EP4073187A1 - Low oxide trench dishing shallow trench isolation chemical mechanical planarization polishing - Google Patents

Low oxide trench dishing shallow trench isolation chemical mechanical planarization polishing

Info

Publication number
EP4073187A1
EP4073187A1 EP20898454.2A EP20898454A EP4073187A1 EP 4073187 A1 EP4073187 A1 EP 4073187A1 EP 20898454 A EP20898454 A EP 20898454A EP 4073187 A1 EP4073187 A1 EP 4073187A1
Authority
EP
European Patent Office
Prior art keywords
ceria
group
methyl
coated
chemical mechanical
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
EP20898454.2A
Other languages
German (de)
French (fr)
Other versions
EP4073187A4 (en
Inventor
Xiaobo Shi
Joseph D. Rose
Hongjun Zhou
Krishna P. Murella
Mark Leonard O'neill
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Versum Materials US LLC
Original Assignee
Versum Materials US LLC
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Priority claimed from US16/711,818 external-priority patent/US11254839B2/en
Application filed by Versum Materials US LLC filed Critical Versum Materials US LLC
Publication of EP4073187A1 publication Critical patent/EP4073187A1/en
Publication of EP4073187A4 publication Critical patent/EP4073187A4/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09GPOLISHING COMPOSITIONS; SKI WAXES
    • C09G1/00Polishing compositions
    • C09G1/02Polishing compositions containing abrasives or grinding agents
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09KMATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K3/00Materials not provided for elsewhere
    • C09K3/14Anti-slip materials; Abrasives
    • C09K3/1436Composite particles, e.g. coated particles
    • C09K3/1445Composite particles, e.g. coated particles the coating consisting exclusively of metals
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01LSEMICONDUCTOR DEVICES NOT COVERED BY CLASS H10
    • H01L21/00Processes or apparatus adapted for the manufacture or treatment of semiconductor or solid state devices or of parts thereof
    • H01L21/02Manufacture or treatment of semiconductor devices or of parts thereof
    • H01L21/04Manufacture or treatment of semiconductor devices or of parts thereof the devices having potential barriers, e.g. a PN junction, depletion layer or carrier concentration layer
    • H01L21/18Manufacture or treatment of semiconductor devices or of parts thereof the devices having potential barriers, e.g. a PN junction, depletion layer or carrier concentration layer the devices having semiconductor bodies comprising elements of Group IV of the Periodic Table or AIIIBV compounds with or without impurities, e.g. doping materials
    • H01L21/30Treatment of semiconductor bodies using processes or apparatus not provided for in groups H01L21/20 - H01L21/26
    • H01L21/31Treatment of semiconductor bodies using processes or apparatus not provided for in groups H01L21/20 - H01L21/26 to form insulating layers thereon, e.g. for masking or by using photolithographic techniques; After treatment of these layers; Selection of materials for these layers
    • H01L21/3105After-treatment
    • H01L21/31051Planarisation of the insulating layers
    • H01L21/31053Planarisation of the insulating layers involving a dielectric removal step
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09KMATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K3/00Materials not provided for elsewhere
    • C09K3/14Anti-slip materials; Abrasives
    • C09K3/1454Abrasive powders, suspensions and pastes for polishing
    • C09K3/1463Aqueous liquid suspensions
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01LSEMICONDUCTOR DEVICES NOT COVERED BY CLASS H10
    • H01L21/00Processes or apparatus adapted for the manufacture or treatment of semiconductor or solid state devices or of parts thereof
    • H01L21/70Manufacture or treatment of devices consisting of a plurality of solid state components formed in or on a common substrate or of parts thereof; Manufacture of integrated circuit devices or of parts thereof
    • H01L21/71Manufacture of specific parts of devices defined in group H01L21/70
    • H01L21/76Making of isolation regions between components
    • H01L21/762Dielectric regions, e.g. EPIC dielectric isolation, LOCOS; Trench refilling techniques, SOI technology, use of channel stoppers
    • H01L21/76224Dielectric regions, e.g. EPIC dielectric isolation, LOCOS; Trench refilling techniques, SOI technology, use of channel stoppers using trench refilling with dielectric materials

