Leveling agent, metal plating composition containing same, preparation method therefor and use thereof

Information

  • Patent Grant
  • 11332471
  • Patent Number
    11,332,471
  • Date Filed
    Friday, December 15, 2017
    7 years ago
  • Date Issued
    Tuesday, May 17, 2022
    2 years ago
Abstract
Disclosed are a leveling agent, a metal plating composition containing same, and a preparation method therefor and the use thereof. The raw materials of the metal electroplating composition comprise a metal plating solution and a leveling agent; the metal plating solution comprises a copper salt, an acidic electrolyte, a source of halide ions and water; and the leveling agent is a compound of formula I. The metal plating composition can be used in the processes of printed circuit board electroplating and integrated circuit copper interconnection electroplating, can achieve the effects of no voids or defects, low purity in the plating layer, good plating homogeneity, a dense structure and small surface roughness, and has better industrial application value.
Description
CROSS-REFERENCE TO RELATED APPLICATIONS

This application is a 371 National Phase of PCT/CN2017/116441 filed Dec. 15, 2017, which claims the benefit of Chinese Patent Application No. 201710613256.3, filed on Jul. 25, 2017. The entire disclosures of the above applications are incorporated herein by reference.


FIELD OF INVENTION

The present invention relates to the field of semiconductor materials, specifically relates to a leveling agent, metal electroplating composition containing the same, preparation method and uses thereof.


PRIOR ARTS

With the development of Very Large Scale Integration (VLSI) and Ultra Large Scale Integration (ULSI), the integration is increasing and the circuit components are getting denser and denser, chip interconnection becomes a key factor affecting the chip performance. The reliability of the interconnect structures is crucial to the success of VLSI and ULSI and the increase in circuit density. However, due to size limitations of the circuitry, the size reduction of interconnects in VLSI and ULSI technologies has raised additional demands on the processing capacity, which comprise the precise processing of multilayer, high aspect ratio structural features.


The width, aperture size, and other feature size of the interconnect decrease with the increase of circuit density. However, the thickness of the dielectric layer will not decrease proportionally. As a result, the aspect ratio feature increases. Secondly, in the back end of line process of integrated circuits, copper has gradually replaced aluminum as the predominant material used in interconnect technology of VLSI interconnection. In current chip manufacturing, the wiring and interconnection of the chip are almost entirely copper plated.


Copper has a lower resistivity (about 35% lower) and a higher resistance to electromigration (about twice as aluminum) than aluminum. Moreover, copper has good thermal conductivity, which is advantageous to the devices of multilayer integration with higher circuit density and current density. Copper can be coated on the substrate by electroplating, sputtering, physical vapor deposition, and chemical vapor deposition. The damascene process (Damascus process) in the form of electroplating is generally considered to be the best method for preparing copper interconnects. The copper damascene process can be filled with micronanoscale pores by electroplating, which has the characteristics of high deposition speed and low cost.


However, with the continuous development of the integrated circuit technology, the requirements for filling the pores of nanoscale are becoming more stringent. Researchers from all over the world are eager to study electroplating methods, electroplating solutions and additives for printed circuit board plating and integrated circuit copper interconnect plating processes to achieve the effects that no hole or defect exists between the metal plating layers, low plating layer impurity, good uniform-plating property, compact structure, and small surface roughness.


Generally, the leveling agents for copper plating can better level the sediment across the surface of the substrate, but tend to impair the uniform-plating capacity of the plating bath. The uniform-plating capacity is defined as the ratio of the thickness of the copper sediment in the center of the pore to the thickness at its surface.


Patent Application No. CN105683250A has disclosed a polymer leveling agent comprising an imidazole structure, which can be used to solve the problem of uniform-plating on PCB plating. However, it is not effective in the application of nano scale Damascus copper interconnect plating.


Therefore, there is an urgent need in the art to develop electroplating methods, electroplating solutions and additives used for printed circuit board electroplating and integrated circuit copper interconnection electroplating processes, which achieve the effects that no hole or defect between the metal plating layers, low plating layer impurity, good uniform-plating property, compact structure, and small surface roughness.


CONTENT OF THE PRESENT INVENTION

An object of the present invention is to provide a leveling agent, metal electroplating composition containing the same, preparation method and uses thereof, in order to solve the problem that the metal plating layers made by the prior electroplating method, electroplating solution and additives have holes and defects, high plating layer impurity, poor uniform-plating property, poor structure density, and rough surface. The leveling agent and the metal electroplating composition containing the leveling agent can be used for printed circuit board electroplating and integrated circuit copper interconnection electroplating processes, which can achieve the effects of no hole or defect in the metal plating layers, low plating layer impurity, good uniform-plating property, compact structure and small surface roughness, and has better industrial application value.


The present invention solves the above technical problems by the following technical solutions.


The first aspect of the present invention provides a use of the compound of formula I as a leveling agent in metal electroplating composition




embedded image



wherein,


R1 is C1-C5 alkyl, propargyl, allyl or benzyl;


R2 is H, C1-C5 alkyl, hydroxy-substituted C1-C5 alkyl, unsaturated five-membered heterocyclic substituted C1-C3 alkyl, phenyl, halogenated phenyl, benzyl, halogenated benzyl or a hydroxyl-substituted benzyl;


R3 is substituted or unsubstituted phenyl, pyridyl, naphthyl, hydroxy-substituted naphthyl, thienyl, furyl or indolyl;


R4 is H or C1-C5 alkyl;


The substituent of the substituted phenyl is selected from the group consisting of halogen, C1-C5 alkyl, nitro, methoxy, hydroxy and C1-C3 alkylamino; the substituents are the same or different when there are more than one substituents attached;


the heteroatom in the unsaturated five-membered heterocyclic ring is selected from the group consisting of O, N and S, and the number of heteroatoms is 1 to 3, the heteroatoms are the same or different when there are more than one heteroatoms.


