CN114959814A - Method for quickly electroplating high-conductivity and high-heat-conductivity copper layer - Google Patents
Method for quickly electroplating high-conductivity and high-heat-conductivity copper layer Download PDFInfo
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- 238000009713 electroplating Methods 0.000 title claims abstract description 90
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 title claims abstract description 79
- 229910052802 copper Inorganic materials 0.000 title claims abstract description 78
- 239000010949 copper Substances 0.000 title claims abstract description 78
- 238000000034 method Methods 0.000 title claims abstract description 42
- 239000002245 particle Substances 0.000 claims abstract description 14
- 239000002131 composite material Substances 0.000 claims description 29
- 229910052751 metal Inorganic materials 0.000 claims description 19
- 239000002184 metal Substances 0.000 claims description 19
- 238000007747 plating Methods 0.000 claims description 16
- 239000002243 precursor Substances 0.000 claims description 11
- UMGDCJDMYOKAJW-UHFFFAOYSA-N thiourea Chemical compound NC(N)=S UMGDCJDMYOKAJW-UHFFFAOYSA-N 0.000 claims description 6
- JZCCFEFSEZPSOG-UHFFFAOYSA-L copper(II) sulfate pentahydrate Chemical compound O.O.O.O.O.[Cu+2].[O-]S([O-])(=O)=O JZCCFEFSEZPSOG-UHFFFAOYSA-L 0.000 claims description 5
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 claims description 4
- 238000003756 stirring Methods 0.000 claims description 4
- KWSLGOVYXMQPPX-UHFFFAOYSA-N 5-[3-(trifluoromethyl)phenyl]-2h-tetrazole Chemical compound FC(F)(F)C1=CC=CC(C2=NNN=N2)=C1 KWSLGOVYXMQPPX-UHFFFAOYSA-N 0.000 claims description 3
- JPVYNHNXODAKFH-UHFFFAOYSA-N Cu2+ Chemical compound [Cu+2] JPVYNHNXODAKFH-UHFFFAOYSA-N 0.000 claims description 3
- 239000003109 Disodium ethylene diamine tetraacetate Substances 0.000 claims description 3
- ZGTMUACCHSMWAC-UHFFFAOYSA-L EDTA disodium salt (anhydrous) Chemical compound [Na+].[Na+].OC(=O)CN(CC([O-])=O)CCN(CC(O)=O)CC([O-])=O ZGTMUACCHSMWAC-UHFFFAOYSA-L 0.000 claims description 3
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Natural products NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 claims description 3
- 229910001431 copper ion Inorganic materials 0.000 claims description 3
- 235000019301 disodium ethylene diamine tetraacetate Nutrition 0.000 claims description 3
- 239000001509 sodium citrate Substances 0.000 claims description 3
- NLJMYIDDQXHKNR-UHFFFAOYSA-K sodium citrate Chemical compound O.O.[Na+].[Na+].[Na+].[O-]C(=O)CC(O)(CC([O-])=O)C([O-])=O NLJMYIDDQXHKNR-UHFFFAOYSA-K 0.000 claims description 3
- 229910001379 sodium hypophosphite Inorganic materials 0.000 claims description 3
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 claims description 2
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 claims description 2
- 230000002378 acidificating effect Effects 0.000 claims description 2
- 229910052804 chromium Inorganic materials 0.000 claims description 2
- 239000011651 chromium Substances 0.000 claims description 2
- 229910052759 nickel Inorganic materials 0.000 claims description 2
- 229910000623 nickel–chromium alloy Inorganic materials 0.000 claims description 2
- 229910052710 silicon Inorganic materials 0.000 claims description 2
- 239000010703 silicon Substances 0.000 claims description 2
- 239000000126 substance Substances 0.000 claims description 2
- 239000000758 substrate Substances 0.000 claims 1
- 230000008021 deposition Effects 0.000 abstract description 6
- 238000004519 manufacturing process Methods 0.000 abstract description 6
- 238000009825 accumulation Methods 0.000 abstract description 3
- 230000007812 deficiency Effects 0.000 abstract description 2
- 238000002360 preparation method Methods 0.000 abstract 1
- 230000010287 polarization Effects 0.000 description 3
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 239000013078 crystal Substances 0.000 description 2
- 239000002253 acid Substances 0.000 description 1
- 230000004913 activation Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 229910052927 chalcanthite Inorganic materials 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- QUQFTIVBFKLPCL-UHFFFAOYSA-L copper;2-amino-3-[(2-amino-2-carboxylatoethyl)disulfanyl]propanoate Chemical compound [Cu+2].[O-]C(=O)C(N)CSSCC(N)C([O-])=O QUQFTIVBFKLPCL-UHFFFAOYSA-L 0.000 description 1
- 239000008367 deionised water Substances 0.000 description 1
- 229910021641 deionized water Inorganic materials 0.000 description 1
- 238000007714 electro crystallization reaction Methods 0.000 description 1
- 238000007772 electroless plating Methods 0.000 description 1
- 239000003792 electrolyte Substances 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000011159 matrix material Substances 0.000 description 1
