KR100326394B1 - Ni-Cr FULL AUTOMATIC PLATING APPARATUS AND PLATING METHOD USING SAID APPARATUS - Google Patents
Ni-Cr FULL AUTOMATIC PLATING APPARATUS AND PLATING METHOD USING SAID APPARATUS Download PDFInfo
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- KR100326394B1 KR100326394B1 KR1019990010680A KR19990010680A KR100326394B1 KR 100326394 B1 KR100326394 B1 KR 100326394B1 KR 1019990010680 A KR1019990010680 A KR 1019990010680A KR 19990010680 A KR19990010680 A KR 19990010680A KR 100326394 B1 KR100326394 B1 KR 100326394B1
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- plating
- nickel
- rack
- voltage
- hanger
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- 238000007747 plating Methods 0.000 title claims abstract description 149
- 238000000034 method Methods 0.000 title claims abstract description 91
- 229910018487 Ni—Cr Inorganic materials 0.000 title claims abstract description 26
- 238000005406 washing Methods 0.000 claims abstract description 35
- VNNRSPGTAMTISX-UHFFFAOYSA-N chromium nickel Chemical compound [Cr].[Ni] VNNRSPGTAMTISX-UHFFFAOYSA-N 0.000 claims abstract description 25
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 24
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 claims abstract description 16
- 230000008569 process Effects 0.000 claims description 66
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 claims description 47
- 229910052759 nickel Inorganic materials 0.000 claims description 23
- 238000005238 degreasing Methods 0.000 claims description 13
- 239000007788 liquid Substances 0.000 claims description 5
- 238000001994 activation Methods 0.000 claims description 4
- 238000005554 pickling Methods 0.000 claims description 4
- 238000011084 recovery Methods 0.000 claims description 4
- 230000018044 dehydration Effects 0.000 claims 1
- 238000006297 dehydration reaction Methods 0.000 claims 1
- 239000011651 chromium Substances 0.000 abstract description 14
- 229910052804 chromium Inorganic materials 0.000 abstract description 10
- 239000011248 coating agent Substances 0.000 abstract description 10
- 238000000576 coating method Methods 0.000 abstract description 10
- 239000002351 wastewater Substances 0.000 abstract description 7
- 230000007547 defect Effects 0.000 abstract description 3
- 239000010410 layer Substances 0.000 description 26
- 239000000047 product Substances 0.000 description 14
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 6
- 239000000243 solution Substances 0.000 description 6
- 230000008901 benefit Effects 0.000 description 5
- 230000008859 change Effects 0.000 description 5
- JOPOVCBBYLSVDA-UHFFFAOYSA-N chromium(6+) Chemical compound [Cr+6] JOPOVCBBYLSVDA-UHFFFAOYSA-N 0.000 description 5
- 230000007797 corrosion Effects 0.000 description 5
- 238000005260 corrosion Methods 0.000 description 5
- 230000008021 deposition Effects 0.000 description 4
- 230000006872 improvement Effects 0.000 description 4
- 238000003911 water pollution Methods 0.000 description 4
- 239000002253 acid Substances 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 238000005342 ion exchange Methods 0.000 description 3
- 238000001556 precipitation Methods 0.000 description 3
- 230000009467 reduction Effects 0.000 description 3
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 229910001430 chromium ion Inorganic materials 0.000 description 2
- 238000003912 environmental pollution Methods 0.000 description 2
- 239000002923 metal particle Substances 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 239000008213 purified water Substances 0.000 description 2
- 238000004062 sedimentation Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- RLLPVAHGXHCWKJ-IEBWSBKVSA-N (3-phenoxyphenyl)methyl (1s,3s)-3-(2,2-dichloroethenyl)-2,2-dimethylcyclopropane-1-carboxylate Chemical compound CC1(C)[C@H](C=C(Cl)Cl)[C@@H]1C(=O)OCC1=CC=CC(OC=2C=CC=CC=2)=C1 RLLPVAHGXHCWKJ-IEBWSBKVSA-N 0.000 description 1
- NWUYHJFMYQTDRP-UHFFFAOYSA-N 1,2-bis(ethenyl)benzene;1-ethenyl-2-ethylbenzene;styrene Chemical compound C=CC1=CC=CC=C1.CCC1=CC=CC=C1C=C.C=CC1=CC=CC=C1C=C NWUYHJFMYQTDRP-UHFFFAOYSA-N 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 230000004913 activation Effects 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 239000012670 alkaline solution Substances 0.000 description 1
- 230000001174 ascending effect Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 239000011247 coating layer Substances 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 230000008878 coupling Effects 0.000 description 1
- 238000010168 coupling process Methods 0.000 description 1
- 238000005859 coupling reaction Methods 0.000 description 1
- 238000005034 decoration Methods 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 238000002845 discoloration Methods 0.000 description 1
- 239000000839 emulsion Substances 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 description 1
- 238000007689 inspection Methods 0.000 description 1
- 239000003456 ion exchange resin Substances 0.000 description 1
- 229920003303 ion-exchange polymer Polymers 0.000 description 1
- 238000010030 laminating Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 238000006386 neutralization reaction Methods 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 238000012805 post-processing Methods 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 230000008961 swelling Effects 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
- 238000004148 unit process Methods 0.000 description 1
Classifications
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- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D17/00—Constructional parts, or assemblies thereof, of cells for electrolytic coating
- C25D17/16—Apparatus for electrolytic coating of small objects in bulk
- C25D17/28—Apparatus for electrolytic coating of small objects in bulk with means for moving the objects individually through the apparatus during treatment
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D17/00—Constructional parts, or assemblies thereof, of cells for electrolytic coating
- C25D17/02—Tanks; Installations therefor
