間隔で複数設けたことを特徴とす
るメッキ加工の前処理脱脂工程における油分離装置を要
旨としている。脱脂成分濾過槽の内部に設けた仕切板に
よって底部に形成される液体流入開口部は、脱脂成分濾
過槽の短手面の内壁面の面積の2割程度の面積とすると
良い。The present invention, which has been made to achieve the above object, is an apparatus used in a degreasing process performed as a pretreatment process for plating, in which a degreasing agent is melted at a constant concentration. The degreasing treatment tank that fills the degreasing treatment aqueous solution and performs the degreasing treatment by inserting the member to be degreased, the inner wall portion of the degreasing treatment tank, the degreasing treatment aqueous solution discharge portion provided at a predetermined position, and the body of the degreasing treatment tank. The upper surface of the part is provided with an opening at a predetermined position to remove the degreasing component floating on the water surface of the degreasing aqueous solution and the overflowing degreasing aqueous solution to the outside, and an overflow part provided near the lower part of the overflowing part, and the degreasing discharged from the overflowing part. A degreasing component filtration tank for filtering the degreasing-treated aqueous solution in which the components are mixed, and a degreasing treatment aqueous solution filtered and discharged in the degreasing-component filtration tank are degreased treated water in the degreasing treatment tank. A circulation path for circulating the liquid discharge portion,
In an oil separation device in a pretreatment degreasing process of plating, which includes a pump provided in the circulation path and a return valve provided in parallel with the pump, the degreasing component filtration tank has an upper surface of the degreasing component filtration tank. A plurality of partition plates formed so as to project from the portion to the bottom, and the lower end side thereof is formed so that a predetermined liquid inflow opening is formed from the bottom of the liquid tank, and a plurality of partition plates are provided at predetermined intervals in the longitudinal direction of the degreasing component filtration tank. The gist is an oil separation device in the pretreatment degreasing step of the plating process, which is characterized in that The liquid inflow opening formed at the bottom by the partition plate provided inside the degreasing component filtration tank may have an area of about 20% of the area of the inner wall surface of the short side surface of the degreasing component filtration tank.
【0007】[0007]
【発明の実施の形態】本発明の実施例について図面に基
づき説明する。図3(a)は本発明のメッキ加工の前処
理脱脂工程における油分離装置を適用した実施例である
油分離装置の内部構造を表した正面図、図3(b)は同
実施例の油分離装置の主要部分を表した平面図である。
本実施例の油分離装置は、図3(a)に示した如く、一
定の水位を超えると水面から外部に溢れ出るオーバーフ
ロー部10をタンク側面に備えた脱脂処理用タンク11
とオーバーフロー部10直下に備えた濾過タンク12と
から成り、更に、濾過タンク12の底部から脱脂処理用
タンク11の内部に脱脂処理液を循環させる溶液循環パ
イプ13,溶液循環パイプ13に直列に介装されている
ポンプ14,ポンプ14に連通している溶液循環パイプ
13に並列に連通したリタンーバルブ15,及び溶液循
環パイプ13の先端に取り付けられている脱脂処理液放
出ノズル13aとで構成されている。この内、濾過タン
ク12の内部には、図3(b)に示した如く、濾過タン
ク12の長尺側の液槽内壁面から対抗する長尺側の液槽
内壁面に対してほぼ直角状の仕切板12aが設けられ、
この仕切板12aが濾過タンク12の長手方向に一定の
間隔で複数枚(本実施例では7枚とした。)取り付けら
れている。尚、この仕切板12aは、図3(a)で明ら
かな様に濾過タンク12の底部に液槽容積の20パーセ
ント程度の流通空間を形成するように上部開口面から底
部にかけて突設されている。BEST MODE FOR CARRYING OUT THE INVENTION Embodiments of the present invention will be described with reference to the drawings. FIG. 3 (a) is a front view showing the internal structure of an oil separation device that is an embodiment to which the oil separation device is applied in the pretreatment degreasing step of the plating process of the present invention, and FIG. 3 (b) is the oil of the same embodiment. It is a top view showing the principal part of a separation device.
