CN101338441A - Matrix for electroplating diamond products and electroplating process thereof - Google Patents
Matrix for electroplating diamond products and electroplating process thereof Download PDFInfo
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- CN101338441A CN101338441A CNA2008101471143A CN200810147114A CN101338441A CN 101338441 A CN101338441 A CN 101338441A CN A2008101471143 A CNA2008101471143 A CN A2008101471143A CN 200810147114 A CN200810147114 A CN 200810147114A CN 101338441 A CN101338441 A CN 101338441A
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- electroplate liquid
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Abstract
The invention relates to a matrix of a diamond product and a plating process thereof. The matrix is characterized in that the matrix consists of electroplated iron or iron-nickel alloy. Electroplating solution adopted by the plating process comprises ferrous sulfate and other sulphates, ferrous chloride and other chlorides, or nickel sulfate, the ferrous sulfate and the chloride. The matrix has the beneficial effects that all of the electroplated iron, the iron-nickel alloy containing 30 to 60 percent of iron and other ferroalloy have higher hardness (HRC35-50) and good bezel setting property for the diamond. Though the matrix is worse than electroplated nickel in wear-resisting property, the matrix is in favor of the exposure of the diamond product and improves the sharpness of the diamond product. Therefore, the matrix is especially suitable for manufacturing the drill pit and the sharper of the diamond. As the cheap iron replaces the expensive nickel, the manufacturing cost of the electroplated diamond product is greatly reduced.
Description
Technical field
The present invention relates to a kind of manufacturing process of diamond composition, especially a kind of carcass of diamond composition and electroplating technology thereof.
Background technology
The carcass of diamond composition is meant and is used to the metal that plates diamond and be connected with the goods matrix in the goods, present known diamond composition carcass all adopts the method for electronickelling or nickelalloy to form, and wherein nickelalloy is limited to nickel cobalt, nickel manganese and nickel cobalt manganese alloy carcass.
Nickel has the good performance that plates to diamond, and itself also has higher wear resistance, good with the switching performance of goods parent, be easy to electroplate, therefore nickel has had the history of decades as the carcass of electroplated diamond goods, but nickel is the higher non-ferrous metal of a kind of price, and the rising of price has been risen more than 5 times the cost of electronickelling tire over past ten years.
Summary of the invention
Purpose of the present invention just provides and a kind ofly can satisfy the requirement of electroplated diamond goods tyre-e/or performance, reduces the carcass material and the electroplating technology of diamond composition production cost simultaneously, to solve the carcass material nickel price problem of higher of prior art.
Technical scheme of the present invention is:
A kind of carcass of diamond composition is characterized in that: this carcass is made of galvanized iron or iron-nickel alloy.
A kind of electroplating technology of carcass of described diamond composition is characterized in that: the electroplate liquid of employing comprises ferrous sulfate and other vitriol, or iron protochloride and other muriate, or single nickel salt, ferrous sulfate and muriate.
Ferrous sulfate in the described electroplate liquid is 150-210g/l; Described other vitriol is sal epsom 125-200g/l, the PH=3.5-4.5 of electroplate liquid, electroplating temperature 25-35 ℃, current density 0.5-2.5A/dm
2
Ferrous sulfate 150-200g/l in the described electroplate liquid; Described other vitriol is ammonium sulfate 80-120g/l, PH=5-5.5, electroplating temperature 25-35 ℃, current density 0.6-0.7A/dm
2
Ferrous ammonium sulphate 350-450g/l in the described electroplate liquid, PH=2.8-3.5, electroplating temperature 25-35 ℃, current density 2-2.5A/dm
2
Iron protochloride 350-400g/l in the described electroplate liquid; Described other muriate is: sodium-chlor 20g/l, Manganous chloride tetrahydrate 10g/l; Also comprise boric acid 2-5g/l, PH=1-1.5, electroplating temperature 30-45 ℃, current density 5-10A/dm
2
Iron protochloride 220-280g/l in the described electroplate liquid, described other muriate are calcium chloride or Repone K 180-200g/l, PH=5-5.5, electroplating temperature 25-40 ℃, current density 2-5A/dm
2
Iron protochloride 350-380g/l in the described electroplate liquid, described other muriate is Manganous chloride tetrahydrate 10-30g/l, and sodium-chlor 10g/l, PH=2.5-3, electroplating temperature 30-35 ℃, current density 1.5-3A/dm
2
Iron protochloride 300-350g/l in the described electroplate liquid, described other muriate is Manganous chloride tetrahydrate 30-50g/l, also has fluoroboric acid 10-15g/l in addition; PH=2.5-3.5, electroplating temperature 25-35 ℃, current density 3-5A/dm
2
The used anode of above acierage technology is a pure iron.
