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WO2018100686A1 - Slurry, polishing liquid, method for producing said slurry, method for producing said polishing liquid, and method for polishing substrate - Google Patents

Slurry, polishing liquid, method for producing said slurry, method for producing said polishing liquid, and method for polishing substrate Download PDF

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Publication number
WO2018100686A1
WO2018100686A1 PCT/JP2016/085589 JP2016085589W WO2018100686A1 WO 2018100686 A1 WO2018100686 A1 WO 2018100686A1 JP 2016085589 W JP2016085589 W JP 2016085589W WO 2018100686 A1 WO2018100686 A1 WO 2018100686A1
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Prior art keywords
polishing
ceria
polishing liquid
slurry
particles
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PCT/JP2016/085589
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French (fr)
Japanese (ja)
Inventor
春仙 玉田
敬太 荒川
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Resonac Corp
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Hitachi Chemical Co Ltd
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    • H10P52/00

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  • the present invention relates to a slurry, a polishing liquid, a manufacturing method thereof, and a polishing method for a substrate.
  • CMP Chemical Mechanical Polishing
  • an inorganic insulating film such as a silicon oxide film is formed by a method such as plasma-CVD (chemical vapor deposition) or low-pressure CVD (chemical vapor deposition).
  • a chemical mechanical polishing liquid for planarizing the inorganic insulating film it has been generally studied to use a fumed silica-based polishing liquid.
  • the fumed silica-based polishing liquid is produced by adjusting the pH of a slurry containing particles obtained by grain growth by a method such as thermal decomposition of tetrachlorosilicic acid.
  • a fumed silica-based polishing liquid has a technical problem that the polishing rate is low.
  • STI is used for element isolation in the integrated circuit.
  • a CMP technique using a colloidal silica-based polishing liquid is used to remove an excess silicon oxide film formed on the substrate.
  • a stopper film having a low polishing rate is formed under the silicon oxide film.
  • a silicon nitride film or the like is used for the stopper film.
  • it is desirable that the ratio of the polishing rate of the silicon oxide film to the polishing rate of the stopper film is large.
  • the conventional colloidal silica-based polishing liquid does not have a characteristic that can withstand practical use for STI.
  • a cerium oxide-based polishing liquid containing cerium oxide particles is used as a polishing liquid for glass surfaces such as photomasks and lenses.
  • the hardness of cerium oxide particles is lower than the hardness of silica particles and alumina particles. Therefore, when a cerium oxide-based polishing liquid containing cerium oxide particles is used, the polishing surface is less likely to be damaged when polishing compared to the case where a polishing liquid containing silica particles or alumina particles is used.
  • This polishing liquid is useful for finish mirror polishing.
  • the cerium oxide-based polishing liquid has an advantage that the polishing rate is faster than silica-based polishing liquids such as fumed silica type and colloidal silica type.
  • Patent Document 1 discloses an abrasive having a volume average particle diameter of 1 nm to 95 nm and a number of particles having a diameter of 0.56 ⁇ m or more of 1 million or less per ml.
  • a polishing liquid for CMP process characterized by comprising water is disclosed.
  • Patent Document 2 discloses a cerium oxide abrasive containing a slurry in which cerium oxide particles having a particle diameter of more than 10 nm and less than 100 nm of primary particles of 90% or more are dispersed in a medium. Yes.
  • the present invention has been made in view of such circumstances, and obtains a polishing liquid that has an excellent polishing rate compared to a polishing liquid containing ceria particles having the same average primary particle diameter, and the polishing liquid. It is an object of the present invention to provide a slurry that can be used, a manufacturing method thereof, and a method of polishing a substrate using the polishing liquid.
  • the present invention is a method for producing a slurry containing ceria particles and water, comprising a crushing step of crushing colloidal ceria dispersed in water to obtain ceria particles.
  • This is a slurry production method in which grinding is performed so that the ratio of the average primary particle diameter of ceria particles to the average primary particle diameter of ceria is less than 0.8.
  • the present invention is a method for producing a slurry containing ceria particles and water, comprising a crushing step of crushing colloidal ceria dispersed in water to obtain ceria particles.
  • This is a slurry manufacturing method in which crushing is performed so that the ratio of sphericity of ceria particles to sphericity of ceria is 0.97 or less.
  • the colloidal ceria may be pulverized using a bead mill.
  • the colloidal ceria may be pulverized using a jet mill.
  • the present invention is a method for producing a polishing liquid containing ceria particles, water, and an additive, wherein the slurry obtained by the above production method is mixed with an additive to obtain a polishing liquid.
  • a method for producing a polishing liquid is a method for producing a polishing liquid.
  • the present invention is a slurry obtained by the above-described slurry manufacturing method.
  • the present invention is a polishing liquid obtained by the above polishing liquid manufacturing method.
  • the present invention is a method for polishing a substrate, comprising a polishing step of polishing a film to be polished formed on the surface of the substrate using the polishing liquid.
  • a polishing liquid having an excellent polishing rate, a slurry constituting the polishing liquid, a manufacturing method thereof, and the polishing A method for polishing a substrate using a liquid can be provided.
  • slurry means a composition containing at least ceria particles (abrasive grains) and water
  • polishing liquid means a composition containing at least ceria particles (abrasive grains), additives and water.
  • the slurry manufacturing method according to the present embodiment is a slurry manufacturing method containing ceria particles and water.
  • colloidal ceria is prepared (preparation process).
  • the colloidal ceria may be, for example, a known one obtained through a process of growing ceria crystals by a liquid phase method. Examples of the liquid phase method include (1) sol-gel method, (2) hydrothermal synthesis method, and (3) precipitation method. Colloidal ceria may be obtained by any method.
  • the average primary particle diameter of colloidal ceria is, for example, 10 to 200 nm.
  • the average primary particle diameter of colloidal ceria is calculated
  • the average secondary particle diameter of colloidal ceria is, for example, 20 to 600 nm.
  • the average secondary particle size of colloidal ceria is a value of D50 (median diameter of volume distribution, cumulative median value) measured using a laser diffraction particle size distribution analyzer (for example, product name: Master Sizer Microplus manufactured by Malvern). ).
  • a sample obtained by diluting the colloidal ceria dispersion to a concentration at which the measurement transmittance (H) with respect to the He—Ne laser is 60 to 70% is used. Measurement is performed under the conditions of laser and absorption: 0.
  • the sphericity of colloidal ceria is, for example, 60 to 100%.
  • the sphericity of colloidal ceria is calculated
  • S (%) r / R ⁇ 100 (1)
  • r indicates the maximum radius (nm) of a circle that can be drawn in one colloidal ceria grain in an image obtained by SEM observation
  • R includes one colloidal ceria grain in the image obtained by SEM observation.
  • the sphericity of 50 colloidal ceria randomly selected from the image of colloidal ceria obtained by SEM observation is similarly determined, and the average value thereof is defined as the sphericity of the colloidal ceria.
  • colloidal ceria dispersed in water is pulverized to obtain ceria particles (pulverization step).
  • colloidal ceria pulverized through a pulverization step is referred to as ceria particles.
  • the method for pulverizing colloidal ceria is not particularly limited.
  • the colloidal ceria may be pulverized using, for example, a bead mill or pulverized using a jet mill.
  • a bead mill first, beads having a hardness equal to or higher than that of a substance to be pulverized (colloidal ceria) are filled in a container (pulverization chamber) for pulverization. After filling, the beads are moved by rotating the rotating shaft in the center of the grinding chamber.
  • colloidal ceria dispersed in water (colloidal ceria aqueous dispersion, also referred to as “water dispersion”) is sent to the grinding chamber, colliding the beads with the colloidal ceria, and grinding the colloidal ceria to crush the colloidal ceria. .
  • colloidal ceria water dispersion of colloidal ceria
  • colloidal ceria water dispersion of colloidal ceria
  • water dispersion of colloidal ceria water dispersion of colloidal ceria
  • colloidal ceria is pulverized by colliding a colloidal ceria with a substance having hardness equal to or higher than that of colloidal ceria.
  • the shape of the substance to be collided is not particularly limited, and examples thereof include a spherical shape, a cylindrical shape, and a lump shape.
  • the substance to be collided is preferably a dispersion in which colloidal ceria is dispersed.
  • the ratio of the average primary particle diameter of the ceria particles to the average primary particle diameter of the colloidal ceria is less than 0.8. So that colloidal ceria is crushed.
  • the ratio of the average primary particle diameter of the ceria particles to the average primary particle diameter of the colloidal ceria may be 0.79 or less, 0.78 or less, or 0.70 or less, for example, 0.10 or more. .
  • the average primary particle diameter of the ceria particles is preferably 5 to 250 nm, more preferably 10 to 200 nm, and still more preferably 10 to 150 nm. If the average primary particle diameter of the ceria particles is 5 nm or more, a better polishing rate tends to be obtained. If the average primary particle size of the ceria particles is 250 nm or less, the film to be polished tends not to be damaged.
  • the measuring method of the average primary particle diameter of ceria particles is the same as the measuring method of the average primary particle diameter of colloidal ceria.
  • the average secondary particle size of the ceria particles is preferably 10 to 500 nm, more preferably 20 to 400 nm, and still more preferably 50 to 300 nm. If the average secondary particle diameter of the ceria particles is 10 nm or more, a better polishing rate tends to be obtained. If the average secondary particle diameter of the ceria particles is 500 nm or less, the film to be polished tends to be hardly damaged.
  • the measuring method of the average secondary particle diameter of ceria particles is the same as the measuring method of the average secondary particle diameter of colloidal ceria.
  • the ratio of the sphericity of the ceria particles to the sphericity of the colloidal ceria is 0.97 or less in the grinding step.
  • Crush colloidal ceria The ratio of the sphericity of the ceria particles to the sphericity of the colloidal ceria may be 0.965 or less, 0.96 or less, or 0.955 or less, for example, 0.30 or more.
  • the sphericity of the ceria particles is, for example, 30 to 90%, 35 to 85%, or 40 to 80%.
  • the method for measuring the sphericity of ceria particles is the same as the method for measuring the sphericity of colloidal ceria.
  • colloidal ceria before pulverization is a regular crystal shape, for example, a shape close to a tetrahedron, a hexahedron, a true sphere, etc., whereas the shape of the crushed colloidal ceria is particularly undefined. Shape.
  • the ceria particles after pulverization may contain colloidal ceria remaining without being pulverized. Moreover, you may mix a ceria particle and the colloidal ceria before a grinding
  • an additive Before the pulverization step, an additive may be added to the aqueous dispersion containing colloidal ceria to mix them. Further, after the pulverization step, an additive may be added to the aqueous dispersion containing ceria particles to mix them.
  • the additive used here may be the same as the additive used for the polishing liquid described later. Examples of the mixing method of the colloidal ceria and the additive and the mixing method of the ceria particles and the additive include a mixing method using stirring, a homogenizer, an ultrasonic disperser, or the like.
  • the ratio of the average primary particle diameter of the ceria particles to the average primary particle diameter of the colloidal ceria is less than 0.8, or the sphericity of the ceria particles relative to the sphericity of the colloidal ceria.
  • the method for producing a polishing liquid according to this embodiment is a method for producing a polishing liquid containing ceria particles, water, and an additive, and the slurry obtained by the above production method is mixed with the additive and polished.
  • a step of obtaining a liquid (additive mixing step) is provided.
  • the method for mixing the slurry and the additive include the same method as the method for mixing the colloidal ceria and the additive and the method for mixing the ceria particles and the additive.
  • the content of the ceria particles is preferably 0.1% by mass or more, more preferably 0.5% by mass or more, based on the total amount of the polishing liquid, from the viewpoint of obtaining a good polishing rate.
  • the content of the ceria particles is preferably 20% by mass or less, more preferably 5% by mass or less, and still more preferably 1.5% by mass from the viewpoint that aggregation of the ceria particles is suppressed and the film to be polished is hardly damaged. It is as follows.
  • the additive examples include a dispersant that increases the dispersibility of abrasive grains, a polishing rate improver that improves the polishing rate, a flattening agent (a flattening agent that reduces unevenness of the polished surface after polishing, a substrate after polishing, For example, a global planarizing agent for improving the global planarity), and a selectivity improving agent for improving the polishing selectivity of the inorganic insulating film with respect to the stopper film such as a silicon nitride film and a polysilicon film.
  • a dispersant that increases the dispersibility of abrasive grains
  • a polishing rate improver that improves the polishing rate
  • a flattening agent a flattening agent that reduces unevenness of the polished surface after polishing, a substrate after polishing
  • a global planarizing agent for improving the global planarity
  • a selectivity improving agent for improving the polishing selectivity of the inorganic insulating film with respect to the stopper film
  • Examples of the dispersant for enhancing the dispersibility of the abrasive grains include a water-soluble anionic dispersant, a water-soluble nonionic dispersant, a water-soluble cationic dispersant, and a water-soluble amphoteric dispersant.
  • the dispersant for enhancing the dispersibility of the abrasive grains is preferably a water-soluble anionic dispersant.
  • the dispersant may be one kind of these, or a mixture of two or more kinds.
  • the water-soluble anionic dispersant is preferably a polymer compound containing acrylic acid as a copolymerization component and a salt thereof, more preferably a salt of the polymer compound.
  • the polymer compound containing acrylic acid as a copolymerization component and a salt thereof include, for example, polyacrylic acid and an ammonium salt thereof, a copolymer of acrylic acid and methacrylic acid and an ammonium salt thereof, and acrylic acid amide and acrylic acid. And copolymers thereof and ammonium salts thereof.
  • water-soluble anionic dispersants include, for example, lauryl sulfate triethanolamine, ammonium lauryl sulfate, polyoxyethylene alkyl ether sulfate triethanolamine, and special polycarboxylic acid type polymer dispersants.
  • water-soluble nonionic dispersant examples include polyethylene glycol monolaurate, polyethylene glycol monostearate, polyethylene glycol distearate, polyethylene glycol monooleate, polyoxyethylene alkylamine, polyoxyethylene hydrogenated castor oil, 2 -Hydroxyethyl methacrylate and alkyl alkanolamides.
  • water-soluble cationic dispersant examples include polyvinyl pyrrolidone, coconut amine acetate, and stearyl amine acetate.
  • water-soluble amphoteric dispersant examples include lauryl betaine, stearyl betaine, lauryl dimethylamine oxide and 2-alkyl-N-carboxymethyl-N-hydroxyethylimidazolinium betaine.
  • Examples of the dispersant other than the above include a polymer compound having at least one selected from the group consisting of a carboxylic acid group and a carboxylic acid group.
  • the polymer compound is preferably a polymer obtained by polymerizing a monomer containing at least one selected from the group consisting of acrylic acid and methacrylic acid, or a salt thereof.
  • Examples of the polymer or a salt thereof include acrylic acid homopolymer (polyacrylic acid), methacrylic acid homopolymer (polymethacrylic acid), a copolymer of acrylic acid and methacrylic acid, acrylic acid or methacrylic acid and Examples include at least one selected from the group consisting of copolymers with other monomers, copolymers of acrylic acid and methacrylic acid with other monomers, and salts thereof.
  • An ammonium acid is mentioned.
  • the content of the dispersant is preferably 0.001 to 10% by mass on the basis of the total amount of the polishing liquid from the viewpoint of improving the dispersibility of the ceria particles to suppress sedimentation and further reducing polishing scratches on the film to be polished. .
  • the weight average molecular weight of the polymer is not particularly limited, but is preferably 100 to 150,000, more preferably 1000 to 20000.
  • the weight average molecular weight of the polymer is 100 or more, a better polishing rate tends to be easily obtained when a film to be polished such as a silicon oxide film or a silicon nitride film is polished.
  • the weight average molecular weight of the polymer is 150,000 or less, the storage stability of the polishing liquid tends to be difficult to decrease.
  • the weight average molecular weight is a value measured by GPC and converted based on standard polyoxyethylene.
  • the method for producing a polishing liquid may further include a step (mixing step) of mixing ceria particles and water.
  • a step (mixing step) of mixing ceria particles and water examples include the same method as the mixing method of the colloidal ceria and the additive and the mixing method of the ceria particles and the additive.
  • Water is not particularly limited, but preferably includes deionized water, ion-exchanged water, ultrapure water, and the like. It suffices if water is contained in the polishing liquid, and the content of water may be the remainder of the polishing liquid excluding the content of other components, and is not particularly limited.
  • the polishing liquid may further contain a solvent other than water as necessary. Examples of the solvent other than water include polar solvents such as ethanol and acetone.
  • the pH of the polishing liquid at room temperature (25 ° C.) is, for example, 4.0 or more and 8.0 or less.