In the use,


preferably, R1 is methyl, propyl, benzyl, propargyl or allyl;


preferably, R2 is benzyl, methyl, hydroxyethyl, thiophene-substituted methyl, furan-substituted ethyl, monohalogenated benzyl (such as




embedded image



or hydroxy-substituted benzyl (such as




embedded image


preferably, R3 is pyridyl (such as




embedded image



thienyl (such as




embedded image



indolyl (such as




embedded image



naphthyl (such as




embedded image



hydroxy-substituted naphthyl (such as




embedded image



phenyl, hydroxy-substituted phenyl (such as




embedded image



monohalogenated phenyl (such as




embedded image



methylphenyl (such as




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nitrophenyl (such as




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methoxyphenyl (such as




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or dimethylamino-substituted phenyl (such as




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preferably, R4 is H or methyl;


the use, wherein,


the leveling agent is preferably selected from the group consisting of:


Compound 1: R1=Propyl-; R2=Bn-; R3=Ph-; R4═H—;


Compound 2: R1=Propyl-; R2=Bn-; R3=2-Cl-Ph-; R4═H—;


Compound 3: R1=Propyl-; R2=Bn-; R3=3-Cl-Ph-; R4═H—;


Compound 4: R1=Propyl-; R2=Bn-; R3=4-Cl-Ph-; R4═H—;


Compound 5: R1=Propyl-; R2=Bn-; R3=4-Br-Ph-; R4═H—;


Compound 6: R1=Propyl-; R2=Bn-; R3=2-F-Ph-; R4═H—;


Compound 7: R1=Propyl-; R2=Bn-; R3=4-Me-Ph-; R4═H—;


Compound 8: R1=Propyl-; R2=Bn-; R3=3,4,5-(MeO)3-Ph-; R4═H—;


Compound 9: R1=Propyl-; R2=Bn-; R3=4-NO2-Ph-; R4═H—;


Compound 10: R1=Propyl-; R2=Bn-; R3=4-(N,N—(CH3)2)-Ph-; R4═H—;


Compound 11: R1=Propyl-; R2=Bn-;




embedded image



R4═H—;


Compound 12: R1=Propyl-; R2=Bn-;




embedded image



R4═H—;


Compound 13: R1=Propyl-; R2=Bn-;




embedded image



R4═H—;


Compound 14: R1=Propyl-; R2=Bn-;




embedded image



R4═H—;


Compound 15: R1=Propyl-; R2=Bn-;




embedded image



R4═H—;


Compound 16: R1=Propyl-; R2=Bn-; R3=Ph-; R4═CH3—;


Compound 17: R1=Propyl-; R2=Bn-; R3=4-MeO-Ph-; R4═CH3—;


Compound 18: R1=Propyl-; R2=Bn-; R3=2-OH-Ph-; R4═CH3—;


Compound 19: R1=Propyl-; R2=Bn-; R3=4-OH-Ph-; R4═CH3—;


Compound 20: R1=Propyl-; R2=Bn-; R3=4-Br-Ph-; R4═CH3—;


Compound 21: R1=Propyl-;




embedded image



R3=2-OH-Ph-; R4═CH3—;


Compound 22: R1=Propyl-; R2=2-Cl-Bn-; R3=2-OH-Ph-; R4═CH3—;


Compound 23: R1=Propyl-; R2=3-Cl-Bn-; R3=2-OH-Ph-; R4═CH3—;


Compound 24: R1=Propyl-; R2=4-Cl-Bn-; R3=2-OH-Ph-; R4—CH3—;


Compound 25: R1=Propyl-; R2=4-Br-Bn-; R3=2-OH-Ph-; R4═CH3—;


Compound 26: R1=Propyl-; R2=4-F-Bn-; R3=2-OH-Ph-; R4═CH3—;


Compound 27: R1=Propyl-;




embedded image



R3=2-OH-Ph-; R4═CH3—;


Compound 28: R1=Propyl-;




embedded image



R3=2-OH-Ph-; R4═CH3—;


Compound 29: R1=Propyl-; R2=4-OH-Bn-; R3=2-OH-Ph-; R4═CH3—;


Compound 30: R1=Propargyl-; R2=Bn-; R3=3,4,5-(MeO)3-Ph-; R4═H—;


Compound 31: R1=Propargyl-; R2=Bn-;




embedded image



R4═H—;


Compound 32: R1=Propargyl-; R2=Bn-; R3=4-(N,N—(CH3)2)-Ph-; R4═H—;


Compound 33: R1=Propargyl-; R2=Bn-; R3=2-OH-Ph-; R4═CH3—;


Compound 34: R1=Bn-; R2=Bn-; R3=3,4,5-(MeO)3-Ph-; R4═H—; and


Compound 35: R1=Bn-; R2=Bn-; R3=2-OH-Ph-; R4═CH3—.


In the present invention, the compound represented by formula I is prepared in accordance with the method disclosed in Chinese Patent Application CN201610853873.6.


The second aspect of the present invention provides a metal electroplating composition, wherein the raw material of the metal electroplating composition comprises a metal electroplating liquid and the leveling agent as defined in the first aspect of the present invention; the metal electroplating liquid comprises a copper salt, acidic electrolyte, halide ions source and water.


The metal electroplating composition, wherein,


The copper salt is preferably selected from the group consisting of copper sulfate, copper halide, copper acetate, copper nitrate, copper fluoroborate, copper alkylsulfonate, copper aryl sulfonate, copper sulfamate and copper gluconate; the copper alkylsulfonate is preferably selected from the group consisting of copper methanesulfonate, copper ethanesulfonate and copper propanesulfonate; the copper aryl sulfonate is preferably selected from the group consisting of copper phenyl sulfonate, copper phenolsulfonate and copper p-toluenesulfonate. The molar concentration of the copper ions in the metal electroplating liquid is 0.15-2.85 mol/L.


The acidic electrolyte is preferably selected from the group consisting of sulfuric acid, phosphoric acid, acetic acid, fluoroboric acid, sulfamic acid, alkyl sulfonic acid, aryl sulfonic acid and hydrochloric acid. The alkyl sulfonic acid is preferably selected from the group consisting of methanesulfonic acid, ethanesulfonic acid, propanesulfonic acid and trifluoromethanesulfonic acid; the aryl sulfonic acid is preferably selected from the group consisting of phenylsulfonic acid, phenolsulfonic acid and toluenesulfonic acid. In each liter of the metal electroplating composition, the mass of the acidic electrolyte is preferably 1-300 g.