Single nickel salt 180-220g/l in the described electroplate liquid, ferrous sulfate 20-40g/l, described muriate are nickelous chloride 40-55g/l, Manganous chloride tetrahydrate 5-10g/l also has boric acid 40-50g/l, electroplate liquid PH=3-4, electroplating temperature 40-45 ℃, current density 2-5A/dm in addition
2, anode ferronickel ratio 6-10: 1.
Single nickel salt 180-220g/l in the described electroplate liquid, ferrous sulfate 30-50g/l, described muriate are sodium-chlor 25-30g/l and Manganous chloride tetrahydrate 5-10g/l, also have boric acid 40-50g/l, PH=3-4, electroplating temperature 40-45 ℃, current density 2-4A/dm in addition
2, anode ferronickel ratio 6-10: 1.
The present invention adopts plating iron and plating iron nickel carcass, has obtained following technique effect:
1. acierage and iron-holder 30-60% iron-nickel alloy or other iron alloys all have higher hardness (HRC35-50), and diamond is also had the good performance that plates.Though its wear resistance is poorer slightly than electronickelling, help the sword that of diamond composition, improve the sharpness of diamond composition, be particularly suitable for the production of diamond head and diamond abrasive tool.
2. substitute expensive nickel with cheap iron, greatly reduce the production cost of electroplated diamond goods.
Description of drawings
Fig. 1 is for realizing process flow sheet of the present invention.
Embodiment
Below in conjunction with accompanying drawing, be that the invention will be further described for example with the electroplated diamond bit:
1. formulation selection: to the electroplated diamond bit performance demands, adopt pure iron to electroplate carcass according to nature of ground, adopt iron nickel to electroplate carcass, and require to adjust the content of iron by adjusting anodic ferronickel ratio according to tyre-e/or performance to the medium ground to strong stratum.
The electroplating technology of acierage of the present invention or iron alloy has multiple formulations, as long as the plating mode that can obtain acierage or iron alloy can be obtained the carcass of electroplated diamond goods, the present invention considers to add adamantine needs in the diamond composition production process, has selected the acierage and the iron-nickel alloy technology of low electroplating temperature.
Below be the prescription and the electroplating technology of several normally used plating iron and iron-nickel alloy electroplated diamond plating of articles, electroplate the main salt of taking and comprise ferrous sulfate and iron protochloride:
1. ferrous sulfate plating iron prescription and technology:
Embodiment 1: ferrous sulfate 180g/l, sal epsom 150g/l, PH=4.0,30 ℃ of electroplating temperatures, current density 1.5A/dm
2
Embodiment 2: ferrous sulfate 180g/l, ammonium sulfate 100g/l, PH=5.2,30 ℃ of electroplating temperatures, current density 0.6-0.7A/dm
2
Embodiment 3: ferrous ammonium sulphate 400g/l, PH=3.2,30 ℃ of electroplating temperatures, current density 2.2A/dm
2
2. iron protochloride plating iron prescription and technology:
Embodiment 4: iron protochloride 380g/l, sodium-chlor 20g/l, Manganous chloride tetrahydrate 10g/l, boric acid 4g/l, PH=1.3,38 ℃ of electroplating temperatures, current density 7A/dm
2
Embodiment 5: iron protochloride 250g/l, calcium chloride 190g/l, PH=5.2,32 ℃ of electroplating temperatures, current density 3A/dm
2
Embodiment 6: iron protochloride 250g/l, Repone K 190g/l, PH=5.2,32 ℃ of electroplating temperatures, current density 3.8A/dm
2
Embodiment 7: iron protochloride 365g/l, Manganous chloride tetrahydrate 20g/l, sodium-chlor 10g/l, PH=2.8,32 ℃ of electroplating temperatures, current density 2.3A/dm
2
Embodiment 8: iron protochloride 320g/l, Manganous chloride tetrahydrate 35g/l, fluoroboric acid 12g/l, PH=3,30 ℃ of electroplating temperatures, current density 4A/dm
2
The anode material that adopts in the technology of above-mentioned acierage is a pure iron.