As shown in FIG. 3 (a), the oil separation apparatus of this embodiment has a degreasing tank 11 provided with an overflow portion 10 on the side surface of the tank, which overflows from the water surface to the outside when the water level exceeds a certain level.
And a filtration tank 12 provided directly below the overflow section 10, and further, a solution circulation pipe 13 for circulating the degreasing treatment liquid from the bottom of the filtration tank 12 to the inside of the degreasing treatment tank 11, and a solution circulation pipe 13 connected in series to the solution circulation pipe 13. It is composed of a pump 14 mounted, a return valve 15 communicating in parallel with the solution circulation pipe 13 communicating with the pump 14, and a degreasing treatment liquid discharge nozzle 13a attached to the tip of the solution circulation pipe 13. . Of these, inside the filtration tank 12, as shown in FIG. 3B, a substantially right-angled shape is formed from the long-side liquid tank inner wall surface of the long-side liquid tank inner wall surface that opposes the long-side liquid tank inner wall surface. A partition plate 12a of
A plurality of partition plates 12a are attached in the longitudinal direction of the filtration tank 12 at regular intervals (7 in this embodiment). As is apparent from FIG. 3A, the partition plate 12a is provided so as to project from the upper opening surface to the bottom so as to form a flow space of about 20% of the liquid tank volume at the bottom of the filtration tank 12. .
【0008】上記構成からなる本実施例の油分離装置の
作用について図面に基づき説明する。図4は本実施例の
油分離装置の作用説明図である。まず、かせいソーダ
(水酸化ナトリウム)と活性剤を混合した脱脂処理水溶
液Aを脱脂処理用タンク11と濾過タンク12及び溶液
循環パイプ13の内部に投入する。次に、プレス加工や
研磨工程で動物性油脂,植物性油脂及び鉱物性油脂等の
有機質・無機質・或いは有機質無機質混合物等の油脂成
分が塗布されたワークを投入し、ワークに付着した油脂
成分が脱脂処理水溶液の液面に浮遊して油脂層Cが形成
されるようにする。この状態で、図3(a)に示したポ
ンプ14を駆動して脱脂処理水溶液の循環運転を開始す
る。すると、脱脂処理用タンク11の上面に突出した脱
脂処理液放出ノズル13aから循環液が脱脂処理水溶液
Aの液面に放水され、脱脂処理水溶液の液面に浮遊して
油脂層Cは循環流によって次第にオーバーフロー部10
に押し出されて、濾過タンク12の最初の仕切板12a
で形成されている液面F1に落下する。そして、この落
下した脱脂処理排出液は、矢印16に示した様に濾過タ
ンク12の底部を流れて溶液循環パイプ13に流れ込
む。この間に、脱脂処理排出液に含まれていた油脂成分
は濾過タンク12の底部を一定の流速で流れる本流か
ら、矢印17に示した様に分離して仕切板12aで区画
されている液面F1から液面F8へと順次浮遊して堆積
されることになる。この作用により、本実施例の油分離
装置は次に示した様な数々の効果を得る事に成功した。 オーバーフロー部10から排出された脱脂処理排出液
を濾過タンクの内部で一定の流速にて循環できるように
したことで、脱脂処理排出液から脱脂成分の分離・浮遊
が容易になり、濾過タンクの濾過処理効率が飛躍的に向
上した。 濾過タンク12に設けられた7枚の仕切板12aで区
画される8カ所の液面F1から液面F8には、脱脂処理
工程の循環運転が開始されると、オーバーフロー部10
の近傍の液面F1から溶液循環パイプ13近傍の液面F
8にかけて脱脂成分が順次堆積するため、堆積した油脂
成分の量の把握や取り除く時期が容易に判断できるよう
になり、装置の保守・点検作業の効率が向上する。 本実施例の油分離装置は、小型の装置から大型プラン
トまでのどのような規模の装置での容易に適用させて同
様の効果がえられるため、極めて応用範囲の広い経済的
な装置を実現した。 本装置の導入により、メッキ処理後のメッキ皮膜のハ
ガレ,ワークとメッキ皮膜との間のフクレの発生,艶の
低下,メッキの不均一などの製品のクオリティを低下さ
せる要因を排除することが可能になる。 本装置の導入により、ピンホールの発生を抑制して耐
食性を向上させることにが可能になる。 本装置の導入により、工場内をクリーンな状態に保つ
事ができようになった。 本装置の導入により、メッキ処理後の製品に発生する
製品の品質の低下を皆無にして生産中の製品に多数の不
良品を発生させてメッキ工業にコスト的に大きなダメー
ジを与えることが殆どなくなった。The operation of the oil separating apparatus of the present embodiment having the above structure will be described with reference to the drawings. FIG. 4 is an explanatory view of the operation of the oil separation device of this embodiment. First, a degreasing treatment aqueous solution A in which caustic soda (sodium hydroxide) and an activator are mixed is put into the degreasing treatment tank 11, the filtration tank 12, and the solution circulation pipe 13. Next, in the pressing or polishing process, the work is coated with the oil / fat component such as the organic / inorganic / organic / inorganic mixture such as animal fat, vegetable fat and mineral fat, and the fat component adhering to the work is removed. The oil / fat layer C is formed so as to float on the liquid surface of the degreasing-treated aqueous solution. In this state, the pump 14 shown in FIG. 3A is driven to start the circulation operation of the degreasing treatment aqueous solution. Then, the circulating liquid is discharged from the degreasing treatment liquid discharge nozzle 13a protruding on the upper surface of the degreasing treatment tank 11 to the liquid surface of the degreasing treatment aqueous solution A, floating on the liquid surface of the degreasing treatment aqueous solution A, and the oil layer C is circulated. Overflow part 10 gradually