Definitions

  • This invention relates to Shallow Trench Isolation (STI) chemical Mechanical Planarization (CMP) polishing compositions.
  • STI Shallow Trench Isolation
  • CMP chemical Mechanical Planarization
  • the STI chemical Mechanical Planarization (CMP) polishing compositions use ceria-coated composite particles, such as ceria-coated silica particles as abrasives and poly (methacrylic acid) (PMAA), its derivatives, or its salts with molecular weight ranged from 1 ,000 to 1 ,000,000; or combinations thereof as chemical additive for achieving low oxide trenching dishing for Shallow Trench Isolation (STI) process.
  • CMP chemical Mechanical Planarization
  • polishing especially surfaces for chemical-mechanical polishing for recovering a selected material and/or planarizing the structure.
  • a SiN layer is deposited under a S1O2 layer to serve as a polish stop.
  • the role of such polish stop is particularly important in Shallow Trench Isolation (STI) structures.
  • Selectivity is characteristically expressed as the ratio of the oxide polish rate to the nitride polish rate.
  • An example is an increased polishing selectivity rate of silicon dioxide (S1O2) as compared to silicon nitride (SiN).
  • US Patent 5,876,490 discloses the polishing compositions containing abrasive particles and exhibiting normal stress effects.
  • the slurry further contains non polishing particles resulting in reduced polishing rate at recesses, while the abrasive particles maintain high polish rates at elevations. This leads to improved planarization.
  • the slurry comprises cerium oxide particles and polymeric electrolyte, and can be used for Shallow Trench Isolation (STI) polishing applications.
  • STI Shallow Trench Isolation
  • US Patent 6,964,923 teaches the polishing compositions containing cerium oxide particles and polymeric electrolyte for Shallow Trench Isolation (STI) polishing applications.
  • Polymeric electrolyte being used includes the salts of polyacrylic acid, similar as those in US Patent 5,876,490.
  • Ceria, alumina, silica & zirconia are used as abrasives.
  • Molecular weight for such listed polyelectrolyte is from 300 to 20,000, but in overall, ⁇ 100,000.
  • US Patent 6,616,514 discloses a chemical mechanical polishing slurry for use in removing a first substance from a surface of an article in preference to silicon nitride by chemical mechanical polishing.
  • the chemical mechanical polishing slurry according to the invention includes an abrasive, an aqueous medium, and an organic polyol that does not dissociate protons, said organic polyol including a compound having at least three hydroxyl groups that are not dissociable in the aqueous medium, or a polymer formed from at least one monomer having at least three hydroxyl groups that are not dissociable in the aqueous medium.
  • the present invention discloses Chemical mechanical polishing (CMP) compositions that provide reduced oxide trench dishing and thus improved over polishing window stability for Shallow Trench Isolation (STI) CMP applications at wide pH range including acidic, neutral and alkaline pH conditions.
  • CMP Chemical mechanical polishing
  • the CMP compositions also provide good oxide film removal rates, suppressed SiN film removal rates and tunable higher S1O2: SiN selectivity.
  • CMP compositions for Shallow Trench Isolation (STI) CMP applications have a unique combination of using ceria-coated inorganic oxide abrasive particles and an oxide trench dishing reducing additives including poly(methacrylic acids) (PMAA), its derivatives, its salts with molecular weight ranging from 1000 to 1,000,000; or combinations thereof .
  • PMAA poly(methacrylic acids)
  • a STI CMP polishing composition comprises: ceria-coated inorganic oxide particles; oxide trenching dishing reducer selected from the group consisting of organic polymer acid, its ester derivatives, its salts, and combinations thereof; water based solvent; and optionally biocide; and pH adjuster; wherein the composition has a pH of 2 to 12, 3 to 10, 3.5 to 9, or 4 to 7; and molecular weight of oxide trenching dishing reducer is from 1,000 to 1,000,000, preferably 1,200 to 100,000, more preferably 1,500 to 15,000.
  • the ceria-coated inorganic oxide particles include, but are not limited to, ceria-coated colloidal silica, ceria-coated high purity colloidal silica, ceria-coated alumina, ceria-coated titania, ceria-coated zirconia, or any other ceria-coated inorganic oxide particles.
  • the preferred ceria-coated inorganic oxide particles are ceria-coated colloidal silica.
  • the water-soluble based solvent includes but is not limited to deionized (Dl) water, distilled water, and alcoholic organic water-based solvents.
  • organic polymer acid, its ester derivatives, or its salts used as oxide trench dishing reducers have a general molecular structure as shown below:
  • R1, R2, and R4 each can be selected independently from the group consisting of hydrogen, alkyl groups; R4 can also be metal ions or ammonium ions, such as Na+, K+ or NH4+; and R3 is selected from alkyl groups.
  • the alkyl groups are C m H 2m+i m is from 1 to 10, 1 to 6, 1 to 4, or 1 to 2; such as methyl, ethyl groups.
  • n is chosen to give the molecular weights of the oxide trenching dishing reducer in the range from 1,000 to 1,000,000; preferably 1,200 to 100,000; and more preferably 1,500 to 15,000.
  • R1, R2, and R4 are hydrogen atoms and R3 is methyl group
  • the molecular structure of poly(methacrylic acid) is shown below:
  • R1 and R2 are hydrogen atoms, R3 is methyl group, and R4 is ammonium ion or a metal such as sodium ion, or potassium ion; then the molecular structure of poly (methacrylic acid) salts is shown below:
  • the poly (methacrylic acid) salts include but are not limited to poly (methacrylic acid) ammonium salts, poly (methacrylic acid) sodium salts, poly (methacrylic acid) potassium salts, or combinations thereof.
  • the preferred polyacrylic acid salt is poly (methacrylic acid) ammonium salt.
  • R1 and R2 are hydrogen atoms
  • R3 and R4 are methyl group
  • PMMA poly (methyl methacrylate)
  • CMP chemical mechanical polishing
  • STI Shallow Trench Isolation
  • the polished silicon oxide films can be Chemical vapor deposition (CVD), Plasma Enhance CVD (PECVD), High Density Deposition CVD(HDP), or spin on oxide films.
  • the substrate disclosed above can further comprises a silicon nitride surface.
  • the removal selectivity of S1O2: SiN is greater than 10, preferably greater than 15.
  • This invention relates to the Chemical mechanical polishing (CMP) compositions for Shallow Trench Isolation (STI) CMP applications generally using the ceria-coated inorganic oxide particles as abrasives and poly(methacrylic acids)(PMAA), its derivatives, its salts, and combinations thereof as the suitable chemical additives which provide the benefits of achieving high oxide film removal rates, low SiN film removal rates, high and tunable Oxide: SiN selectivity, and more importantly, significantly reducing oxide trench dishing and improving over polishing window stability.
  • CMP Chemical mechanical polishing
  • STI Shallow Trench Isolation
  • a STI CMP polishing composition comprises: ceria-coated inorganic oxide particles; oxide trenching dishing reducer selected from organic polymer acid, its ester derivatives, its salts, and combinations thereof; water based solvent; and optionally biocide; and pH adjuster; wherein the composition has a pH of 2 to 12, 3 to 10, 3.5 to 9, or 4 to 8; the molecular weight of oxide trenching dishing reducer is in the ranges of 1,000 to
  • the oxide trenching dishing reducer also includes 2-alkyl group substituted derivatives of the organic polymer acid, where 2-alkyl group includes methyl, ethyl, propyl, butyl, pentyl or hexyl group.
  • the ceria-coated inorganic oxide particles include, but are not limited to, ceria-coated colloidal silica, ceria-coated high purity colloidal silica, ceria-coated alumina, ceria-coated titania, ceria-coated zirconia, or any other ceria-coated inorganic oxide particles.
  • the preferred ceria-coated inorganic oxide particles are ceria-coated colloidal silica particles.
  • the particle sizes measured by a known method, such as Dynamic Light Scattering, of these ceria-coated inorganic oxide particles in the disclosed invention herein are ranged from 10nm to 1,000nm, the preferred mean particle sized are ranged from 20nm to 500nm, the more preferred mean particle sizes are ranged from 50nm to 250nm.
  • concentrations of these ceria-coated inorganic oxide particles range from 0.01 wt.% to 20 wt.%, the preferred concentrations range from 0.05 wt.% to 10 wt.%, the more preferred concentrations range from 0.1 wt.% to 5 wt.%.
  • the water-based solvent includes but is not limited to deionized (Dl) water, distilled water, and alcoholic organic water-based solvents.
  • the preferred water-based solvent is Dl water.
  • the STI CMP slurry may contain biocide ranging from 0.0001 wt.% to 0.05 wt.%; preferably from 0.0005 wt.% to 0.025 wt.%, and more preferably from 0.001 wt.% to 0.01 wt.%.