3. iron-nickel alloy electroplating formula and technology:
Embodiment 9: single nickel salt 200g/l, nickelous chloride 48g/l, ferrous sulfate 30g/l, boric acid 45g/l, Manganous chloride tetrahydrate 8g/l, PH=3.5,43 ℃ of electroplating temperatures, current density 3A/dm
2, anode ferronickel ratio 8: 1.
Embodiment 10: single nickel salt 200g/l, sodium-chlor 27g/l, ferrous sulfate 40g/l, boric acid 45g/l, Manganous chloride tetrahydrate 5-10g/l, PH=3.5,43 ℃ of electroplating temperatures, current density 3A/dm
2, anode ferronickel ratio 7: 1.
Electroplating technology of the present invention is in concrete implementation process, can in certain scope (disclosed in the technical scheme part), adjust test to each components in proportions and other each processing parameters of electroplate liquid, to obtain electroplating quality preferably about parameter area as the present invention.
The electroplate liquid starting material can be by the buying of chemical reagent shop, and all ingredients should use the CP level, and the plating bath preparation should be used distilled water, to guarantee the platability energy of plating bath, should at first try plating after the plating bath preparation, determines that the plating solution performance rear can be used for plating of articles.Purposes according to goods differs, and matrix can be purchased or processing voluntarily, and the matrix of purchasing or processing must insulate the electroless plating face before groove is electroplated under the matrix through using after the assay was approved, and electroplates by going into plating tank after oil removing and the activation.The mosaic gold hard rock is meant removes cloth on plating face with diamond, the process that allows plated metal that diamond is plated, and according to different needs, used diamond is different.According to the product-use difference, the mosaic gold hard rock can be one deck (promptly once) or multilayer, need treat generally during multi-layer plating that one deck diamond is plated by coating and inlay second layer diamond again after reaching 85-90% that be generally one deck as electroplating emery wheel, electroplated diamond bit needs the 16-20 layer.The last one deck diamond electroplating of goods goes out coating bath after plating and finishing, and carries out follow-up arrangement then and decorates processing.
Plating solution formula adopts CP level reagent, and with the distilled water preparation, boric acid dissolves with 80 ℃ of warm water, and plating bath prepares and filter back examination plating, and the qualified back of examination plating is used for drill bit as formal electroplating bath solution and electroplates.
2. production process:
Bit matrix is processed voluntarily, carrying out insulating bag after the matrix that processes is qualified by inspection pricks, going into must be through oil removing and activation before the groove, matrix after the activation connects electroplating power supply immediately after hot water cleans, chargedly go into ready coating bath, after the empty plating of 30min, inlay the first layer diamond (deserving to be called sand down), sand two parts on sand and the end face are gone up in the inside and outside footpath of protecting of the last sand branch of diamond head, when interior external diameter plating reaches dimensional requirement (generally needing 3-4 layer diamond), need interior external diameter to be insulated with mould, continue end face and partly go up the sand process, according to the diamond grit difference, end face generally needs 16-20 layer diamond, and the selection of diamond grit is that the nature of ground of creeping into according to drill bit determines.
Claims (12)
1, a kind of carcass of diamond composition is characterized in that: this carcass is made of galvanized iron or iron-nickel alloy.
2, the electroplating technology of the carcass of the described diamond composition of a kind of claim 1 is characterized in that: the electroplate liquid of employing comprises ferrous sulfate and other vitriol, or iron protochloride and other muriate, or single nickel salt, ferrous sulfate and muriate.