The first partition plate 12a of the filtration tank 12 that has been pushed out to
It falls on the liquid surface F1 formed by. Then, the dropped degreasing treatment discharge liquid flows through the bottom portion of the filtration tank 12 and into the solution circulation pipe 13 as shown by an arrow 16. During this period, the oil and fat components contained in the degreasing treatment discharge liquid are separated from the main stream flowing at a constant flow rate through the bottom of the filtration tank 12 as shown by arrow 17, and are separated by the partition plate 12a to form the liquid level F1. From the liquid surface to the liquid surface F8 are sequentially floated and deposited. Due to this action, the oil separation apparatus of this embodiment succeeded in obtaining various effects as shown below. By allowing the degreasing treatment discharge liquid discharged from the overflow section 10 to be circulated at a constant flow rate inside the filtration tank, separation and suspension of the degreasing components from the degreasing treatment discharge liquid are facilitated, and filtration of the filtration tank is facilitated. The processing efficiency has improved dramatically. When the circulation operation of the degreasing process is started from the eight liquid levels F1 to F8 divided by the seven partition plates 12a provided in the filtration tank 12, the overflow section 10
From the liquid level F1 near the liquid circulation pipe 13 to the liquid level F near the solution circulation pipe 13
Since the degreasing components are sequentially deposited over 8, it becomes possible to easily grasp the amount of the accumulated fats and oils components and to determine the removal time, and improve the efficiency of the maintenance and inspection work of the device. The oil separation device of the present embodiment can be easily applied to any size device from a small device to a large plant and the same effect can be obtained, so that an economical device having a wide range of applications is realized. . By introducing this device, it is possible to eliminate factors that deteriorate product quality, such as peeling of the plated film after plating, generation of blisters between the work and the plated film, deterioration of gloss, and uneven plating. become. By introducing this device, it becomes possible to suppress the generation of pinholes and improve the corrosion resistance. The introduction of this device has made it possible to keep the factory clean. With the introduction of this device, there is almost no deterioration in the quality of the product after plating, and many defective products are produced in the process of production, and it is almost impossible to damage the plating industry costly. It was
【0009】尚、本発明のメッキ加工の前処理脱脂工程
における油分離装置は上記実施例の油分離装置にのみ限
定されるものではなく、本発明の技術思想を適用した多
様なバリエーションが考えられる。例えば、濾過タンク
12の内部を流れる脱脂処理排出液の流速を最適な状態
にするために、濾過タンク12の内部に流速測定センサ
ーを設け、この流速測定センサーからの信号をマイクロ
コンピュータに読み込む。そして、マイクロコンピュー
タは予め記憶されているプログラムのアルゴリズムに従
ってリタンーバルブ15の開度をフィードバック制御す
る全自動油分離装置に適用することも可能である。The oil separation device in the pretreatment degreasing step of the plating process of the present invention is not limited to the oil separation device of the above embodiment, and various variations applying the technical idea of the present invention are conceivable. . For example, in order to optimize the flow rate of the degreasing treatment effluent flowing through the inside of the filtration tank 12, a flow rate measurement sensor is provided inside the filtration tank 12, and the signal from this flow rate measurement sensor is read into the microcomputer. The microcomputer can also be applied to a fully automatic oil separation device that feedback-controls the opening degree of the return valve 15 according to an algorithm of a program stored in advance.