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D17/00—Constructional parts, or assemblies thereof, of cells for electrolytic coating
- C25D17/06—Suspending or supporting devices for articles to be coated
- C25D17/08—Supporting racks, i.e. not for suspending
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D21/00—Processes for servicing or operating cells for electrolytic coating
- C25D21/08—Rinsing
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D21/00—Processes for servicing or operating cells for electrolytic coating
- C25D21/12—Process control or regulation
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D21/00—Processes for servicing or operating cells for electrolytic coating
- C25D21/16—Regeneration of process solutions
- C25D21/22—Regeneration of process solutions by ion-exchange
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D5/00—Electroplating characterised by the process; Pretreatment or after-treatment of workpieces
- C25D5/10—Electroplating with more than one layer of the same or of different metals
- C25D5/12—Electroplating with more than one layer of the same or of different metals at least one layer being of nickel or chromium
- C25D5/14—Electroplating with more than one layer of the same or of different metals at least one layer being of nickel or chromium two or more layers being of nickel or chromium, e.g. duplex or triplex layers
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D5/00—Electroplating characterised by the process; Pretreatment or after-treatment of workpieces
- C25D5/34—Pretreatment of metallic surfaces to be electroplated
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D5/00—Electroplating characterised by the process; Pretreatment or after-treatment of workpieces
- C25D5/627—Electroplating characterised by the visual appearance of the layers, e.g. colour, brightness or mat appearance
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Automation & Control Theory (AREA)
- Electroplating Methods And Accessories (AREA)
Abstract
본 발명은 자동화된 니켈-크롬 도금설비 및 도금방법에 관한 것으로서, 랙과 행거의 접촉부 형상을 개선하여 전기 효율을 향상하고, 제품의 표면에 퇴적되는 도금층의 피복두께를 균일하게 함과 동시에 피복강도를 향상한 도금설비 및 도금방법에 관한 것이다. 상기의 목적을 달성하기 위해 안출된 본 발명의 도금설비는,BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an automated nickel-chromium plating apparatus and plating method, which improves electrical efficiency by improving the shape of a contact portion of a rack and a hanger, and makes coating thickness of the plating layer deposited on the surface of the product uniform and at the same time coating strength. It relates to a plating facility and a plating method improved. Plating equipment of the present invention devised to achieve the above object,
① 상기 랙(21)이 행거(22)에 안정적으로 설치될 수 있게, 랙(21)의 선단부 형상을 '' 형상으로 하고, 랙(21)의 선단부가 걸리게 되는 행거(22)의 가로대(22a)도 상기 랙과 어울릴 수 있도록 적당한 간격을 두고서 '' 형의 접촉부(23b)를 형성하여, 이들간의 쐐기 끼움으로 랙의 흔들림을 방지함과 동시에 통전상태가 순간적으로 단락됨으로서 발생되는 도금불량을 방지하며, ② Cr의 피복력 향상을 위해 초기에 고전압을 소정 시간동안 인가한 후, 인가 전압을 선형적으로 낮추어, 일정 시간이 지난 후에는 표준상태의 전압을 유지하도록 도금설비의 전원을 정류기로 제어하며, ③ 바이폴러(Bipolar) 현상이 발생되지 않도록, 단위 엘리베이터(30)의 상하 이동부위에 약전압 인가시점을 결정하는 음극 슬라이드 바(31)를 설치하고, ④ 수세작업중에 발생되는 폐수로부터 크롬을 회수하기 위해, 펌프(51) 등을 구비한 이온교환장치(40)를 설치한 구성으로 되어 있다.① The shape of the tip of the rack 21 so that the rack 21 can be stably installed on the hanger 22 ' The cross section 22a of the hanger 22 to which the front end of the rack 21 is fitted, with appropriate spacing so as to fit with the rack, 'Form contact portion 23b to prevent wobble between the racks and prevent plating defects caused by short-circuit of the energized state, and ② high voltage at the initial stage to improve the coating power of Cr After applying for a predetermined time, the applied voltage is linearly lowered, and after a certain time, the power of the plating equipment is controlled by the rectifier to maintain the voltage in a standard state. ③ To prevent the occurrence of a bipolar phenomenon, A negative electrode slide bar 31 for determining the time of application of the weak voltage is installed on the vertical movement portion of the unit elevator 30, and ④ with a pump 51 or the like to recover chromium from the wastewater generated during the water washing operation. The exchanger 40 is provided.
Description
본 발명은 도금 대상물의 투입에서 인출까지의 각 작업공정이 연속적으로 이루어질 수 있도록, 설비자체가 완전히 무인 자동화된 니켈-크롬 도금설비(장치) 및 도금방법에 관한 것으로서, 특히 도금 대상물이 장착되는 랙과, 이 랙이 걸려 있는 행거의 접촉부 형상을 개선하여 전기 전도율(효율)을 향상하고, 이와 더불어 제품의 표면에 퇴적되는 도금층의 피복두께를 균일하게 하면서 피복강도(력)를 향상하여 제품의 내부식성 및 내구성을 향상한, 니켈-크롬 도금설비 및 도금방법에 관한 것이다.The present invention relates to an automated nickel-chromium plating apparatus (apparatus) and a plating method in which the equipment itself is completely unattended so that each work process from the input to the plating object can be continuously performed. And improve the electrical conductivity (efficiency) by improving the shape of the contact portion of the hanger on which the rack is hung, and also improve the coating strength (force) while making the coating thickness of the plating layer deposited on the surface of the product uniform. The present invention relates to a nickel-chromium plating apparatus and a plating method which have improved corrosion resistance and durability.
또한, 본 발명은 이온교환방법에 의해, 도금공정에서 발생되는 폐수로부터 니켈 및 크롬을 회수함으로서 수질 오염을 예방함과 동시에 회수된 니켈과 크롬을다시 사용하여 경제적으로도 이득을 볼 수 있게 한, 니켈-크롬 도금설비 및 도금방법에 관한 것이다.In addition, the present invention by the ion exchange method, by recovering the nickel and chromium from the wastewater generated in the plating process to prevent water pollution and at the same time, the recovered nickel and chromium can be used again to benefit economically, Nickel-chromium plating equipment and plating method.
첨부된 도면중 도8은 종래의 니켈-크롬 도금 공정도이다.8 of the accompanying drawings is a conventional nickel-chromium plating process.
상기 도면에서 참조되는 바와 같이, 종래의 니켈-크롬 도금공정은, 크게 전처리공정(100)과 본공정(200), 그리고 후처리공정(300)으로 이루어져 있다.As referred to in the figure, the conventional nickel-chromium plating process is largely composed of a pretreatment step 100, the main step 200, and the post-treatment step 300.