The halide ions source is preferably a chloride ions source. The chloride ions source is preferably selected from the group consisting of copper chloride, tin chloride and hydrochloric acid. The concentration of the halide ions of the halide ions source is preferably 0-100 ppm but not 0, more preferably 50-100 ppm.


In the present invention, the metal electroplating liquid is preferably an electroplating copper solution SYSD2110, and the manufacturer thereof is Shanghai Xinyang Semiconductor Material Co., Ltd. The preparation of SYSD2110 can refer to the method disclosed in Chinese Patent No. CN100529194C.


In the present invention, the raw material of the metal electroplating composition further comprises an accelerator, wherein the accelerator (also referred to as a brightener) refers to an organic additive capable of increasing the plating rate of the plating bath, and the accelerator is the accelerator acceptable in the art. The accelerator is preferably selected from the group consisting of N,N-dimethyl-disulfenyl carbamic acid-(3-sulfopropyl) ester, 3-mercapto-propylsulfonic acid-(3-sulfopropyl) ester, 3-mercapto-propyl sulfonate sodium salt; disulfenyl carbonate-o-ethyl ester-s-ester and 3-mercapto-1-propane sulfonate potassium salt, disulfopropyl disulfide, 3-(benzothiazolyl-s-sulfenyl)propyl sulfonate sodium salt, pyridinium propyl sulfonyl betaine, 1-sodium-3-mercapto propane-1-sulfonate, N,N-dimethyl-disulfenyl carbamic acid-(3-sulfoethyl) ester, 3-mercapto-ethyl propyl sulfonic acid-(3-sulfoethyl) ester, 3-mercapto-ethyl sulfonate sodium salt, carbonic acid-disulfenyl-o-ethyl ester-s-ester and 3-mercapto-1-ethanesulfonate potassium salt, disulfoethyl disulfide, 3-(benzothiazolyl-s-sulfenyl)ethyl sulfonate sodium salt, pyridinium ethyl sulfonyl betaine and 1-sodium-3-mercaptoethane-1-sulfonate; the concentration of the accelerator is preferably 0.1 ppm-1000 ppm.


In a preferred embodiment of the present invention, the accelerator is UPD3115A, which is applied by Shanghai Xinyang Semiconductor Materials Co., Ltd.


In the present invention, the raw material of the metal electroplating composition further comprises an inhibitor, and the inhibitor refers to an organic additive capable of suppressing the rate of metal electroplating. The inhibitor is preferably selected from the group consisting of polypropylene glycol copolymer, polyethylene glycol copolymer, ethylene oxide-propylene oxide (EO/PO) copolymer and butanol-ethylene oxide-propylene oxide copolymer; the butanol-ethylene oxide-propylene oxide copolymer preferably has a weight-average molecular weight of 100-100,000, more preferably 500-10,000; the concentration of the inhibitor is preferably 1-10000 ppm, more preferably 5-10000 ppm.


In a preferred embodiment of the invention, the inhibitor is UPD3115S, which is applied by Shanghai Xinyang Semiconductor Materials Co., Ltd.


In the present invention, the concentration of the leveling agent is the concentration acceptable in the art, preferably 1-10 ppm, more preferably 5-10 ppm.


In a preferred embodiment of the invention, the raw material of the metal electroplating composition consists of the metal electroplating liquid, the leveling agent, the accelerator and the inhibitor.


The third aspect of the present invention provides a method for preparing the metal electroplating composition as defined in the second aspect of the present invention, which preferably comprises mixing the raw material components uniformly.


The fourth aspect of the present invention provides the use of the metal electroplating composition as defined in the second aspect of the present invention in printed circuit board electroplating and integrated circuit copper interconnection electroplating processes, the use preferably comprises:


(1) contacting the substrate to be electroplated with the metal electroplating composition;


(2) applying an electric current for electroplating.


In step (1), the substrate is any substrate acceptable in the art, preferably a wafer or chip of a printed circuit board or an integrated circuit.


In step (2), the current density of the electroplating is acceptable in the art, preferably 0.1-10 ASD, more preferably 0.3-5 ASD, the most preferably 0.5-1.5 ASD;


in step (2), the electroplating time is acceptable in the art, preferably 53-110 s, preferably 80-110 s.


in step (2), the electroplating temperature is acceptable in the art, preferably 10-65° C., more preferably 10-35° C., the most preferably 20-30° C.


In a preferred embodiment of the invention, step (2) is preferably carried out in three steps:


in the first step, the current density is 0.1-0.5 ASD, more preferably 0.3 ASD; the electroplating time is 3-20 s, more preferably 10 s; the electroplating temperature is 10-65° C., more preferably 10-35° C., the most preferably 20-30° C., for example 25° C.;


in the second step, the current density is 0.5-1.5 ASD, more preferably 1.0 ASD; the electroplating time is 20-30s, more preferably 25s; the electroplating temperature is 10-65° C., more preferably 10-35° C., the most preferably 20-30° C., for example 25° C.;


in the third step, the current density is 1-10 ASD, more preferably 5 ASD; the electroplating time is 30-60s, more preferably 45s; the electroplating temperature is 10-65° C., more preferably 10-35° C., the most preferably 20-30° C., for example 25° C.


In the present invention, the term “Propyl-” refers to propyl, of which structure is




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In the present invention, the term “Propargyl-” refers to propargyl, of which structure is




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In the present invention, the term “Bn-” refers to benzyl, of which structure is




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In the present invention, the term “Ph-” refers to phenyl, of which structure is




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In the present invention, the term “C1-C5 alkyl” is preferably methyl, ethyl, n-propyl, isopropyl, n-butyl, isobutyl, tert-butyl, n-pentyl, isopentyl or neopentyl. Unless otherwise specified, propyl, butyl or pentyl refers to n-propyl, n-butyl or n-pentyl, respectively.


In the present invention, the term “unsaturated five-membered heterocyclic ring” preferably has aromaticity. The unsaturated five-membered heterocyclic ring is preferably furan, thiophene, pyrazole, imidazole, thiazole, triazole or tetrazolium and the like.


