CN109437913A - A kind of method that low temperature is synthetically prepared Silicon Carbide Powder - Google Patents

A kind of method that low temperature is synthetically prepared Silicon Carbide Powder Download PDF

Info

Publication number
CN109437913A
CN109437913A CN201811616833.5A CN201811616833A CN109437913A CN 109437913 A CN109437913 A CN 109437913A CN 201811616833 A CN201811616833 A CN 201811616833A CN 109437913 A CN109437913 A CN 109437913A
Authority
CN
China
Prior art keywords
waterglass
silicon carbide
hydrochloric acid
furnace
carbide powder
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
CN201811616833.5A
Other languages
Chinese (zh)
Other versions
CN109437913B (en
Inventor
张宁
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Shenyang University
Original Assignee
Shenyang University
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Shenyang University filed Critical Shenyang University
Priority to CN201811616833.5A priority Critical patent/CN109437913B/en
Publication of CN109437913A publication Critical patent/CN109437913A/en
Application granted granted Critical
Publication of CN109437913B publication Critical patent/CN109437913B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B35/00Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
    • C04B35/515Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on non-oxide ceramics
    • C04B35/56Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on non-oxide ceramics based on carbides or oxycarbides
    • C04B35/565Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on non-oxide ceramics based on carbides or oxycarbides based on silicon carbide
    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B35/00Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
    • C04B35/622Forming processes; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B35/00Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
    • C04B35/622Forming processes; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
    • C04B35/626Preparing or treating the powders individually or as batches ; preparing or treating macroscopic reinforcing agents for ceramic products, e.g. fibres; mechanical aspects section B
    • C04B35/62605Treating the starting powders individually or as mixtures
    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B2235/00Aspects relating to ceramic starting mixtures or sintered ceramic products
    • C04B2235/65Aspects relating to heat treatments of ceramic bodies such as green ceramics or pre-sintered ceramics, e.g. burning, sintering or melting processes
    • C04B2235/656Aspects relating to heat treatments of ceramic bodies such as green ceramics or pre-sintered ceramics, e.g. burning, sintering or melting processes characterised by specific heating conditions during heat treatment
    • C04B2235/6567Treatment time
    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B2235/00Aspects relating to ceramic starting mixtures or sintered ceramic products
    • C04B2235/70Aspects relating to sintered or melt-casted ceramic products
    • C04B2235/95Products characterised by their size, e.g. microceramics

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Ceramic Engineering (AREA)
  • Manufacturing & Machinery (AREA)
  • Materials Engineering (AREA)
  • Structural Engineering (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Carbon And Carbon Compounds (AREA)

Abstract

A kind of method that low temperature is synthetically prepared Silicon Carbide Powder, comprising the following steps: (1) sequentially add waterglass, coupling agent, polyethylene glycol and hydrochloric acid in deionized water, gel is made in stirring;It is filtered after washing and alcohol is washed;(2) it is put into dehydrated alcohol, phenolic resin is added under agitation, stirring forms paste;It dries under the conditions of 65~200 DEG C, is ground after being cooled to;(3) it is put into heating furnace, is passed through argon gas and keeps circulating;It is warming up to 1400~1550 DEG C of progress carbothermic reduction reactions, furnace cooling;(4) it is placed in resistance furnace, heat preservation makes remaining carbon removal under the conditions of 550~650 DEG C, grinds after cooling to room temperature with the furnace.Raw material sources of the present invention are extensive, by modes such as catalytic modifications, silicon source and carbon source made to reach atom or the other uniform mixing of molecular level, to reduce carbothermic reduction reaction temperature, reduce production cost.