일반적으로, 도금 불량율의 50% 이상은 전처리공정에 원인이 있는데, 전처리공정에 의해 야기되는 결함으로는, ①도금층의 박리 또는 부풀음(氣泡), ②얼룩, 구름낌 등의 광택의 불균일, ③도금층의 요철(더덕 부착)이나 피트, ④핀홀의 발생에 의한 도금 대상물의 내식성 저하, ⑤도금 피막의 부서짐(취성) 등이 있다.In general, more than 50% of the plating failure rate is caused by the pretreatment process. The defects caused by the pretreatment process include (1) peeling or swelling of the plating layer, (2) unevenness of gloss such as spots and cloudiness, and (3) plating layer. Unevenness (adhesion), pits, corrosion resistance of the plating target due to the occurrence of pinholes, brittleness of the plating film, and the like.
이러한 전처리공정은, 도금 대상물의 재질이나 도금방법에 따라 조금씩 다르기는 하지만, 대개의 경우 도8에 도시된 다음의 작업들로 구성되어 있다.This pretreatment process, although slightly different depending on the material or the plating method of the plating object, usually consists of the following operations shown in FIG.
탈지(degreasing, cleaning) 작업공정(110)Degreasing, Cleaning Process (110)
도금 대상물의 표면에 부착되어 있는 유지성(油脂性)의 더러움을 제거하는 작업으로서, 용제탈지와 알칼리탈지, 전해탈지(마무리탈지), 에멀션탈지, 기계적 탈지 등이 있다.As a work for removing the oil-retaining dirt adhering to the surface of the plating object, there are solvent degreasing, alkali degreasing, electrolytic degreasing (finishing degreasing), emulsion degreasing and mechanical degreasing.
산세(pickling) 작업공정(120)Pickling Work Process (120)
도금 대상물의 표면에 발생한 산화피막이나 수산화물을 산(酸)으로 제거하는 화학적 방법이다.It is a chemical method for removing an oxide film or hydroxide generated on the surface of a plating object with an acid.
수세 작업공정(130)Water washing work process (130)
도금 대상물의 표면에 부착되어 있는 전(前)공정의 용액을 단시간에 확산시키기 위한 공정으로서, 확산을 촉진하기 위해 공기교반, 강제대류, 온수수세, 스프레이수세 등을 한다.As a step for diffusing the solution of the previous process adhering to the surface of the plating object in a short time, air stirring, forced convection, hot water washing, spray washing and the like are performed to promote diffusion.
중화 작업공정(140)Neutralization Work Process (140)
산세 작업공정(120)을 거쳐 나온 도금 대상물을 알칼리 용액에 침적하여 표면을 중화시킨다.The object to be plated through the pickling process 120 is deposited in an alkaline solution to neutralize the surface.
상기의 전처리공정(100)을 거치면서 깨끗한 표면을 얻게 된 도금 대상물은, 본공정(200)에서 니켈-크롬 도금된다.The plating object obtained with a clean surface through the pretreatment step 100 is nickel-chromium plated in the main step 200.
상기의 본공정은 도8에 도시된 것과 같이, 다음의 작업들로 구성되어 있다.This main process is composed of the following operations, as shown in FIG.
니켈도금 작업공정(210)Nickel Plating Work Process (210)
상기의 전처리공정(100)을 거쳐 나온 도금 대상물의 표면에, 방식(防蝕)과 장식의 목적으로, 일정 두께의 니켈(Ni)을 퇴적시킨다.Nickel (Ni) of a certain thickness is deposited on the surface of the plating object passed through the pretreatment step 100 for the purpose of anticorrosion and decoration.
이 작업은, 종래에는 수작업으로 이루어졌으며, 아디온(adion)이 도금 대상물의 표면에 충분히 확산되어서 금속격자의 일부를 구성할 수 있도록, 저전류밀도에서 수행되었다.This operation was conventionally performed by hand, and was carried out at low current density so that an adion could be sufficiently diffused on the surface of the plating object to form part of the metal lattice.
그러나, 이 경우에는 퇴적층(도금층)의 입자가 조대(粗大)하여 쉽게 벗겨지는 단점이 있었기 때문에, 개선이 요구되고 있다.However, in this case, since the particle | grains of a deposited layer (plating layer) have the disadvantage that it coarsens and peels easily, improvement is calculated | required.
수세 작업공정(220)Water washing work process (220)
도금 대상물의 표면에 부착되어 있는 도금액의 피막을 단시간에 씻어내는 작업공정으로서, 물을 공급하는 방법에 따라 병렬식과 직렬역류식이 있다.As a work process for washing a film of plating liquid adhering to the surface of a plating object in a short time, there are a parallel type and a series countercurrent type depending on a method of supplying water.
크롬도금 작업공정(230)Chrome Plating Work Process (230)
제품의 외관을 미려하게 하기 위하여, 또한 대기 중에서의 변색 방지와 산에 대한 내부식성의 향상을 위해 실시된다.In order to enhance the appearance of the product, it is also carried out to prevent discoloration in the atmosphere and to improve corrosion resistance against acids.
그런데, 종래의 크롬도금 방법에 의하면, 전기전도율(효율)이 15% 이하로 극히 낮고, 또한 피막층(퇴적층, 도금층)의 두께가 불균일하여 제품의 내구성에 나쁜 영향을 미쳤다. 즉, 니켈 도금층 위에 크롬 도금층이 퇴적되지 않으면, 니켈 도금층이 대기와 반응하여 산화되고, 이로 인해 제품 표면에 검은색 무늬가 생기게 되는 등, 외관 형상이 나빠지게 된다. 따라서, 이 분야에서도 개선의 요구가 비등해지고 있다.By the way, according to the conventional chromium plating method, the electrical conductivity (efficiency) is extremely low at 15% or less, and the thickness of the coating layer (sedimentation layer, plating layer) is uneven, which adversely affects the durability of the product. That is, if the chromium plating layer is not deposited on the nickel plating layer, the nickel plating layer reacts with the atmosphere and oxidizes, resulting in a deterioration in appearance such as black pattern on the surface of the product. Therefore, the demand for improvement also boils in this field.
수세 및 탈수 작업공정(240)Water washing and dewatering work process (240)
도금 대상물(제품)의 표면을 완전히 건조시킨다.Completely dry the surface of the plating object (product).