- 229910021645 metal ion Inorganic materials 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000006911 nucleation Effects 0.000 description 1
- 238000010899 nucleation Methods 0.000 description 1
- 239000004065 semiconductor Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
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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
- C25D5/00—Electroplating characterised by the process; Pretreatment or after-treatment of workpieces
- C25D5/18—Electroplating using modulated, pulsed or reversing current
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D3/00—Electroplating: Baths therefor
- C25D3/02—Electroplating: Baths therefor from solutions
- C25D3/38—Electroplating: Baths therefor from solutions of copper
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D7/00—Electroplating characterised by the article coated
- C25D7/12—Semiconductors
- C25D7/123—Semiconductors first coated with a seed layer or a conductive layer
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/50—Manufacturing or production processes characterised by the final manufactured product
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- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
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- Organic Chemistry (AREA)
- Electroplating Methods And Accessories (AREA)
Abstract
本发明涉及铜的电镀工艺,具体涉及一种快速电镀高导电高导热铜层的方法,用于解决现有脉冲电镀铜层方法由于沉积速率较慢导致铜层制备产能较低,成本较高的不足之处。该快速电镀高导电高导热铜层的方法采用双极性脉冲电镀,并且将电镀过程分为三个阶段,其中第一阶段和第二阶段采用低电流密度在种子层表面形成的附着致密层,第三阶段采用高电流密度在附着致密层上形成的铜颗粒堆积层和致密填充层;本发明可实现铜层的快速沉积,且所沉积的铜层的电学性能接近纯铜,提高了铜层制备产能,降低了生产成本。The invention relates to a copper electroplating process, in particular to a method for rapidly electroplating a copper layer with high electrical conductivity and high thermal conductivity, which is used to solve the problem of low production capacity and high cost of copper layer preparation due to the slow deposition rate of the existing pulse electroplating copper layer method. deficiencies. The method for rapidly electroplating a copper layer with high electrical conductivity and high thermal conductivity adopts bipolar pulse electroplating, and divides the electroplating process into three stages. The third stage adopts the copper particle accumulation layer and dense filling layer formed on the adhesion dense layer with high current density; the invention can realize the rapid deposition of the copper layer, and the electrical properties of the deposited copper layer are close to pure copper, and the copper layer is improved. The production capacity is reduced, and the production cost is reduced.
Description
技术领域technical field
本发明涉及铜的电镀工艺,具体涉及一种快速电镀高导电高导热铜层的方法。The invention relates to a copper electroplating process, in particular to a method for rapidly electroplating a copper layer with high electrical conductivity and high thermal conductivity.
背景技术Background technique
电镀铜层作为高导电和高导热材料,并且具有较高性价比,广泛应用于半导体器件和光伏产品。电镀铜层的常用方法为脉冲电镀,其原理是利用电流(或电压)脉冲的张弛增加阴极的活化极化和降低阴极的浓差极化;当电流导通时,接近阴极的金属离子充分地被沉积;当电流关断时,阴极周围的放电离子恢复到初始浓度;这样周期的连续重复脉冲电流主要用于金属离子的还原,从而改善镀层的物理化学性能。在电镀过程中,随着电流密度的增加,铜层的电阻率会先急剧下降再缓慢上升,这是由于低电流密度下,铜电结晶瞬间成核,表面成核数目少,晶粒间较大,随着电流密度的增加,晶核数量增多,但晶粒直径较小,不利于互连,因此现有脉冲电镀方法通常采用电流密度为2~4A/dm2,但在该电流密度下铜层沉积速率较小导致电镀铜层的产能降低、成本增高。Electroplated copper layer is widely used in semiconductor devices and photovoltaic products as a material with high electrical conductivity and high thermal conductivity, and has a high cost performance. The common method of electroplating copper layer is pulse electroplating. The principle is to use the relaxation of current (or voltage) pulse to increase the activation polarization of the cathode and reduce the concentration polarization of the cathode; are deposited; when the current is turned off, the discharge ions around the cathode return to the initial concentration; such a cycle of continuous and repeated pulse current is mainly used for the reduction of metal ions, thereby improving the physical and chemical properties of the coating. During the electroplating process, with the increase of the current density, the resistivity of the copper layer will first decrease sharply and then slowly increase. This is because the copper electrocrystallization nucleates instantaneously at low current density, the number of surface nucleation is small, and the grains are relatively nucleated. As the current density increases, the number of crystal nuclei increases, but the crystal grain diameter is small, which is not conducive to interconnection. Therefore, the current pulse plating method usually adopts a current density of 2-4A/dm 2 , but at this current density The lower deposition rate of the copper layer results in lower productivity and higher cost of electroplated copper layers.