  • the pH of the polishing liquid is preferably 4.5 or more, more preferably 4.8 or more.
  • the pH of the polishing liquid is 8.0 or less, the flatness improving effect tends to be sufficiently exhibited.
  • the pH of the polishing liquid is preferably 7.5 or less, more preferably 7.0 or less.
  • the pH of the polishing liquid is determined by measuring with a pH meter (for example, Model PH81 (trade name) manufactured by Yokogawa Electric Corporation).
  • the pH of the polishing solution is 2 using, for example, a standard buffer solution (phthalate pH buffer solution, pH: 4.21 (25 ° C.), neutral phosphate pH buffer solution, pH 6.86 (25 ° C.)).
  • a standard buffer solution phthalate pH buffer solution, pH: 4.21 (25 ° C.), neutral phosphate pH buffer solution, pH 6.86 (25 ° C.)
  • the electrode is put into a polishing liquid and measured as a value after being stabilized at 25 ° C. for 2 minutes or more.
  • the ratio of the average primary particle diameter of the ceria particles to the average primary particle diameter of the colloidal ceria is less than 0.8, or the spheres of the ceria particles with respect to the sphericity of the colloidal ceria
  • the polishing liquid according to this embodiment is preferably used for polishing a film to be polished, which will be described later, and is also preferably used for shallow trench isolation.
  • the polishing liquid according to the present embodiment may be stored as a one-part polishing liquid containing ceria particles, an additive, and water, and a ceria particle dispersion (first liquid) containing ceria particles, a dispersant, and water; And an additive liquid (second liquid) containing an additive other than the dispersant and water, and may be stored as a two-component polishing liquid.
  • the polishing liquid is preferably stored as a two-part polishing liquid.
  • additives other than the dispersant may be contained in the ceria particle dispersion.
  • planarization characteristics and polishing rate can be adjusted by arbitrarily changing the blend of these two liquids.
  • the polishing liquid may be stored as a two-part polishing liquid composed of a first liquid containing ceria particles and water and a second liquid containing an additive and water.
  • a two-part polishing liquid composed of a first liquid containing ceria particles and water and a second liquid containing an additive and water.
  • the slurry and polishing liquid according to the present embodiment is a slurry storage liquid that is used after being diluted with a liquid medium such as water at the time of use, for example, by a factor of 2 or more, from the viewpoint of suppressing costs related to storage, transportation, storage, and the like. Or it can be stored as a stock solution for polishing liquid.
  • the dilution rate of the stock solution is preferably 2 times or more, more preferably 3 times or more, from the viewpoint that the higher the magnification, the higher the cost-saving effect related to storage, transportation, storage and the like.
  • the upper limit of the dilution ratio of the stock solution is not particularly limited, but from the viewpoint of increasing the amount of components contained in the stock solution (higher concentration) and lowering the stability during storage as the magnification increases. In general, it is preferably 10 times or less, more preferably 7 times or less, and still more preferably 5 times or less. In addition, you may divide a structural component into 3 or more liquids, and also in that case, the dilution rate is the same as the above.
  • substrate polishing method Next, a method for polishing a substrate according to the present embodiment will be described.
  • a substrate on which a film to be polished is formed is prepared (substrate preparing step).
  • the substrate on which the film to be polished is formed is obtained, for example, by forming a film to be polished on the substrate by a low-pressure CVD method, a plasma CVD method, or the like, which will be described later.
  • Examples of the substrate include a substrate (semiconductor substrate) for manufacturing a semiconductor element.
  • Examples of the substrate related to the manufacture of the semiconductor element include a semiconductor substrate in which an inorganic insulating film is formed on the semiconductor substrate. For example, the semiconductor substrate in the stage where the circuit element and the wiring pattern are formed, the stage in which the circuit element is formed And the like.
  • Examples of the film to be polished include interlayer insulating films, BPSG films (silicon dioxide films doped with boron and phosphorus), STI formation films, and the like.
  • Examples of the interlayer insulating film include inorganic insulating films.
  • Examples of the inorganic insulating film include a silicon oxide film, a silicon nitride film, a composite film of a silicon oxide film, and the like.
  • the polishing film formed on the substrate surface is polished using the polishing liquid (polishing step). More specifically, for example, while the polishing film formed on the substrate surface is pressed against the polishing pad of the polishing surface plate, the polishing liquid is supplied between the polishing film and the polishing pad while the polishing liquid is being supplied between the polishing film and the polishing pad.
  • the film to be polished is polished by moving the disk relatively.
  • the ceria particle dispersion and additive liquid are sent through separate pipes, and these pipes are merged just before the outlet of the supply pipe to mix the two liquids, thereby polishing the pad.
  • the ceria particle dispersion liquid and the additive liquid may be mixed immediately before polishing.
  • a polishing liquid When using a stock solution for polishing liquid, a polishing liquid may be obtained by diluting the stock solution for polishing liquid with a liquid medium before the polishing step (stock solution diluting step).
  • the polishing liquid is obtained, for example, by supplying a polishing storage liquid and a liquid medium onto a polishing pad and diluting the polishing liquid on the polishing pad.
  • the storage liquid for polishing liquid in the polishing process, the film to be polished is polished using the polishing liquid obtained in the storage liquid dilution process.
  • the polishing liquid may be adjusted to a desired pH before the polishing step (pH adjustment step).
  • the pH is adjusted by, for example, a pH adjuster.
  • a pH adjuster for example, an acid and a base are mentioned.
  • the acid include nitric acid, sulfuric acid, hydrochloric acid, phosphoric acid, boric acid, and acetic acid.
  • the base include sodium hydroxide, ammonia, potassium hydroxide and calcium hydroxide.
  • the base is preferably ammonia.
  • the pH adjuster include ammonium salts of water-soluble polymers that have been partially neutralized with ammonia in advance.
  • the method for polishing a substrate by polishing the film to be polished using the above polishing liquid, unevenness on the surface of the film to be polished (for example, an inorganic insulating film) is eliminated, and the entire surface of the substrate is removed. A smooth surface can be obtained.
  • unevenness on the surface of the film to be polished for example, an inorganic insulating film
  • a substrate on which an inorganic insulating film is formed is prepared (first step).
  • the substrate on which the inorganic insulating film is formed can be obtained, for example, by forming an inorganic insulating film on the substrate by a low pressure CVD method, a plasma CVD method or the like.
  • the inorganic insulating film examples include a silicon oxide film and a silicon nitride film.
  • the silicon oxide film may be doped with elements such as phosphorus and boron.
  • the silicon oxide film In the formation of the silicon oxide film by the low pressure CVD method, monosilane: SiH 4 is used as the Si source, and oxygen: O 2 is used as the oxygen source.
  • SiH 4 —O 2 -based oxidation reaction By performing the SiH 4 —O 2 -based oxidation reaction at a low temperature of 400 ° C. or lower, a silicon oxide film can be obtained.
  • the silicon oxide film obtained by the low temperature CVD method is heat-treated at a temperature of 1000 ° C. or lower.
  • the silicon oxide film is doped with phosphorus: P in order to achieve surface planarization by high-temperature reflow, the silicon oxide film is preferably doped with phosphorus using a SiH 4 —O 2 —PH 3 based reaction gas.
  • Formation of a silicon oxide film by plasma CVD has an advantage that a chemical reaction requiring a high temperature can be performed at a low temperature under normal thermal equilibrium.
  • the plasma generation method there are two methods of capacitive coupling type and inductive coupling type.
  • the reaction gases SiH 4 as an Si source, SiH 4 -N 2 O-containing gas using N 2 O as oxygen source, and TEOS-O-based gas using tetraethoxysilane (TEOS) in an Si source (TEOS- Plasma CVD method).
  • the substrate temperature is preferably 250 to 400 ° C.
  • the reaction pressure is preferably 67 to 400 Pa.
  • SiH 2 Cl 2 —NH 3 oxidation reaction By performing the SiH 2 Cl 2 —NH 3 oxidation reaction at a high temperature of 900 ° C., a silicon nitride film can be obtained.
  • reaction gas used for forming the silicon nitride film by the plasma CVD method examples include SiH 4 —NH 3 based gas using SiH 4 as the Si source and NH 3 as the nitrogen source.
  • the substrate temperature is preferably 300 to 400 ° C.
  • the substrate on which the inorganic insulating film is formed is placed in a polishing apparatus (second step).
  • the substrate is arranged so that the inorganic insulating film on the substrate faces the polishing pad of the polishing apparatus.
  • a polishing apparatus As a polishing apparatus, a general polishing apparatus having a holder for holding a substrate such as a semiconductor substrate having a film to be polished, a motor capable of changing the number of rotations, and a polishing surface plate to which a polishing pad (polishing cloth) can be attached Is mentioned.
  • the polishing apparatus include polishing apparatuses manufactured by Ebara Corporation: F-REX, MIRRA manufactured by AMAT, and Reflexion.
  • the polishing pad is not particularly limited, and examples thereof include general nonwoven fabrics, foamed polyurethane, and porous fluororesins.
  • the polishing pad is preferably grooved so that the polishing liquid is accumulated.
  • the film to be polished is polished using the polishing liquid (third step).
  • the method for polishing the film to be polished is the same as the method for polishing the film to be polished in the polishing step.
  • the polishing liquid is continuously supplied to the polishing pad with a pump or the like during polishing.
  • Polishing conditions are not limited.
  • the rotation speed of the polishing platen is preferably a low rotation of 200 rotations / minute or less so that the semiconductor substrate does not jump out.
  • the pressure (processing load) applied to the semiconductor substrate is preferably 100 kPa or less so as not to cause scratches after polishing.
  • the supply amount of the polishing liquid is not particularly limited, but is preferably such an amount that the surface of the polishing pad is always covered with the polishing liquid.
  • the polished substrate may be washed and dried (cleaning and drying step).
  • the substrate is thoroughly washed in running water, for example, and then dried by removing water droplets adhering to the substrate using a spin dryer or the like.
  • the method for polishing a substrate it is possible to obtain a high polishing rate by polishing the film to be polished using the above polishing liquid (the film to be polished can be quickly polished).
  • polishing an inorganic insulating film, which is a film to be polished, with the above-described polishing liquid surface irregularities can be eliminated and the entire surface of the substrate can be made smooth.
  • the substrate polishing method according to the present embodiment can be applied not only to polishing an inorganic insulating film formed on a semiconductor substrate but also to manufacturing processes of various semiconductor devices.
  • the substrate polishing method according to the present embodiment includes, for example, a silicon oxide film formed on a wiring board having predetermined wiring, an inorganic insulating film such as glass and silicon nitride, polysilicon, Al, Cu, Ti, TiN, W , Optical glass such as photomasks, lenses and prisms, inorganic conductive films such as ITO, optical integrated circuits, optical switching elements, optical waveguides, optical fibers Polishing of the end face of the substrate, optical single crystal such as scintillator, solid laser single crystal, sapphire substrate for blue laser LED, semiconductor single crystal such as SiC, GaP and GaAs, glass substrate for magnetic disk, magnetic head, etc. Can be applied.
  • the semiconductor substrate is manufactured as follows, for example. First, a flattened shallow trench is formed, then a metal wiring such as aluminum is formed on the inorganic insulating film, and an inorganic insulating film is formed again between and on the wiring. Thereafter, the inorganic insulating film is polished using a polishing liquid to obtain a smooth surface. By repeating these steps a predetermined number of times, a semiconductor substrate having a desired number of layers can be obtained.
  • Example 1 (Production of slurry) An aqueous dispersion containing colloidal ceria having an average primary particle diameter of 90 nm and an average secondary particle diameter of 213 nm was prepared. The bead mill treatment was performed for 100 minutes, and colloidal ceria was pulverized until the average primary particle size was 50 nm and the average secondary particle size was 145 nm, to obtain a slurry containing ceria particles (ground abrasive grains) and water.
  • the ratio R2 / R1 of the average primary particle diameter (R2) of the ceria particles to the average primary particle diameter (R1) of the colloidal ceria is 0.56
  • the sphericity S of the ceria particles relative to the sphericity S a of the colloidal ceria the ratio S b / S a and b were crushed colloidal ceria as 0.95 or less.
  • Colloidal ceria before the bead mill treatment and ceria particles after the bead mill treatment were observed with an SEM. The obtained image is shown in FIG.
  • the average primary particle size of colloidal silica before pulverization and ceria particles after pulverization was determined by image analysis by SEM observation. That is, first, an image of ceria particles was obtained by SEM observation, and the obtained image of ceria particles was approximated by a circle, and the diameter of the circle was measured as the primary particle diameter. The primary particle diameters of 50 particles randomly selected from the image of the particles obtained by SEM observation were measured, and the average value was defined as the average primary particle diameter.
  • the average secondary particle size of the ceria particles contained in the slurry was measured using a laser diffraction particle size distribution meter (trade name: Master Sizer Microplus manufactured by Malvern). That is, first, the slurry for measurement was obtained by diluting the slurry to a concentration at which the measurement transmittance (H) for the He—Ne laser was 60 to 70%. The value of D50 obtained by measurement under the conditions of a refractive index of 1.93, a light source He—Ne laser, and zero absorption was taken as the average secondary particle diameter.
  • the sphericity of colloidal ceria before pulverization and ceria particles after pulverization was determined as follows. That is, first, image analysis by SEM observation was performed, and the true sphericity was obtained by the following formula (1).
  • S (%) r / R ⁇ 100 (1)
  • S represents the sphericity ratio (%)
  • r represents the maximum radius of a circle that can be drawn in one particle obtained by SEM observation
  • R represents one particle obtained by SEM observation. Indicates the minimum radius of the circle that contains.
  • the sphericity of 50 particles randomly selected from the image of the particles obtained by SEM observation was determined by the above method, and the average value thereof was defined as the sphericity.
  • a polishing liquid (content of pulverized abrasive: 0.25% by mass) having a total amount of 1000 g and a pH of 6.0 (25 ° C.).
  • the ceria particles contained in the polishing liquid had an average primary particle size of 50 nm and an average secondary particle size of 145 nm.
  • the average primary particle size and average secondary particle size of the ceria particles contained in the polishing liquid were determined in the same manner as the average primary particle size and average secondary particle size of the ceria particles contained in the slurry, respectively.
  • the pH of the polishing liquid was measured with a pH meter (Model PH81 (trade name) manufactured by Yokogawa Electric Corporation).
  • a blanket wafer on which no pattern was formed was used.
  • a silicon (Si) substrate having a silicon oxide film formed by a plasma TEOS method and a silicon (Si) substrate having a silicon nitride film formed by a low pressure CVD method were used.
  • the wafer was polished by a polishing apparatus (F-REX-300 manufactured by Ebara Corporation).
  • the wafer was set in a holder to which a substrate mounting suction pad was attached in a polishing apparatus.
  • the processing load is set to 210 gf / cm 2 (20.6 kPa), and the polishing platen and the wafer are rotated at 130 rpm for each time while the polishing liquid is dropped on the polishing pad at a rate of 250 ml / min.
  • the wafer was polished. After polishing, the wafer was thoroughly washed with pure water and dried.
  • the film thickness before and after polishing was measured using an optical interference type film thickness measuring apparatus to examine the polishing rate. The results are shown in Table 1.
  • Example 2 Slurry and polishing were carried out in the same manner as in Example 1 except that the processing time of the bead mill was changed as follows to pulverize the colloidal ceria until the average primary particle size and average secondary particle size shown in Table 1 were obtained.
  • a liquid was prepared. Using the prepared polishing liquid, the film to be polished was polished in the same manner as in Example 1, and the polishing rate was examined. The results are shown in Table 1. Processing time of bead mill Example 2: 50 minutes
  • Example 4 20 minutes
  • Example 3 A slurry and a polishing liquid were prepared in the same manner as in Example 1 except that a jet mill was used instead of the bead mill. Using the prepared polishing liquid, the film to be polished was polished in the same manner as in Example 1, and the polishing rate was examined. The results are shown in Table 1.
  • Example 3 A polishing liquid was prepared in the same manner as in Example 1 except that a slurry containing colloidal ceria having the average primary particle size and average secondary particle size shown in Table 1 and water was prepared without pulverizing the colloidal ceria. . Using the prepared polishing liquid, the film to be polished was polished in the same manner as in Example 1, and the polishing rate was examined. The results are shown in Table 1.
  • the polishing liquid obtained by subjecting colloidal ceria to the grinding treatment is the same as the polishing liquid obtained without performing the grinding treatment. It can be seen that the polishing rate is higher than that.