  • the biocide includes, but is not limited to, KathonTM, KathonTM CG/ICP II, from Dupont/Dow Chemical Co. Bioban from Dupont/Dow Chemical Co. They have active ingredients of 5-chloro-2-methyl-4-isothiazolin-3-one and 2-methyl-4-isothiazolin- 3-one.
  • the STI CMP slurry may contain a pH adjustor.
  • An acidic or basic pH adjustor can be used to adjust the STI polishing compositions to the optimized pH value.
  • the acidic pH adjustors include, but are not limited to nitric acid, hydrochloric acid, sulfuric acid, phosphoric acid, other inorganic or organic acids, and mixtures thereof.
  • pH adjustors also include the basic pH adjustors, such as sodium hydride, potassium hydroxide, ammonium hydroxide, tetraalkyl ammonium hydroxide, organic quaternary ammonium hydroxide compounds, organic amines, and other chemical reagents that can be used to adjust pH towards the more alkaline direction.
  • basic pH adjustors such as sodium hydride, potassium hydroxide, ammonium hydroxide, tetraalkyl ammonium hydroxide, organic quaternary ammonium hydroxide compounds, organic amines, and other chemical reagents that can be used to adjust pH towards the more alkaline direction.
  • the STI CMP slurry contains 0 wt.% to 1 wt.%; preferably 0.01 wt.% to 0.5 wt.%; more preferably 0.1 wt.% to 0.25 wt.% of a pH adjustor.
  • the organic polymer acid, its ester derivatives, its 2-alkyl group substituted derivatives (2-alkyl group is selected from methyl, ethyl, propyl, butyl, pentyl or hexyl group), or its salts used as oxide trench dishing reducers have a general molecular structure as shown below:
  • R1, R2, and R4 can be selected independently from the group consisting of hydrogen, alkyl groups; R4 can also be metal ions or ammonium ions, such as Na+, K+ or NH4+; and R3 is selected from alkyl groups.
  • the alkyl groups are C m H 2m+i m is from 1 to 10, 1 to 6, 1 to 4, or 1 to 2; such as methyl, ethyl groups.
  • n is chosen to give the molecular weights in the range from 1 ,000 to 1,000,000; preferably 1,200 to 100,000; and more preferably 1,500 to 15,000.
  • R1, R2, and R4 are hydrogen atoms and R3 is methyl group
  • molecular structure (a) of Poly(methacrylic acid) is shown below:
  • the poly(methacrylic acid) salts include but are not limited to poly (methacrylic acid) ammonium salts, poly(methacrylic acid) sodium salts, poly (methacrylic acid) potassium salts, or combinations thereof.
  • the preferred poly(methacrylic acid) salt is poly(methacrylic acid) ammonium salt.
  • R1 and R2 are hydrogen atoms
  • R3 and R4 are methyl group
  • PMMA poly (methyl methacrylate)
  • R1 and R2 are hydrogen atoms, R3 is methyl group, and R4 is ethyl group, the molecular structure of poly (ethyl methacrylate) (PEMA) is shown below:
  • R1 and R4 are hydrogen atoms
  • R2 and R3 are methyl group
  • the molecular structure of 2-methyl-poly (methacrylic acid) is shown below:
  • the STI CMP slurry contains 0.001 wt.% to 2.0% wt.%, preferably 0.005 wt.% to 0.75 wt.%, and preferable 0.01 wt.% to 0.5 wt.% of the oxide trenching dishing reducer.
  • CMP chemical mechanical polishing
  • CMP chemical mechanical polishing
  • STI Shallow Trench Isolation
  • PECVD Enhance CVD
  • HDP High Density Deposition CVD
  • spin on oxide films PECVD
  • PECVD Enhance CVD
  • HDP High Density Deposition CVD
  • the substrate disclosed above can further comprises a silicon nitride surface.
  • the removal selectivity of S1O2: SiN is greater than 10, preferably greater than 20, and more preferably greater than 30.
  • CMP chemical mechanical polishing
  • the polished oxide films can be CVD oxide, PECVD oxide, High density oxide, or Spin on oxide films.
  • Ceria-coated Silica used as abrasive having a particle size of approximately 100 nanometers (nm); such ceria-coated silica particles can have a particle size of ranged from approximately 20 nanometers (nm) to 500 nanometers (nm).
  • Ceria-coated Silica particles (with varied sizes) were supplied by JGC Inc. in Japan.
  • TEOS tetraethyl orthosilicate
  • Polishing Pad Polishing pad, IC1010 and other pads were used during
  • a or A angstrom(s) - a unit of length
  • BP back pressure, in psi units
  • CS carrier speed
  • PS platen rotational speed of polishing tool, in rpm (revolution(s) per minute)
  • SF slurry flow, ml/min
  • Wt. % weight percentage (of a listed component)
  • TEOS SiN Selectivity: (removal rate of TEOS)/ (removal rate of SiN)
  • HDP high density plasma deposited TEOS
  • TEOS or HDP Removal Rates Measured TEOS or HDP removal rate at a given down pressure.
  • the down pressure of the CMP tool was 2.0, 3.0 or 4.0 psi in the examples listed below.
  • SiN Removal Rates Measured SiN removal rate at a given down pressure.
  • the down pressure of the CMP tool was 3.0 psi in the examples listed.
  • the CMP tool that was used is a 200mm Mirra, or 300mm Reflexion manufactured by Applied Materials, 3050 Boweres Avenue, Santa Clara, California, 95054.
  • An IC1000 pad supplied by DOW, Inc, 451 Bellevue Rd., Newark, DE 19713 was used on platen 1 for blanket and pattern wafer studies.
  • the IC1010 pad or other pad was broken in by conditioning the pad for 18 mins. At 7 lbs. down force on the conditioner. To qualify the tool settings and the pad break-in two tungsten monitors and two TEOS monitors were polished with Versum® STI2305 slurry, supplied by Versum Materials Inc. at baseline conditions.
  • Polishing experiments were conducted using PECVD or LECVD or HD TEOS wafers. These blanket wafers were purchased from Silicon Valley Microelectronics, 2985 Kifer Rd., Santa Clara, CA 95051. Polishing Experiments
  • TEOS SiN Selectivity: (removal rate of TEOS)/ (removal rate of SiN) obtained from the STI CMP polishing compositions were tunable.
  • a STI polishing composition comprising 0.2 wt.% cerium-coated silica, a biocide ranging from 0.0001 wt.% to 0.05 wt.%, and deionized water was prepared as base or reference composition.
  • the STI CMP polishing compositions comprised additional chemical additives, such poly (methacrylic acid) (PMAA) with structure (a) with different molecular weights and/or polyacrylic acid ammonium salt (PAAAS) with around 3000 molecular weights.
  • PMAA poly (methacrylic acid)
  • PAAAS polyacrylic acid ammonium salt
  • pH of the compositions was adjusted by using nitric acid or ammonium hydroxide.
  • Example 1 [0097] In Example 1, the polishing compositions were prepared as shown in Table 1. pH was around 5.35 for the compositions.
  • Example 2 the polishing compositions were prepared as shown in Table 2.
  • the CMP polishing compositions have pH values at 5.35.
  • polishing compositions were prepared as shown in Table 3.
  • 0.2 wt.% ceria-coated silica was used as abrasives in reference and all three tested samples. pH was around 5.35 for each of these compositions.
  • the oxide trench dishing rates were reduced significantly when PMAA was used at 0.05 wt.% , 0.1 wt.% or 0.15 wt.% on 100pm and 200pm oxide trench features while comparing the dishing rates on these two oxide trench features obtained with the polishing composition only using 0.2 wt.% ceria- coated silica abrasive based polishing composition.
  • Example 4 [00116] In example 4, the effects of pH conditions on film removal rates, oxide trenching loss rates, and oxide trench dishing rates were tested for compositions using 0.1 wt. % PMAA having 5,000 MW and 0.2 wt.% ceria-coated silica as abrasives.
  • Example 5 [0003] In example 5, the tests were performed with PMAA having different MW: 5,000,
  • compositions comprised 0.1 wt. % PMAA and 0.2 wt.% ceria- coated silica as abrasives. pH of the compositions was at 5.35.
  • compositions comprised 0.2 wt.% ceria-coated silica as abrasives. pH of the compositions at 5.35 was used as reference sample.
  • the polishing compositions using 0.05 wt.% or 0.1 wt.% PMAA as chemical additive salt significantly reduced the P200mm trench RR/Blanket HDP RR ratios than such ratios obtained from reference sample without using chemical additive or the polishing compositions using 0.01 wt.% or 0.1 wt.% PAAAS as chemical additives.
  • Different sized oxide trench RR/Blanket oxide film RR ratio is a key parameter to judge on whether the oxide polishing composition can afford lower oxide dishing while used for oxide polishing CMP applications. In general, the smaller of such ratios are, the lower of oxide trench dishing are.
  • polishing composition used PMAA as the chemical additive provided significant oxide trench dishing reduction than the polishing composition used PAAAS as chemical additive at same pH and same abrasive concentrations.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Condensed Matter Physics & Semiconductors (AREA)
  • Physics & Mathematics (AREA)
  • General Physics & Mathematics (AREA)
  • Manufacturing & Machinery (AREA)
  • Computer Hardware Design (AREA)
  • Microelectronics & Electronic Packaging (AREA)
  • Power Engineering (AREA)
  • Materials Engineering (AREA)
  • Composite Materials (AREA)
  • Mechanical Treatment Of Semiconductor (AREA)
  • Finish Polishing, Edge Sharpening, And Grinding By Specific Grinding Devices (AREA)