发明内容SUMMARY OF THE INVENTION
本发明的目的是解决现有脉冲电镀铜层方法由于沉积速率较慢导致铜层制备产能较低,成本较高的不足之处,而提供一种快速电镀高导电高导热铜层的方法。The purpose of the present invention is to solve the shortcomings of the existing pulse electroplating copper layer method due to the slow deposition rate resulting in low copper layer production capacity and high cost, and to provide a rapid electroplating method for high electrical conductivity and high thermal conductivity copper layer.
为了解决上述现有技术所存在的不足之处,本发明提供了如下技术解决方案:In order to solve the deficiencies existing in the above-mentioned prior art, the present invention provides the following technical solutions:
一种快速电镀高导电高导热铜层的方法,其特殊之处在于,包括如下步骤:A method for rapidly electroplating a copper layer with high electrical conductivity and high thermal conductivity is special in that it includes the following steps:
步骤1、制备复合电镀溶液;Step 1, prepare a composite electroplating solution;
所述复合电镀溶液包括金属铜离子和金属铜颗粒,所述金属铜颗粒均一悬浮于复合电镀溶液中;复合电镀溶液为酸性;The composite electroplating solution includes metal copper ions and metal copper particles, and the metal copper particles are uniformly suspended in the composite electroplating solution; the composite electroplating solution is acidic;
步骤2、电镀铜层;Step 2, electroplating copper layer;
采用双极性脉冲电镀,将恒流电源的正极与金属铜电连接,负极与待镀前驱体电连接,待镀前驱体上镀有种子层;将所述金属铜和待镀前驱体置于步骤1所制备的复合电镀溶液中;Using bipolar pulse electroplating, the positive electrode of the constant current power supply is electrically connected to the metal copper, and the negative electrode is electrically connected to the precursor to be plated, and the precursor to be plated is plated with a seed layer; the metal copper and the precursor to be plated are placed on the in the composite electroplating solution prepared in step 1;
控制复合电镀溶液的温度为25℃~80℃,并对复合电镀溶液进行搅拌;The temperature of the composite electroplating solution is controlled to be 25°C to 80°C, and the composite electroplating solution is stirred;
设置恒流电源参数,快速电镀高导电高导热铜层;Set constant current power supply parameters, quickly electroplating copper layer with high electrical conductivity and high thermal conductivity;
电镀过程分为三个阶段,三个阶段的恒流电源参数分别为:The electroplating process is divided into three stages, and the constant current power supply parameters of the three stages are:
第一阶段电流密度为0.5~2A/dm2,正向电流脉冲占空比为30%~70%,反向电流脉冲占空比为0%~20%,电镀时间为60s;In the first stage, the current density is 0.5~2A/dm 2 , the forward current pulse duty ratio is 30%~70%, the reverse current pulse duty ratio is 0%~20%, and the electroplating time is 60s;
第二阶段电流密度设置为2~5A/dm2,正向电流脉冲占空比为30%~70%,反向电流脉冲占空比为0%~20%,电镀时间为120s;In the second stage, the current density is set to 2~5A/dm 2 , the forward current pulse duty ratio is 30%~70%, the reverse current pulse duty ratio is 0%~20%, and the electroplating time is 120s;
第三阶段电流密度设置为17~20A/dm2,正向电流脉冲占空比为30%~70%,反向电流脉冲占空比为0%~20%,电镀时间为200s~600s。In the third stage, the current density is set to 17-20A/dm 2 , the forward current pulse duty ratio is 30%-70%, the reverse current pulse duty ratio is 0%-20%, and the electroplating time is 200s-600s.