【0010】[0010]
【発明の効果】以上、詳述したように本発明のメッキ加
工の前処理脱脂工程における油分離装置は、メッキ加工
の前処理工程として行われる脱脂工程で用いられれ装置
であって、脱脂剤を一定の濃度で溶融させた脱脂処理水
溶液を満たし、被脱脂部材を投入して脱脂処理をおこな
う脱脂処理槽と、脱脂処理槽の内壁部所定の位置に設け
た脱脂処理水溶液放出部と、脱脂処理槽の胴部上面所定
の位置に開口を設け、脱脂処理水溶液の水面に浮遊した
脱脂成分と溢れた脱脂処理水溶液を外部に排除するオー
バーフロー部と、オーバーフロー部下部近傍に設け、オ
ーバーフロー部から排出された脱脂成分が混合した脱脂
処理水溶液を濾過する脱脂成分濾過槽と、脱脂成分濾過
槽で濾過処理されて排出された脱脂処理水溶液を脱脂処
理槽の脱脂処理水溶液放出部に循環させる循環経路と、
循環経路に介装されたポンプと、当該ポンプに並装され
たリターンバルブとから成るメッキ加工の前処理脱脂工
程における油分離装置の脱脂成分濾過槽には、脱脂成分
濾過槽の上面部から底部にかけて突設し、その下端辺は
液槽底部より所定の液体流入開口部が形成されるように
形成した仕切板を、脱脂成分濾過槽の長手方向に所定の
間隔で複数設け、更に脱脂成分濾過槽の内部に設けた仕
切板によって底部に形成される液体流入開口部は、脱脂
成分濾過槽の短手面の内壁面の面積の2割程度の面積と
したことで、本発明は次の効果を得ることができる。 (1)脱脂処理排出液から脱脂成分の分離・浮遊が容易
になり、濾過タンクの濾過処理効率が飛躍的に向上し
た。 (2)堆積した油脂成分の量の把握や取り除く時期が容
易に判断できるようになり、装置の保守・点検作業の効
率が向上した。 (3)排水処理工程に持ち込まれれる油分が低減し、B
OD低減期待がもてる。 (4)小型の装置から大型プラントまでのどのような規
模の装置での容易に適用させて同様の効果がえられるた
め、極めて応用範囲の広い経済的な装置を実現した。ま
た、本発明の導入により、二次的に発生する効果として
は、 (5)メッキ処理後のメッキ皮膜のハガレ,ワークとメ
ッキ皮膜との間のフクレの発生,艶の低下,メッキの不
均一などの製品のクオリティを低下させる要因を排除す
ることが可能になる。 (6)ピンホールの発生を抑制して耐食性を向上させる
ことにが可能になる。 (7)工場内をクリーンな状態に保つ事ができようにな
った。 (8)メッキ処理後の製品に発生する製品の品質の低下
を皆無にして生産中の製品に多数の不良品を発生させて
金属表面処理工業にコスト的に大きなダメージを与える
ことが殆どなくなった。 と言った、一次的及び二次的な数々の効果を得ることに
成功した画期的な発明であり、業界に与える技術的な効
果は絶大であり産業界全体に与える恩恵も計り知れない
ものがある。As described above in detail, the oil separation device in the pretreatment degreasing process of the plating process of the present invention is a device used in the degreasing process performed as the pretreatment process of the plating process, and the degreasing agent is used. A degreasing treatment tank that fills the degreasing treatment solution melted at a certain concentration and performs the degreasing treatment by introducing the degreasing target material, the inner wall of the degreasing treatment tank, and the degreasing treatment solution discharge part provided at a predetermined position, and the degreasing treatment An opening is provided at a predetermined position on the upper surface of the body of the tank to provide an overflow part for removing the degreasing component floating on the water surface of the degreasing aqueous solution and the overflowing degreasing aqueous solution to the outside, and an overflow part near the lower part of the overflowing part for discharging from the overflow part. The degreasing component filtering tank that filters the degreasing-treated aqueous solution mixed with the degreasing component and the degreasing-treated aqueous solution that has been filtered by the degreasing component filtering tank and discharged A circulation path for circulating the liquid discharge portion,
The degreasing component filtration tank of the oil separation device in the pretreatment degreasing process for plating, which includes a pump installed in the circulation path and a return valve arranged in parallel with the pump, includes a top portion to a bottom portion of the degreasing component filtration tank. A plurality of partition plates are provided so as to project from the bottom of the liquid tank so that a predetermined liquid inflow opening is formed from the bottom of the liquid tank, and a plurality