3, the electroplating technology of the carcass of diamond composition according to claim 2 is characterized in that: the ferrous sulfate in the described electroplate liquid is 150-210g/l; Described other vitriol is sal epsom 125-200g/l, the PH=3.5-4.5 of electroplate liquid, electroplating temperature 25-35 ℃, current density 0.5-2.5A/dm
2
4, the electroplating technology of the carcass of diamond composition according to claim 2 is characterized in that: the ferrous sulfate 150-200g/l in the described electroplate liquid; Described other vitriol is ammonium sulfate 80-120g/l, PH=5-5.5, electroplating temperature 25-35 ℃, current density 0.6-0.7A/dm
2
5, the electroplating technology of the carcass of diamond composition according to claim 2 is characterized in that: the ferrous ammonium sulphate 350-450g/l in the described electroplate liquid, PH=2.8-3.5, electroplating temperature 25-35 ℃, current density 2-2.5A/dm
2
6, the electroplating technology of the carcass of diamond composition according to claim 2 is characterized in that: the iron protochloride 350-400g/l in the described electroplate liquid; Described other muriate is: sodium-chlor 20g/l, Manganous chloride tetrahydrate 10g/l; Also comprise boric acid 2-5g/l, PH=1-1.5, electroplating temperature 30-45 ℃, current density 5-10A/dm
2
7, the electroplating technology of the carcass of diamond composition according to claim 2, it is characterized in that: the iron protochloride 220-280g/l in the described electroplate liquid, described other muriate is calcium chloride or Repone K 180-200g/l, PH=5-5.5, electroplating temperature 25-40 ℃, current density 2-5A/dm
2
8, the electroplating technology of the carcass of diamond composition according to claim 2, it is characterized in that: the iron protochloride 350-380g/l in the described electroplate liquid, described other muriate is Manganous chloride tetrahydrate 10-30g/l, and sodium-chlor 10g/l, PH=2.5-3, electroplating temperature 30-35 ℃, current density 1.5-3A/dm
2
9, the electroplating technology of the carcass of diamond composition according to claim 2 is characterized in that: the iron protochloride 300-350g/l in the described electroplate liquid, and described other muriate is Manganous chloride tetrahydrate 30-50g/l, also has fluoroboric acid 10-15g/l in addition; PH=2.5-3.5, electroplating temperature 25-35 ℃, current density 3-5A/dm
2
10, according to the electroplating technology of the carcass of any one described diamond composition of claim 2~9, it is characterized in that: used anode is a pure iron.
11, the electroplating technology of the carcass of diamond composition according to claim 2, it is characterized in that: the single nickel salt 180-220g/l in the described electroplate liquid, ferrous sulfate 20-40g/l, described muriate is nickelous chloride 40-55g/l, Manganous chloride tetrahydrate 5-10g/l also has boric acid 40-50g/l, electroplate liquid PH=3-4 in addition, electroplating temperature 40-45 ℃, current density 2-5A/dm
2, anode ferronickel ratio 6-10: 1.
12, the electroplating technology of the carcass of diamond composition according to claim 2, it is characterized in that: the single nickel salt 180-220g/l in the described electroplate liquid, ferrous sulfate 30-50g/l, described muriate is sodium-chlor 25-30g/l and Manganous chloride tetrahydrate 5-10g/l, also has boric acid 40-50g/l in addition, PH=3-4, electroplating temperature 40-45 ℃, current density 2-4A/dm
2, anode ferronickel ratio 6-10: 1.