그런데, 이 작업공정에서 발생된 폐수를 처리함에 있어, 종래에는 그대로 하수관을 통해 방류하거나 침전조에서 일차 침전시킨 후 방류함으로서, 수질의 오염을 일으키는 문제점이 있었다. 참고로, 국내법에서는, 6가크롬의 경우에, 배출 농도가 0.5ppm 이하로 되어야 한다고 규정되어 있다.By the way, in treating the wastewater generated in this work process, conventionally discharged through the sewage pipe as it is, or discharged after the first settling in the sedimentation tank, there was a problem causing water pollution. For reference, the national law stipulates that in the case of hexavalent chromium, the emission concentration should be 0.5 ppm or less.
따라서, 이 부분에 관해서도 개선의 여지가 있다.Therefore, there is room for improvement in this part as well.
이와같이 하여, 상기의 본공정(200)을 거쳐 나온 제품은, 후처리공정(30)에서 품질검사를 한 후 포장하여 출하시킨다.In this way, the product which passed through the said main process 200 is packaged and shipped after quality inspection in the post-processing process 30.
첨부된 도면중 도9는, 상기에서 설명한 도금방법에 따라, 종래의 도금설비로 제품을 도금했을 때의 도금층 두께 변화를 도시한 개략도이다.9 of the accompanying drawings is a schematic diagram showing a change in plating layer thickness when a product is plated with a conventional plating facility according to the plating method described above.
일반적으로, 저전류 밀도하에서 도금 대상물의 표면에 도금층을 적층하게 되면, 여타의 부위보다 모서리 부위에 더 많은 음전하가 배치되기 때문에, 이 부분에서의 도금층의 두께가 다른 부위보다 상대적으로 두꺼워진다.In general, when the plating layer is laminated on the surface of the object to be plated under a low current density, since more negative charges are disposed at the corner portions than at other portions, the thickness of the plating layer at this portion becomes relatively thicker than other portions.
특히, 도금층이 적층되는 과정을 살펴 보면, 마치 눈사람을 만드는 것처럼, 퇴적 두께가 두꺼운 부분일수록 더욱더 퇴적층의 퇴적속도가 빠르다.In particular, looking at the process of laminating the plating layer, as if making a snowman, the thicker portion of the deposition thickness, the faster the deposition rate of the deposition layer.
이상과 같이, 종래의 니켈-크롬 도금방법에는 몇가지 개선해야 될 단점들이 있으며, 특히 종래 도금설비는 수동식이거나 반자동식(semi-automatic)이어서, 작업자의 숙련도에 따라 제품의 품질이 달라지는 단점이 있다.As described above, there are some disadvantages to be improved in the conventional nickel-chromium plating method, in particular, the conventional plating facilities are manual or semi-automatic, there is a disadvantage that the quality of the product varies depending on the skill of the operator.
특히, 종래의 도금설비(장치)는, 도금 대상물을 걸어 두는 랙과 행거의 접촉부위가 불안정하여, 다음 공정으로의 이동시, 랙이 행거를 중심으로 앞뒤로 흔들려서, 도금 대상물(제품)이 땅에 떨어지거나, 또는 도금욕(浴)의 테두리 부위에 랙이 부딪혀 랙 자체가 땅에 떨어지는 등의 단점이 있었다. 따라서, 이에 대한 개선도 시급한 실정이다.In particular, in the conventional plating equipment (apparatus), the contact area between the rack to hang the plating object and the hanger is unstable, and when moving to the next process, the rack swings back and forth around the hanger, and the plating object (product) falls to the ground. Or, the rack hits the edge portion of the plating bath (혀), there was a disadvantage that the rack itself falls on the ground. Therefore, there is an urgent need for improvement.
본 발명은 앞에서 언급한 종래의 문제점을 개선하기 위해 안출된 것으로서, 랙과 행거의 접촉부위 형상을 개선하여 전기전도율(효율)을 향상하고, 시간에 따른 인가전압의 볼티지를 서로 다르게 하여 Cr의 피복력을 향상하며, 현재 국내에 널리 보급되어 있는 수동식 또는 반자동식의 도금설비를 완전히 무인 자동화하여 제품의 품질이 항상 일정한 수준을 유지할 수 있게 하고, 더욱이 수세 작업공정에서 배출되는 폐수를 이온교환장치로 정화하여 환경오염을 방지함과 동시에, 이 장치에 의해 환원된 니켈-크롬을 다시 사용함으로서 경제적인 이득도 볼 수 있게 한, 니켈-크롬 도금설비 및 이 도금설비를 이용한 연속 도금처리방법을 제공함에 목적이 있다. 이러한 상기의 목적을 달성하기 위하여, 본 발명에서는 다음과 같은 수단을 강구하였다.The present invention has been made to improve the above-mentioned conventional problems, improve the conductivity (efficiency) by improving the shape of the contact portion of the rack and the hanger, the voltage of the applied voltage over time to different Cr It improves the coating power and fully unmanned automatization of the manual or semi-automatic plating equipment, which is now widely distributed in Korea, so that the quality of products can always be maintained at a constant level. It provides a nickel-chromium plating facility and a continuous plating treatment method using the plating facility, which purifies and prevents environmental pollution, and also provides economic benefits by reusing nickel-chromium reduced by this device. There is a purpose. In order to achieve the above object, the present invention has been devised the following means.
즉, ① 도금 대상물을 장착한 랙이 행거에 안정적으로 설치될 수 있게, 상기 랙의 선단부 형상을 '' 형상으로 하고, 이와 더불어 상기 랙의 선단부가 걸리게 되는 행거의 가로대 형상도 상기 랙과 어울릴 수 있도록 '' 형상으로 구성함으로서, 쐐기형태로 삽입·고정할 수 있도록 하여, 랙이 이동하는 도중에 흔들려서 순간적으로 전원이 단락되는 전기접촉 불량을 방지하였다.That is, ① the rack is mounted on the object to be stably installed in the hanger, the shape of the leading end of the rack ' And the cross-sectional shape of the hanger on which the front end of the rack is hooked with the rack. In the configuration, it was possible to insert and fix in a wedge shape, thereby preventing electrical contact failure in which the power supply was momentarily shorted by shaking while the rack was moving.