Description

A kind of method that low temperature is synthetically prepared Silicon Carbide Powder
Technical field
The invention belongs to field of inorganic nonmetallic material, in particular to a kind of low temperature is synthetically prepared Silicon Carbide Powder Method.
Background technique
Silicon carbide (SiC) ceramics have the excellent properties such as high temperature resistant, corrosion-resistant, high rigidity, high intensity and receive much attention, with The continuous development of high-technology field, thyrite is in high-techs such as refractory material, metallurgy, machinery, chemical industry and military projects Skill field has extensive development prospect;But presently, there are main problem be that the production cost of silicon carbide ceramics is higher, sternly Ghost image rings the commercialization promotion and application of thyrite;For this purpose, there is an urgent need to reduce the production of thyrite Cost.
One of the effective way for reducing thyrite production cost is to reduce raw materials for production (silicon carbide ceramics powder Body) production cost;Currently, the production method that most Silicon Carbide Powder is promoted in commercialization is wet chemistry method and carbon thermal reduction The method combined, existing main problem are that carbothermic reduction reaction temperature is higher, generally at 1550~1650 DEG C or so, are reunited Caking phenomenon is serious, and common silicon source is mainly ethyl orthosilicate, and price is higher;For this purpose, inhibiting to reunite, reducing carbothermic reduction reaction The price of temperature and silicon source is imperative.
Summary of the invention
The object of the present invention is to provide a kind of methods that low temperature is synthetically prepared Silicon Carbide Powder, by selecting raw material to match Process flow is closed, on the basis of low temperature synthesis, high-purity carborundum is prepared, improves production efficiency while reducing cost.
The method of the present invention includes the following steps:
1, it prepares gel: preparing silicon source waterglass, hydrochloric, surfactant coupling agent and polyethylene glycol, wherein The mass concentration of hydrochloric acid is 5~35%;Hydrochloric acid accounts for the percent by volume 1~30% of waterglass, and coupling agent accounts for waterglass and hydrochloric acid The 0.01~10.0% of total volume, polyethylene glycol are the 0.01~10.0% of waterglass and hydrochloric acid gross mass;By waterglass, coupling Agent, polyethylene glycol and hydrochloric acid sequentially add in deionized water, stir evenly and gel is made;By gel after washing and alcohol is washed, mistake Filter obtains aqueous precursor gel;
2, it prepares presoma powder: aqueous precursor gel is put into dehydrated alcohol, phenolic resin is added under agitation, Dissolve phenolic resin in dehydrated alcohol, aqueous precursor gel is dispersed, until whole materials form paste;Paste is set In baking oven, drying removal volatile ingredient, surplus material cool to room temperature with the furnace under the conditions of 65~200 DEG C, take out grinding system At presoma powder;Wherein the molar ratio of phenolic resin and waterglass is 0.5~10;
3, it synthesizes: presoma powder being put into heating furnace, argon gas is passed through into heating furnace and drives away air, and keeps argon Air-flow is logical;Then heating furnace is warming up to 1400~1550 DEG C, keeps the temperature 2~5 hours, carry out carbothermic reduction reaction, reaction is completed After cool to room temperature with the furnace, obtain coarse dispersion;
4, decarburization: coarse dispersion is placed in resistance furnace, is kept the temperature 2~8 hours under the conditions of 550~650 DEG C, is made remaining carbon Removal, the material after reaction cools to room temperature with the furnace, then grinds and Silicon Carbide Powder is made.
The degree of polymerization of above-mentioned polyethylene glycol is 2000~20000.
In above-mentioned step 1, after the dosage of deionized water is with deionized water and mixed in hydrochloric acid, waterglass, idol are all dissolved Join subject to agent and polyethylene glycol.
In above-mentioned step 2, the dosage of dehydrated alcohol, which is subject to, dissolves whole phenolic resin.
The partial size of above-mentioned Silicon Carbide Powder is 200~1000 nanometers.
The silicon source that the present invention uses is waterglass cheap, from a wealth of sources, instead of ethyl orthosilicate on the high side, Carbon source phenolic resin higher using phosphorus content, cheap;Due to waterglass and phenolic resin objectionable intermingling, lean on completely Mechanical mixture, be difficult to make to reach between waterglass and phenolic resin atom or molecular level it is other it is uniform mix, therefore pass through hydrochloric acid Catalytic action promote waterglass to hydrolyze, in combination with the grafting of coupling agent and polyethylene glycol, surface is modified makees with dispersion With making that colloidal particles obtain dispersion and surface is modified, even if silicon source and carbon source can be compatible, and reach atom or molecular level is other Uniformly mixing reduces production cost to reduce carbothermic reduction reaction temperature.