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Abstract

One embodiment of the present invention is a method for producing a slurry containing ceria particles and water. This method for producing a slurry comprises a pulverization step wherein ceria particles are obtained by pulverizing colloidal ceria dispersed in water. In the pulverization step, the colloidal ceria is pulverized so that the ratio of the average primary particle diameter of the ceria particles to the average primary particle diameter of the colloidal ceria is less than 0.8.

Description

スラリ、研磨液及びそれらの製造方法、並びに基板の研磨方法SLURRY, POLISHING LIQUID, PROCESS FOR PRODUCING THEM, AND METHOD FOR POLISHING SUBSTRATE

 本発明は、スラリ、研磨液及びそれらの製造方法、並びに基板の研磨方法に関する。 The present invention relates to a slurry, a polishing liquid, a manufacturing method thereof, and a polishing method for a substrate.

 現在のULSI(Ultra Large Scale Integration)半導体素子製造工程では、半導体素子の高密度・微細化のための加工技術が研究開発されている。その加工技術の一つであるCMP(ケミカルメカニカルポリッシング:化学機械研磨)技術は、半導体素子製造工程において、層間絶縁膜の平坦化、シャロートレンチ分離(STI)の形成、プラグ及び埋め込み金属配線形成等を行う際に、必須の技術となってきている。 In the current ULSI (Ultra Large Scale Integration) semiconductor device manufacturing process, processing technologies for high density and miniaturization of semiconductor devices are being researched and developed. CMP (Chemical Mechanical Polishing) technology, which is one of the processing technologies, is used in semiconductor device manufacturing processes, such as planarization of interlayer insulating films, formation of shallow trench isolation (STI), formation of plugs and buried metal wiring, etc. Has become an indispensable technology.

 従来、半導体素子製造工程において、酸化珪素膜等の無機絶縁膜はプラズマ-CVD(化学気相成長)、低圧-CVD(化学気相成長)等の方法で形成されている。この無機絶縁膜を平坦化するための化学機械研磨液として、フュームドシリカ系の研磨液を用いることが一般的に検討されている。フュームドシリカ系の研磨液は、四塩化珪酸を熱分解する等の方法で粒成長させて得られた粒子が配合されたスラリのpHを調整することによって製造される。但し、この様なフュームドシリカ系の研磨液では、研磨速度が低いという技術課題がある。 Conventionally, in a semiconductor element manufacturing process, an inorganic insulating film such as a silicon oxide film is formed by a method such as plasma-CVD (chemical vapor deposition) or low-pressure CVD (chemical vapor deposition). As a chemical mechanical polishing liquid for planarizing the inorganic insulating film, it has been generally studied to use a fumed silica-based polishing liquid. The fumed silica-based polishing liquid is produced by adjusting the pH of a slurry containing particles obtained by grain growth by a method such as thermal decomposition of tetrachlorosilicic acid. However, such a fumed silica-based polishing liquid has a technical problem that the polishing rate is low.

 また、デザインルール0.25μm以降の世代では、集積回路内の素子分離にSTIが用いられている。STIの形成では、基板上に成膜した余分な酸化珪素膜を取り除くために、例えばコロイダルシリカ系の研磨液を用いたCMP技術が使用される。この場合、任意の深さにて研磨を停止させるために、酸化珪素膜の下に研磨速度の低いストッパ膜が形成される。ストッパ膜には、窒化珪素膜等が使用される。余分な酸化珪素膜を効率的に取り除くとともに、その後の研磨の進行を充分に抑制するには、ストッパ膜の研磨速度に対する酸化珪素膜の研磨速度の比が大きいことが望ましい。しかし、従来のコロイダルシリカ系の研磨液を用いた場合の上記研磨速度の比は3程度と小さいため、従来のコロイダルシリカ系研磨液は、STI用として実用に耐える特性を有していない。 In the generations after the design rule 0.25 μm, STI is used for element isolation in the integrated circuit. In the formation of STI, for example, a CMP technique using a colloidal silica-based polishing liquid is used to remove an excess silicon oxide film formed on the substrate. In this case, in order to stop the polishing at an arbitrary depth, a stopper film having a low polishing rate is formed under the silicon oxide film. A silicon nitride film or the like is used for the stopper film. In order to efficiently remove the excess silicon oxide film and sufficiently suppress the subsequent polishing, it is desirable that the ratio of the polishing rate of the silicon oxide film to the polishing rate of the stopper film is large. However, since the ratio of the above-mentioned polishing rates when a conventional colloidal silica-based polishing liquid is used is as small as about 3, the conventional colloidal silica-based polishing liquid does not have a characteristic that can withstand practical use for STI.

 一方、フォトマスク、レンズ等のガラス表面に対する研磨液として、酸化セリウム粒子を含む酸化セリウム系研磨液が用いられている。酸化セリウム粒子の硬度は、シリカ粒子及びアルミナ粒子の硬度に比べて低い。したがって、酸化セリウム粒子を含む酸化セリウム系の研磨液を用いた場合、シリカ粒子又はアルミナ粒子を含む研磨液を用いた場合に比べて、研磨に際し研磨表面に傷が入りにくいことから、酸化セリウム系の研磨液は、仕上げ鏡面研磨に有用である。また、酸化セリウム系研磨液では、フュームドシリカ系、コロイダルシリカ系等のシリカ系研磨液に比べ、研磨速度が速いという利点がある。 On the other hand, a cerium oxide-based polishing liquid containing cerium oxide particles is used as a polishing liquid for glass surfaces such as photomasks and lenses. The hardness of cerium oxide particles is lower than the hardness of silica particles and alumina particles. Therefore, when a cerium oxide-based polishing liquid containing cerium oxide particles is used, the polishing surface is less likely to be damaged when polishing compared to the case where a polishing liquid containing silica particles or alumina particles is used. This polishing liquid is useful for finish mirror polishing. Further, the cerium oxide-based polishing liquid has an advantage that the polishing rate is faster than silica-based polishing liquids such as fumed silica type and colloidal silica type.

 ところで、配線及びSTIのデザインルールの微細化の進展に伴い、研磨の際に生じる研磨傷の低減がこれまで以上に求められている。研磨傷を低減できる研磨剤として、例えば、特許文献1には、1nm以上95nm以下の体積平均粒径を有し、直径0.56μm以上の粒子数が1mlあたり100万個以下である研磨材と水とからなることを特徴とするCMPプロセス用研磨液が開示されている。また、特許文献2には、粒子径が10nmを超えかつ100nm未満である1次粒子が全数の90%以上である酸化セリウム粒子を媒体に分散させたスラリーを含む酸化セリウム研磨剤が開示されている。 By the way, with the progress of miniaturization of wiring and STI design rules, reduction of polishing flaws that occur during polishing is required more than ever. As an abrasive capable of reducing polishing scratches, for example, Patent Document 1 discloses an abrasive having a volume average particle diameter of 1 nm to 95 nm and a number of particles having a diameter of 0.56 μm or more of 1 million or less per ml. A polishing liquid for CMP process characterized by comprising water is disclosed. Patent Document 2 discloses a cerium oxide abrasive containing a slurry in which cerium oxide particles having a particle diameter of more than 10 nm and less than 100 nm of primary particles of 90% or more are dispersed in a medium. Yes.

特開2003-188122号公報JP 2003-188122 A 特開平10-106994号公報JP-A-10-106994

 しかしながら、粒径を小さくすると、研磨傷が低減する一方で、研磨速度が低下して、研磨作業の効率が下がるという問題が生じる場合がある。本発明は、このような実情に鑑みてなされたものであり、同程度の平均一次粒子径を有するセリア粒子を含有する研磨液と比べて、研磨速度に優れる研磨液、当該研磨液を得ることが可能なスラリ、及びこれらの製造方法、並びに当該研磨液を用いた基板の研磨方法を提供することを目的とする。 However, when the particle size is reduced, there is a problem that the polishing scratches are reduced, while the polishing rate is lowered and the efficiency of the polishing operation is lowered. The present invention has been made in view of such circumstances, and obtains a polishing liquid that has an excellent polishing rate compared to a polishing liquid containing ceria particles having the same average primary particle diameter, and the polishing liquid. It is an object of the present invention to provide a slurry that can be used, a manufacturing method thereof, and a method of polishing a substrate using the polishing liquid.