In the present invention, the term “hydroxy-substituted X group” refers to an X group substituted by one or more than one hydroxy (the number of hydroxy depends on the number of H atoms, for example 1-6, preferably 1-3), wherein the position of the hydroxy is optional. For example, “hydroxy substituted benzyl” refers to a benzyl group substituted with one or more hydroxy, including but not limited to




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and the like.


In the present invention, the term “halogenated Y group” refers to a Y group substituted by one or more than one halogens (the number of halogens may be determined according to the number of H, for example 1 to 6, preferably 1 to 3). For example, halogenated phenyl refers to a phenyl substituted with one or more than one halogens, wherein the halogens may be the same or different, including but not limited to




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and the like.


In the present invention, the term “halogen” refers to F, Cl, Br or I.


In the present invention, the term “concentration” refers to the concentration of each substance in 1 L metal electroplating liquid.


In the present invention, unless otherwise specified in the context, the following abbreviations should have the following meanings: A=amperes; A/dm2=amps per square decimeter=ASD; ° C.=degrees Celsius; ppm=parts per million. Unless otherwise indicated, all % refer to mass percentage. All numerical ranges are inclusive and can be combined in any order, but it is obvious that the sum of such numerical ranges are limited to 100%.


In the present invention, “feature” refers to the geometry on the substrate. “Aperture” refers to a sunken feature that comprises a through hole and a blind channel. “Halide” refers to fluoride, chloride, bromide and iodide.


In the present invention, the temperature of “ice bath” refers to −5° C.−5° C., preferably −5° C.−0° C.


Based on the common knowledge in the art, the above various preferred conditions can be optionally combined to obtain preferred embodiments of the present invention.


The reagents and raw materials used in the present invention are commercially available.


The positive effects of the present invention are as follows:


the metal electroplating composition of the present invention comprises a leveling agent represented by the formula I. The metal electroplating composition can be used for printed circuit board electroplating and integrated circuit copper interconnection electroplating processes, which achieves the effects of free of holes and defects, low plated layer impurity, good uniform-plating property, compact structure, and small surface roughness. Furthermore, the metal electroplating composition has good thermal reliability and uniform-plating property, and can solve the problem of orifice sealing, and has good industrial application value.







EMBODIMENT
Preparation Embodiments: Preparation of Metal Electroplating Compositions 1-35 and Comparative Metal Electroplating Compositions 1-6

The components of the metal electroplating compositions 1-35 and the comparative metal electroplating compositions 1-6 are shown in Table 1, wherein, the metal ions source and the electrolyte is provided by electroplating copper solution of the trademark SYSD2110, which is purchased from Shanghai Xinyang Semiconductor Materials Co., Ltd. The accelerator of the trademark UPD3115 A is purchased from Shanghai Xinyang Semiconductor Materials Co., Ltd. The inhibitor of the trademark UPD3115S is purchased from Shanghai Xinyang Semiconductor Materials Co., Ltd.

