Abstract

The present invention discloses STI CMP polishing compositions, methods and systems that significantly reduce oxide trench dishing and improve over-polishing window stability in addition to provide high and tunable silicon oxide removal rates, low silicon nitride removal rates, and tunable high selectivity of SiO2: SiN through the use of an unique combination of ceria inorganic oxide particles, such as ceria coated silica particles as abrasives, and an oxide trench dishing reducing additive of poly(methacrylic acids), its derivatives, its salts, or combinations thereof.

Description

TITLE OF THE INVENTION:
LOW OXIDE TRENCH DISHING SHALLOWTRENCH ISOLATION CHEMICAL MECHANICAL PLANARIZATION POLISHING
CROSS REFERENCE TO RELATED PATENT APPLICATIONS [0001] This application claims the benefit of priority to U.S. patent application Serial Number 16/711,818 filed on 12 December 2019, which is entirely incorporated herein by reference.
BACKGROUND OF THE INVENTION
[0002] This invention relates to Shallow Trench Isolation (STI) chemical Mechanical Planarization (CMP) polishing compositions.
[0003] More specifically, the STI chemical Mechanical Planarization (CMP) polishing compositions use ceria-coated composite particles, such as ceria-coated silica particles as abrasives and poly (methacrylic acid) (PMAA), its derivatives, or its salts with molecular weight ranged from 1 ,000 to 1 ,000,000; or combinations thereof as chemical additive for achieving low oxide trenching dishing for Shallow Trench Isolation (STI) process.
[0004] In the fabrication of microelectronics devices, an important step involved is polishing, especially surfaces for chemical-mechanical polishing for recovering a selected material and/or planarizing the structure.
[0005] For example, a SiN layer is deposited under a S1O2 layer to serve as a polish stop. The role of such polish stop is particularly important in Shallow Trench Isolation (STI) structures. Selectivity is characteristically expressed as the ratio of the oxide polish rate to the nitride polish rate. An example is an increased polishing selectivity rate of silicon dioxide (S1O2) as compared to silicon nitride (SiN).
[0006] In the global planarization of patterned STI structures, reducing oxide trench dishing is a key factor to be considered. The lower trench oxide loss will prevent electrical current leaking between adjacent transistors. Non-uniform trench oxide loss across die (within Die) will affect transistor performance and device fabrication yields. Severe trench oxide loss (high oxide trench dishing) will cause poor isolation of transistor resulting in device failure. Therefore, it is important to reduce trench oxide loss by reducing oxide trench dishing in STI CMP polishing compositions.
[0007] US Patent 5,876,490 discloses the polishing compositions containing abrasive particles and exhibiting normal stress effects. The slurry further contains non polishing particles resulting in reduced polishing rate at recesses, while the abrasive particles maintain high polish rates at elevations. This leads to improved planarization. More specifically, the slurry comprises cerium oxide particles and polymeric electrolyte, and can be used for Shallow Trench Isolation (STI) polishing applications.
[0008] US Patent 6,964,923 teaches the polishing compositions containing cerium oxide particles and polymeric electrolyte for Shallow Trench Isolation (STI) polishing applications. Polymeric electrolyte being used includes the salts of polyacrylic acid, similar as those in US Patent 5,876,490. Ceria, alumina, silica & zirconia are used as abrasives. Molecular weight for such listed polyelectrolyte is from 300 to 20,000, but in overall, <100,000.
[0009] US Patent 6,616,514 discloses a chemical mechanical polishing slurry for use in removing a first substance from a surface of an article in preference to silicon nitride by chemical mechanical polishing. The chemical mechanical polishing slurry according to the invention includes an abrasive, an aqueous medium, and an organic polyol that does not dissociate protons, said organic polyol including a compound having at least three hydroxyl groups that are not dissociable in the aqueous medium, or a polymer formed from at least one monomer having at least three hydroxyl groups that are not dissociable in the aqueous medium.
[0010] However, those prior disclosed Shallow Trench Isolation (STI) polishing compositions did not address the importance of oxide trench dishing reducing.
[0011] It should be readily apparent from the foregoing that there remains a need within the art for compositions, methods and systems of chemical mechanical polishing that can afford the reduced oxide trench dishing and improved over polishing window stability in a STI chemical and mechanical polishing (CMP) process, in addition to high removal rate of silicon dioxide as well as high selectivity for silicon dioxide to silicon nitride. BRIEF SUMMARY OF THE INVENTION
[0012] The present invention discloses Chemical mechanical polishing (CMP) compositions that provide reduced oxide trench dishing and thus improved over polishing window stability for Shallow Trench Isolation (STI) CMP applications at wide pH range including acidic, neutral and alkaline pH conditions.
[0013] The CMP compositions also provide good oxide film removal rates, suppressed SiN film removal rates and tunable higher S1O2: SiN selectivity.
[0014] The disclosed chemical mechanical polishing (CMP) compositions for Shallow Trench Isolation (STI) CMP applications have a unique combination of using ceria-coated inorganic oxide abrasive particles and an oxide trench dishing reducing additives including poly(methacrylic acids) (PMAA), its derivatives, its salts with molecular weight ranging from 1000 to 1,000,000; or combinations thereof .
[0015] In one aspect, there is provided a STI CMP polishing composition comprises: ceria-coated inorganic oxide particles; oxide trenching dishing reducer selected from the group consisting of organic polymer acid, its ester derivatives, its salts, and combinations thereof; water based solvent; and optionally biocide; and pH adjuster; wherein the composition has a pH of 2 to 12, 3 to 10, 3.5 to 9, or 4 to 7; and molecular weight of oxide trenching dishing reducer is from 1,000 to 1,000,000, preferably 1,200 to 100,000, more preferably 1,500 to 15,000.
[0016] The ceria-coated inorganic oxide particles include, but are not limited to, ceria-coated colloidal silica, ceria-coated high purity colloidal silica, ceria-coated alumina, ceria-coated titania, ceria-coated zirconia, or any other ceria-coated inorganic oxide particles. The preferred ceria-coated inorganic oxide particles are ceria-coated colloidal silica. [0017] The water-soluble based solvent includes but is not limited to deionized (Dl) water, distilled water, and alcoholic organic water-based solvents.
[0018] The organic polymer acid, its ester derivatives, or its salts used as oxide trench dishing reducers have a general molecular structure as shown below:
[0019] Where R1, R2, and R4 each can be selected independently from the group consisting of hydrogen, alkyl groups; R4 can also be metal ions or ammonium ions, such as Na+, K+ or NH4+; and R3 is selected from alkyl groups. Where the alkyl groups are CmH2m+i m is from 1 to 10, 1 to 6, 1 to 4, or 1 to 2; such as methyl, ethyl groups.
[0020] n is chosen to give the molecular weights of the oxide trenching dishing reducer in the range from 1,000 to 1,000,000; preferably 1,200 to 100,000; and more preferably 1,500 to 15,000.
[0021] When R1, R2, and R4 are hydrogen atoms and R3 is methyl group, the molecular structure of poly(methacrylic acid) is shown below: [0022] When R1 and R2 are hydrogen atoms, R3 is methyl group, and R4 is ammonium ion or a metal such as sodium ion, or potassium ion; then the molecular structure of poly (methacrylic acid) salts is shown below:
[0023] The poly (methacrylic acid) salts include but are not limited to poly (methacrylic acid) ammonium salts, poly (methacrylic acid) sodium salts, poly (methacrylic acid) potassium salts, or combinations thereof. The preferred polyacrylic acid salt is poly (methacrylic acid) ammonium salt.
[0024] When R1 and R2 are hydrogen atoms, R3 and R4 are methyl group, the molecular structure of poly (methyl methacrylate) (PMMA) is shown below:
[0025] When R1 and R2 are hydrogen atoms, R3 is methyl group, and R4 is ethyl group, the molecular structure of poly (ethyl methacrylate) (PEMA) is shown below: [0026] When R1 and R4 are hydrogen atoms, R2 and R3 are methyl group, the molecular structure of 2-methyl-poly (methacrylic acid) is shown below:
[0027] In another aspect, there is provided a method of chemical mechanical polishing (CMP) a substrate having at least one surface comprising silicon dioxide using the chemical mechanical polishing (CMP) composition described above in Shallow Trench Isolation (STI) process. [0028] In another aspect, there is provided a system of chemical mechanical polishing (CMP) a substrate having at least one surface comprising silicon dioxide using the chemical mechanical polishing (CMP) composition described above in Shallow Trench Isolation (STI) process. [0029] The polished silicon oxide films can be Chemical vapor deposition (CVD), Plasma Enhance CVD (PECVD), High Density Deposition CVD(HDP), or spin on oxide films.
[0030] The substrate disclosed above can further comprises a silicon nitride surface. The removal selectivity of S1O2: SiN is greater than 10, preferably greater than 15.
DETAILED DESCRIPTION OF THE INVENTION
[0031] This invention relates to the Chemical mechanical polishing (CMP) compositions for Shallow Trench Isolation (STI) CMP applications generally using the ceria-coated inorganic oxide particles as abrasives and poly(methacrylic acids)(PMAA), its derivatives, its salts, and combinations thereof as the suitable chemical additives which provide the benefits of achieving high oxide film removal rates, low SiN film removal rates, high and tunable Oxide: SiN selectivity, and more importantly, significantly reducing oxide trench dishing and improving over polishing window stability.
[0032] In the global planarization of patterned STI structures, reducing oxide trench dishing is a key factor to be considered. The lower trench oxide loss will prevent electrical current leaking between adjacent transistors. Non-uniform trench oxide loss across die (within Die) will affect transistor performance and device fabrication yields. Severe trench oxide loss (high oxide trench dishing) will cause poor isolation of transistor resulting in device failure. Therefore, it is important to reduce trench oxide loss by reducing oxide trench dishing in STI CMP polishing compositions.