 本発明は、一態様において、セリア粒子と水とを含有するスラリの製造方法であって、水中に分散されたコロイダルセリアを粉砕して、セリア粒子を得る粉砕工程を備え、粉砕工程において、コロイダルセリアの平均一次粒子径に対するセリア粒子の平均一次粒子径の比が0.8未満となるように粉砕する、スラリの製造方法である。 In one aspect, the present invention is a method for producing a slurry containing ceria particles and water, comprising a crushing step of crushing colloidal ceria dispersed in water to obtain ceria particles. This is a slurry production method in which grinding is performed so that the ratio of the average primary particle diameter of ceria particles to the average primary particle diameter of ceria is less than 0.8.

 本発明は、一態様において、セリア粒子と水とを含有するスラリの製造方法であって、水中に分散されたコロイダルセリアを粉砕して、セリア粒子を得る粉砕工程を備え、粉砕工程において、コロイダルセリアの真球度に対するセリア粒子の真球度の比が0.97以下となるように粉砕する、スラリの製造方法である。 In one aspect, the present invention is a method for producing a slurry containing ceria particles and water, comprising a crushing step of crushing colloidal ceria dispersed in water to obtain ceria particles. This is a slurry manufacturing method in which crushing is performed so that the ratio of sphericity of ceria particles to sphericity of ceria is 0.97 or less.

 粉砕工程において、コロイダルセリアはビーズミルを用いて粉砕されてよい。 In the pulverization step, the colloidal ceria may be pulverized using a bead mill.

 粉砕工程において、また、コロイダルセリアはジェットミルを用いて粉砕されてよい。 In the pulverization step, the colloidal ceria may be pulverized using a jet mill.

 本発明は、一態様において、セリア粒子と水と添加剤とを含有する研磨液の製造方法であって、上記の製造方法によって得られたスラリと添加剤とを混合して研磨液を得る工程と備える、研磨液の製造方法である。 In one aspect, the present invention is a method for producing a polishing liquid containing ceria particles, water, and an additive, wherein the slurry obtained by the above production method is mixed with an additive to obtain a polishing liquid. A method for producing a polishing liquid.

 本発明は、一態様において、上記のスラリの製造方法により得られたスラリである。 In one aspect, the present invention is a slurry obtained by the above-described slurry manufacturing method.

 本発明は、一態様において、上記の研磨液の製造方法により得られた研磨液である。 In one aspect, the present invention is a polishing liquid obtained by the above polishing liquid manufacturing method.

 本発明は、一態様において、上記の研磨液を用いて、基板表面に形成された被研磨膜を研磨する研磨工程を備える、基板の研磨方法である。 In one aspect, the present invention is a method for polishing a substrate, comprising a polishing step of polishing a film to be polished formed on the surface of the substrate using the polishing liquid.

 本発明によれば、同程度の平均一次粒子径を有するセリア粒子を含有する研磨液と比べて、研磨速度に優れる研磨液、当該研磨液を構成するスラリ、及びこれらの製造方法、並びに当該研磨液を用いた基板の研磨方法を提供することができる。 According to the present invention, as compared with a polishing liquid containing ceria particles having the same average primary particle diameter, a polishing liquid having an excellent polishing rate, a slurry constituting the polishing liquid, a manufacturing method thereof, and the polishing A method for polishing a substrate using a liquid can be provided.

(a)粉砕前のコロイダルセリアの画像である。(b)粉砕後のセリア粒子の画像である。(A) An image of colloidal ceria before pulverization. (B) An image of ceria particles after pulverization.

 以下、本発明の実施形態について詳細に説明する。 Hereinafter, embodiments of the present invention will be described in detail.

 本明細書において、「スラリ」は少なくともセリア粒子(砥粒)及び水を含む組成物を意味し、「研磨液」は少なくともセリア粒子(砥粒)、添加剤及び水を含む組成物を意味する。 In this specification, “slurry” means a composition containing at least ceria particles (abrasive grains) and water, and “polishing liquid” means a composition containing at least ceria particles (abrasive grains), additives and water. .

[スラリの製造方法]
 本実施形態に係るスラリの製造方法は、セリア粒子と水とを含有するスラリの製造方法である。この製造方法では、まず、コロイダルセリアを用意する(用意工程)。コロイダルセリアは、例えば、液相法によってセリアの結晶を成長させるプロセスを経て得られる公知のものであってよい。液相法としては、例えば、(1)ゾルゲル法、(2)水熱合成法、(3)沈殿法等が挙げられる。コロイダルセリアは、いずれの方法で得られたものであってもよい。
[Slurry manufacturing method]
The slurry manufacturing method according to the present embodiment is a slurry manufacturing method containing ceria particles and water. In this manufacturing method, first, colloidal ceria is prepared (preparation process). The colloidal ceria may be, for example, a known one obtained through a process of growing ceria crystals by a liquid phase method. Examples of the liquid phase method include (1) sol-gel method, (2) hydrothermal synthesis method, and (3) precipitation method. Colloidal ceria may be obtained by any method.

 コロイダルセリアの平均一次粒子径は、例えば、10~200nmである。なお、コロイダルセリアの平均一次粒子径は、SEM観察による画像解析で求められる。すなわち、まず、SEM観察で得られたコロイダルセリアの画像を円で近似し、その円の直径を一次粒子径として測定する。SEM観察によって得られたコロイダルセリアの画像から無作為に選ばれた50粒のコロイダルセリアについて同様に一次粒子径を測定し、それらの平均値を平均一次粒子径とする。 The average primary particle diameter of colloidal ceria is, for example, 10 to 200 nm. In addition, the average primary particle diameter of colloidal ceria is calculated | required by the image analysis by SEM observation. That is, first, an image of colloidal ceria obtained by SEM observation is approximated by a circle, and the diameter of the circle is measured as the primary particle diameter. For 50 colloidal ceria randomly selected from an image of colloidal ceria obtained by SEM observation, the primary particle diameter is measured in the same manner, and the average value thereof is taken as the average primary particle diameter.

 コロイダルセリアの平均二次粒子径は、例えば、20~600nmである。なお、コロイダルセリアの平均二次粒子径は、レーザ回折式粒度分布計(例えば、Malvern社製 商品名:Master Sizer Microplus)を用いて測定されるD50の値(体積分布のメジアン径、累積中央値)を意味する。測定の際には、He-Neレーザに対する測定時透過率(H)が60~70%となる濃度にコロイダルセリア分散液を希釈したサンプルを用い、屈折率:1.93、光源:He-Neレーザ、及び吸収:0の条件で測定する。 The average secondary particle diameter of colloidal ceria is, for example, 20 to 600 nm. The average secondary particle size of colloidal ceria is a value of D50 (median diameter of volume distribution, cumulative median value) measured using a laser diffraction particle size distribution analyzer (for example, product name: Master Sizer Microplus manufactured by Malvern). ). In the measurement, a sample obtained by diluting the colloidal ceria dispersion to a concentration at which the measurement transmittance (H) with respect to the He—Ne laser is 60 to 70% is used. Measurement is performed under the conditions of laser and absorption: 0.

 コロイダルセリアの真球度は、例えば、60~100%である。なお、コロイダルセリアの真球度は、SEM観察による画像解析を行い、下記式(1)で表される真球率S(%)を用いて求められる。
 S(%)=r/R×100・・・(1)
 式(1)中、rはSEM観察で得られた画像においてコロイダルセリア一粒の中に描ける円の最大半径(nm)を示し、RはSEM観察で得られた画像においてコロイダルセリア一粒を内包する円の最小半径(nm)を示す。SEM観察によって得られたコロイダルセリアの画像から無作為に選ばれた50粒のコロイダルセリアについて同様に真球率を求め、それらの平均値をコロイダルセリアの真球度とする。
The sphericity of colloidal ceria is, for example, 60 to 100%. In addition, the sphericity of colloidal ceria is calculated | required using image analysis by SEM observation and using the sphericity ratio S (%) represented by following formula (1).
S (%) = r / R × 100 (1)
In the formula (1), r indicates the maximum radius (nm) of a circle that can be drawn in one colloidal ceria grain in an image obtained by SEM observation, and R includes one colloidal ceria grain in the image obtained by SEM observation. The minimum radius (nm) of a circle to be played. The sphericity of 50 colloidal ceria randomly selected from the image of colloidal ceria obtained by SEM observation is similarly determined, and the average value thereof is defined as the sphericity of the colloidal ceria.

 用意工程に続いて、水中に分散されたコロイダルセリアを粉砕して、セリア粒子を得る(粉砕工程)。なお、本明細書では、粉砕工程を経て粉砕されたコロイダルセリアをセリア粒子と呼ぶ。 Following the preparation step, colloidal ceria dispersed in water is pulverized to obtain ceria particles (pulverization step). In the present specification, colloidal ceria pulverized through a pulverization step is referred to as ceria particles.

 コロイダルセリアを粉砕する方法は、特に制限されない。コロイダルセリアは、例えば、ビーズミルを用いて粉砕されてもよく、ジェットミルを用いて粉砕されてもよい。ビーズミルを用いる場合、まず、粉砕を行う容器(粉砕室)の中に、粉砕の対象となる物質(コロイダルセリア)と同等か、又はそれよりも高い硬度を有するビーズを充填する。充填後、粉砕室中央の回転軸を回転させることで、ビーズを運動させる。水中に分散されたコロイダルセリア(コロイダルセリアの水分散液、「水分散液」ともいう)を粉砕室に送り込み、ビーズとコロイダルセリアとを衝突させ、コロイダルセリアを摺りつぶすことによってコロイダルセリアを粉砕する。 The method for pulverizing colloidal ceria is not particularly limited. The colloidal ceria may be pulverized using, for example, a bead mill or pulverized using a jet mill. When using a bead mill, first, beads having a hardness equal to or higher than that of a substance to be pulverized (colloidal ceria) are filled in a container (pulverization chamber) for pulverization. After filling, the beads are moved by rotating the rotating shaft in the center of the grinding chamber. Colloidal ceria dispersed in water (colloidal ceria aqueous dispersion, also referred to as “water dispersion”) is sent to the grinding chamber, colliding the beads with the colloidal ceria, and grinding the colloidal ceria to crush the colloidal ceria. .

 ジェットミルを用いる場合、粉砕室の中に、水中に分散されたコロイダルセリア(コロイダルセリアの水分散液)を高圧かつ高速な条件で噴射する。高圧かつ高速に噴射することにより、コロイダルセリアと同等かそれ以上の硬度を有する物質とコロイダルセリアとを衝突させて、コロイダルセリアを粉砕する。衝突させる物質の形状としては、特に制限なく、球状、円柱状、塊状等が挙げられる。衝突させる物質は、好ましくはコロイダルセリアを分散させた分散液である。 When using a jet mill, colloidal ceria (water dispersion of colloidal ceria) dispersed in water is injected into the grinding chamber under high pressure and high speed. By injecting at high pressure and high speed, colloidal ceria is pulverized by colliding a colloidal ceria with a substance having hardness equal to or higher than that of colloidal ceria. The shape of the substance to be collided is not particularly limited, and examples thereof include a spherical shape, a cylindrical shape, and a lump shape. The substance to be collided is preferably a dispersion in which colloidal ceria is dispersed.

 一実施形態では、粉砕工程において、コロイダルセリアの平均一次粒子径に対するセリア粒子の平均一次粒子径の比(セリア粒子の平均一次粒子径/コロイダルセリアの平均一次粒子径)が0.8未満となるように、コロイダルセリアを粉砕する。コロイダルセリアの平均一次粒子径に対するセリア粒子の平均一次粒子径の比は、0.79以下、0.78以下、又は0.70以下であってもよく、例えば0.10以上であってもよい。 In one embodiment, in the pulverization step, the ratio of the average primary particle diameter of the ceria particles to the average primary particle diameter of the colloidal ceria (average ceria particle primary particle diameter / colloidal ceria average primary particle diameter) is less than 0.8. So that colloidal ceria is crushed. The ratio of the average primary particle diameter of the ceria particles to the average primary particle diameter of the colloidal ceria may be 0.79 or less, 0.78 or less, or 0.70 or less, for example, 0.10 or more. .

 セリア粒子の平均一次粒子径は、好ましくは5~250nm、より好ましくは10~200nm、更に好ましくは10~150nmである。セリア粒子の平均一次粒子径が5nm以上であれば、更に良好な研磨速度が得られる傾向にある。セリア粒子の平均一次粒子径が250nm以下であれば、被研磨膜に傷がつきにくくなる傾向にある。なお、セリア粒子の平均一次粒子径の測定方法は、コロイダルセリアの平均一次粒子径の測定方法と同様である。 The average primary particle diameter of the ceria particles is preferably 5 to 250 nm, more preferably 10 to 200 nm, and still more preferably 10 to 150 nm. If the average primary particle diameter of the ceria particles is 5 nm or more, a better polishing rate tends to be obtained. If the average primary particle size of the ceria particles is 250 nm or less, the film to be polished tends not to be damaged. In addition, the measuring method of the average primary particle diameter of ceria particles is the same as the measuring method of the average primary particle diameter of colloidal ceria.

 セリア粒子の平均二次粒径は、好ましくは10~500nm、より好ましくは20~400nm、更に好ましくは50~300nmである。セリア粒子の平均二次粒子径が10nm以上であれば、更に良好な研磨速度が得られる傾向にある。セリア粒子の平均二次粒子径が500nm以下であれば、被研磨膜に傷がつきにくくなる傾向にある。なお、セリア粒子の平均二次粒子径の測定方法は、コロイダルセリアの平均二次粒子径の測定方法と同様である。 The average secondary particle size of the ceria particles is preferably 10 to 500 nm, more preferably 20 to 400 nm, and still more preferably 50 to 300 nm. If the average secondary particle diameter of the ceria particles is 10 nm or more, a better polishing rate tends to be obtained. If the average secondary particle diameter of the ceria particles is 500 nm or less, the film to be polished tends to be hardly damaged. In addition, the measuring method of the average secondary particle diameter of ceria particles is the same as the measuring method of the average secondary particle diameter of colloidal ceria.