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CN101858343A (en) * | 2010-05-27 | 2010-10-13 | 浏阳湘德机械制造厂 | Cutting ring and glasses plate and processing method thereof |
CN102443839A (en) * | 2010-10-15 | 2012-05-09 | 深圳市常兴金刚石磨具有限公司 | Method for electroplating diamond grinding apparatus |
CN102534707A (en) * | 2011-12-31 | 2012-07-04 | 兰桥昌 | Electroplating solution and method using the same in manufacturing diamond drill bit matrix |
CN102560575A (en) * | 2011-12-31 | 2012-07-11 | 兰桥昌 | Electroplating solution and method for manufacturing casing of diamond grinding tools with same |
CN102560585A (en) * | 2012-03-01 | 2012-07-11 | 湖北盛友钻石材料有限公司 | Method and device for manufacturing diamond wire saw |
CN102586843A (en) * | 2012-03-15 | 2012-07-18 | 武汉万邦激光金刚石工具有限公司 | Manufacturing method for long life electroplated diamond bit |
CN103046087A (en) * | 2012-12-17 | 2013-04-17 | 武汉天立表面技术有限公司 | Pure iron plating method and electroplating liquid thereof |
CN106929875A (en) * | 2017-03-23 | 2017-07-07 | 黎明职业大学 | A kind of method that ferrate is prepared based on carbon plate plating iron |
CN108085730A (en) * | 2016-11-23 | 2018-05-29 | 丹阳市雅本化工技术有限公司 | A kind of processing technology of ultrasonic electroplating of diamond drilling bit |
CN110315415A (en) * | 2018-03-29 | 2019-10-11 | 株式会社迪思科 | Cyclic annular grinding tool |
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2008
- 2008-08-19 CN CNA2008101471143A patent/CN101338441A/en active Pending
Cited By (17)
Publication number | Priority date | Publication date | Assignee | Title |
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CN101858343B (en) * | 2010-05-27 | 2012-09-05 | 浏阳湘德机械制造厂 | Cutting ring and glasses plate and processing method thereof |
CN101858343A (en) * | 2010-05-27 | 2010-10-13 | 浏阳湘德机械制造厂 | Cutting ring and glasses plate and processing method thereof |
CN102443839A (en) * | 2010-10-15 | 2012-05-09 | 深圳市常兴金刚石磨具有限公司 | Method for electroplating diamond grinding apparatus |
CN102534707A (en) * | 2011-12-31 | 2012-07-04 | 兰桥昌 | Electroplating solution and method using the same in manufacturing diamond drill bit matrix |
CN102560575A (en) * | 2011-12-31 | 2012-07-11 | 兰桥昌 | Electroplating solution and method for manufacturing casing of diamond grinding tools with same |
CN102560585A (en) * | 2012-03-01 | 2012-07-11 | 湖北盛友钻石材料有限公司 | Method and device for manufacturing diamond wire saw |
CN102586843B (en) * | 2012-03-15 | 2014-05-21 | 武汉万邦激光金刚石工具有限公司 | Manufacturing method for long life electroplated diamond bit |
CN102586843A (en) * | 2012-03-15 | 2012-07-18 | 武汉万邦激光金刚石工具有限公司 | Manufacturing method for long life electroplated diamond bit |
CN103046087A (en) * | 2012-12-17 | 2013-04-17 | 武汉天立表面技术有限公司 | Pure iron plating method and electroplating liquid thereof |
CN103046087B (en) * | 2012-12-17 | 2015-09-02 | 武汉天立表面技术有限公司 | A kind of method and electroplate liquid thereof plating pure iron |
CN108085730A (en) * | 2016-11-23 | 2018-05-29 | 丹阳市雅本化工技术有限公司 | A kind of processing technology of ultrasonic electroplating of diamond drilling bit |
CN106929875A (en) * | 2017-03-23 | 2017-07-07 | 黎明职业大学 | A kind of method that ferrate is prepared based on carbon plate plating iron |
CN106929875B (en) * | 2017-03-23 | 2019-02-22 | 黎明职业大学 | A method of ferrate is prepared based on carbon plate plating iron |
CN110315415A (en) * | 2018-03-29 | 2019-10-11 | 株式会社迪思科 | Cyclic annular grinding tool |
CN110315415B (en) * | 2018-03-29 | 2023-02-21 | 株式会社迪思科 | Ring-shaped grinding tool for cutting using cutting water mixed with carbon dioxide |
CN110983143A (en) * | 2019-04-08 | 2020-04-10 | 成都惠灵丰金刚石钻头有限公司 | PDC matrix drill bit powder formula |
CN110983143B (en) * | 2019-04-08 | 2021-04-23 | 成都惠灵丰金刚石钻头有限公司 | PDC matrix drill bit powder formula |
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