[0033] In one aspect, there is provided a STI CMP polishing composition comprises: ceria-coated inorganic oxide particles; oxide trenching dishing reducer selected from organic polymer acid, its ester derivatives, its salts, and combinations thereof; water based solvent; and optionally biocide; and pH adjuster; wherein the composition has a pH of 2 to 12, 3 to 10, 3.5 to 9, or 4 to 8; the molecular weight of oxide trenching dishing reducer is in the ranges of 1,000 to
1,000,000, preferably 1,200 to 100,000, more preferably 1,500 to 15,000.
[0034] The oxide trenching dishing reducer also includes 2-alkyl group substituted derivatives of the organic polymer acid, where 2-alkyl group includes methyl, ethyl, propyl, butyl, pentyl or hexyl group.
[0035] The ceria-coated inorganic oxide particles include, but are not limited to, ceria-coated colloidal silica, ceria-coated high purity colloidal silica, ceria-coated alumina, ceria-coated titania, ceria-coated zirconia, or any other ceria-coated inorganic oxide particles.
[0036] The preferred ceria-coated inorganic oxide particles are ceria-coated colloidal silica particles.
[0037] The particle sizes measured by a known method, such as Dynamic Light Scattering, of these ceria-coated inorganic oxide particles in the disclosed invention herein are ranged from 10nm to 1,000nm, the preferred mean particle sized are ranged from 20nm to 500nm, the more preferred mean particle sizes are ranged from 50nm to 250nm.
[0038] The concentrations of these ceria-coated inorganic oxide particles range from 0.01 wt.% to 20 wt.%, the preferred concentrations range from 0.05 wt.% to 10 wt.%, the more preferred concentrations range from 0.1 wt.% to 5 wt.%.
[0039] The water-based solvent includes but is not limited to deionized (Dl) water, distilled water, and alcoholic organic water-based solvents.
[0040] The preferred water-based solvent is Dl water.
[0041] The STI CMP slurry may contain biocide ranging from 0.0001 wt.% to 0.05 wt.%; preferably from 0.0005 wt.% to 0.025 wt.%, and more preferably from 0.001 wt.% to 0.01 wt.%.
[0042] The biocide includes, but is not limited to, Kathon™, Kathon™ CG/ICP II, from Dupont/Dow Chemical Co. Bioban from Dupont/Dow Chemical Co. They have active ingredients of 5-chloro-2-methyl-4-isothiazolin-3-one and 2-methyl-4-isothiazolin- 3-one. [0043] The STI CMP slurry may contain a pH adjustor.
[0044] An acidic or basic pH adjustor can be used to adjust the STI polishing compositions to the optimized pH value.
[0045] The acidic pH adjustors include, but are not limited to nitric acid, hydrochloric acid, sulfuric acid, phosphoric acid, other inorganic or organic acids, and mixtures thereof.
[0046] pH adjustors also include the basic pH adjustors, such as sodium hydride, potassium hydroxide, ammonium hydroxide, tetraalkyl ammonium hydroxide, organic quaternary ammonium hydroxide compounds, organic amines, and other chemical reagents that can be used to adjust pH towards the more alkaline direction.
[0047] The STI CMP slurry contains 0 wt.% to 1 wt.%; preferably 0.01 wt.% to 0.5 wt.%; more preferably 0.1 wt.% to 0.25 wt.% of a pH adjustor.
[0048] The organic polymer acid, its ester derivatives, its 2-alkyl group substituted derivatives (2-alkyl group is selected from methyl, ethyl, propyl, butyl, pentyl or hexyl group), or its salts used as oxide trench dishing reducers have a general molecular structure as shown below:
[0049] Where R1, R2, and R4 can be selected independently from the group consisting of hydrogen, alkyl groups; R4 can also be metal ions or ammonium ions, such as Na+, K+ or NH4+; and R3 is selected from alkyl groups. Where the alkyl groups are CmH2m+i m is from 1 to 10, 1 to 6, 1 to 4, or 1 to 2; such as methyl, ethyl groups.
[0050] n is chosen to give the molecular weights in the range from 1 ,000 to 1,000,000; preferably 1,200 to 100,000; and more preferably 1,500 to 15,000. [0051] When R1, R2, and R4 are hydrogen atoms and R3 is methyl group, molecular structure (a) of Poly(methacrylic acid) is shown below:
[0052] When R1 and R2 are hydrogen atoms, R3 is methyl group, and R4 is a metal ion, then the molecular structure (b) of poly(methacrylic acid) salt is shown below:
[0053] The poly(methacrylic acid) salts include but are not limited to poly (methacrylic acid) ammonium salts, poly(methacrylic acid) sodium salts, poly (methacrylic acid) potassium salts, or combinations thereof. The preferred poly(methacrylic acid) salt is poly(methacrylic acid) ammonium salt.
[0054] When R1 and R2 are hydrogen atoms, R3 and R4 are methyl group, the molecular structure of poly (methyl methacrylate) (PMMA) is shown below:
[0055] When R1 and R2 are hydrogen atoms, R3 is methyl group, and R4 is ethyl group, the molecular structure of poly (ethyl methacrylate) (PEMA) is shown below:
[0056] When R1 and R4 are hydrogen atoms, R2 and R3 are methyl group, the molecular structure of 2-methyl-poly (methacrylic acid) is shown below:
[0057] The STI CMP slurry contains 0.001 wt.% to 2.0% wt.%, preferably 0.005 wt.% to 0.75 wt.%, and preferable 0.01 wt.% to 0.5 wt.% of the oxide trenching dishing reducer.
[0058] In another aspect, there is provided a method of chemical mechanical polishing (CMP) a substrate having at least one surface comprising silicon dioxide using the chemical mechanical polishing (CMP) composition described above in Shallow Trench Isolation (STI) process.
[0059] In another aspect, there is provided a system of chemical mechanical polishing (CMP) a substrate having at least one surface comprising silicon dioxide using the chemical mechanical polishing (CMP) composition described above in Shallow Trench Isolation (STI) process. [0060] The polished oxide films can be Chemical vapor deposition (CVD), Plasma
Enhance CVD (PECVD), High Density Deposition CVD(HDP), or spin on oxide films.
[0061] The substrate disclosed above can further comprises a silicon nitride surface. The removal selectivity of S1O2: SiN is greater than 10, preferably greater than 20, and more preferably greater than 30. [0062] In another aspect, there is provided a method of chemical mechanical polishing (CMP) a substrate having at least one surface comprising silicon dioxide using the chemical mechanical polishing (CMP) composition described above in Shallow Trench Isolation (STI) process. The polished oxide films can be CVD oxide, PECVD oxide, High density oxide, or Spin on oxide films. [0063] The following non-limiting examples are presented to further illustrate the present invention.
CMP Methodology [0064] In the examples presented below, CMP experiments were run using the procedures and experimental conditions given below.
GLOSSARY
COMPONENTS
[0065] Ceria-coated Silica: used as abrasive having a particle size of approximately 100 nanometers (nm); such ceria-coated silica particles can have a particle size of ranged from approximately 20 nanometers (nm) to 500 nanometers (nm).
[0066] Ceria-coated Silica particles (with varied sizes) were supplied by JGC Inc. in Japan.
[0067] Chemical additives, poly(methacrylic acid) or salts were supplied by Sigma- Aldrich, St. Louis, MO [0068] Chemical additives, polyacrylic acid ammonium salts(PAAAS) were supplied by
Kao Chemicals Inc. in Japan.
[0069] TEOS: tetraethyl orthosilicate
[0070] Polishing Pad: Polishing pad, IC1010 and other pads were used during
CMP, supplied by DOW, Inc.
PARAMETERS
General
[0071] A or A: angstrom(s) - a unit of length [0072] BP: back pressure, in psi units
[0073] CMP: chemical mechanical planarization = chemical mechanical polishing [0074] CS: carrier speed
[0075] DF: Down force: pressure applied during CMP, units psi [0076] min: minute(s)
[0077] ml: milliliter(s)
[0078] mV: millivolt(s)
[0079] psi: pounds per square inch
[0080] PS: platen rotational speed of polishing tool, in rpm (revolution(s) per minute) [0081] SF: slurry flow, ml/min [0082] Wt. %: weight percentage (of a listed component)
[0083] TEOS: SiN Selectivity: (removal rate of TEOS)/ (removal rate of SiN)
[0084] HDP: high density plasma deposited TEOS
[0085] TEOS or HDP Removal Rates: Measured TEOS or HDP removal rate at a given down pressure. The down pressure of the CMP tool was 2.0, 3.0 or 4.0 psi in the examples listed below.
[0086] SiN Removal Rates: Measured SiN removal rate at a given down pressure. The down pressure of the CMP tool was 3.0 psi in the examples listed.
Metrology
[0087] Films were measured with a ResMap CDE, model 168, manufactured by Creative Design Engineering, Inc, 20565 Alves Dr., Cupertino, CA, 95014. The ResMap tool is a four-point probe sheet resistance tool. Forty-nine-point diameter scan at 5mm edge exclusion for film was taken.
CMP Tool
[0088] The CMP tool that was used is a 200mm Mirra, or 300mm Reflexion manufactured by Applied Materials, 3050 Boweres Avenue, Santa Clara, California, 95054. An IC1000 pad supplied by DOW, Inc, 451 Bellevue Rd., Newark, DE 19713 was used on platen 1 for blanket and pattern wafer studies.
[0089] The IC1010 pad or other pad was broken in by conditioning the pad for 18 mins. At 7 lbs. down force on the conditioner. To qualify the tool settings and the pad break-in two tungsten monitors and two TEOS monitors were polished with Versum® STI2305 slurry, supplied by Versum Materials Inc. at baseline conditions.
Wafers
[0090] Polishing experiments were conducted using PECVD or LECVD or HD TEOS wafers. These blanket wafers were purchased from Silicon Valley Microelectronics, 2985 Kifer Rd., Santa Clara, CA 95051. Polishing Experiments
[0091] In blanket wafer studies, oxide blanket wafers, and SiN blanket wafers were polished at baseline conditions. The tool baseline conditions were: table speed; 87 rpm, head speed: 93 rpm, membrane pressure; 3.0 psi, slurry flow; 200 ml/min. [0092] The slurry was used in polishing experiments on patterned wafers (MIT860) which were supplied by SWK Associates, Inc. 2920 Scott Blvd. Santa Clara, CA 95054). These wafers were measured on the Veeco VX300 profiler/AFM instrument. The 2 or 3 different sized pitch structures were used for oxide dishing measurement. The wafer was measured at center, middle, and edge die positions. [0093] TEOS: SiN Selectivity: (removal rate of TEOS)/ (removal rate of SiN) obtained from the STI CMP polishing compositions were tunable.
Working Examples
[0094] In the following working examples, a STI polishing composition comprising 0.2 wt.% cerium-coated silica, a biocide ranging from 0.0001 wt.% to 0.05 wt.%, and deionized water was prepared as base or reference composition.