进一步地,步骤2中,所述电镀过程分为三个阶段,三个阶段的恒流电源参数分别为:Further, in step 2, the electroplating process is divided into three stages, and the constant current power supply parameters of the three stages are:
第一阶段电流密度为2A/dm2,正向电流脉冲占空比为70%,反向电流脉冲占空比为0%,电镀时间为60s;In the first stage, the current density is 2A/dm 2 , the forward current pulse duty cycle is 70%, the reverse current pulse duty cycle is 0%, and the electroplating time is 60s;
第二阶段电流密度设置为5A/dm2,正向电流脉冲占空比为70%,反向电流脉冲占空比为20%,电镀时间为120s;In the second stage, the current density is set to 5A/dm 2 , the forward current pulse duty cycle is 70%, the reverse current pulse duty cycle is 20%, and the plating time is 120s;
第三阶段电流密度设置为17.7A/dm2,正向电流脉冲占空比为70%,反向电流脉冲占空比为20%,电镀时间为200s。In the third stage, the current density was set to 17.7 A/dm 2 , the duty cycle of the forward current pulse was 70%, the duty cycle of the reverse current pulse was 20%, and the electroplating time was 200s.
进一步地,步骤1中,所述复合电镀溶液包括五水合硫酸铜(CuSO4·5H2O),五水合硫酸铜和金属铜颗粒之间的质量比为5:1。Further, in step 1, the composite electroplating solution includes copper sulfate pentahydrate (CuSO4·5H2O), and the mass ratio between copper sulfate pentahydrate and metal copper particles is 5:1.
进一步地,步骤1中,所述金属铜颗粒直径为0.1~20μm;金属铜颗粒直径较小,会导致成本增高,金属铜颗粒直径过大,会减弱吸附力。Further, in step 1, the diameter of the metal copper particles is 0.1-20 μm; the smaller diameter of the metal copper particles will increase the cost, and the excessively large diameter of the metal copper particles will weaken the adsorption force.
进一步地,步骤1中,所述复合电镀溶液还包括次亚磷酸钠、柠檬酸钠、乙二胺四乙酸二钠、硫脲,复合电镀溶液的pH为5。Further, in step 1, the composite electroplating solution further includes sodium hypophosphite, sodium citrate, disodium EDTA, and thiourea, and the pH of the composite electroplating solution is 5.
进一步地,步骤2中,所述种子层采用物理真空法或者化学镀法制备,种子层为铜层或镍层或铬层或镍铬合金层,种子层的厚度为0.1~10μm;种子层为电镀提供一层导电层。Further, in step 2, the seed layer is prepared by a physical vacuum method or an electroless plating method, the seed layer is a copper layer or a nickel layer or a chromium layer or a nickel-chromium alloy layer, and the thickness of the seed layer is 0.1-10 μm; Electroplating provides a conductive layer.
进一步地,步骤2中,所述待镀前驱体为设置有透明导电层的异质结电池或硅基体电池。Further, in step 2, the precursor to be plated is a heterojunction cell or a silicon matrix cell provided with a transparent conductive layer.
与现有技术相比,本发明的有益效果是:Compared with the prior art, the beneficial effects of the present invention are:
本发明一种快速电镀高导电高导热铜层的方法,其采用双极性脉冲电镀,并且将电镀过程分为三个阶段,其中第一阶段和第二阶段采用低电流密度在种子层表面形成的附着致密层,第三阶段采用高电流密度在附着致密层上形成的铜颗粒堆积层和致密填充层;本发明可实现铜层的快速沉积,且所沉积的铜层的电学性能接近纯铜,提高了铜层制备产能,降低了生产成本。The present invention is a method for rapidly electroplating a copper layer with high electrical conductivity and high thermal conductivity, which adopts bipolar pulse electroplating, and divides the electroplating process into three stages, wherein the first stage and the second stage are formed on the surface of the seed layer by using low current density In the third stage, a copper particle accumulation layer and a dense filling layer formed on the adhesion dense layer with high current density are used; the invention can realize the rapid deposition of the copper layer, and the electrical properties of the deposited copper layer are close to pure copper , the production capacity of the copper layer is improved, and the production cost is reduced.
具体实施方式Detailed ways
下面结合示例性实施例对本发明作进一步地说明。The present invention will be further described below in conjunction with exemplary embodiments.