TABLE 1










Amount






Electro-



of


Amount



plating



electroplating
Amount
Amount
of


Formula
copper


Leveling
copper
of
of
leveling


No.
solution
Accelerator
Inhibitor
agent
solution
accelerator
inhibitor
agent







Metal
SYSD2110
UPD3115 A
UPD3115S
Compound 1
1 L
10 ppm
100 ppm
1 ppm


electroplating


composition 1


Metal
SYSD2110
UPD3115 A
UPD3115S
Compound 2
1 L
50 ppm
500 ppm
5 ppm


electroplaing


composition 2


Metal
SYSD2110
UPD3115 A
UPD3115S
Compound 3
1 L
100 ppm 
1000 ppm 
10 ppm 


electroplating


composition 3


Metal
SYSD2110
N,N-
Butanol-
Compound 4
1 L
10 ppm
100 ppm
1 ppm


electroplating

dimethyl-
ethylene


composition 4

disulfenyl
oxide-




carbamic
alkylene




acid-(3-
oxide,




sulfopropyl)ester
Mw =





1000


Metal
SYSD2110
1-sodium-3-
Butanol-
Compound 5
1 L
50 ppm
500 ppm
5 ppm


electroplating

mercapto
ethylene


composition 5

propane-1-
oxide-




sulfonate
alkylene





oxide,





Mw =





3000


Metal
SYSD2110
3-
Butanol-
Compound 6
1 L
100 ppm 
1000 ppm 
10 ppm 


electroplating

(benzothiazolyl-
ethylene


composition 6

s-
oxide-




sulfenyl)propyl
alkylene




sulfonate
oxide,




sodium salt
Mw =





10000


Metal
SYSD2110
UPD3115 A
UPD3115S
Compound 7
1 L
10 ppm
100 ppm
1 ppm


electroplating


composition 7


Metal
SYSD2110
UPD3115 A
UPD3115S
Compound 8
1 L
50 ppm
500 ppm
5 ppm


electroplating


composition 8


Metal
SYSD2110
UPD3115 A
UPD3115S
Compound 9
1 L
100 ppm 
1000 ppm 
10 ppm 


electroplating


composition 9


Metal
SYSD2110
N,N-
Butanol-
Compound
1 L
10 ppm
100 ppm
1 ppm


electroplating

dimethyl-
ethylene
10


composition

disulfenyl
oxide-


10

carbamic
alkylene




acid-(3-
oxide,




sulfopropyl)ester
Mw = 1000


Metal
SYSD2110
1-sodium-3-
Butanol-
Compound
1 L
50 ppm
500 ppm
5 ppm


electroplating

mercapto
ethylene
11


composition

propane-1-
oxide-


11

sulfonate
alkylene





oxide,





Mw = 3000


Metal
SYSD2110
3-
Butanol-
Compound
1 L
100 ppm 
1000 ppm 
10 ppm 


electroplating

(benzothiazolyl-
ethylene
12


composition

s-
oxide-


12

sulfenyl)propyl
alkylene




sulfonate
oxide,




sodium salt
Mw = 10000


Metal
SYSD2110
UPD3115 A
UPD3115S
Compound
1 L
10 ppm
100 ppm
1 ppm


electroplating



13


composition


13


Metal
SYSD2110
UPD3115 A
UPD3115S
Compound
1 L
50 ppm
500 ppm
5 ppm


electroplating



14


composition


14


Metal
SYSD2110
UPD3115 A
UPD3115S
Compound
1 L
100 ppm 
1000 ppm 
10 ppm 


electroplating



15


composition


15


Metal
SYSD2110
N,N-
Butanol-
Compound
1 L
10 ppm
100 ppm
1 ppm


electroplating

dimethyl-
ethylene
16


composition

disulfenyl
oxide-


16

carbamic
alkylene




acid-(3-
oxide,




sulfopropyl)ester
Mw = 1000


Metal
SYSD2110
1-sodium-3-
Butanol-
Compound
1 L
50 ppm
500 ppm
5 ppm


electroplating

mercapto
ethylene
17


composition

propane-1-
oxide-


17

sulfonate
alkylene





oxide,





Mw = 3000


Metal
SYSD2110
3-
Butanol-
Compound
1 L
100 ppm 
1000 ppm 
10 ppm 


electroplating

(benzothiazolyl-
ethylene
18


composition

s-
oxide-


18

sulfenyl)propyl
alkylene




sulfonate
oxide,




sodium salt
Mw = 10000


Metal
SYSD2110
UPD3115 A
UPD3115S
Compound
1 L
10 ppm
100 ppm
1 ppm


electroplating



19


composition


19


Metal
SYSD2110
UPD3115 A
UPD3115S
Compound
1 L
50 ppm
500 ppm
5 ppm


electroplating



20


composition


20


Metal
SYSD2110
UPD3115 A
UPD3115S
Compound
1 L
100 ppm 
1000 ppm 
10 ppm 


electroplating



21


composition


21


Metal
SYSD2110
N,N-
Butanol-
Compound
1 L
10 ppm
100 ppm
1 ppm


electroplating

dimethyl-
ethylene
22


composition

disulfenyl
oxide-


22

carbamic
alkylene




acid-(3-
oxide,




sulfopropyl)ester
Mw = 1000


Metal
SYSD2110
1-sodium-3-
Butanol-
Compound
1 L
50 ppm
500 ppm
5 ppm


electroplating

mercapto
ethylene
23


composition

propane-1-
oxide-


23

sulfonate
alkylene





oxide,





Mw = 3000


Metal
SYSD2110
3-
Butanol-
Compound
1 L
100 ppm 
1000 ppm 
10 ppm 


electroplating

(benzothiazolyl-
ethylene
24


composition

s-
oxide-


24

sulfenyl)propyl
alkylene




sulfonate
oxide,




sodium salt
Mw = 10000


Metal
SYSD2110
UPD3115 A
UPD3115S
Compound
1 L
10 ppm
100 ppm
1 ppm


electroplating



25


composition


25


Metal
SYSD2110
UPD3115 A
UPD3115S
Compound
1 L
50 ppm
500 ppm
5 ppm


electroplating



26


composition


26


Metal
SYSD2110
UPD3115 A
UPD3115S
Compound
1 L
100 ppm 
1000 ppm 
10 ppm 


electroplating



27


composition


27


Metal
SYSD2110
N,N-
Butanol-
Compound
1 L
10 ppm
100 ppm
1 ppm


electroplating

dimethyl-
ethylene
28


composition

disulfenyl
oxide-


28

carbamic
alkylene




acid-(3-
oxide,




sulfopropyl)ester
Mw = 1000


Metal
SYSD2110
1-sodium-3-
Butanol-
Compound
1 L
50 ppm
500 ppm
5 ppm


electroplating

mercapto
ethylene
29


composition

propane-1-
oxide-


29

sulfonate
alkylene





oxide,





Mw = 3000


Metal
SYSD2110
3-
Butanol-
Compound
1 L
100 ppm 
1000 ppm 
10 ppm 


electroplating

(benzothiazolyl-
ethylene
30


composition

s-
oxide-


30

sulfenyl)propyl
alkylene




sulfonate
oxide,




sodium salt
Mw = 10000


Metal
SYSD2110
UPD3115 A
UPD3115S
Compound
1 L
10 ppm
100 ppm
1 ppm


electroplating



31


composition


31


Metal
SYSD2110
UPD3115 A
UPD3115S
Compound
1 L
50 ppm
500 ppm
5 ppm


electroplating



32


composition


32


Metal
SYSD2110
UPD3115 A
UPD3115S
Compound
1 L
100 ppm 
1000 ppm 
10 ppm 


electroplating



33


composition


33


Metal
SYSD2110
N,N-
Butanol-
Compound
1 L
10 ppm
100 ppm
1 ppm


electroplating

dimethyl-
ethylene
34


composition

disulfenyl
oxide-


34

carbamic
alkylene




acid-(3-
oxide,




sulfopropyl)ester
Mw = 1000


Metal
SYSD2110
1-sodium-3-
Butanol-
Compound
1 L
50 ppm
500 ppm
5 ppm


electroplating

mercapto
ethylene
35


composition

propane-1-
oxide-


35

sulfonate
alkylene





oxide,





Mw = 3000


Comparative
SYSD2110
UPD3115 A
UPD3115S
The
1 L
10 ppm
100 ppm
1 ppm


Metal



polymer


electroplating



obtained


composition 1



by the






method of






Example 1






in






CN105705491 A


Comparative
SYSD2110
UPD3115 A
UPD3115S
The
1 L
50 ppm
500 ppm
5 ppm


Metal



polymer


electroplating



obtained


composition 2



by the






method of






Example 2






in






CN105705491 A


Comparative
SYSD2110
UPD3115 A
UPD3115S
The
1 L
100 ppm 
1000 ppm 
10 ppm 


Metal



polymer


electroplating



obtained


composition 3



by the






method of






Example 3






in






CN105705491 A


Comparative
SYSD2110
N,N-
Butanol-
The
1 L
10 ppm
100 ppm
1 ppm


Metal

dimethyl-
ethylene
polymer


electroplating

disulfenyl
oxide-
obtained


composition 4

carbamic
alkylene
by the




acid-(3-
oxide,
method of




sulfopropyl)ester
Mw = 1000
Example 1






in






CN105705491 A


Comparative
SYSD2110
1-sodium-3-
Butanol-
The
1 L
50 ppm
500 ppm
5 ppm


Metal

mercapto
ethylene
polymer


electroplating

propane-1-
oxide-
obtained


composition 5

sulfonate
alkylene
by the





oxide,
method of





Mw = 3000
Example 2






in






CN105705491 A


Comparative
SYSD2110
3-
Butanol-
The
1 L
100 ppm 
1000 ppm 
10 ppm 


Metal

(benzothiazolyl-
ethylene
polymer


electroplating

s-
oxide-
obtained


composition 6

sulfenyl)propyl
alkylene
by the




sulfonate
oxide,
method of




sodium salt
Mw = 10000
Example 3






in






CN105705491 A









Application Embodiments 1-35 and Comparative Application Embodiments 1-6

In the present invention, Application embodiments 1-35 and Comparative application embodiments 1-6 are carried out with metal electroplating compositions 1-35 and comparative metal electroplating compositions 1-6, respectively. The parameters of the electroplating process are carried out according to the parameters listed in Table 2.