[0095] The STI CMP polishing compositions comprised additional chemical additives, such poly (methacrylic acid) (PMAA) with structure (a) with different molecular weights and/or polyacrylic acid ammonium salt (PAAAS) with around 3000 molecular weights.
[0096] pH of the compositions was adjusted by using nitric acid or ammonium hydroxide.
Example 1 [0097] In Example 1, the polishing compositions were prepared as shown in Table 1. pH was around 5.35 for the compositions.
[0098] The chemical additives poly(methacrylic acid) (PMAA) or its deionized form (deionized PMAA) having MW around 5,000 were used at 0.10 wt.%, respectively as shown in Table 1. [0099] The removal rates (RR at A/min) for different films were tested. The results were shown in Table 1.
[00100] The effects of PMAA having 5,000 molecular weights or its deionized form on the film removal rates and selectivity were observed. Table 1. Effects of Additives on Film RRs & Selectivity
[00101] As shown in Table 1, the addition of the chemical additives of poly (methacrylic acid)(PMAA), or its deionized form, reduced the removal rates for all tested films. Similar TEOS: SiN film polishing selectivity were obtained.
Example 2
[00102] In Example 2, the polishing compositions were prepared as shown in Table 2. The CMP polishing compositions have pH values at 5.35.
[00103] The chemical additives poly(methacrylic acid) having molecular weights around 5,000 was used at 0.10 wt.%.
[00104] The oxide trenching 100pm and 200pm dishing vs over polishing amounts were tested and the results were shown in Table 2.
Table 2. Effects of PMAA on Oxide Trench Dishing vs OP Amt. [00105] As the results shown in Table 2, the addition of 0.1 wt.% PMAA with 5,000 MW into the reference STI CMP polishing composition having 0.2 wt. % ceria-coated silica abrasives significantly reduced oxide trench dishing, the oxide trench dishing reduction was by > 100% for both different sized oxide trench features. [00106] Dishing was significantly reduced with the use of MW 5,000 PMAA as oxide trench dishing reducer vs different over polishing thickness of oxide films.
Example 3
[00107] In example 3, the polishing compositions were prepared as shown in Table 3. In the listed polishing compositions, 0.2 wt.% ceria-coated silica was used as abrasives in reference and all three tested samples. pH was around 5.35 for each of these compositions.
[00108] The deionized PMAA with molecular weight 5,000 was used at 0.05 wt.%, 0.1 wt.% , and 0.15 wt.% respectively. [00109] Removal rates from those polishing compositions were tested and shown in
Table 3.
Table 3. Film RRs from Polishing Compositions having PMAA at Different%
[00110] As the results shown in Table 3, all three types of film removal rates were reduced when different concentrations of PMAA was used as chemical additive in the polishing compositions, but the concentration changes of PMAA with MW 5,000 within the tested range had no significant effects on TEOS, HDP, SiN film removal rates, and using PMAA as chemical additive in the polishing compositions increased TEOS: SiN selectivity slightly. [00111] The effects of PMAA concentrations on various sized oxide trench loss rates were listed in Table 4.
Table 4. Effects of PMAA% on Oxide Trench Loss Rates [00112] As showed in Table 4, the oxide trench loss rates were significantly reduced when PMAA was used at different wt.% concentrations on 100pm and 200pm oxide trench features while comparing with the polishing composition only using 0.2 wt.% ceria-coated silica reference sample.
[00113] The results shown in Table 4 also shown that when PMAA concentrations were used at 0.1 wt.% or at 0.15 wt.%, significant oxide trench loss rates were obtained while comparing the polishing composition used 0.05 wt.% PMAA as chemical additive.
[00114] The effects of PMAA concentrations on various sized oxide trench dishing rates were listed in Table 5.
Table 5. Effects of PMAA% on Oxide Trench Dishing Rates
[00115] As the results shown in Table 5, the oxide trench dishing rates were reduced significantly when PMAA was used at 0.05 wt.% , 0.1 wt.% or 0.15 wt.% on 100pm and 200pm oxide trench features while comparing the dishing rates on these two oxide trench features obtained with the polishing composition only using 0.2 wt.% ceria- coated silica abrasive based polishing composition.
Example 4 [00116] In example 4, the effects of pH conditions on film removal rates, oxide trenching loss rates, and oxide trench dishing rates were tested for compositions using 0.1 wt. % PMAA having 5,000 MW and 0.2 wt.% ceria-coated silica as abrasives.
[00117] The results of the effects of pH on Film were listed in Table 6.
Table 6. Effects of pH on Film RR
[00118] As the results shown in Table 6, the removal rates for TEOS film were increased as pH increased from 5.35 to 6 or from 5.35 to 8. The HDP film removal rate was increased as pH increased from 5.35 to 6, then, slightly reduced as pH increased from 5.35 to 8. The TEOS: SiN selectivity were increased as pH increased from 5.35 to 6, and 8 respectively.
[00119] The effects of pH conditions of the polishing compositions on various sized oxide trench loss rates were listed in Table 7.
Table 7. Effects of pH Conditions on Oxide Trench Loss Rates [00120] The effects of pH conditions on various sized oxide trench dishing rates were listed in Table 8.
Table 8. Effects of pH Conditions on Oxide Trench Dishing Rates
[0001] As showed in Table 7, in overall, the composition at pH 5.35 showed the lowest oxide trench loss rates across all tested oxide trench features.
[0002] As showed in Table 8, in overall, the composition at pH 5.35 showed the lowest oxide trench dishing rates across all tested oxide trench features.
Example 5 [0003] In example 5, the tests were performed with PMAA having different MW: 5,000,
15,000 and 100,000. The compositions comprised 0.1 wt. % PMAA and 0.2 wt.% ceria- coated silica as abrasives. pH of the compositions was at 5.35.
[0004] The results from different molecular weights of PMAA or poly (methacrylic acid) ammonium salts (PMAAAM) on the film removal rates and TEOS: SiN selectivity were listed in Table 9.
Table 9. Effects of Different MW of PMAA or Its Salt on Film RR & TEOS: SiN Selectivity [0005] As the results showed in Table 9, using PMAA or its salt as oxide trench dishing reducing agent suppressed TEOS, HDP and SiN removal rates. The selectivity of TEOS: SiN was kept high and increased for PMAA MW < 100,000 from MW 5K to 15K.
[0006] Different molecular weights of PMAA or poly (methacrylic acid) ammonium salts (PMAAAM) as chemical additives to reduce oxide trench dishing were tested. The results were listed in Table 10.
Table 10. Effects of Different MW of PMAA or Its Salt on Oxide Trench Dishing Rates
[0007] As the results showed in Table 10, using PMAA or its salt as oxide trench dishing reducing agents provided the reduced oxide trench dishing performances on 100pm and 200pm oxide trench features.
Example 6
[0008] In example 6, two chemical additives, polyacrylic acid ammonium salt, (PAAAS) vs PMAA were compared on their effects on oxide polishing composition performances.
[0009] The compositions comprised 0.2 wt.% ceria-coated silica as abrasives. pH of the compositions at 5.35 was used as reference sample.
[0010] The effects of PAAAS or PMAA as chemical additives in the polishing compositions on HDP film and SiN film removal rates were studied and the results were listed in Table 11.
[0011] As the results shown in Table 11 , at same pH and same abrasive concentration conditions, 0.1 wt.% PAAAS significantly suppressed HDP oxide film removal rate while comparing the HDP film removal rate obtained using 0.1 wt.% PMAA as chemical additive in the polishing composition. The composition of ceria-coated silica and 0.1 wt.% PAAAS salt used in the composition would not offer an acceptable removal rate of HDP.
Table 11. Effects of PAA Salt vs PMAA on Film Removal Rates
[0012] The effects of PAAAS or PMAA as chemical additives in the polishing compositions employed ceria-coated silica particles as abrasives on P200pm trench rates and P200pm Trench RR/Blanket HDP film RR ratios were studied, and the results were listed in Table 12.
Table 12. Effects of PAA Salt vs PMAA on P200 Trench Rates & P200
Trench RR/Blanket RR Ratios
[0013] As the results shown in Table 12, at same pH and same abrasive concentration conditions, the polishing compositions using 0.05 wt.% or 0.1 wt.% PMAA as chemical additive salt significantly reduced the P200mm trench RR/Blanket HDP RR ratios than such ratios obtained from reference sample without using chemical additive or the polishing compositions using 0.01 wt.% or 0.1 wt.% PAAAS as chemical additives.
[0014] Different sized oxide trench RR/Blanket oxide film RR ratio is a key parameter to judge on whether the oxide polishing composition can afford lower oxide dishing while used for oxide polishing CMP applications. In general, the smaller of such ratios are, the lower of oxide trench dishing are.
[0015] The effects of PAAAS or PMAA as chemical additives in the polishing compositions employed ceria-coated silica particles as abrasives on P200pm trench dishing vs the over polished removal amounts were studied, and the results were listed in Table 13. Table 13. Effects of PAA Salt vs PMAA on P200 Trench Dishing vs OP Amt.
[0016] As the results shown in Table 13, at same pH and same abrasive concentration conditions, the HDP film removal rates were tuned to the similar removal rates so that the trench dishing data vs the over polished removal amounts could be compared more relatively.
[0017] The P200pm dishing vs two different over polishing removal amounts demonstrated significant lower oxide trench dishing vs over polishing amounts when using PMAA as chemical additives than that trenching dishing vs over polishing amounts when using PAAAS as chemical additive in the polishing composition.
[0018] The example 6 had shown that the polishing composition used PMAA as the chemical additive provided significant oxide trench dishing reduction than the polishing composition used PAAAS as chemical additive at same pH and same abrasive concentrations.
[0019] The embodiments of this invention listed above, including the working example, are exemplary of numerous embodiments that may be made of this invention. It is contemplated that numerous other configurations of the process may be used, and the materials used in the process may be elected from numerous materials other than those specifically disclosed.