实施例1Example 1
一种快速电镀高导电高导热铜层的方法,包括如下步骤:A method for rapidly electroplating a copper layer with high electrical conductivity and high thermal conductivity, comprising the following steps:
步骤1、制备复合电镀溶液;Step 1, prepare a composite electroplating solution;
取500g五水合硫酸铜(CuSO4·5H2O)、50g次亚磷酸钠、50g柠檬酸钠、10g乙二胺四乙酸二钠、25g硫脲依次加入去离子水中搅拌使其溶解;加入硫酸调整pH为5;再加入100g平均直径为5μm的金属铜颗粒,通过搅拌使得弱酸溶液将铜粉表面的杂质去除,得到复合电镀溶液;Take 500g of copper sulfate pentahydrate (CuSO 4 ·5H 2 O), 50g of sodium hypophosphite, 50g of sodium citrate, 10g of disodium EDTA, 25g of thiourea and then add in deionized water and stir to dissolve; add sulfuric acid Adjust the pH to 5; then add 100 g of metal copper particles with an average diameter of 5 μm, and stir the weak acid solution to remove impurities on the surface of the copper powder to obtain a composite electroplating solution;
步骤2、电镀铜层;Step 2, electroplating copper layer;
采用双极性脉冲电镀,将恒流电源的正极与金属铜电连接,负极与待镀前驱体电连接,待镀前驱体上镀有种子层,种子层的厚度为0.1~10μm;Using bipolar pulse electroplating, the positive electrode of the constant current power supply is electrically connected to the metal copper, and the negative electrode is electrically connected to the precursor to be plated, and the precursor to be plated is plated with a seed layer, and the thickness of the seed layer is 0.1-10 μm;
将所述金属铜和待镀前驱体置于步骤1所制备的复合电镀溶液中;placing the metallic copper and the precursor to be plated in the composite electroplating solution prepared in step 1;
控制复合电镀溶液的温度为50℃;Control the temperature of the composite electroplating solution to 50°C;
复合电镀溶液中设置有搅拌装置,转速设置为600r/min,可以使电镀过程中阴极附件电解液中的金属铜离子浓度保持正常,降低浓差极化和提高阴极电流密度,加快沉积速度;A stirring device is arranged in the composite electroplating solution, and the rotating speed is set to 600r/min, which can keep the concentration of metal copper ions in the electrolyte of the cathode accessories in the electroplating process normal, reduce the concentration polarization and improve the cathode current density, and accelerate the deposition speed;
设置恒流电源参数快速电镀高导电高导热铜层;Set constant current power supply parameters to quickly electroplate high electrical conductivity and high thermal conductivity copper layer;
电镀过程分为三个阶段,三个阶段的恒流电源参数分别为:The electroplating process is divided into three stages, and the constant current power supply parameters of the three stages are:
第一阶段电流密度为2A/dm2,正向电流脉冲占空比为70%,反向电流脉冲占空比为0%,电镀时间为60s;In the first stage, the current density is 2A/dm 2 , the forward current pulse duty cycle is 70%, the reverse current pulse duty cycle is 0%, and the electroplating time is 60s;
第二阶段电流密度设置为5A/dm2,正向电流脉冲占空比为70%,反向电流脉冲占空比为20%,电镀时间为120s;In the second stage, the current density is set to 5A/dm 2 , the forward current pulse duty cycle is 70%, the reverse current pulse duty cycle is 20%, and the plating time is 120s;
第三阶段电流密度设置为17.7A/dm2,正向电流脉冲占空比为70%,反向电流脉冲占空比为20%,电镀时间为200s;In the third stage, the current density is set to 17.7A/dm 2 , the duty cycle of the forward current pulse is 70%, the duty cycle of the reverse current pulse is 20%, and the electroplating time is 200s;
第三阶段结束后得到铜层,铜层包括第一阶段和第二阶段采用的低电流密度形成的附着致密层,以及第三阶段采用的高电流密度形成的铜颗粒堆积层和致密填充层,铜层总厚度为10.25μm,方阻为0.00185Ω/□,体电阻率为1.85μΩ·cm。After the third stage, a copper layer is obtained, and the copper layer includes the adhesion dense layer formed by the low current density adopted in the first and second stages, and the copper particle accumulation layer and dense filling layer formed by the high current density adopted in the third stage, The total thickness of the copper layer is 10.25 μm, the square resistance is 0.00185Ω/□, and the volume resistivity is 1.85 μΩ·cm.