TABLE 2








Pattern wafer with PVD seed layer (graphics)














Electroplating
Current
Electroplating
Electroplating











Electroplating target
parameters
density
time
temperature















Embodiment
Three-step
Step 1
0.1
 3 s
20° C.


1, 4, 7, 10,
electroplating

ASD




13, 16, 19,

Step 2
0.5
20 s
20° C.


22, 25, 28,


ASD




31, 34

Step 3
 1 ASD
30 s
20° C.


Embodiment
Three-step
Step 1
0.3
10 s
25° C.


2, 5, 8, 11,
electroplating

ASD




14, 17, 20,

Step 2
1.0
25 s
25° C.


23, 26, 29,


ASD




32, 35

Step 3
 5 ASD
45 s
25° C.


Embodiment
Three-step
Step 1
0.5
20 s
30° C.


3, 6, 9, 12,
electroplating

ASD




15, 18, 21,

Step 2
1.5
30 s
30° C.


24, 27, 30,


ASD




33

Step 3
10 ASD
60 s
30° C.


Comparative
Three-step
Step 1
0.1
 3 s
20° C.


Application
electroplating

ASD




Embodiment 1

Step 2
0.5
20 s
20° C.





ASD






Step 3
 1 ASD
30 s
20° C.


Comparative
Three-step
Step 1
0.3
10 s
25° C.


Application
electroplating

ASD




Embodiment 2

Step 2
1.0
25 s
25° C.





ASD






Step 3
 5 ASD
45 s
25° C.


Comparative
Three-step
Step 1
0.5
20 s
30° C.


Application
electroplating

ASD




Embodiment

Step 2
1.5
30 s
30° C.


3


ASD






Step 3
10 ASD
60 s
30° C.


Comparative
Three-step
Step 1
0.1
 3 s
20° C.


Application
electroplating

ASD




Embodiment 4

Step 2
0.5
20 s
20° C.





ASD






Step 3
 1 ASD
30 s
20° C.


Comparative
Three-step
Step 1
0.3
10 s
25° C.


Application
electroplating

ASD




Embodiment

Step 2
1.0
25 s
25° C.


5


ASD






Step 3
 5 ASD
45 s
25° C.


Comparative
Three-step
Step 1
0.5
20 s
30° C.


Application
electroplating

ASD




Embodiment

Step 2
1.5
30 s
30° C.


6


ASD






Step 3
10 ASD
60 s
30° C.









Application Effects


The application effect is shown in Table 3. Wherein, the impurity content is analyzed by elemental analysis of combustion method, and the holes condition, the uniform-plating property, the structure compactness and the surface roughness are observed by SEM electron microscopy.
