of partition plates are provided at predetermined intervals in the longitudinal direction of the degreasing component filtration tank. The liquid inflow opening formed at the bottom by the partition plate provided inside the tank is about 20% of the area of the inner wall surface of the short side surface of the degreasing component filtration tank, and the present invention has the following effects. Can be obtained. (1) Degreasing treatment It becomes easier to separate and float degreasing components from the discharged liquid, and the filtration treatment efficiency of the filtration tank is dramatically improved. (2) The amount of accumulated oil and fat components can be easily grasped and the time to remove it can be easily determined, and the efficiency of equipment maintenance and inspection work has improved. (3) Oil content brought into the wastewater treatment process is reduced, and B
We can expect OD reduction. (4) Since the same effect can be obtained by easily applying to any size device from a small device to a large plant, an economical device having a very wide range of application is realized. In addition, as a result of secondary introduction of the present invention, (5) peeling of the plating film after plating, generation of blisters between the work and the plating film, deterioration of gloss, and nonuniform plating It becomes possible to eliminate the factors that deteriorate the quality of the product such as. (6) It becomes possible to suppress the generation of pinholes and improve the corrosion resistance. (7) It has become possible to keep the factory clean. (8) There is almost no deterioration in the quality of the product after the plating treatment, and a large number of defective products are generated in the product under production, and the cost of the metal surface treatment industry is hardly damaged. . It was an epoch-making invention that succeeded in obtaining a number of primary and secondary effects, the technical effect on the industry was enormous, and the benefit to the entire industry was immeasurable. There is.
【図1】本発明のメッキ加工の前処理脱脂工程における
油分離装置の従来技術としての具体的な脱脂工程を表し
た溶剤脱脂装置の説明図である。FIG. 1 is an explanatory view of a solvent degreasing device showing a specific degreasing process as a conventional technique of an oil separation device in a pretreatment degreasing process of plating processing of the present invention.
【図2】本発明のメッキ加工の前処理脱脂工程における
油分離装置の従来技術としての具体的な脱脂工程を表し
た溶剤脱脂装置の説明図である。FIG. 2 is an explanatory view of a solvent degreasing device showing a specific degreasing process as a conventional technique of an oil separation device in a pretreatment degreasing process of plating processing of the present invention.
【図3】本発明のメッキ加工の前処理脱脂工程における
油分離装置を適用した実施例である油分離装置の内部構
造を表した正面図(a)及び油分離装置の主要部分の平
面図である。FIG. 3 is a front view (a) showing an internal structure of an oil separation device, which is an embodiment to which an oil separation device is applied in a pretreatment degreasing step of the plating process of the present invention, and a plan view of main parts of the oil separation device. is there.