 他の一実施形態では、粉砕工程において、コロイダルセリアの真球度に対するセリア粒子の真球度の比(セリア粒子の真球度/コロイダルセリアの真球度)が0.97以下となるように、コロイダルセリアを粉砕する。コロイダルセリアの真球度に対するセリア粒子の真球度の比は、0.965以下、0.96以下、又は0.955以下であってもよく、例えば0.30以上であってよもよい。 In another embodiment, the ratio of the sphericity of the ceria particles to the sphericity of the colloidal ceria (the sphericity of the ceria particles / the sphericity of the colloidal ceria) is 0.97 or less in the grinding step. , Crush colloidal ceria. The ratio of the sphericity of the ceria particles to the sphericity of the colloidal ceria may be 0.965 or less, 0.96 or less, or 0.955 or less, for example, 0.30 or more.

 セリア粒子の真球度は、例えば30~90%、35~85%又は40~80%である。なお、セリア粒子の真球度の測定方法は、コロイダルセリアの真球度の測定方法と同様である。 The sphericity of the ceria particles is, for example, 30 to 90%, 35 to 85%, or 40 to 80%. The method for measuring the sphericity of ceria particles is the same as the method for measuring the sphericity of colloidal ceria.

 なお、コロイダルセリアが粉砕されたか否かは、例えば、走査型電子顕微鏡(SEM、例えば、株式会社日立ハイテクノロジーズ製、S-4800)を用いた観察によって確認可能である。粉砕前のコロイダルセリアの形状は規則正しい結晶形、例えば、四面体、十六面体、真球状等に近しい形状であるのに対して、粉砕されたコロイダルセリアの形状は、特に形の定まっていないいびつな形状である。粉砕後のセリア粒子には、粉砕されずに残ったコロイダルセリアが混在していてもよい。また、粉砕工程の後に、セリア粒子と粉砕前のコロイダルセリアとを任意の割合で混合してもよい。 Note that whether or not the colloidal ceria has been crushed can be confirmed by observation using, for example, a scanning electron microscope (SEM, for example, S-4800, manufactured by Hitachi High-Technologies Corporation). The shape of colloidal ceria before pulverization is a regular crystal shape, for example, a shape close to a tetrahedron, a hexahedron, a true sphere, etc., whereas the shape of the crushed colloidal ceria is particularly undefined. Shape. The ceria particles after pulverization may contain colloidal ceria remaining without being pulverized. Moreover, you may mix a ceria particle and the colloidal ceria before a grinding | pulverization in arbitrary ratios after a grinding | pulverization process.

 粉砕工程の前において、コロイダルセリアを含む水分散液に添加剤を添加して両者を混合してもよい。また、粉砕工程の後において、セリア粒子を含む水分散液に添加剤を添加して両者を混合してもよい。ここで用いられる添加剤は、後述する研磨液に用いられる添加剤と同様であってよい。コロイダルセリアと添加剤との混合方法及びセリア粒子と添加剤との混合方法としては、例えば、攪拌、ホモジナイザー、超音波分散機等による混合方法が挙げられる。 Before the pulverization step, an additive may be added to the aqueous dispersion containing colloidal ceria to mix them. Further, after the pulverization step, an additive may be added to the aqueous dispersion containing ceria particles to mix them. The additive used here may be the same as the additive used for the polishing liquid described later. Examples of the mixing method of the colloidal ceria and the additive and the mixing method of the ceria particles and the additive include a mixing method using stirring, a homogenizer, an ultrasonic disperser, or the like.

 本実施形態に係るスラリの製造方法によれば、コロイダルセリアの平均一次粒子径に対するセリア粒子の平均一次粒子径の比が0.8未満、又はコロイダルセリアの真球度に対するセリア粒子の真球度の比が0.97以下となるように、水中に分散されたコロイダルセリアを粉砕してセリア粒子を得ることにより、当該セリア粒子及び水を含有するスラリから、研磨速度に優れる研磨液を得ることが可能である。すなわち、上記製造方法によってスラリを製造することにより、同程度の平均一次粒子径を有するセリア粒子を含有する研磨液に比べて、研磨速度に優れる研磨液を得ることが可能なスラリを製造可能である。 According to the slurry production method of the present embodiment, the ratio of the average primary particle diameter of the ceria particles to the average primary particle diameter of the colloidal ceria is less than 0.8, or the sphericity of the ceria particles relative to the sphericity of the colloidal ceria. By obtaining a ceria particle by pulverizing colloidal ceria dispersed in water so that the ratio is 0.97 or less, a polishing liquid having an excellent polishing rate can be obtained from the slurry containing the ceria particle and water. Is possible. That is, by producing a slurry by the above production method, it is possible to produce a slurry capable of obtaining a polishing liquid having an excellent polishing rate compared to a polishing liquid containing ceria particles having the same average primary particle diameter. is there.

[研磨液の製造方法]
 本実施形態に係る研磨液の製造方法は、セリア粒子と水と添加剤とを含有する研磨液の製造方法であって、上記の製造方法により得られたスラリと添加剤とを混合して研磨液を得る工程(添加剤混合工程)を備える。スラリと添加剤との混合方法としては、上記コロイダルセリアと添加剤との混合方法及びセリア粒子と添加剤との混合方法と同様の方法が挙げられる。
[Production method of polishing liquid]
The method for producing a polishing liquid according to this embodiment is a method for producing a polishing liquid containing ceria particles, water, and an additive, and the slurry obtained by the above production method is mixed with the additive and polished. A step of obtaining a liquid (additive mixing step) is provided. Examples of the method for mixing the slurry and the additive include the same method as the method for mixing the colloidal ceria and the additive and the method for mixing the ceria particles and the additive.

 セリア粒子の含有量は、良好な研磨速度が得られる観点で、研磨液全量基準で、好ましくは0.1質量%以上、より好ましくは0.5質量%以上である。セリア粒子の含有量は、セリア粒子の凝集が抑制されて被研磨膜に傷がつきにくくなる観点から、好ましくは20質量%以下、より好ましくは5質量%以下、更に好ましくは1.5質量%以下である。 The content of the ceria particles is preferably 0.1% by mass or more, more preferably 0.5% by mass or more, based on the total amount of the polishing liquid, from the viewpoint of obtaining a good polishing rate. The content of the ceria particles is preferably 20% by mass or less, more preferably 5% by mass or less, and still more preferably 1.5% by mass from the viewpoint that aggregation of the ceria particles is suppressed and the film to be polished is hardly damaged. It is as follows.

 添加剤としては、例えば、砥粒の分散性を高める分散剤、研磨速度を向上させる研磨速度向上剤、平坦化剤(研磨後の被研磨面の凹凸を低減する平坦化剤、研磨後の基板のグローバル平坦性を向上させるグローバル平坦化剤)、窒化珪素膜及びポリシリコン膜等のストッパ膜に対する無機絶縁膜の研磨選択比を向上させる選択比向上剤等が挙げられる。 Examples of the additive include a dispersant that increases the dispersibility of abrasive grains, a polishing rate improver that improves the polishing rate, a flattening agent (a flattening agent that reduces unevenness of the polished surface after polishing, a substrate after polishing, For example, a global planarizing agent for improving the global planarity), and a selectivity improving agent for improving the polishing selectivity of the inorganic insulating film with respect to the stopper film such as a silicon nitride film and a polysilicon film.

 砥粒の分散性を高める分散剤としては、例えば、水溶性陰イオン性分散剤、水溶性非イオン性分散剤、水溶性陽イオン性分散剤、水溶性両性分散剤等が挙げられる。砥粒の分散性を高める分散剤は、好ましくは水溶性陰イオン性分散剤である。分散剤は、これらの一種単独であってもよく、二種以上の混合物であってもよい。 Examples of the dispersant for enhancing the dispersibility of the abrasive grains include a water-soluble anionic dispersant, a water-soluble nonionic dispersant, a water-soluble cationic dispersant, and a water-soluble amphoteric dispersant. The dispersant for enhancing the dispersibility of the abrasive grains is preferably a water-soluble anionic dispersant. The dispersant may be one kind of these, or a mixture of two or more kinds.

 水溶性陰イオン性分散剤は、好ましくは共重合成分としてアクリル酸を含む高分子化合物及びその塩、より好ましくは当該高分子化合物の塩である。共重合成分としてアクリル酸を含む高分子化合物及びその塩としては、例えば、ポリアクリル酸及びそのアンモニウム塩、アクリル酸とメタクリル酸との共重合体及びそのアンモニウム塩、並びにアクリル酸アミドとアクリル酸との共重合体及びそのアンモニウム塩が挙げられる。 The water-soluble anionic dispersant is preferably a polymer compound containing acrylic acid as a copolymerization component and a salt thereof, more preferably a salt of the polymer compound. Examples of the polymer compound containing acrylic acid as a copolymerization component and a salt thereof include, for example, polyacrylic acid and an ammonium salt thereof, a copolymer of acrylic acid and methacrylic acid and an ammonium salt thereof, and acrylic acid amide and acrylic acid. And copolymers thereof and ammonium salts thereof.

 その他の水溶性陰イオン性分散剤としては、例えば、ラウリル硫酸トリエタノールアミン、ラウリル硫酸アンモニウム、ポリオキシエチレンアルキルエーテル硫酸トリエタノールアミン及び特殊ポリカルボン酸型高分子分散剤が挙げられる。 Other water-soluble anionic dispersants include, for example, lauryl sulfate triethanolamine, ammonium lauryl sulfate, polyoxyethylene alkyl ether sulfate triethanolamine, and special polycarboxylic acid type polymer dispersants.

 水溶性非イオン性分散剤としては、例えば、ポリエチレングリコールモノラウレート、ポリエチレングリコールモノステアレート、ポリエチレングリコールジステアレート、ポリエチレングリコールモノオレエート、ポリオキシエチレンアルキルアミン、ポリオキシエチレン硬化ヒマシ油、2-ヒドロキシエチルメタクリレート及びアルキルアルカノールアミドが挙げられる。 Examples of the water-soluble nonionic dispersant include polyethylene glycol monolaurate, polyethylene glycol monostearate, polyethylene glycol distearate, polyethylene glycol monooleate, polyoxyethylene alkylamine, polyoxyethylene hydrogenated castor oil, 2 -Hydroxyethyl methacrylate and alkyl alkanolamides.

 水溶性陽イオン性分散剤としては、例えば、ポリビニルピロリドン、ココナットアミンアセテート及びステアリルアミンアセテートが挙げられる。 Examples of the water-soluble cationic dispersant include polyvinyl pyrrolidone, coconut amine acetate, and stearyl amine acetate.

 水溶性両性分散剤としては、例えば、ラウリルベタイン、ステアリルベタイン、ラウリルジメチルアミンオキサイド及び2-アルキル-N-カルボキシメチル-N-ヒドロキシエチルイミダゾリニウムベタインが挙げられる。 Examples of the water-soluble amphoteric dispersant include lauryl betaine, stearyl betaine, lauryl dimethylamine oxide and 2-alkyl-N-carboxymethyl-N-hydroxyethylimidazolinium betaine.

 上記以外の分散剤としては、カルボン酸基及びカルボン酸塩基からなる群より選ばれる少なくとも一種を有する高分子化合物が挙げられる。当該高分子化合物は、好ましくはアクリル酸及びメタクリル酸からなる群より選ばれる少なくとも一種を含む単量体を重合させて得られる重合体又はその塩である。当該重合体又はその塩としては、アクリル酸の単独重合体(ポリアクリル酸)、メタクリル酸の単独重合体(ポリメタクリル酸)、アクリル酸とメタクリル酸との共重合体、アクリル酸又はメタクリル酸と上記他の単量体との共重合体、アクリル酸及びメタクリル酸と上記他の単量体との共重合体、並びにこれらの塩からなる群より選ばれる少なくとも一種が挙げられ、例えば、ポリアクリル酸アンモニウムが挙げられる。 Examples of the dispersant other than the above include a polymer compound having at least one selected from the group consisting of a carboxylic acid group and a carboxylic acid group. The polymer compound is preferably a polymer obtained by polymerizing a monomer containing at least one selected from the group consisting of acrylic acid and methacrylic acid, or a salt thereof. Examples of the polymer or a salt thereof include acrylic acid homopolymer (polyacrylic acid), methacrylic acid homopolymer (polymethacrylic acid), a copolymer of acrylic acid and methacrylic acid, acrylic acid or methacrylic acid and Examples include at least one selected from the group consisting of copolymers with other monomers, copolymers of acrylic acid and methacrylic acid with other monomers, and salts thereof. An ammonium acid is mentioned.

 分散剤の含有量は、セリア粒子の分散性を向上させて沈降を抑制し、被研磨膜の研磨傷を更に低減する観点から、好ましくは研磨液全量基準で0.001~10質量%である。 The content of the dispersant is preferably 0.001 to 10% by mass on the basis of the total amount of the polishing liquid from the viewpoint of improving the dispersibility of the ceria particles to suppress sedimentation and further reducing polishing scratches on the film to be polished. .

 分散剤がポリマーを含む場合、ポリマーの重量平均分子量は、特に制限はないが、好ましくは100~150000、より好ましくは1000~20000である。ポリマーの重量平均分子量が100以上であれば、酸化珪素膜、窒化珪素膜等の被研磨膜を研磨するときに、更に良好な研磨速度が得られやすい傾向にある。ポリマーの重量平均分子量が150000以下であれば、研磨液の保存安定性が低下しにくい傾向にある。なお、重量平均分子量は、GPCで測定し、標準ポリオキシエチレンに基づき換算した値である。 When the dispersant contains a polymer, the weight average molecular weight of the polymer is not particularly limited, but is preferably 100 to 150,000, more preferably 1000 to 20000. When the weight average molecular weight of the polymer is 100 or more, a better polishing rate tends to be easily obtained when a film to be polished such as a silicon oxide film or a silicon nitride film is polished. If the weight average molecular weight of the polymer is 150,000 or less, the storage stability of the polishing liquid tends to be difficult to decrease. The weight average molecular weight is a value measured by GPC and converted based on standard polyoxyethylene.