TABLE 3







Impurity
Impurity
Impurity







in
in
in




plated
plated
plated
uniform-



Holes
layer
layer
layer
plating
Structure
Surface


No.
condition
(C)
(O)
(S)
property
compactness
roughness







Application
No hole
<20 ppm
<10 ppm
<10 ppm
No
compact
Smooth


embodiment 1




orifice







bulge


Application
No hole
<20 ppm
<10 ppm
<10 ppm
No
compact
Smooth


embodiment 2




orifice







bulge


Application
No hole
<20 ppm
<10 ppm
<10 ppm
No
compact
Smooth


embodiment 3




orifice







bulge


Application
No hole
<20 ppm
<10 ppm
<10 ppm
No
compact
Smooth


embodiment 4




orifice







bulge


Application
No hole
<20 ppm
<10 ppm
<10 ppm
No
compact
Smooth


embodiment 5




orifice







bulge


Application
No hole
<20 ppm
<10 ppm
<10 ppm
No
compact
Smooth


embodiment 6




orifice







bulge


Application
Small
<20 ppm
<10 ppm
<10 ppm
Slight
Slightly
Slightly


embodiment 7
holes



orifice
loose
rough







bulge


Application
No hole
<20 ppm
<10 ppm
<10 ppm
No
compact
Smooth


embodiment 8




orifice







bulge


Application
No hole
<20 ppm
<10 ppm
<10 ppm
No
compact
Smooth


embodiment 9




orifice







bulge


Application
No hole
<20 ppm
<10 ppm
<10 ppm
No
compact
Smooth


embodiment




orifice


10




bulge


Application
Small
<20 ppm
<10 ppm
<10 ppm
Slight
Slightly
Slightly


embodiment
holes or



orifice
loose
rough


11
defects



bulge


Application
No hole
<20 ppm
<10 ppm
<10 ppm
No
compact
Smooth


embodiment




orifice


12




bulge


Application
No hole
<20 ppm
<10 ppm
<10 ppm
No orifice
compact
Smooth


embodiment




orifice


13




bulge


Application
No hole
<20 ppm
<10 ppm
<10 ppm
No
compact
Smooth


embodiment




orifice


14




bulge


Application
No hole
<20 ppm
<10 ppm
<10 ppm
No
compact
Smooth


embodiment




orifice


15




bulge


Application
No hole
<20 ppm
<10 ppm
<10 ppm
No
compact
Smooth


embodiment




orifice


16




bulge


Application
No hole
<20 ppm
<10 ppm
<10 ppm
No
compact
Smooth


embodiment




orifice


17




bulge


Application
No hole
<20 ppm
<10 ppm
<10 ppm
No
compact
Smooth


embodiment




orifice


18




bulge


Application
No hole
<20 ppm
<10 ppm
<10 ppm
No
compact
Smooth


embodiment




orifice


19




bulge


Application
Small
<20 ppm
<10 ppm
<10 ppm
Slight
Slightly
Slightly


embodiment
holes



orifice
loose
rough


20




bulge


Application
No hole
<20 ppm
<10 ppm
<10 ppm
No
compact
Smooth


embodiment




orifice


21




bulge


Application
No hole
<20 ppm
<10 ppm
<10 ppm
No
compact
Smooth


embodiment




orifice


22




bulge


Application
No hole
<20 ppm
<10 ppm
<10 ppm
No
compact
Smooth


embodiment




orifice


23




bulge


Application
No hole
<20 ppm
<10 ppm
<10 ppm
No
compact
Smooth


embodiment




orifice


24




bulge


Application
No hole
<20 ppm
<10 ppm
<10 ppm
No
compact
Smooth


embodiment




orifice


25




bulge


Application
No hole
<20 ppm
<10 ppm
<10 ppm
No
compact
Smooth


embodiment




orifice


26




bulge


Application
No hole
<20 ppm
<10 ppm
<10 ppm
No
compact
Smooth


embodiment




orifice


27




bulge


Application
No hole
<20 ppm
<10 ppm
<10 ppm
No
compact
Smooth


embodiment




orifice


28




bulge


Application
No hole
<20 ppm
<10 ppm
<10 ppm
No
compact
Smooth


embodiment




orifice


29




bulge


Application
Small
<20 ppm
<10 ppm
<10 ppm
Slight
Slightly
Slightly


embodiment
holes



orifice
loose
rough


30




bulge


Application
No hole
<20 ppm
<10 ppm
<10 ppm
No
compact
Smooth


embodiment




orifice


31




bulge


Application
No hole
<20 ppm
<10 ppm
<10 ppm
No
compact
Smooth


embodiment




orifice


32




bulge


Application
No hole
<20 ppm
<10 ppm
<10 ppm
No
compact
Smooth


embodiment




orifice


33




bulge


Application
No hole
<20 ppm
<10 ppm
<10 ppm
No
compact
Smooth


embodiment




orifice


34




bulge


Application
No hole
<20 ppm
<10 ppm
<10 ppm
No
compact
Smooth


embodiment




orifice


35




bulge


Comparative
Large
>20 ppm
>10 ppm
>10 ppm
Obvious
Loose
Rough


application
holes



orifice


embodiment 1




bulge


Comparative
Only a
>20 ppm
>10 ppm
>10 ppm
more
Loose
Rough


application
few



orifice


embodiment 2
holes



bulge


Comparative
Only a
>20 ppm
>10 ppm
>10 ppm
more
Loose
Slightly


application
few



orifice

rough


embodiment 3
holes



bulge


Comparative
Large
>20 ppm
>10 ppm
>10 ppm
Obvious
Loose
Rough


application
holes



orifice


embodiment 4




bulge


Comparative
Only a
>20 ppm
>10 ppm
>10 ppm
more
Loose
Rough


application
few



orifice


embodiment 5
holes



bulge


Comparative
Only a
>20 ppm
>10 ppm
>10 ppm
more
Loose
Slightly


application
few



orifice

rough


embodiment 6
holes



bulge









The above embodiments show that using the metal electroplating compositions of the present invention for electroplating can achieve the effects of free of hole or defect, low plating layer impurity, good uniform-plating property, compact structure, and low surface roughness. Meanwhile, the usage of the polymer leveling agent containing imidazole structure disclosed in Patent application No. CN105705491A has the disadvantages of free of holes and defects, high plating layer impurity, poor uniform-plating property, loose structure, high surface roughness.


Although the specific embodiments of the present invention are described above, a person skilled in the art should understand that these are only examples and can be changed or modified in a variety of ways without deviating from the principle and essence of the present invention. Accordingly, the scope of the present invention is defined by the appended claims.