【図4】本発明のメッキ加工の前処理脱脂工程における
油分離装置を適用した実施例である油分離装置の作用説
明図である。FIG. 4 is an operation explanatory view of an oil separation device that is an embodiment to which the oil separation device is applied in the pretreatment degreasing step of the plating process of the present invention.
1,10 オーバーフロー部 2,11 脱脂処理用タンク 3,12 濾過タンク 3a,3c 上部仕切板 3b 下部仕切板 4,14 ポンプ 5,15 リタンーバルブ 6,13 溶液循環パイプ 7 ワーク 12a 仕切板 13a 先端放出口 A 脱脂処理水溶液 B,C 油脂成分 D1,D2,F1,F2,F3,F4,F5,F6,F
7,F8 液面1,10 Overflow part 2,11 Degreasing tank 3,12 Filtration tank 3a, 3c Upper partition plate 3b Lower partition plate 4,14 Pump 5,15 Return valve 6,13 Solution circulation pipe 7 Workpiece 12a Partition plate 13a Tip discharge port A Degreasing treatment aqueous solution B, C Oil and fat component D1, D2, F1, F2, F3, F4, F5, F6, F
7, F8 liquid level
Claims (2)
脱脂工程で用いられれ装置であって、 脱脂剤を一定の濃度で溶融させた脱脂処理水溶液を満た
し、被脱脂部材を投入して脱脂処理をおこなう脱脂処理
槽と、 当該脱脂処理槽の内壁部所定の位置に設けた脱脂処理水
溶液放出部と、 上記脱脂処理槽の胴部上面所定の位置に開口を設け、脱
脂処理水溶液の水面に浮遊した脱脂成分と溢れた脱脂処
理水溶液を外部に排除するオーバーフロー部と、 当該オーバーフロー部下部近傍に設け、オーバーフロー
部から排出された脱脂成分が混合した脱脂処理水溶液を
濾過する脱脂成分濾過槽と、 当該脱脂成分濾過槽で濾過処理されて排出された脱脂処
理水溶液を上記脱脂処理槽の脱脂処理水溶液放出部に循
環させる循環経路と、 当該循環経路に介装されたポンプと、 当該ポンプに並装されたリターンバルブとから成るメッ
キ加工の前処理脱脂工程における油分離装置において、 脱脂成分濾過槽には、当該脱脂成分濾過槽の上面部から
底部にかけて突設し、その下端辺は液槽底部より所定の
液体流入開口部が形成されるように形成した仕切板を、
当該脱脂成分濾過槽の長手方向に所定の間隔で複数設け
たことを特徴とするメッキ加工の前処理脱脂工程におけ
る油分離装置。1. A device used in a degreasing process performed as a pretreatment process for plating, which is filled with a degreasing treatment aqueous solution in which a degreasing agent is melted at a constant concentration, and a member to be degreased is charged to perform the degreasing treatment. The degreasing treatment tank to be performed, the degreasing treatment aqueous solution discharge part provided at a predetermined position on the inner wall of the degreasing treatment tank, and the opening on the upper surface of the body of the degreasing treatment tank at a predetermined position, floating on the water surface of the degreasing treatment solution An overflow section for removing the degreasing component and the overflowed degreasing aqueous solution to the outside, and a degreasing component filtering tank provided near the lower part of the overflow section for filtering the degreasing aqueous solution mixed with the degreasing component discharged from the overflow section, and the degreasing unit. A circulation path that circulates the degreasing aqueous solution that has been filtered and discharged in the component filtering tank to the degreasing aqueous solution discharge section of the degreasing tank, and is installed in the circulation path. In the oil separation device in the pretreatment degreasing process for plating, which consists of a pump and a return valve installed in parallel with the pump, the degreasing component filtration tank is provided with a protrusion from the top to the bottom of the degreasing component filtration tank. The lower end of the partition plate is formed so that a predetermined liquid inflow opening is formed from the bottom of the liquid tank.
An oil separation device in a pretreatment degreasing step of plating, wherein a plurality of degreasing component filtration tanks are provided at predetermined intervals in a longitudinal direction.