 研磨液の製造方法は、セリア粒子と水とを混合する工程(混合工程)を更に備えていてもよい。セリア粒子と水との混合方法としては、上記コロイダルセリアと添加剤との混合方法及びセリア粒子と添加剤との混合方法と同様の方法が挙げられる。 The method for producing a polishing liquid may further include a step (mixing step) of mixing ceria particles and water. Examples of the mixing method of the ceria particles and water include the same method as the mixing method of the colloidal ceria and the additive and the mixing method of the ceria particles and the additive.

 水としては、特に制限されないが、好ましくは脱イオン水、イオン交換水、超純水等が挙げられる。水が研磨液に含有されていればよく、水の含有量は、他の含有成分の含有量を除いた研磨液の残部でよく、特に限定されない。なお、研磨液は、必要に応じて水以外の溶媒を更に含有されてもよい。水以外の溶媒としては、例えば、エタノール、アセトン等の極性溶媒等が挙げられる。 Water is not particularly limited, but preferably includes deionized water, ion-exchanged water, ultrapure water, and the like. It suffices if water is contained in the polishing liquid, and the content of water may be the remainder of the polishing liquid excluding the content of other components, and is not particularly limited. The polishing liquid may further contain a solvent other than water as necessary. Examples of the solvent other than water include polar solvents such as ethanol and acetone.

[研磨液の特性]
 室温(25℃)における研磨液のpHは、例えば4.0以上8.0以下である。研磨液のpHが4.0以上であると研磨液の保存安定性が向上し、被研磨膜の傷の発生数が減少する傾向にある。研磨液のpHは、同様の観点から、好ましくは4.5以上、より好ましくは4.8以上である。研磨液のpHが8.0以下であると、平坦性の向上効果を充分に発揮することができる傾向にある。研磨液のpHは、同様の観点から、好ましくは7.5以下、より好ましくは7.0以下である。研磨液のpHは、pHメータ(例えば、横河電機株式会社製のModel PH81(商品名))で測定して求められる。研磨液のpHは、例えば、標準緩衝液(フタル酸塩pH緩衝液,pH:4.21(25℃)、中性リン酸塩pH緩衝液,pH6.86(25℃))を用いて2点校正した後、電極を研磨液に入れて、25℃で2分以上経過して安定した後の値として測定される。
[Characteristics of polishing liquid]
The pH of the polishing liquid at room temperature (25 ° C.) is, for example, 4.0 or more and 8.0 or less. When the pH of the polishing liquid is 4.0 or more, the storage stability of the polishing liquid is improved, and the number of scratches on the film to be polished tends to decrease. From the same viewpoint, the pH of the polishing liquid is preferably 4.5 or more, more preferably 4.8 or more. When the pH of the polishing liquid is 8.0 or less, the flatness improving effect tends to be sufficiently exhibited. From the same viewpoint, the pH of the polishing liquid is preferably 7.5 or less, more preferably 7.0 or less. The pH of the polishing liquid is determined by measuring with a pH meter (for example, Model PH81 (trade name) manufactured by Yokogawa Electric Corporation). The pH of the polishing solution is 2 using, for example, a standard buffer solution (phthalate pH buffer solution, pH: 4.21 (25 ° C.), neutral phosphate pH buffer solution, pH 6.86 (25 ° C.)). After the point calibration, the electrode is put into a polishing liquid and measured as a value after being stabilized at 25 ° C. for 2 minutes or more.

 本実施形態に係る研磨液の製造方法によれば、コロイダルセリアの平均一次粒子径に対するセリア粒子の平均一次粒子径の比が0.8未満、又はコロイダルセリアの真球度に対するセリア粒子の真球度の比が0.97以下となるように、水中に分散されたコロイダルセリアを粉砕して、セリア粒子を得ることにより、研磨速度に優れる研磨液を得ることが可能である。すなわち、上記製造方法によって研磨液を製造することにより、同程度の平均一次粒子径を有するセリア粒子を含有する研磨液に比べて、研磨速度に優れる研磨液を得ることが可能である。 According to the method for producing a polishing liquid according to the present embodiment, the ratio of the average primary particle diameter of the ceria particles to the average primary particle diameter of the colloidal ceria is less than 0.8, or the spheres of the ceria particles with respect to the sphericity of the colloidal ceria By crushing colloidal ceria dispersed in water so that the degree ratio is 0.97 or less to obtain ceria particles, it is possible to obtain a polishing liquid having an excellent polishing rate. That is, by producing a polishing liquid by the above production method, it is possible to obtain a polishing liquid having an excellent polishing rate as compared with a polishing liquid containing ceria particles having the same average primary particle diameter.

 本実施形態に係る研磨液は、後述の被研磨膜の研磨に好適に使用され、シャロートレンチ分離にも好適に使用される。 The polishing liquid according to this embodiment is preferably used for polishing a film to be polished, which will be described later, and is also preferably used for shallow trench isolation.

[スラリ及び研磨液の保存方法]
 本実施形態に係る研磨液は、セリア粒子、添加剤及び水を含む一液式研磨液として保存されてもよく、セリア粒子、分散剤及び水を含むセリア粒子分散液(第1の液)と、分散剤以外の添加剤及び水を含む添加液(第2の液)と、から構成される二液式研磨液として保存されてもよい。分散剤以外の添加剤がセリア粒子の分散安定性に影響しない観点から、研磨液は、好ましくは二液式研磨液として保存される。なお、二液式研磨液の場合、分散剤以外の添加剤は、セリア粒子分散液にも含有されていてもよい。
[Method of storing slurry and polishing liquid]
The polishing liquid according to the present embodiment may be stored as a one-part polishing liquid containing ceria particles, an additive, and water, and a ceria particle dispersion (first liquid) containing ceria particles, a dispersant, and water; And an additive liquid (second liquid) containing an additive other than the dispersant and water, and may be stored as a two-component polishing liquid. From the standpoint that additives other than the dispersant do not affect the dispersion stability of the ceria particles, the polishing liquid is preferably stored as a two-part polishing liquid. In the case of a two-component polishing liquid, additives other than the dispersant may be contained in the ceria particle dispersion.

 セリア粒子分散液と添加液とに分けた二液式研磨液として保存する場合、これら二液の配合を任意に変えることにより、平坦化特性と研磨速度の調整が可能となる。 When storing as a two-part polishing liquid divided into a ceria particle dispersion and an additive liquid, the planarization characteristics and polishing rate can be adjusted by arbitrarily changing the blend of these two liquids.

 他の態様において、研磨液は、セリア粒子及び水を含む第1の液と、添加剤及び水を含む第2の液とから構成される二液式研磨液として保存されてもよい。セリア粒子と添加剤とを分けて保存することにより、研磨液を使用する直前までセリア粒子の分散安定性をより良好に保つことができるため、より効果的な研磨速度及び平坦性を得ることが可能である。 In another embodiment, the polishing liquid may be stored as a two-part polishing liquid composed of a first liquid containing ceria particles and water and a second liquid containing an additive and water. By storing ceria particles and additives separately, the dispersion stability of the ceria particles can be kept better until just before using the polishing liquid, so that more effective polishing speed and flatness can be obtained. Is possible.

 本実施形態に係るスラリ及び研磨液は、貯蔵・運搬・保管等に係るコストを抑制できる観点から、使用時に水等の液状媒体で、例えば2倍以上に希釈されて使用されるスラリ用貯蔵液又は研磨液用貯蔵液として保管されることができる。 The slurry and polishing liquid according to the present embodiment is a slurry storage liquid that is used after being diluted with a liquid medium such as water at the time of use, for example, by a factor of 2 or more, from the viewpoint of suppressing costs related to storage, transportation, storage, and the like. Or it can be stored as a stock solution for polishing liquid.

 貯蔵液の希釈倍率は、倍率が高いほど貯蔵・運搬・保管等に係るコストの抑制効果が高い観点から、好ましくは2倍以上、より好ましくは3倍以上である。貯蔵液の希釈倍率の上限値は、特に制限はないが、倍率が高いほど貯蔵液に含まれる成分の量が多く(濃度が高く)なり、保管中の安定性が低下する傾向がある観点から、一般的には、好ましくは10倍以下、より好ましくは7倍以下、更に好ましくは5倍以下である。なお、構成成分を三液以上に分けてもよく、その場合についても希釈倍率は上記と同様である。 The dilution rate of the stock solution is preferably 2 times or more, more preferably 3 times or more, from the viewpoint that the higher the magnification, the higher the cost-saving effect related to storage, transportation, storage and the like. The upper limit of the dilution ratio of the stock solution is not particularly limited, but from the viewpoint of increasing the amount of components contained in the stock solution (higher concentration) and lowering the stability during storage as the magnification increases. In general, it is preferably 10 times or less, more preferably 7 times or less, and still more preferably 5 times or less. In addition, you may divide a structural component into 3 or more liquids, and also in that case, the dilution rate is the same as the above.

[基板の研磨方法]
 次に、本実施形態に係る基板の研磨方法について説明する。まず、被研磨膜が形成されている基板を用意する(基板用意工程)。被研磨膜が形成された基板は、例えば、基板上に後述の低圧CVD法、プラズマCVD法等により被研磨膜を形成することにより得られる。
[Substrate polishing method]
Next, a method for polishing a substrate according to the present embodiment will be described. First, a substrate on which a film to be polished is formed is prepared (substrate preparing step). The substrate on which the film to be polished is formed is obtained, for example, by forming a film to be polished on the substrate by a low-pressure CVD method, a plasma CVD method, or the like, which will be described later.

 基板としては、半導体素子の製造に係る基板(半導体基板)等が挙げられる。半導体素子の製造に係る基板としては、半導体基板上に無機絶縁膜が形成された半導体基板が挙げられ、例えば、回路素子及び配線パターンが形成された段階の半導体基板、回路素子が形成された段階の半導体基板等が挙げられる。 Examples of the substrate include a substrate (semiconductor substrate) for manufacturing a semiconductor element. Examples of the substrate related to the manufacture of the semiconductor element include a semiconductor substrate in which an inorganic insulating film is formed on the semiconductor substrate. For example, the semiconductor substrate in the stage where the circuit element and the wiring pattern are formed, the stage in which the circuit element is formed And the like.

 被研磨膜としては、層間絶縁膜、BPSG膜(ボロン、リンをドープした二酸化珪素膜)、STI形成膜等が挙げられる。層間絶縁膜としては、無機絶縁膜が挙げられる。無機絶縁膜としては、例えば、酸化珪素膜、窒化珪素膜、酸化珪素膜の複合膜等が挙げられる。 Examples of the film to be polished include interlayer insulating films, BPSG films (silicon dioxide films doped with boron and phosphorus), STI formation films, and the like. Examples of the interlayer insulating film include inorganic insulating films. Examples of the inorganic insulating film include a silicon oxide film, a silicon nitride film, a composite film of a silicon oxide film, and the like.

 基板用意工程に続いて、上記研磨液を用いて、基板表面に形成された被研磨膜を研磨する(研磨工程)。より詳しくは、例えば、基板表面に形成された被研磨膜を研磨定盤の研磨パッドに押圧した状態で、前記研磨液を被研磨膜と研磨パッドとの間に供給しながら、基板と研磨定盤とを相対的に動かすことにより、被研磨膜は研磨される。 Subsequent to the substrate preparation step, the polishing film formed on the substrate surface is polished using the polishing liquid (polishing step). More specifically, for example, while the polishing film formed on the substrate surface is pressed against the polishing pad of the polishing surface plate, the polishing liquid is supplied between the polishing film and the polishing pad while the polishing liquid is being supplied between the polishing film and the polishing pad. The film to be polished is polished by moving the disk relatively.

 二液式研磨液を用いて研磨する場合、セリア粒子分散液及び添加液をそれぞれ別の配管で送液し、これらの配管を供給配管出口の直前で合流させて両液を混合して研磨パッド上に供給してもよく、研磨直前にセリア粒子分散液と添加液とを混合してもよい。 When polishing with a two-part polishing liquid, the ceria particle dispersion and additive liquid are sent through separate pipes, and these pipes are merged just before the outlet of the supply pipe to mix the two liquids, thereby polishing the pad. The ceria particle dispersion liquid and the additive liquid may be mixed immediately before polishing.

 研磨液用貯蔵液を用いる場合、研磨工程の前に、研磨液用貯蔵液を液状媒体で希釈して研磨液を得てもよい(貯蔵液希釈工程)。研磨液は、例えば、研磨パッド上に研磨用貯蔵液と液状媒体とを供給し、研磨パッド上で希釈することにより得られる。研磨液用貯蔵液を用いる場合、研磨工程では、貯蔵液希釈工程において得られた研磨液を用いて被研磨膜を研磨する。 When using a stock solution for polishing liquid, a polishing liquid may be obtained by diluting the stock solution for polishing liquid with a liquid medium before the polishing step (stock solution diluting step). The polishing liquid is obtained, for example, by supplying a polishing storage liquid and a liquid medium onto a polishing pad and diluting the polishing liquid on the polishing pad. In the case of using the storage liquid for polishing liquid, in the polishing process, the film to be polished is polished using the polishing liquid obtained in the storage liquid dilution process.