또한, ② Cr의 피복력 향상을 위해, 초기에 고전압(본 실시예의 경우에는 약 7볼트)을 소정 시간동안 인가한 후, 인가 전압을 선형적으로 낮추어, 일정 시간이 지난 후에는 표준상태(본 실시예의 경우에는 약 4볼트)의 전압을 유지하도록, 도금설비의 전원을 정류기로 제어함으로서, 크롬도금의 특성상 야기되던 피복력 저하에 의한 도금불량을 해소하였다.(2) In order to improve the coating power of Cr, at first, a high voltage (approximately 7 volts in this embodiment) is applied for a predetermined time, and then the applied voltage is linearly lowered. In the case of the example, by controlling the power supply of the plating equipment with a rectifier so as to maintain a voltage of about 4 volts), the plating failure caused by the decrease in coating power caused by the characteristics of the chromium plating was eliminated.
또한, ③ 도금설비의 완전 무인 자동화를 위해, 단속식으로 이동하는 엘리베이터 장치를 설치하였다.In addition, for the unattended automation of the plating equipment, an elevator device that moves intermittently was installed.
한편, 본 발명의 도금설비에 있어서는, 도금 대상물이 연속하여 다음 공정으로 이송됨으로, 도금욕 내에서의 이송시, 도금 대상물의 표면에 바이폴러(BIPOLAR) 현상이 발생하게 된다. 이러한 바이폴러 현상은, 도금 대상물 표면에의 도금층 형성을 방해하므로 반드시 해결해야 할 기술적 과제이다.On the other hand, in the plating equipment of the present invention, the plating object is continuously transferred to the next step, so that a bipolar phenomenon occurs on the surface of the plating object during transfer in the plating bath. This bipolar phenomenon is a technical problem that must be solved because it prevents the plating layer from being formed on the surface of the plating object.
이에 본 발명에서는, ④ 도금 대상물이 도금욕 내에 침적되기 직전, 행거와 랙을 통해, 도금 대상물의 표면에 음전하가 배치될 수 있도록, 단위 엘리베이터의 상하 이동부위에 약전압 인가시점을 결정하는 음극 슬라이드 바를 설치함으로서, 저전압(저항부착)이 통전된 상태로 투입되어 바이폴러 현상을 예방하면서, 동시에 고전압에 의한 도금불량(도금층의 산화)을 해소하였다.In the present invention, ④ the negative electrode slide to determine the time of applying a weak voltage to the vertical moving portion of the unit elevator, so that the negative object can be disposed on the surface of the object to be plated through the hanger and the rack, just before the object to be plated is deposited in the plating bath. By providing the bar, the low voltage (with resistance) was energized to prevent the bipolar phenomenon while simultaneously eliminating the plating failure (oxidation of the plating layer) due to the high voltage.
더욱이, 본 발명에서는, ⑤ 수세(水洗)작업중에 발생되는 폐수로부터 3가 및 6가 크롬을 이온교환법으로 회수함으로서, 수질의 오염을 예방함과 동시에 폐수의 발생량을 감소시켰다.Furthermore, in the present invention, by recovering trivalent and hexavalent chromium from the wastewater generated during the washing operation of the water by ion exchange, water pollution is prevented and the amount of wastewater generated is reduced.
도1은 본 발명에 따른 니켈-크롬 도금방법의 공정 순서도,1 is a process flowchart of a nickel-chromium plating method according to the present invention;
도2는 본 발명에 따른 니켈-크롬 도금설비의 배치도,2 is a layout view of the nickel-chromium plating equipment according to the present invention;
도3은 본 발명에 따른 랙과 행거의 결합부위를 나타낸 개략적인 사시도,3 is a schematic perspective view showing a coupling portion of a rack and a hanger according to the present invention;
도4는 도3에 도시된의 랙의 사시도,4 is a perspective view of the rack of FIG. 3;
도5a는 본 발명에 따른 단속(斷續) 이동식 엘리베이터 장치의 정면도,5A is a front view of an intermittent mobile elevator apparatus according to the present invention;
도5b는 도5a의 측면도 및 요부확대 사시도,Figure 5b is a side view and enlarged perspective view of Figure 5a,
도6은 세척수 속에 포함된 3가 Cr과 6가 Cr의 회수과정을 설명하기 위한 설명도,6 is an explanatory diagram for explaining a recovery process of trivalent Cr and hexavalent Cr contained in the washing water;
도7은 본 발명에 따른 전압의 추이를 도시한 시간-전압 그래프 대 종래의 시간-전압 변화 그래프를 도시한 도면,7 shows a time-voltage graph versus a conventional time-voltage change graph showing the transition of voltage according to the present invention;
도8은 종래의 니켈-크롬 도금 공정도,8 is a conventional nickel-chromium plating process chart,
도9는 종래의 도금설비로 제품(도금 대상물)을 도금했을 때의 각 부위별 도금층 두께를 나타낸 개략도.Fig. 9 is a schematic diagram showing the thickness of each layer when the product (plating object) is plated by the conventional plating equipment.
〔도면 부호의 설명〕[Description of Drawing Reference]
1...탈지공정, 2,4,6,10,12,14...수세공정,1, degreasing process, 2, 4, 6, 10, 12, 14 ...
3...전해산세공정, 5...전해탈지공정,3. electrolytic acid wash process, 5 electrolytic degreasing process,
7...활성화공정, 9...니켈 스트라이크공정,7 activation process, 9 nickel strike process,
11...니켈도금공정, 13...크롬도금공정,11 ... nickel plating process, 13 ... chrome plating process,
15...탕세공정, 21...랙,15 ... washing process, 21 ... rack,
22...행거, 23a,23b...접촉부,22 hangers, 23a, 23b ...
31...음극 슬라이드 바, 41a,41b...이온교환기,31.Negative electrode slide bar, 41a, 41b ...
51...펌프, 61...유입관,51 pump, 61 inlet pipe,
62...배출관.62 ... exhaust pipe.
이하, 첨부된 도면을 참조하여 본 발명에 따른 니켈-크롬 도금설비 및 도금방법에 관하여 설명한다.Hereinafter, a nickel-chromium plating apparatus and a plating method according to the present invention will be described with reference to the accompanying drawings.
도1은 본 발명에 따른 니켈-크롬 도금방법의 공정 순서도이다.1 is a process flowchart of a nickel-chromium plating method according to the present invention.