实施例2Example 2
本实施例步骤2中,控制复合电镀溶液的温度为25℃;In step 2 of this embodiment, the temperature of the composite electroplating solution is controlled to be 25°C;
所述电镀过程分为三个阶段,三个阶段的恒流电源参数分别为:The electroplating process is divided into three stages, and the constant current power supply parameters of the three stages are:
第一阶段电流密度为1A/dm2,正向电流脉冲占空比为40%,反向电流脉冲占空比为10%,电镀时间为60s;In the first stage, the current density is 1A/dm 2 , the forward current pulse duty cycle is 40%, the reverse current pulse duty cycle is 10%, and the plating time is 60s;
第二阶段电流密度设置为3A/dm2,正向电流脉冲占空比为40%,反向电流脉冲占空比为10%,电镀时间为120s;In the second stage, the current density is set to 3A/dm 2 , the forward current pulse duty cycle is 40%, the reverse current pulse duty cycle is 10%, and the electroplating time is 120s;
第三阶段电流密度设置为18.5A/dm2,正向电流脉冲占空比为40%,反向电流脉冲占空比为10%,电镀时间为300s;In the third stage, the current density is set to 18.5A/dm 2 , the forward current pulse duty cycle is 40%, the reverse current pulse duty cycle is 10%, and the plating time is 300s;
第三阶段结束后得到铜层,铜层总厚度为15.74μm,方阻为0.00128Ω/□,体电阻率为1.92μΩ·cm。After the third stage, a copper layer was obtained. The total thickness of the copper layer was 15.74 μm, the square resistance was 0.00128Ω/□, and the volume resistivity was 1.92 μΩ·cm.
本实施例其余设置均与实施例1相同。The rest of the settings in this embodiment are the same as those in Embodiment 1.
实施例3Example 3
本实施例步骤2中,控制复合电镀溶液的温度为80℃;In step 2 of this embodiment, the temperature of the composite electroplating solution is controlled to be 80°C;
所述电镀过程分为三个阶段,三个阶段的恒流电源参数分别为:The electroplating process is divided into three stages, and the constant current power supply parameters of the three stages are:
第一阶段电流密度为2A/dm2,正向电流脉冲占空比为50%,反向电流脉冲占空比为15%,电镀时间为60s;In the first stage, the current density is 2A/dm 2 , the forward current pulse duty cycle is 50%, the reverse current pulse duty cycle is 15%, and the electroplating time is 60s;
第二阶段电流密度设置为4A/dm2,正向电流脉冲占空比为50%,反向电流脉冲占空比为15%,电镀时间为120s;In the second stage, the current density is set to 4A/dm 2 , the duty cycle of the forward current pulse is 50%, the duty cycle of the reverse current pulse is 15%, and the electroplating time is 120s;
第三阶段电流密度设置为18.8A/dm2,正向电流脉冲占空比为50%,反向电流脉冲占空比为15%,电镀时间为400s;In the third stage, the current density is set to 18.8A/dm 2 , the forward current pulse duty cycle is 50%, the reverse current pulse duty cycle is 15%, and the plating time is 400s;
第三阶段结束后得到铜层,铜层总厚度为20.63μm,方阻为0.00093Ω/□,体电阻率为1.86μΩ·cm。After the third stage, a copper layer is obtained. The total thickness of the copper layer is 20.63 μm, the square resistance is 0.00093Ω/□, and the volume resistivity is 1.86 μΩ·cm.
本实施例其余设置均与实施例1相同。The rest of the settings in this embodiment are the same as those in Embodiment 1.
实施例4Example 4
本实施例步骤2中,控制复合电镀溶液的温度为80℃;In step 2 of this embodiment, the temperature of the composite electroplating solution is controlled to be 80°C;
所述电镀过程分为三个阶段,三个阶段的恒流电源参数分别为:The electroplating process is divided into three stages, and the constant current power supply parameters of the three stages are:
第一阶段电流密度为0.5A/dm2,正向电流脉冲占空比为30%,反向电流脉冲占空比为0%,电镀时间为60s;In the first stage, the current density is 0.5A/dm 2 , the forward current pulse duty cycle is 30%, the reverse current pulse duty cycle is 0%, and the electroplating time is 60s;
第二阶段电流密度设置为2A/dm2,正向电流脉冲占空比为30%,反向电流脉冲占空比为0%,电镀时间为120s;In the second stage, the current density is set to 2A/dm 2 , the forward current pulse duty cycle is 30%, the reverse current pulse duty cycle is 0%, and the electroplating time is 120s;
第三阶段电流密度设置为19.1A/dm2,正向电流脉冲占空比为30%,反向电流脉冲占空比为0%,电镀时间为500s;In the third stage, the current density is set to 19.1A/dm 2 , the forward current pulse duty cycle is 30%, the reverse current pulse duty cycle is 0%, and the plating time is 500s;
第三阶段结束后得到铜层,铜层总厚度为25.19μm,方阻为0.000784Ω/□,体电阻率为1.96μΩ·cm。After the third stage, a copper layer was obtained. The total thickness of the copper layer was 25.19 μm, the square resistance was 0.000784Ω/□, and the volume resistivity was 1.96 μΩ·cm.