 研磨液は、研磨工程の前に、所望のpHに調整されてよい(pH調整工程)。pHは、例えば、pH調整剤により調整される。pH調整剤としては、特に制限はないが、例えば、酸及び塩基が挙げられる。酸としては、硝酸、硫酸、塩酸、リン酸、ホウ酸及び酢酸が挙げられる。塩基としては、水酸化ナトリウム、アンモニア、水酸化カリウム及び水酸化カルシウム等が挙げられる。研磨液が半導体基板の被研磨膜の研磨に使用される場合には、塩基は、好ましくはアンモニアである。pH調整剤としては、また、予めアンモニアで部分的に中和された水溶性高分子のアンモニウム塩が挙げられる。 The polishing liquid may be adjusted to a desired pH before the polishing step (pH adjustment step). The pH is adjusted by, for example, a pH adjuster. Although there is no restriction | limiting in particular as a pH adjuster, For example, an acid and a base are mentioned. Examples of the acid include nitric acid, sulfuric acid, hydrochloric acid, phosphoric acid, boric acid, and acetic acid. Examples of the base include sodium hydroxide, ammonia, potassium hydroxide and calcium hydroxide. When the polishing liquid is used for polishing a film to be polished on a semiconductor substrate, the base is preferably ammonia. Examples of the pH adjuster include ammonium salts of water-soluble polymers that have been partially neutralized with ammonia in advance.

 本実施形態に係る基板の研磨方法によれば、上記研磨液を用いて被研磨膜を研磨することによって、被研磨膜(例えば、無機絶縁膜)表面の凹凸を解消し、基板表面の全面を平滑な面とすることができる。 According to the method for polishing a substrate according to the present embodiment, by polishing the film to be polished using the above polishing liquid, unevenness on the surface of the film to be polished (for example, an inorganic insulating film) is eliminated, and the entire surface of the substrate is removed. A smooth surface can be obtained.

 以下、無機絶縁膜が形成された半導体基板の研磨方法を例に挙げて、基板の研磨方法を更に詳細に説明する。まず、無機絶縁膜が形成された基板を用意する(第1工程)。無機絶縁膜が形成された基板は、例えば基板上に低圧CVD法、プラズマCVD法等により無機絶縁膜を形成することにより得られる。 Hereinafter, the method for polishing a substrate will be described in more detail by taking a method for polishing a semiconductor substrate on which an inorganic insulating film is formed as an example. First, a substrate on which an inorganic insulating film is formed is prepared (first step). The substrate on which the inorganic insulating film is formed can be obtained, for example, by forming an inorganic insulating film on the substrate by a low pressure CVD method, a plasma CVD method or the like.

 無機絶縁膜としては、例えば、酸化珪素膜及び窒化珪素膜が挙げられる。酸化珪素膜は、リン及びホウ素等の元素がドープされていても良い。 Examples of the inorganic insulating film include a silicon oxide film and a silicon nitride film. The silicon oxide film may be doped with elements such as phosphorus and boron.

 低圧CVD法による酸化珪素膜形成では、Si源としてモノシラン:SiH、酸素源として酸素:Oを用いる。SiH-O系酸化反応を400℃以下の低温で行うことにより、酸化珪素膜が得られる。場合によっては、低温CVD法により得られた酸化珪素膜は、1000℃又はそれ以下の温度で熱処理される。高温リフローによる表面平坦化を図るために、酸化珪素膜にリン:Pをドープするときには、酸化珪素膜は、好ましくはSiH-O-PH系反応ガスを用いてリンをドープされる。 In the formation of the silicon oxide film by the low pressure CVD method, monosilane: SiH 4 is used as the Si source, and oxygen: O 2 is used as the oxygen source. By performing the SiH 4 —O 2 -based oxidation reaction at a low temperature of 400 ° C. or lower, a silicon oxide film can be obtained. In some cases, the silicon oxide film obtained by the low temperature CVD method is heat-treated at a temperature of 1000 ° C. or lower. When the silicon oxide film is doped with phosphorus: P in order to achieve surface planarization by high-temperature reflow, the silicon oxide film is preferably doped with phosphorus using a SiH 4 —O 2 —PH 3 based reaction gas.

 プラズマCVD法による酸化珪素膜形成は、通常の熱平衡下では高温を必要とする化学反応を低温でできるという利点を有する。プラズマ発生法としては、容量結合型と誘導結合型の2つが挙げられる。反応ガスとしては、Si源としてSiH、酸素源としてNOを用いたSiH-NO系ガス、及びテトラエトキシシラン(TEOS)をSi源に用いたTEOS-O系ガス(TEOS-プラズマCVD法)が挙げられる。基板温度は好ましくは250~400℃、反応圧力は好ましくは67~400Paである。 Formation of a silicon oxide film by plasma CVD has an advantage that a chemical reaction requiring a high temperature can be performed at a low temperature under normal thermal equilibrium. As the plasma generation method, there are two methods of capacitive coupling type and inductive coupling type. The reaction gases, SiH 4 as an Si source, SiH 4 -N 2 O-containing gas using N 2 O as oxygen source, and TEOS-O-based gas using tetraethoxysilane (TEOS) in an Si source (TEOS- Plasma CVD method). The substrate temperature is preferably 250 to 400 ° C., and the reaction pressure is preferably 67 to 400 Pa.

 低圧CVD法による窒化珪素膜形成では、Si源としてジクロルシラン:SiHCl、窒素源としてアンモニア:NHを用いる。SiHCl-NH系酸化反応を900℃の高温で行うことにより、窒化珪素膜が得られる。 A silicon nitride film formed by low pressure CVD method, dichlorosilane as Si source: SiH 2 Cl 2, ammonia as a nitrogen source: the NH 3 is used. By performing the SiH 2 Cl 2 —NH 3 oxidation reaction at a high temperature of 900 ° C., a silicon nitride film can be obtained.

 プラズマCVD法による窒化珪素膜形成で用いる反応ガスとしては、Si源としてSiH、窒素源としてNHを用いたSiH-NH系ガスが挙げられる。基板温度は、好ましくは300~400℃である。 Examples of the reaction gas used for forming the silicon nitride film by the plasma CVD method include SiH 4 —NH 3 based gas using SiH 4 as the Si source and NH 3 as the nitrogen source. The substrate temperature is preferably 300 to 400 ° C.

 第1工程に続いて、無機絶縁膜が形成された基板を研磨装置に配置する(第2工程)。基板上の無機絶縁膜が研磨装置の研磨パッドに対向するように、基板を配置する。 Subsequent to the first step, the substrate on which the inorganic insulating film is formed is placed in a polishing apparatus (second step). The substrate is arranged so that the inorganic insulating film on the substrate faces the polishing pad of the polishing apparatus.

 研磨装置としては、被研磨膜を有する半導体基板等の基板を保持するホルダー、回転数を変更可能なモータ、及び研磨パッド(研磨布)を貼り付け可能な研磨定盤を有する一般的な研磨装置が挙げられる。研磨装置としては、例えば、株式会社荏原製作所製の研磨装置:F-REX、AMAT製MIRRA,Reflexion等が挙げられる。 As a polishing apparatus, a general polishing apparatus having a holder for holding a substrate such as a semiconductor substrate having a film to be polished, a motor capable of changing the number of rotations, and a polishing surface plate to which a polishing pad (polishing cloth) can be attached Is mentioned. Examples of the polishing apparatus include polishing apparatuses manufactured by Ebara Corporation: F-REX, MIRRA manufactured by AMAT, and Reflexion.

 研磨パッドとしては、特に制限なく、一般的な不織布、発泡ポリウレタン、多孔質フッ素樹脂等が挙げられる。研磨パッドには、好ましくは研磨液が溜まるような溝加工が施されている。 The polishing pad is not particularly limited, and examples thereof include general nonwoven fabrics, foamed polyurethane, and porous fluororesins. The polishing pad is preferably grooved so that the polishing liquid is accumulated.

 第2工程に続いて、上記研磨液を用いて被研磨膜を研磨する(第3工程)。被研磨膜の研磨方法は、上記研磨工程における被研磨膜の研磨方法と同様である。研磨液は、研磨している間、研磨パッドにポンプ等で連続的に供給される。 Subsequent to the second step, the film to be polished is polished using the polishing liquid (third step). The method for polishing the film to be polished is the same as the method for polishing the film to be polished in the polishing step. The polishing liquid is continuously supplied to the polishing pad with a pump or the like during polishing.

 研磨条件に制限はない。研磨定盤の回転速度は、半導体基板が飛び出さないように、好ましくは200回転/分以下の低回転である。半導体基板にかける圧力(加工荷重)は、研磨後に傷が発生しないように、好ましくは100kPa以下である。研磨液の供給量は、特に制限はないが、好ましくは研磨パッドの表面が常に研磨液で覆われている程度の量である。 Polishing conditions are not limited. The rotation speed of the polishing platen is preferably a low rotation of 200 rotations / minute or less so that the semiconductor substrate does not jump out. The pressure (processing load) applied to the semiconductor substrate is preferably 100 kPa or less so as not to cause scratches after polishing. The supply amount of the polishing liquid is not particularly limited, but is preferably such an amount that the surface of the polishing pad is always covered with the polishing liquid.

 第3工程に続いて、研磨後の基板を洗浄及び乾燥させてよい(洗浄及び乾燥工程)。基板は、例えば、流水中でよく洗浄後、スピンドライヤ等を用いて基板上に付着した水滴を払い落として、乾燥させる。 Subsequent to the third step, the polished substrate may be washed and dried (cleaning and drying step). The substrate is thoroughly washed in running water, for example, and then dried by removing water droplets adhering to the substrate using a spin dryer or the like.

 本実施形態に係る基板の研磨方法によれば、上記研磨液を用いて被研磨膜を研磨することにより、高い研磨速度を得ることが可能である(被研磨膜を素早く研磨可能である)。被研磨膜である無機絶縁膜を上記研磨液で研磨することによって、表面の凹凸を解消し、基板表面の全面を平滑な面にすることが可能である。 According to the method for polishing a substrate according to this embodiment, it is possible to obtain a high polishing rate by polishing the film to be polished using the above polishing liquid (the film to be polished can be quickly polished). By polishing an inorganic insulating film, which is a film to be polished, with the above-described polishing liquid, surface irregularities can be eliminated and the entire surface of the substrate can be made smooth.

 本実施形態に係る基板の研磨方法は、半導体基板に形成された無機絶縁膜の研磨だけでなく、各種半導体装置の製造プロセス等にも適用されうる。本実施形態に係る基板の研磨方法は、例えば、所定の配線を有する配線板に形成された酸化珪素膜、ガラス及び窒化珪素等の無機絶縁膜、ポリシリコン、Al、Cu、Ti、TiN、W、Ta及びTaN等を主として含有する膜、フォトマスク・レンズ・プリズム等の光学ガラス、ITO等の無機導電膜、ガラス及び結晶質材料で構成される光集積回路・光スイッチング素子・光導波路、光ファイバーの端面、シンチレータ等の光学用単結晶、固体レーザ単結晶、青色レーザLED用サファイヤ基板、SiC、GaP及びGaAs等の半導体単結晶、磁気ディスク用ガラス基板、並びに磁気ヘッド等を研磨することにも適用されうる。 The substrate polishing method according to the present embodiment can be applied not only to polishing an inorganic insulating film formed on a semiconductor substrate but also to manufacturing processes of various semiconductor devices. The substrate polishing method according to the present embodiment includes, for example, a silicon oxide film formed on a wiring board having predetermined wiring, an inorganic insulating film such as glass and silicon nitride, polysilicon, Al, Cu, Ti, TiN, W , Optical glass such as photomasks, lenses and prisms, inorganic conductive films such as ITO, optical integrated circuits, optical switching elements, optical waveguides, optical fibers Polishing of the end face of the substrate, optical single crystal such as scintillator, solid laser single crystal, sapphire substrate for blue laser LED, semiconductor single crystal such as SiC, GaP and GaAs, glass substrate for magnetic disk, magnetic head, etc. Can be applied.

 半導体基板は、例えば次のようにして製造される。まず、平坦化されたシャロートレンチを形成した後、無機絶縁膜の上にアルミニウム等の金属配線を形成し、その配線間及び配線上に再度無機絶縁膜を形成する。その後、研磨液を用いて当該無機絶縁膜を研磨して平滑な面を得る。これらの工程を所定数繰り返すことにより、所望の層数を有する半導体基板が得られる。 The semiconductor substrate is manufactured as follows, for example. First, a flattened shallow trench is formed, then a metal wiring such as aluminum is formed on the inorganic insulating film, and an inorganic insulating film is formed again between and on the wiring. Thereafter, the inorganic insulating film is polished using a polishing liquid to obtain a smooth surface. By repeating these steps a predetermined number of times, a semiconductor substrate having a desired number of layers can be obtained.

 以下、実施例により本発明を説明するが、本発明はこれらの実施例に制限されるものではない。 Hereinafter, the present invention will be described with reference to examples, but the present invention is not limited to these examples.

<実施例1>
(スラリの作製)
 平均一次粒子径が90nm、平均二次粒子径が213nmのコロイダルセリアを含む水分散液を準備した。ビーズミル処理を100分間行い、平均一次粒子径が50nm、平均二次粒子径が145nmになるまでコロイダルセリアを粉砕して、セリア粒子(粉砕砥粒)と水とを含むスラリを得た。すなわち、コロイダルセリアの平均一次粒子径(R1)に対するセリア粒子の平均一次粒子径(R2)の比R2/R1が0.56、及びコロイダルセリアの真球度Sに対するセリア粒子の真球度Sの比S/Sが0.95以下となるようにコロイダルセリアを粉砕した。
 ビーズミル処理前のコロイダルセリア及びビーズミル処理後のセリア粒子をSEMで観察した。得られた画像を図1に示す。
<Example 1>
(Production of slurry)
An aqueous dispersion containing colloidal ceria having an average primary particle diameter of 90 nm and an average secondary particle diameter of 213 nm was prepared. The bead mill treatment was performed for 100 minutes, and colloidal ceria was pulverized until the average primary particle size was 50 nm and the average secondary particle size was 145 nm, to obtain a slurry containing ceria particles (ground abrasive grains) and water. That is, the ratio R2 / R1 of the average primary particle diameter (R2) of the ceria particles to the average primary particle diameter (R1) of the colloidal ceria is 0.56, and the sphericity S of the ceria particles relative to the sphericity S a of the colloidal ceria the ratio S b / S a and b were crushed colloidal ceria as 0.95 or less.
Colloidal ceria before the bead mill treatment and ceria particles after the bead mill treatment were observed with an SEM. The obtained image is shown in FIG.