Claims

1. A chemical mechanical polishing composition comprising: ceria-coated inorganic oxide particles; oxide trenching dishing reducer selected from the group consisting of organic polymer acid, its ester derivative, its salt, and combinations thereof; water based solvent; and optionally biocide; and pH adjuster; wherein the composition has a pH of 3 to 10; and the oxide trench dishing reducer has a general molecular structure as shown below: wherein R1and R2 each independently is selected from the group consisting of hydrogen and an alkyl group CmH2m+i and m is from 1 to 4; R3 is an alkyl group CmH2m+i and m is from 1 to 4; R4 is selected from the group consisting of hydrogen, an alkyl group CmH2m+i and m is from 1 to 4, metal ion, and ammonium ion; and n is chosen to give a molecular weight from 1,000 to 1,000,000.
2. The chemical mechanical polishing composition of Claim 1, wherein the ceria-coated inorganic oxide particles are selected from the group consisting of ceria-coated colloidal silica, ceria-coated high purity colloidal silica, ceria-coated alumina, ceria-coated titania, ceria-coated zirconia particles and combinations thereof; the oxide trench dishing reducer has a general molecular structure selected from the group consisting of:
(a) poly(methacrylic acid) when R1, R2, and R4 are hydrogen, and R3 is methyl;
(b) salt of poly(methacrylic acid) when R1 and R2 are hydrogen, R3 is methyl, and R4 is a metal ion or ammonium M+;
(c)poly (methyl methacrylate) (PMMA) when R1 and R2 are hydrogen, R3 and R4 are methyl;
(d)poly (ethyl methacrylate) (PEMA) when R1 and R2 are hydrogen, R3 is methyl, and R4 is ethyl;
(e)2-methyl-poly (methacrylic acid) when R1 and R4 are hydrogen, R2 and R3 are methyl; the water based solvent is selected from the group consisting of deionized (Dl) water, distilled water, and alcoholic organic water based solvents.
3. The chemical mechanical polishing composition of Claim 1, wherein the chemical mechanical polishing composition further comprises at least one of the biocide having an active ingredient selected from the group consisting of 5- chloro-2-methyl-4-isothiazolin-3-one, 2-methyl-4-isothiazolin-3-one, and combinations thereof; and the pH adjustor selected from the group consisting of nitric acid, hydrochloric acid, sulfuric acid, phosphoric acid, and combinations thereof for acidic pH conditions; or is selected from the group consisting of sodium hydride, potassium hydroxide, ammonium hydroxide, tetraalkyl ammonium hydroxide, organic quaternary ammonium hydroxide compounds, organic amines, and combinations thereof for alkaline pH conditions.
4. The chemical mechanical polishing composition of Claim 1, wherein the ceria-coated inorganic oxide particles are consisting of ceria-coated colloidal silica, ceria-coated high purity colloidal silica, and combinations thereof; the oxide trench dishing reducer has a molecular weight of 1,200 to 100,000 and is selected from the group consisting of poly (methacrylic acid), salt of poly(methacrylic acid), and combinations thereof; the water based solvent is deionized (Dl) water; and the chemical mechanical polishing composition has a pH of 3.5 to 9.
5. The chemical mechanical polishing composition of claim 1 , wherein the chemical mechanical polishing composition comprises the ceria-coated inorganic oxide particles are selected from the group consisting of ceria-coated colloidal silica, ceria-coated high purity colloidal silica, and combinations thereof; the oxide trench dishing reducer has a molecular weight of 1,500 to 15000 and is selected from the group consisting of poly (methacrylic acid), salt of poly(methacrylic acid), and combinations thereof; deionized (Dl) water; the biocide having an active ingredient selected from the group consisting of 5- chloro-2-methyl-4-isothiazolin-3-one, 2-methyl-4-isothiazolin-3-one, and combinations thereof; nitric acid or ammonium hydroxide; and the chemical mechanical polishing composition has a pH of 4 to 7.
6. The chemical mechanical polishing composition of claim 1 comprises ceria-coated colloidal silica; poly (methacrylic acids) having a molecular weight of 1,200 to 100,000; deionized (Dl) water; and the chemical mechanical polishing composition has a pH of 3.5 to 9.
7. The chemical mechanical polishing composition of claim 1 , wherein the chemical mechanical polishing composition comprises ceria-coated colloidal silica; poly (methacrylic acids) having a molecular weight of 1,200 to 100,000; deionized (Dl) water; the biocide having an active ingredient selected from the group consisting of 5- chloro-2-methyl-4-isothiazolin-3-one, 2-methyl-4-isothiazolin-3-one, and combinations thereof; nitric acid or ammonium hydroxide; and the chemical mechanical polishing composition has a pH of 4 to 7.
8. A method of chemical mechanical polishing (CMP) a semiconductor substrate having at least one surface comprising a silicon oxide film, comprising providing the semiconductor substrate; providing a polishing pad; providing the chemical mechanical polishing (CMP) composition comprising ceria-coated inorganic oxide particles; oxide trenching dishing reducer selected from the group consisting of organic polymer acid, its ester derivative, its salt, and combinations thereof; water based solvent; and optionally biocide; and pH adjuster; wherein the composition has a pH of 3 to 9; and the oxide trench dishing reducer has a general molecular structure as shown below: wherein R1and R2 each independently is selected from the group consisting of hydrogen and an alkyl group CmH2m+i and m is from 1 to 4; R3 is an alkyl group CmH2m+i and m is from 1 to 4; R4 is selected from the group consisting of hydrogen, an alkyl group CmH2m+i and m is from 1 to 4, metal ion, and ammonium ion; and n is chosen to give a molecular weight in from 1,000 to 1,000,000; contacting the at least one surface of the semiconductor substrate with the polishing pad and the chemical mechanical polishing composition; and polishing the at least one surface comprising the silicon oxide film; wherein the silicon oxide film is selected from the group consisting of Chemical vapor deposition (CVD), Plasma Enhance CVD (PECVD), High Density Deposition CVD(HDP), or spin on silicon oxide film.
9. The method of claim 8; wherein the ceria-coated inorganic oxide particles are selected from the group consisting of ceria-coated colloidal silica, ceria-coated high purity colloidal silica, ceria-coated alumina, ceria-coated titania, ceria-coated zirconia particles and combinations thereof; the oxide trench dishing reducer has a general molecular structure selected from the group consisting of:
(a) poly(methacrylic acid) when R1, R2, and R4 are hydrogen, and R3 is methyl;
(b) salt of poly(methacrylic acid) when R1 and R2 are hydrogen, R3 is methyl, and R4 is a metal ion or ammonium M+;
(c)poly (methyl methacrylate) (PMMA) when R1 and R2 are hydrogen, R3 and R4 are methyl;
(d)poly (ethyl methacrylate) (PEMA) when R1 and R2 are hydrogen, R3 is methyl, and R4 is ethyl;
(e)2-methyl-poly (methacrylic acid) when R1 and R4 are hydrogen, R2 and R3 are methyl; and combinations thereof; and the water based solvent is selected from the group consisting of deionized (Dl) water, distilled water, and alcoholic organic water based solvents.
10. The method of claim 8; wherein the chemical mechanical polishing composition further comprises at least one of the biocide having an active ingredient selected from the group consisting of 5- chloro-2-methyl-4-isothiazolin-3-one, 2-methyl-4-isothiazolin-3-one, and combinations thereof; and the pH adjustor selected from the group consisting of nitric acid, hydrochloric acid, sulfuric acid, phosphoric acid, and combinations thereof for acidic pH conditions; or is selected from the group consisting of sodium hydride, potassium hydroxide, ammonium hydroxide, tetraalkyl ammonium hydroxide, organic quaternary ammonium hydroxide compounds, organic amines, and combinations thereof for alkaline pH conditions
11. The method of claim 8; wherein the chemical mechanical polishing composition comprises the ceria-coated inorganic oxide particles selected from the group consisting of ceria- coated colloidal silica, ceria-coated high purity colloidal silica, and combinations thereof; the oxide trench dishing reducer having a molecular weight of 1,200 to 100,000 and is selected from the group consisting of poly (methacrylic acid), salt of poly(methacrylic acid), and combinations thereof; deionized (Dl) water.
12. The method of claim 8; wherein the chemical mechanical polishing composition comprises the ceria-coated inorganic oxide particles are selected from the group consisting of ceria-coated colloidal silica, ceria-coated high purity colloidal silica, and combinations thereof; the oxide trench dishing reducer has a molecular weight of 1,500 to 15000 and is selected from the group consisting of poly (methacrylic acid), salt of poly(methacrylic acid), and combinations thereof; deionized (Dl) water; the biocide having an active ingredient selected from the group consisting of 5- chloro-2-methyl-4-isothiazolin-3-one, 2-methyl-4-isothiazolin-3-one, and combinations thereof; nitric acid or ammonium hydroxide; and the chemical mechanical polishing composition has a pH of 4 to 7.
13. The method of claim 8; wherein the chemical mechanical polishing composition comprises ceria-coated colloidal silica; poly (methacrylic acids) having a molecular weight of 1,200 to 100,000; and deionized (Dl) water.
14. The method of claim 8; wherein the chemical mechanical polishing composition comprises ceria-coated colloidal silica; poly (methacrylic acids) having a molecular weight of 1,500 to 15000; deionized (Dl) water; the biocide having an active ingredient selected from the group consisting of 5- chloro-2-methyl-4-isothiazolin-3-one, 2-methyl-4-isothiazolin-3-one, and combinations thereof; nitric acid or ammonium hydroxide; and the chemical mechanical polishing composition has a pH of 4 to 7.
15. The method of claim 8; wherein the silicon oxide film is S1O2 film; the semiconductor substrate further having at least one surface comprises a silicon nitride film; and removal selectivity of silicon oxide: silicon nitride is greater than 10.
16. A system of chemical mechanical polishing (CMP) a semiconductor substrate having at least one surface comprising a silicon oxide film, comprising a. the semiconductor substrate; b. the chemical mechanical polishing (CMP) composition comprising ceria-coated inorganic oxide particles; oxide trenching dishing reducer selected from the group consisting of organic polymer acid, its ester derivative, its salt, and combinations thereof; water based solvent; and optionally biocide; and pH adjuster; wherein the composition has a pH of 3.5 to 9; and the oxide trench dishing reducer has a general molecular structure as shown below: wherein R1and R2 each independently is selected from the group consisting of hydrogen and an alkyl group CmH2m+i and m is from 1 to 4; R3 is an alkyl group CmH2m+i and m is from 1 to 4; R4 is selected from the group consisting of hydrogen, an alkyl group CmH2m+i and m is from 1 to 4, metal ion, and ammonium ion; and n is chosen to give a molecular weight from 1,000 to 1,000,000; c. a polishing pad; wherein the silicon oxide film is selected from the group consisting of Chemical vapor deposition (CVD), Plasma Enhance CVD (PECVD), High Density Deposition CVD(HDP), or spin on silicon oxide film; and the at least one surface comprising the silicon oxide film is in contact with the polishing pad and the chemical mechanical polishing composition.
17. The system of claim 16; wherein the ceria-coated inorganic oxide particles are selected from the group consisting of ceria-coated colloidal silica, ceria-coated high purity colloidal silica, ceria-coated alumina, ceria-coated titania, ceria-coated zirconia particles and combinations thereof; the oxide trench dishing reducer has a general molecular structure selected from the group consisting of:
(a)poly(methacrylic acid) when R1, R2, and R4 are hydrogen, and R3 is methyl;
(b)salt of poly(methacrylic acid) when R1 and R2 are hydrogen, R3 is methyl, and R4 is a metal ion or ammonium M+;
(c)poly (methyl methacrylate) (PMMA) when R1 and R2 are hydrogen, R3 and R4 are methyl;
(d)poly (ethyl methacrylate) (PEMA) when R1 and R2 are hydrogen, R3 is methyl, and R4 is ethyl;
(e)2-methyl-poly (methacrylic acid) when R1 and R4 are hydrogen, R2 and R3 are methyl; and combinations thereof; and the water based solvent is selected from the group consisting of deionized (Dl) water, distilled water, and alcoholic organic water based solvents.
18. The system of claim 16; wherein the chemical mechanical polishing composition further comprises at least one of the biocide having an active ingredient selected from the group consisting of 5- chloro-2-methyl-4-isothiazolin-3-one, 2-methyl-4-isothiazolin-3-one, and combinations thereof; and the pH adjustor selected from the group consisting of nitric acid, hydrochloric acid, sulfuric acid, phosphoric acid, and combinations thereof for acidic pH conditions; or is selected from the group consisting of sodium hydride, potassium hydroxide, ammonium hydroxide, tetraalkyl ammonium hydroxide, organic quaternary ammonium hydroxide compounds, organic amines, and combinations thereof for alkaline pH conditions
19. The system of claim 16; wherein the chemical mechanical polishing composition comprises the ceria-coated inorganic oxide particles selected from the group consisting of ceria- coated colloidal silica, ceria-coated high purity colloidal silica, and combinations thereof; the oxide trench dishing reducer having a molecular weight of 1,200 to 100,000 and is selected from the group consisting of poly (methacrylic acid), salt of poly(methacrylic acid), and combinations thereof; and deionized (Dl) water.
20. The system of claim 16; the chemical mechanical polishing composition comprises the ceria-coated inorganic oxide particles are selected from the group consisting of ceria-coated colloidal silica, ceria-coated high purity colloidal silica, and combinations thereof; the oxide trench dishing reducer has a molecular weight of 1,500 to 15000 and is selected from the group consisting of poly (methacrylic acid), salt of poly(methacrylic acid), and combinations thereof; deionized (Dl) water; the biocide having an active ingredient selected from the group consisting of 5- chloro-2-methyl-4-isothiazolin-3-one, 2-methyl-4-isothiazolin-3-one, and combinations thereof; nitric acid or ammonium hydroxide; and the chemical mechanical polishing composition has a pH of 4 to 7.
21. The system of claim 16; wherein the chemical mechanical polishing composition comprises ceria-coated colloidal silica, poly (methacrylic acids) having a molecular weight of 1,500 to 15,000; biocide having an active ingredient selected from the group consisting of 5-chloro-2-methyl-4-isothiazolin-3-one, 2-methyl-4-isothiazolin-3-one, and combinations thereof; nitric acid or ammonium hydroxide; deionized (Dl) water; and the chemical mechanical polishing composition has a pH of 4 to 7.
22. The system of claim 16; wherein the silicon oxide film is S1O2 film; the semiconductor substrate further having at least one surface comprises a silicon nitride film, wherein the at least one surface comprising a silicon nitride film is in contact with the polishing pad and the chemical mechanical polishing composition; and removal selectivity of silicon oxide: silicon nitride is greater than 10, when the at least surface comprising a silicon oxide film and the at least one surface comprising a silicon nitride film are polished with the polishing pad and the chemical mechanical polishing composition.
EP20898454.2A 2019-12-12 2020-10-21 Low oxide trench dishing shallow trench isolation chemical mechanical planarization polishing Pending EP4073187A4 (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
US16/711,818 US11254839B2 (en) 2019-12-12 2019-12-12 Low oxide trench dishing shallow trench isolation chemical mechanical planarization polishing
TW109135359A TWI763076B (en) 2019-12-12 2020-10-13 Low oxide trench dishing shallow trench isolation chemical mechanical planarization polishing composition, system and method
PCT/US2020/056673 WO2021118694A1 (en) 2019-12-12 2020-10-21 Low oxide trench dishing shallow trench isolation chemical mechanical planarization polishing