本实施例其余设置均与实施例1相同。The rest of the settings in this embodiment are the same as those in Embodiment 1.
实施例5Example 5
本实施例步骤2中,控制复合电镀溶液的温度为80℃;In step 2 of this embodiment, the temperature of the composite electroplating solution is controlled to be 80°C;
所述电镀过程分为三个阶段,三个阶段的恒流电源参数分别为:The electroplating process is divided into three stages, and the constant current power supply parameters of the three stages are:
第一阶段电流密度为2A/dm2,正向电流脉冲占空比为70%,反向电流脉冲占空比为20%,电镀时间为60s;In the first stage, the current density is 2A/dm 2 , the forward current pulse duty cycle is 70%, the reverse current pulse duty cycle is 20%, and the electroplating time is 60s;
第二阶段电流密度设置为5A/dm2,正向电流脉冲占空比为70%,反向电流脉冲占空比为20%,电镀时间为120s;In the second stage, the current density is set to 5A/dm 2 , the forward current pulse duty cycle is 70%, the reverse current pulse duty cycle is 20%, and the plating time is 120s;
第三阶段电流密度设置为18.6A/dm2,正向电流脉冲占空比为70%,反向电流脉冲占空比为20%,电镀时间为600s;In the third stage, the current density is set to 18.6A/dm 2 , the forward current pulse duty cycle is 70%, the reverse current pulse duty cycle is 20%, and the plating time is 600s;
第三阶段结束后得到铜层,铜层总厚度为30.38μm,方阻为0.000676Ω/□,体电阻率为2.03μΩ·cm。After the third stage, a copper layer was obtained. The total thickness of the copper layer was 30.38 μm, the square resistance was 0.000676Ω/□, and the volume resistivity was 2.03 μΩ·cm.
本实施例其余设置均与实施例1相同。The rest of the settings in this embodiment are the same as those in Embodiment 1.
实施例1至5,第三阶段的恒流电源参数设置及所制备铜层的性能如表1所示:Examples 1 to 5, the parameter settings of the constant current power supply in the third stage and the performance of the prepared copper layer are shown in Table 1:
表1Table 1
从表1可以得出,在其余设置相同的情况下,第三阶段中,随着电镀时间的增加,镀层的厚度呈线性增加,而镀铜层的体电阻率接近纯铜的体电阻率(1.76μΩ·cm),由此来看,本发明所制备的铜层的电性能具有纯铜的电学性能。It can be concluded from Table 1 that in the third stage, with the increase of the plating time, the thickness of the plating layer increases linearly, and the volume resistivity of the copper plating layer is close to that of pure copper ( 1.76 μΩ·cm), from this point of view, the electrical properties of the copper layer prepared by the present invention have the electrical properties of pure copper.
以上实施例仅用以说明本发明的技术方案,而非对其限制,对于本领域的普通专业技术人员来说,可以对前述各实施例所记载的具体技术方案进行修改,或者对其中部分技术特征进行等同替换,而这些修改或者替换,并不使相应技术方案的本质脱离本发明所保护技术方案的范围。The above embodiments are only used to illustrate the technical solutions of the present invention, but not to limit them. For those skilled in the art, the specific technical solutions recorded in the foregoing embodiments can be modified, or some of the technical solutions can be modified. The features are equivalently replaced, and these modifications or replacements do not make the essence of the corresponding technical solutions deviate from the scope of the technical solutions protected by the present invention.
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| CN113881983A (en) * | 2021-10-19 | 2022-01-04 | 广州市慧科高新材料科技有限公司 | Through hole pulse electroplating liquid and through hole pulse electroplating coating method |
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