よって底部に形成される液体流入開口部は、脱脂成分濾
過槽の短手面の内壁面の面積の2割程度の面積としたこ
とを特徴とする請求項1記載のメッキ加工の前処理脱脂
工程における油分離装置。2. The liquid inflow opening formed at the bottom by a partition plate provided inside the degreasing component filtration tank has an area of about 20% of the area of the inner wall surface of the short side of the degreasing component filtration tank. The oil separation device in the pretreatment degreasing step of the plating process according to claim 1.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15315296A JPH09314142A (en) | 1996-05-23 | 1996-05-23 | Oil separator in pretreatment degreasing process of plating |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15315296A JPH09314142A (en) | 1996-05-23 | 1996-05-23 | Oil separator in pretreatment degreasing process of plating |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH09314142A true JPH09314142A (en) | 1997-12-09 |
Family
ID=15556167
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP15315296A Pending JPH09314142A (en) | 1996-05-23 | 1996-05-23 | Oil separator in pretreatment degreasing process of plating |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH09314142A (en) |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2001336193A (en) * | 2000-05-29 | 2001-12-07 | Daito Giken:Kk | Discharging method with the least water by overflow of fats and oils floating on waste water mixed with oil |
| JP2007071031A (en) * | 2005-09-02 | 2007-03-22 | Mitsubishi Heavy Ind Ltd | Part of rotary machine and rotary machine |
| JP2011115727A (en) * | 2009-12-04 | 2011-06-16 | Kansai Electric Power Co Inc:The | Oil-water separation drainage system |
| KR20150059109A (en) * | 2013-11-21 | 2015-05-29 | 친룬 창 | Oil separating apparatus |
| CN107792995A (en) * | 2017-11-07 | 2018-03-13 | 陈鸣岐 | A kind of sewage-treatment plant of efficient galvanization production line |
| CN108486590A (en) * | 2018-04-08 | 2018-09-04 | 珠海市玛斯特五金塑胶制品有限公司 | Oil removing and sour reutilization system and method is electroplated |
| WO2023243715A1 (en) * | 2022-06-17 | 2023-12-21 | ナルコジャパン合同会社 | Method for operating direct cooling water system, oil content separation promoter, and treatment facility for direct cooling water system |
-
1996
- 1996-05-23 JP JP15315296A patent/JPH09314142A/en active Pending
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2001336193A (en) * | 2000-05-29 | 2001-12-07 | Daito Giken:Kk | Discharging method with the least water by overflow of fats and oils floating on waste water mixed with oil |
| JP2007071031A (en) * | 2005-09-02 | 2007-03-22 | Mitsubishi Heavy Ind Ltd | Part of rotary machine and rotary machine |
| US7947381B2 (en) | 2005-09-02 | 2011-05-24 | Mitsubishi Heavy Industries, Ltd. | Rotating machine and parts of the same |
| JP2011115727A (en) * | 2009-12-04 | 2011-06-16 | Kansai Electric Power Co Inc:The | Oil-water separation drainage system |
| KR20150059109A (en) * | 2013-11-21 | 2015-05-29 | 친룬 창 | Oil separating apparatus |
| CN107792995A (en) * | 2017-11-07 | 2018-03-13 | 陈鸣岐 | A kind of sewage-treatment plant of efficient galvanization production line |
| CN108486590A (en) * | 2018-04-08 | 2018-09-04 | 珠海市玛斯特五金塑胶制品有限公司 | Oil removing and sour reutilization system and method is electroplated |
| CN108486590B (en) * | 2018-04-08 | 2019-11-19 | 珠海市玛斯特五金塑胶制品有限公司 | Oil removing and sour reutilization system and method is electroplated |
| WO2023243715A1 (en) * | 2022-06-17 | 2023-12-21 | ナルコジャパン合同会社 | Method for operating direct cooling water system, oil content separation promoter, and treatment facility for direct cooling water system |
| JP2023184205A (en) * | 2022-06-17 | 2023-12-28 | Jfeスチール株式会社 | Direct cooling water system operation method, oil separation promoter, and direct cooling water system treatment equipment |
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