US2006032149A1PendingUtilityA1
Polishing slurry, method of producing same, and method of polishing substrate
Est. expiryJul 28, 2024(expired)· nominal 20-yr term from priority
C01P 2004/52C01P 2004/64C01P 2006/12C09G 1/02B82Y 30/00C09K 3/1463C01P 2006/22C01F 17/235
51
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Claims
Abstract
Disclosed is a polishing slurry, particularly, a slurry for chemical mechanical polishing, which is used in a chemical mechanical polishing process for flattening a semiconductor laminate. More particularly, the present invention provides a method of producing a slurry which has high removal selectivity to a nitride layer used as a barrier film in a shallow trench isolation CMP process needed to fabricate ultra highly integrated semiconductors of 256 mega D-RAM or more (Design rule of 0.13 μm or less) and which decreases the occurrence of scratches on a flattened surface, and a method of polishing a substrate using the same.
Claims
exact text as granted — not AI-modified1 . A polishing slurry, comprising:
polishing particles in which a surface area per unit weight is changed so as to minimize agglomeration of the polishing particles and improve dispersion stability.
2 . The polishing slurry as set forth in claim 1 , wherein the surface area per unit weight of the polishing particles is 1-100 m 2 /g.
3 . The polishing slurry as set forth in claim 1 , wherein the surface area per unit weight of the polishing particles is 3-72 m 2 /g.
4 . The polishing slurry as set forth in claim 1 , wherein the surface area per unit weight of the polishing particles is 5-25 m 2 /g.
5 . The polishing slurry as set forth in claim 1 , wherein a grain size of each of the polishing particles is 15-40 nm.
6 . The polishing slurry as set forth in claim 1 , wherein a grain size of each of the polishing particles is 18-30 nm.
7 . The polishing slurry as set forth in claim 1 , wherein a grain size of each of the polishing particles is 20-25 nm.
8 . The polishing slurry as set forth in claim 1 , wherein the surface area per unit weight of the polishing particles is controlled depending on a temperature or a holding time of a calcination process.
9 . A polishing slurry, which comprises polishing particles, deionized water, and a dispersing agent, in which agglomeration of the polishing particles is minimized and a variation (dD50) of a median particle size of the polishing particles is 30 or less before and after forcible dispersion treatment, by controlling an amount of dispersing agent added or a stage at which the dispersing agent is added.
10 . The polishing slurry as set forth in claim 9 , wherein the variation (dD50) of the median particle size of the polishing particles is 10 or less.
11 . The polishing slurry as set forth in claim 9 , wherein conductivity of the polishing slurry is 300-900 μs/cm.
12 . The polishing slurry as set forth in claim 9 , wherein conductivity of the polishing slurry is 500-600 μs/cm.
13 . The polishing slurry as set forth in claim 9 , wherein the dispersing agent is made of an anionic polymer compound, and the anionic polymer compound is at least one selected from a group consisting of polymethacrylic acid, polyacrylic acid, ammonium polymethacrylate, ammonium polycarboxylate, and carboxyl-acryl polymer.
14 . The polishing slurry as set forth in claim 1 , wherein the polishing particles are ceria.
15 . A method of producing a polishing slurry, comprising:
preparing polishing particles, deionized water, and a dispersing agent; preparing a mixture of the polishing particles, the deionized water, and the dispersing agent; and milling the mixture of the polishing particles, the deionized water, and the dispersing agent.
16 . The method as set forth in claim 15 , wherein the preparation of the mixture of the polishing particles, the deionized water, and the dispersing agent comprises:
milling a mixture of the polishing particles and the deionized water; measuring a pH of the mixture of the polishing particles and the deionized water; determining an amount of dispersing agent to be added, depending on the pH; and mixing the dispersing agent with the mixture of the polishing particles and the deionized water.
17 . The method as set forth in claim 16 , wherein the amount of dispersing agent added is 2.2-3.0 wt % based on the polishing particles when the pH of the mixture of the polishing particles and the deionized water is 8.7-9.5 in the determination of the amount of dispersing agent.
18 . The method as set forth in claim 16 , wherein the amount of dispersing agent added is 1.4-2.2 wt % based on the polishing particles when the pH of the mixture of the polishing particles and the deionized water is 8.0-8.7 in the determination of the amount of dispersing agent.
19 . The method as set forth in claim 16 , wherein the amount of dispersing agent added is 0.6-1.4 wt % based on the polishing particles when the pH of the mixture of the polishing particles and the deionized water is 7.4-8.0 in the determination of the amount of dispersing agent.
20 . The method as set forth in claim 15 , wherein the preparation of the mixture comprises:
adding the dispersing agent to the deionized water and mixing them; and mixing the polishing particles with the deionized water to which the dispersing agent is added.
21 . The method as set forth in claim 15 , wherein the preparation of the mixture comprises:
adding the polishing particles to the deionized water; and mixing the dispersing agent with the deionized water to which the polishing particles are added.
22 . The method as set forth in claim 15 , wherein the preparation of the mixture comprises:
adding the dispersing agent and the polishing particles to the deionized water and mixing them.
23 . The method as set forth in claim 15 , wherein the milling of the mixture of the polishing particles, the deionized water, and the dispersing agent comprises:
additionally adding the dispersing agent at least one time.
24 . The method as set forth in claim 23 , wherein the dispersing agent is added in an amount of 0.0001-10 wt % based on the polishing particles in such a way that the dispersing agent added in deionized water is an amount of 100-50% based on a total amount of dispersing agent, and that the dispersing agent added in the course of milling the mixture is an amount of 50% or less based on the total amount of dispersing agent.
25 . The method as set forth in claim 15 , wherein the preparation of the polishing particles, the deionized water, and the dispersing agent comprises:
producing the polishing particles through a calcination process at a predetermined calcination temperature for a predetermined holding time.
26 . The method as set forth in claim 25 , wherein the calcination temperature is 500-1000° C. in the production of the polishing particles.
27 . The method as set forth in claim 25 , wherein the holding time is 10 min-10 hours at the calcination temperature in the production of the polishing particles.
28 . The method as set forth in claim 25 , wherein the production of the polishing particles comprises:
preparing a crude precursor; removing water of crystallization and adsorbed water; removing a carbonate functional group; and conducting recrystallization.
29 . The method as set forth in claim 28 , wherein the crude precursor is cerium carbonate in the production of the polishing particles.
30 . The method as set forth in claim 15 , further comprising:
adding an additive, including a weak acid or a weak base, to the mixture to control a pH of the slurry; and conducting filtering to remove large particles, after the milling of the mixture of the polishing particles, the deionized water, and the dispersing agent.
31 . A method of polishing a predetermined substrate using the polishing slurry according to claim 1.Cited by (0)
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