 粉砕前のコロイダルシリカ及び粉砕後のセリア粒子の平均1次粒子径を、SEM観察による画像解析で求めた。すなわち、まず、SEM観察でセリア粒子の画像を得て、得られたセリア粒子の画像を円で近似し、その円の直径を一次粒子径として測定した。SEM観察によって得られた粒子の画像から無作為に選ばれた50粒の一次粒子径を測定し、その平均値を平均一次粒子径とした。 The average primary particle size of colloidal silica before pulverization and ceria particles after pulverization was determined by image analysis by SEM observation. That is, first, an image of ceria particles was obtained by SEM observation, and the obtained image of ceria particles was approximated by a circle, and the diameter of the circle was measured as the primary particle diameter. The primary particle diameters of 50 particles randomly selected from the image of the particles obtained by SEM observation were measured, and the average value was defined as the average primary particle diameter.

 スラリに含まれるセリア粒子の平均二次粒子径を、レーザ回折式粒度分布計(Malvern社製 商品名:Master Sizer Microplus)を用いて測定した。すなわち、まず、He-Neレーザに対する測定時透過率(H)が60~70%となる濃度にスラリを希釈して測定用サンプルを得た。屈折率1.93、光源He-Neレーザ、及び吸収0の条件で測定して得られたD50の値を平均二次粒子径とした。 The average secondary particle size of the ceria particles contained in the slurry was measured using a laser diffraction particle size distribution meter (trade name: Master Sizer Microplus manufactured by Malvern). That is, first, the slurry for measurement was obtained by diluting the slurry to a concentration at which the measurement transmittance (H) for the He—Ne laser was 60 to 70%. The value of D50 obtained by measurement under the conditions of a refractive index of 1.93, a light source He—Ne laser, and zero absorption was taken as the average secondary particle diameter.

 粉砕前のコロイダルセリア及び粉砕後のセリア粒子の真球度をそれぞれ、次にようにして求めた。すなわち、まず、SEM観察による画像解析を行い、下記式(1)により、真球率を求めた。
 S(%)=r/R×100・・・(1)
 式(1)中、Sは真球率(%)を示し、rはSEM観察で得られた粒子一粒の中に描ける円の最大半径を示し、RはSEM観察で得られた粒子一粒を内包する円の最小半径を示す。SEM観察によって得られた粒子の画像から無作為に選ばれた50粒の各真球率を上記方法により求め、それらの平均値を真球度とした。
The sphericity of colloidal ceria before pulverization and ceria particles after pulverization was determined as follows. That is, first, image analysis by SEM observation was performed, and the true sphericity was obtained by the following formula (1).
S (%) = r / R × 100 (1)
In the formula (1), S represents the sphericity ratio (%), r represents the maximum radius of a circle that can be drawn in one particle obtained by SEM observation, and R represents one particle obtained by SEM observation. Indicates the minimum radius of the circle that contains. The sphericity of 50 particles randomly selected from the image of the particles obtained by SEM observation was determined by the above method, and the average value thereof was defined as the sphericity.

(研磨液の作製)
 得られたスラリを適量採取して、粉砕砥粒の含有量が5質量%、ポリアクリル酸アンモニウム(重量平均分子量:8000)の濃度が0.1質量%となるように、スラリ、ポリアクリル酸アンモニウム及び水を混合して混合液を得た。この混合液を、超音波分散機を用いて分散させて、粉砕砥粒分散液を得た。
(Preparation of polishing liquid)
An appropriate amount of the obtained slurry was sampled, and the slurry and polyacrylic acid were adjusted so that the content of crushed abrasive grains was 5% by mass and the concentration of ammonium polyacrylate (weight average molecular weight: 8000) was 0.1% by mass. Ammonium and water were mixed to obtain a mixed solution. This mixed liquid was dispersed using an ultrasonic disperser to obtain a pulverized abrasive dispersion.

 粉砕砥粒分散液に脱イオン水とプロピオン酸とを加えて、全量が1000g、pHが6.0(25℃)の研磨液(粉砕砥粒の含有量:0.25質量%)を作製した。なお、研磨液に含まれるセリア粒子の平均一次粒子径は50nm、平均二次粒子径は145nmであった。なお、研磨液に含まれるセリア粒子の平均一次粒子径及び平均二次粒子径をそれぞれ、スラリに含まれるセリア粒子の平均一次粒子径及び平均二次粒子径と同様にして求めた。研磨液のpHを、pHメータ(横河電機株式会社製のModel PH81(商品名))で測定した。 Deionized water and propionic acid were added to the pulverized abrasive dispersion to prepare a polishing liquid (content of pulverized abrasive: 0.25% by mass) having a total amount of 1000 g and a pH of 6.0 (25 ° C.). . The ceria particles contained in the polishing liquid had an average primary particle size of 50 nm and an average secondary particle size of 145 nm. The average primary particle size and average secondary particle size of the ceria particles contained in the polishing liquid were determined in the same manner as the average primary particle size and average secondary particle size of the ceria particles contained in the slurry, respectively. The pH of the polishing liquid was measured with a pH meter (Model PH81 (trade name) manufactured by Yokogawa Electric Corporation).

(被研磨膜の研磨)
 研磨試験に用いるウエハとして、パターンが形成されていないブランケットウエハ(Blanket wafer)を用いた。ブランケットウエハとして、シリコン(Si)基板上に、プラズマTEOS法で酸化珪素膜を形成したものと、シリコン(Si)基板上に低圧CVD法で窒化珪素膜を形成したものとを用いた。
(Polishing the film to be polished)
As a wafer used for the polishing test, a blanket wafer on which no pattern was formed was used. As a blanket wafer, a silicon (Si) substrate having a silicon oxide film formed by a plasma TEOS method and a silicon (Si) substrate having a silicon nitride film formed by a low pressure CVD method were used.

 ウエハの研磨を、研磨装置(荏原製作所製のF-REX-300)により行った。研磨装置における基板取り付け用の吸着パッドを貼り付けたホルダーに、ウエハをセットした。研磨装置における直径600mmの研磨定盤に、多孔質ウレタン樹脂製の研磨パッド(溝形状=グルーブタイプ:ダウ・コーニング社製、型番VP3100)を貼り付けた。更に、被研磨膜である絶縁膜(酸化珪素膜又は窒化珪素膜)が上記研磨パッドに対向するように前記ホルダーを研磨定盤上に載せた。加工荷重を210gf/cm(20.6kPa)に設定し、前記研磨パッド上に前記研磨液を250ミリリットル/分の速度で滴下しながら、研磨定盤とウエハとをそれぞれ130回転/分で回転させて、ウエハを研磨した。研磨後、ウエハを、純水で良く洗浄し、乾燥した。光干渉式膜厚測定装置を用いて研磨前後の膜厚を測定して、研磨速度を調べた。結果を表1に示す。 The wafer was polished by a polishing apparatus (F-REX-300 manufactured by Ebara Corporation). The wafer was set in a holder to which a substrate mounting suction pad was attached in a polishing apparatus. A polishing pad made of porous urethane resin (groove shape = groove type: manufactured by Dow Corning, model number VP3100) was attached to a polishing surface plate having a diameter of 600 mm in a polishing apparatus. Further, the holder was placed on a polishing surface plate so that an insulating film (silicon oxide film or silicon nitride film) as a film to be polished was opposed to the polishing pad. The processing load is set to 210 gf / cm 2 (20.6 kPa), and the polishing platen and the wafer are rotated at 130 rpm for each time while the polishing liquid is dropped on the polishing pad at a rate of 250 ml / min. The wafer was polished. After polishing, the wafer was thoroughly washed with pure water and dried. The film thickness before and after polishing was measured using an optical interference type film thickness measuring apparatus to examine the polishing rate. The results are shown in Table 1.

(実施例2,4)
 表1に示す平均一次粒子径及び平均二次粒子径になるまでコロイダルセリアを粉砕するためにビーズミルの処理時間をそれぞれ以下のように変更したこと以外は、実施例1と同様にしてスラリ及び研磨液を作製した。作製した研磨液を用いて、実施例1と同様にして、被研磨膜の研磨を行い、研磨速度を調べた。結果を表1に示す。
 ビーズミルの処理時間
  実施例2:50分間
  実施例4:20分間
(Examples 2 and 4)
Slurry and polishing were carried out in the same manner as in Example 1 except that the processing time of the bead mill was changed as follows to pulverize the colloidal ceria until the average primary particle size and average secondary particle size shown in Table 1 were obtained. A liquid was prepared. Using the prepared polishing liquid, the film to be polished was polished in the same manner as in Example 1, and the polishing rate was examined. The results are shown in Table 1.
Processing time of bead mill Example 2: 50 minutes Example 4: 20 minutes

(実施例3)
 ビーズミルの代わりにジェットミルを用いたこと以外は、実施例1と同様にしてスラリ及び研磨液を作製した。作製した研磨液を用いて、実施例1と同様にして、被研磨膜の研磨を行い、研磨速度を調べた。結果を表1に示す。
(Example 3)
A slurry and a polishing liquid were prepared in the same manner as in Example 1 except that a jet mill was used instead of the bead mill. Using the prepared polishing liquid, the film to be polished was polished in the same manner as in Example 1, and the polishing rate was examined. The results are shown in Table 1.

(比較例1~3)
 コロイダルセリアを粉砕せず、表1に示す平均一次粒子径及び平均二次粒子径を有するコロイダルセリアと水とを含むスラリを作製したこと以外は、実施例1と同様にして研磨液を作製した。作製した研磨液を用いて、実施例1と同様にして、被研磨膜の研磨を行い、研磨速度を調べた。結果を表1に示す。
(Comparative Examples 1 to 3)
A polishing liquid was prepared in the same manner as in Example 1 except that a slurry containing colloidal ceria having the average primary particle size and average secondary particle size shown in Table 1 and water was prepared without pulverizing the colloidal ceria. . Using the prepared polishing liquid, the film to be polished was polished in the same manner as in Example 1, and the polishing rate was examined. The results are shown in Table 1.

Figure JPOXMLDOC01-appb-T000001
Figure JPOXMLDOC01-appb-T000001

 表1から、同程度の平均一次粒子径を有するセリア粒子を含有する研磨液では、コロイダルセリアに粉砕処理を施して得られた研磨液の方が、粉砕処理を施さずに得た研磨液と比べて、研磨速度が高いことがわかる。 From Table 1, in the polishing liquid containing ceria particles having the same average primary particle diameter, the polishing liquid obtained by subjecting colloidal ceria to the grinding treatment is the same as the polishing liquid obtained without performing the grinding treatment. It can be seen that the polishing rate is higher than that.

Claims (8)

 セリア粒子と水とを含有するスラリの製造方法であって、
 水中に分散されたコロイダルセリアを粉砕して、前記セリア粒子を得る粉砕工程を備え、
 前記粉砕工程において、前記コロイダルセリアの平均一次粒子径に対する前記セリア粒子の平均一次粒子径の比が0.8未満となるように粉砕する、スラリの製造方法。
A method for producing a slurry containing ceria particles and water,
Crushing colloidal ceria dispersed in water to provide the ceria particles,
In the pulverizing step, the slurry is pulverized so that a ratio of an average primary particle diameter of the ceria particles to an average primary particle diameter of the colloidal ceria is less than 0.8.
 セリア粒子と水とを含有するスラリの製造方法であって、
 水中に分散されたコロイダルセリアを粉砕して、前記セリア粒子を得る粉砕工程を備え、
 前記粉砕工程において、前記コロイダルセリアの真球度に対する前記セリア粒子の真球度の比が0.97以下となるように粉砕する、スラリの製造方法。
A method for producing a slurry containing ceria particles and water,
Crushing colloidal ceria dispersed in water to provide the ceria particles,
In the pulverizing step, the slurry is pulverized so that a ratio of the sphericity of the ceria particles to the sphericity of the colloidal ceria is 0.97 or less.
 前記粉砕工程において、前記コロイダルセリアはビーズミルを用いて粉砕される、請求項1又は2に記載のスラリの製造方法。 The method for producing a slurry according to claim 1 or 2, wherein in the pulverizing step, the colloidal ceria is pulverized using a bead mill.  前記粉砕工程において、前記コロイダルセリアはジェットミルを用いて粉砕される、請求項1又は2に記載のスラリの製造方法。 The method for producing a slurry according to claim 1 or 2, wherein in the pulverizing step, the colloidal ceria is pulverized using a jet mill.  セリア粒子と水と添加剤とを含有する研磨液の製造方法であって、
 請求項1~4のいずれか一項に記載の製造方法により得られたスラリと、添加剤とを混合して研磨液を得る工程を備える、研磨液の製造方法。
A method for producing a polishing liquid comprising ceria particles, water and an additive,
A method for producing a polishing liquid, comprising the step of mixing the slurry obtained by the production method according to any one of claims 1 to 4 with an additive to obtain a polishing liquid.
 請求項1~4のいずれか一項に記載のスラリの製造方法により得られたスラリ。 A slurry obtained by the slurry production method according to any one of claims 1 to 4.  請求項5に記載の研磨液の製造方法により得られた研磨液。 A polishing liquid obtained by the method for producing a polishing liquid according to claim 5.  請求項7に記載の研磨液を用いて、基板表面に形成された被研磨膜を研磨する研磨工程を備える、基板の研磨方法。 A method for polishing a substrate, comprising a polishing step of polishing a film to be polished formed on the surface of the substrate using the polishing liquid according to claim 7.
PCT/JP2016/085589 2016-11-30 2016-11-30 Slurry, polishing liquid, method for producing said slurry, method for producing said polishing liquid, and method for polishing substrate Ceased WO2018100686A1 (en)

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