Publications (2)

Publication Number Publication Date
EP4073187A1 true EP4073187A1 (en) 2022-10-19
EP4073187A4 EP4073187A4 (en) 2023-12-13

Family

ID=76330356

Family Applications (1)

Application Number Title Priority Date Filing Date
EP20898454.2A Pending EP4073187A4 (en) 2019-12-12 2020-10-21 Low oxide trench dishing shallow trench isolation chemical mechanical planarization polishing

Country Status (5)

Country Link
EP (1) EP4073187A4 (en)
JP (1) JP2023506487A (en)
KR (1) KR20220113497A (en)
IL (1) IL293769A (en)
WO (1) WO2021118694A1 (en)

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20020173243A1 (en) * 2001-04-05 2002-11-21 Costas Wesley D. Polishing composition having organic polymer particles
JP2003313542A (en) * 2002-04-22 2003-11-06 Jsr Corp Aqueous dispersion for chemomechanical polishing use
EP1813656A3 (en) * 2006-01-30 2009-09-02 FUJIFILM Corporation Metal-polishing liquid and chemical mechanical polishing method using the same
US20100015807A1 (en) * 2006-12-22 2010-01-21 Techno Semichem Co., Ltd. Chemical Mechanical Polishing Composition for Copper Comprising Zeolite
US10109493B2 (en) * 2015-01-12 2018-10-23 Versum Materials Us, Llc Composite abrasive particles for chemical mechanical planarization composition and method of use thereof
US10032644B2 (en) * 2015-06-05 2018-07-24 Versum Materials Us, Llc Barrier chemical mechanical planarization slurries using ceria-coated silica abrasives

Also Published As

Publication number Publication date
EP4073187A4 (en) 2023-12-13
JP2023506487A (en) 2023-02-16
IL293769A (en) 2022-08-01
KR20220113497A (en) 2022-08-12
WO2021118694A1 (en) 2021-06-17

Similar Documents

Publication Publication Date Title
EP3608379B1 (en) Oxide chemical mechanical planarization (cmp) polishing compositions
US11692110B2 (en) Low oxide trench dishing chemical mechanical polishing
JP7557532B2 (en) Shallow trench isolation chemical mechanical planarization compositions having high oxide removal rates - Patents.com
CN110655869A (en) Low oxide trench recess chemical mechanical polishing
JP2023104945A (en) Method for increasing oxide/nitride selectivity and low oxide trench dishing uniformity in chemical mechanical planarization (cmp) for shallow trench isolation (sti)
CN114729229B (en) Shallow trench isolation chemical mechanical planarization composition with high oxide removal rate
EP3702424B1 (en) Shallow trench isolation chemical and mechanical polishing slurry
US11254839B2 (en) Low oxide trench dishing shallow trench isolation chemical mechanical planarization polishing
WO2021118694A1 (en) Low oxide trench dishing shallow trench isolation chemical mechanical planarization polishing
KR20200049631A (en) Suppressing SiN Removal Rates and Reducing Oxide Trench Dishing for Shallow Trench Isolation (STI) Process
WO2023059999A1 (en) Chemical mechanical planarization polishing for shallow trench isolation
TWI766267B (en) Selective chemical mechanical planarization polishing
EP4157955A1 (en) Low dishing oxide cmp polishing compositions for shallow trench isolation applications and methods of making thereof
WO2024173029A1 (en) Chemical mechanical planarization for shallow trench isolation
WO2021113285A1 (en) High oxide film removal rate shallow trench isolation (sti) chemical mechanical planarization (cmp) polishing

Legal Events

Date Code Title Description
STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: THE INTERNATIONAL PUBLICATION HAS BEEN MADE

PUAI Public reference made under article 153(3) epc to a published international application that has entered the european phase

Free format text: ORIGINAL CODE: 0009012

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: REQUEST FOR EXAMINATION WAS MADE

17P Request for examination filed

Effective date: 20220527

AK Designated contracting states

Kind code of ref document: A1

Designated state(s): AL AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO RS SE SI SK SM TR

DAV Request for validation of the european patent (deleted)
DAX Request for extension of the european patent (deleted)
P01 Opt-out of the competence of the unified patent court (upc) registered

Effective date: 20230602

A4 Supplementary search report drawn up and despatched

Effective date: 20231110

RIC1 Information provided on ipc code assigned before grant

Ipc: H01L 21/02 20060101ALI20231107BHEP

Ipc: H01L 21/3105 20060101ALI20231107BHEP

Ipc: H01L 21/762 20060101ALI20231107BHEP

Ipc: C09K 3/14 20060101ALI20231107BHEP

Ipc: C09G 1/02 20060101AFI20231107BHEP

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: EXAMINATION IS IN PROGRESS