상기의 도면에서 참조되는 바와 같이, 본 발명의 니켈-크롬 도금방법은 다음과 같은 공정들로 이루어져 있다.As referred to in the drawings, the nickel-chromium plating method of the present invention consists of the following processes.
전처리공정(A)Pretreatment Process (A)
탈지공정(1)→수세공정(2)→전해산세공정(3)→수세공정(4)→전해탈지공정(5)→수세공정(6)→활성화공정(7)→니켈 스트라이크공정(9)→수세공정(10)Degreasing step (1) → washing step (2) → electrolytic pickling step (3) → washing step (4) → electrolytic degreasing step (5) → washing step (6) → activation step (7) → nickel strike step (9) → washing process (10)
상기에서, 활성화공정(7)과 니켈 스트라이크공정(9)은, 후술할 본공정에서의 니켈 도금시, 도금 대상물과 니켈 퇴적층 사이의 밀착력을 향상시키기 위해 이루어지는 공정들로서, 니켈 도금욕에서 순간적으로 고전압을 인가하여 아주 얇은 니켈 도금층이 도금 대상물의 표면에 형성되게 하는 공정들이다.In the above, the activation process (7) and the nickel strike process (9) are processes that are performed to improve the adhesion between the object to be deposited and the nickel deposition layer during nickel plating in this process, which will be described later, and instantaneously high voltage in the nickel plating bath. Are applied to form a very thin nickel plating layer on the surface of the plating object.
그 이외의 각 공정들의 특징 및 작업방법은 앞서 설명한 종래의 예와 같다.Features and working method of each other process is the same as the conventional example described above.
본공정(B)Main process (B)
니켈도금공정(11)→수세공정(니켈도금액 회수공정)(12)→크롬도금공정(13)→수세공정(14)→탕세공정(15)→탈수공정(16)Nickel Plating Process (11) → Washing Process (Nickel Plating Solution Recovery Process) (12) → Chrome Plating Process (13) → Washing Process (14) → Hot Water Treatment Process (15) → Dewatering Process (16)
상기의 탕세(湯洗)공정(15)은, 도금욕을 거쳐 나온 도금 대상물(제품)의 표면에서 도금액을 완전히 제거(세척)하는 공정으로, 뜨거운 물에서 이루어진다.The hot water washing step 15 is a step of completely removing (washing) the plating liquid from the surface of the object to be plated (product) which has passed through the plating bath, and is made of hot water.
한편, 상기의 수세공정(14)에서 사용된 물 속에는, 3가 크롬과 6가 크롬이 포함되어 있기 때문에, 그대로 방류할 경우에는 수질의 오염을 야기하게 된다.On the other hand, since the water used in the above-described washing step 14 contains trivalent chromium and hexavalent chromium, when discharged as it is, it causes water pollution.
본 발명에서는 이러한 수질의 오염을 예방하기 위해, 도6에 도시한 것처럼, 수세조에 연통되게 설치해 놓은 유입관(61)을 통해, 상기의 수세공정(14)에서 배출되는 폐수를 6가크롬 이온교환기(41a) 내에 도입하여 환원석출하고, 다시 이 물을 3가크롬 이온교환기(41b) 내로 도입하여 환원석출한 후, 청정해진 물을 배출관(62)을 통해 상기의 수세조에 다시 공급할 수 있도록 구성하였다. 여기서, 미설명 부호 51은 펌프이다.In the present invention, in order to prevent such contamination of the water quality, as shown in Figure 6, through the inlet pipe 61 is installed in communication with the water tank, the waste water discharged from the water washing step 14, the hexavalent chromium ion It is introduced into the exchanger (41a) for reduction precipitation, and this water is introduced into the trivalent chromium ion exchanger (41b) for reduction and precipitation. Then, the purified water can be supplied to the water washing tank again through the discharge pipe (62). Configured. Here, reference numeral 51 is a pump.
그러나, 상기의 이온교환기(41a,41b)를 통한 크롬의 환원석출반응은 그 순서가 뒤바뀔수도 있다. 즉, 3가 크롬을 먼저 환원석출한 다음 6가 크롬을 환원석출할 수도 있다.However, the reduction precipitation reaction of chromium through the ion exchange groups 41a and 41b may be reversed in order. That is, trivalent chromium may be reduced precipitated first and then hexavalent chromium may be reduced precipitated.
한편, 이온교환기(41a,41b)내에 충전된 이온교환수지는 그 수명이 다한 경우, 황산(H2SO4)이나 수산화나트륨(NaOH)으로 다시 환원시켜 재사용할 수 있다.On the other hand, the ion exchange resin filled in the ion exchanger (41a, 41b) can be reused by reducing it back to sulfuric acid (H 2 SO 4 ) or sodium hydroxide (NaOH) when the lifetime of the ion exchanger.
후처리공정(C)Post Treatment Process (C)
본 발명의 후처리공정은 종래와 같으므로, 여기서는 그의 설명을 생략한다.Since the post-treatment step of the present invention is the same as the conventional one, the description thereof is omitted here.
한편, 상기의 공정 순서에 따라 도금작업이 이루어지는 본 발명의 도금설비는, 예를 들면, 도2에 도시한 바와 같은 형태로 배치될 수 있다(일 실시예).On the other hand, the plating equipment of the present invention, the plating operation is performed according to the above process sequence, for example, can be arranged in the form as shown in Figure 2 (an embodiment).
상기의 도2는, 현재 본 출원인이 실시하고 있는 니켈-크롬 도금설비의 배치도로서, 각각의 단위 공정들중, 수세공정(2,4,6,12,14)과 니켈도금공정(11)은, 필요에 따라 여러 개의 욕조(浴槽)로 나뉘어 설치될 수 있다.FIG. 2 is a layout view of the nickel-chromium plating facility currently carried out by the applicant, and among the unit processes, the washing processes 2, 4, 6, 12, 14 and the nickel plating process 11 are If necessary, it can be divided into several bathtubs.
한편, 본 발명에서는, 니켈도금공정(11)과 크롬도금공정(13) 이후에 배치되는 수세공정(12,14)을 3조 이상으로 나누어, 예를 들면, 앞의 2조는 도금액을 회수하는 역할을 하고 뒤의 수세조는 순수하게 수세하는 역할을 수행하도록 하였다.On the other hand, in the present invention, the washing step (12, 14) disposed after the nickel plating step (11) and the chrome plating step (13) is divided into three or more sets, for example, the previous two sets of roles to recover the plating solution And the later washing tank was to perform the role of pure washing.