Claims
  • 1. A metal electroplating composition, wherein a raw material of the metal electroplating composition comprises a leveling agent represented by formula I,
  • 2. The metal electroplating composition according to claim 1, wherein in the leveling agent represented by formula I, at least one of the following is present: R1 is methyl, propyl, benzyl, propargyl or allyl;R2 is benzyl, methyl, hydroxyethyl, thiophene-substituted methyl, furan-substituted ethyl, monohalogenated benzyl, or hydroxy-substituted benzyl;R3 is pyridyl, thienyl, indolyl, naphthyl, hydroxy-substituted naphthyl, phenyl, hydroxy-substituted phenyl, monohalogenated phenyl, methylphenyl, nitrophenyl, methoxyphenyl or dimethylamino phenyl;R4 is H or methyl; andthe halogen is F, Cl or Br.
  • 3. The metal electroplating composition according to claim 1, wherein the leveling agent represented by formula I is selected from the group consisting of Compound 1: R1=Propyl-; R2=Bn-; R3=Ph-; R4═H—;Compound 2: R1=Propyl-; R2=Bn-; R3=2-Cl-Ph-; R4═H—;Compound 3: R1=Propyl-; R2=Bn-; R3=3-Cl-Ph-; R4═H—;Compound 4: R1=Propyl-; R2=Bn-; R3=4-Cl-Ph-; R4═H—;Compound 5: R1=Propyl-; R2=Bn-; R3=4-Br-Ph-; R4═H—;Compound 6: R1=Propyl-; R2=Bn-; R3=2-F-Ph-; R4═H—;Compound 7: R1=Propyl-; R2=Bn-; R3=4-Me-Ph-; R4═H—;Compound 8: R1=Propyl-; R2=Bn-; R3=3,4,5-(MeO)3-Ph-; R4═H—;Compound 9: R1=Propyl-; R2=Bn-; R3=4-NO2-Ph-; R4═H—;Compound 10: R1=Propyl-; R2=Bn-; R3=4-(N,N—(CH3)2)-Ph-; R4═H—;Compound 11: R1=Propyl-; R2=Bn-;
  • 4. The metal electroplating composition according to claim 1, wherein the metal electroplating liquid includes at least one selected from the group consisting of: the copper salt being selected from the group consisting of copper sulfate, copper halide, copper acetate, copper nitrate, copper fluoroborate, copper alkylsulfonate, copper arylsulfonate, copper sulfamate and copper gluconate;a molar concentration of copper ions in the metal electroplating liquid being in a range of 0.15-2.85 mol/L;the acidic electrolyte being selected from the group consisting of sulfuric acid, phosphoric acid, acetic acid, fluoroboric acid, sulfamic acid, alkylsulfonic acid, arylsulfonic acid and hydrochloric acid;in each liter of the metal electroplating composition, a mass of the acidic electrolyte being 1-300 g;the halide ion source being a chloride ion source;a concentration of the halide ion of the halide ion source being 0-100 ppm; anda concentration of the leveling agent being 1-10 ppm.
  • 5. The metal electroplating composition according to claim 4, wherein, the metal electroplating liquid includes at least one selected from the group consisting of: the copper alkylsulfonate being selected from the group consisting of copper methanesulfonate, copper ethanesulfonate and copper propanesulfonate;the copper arylsulfonate being selected from the group consisting of copper phenyl sultanate, copper phenolsulfonate and copper p-toluenesulfonate;the alkylsulfonic acid being selected from the group consisting of methanesulfonic acid, ethanesulfonic acid, propanesulfonic acid and trifluoromethanesulfonic acid;the arylsulfonic acid being selected from the group consisting of phenylsulfonic acid, phenolsulfonic acid and toluenesulfonic acid;the chloride ion source being selected from the group consisting of copper chloride, tin chloride and hydrochloric acid;the concentration of the halide ions of the halide ion source being 50-100 ppm; andthe concentration of the leveling agent being 5-10 ppm.
  • 6. The metal electroplating composition according to claim 1, wherein the raw material of the metal electroplating composition comprises at least one of an accelerator and an inhibitor.
  • 7. The metal electroplating composition according to claim 6, wherein when the raw material of the metal electroplating composite comprises the accelerator, a concentration of the accelerator is 0.1 to 1000 ppm and the accelerator is selected from the group consisting of N,N-dimethyl-disulfenylcarbamic acid-(3-sulfopropyl) ester, 3-mercapto-propylsulfonic acid-(3-sulfopropyl) ester, 3-mercapto-propylsulfonate sodium salt; disulfenyl carbonate-o-ethyl ester-s-ester and 3-mercapto-1-propane sultanate potassium salt, disulfopropyl disulfide, 3-(benzothiazolyl-s-sulfenyl)propyl sultanate sodium salt, pyridinium propyl sulfonyl betaine, 1-sodium-3-mercapto propane-1-sulfonate, N,N-dimethyl-disulfenyl carbamic acid-(3-sulfoethyl) ester, 3-mercapto-ethyl propyl sulfonic acid-(3-sulfoethyl) ester, 3-mercapto-ethyl sultanate sodium salt, carbonic acid-disulfenyl-o-ethyl ester-s-ester and 3-mercapto-1-ethanesulfonate potassium salt, disulfoethyl disulfide, 3-(benzothiazolyl-s-sulfenyl)ethyl sultanate sodium salt, pyridinium ethyl sulfonyl betaine and 1-sodium-3-mercaptoethane-1-sulfonate; and wherein when the raw material of the metal electroplating composition comprises the inhibitor, a concentration of the inhibitor is 1 to 10000 ppm and the inhibitor is selected from the group consisting of polypropylene glycol copolymer, polyethylene glycol copolymer, ethylene oxide-propylene oxide copolymer, and butanol-ethylene oxide-propylene oxide copolymer.
  • 8. The metal electroplating composition according to claim 7, wherein when the raw material of the metal electroplating composition comprises the inhibitor, the inhibitor is a butanol-ethylene oxide-propylene oxide copolymer having a weight-average molecular weight of 100-100,000; and the concentration of the inhibitor is 5-10000 ppm.
  • 9. The metal electroplating composition of claim 6, wherein the raw material of the metal electroplating composition consists of the metal electroplating liquid, the leveling agent, the accelerator and the inhibitor.
  • 10. A method for electroplating a substrate, which comprises: (1) contacting the substrate to be electroplated with the metal electroplating composition according to claim 1;(2) applying an electric current for electroplating.
  • 11. The method according to claim 10, wherein the method includes at least one selected from the group consisting of: in step (1), the substrate is a wafer or chip of a printed circuit board or an integrated circuit;in step (2), the current density of the electroplating is 0.1-10 ASD;in step (2), the electroplating time is 53-110 s;in step (2), the electroplating temperature is 10-65° C.
  • 12. The method according to claim 10, wherein step (2) is carried out in three steps: in a first step, the current density is 0.1-0.5 ASD; the electroplating time is 3-20 s;and the electroplating temperature is 10-65° C.;in a second step, the current density is 0.5-1.5 ASD; the electroplating time is 20-30 s; and the electroplating temperature is 10-65° C.;in a third step, the current density is 1-10 ASD; the electroplating time is 30-60 s;and the electroplating temperature is 10-65° C.
  • 13. The method according to claim 11, wherein, the method includes at least one selected from the group consisting of: in step (2), the current density of the electroplating is 0.3-5 ASD;in step (2), the electroplating time is 80-110 s;in step (2), the electroplating temperature is 10-35° C.
  • 14. The method according to claim 13, wherein, the method includes at least one selected from the group consisting of: in step (2), the current density of the electroplating is 0.5-1.5 ASD;in step (2), the electroplating temperature is 20-30° C.
Priority Claims (1)
Number Date Country Kind
201710613256.3 Jul 2017 CN national
PCT Information
Filing Document Filing Date Country Kind
PCT/CN2017/116441 12/15/2017 WO 00
Publishing Document Publishing Date Country Kind
WO2019/019532 1/31/2019 WO A
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Number Date Country
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106432247 Feb 2017 CN
107217283 Sep 2017 CN
107313082 Nov 2017 CN
2366686 Sep 2011 EP
2007135380 Nov 2007 WO
2009034386 Mar 2009 WO
2015066848 May 2015 WO
Non-Patent Literature Citations (1)
Entry
International Search Report and Written Opinion of PCT/CN2017/116441 dated Apr. 19, 2018.
Related Publications (1)
Number Date Country
20190367522 A1 Dec 2019 US