여기서, 도금액의 회수란, 단지 농도가 묽은 욕조의 용액을 전단계의 농도가 진한 욕조나 도금욕에 재투입함으로서, 별도로 도금액(또는 약품)을 투입하지 않아도 도금작업을 계속하여 실시할 수 있다는 의미로 사용되고 있다. 따라서, 경제적인 이득을 볼 수 있다.Here, the recovery of the plating liquid means that the plating solution can be continuously carried out even if the plating liquid (or chemicals) is not added separately by re-inserting the solution of the bath having a weak concentration into the bath or the plating bath of the previous concentration. It is used. Thus, there is an economic benefit.
상기의 도2에 도시한 니켈-크롬 도금설비에서, 각 공정간의 이동이나 인접한 욕조로의 이동시 또는 욕조 내에서의 위치이동은, 도5a와 도5b에 도시한 엘리베이터 장치에 의해 단속적(斷續的)으로 이루어진다.In the nickel-chromium plating apparatus shown in FIG. 2, the movement between the respective processes, the movement to the adjacent bathtub, or the position movement in the bathtub is intermittent by the elevator apparatus shown in FIGS. 5A and 5B. )
상기의 도5a와 도5b는, 본 발명의 도금설비에서 사용하는 엘리베이터 장치의 정면도 및 측면도로서, 랙(21)이 결려 있는 행거(22)에 롤러를 설치하여 상기 롤러가 가이드로드(25)를 타고 상하로 이동할 수 있도록 하며, 다시 이 가이드로드(25)는 체인형의 구동수단(26)에 의해 단속적으로 전진 이동할 수 있게 구성되어 있다.즉, 엘리베이터 장치를 구성하고 있는 가이드로드(25)와 체인형의 구동수단(26)에 의해 랙(21)과 행거(22)를 각 작업공정 내에서 이동시킨다는 점은 종래의 설비와 동일하지만, 본 발명에서는 각 작업공정 사이에도 체인형의 구동수단(26)을 연결하여 상기 랙과 행거가 상기 체인형의 구동수단에 의해 작업공정 전체를 따라 연속적으로 이동하도록 한 것을 특징으로 하고 있다.5A and 5B are front and side views of an elevator apparatus used in the plating apparatus of the present invention, in which a roller is installed on a hanger 22 having a rack 21, and the roller is a guide rod 25. The guide rod 25 is configured to be able to move forward and intermittently by the chain-shaped driving means 26. That is, the guide rod 25 constituting the elevator device is provided. The movement of the rack 21 and the hanger 22 in each work process by the chain drive means 26 is the same as that of the conventional equipment. However, in the present invention, the chain drive means is also used between the work processes. The rack and the hanger are connected to each other so that the chain and the hanger are continuously moved along the entire work process by the chain drive means.
그런데, 본 발명에서와 같이, 도금 대상물(도시하지 않음)이 각 공정 사이를 연속하여 이동하는 경우에는, 도금욕에서 바이폴러 현상이 필연적으로 발생하게 되고, 이러한 바이폴러 현상은 도금불량율을 증가시키므로, 반드시 그 해결책이 강구되어야 한다.However, as in the present invention, when the plating object (not shown) continuously moves between the respective processes, a bipolar phenomenon inevitably occurs in the plating bath, and this bipolar phenomenon increases the plating defect rate. The solution must be found.
이에 본 발명에서는 상기의 바이폴러 현상을 저감하기 위해서, 도금 대상물이 도금욕 내에 침적(dipping)되기 직전에 약전압을 인가하는데, 전압의 인가(시점)는, 도5b에 도시한 바와 같이, 저항기(32)에 연결된 음극 슬라이드 바(31)의 측면이 가이드로드(25)를 타고 승하강 하는 행거(22)의 한 쪽에 부착된 통전판(음극 슬라이드 바의 측면과 마주보고 있다)과 접촉되는 순간 이루어지게 구성되어 있다. 즉, 본 발명에서는 도금욕 안으로 도금 대상물이 투입될 경우와 도금욕에서 취출될 경우, 행거(22)와 랙(21)을 통해 도금 대상물에 인가되고 있는 강전압이 약전압으로 변경되도록 하기 위해서, 각각 1Ω과 2Ω의 저항기를 별도로 설치하였으며, 도5b에 스프링 형태로 도시된 저항기(32)에 연결된 음극 슬라이드 바(31)의 상단 또는 하단과 행거(22)의 통전판과 동시에 접촉될 때 약전압으로 변경되도록 하였다.In the present invention, in order to reduce the bipolar phenomenon, a weak voltage is applied just before the plating object is dipped in the plating bath. However, the application of the voltage (time) is performed by the resistor as shown in Fig. 5B. At the moment when the side of the negative electrode slide bar 31 connected to the 32 is in contact with an energizing plate (facing the side of the negative electrode slide bar) attached to one side of the hanger 22 ascending and descending on the guide rod 25. It is configured to be made. That is, in the present invention, in order to change the strong voltage applied to the plating object through the hanger 22 and the rack 21 when the plating object is introduced into the plating bath and taken out of the plating bath, the weak voltage is changed. The resistors of 1 kV and 2 kV were separately installed, respectively, and the weak voltage when contacted simultaneously with the top or bottom of the negative electrode slide bar 31 connected to the resistor 32 shown in spring form in FIG. It was changed to.
첨부된 도면중 도7은, 본 발명의 랙을 통해 도금 대상물에 인가되는 전압의 시간에 따른 변화 그래프와, 종래의 방법에 따른 시간-전압 변화 그래프를 비교하여 도시한 도면이다.7 of the accompanying drawings is a view showing a comparison of the time-voltage change graph according to the conventional method and the change graph of the voltage applied to the plating target through the rack of the present invention.
상기 도면에서 참조되듯이, 종래에는 표준전압을 인가한 다음 서서히 전압을 올려 고전압 상태가 되도록 하였기 때문에, 도금 대상물에 가장 먼저 전착(電着)되는 도금층의 금속입자가 조대하여 계면밀착력이 낮았다. 따라서, 그 위로 도금층이 퇴적되더라도 도금층이 쉽게 벗겨지는 단점이 있었으며, 도금 대상물의 형상이 복잡한 경우, 상대적으로 안쪽에 위치하는 부분이나 끝이 뭉툭한 부분은 전기전도율이 좋지 않아 도금이 되지 않는 단점이 있었다.As referred to in the drawing, in the past, since the voltage was gradually raised to a high voltage state after applying a standard voltage, the metal particles of the plating layer first electrodeposited to the plating object were coarse, and thus the interfacial adhesion was low. Therefore, even if a plating layer is deposited thereon, the plating layer is easily peeled off, and in the case where the shape of the plating object is complicated, the relatively inner portion or the blunt end portion has a disadvantage in that plating is not performed due to poor electrical conductivity. .
그러나, 본 발명에서와 같이, 초기에 고전압을 인가하게 되면, 도금 대상물의 표면 바로 위에 퇴적되는 도금층의 입자가 미세화하므로, 계면에서의 밀착력이 크다. 따라서, 제품(도금 대상물)의 피복강도가 높아 내구성 및 내식성이 우수해진다. 게다가, 처음에 고전압을 인가할 경우, 상대적으로 도금이 잘되지 않는 부분도 어느정도 도금층이 퇴적되므로, 불량율이 줄어들게 된다.However, as in the present invention, when a high voltage is initially applied, the particles of the plating layer deposited directly on the surface of the plating object become fine, and thus the adhesion at the interface is large. Therefore, the coating strength of a product (plating object) is high, and durability and corrosion resistance are excellent. In addition, when a high voltage is initially applied, even in a portion where plating is relatively poor, the plating layer is deposited to some extent, thereby reducing the defective rate.
이러한, 전압의 인가 형태는, 통상의 정류기에 의해, 사용자 편의에 따라 조절할 수 있으며, 도면에 도시된 각 단계의 시간도 조절할 수 있다.Such an application form of the voltage may be adjusted according to a user's convenience by a general rectifier, and the time of each step shown in the figure may also be adjusted.
도3과 도4는 본 발명의 랙(21)과 행거(22)의 결합상태를 설명하기 위한 개략적인 사시도이다.3 and 4 are schematic perspective views for explaining the combined state of the rack 21 and the hanger 22 of the present invention.
상기 도면에서 참조되는 바와 같이, 본 발명의 랙(21)은 상단부가 '' 형태로 구부려져 있으며, 행거(22)의 가로대(22a)에도 이 랙(21)의 상단부가 안정적으로 걸릴 수 있도록 홈 형태의 접촉부(23b)가 형성되어 있다.As referenced in the figure, the rack 21 of the present invention has an upper end ' It is bent in the form of ', and the groove 22a of the hanger 22 is formed with a contact portion 23b in the form of a groove so that the upper end of the rack 21 can be stably hung.
따라서, '' 형태로 구부려져 있는 랙(21) 상단의 접촉부(23a)가 상기 행거상에 형성된 접촉부(23b)에 걸리게 됨으로써, 이동시, 전후로 흔들지 않게 되며, 통전상태도 양호하게 되는 장점이 있다.therefore, ' The contact portion 23a of the upper end of the rack 21 bent in the form of 'is caught by the contact portion 23b formed on the hanger, so that it does not shake back and forth during movement, and the energized state is also good.
이상과 같이, 본 발명에 따라 구성되는 니켈-크롬 도금설비는, 각 공정간의 이동이 연속적으로 이루어지기 때문에, 인건비의 절감을 이룰 수 있다.As described above, in the nickel-chromium plating facility constituted according to the present invention, the labor cost can be reduced because the movement between the processes is performed continuously.
또한, 모든 프로세스(공정)는 정해진 조건하에서 규칙적으로 진행되므로, 제품의 도금상태를 일정하게 유지할 수 있다는 장점이 있다.In addition, all processes (processes) are carried out regularly under a predetermined condition, there is an advantage that the plating state of the product can be kept constant.
또한, 종래와 달리, 약전압→고전압→표준전압의 형태로 전압을 인가함으로서, 도금층의 피복력을 향상하여, 최종 제품의 내구성 및 내식성을 우수하게 하는 특징이 있다.In addition, unlike the prior art, by applying a voltage in the form of weak voltage → high voltage → standard voltage, it is characterized by improving the coating force of the plating layer, excellent durability and corrosion resistance of the final product.
게다가, 수세공정에서 발생된 폐수를 이온교환기(41a,41b)로 재처리하여, 청정하게 된 물은 다시 수세공정에 되돌리고, 이온교환기에서 석출된 금속입자만 수거하여 폐기하므로, 환경의 오염을 줄일 수 있다는 장점이 있다.In addition, the wastewater generated in the water washing process is reprocessed by the ion exchangers 41a and 41b, and the purified water is returned to the water washing process again, and only the metal particles precipitated in the ion exchanger are collected and disposed of, thereby reducing environmental pollution. There is an advantage that it can.
Claims (5)
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KR101141723B1 (en) | 2010-01-13 | 2012-05-04 | 신양에너지 주식회사 | Black metal plating method using the same for copper plate with low emissivity and high absorption of solar energy |
KR101363026B1 (en) * | 2012-02-14 | 2014-02-14 | 동양기전 주식회사 | A apparatus for protecting chrome mist from plating bath |
KR101461934B1 (en) | 2014-04-29 | 2014-11-14 | 전진구 | System of iron core-plating process for car headrest |
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FR2883576B1 (en) * | 2005-02-09 | 2009-05-29 | Frederic Vacheron | SURFACE TREATMENT METHOD FOR HOLLOW PIECES, TANK FOR IMPLEMENTING SUCH METHOD, PROCESS AND INSTALLATION FOR CONTINUOUS SURFACE TREATMENT USING SUCH A TANK |
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Cited By (3)
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KR101141723B1 (en) | 2010-01-13 | 2012-05-04 | 신양에너지 주식회사 | Black metal plating method using the same for copper plate with low emissivity and high absorption of solar energy |
KR101363026B1 (en) * | 2012-02-14 | 2014-02-14 | 동양기전 주식회사 | A apparatus for protecting chrome mist from plating bath |
KR101461934B1 (en) | 2014-04-29 | 2014-11-14 | 전진구 | System of iron core-plating process for car headrest |
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