Detailed description of the invention
Fig. 1 is the X-ray diffractogram of the Silicon Carbide Powder in the embodiment of the present invention 1;
Fig. 2 is the SEM photograph figure of the Silicon Carbide Powder in the embodiment of the present invention 1.
Specific embodiment
Waterglass, coupling agent, polyethylene glycol and the phenolic resin used in the embodiment of the present invention is commercial products.
X-ray diffractometer model PW3040/60 is used in the embodiment of the present invention.
Scanning electron microscope model SSX-550 is used in the embodiment of the present invention.
In the embodiment of the present invention, it is that gel is first placed in water to stirring at least 5min that washing and alcohol, which are washed, then takes out and is placed in At least 5min is stirred in ethyl alcohol.
In the embodiment of the present invention, the time dried under the conditions of 65~200 DEG C is 2~24 hours.
Coupling agent selects KH-550, KH-560 or KH-570 in the embodiment of the present invention.
Phenolic resin selects FQ-9 in the embodiment of the present invention.
Embodiment 1
Prepare silicon source waterglass, hydrochloric, surfactant coupling agent and polyethylene glycol, wherein the quality of hydrochloric acid is dense Degree is 35%;Hydrochloric acid accounts for the percent by volume 1% of waterglass, and coupling agent accounts for the 0.01% of waterglass and hydrochloric acid total volume, poly- second Glycol is the 0.01% of waterglass and hydrochloric acid gross mass;Waterglass, coupling agent, polyethylene glycol and hydrochloric acid are sequentially added into deionization In water, stirs evenly and gel is made;By gel after washing and alcohol is washed, the solid phase of acquisition is filtered as aqueous precursor gel;Wherein The degree of polymerization of polyethylene glycol is 2000;After the dosage of deionized water is with deionized water and mixed in hydrochloric acid, waterglass, idol are all dissolved Join subject to agent and polyethylene glycol;
Aqueous precursor gel is put into dehydrated alcohol, phenolic resin is added under agitation, makes phenolic resin anhydrous It is dissolved in ethyl alcohol, aqueous precursor gel is dispersed, until whole materials form paste;Paste is placed in baking oven, at 65 DEG C Under the conditions of drying removal volatile ingredient, surplus material cools to room temperature with the furnace, takes out grinding and presoma powder is made;Dehydrated alcohol Dosage be subject to by whole phenolic resin dissolve;The molar ratio of phenolic resin and waterglass is 2;
Presoma powder is put into heating furnace, argon gas is passed through into heating furnace and drives away air, and argon gas is kept to circulate; Then heating furnace is warming up to 1400 DEG C, keeps the temperature 5 hours, carried out carbothermic reduction reaction, cool to room temperature with the furnace after the reaction was completed, Obtain coarse dispersion;
Coarse dispersion is placed in resistance furnace, 8 hours is kept the temperature under the conditions of 550 DEG C, makes remaining carbon removal, the object after reaction Material cools to room temperature with the furnace, then grinds and Silicon Carbide Powder is made, and 100~350 nanometers of partial size, X-ray diffraction result such as Fig. 1 Shown, product does not have apparent impurity as seen from the figure, and silicon carbide powder SEM photograph is as shown in Figure 2.
Embodiment 2
With embodiment 1, difference is method:
(1) mass concentration of hydrochloric acid is 25%;Hydrochloric acid accounts for the percent by volume 10% of waterglass, coupling agent account for waterglass and The 1% of hydrochloric acid total volume, polyethylene glycol are the 1% of waterglass and hydrochloric acid gross mass;The degree of polymerization of polyethylene glycol is 4000;
(2) molar ratio of phenolic resin and waterglass is 5, and paste dries removal volatile ingredient under the conditions of 80 DEG C;
(3) heating furnace is warming up to 1450 DEG C and keeps the temperature 4 hours, carry out carbothermic reduction reaction;
(4) coarse dispersion keeps the temperature 6 hours under the conditions of 600 DEG C, makes remaining carbon removal, the material after reaction cools to the furnace Room temperature, then grind and Silicon Carbide Powder is made, 200~450 nanometers of partial size.
Embodiment 3
With embodiment 1, difference is method:
(1) mass concentration of hydrochloric acid is 15%;Hydrochloric acid accounts for the percent by volume 20% of waterglass, coupling agent account for waterglass and The 5% of hydrochloric acid total volume, polyethylene glycol are the 10% of waterglass and hydrochloric acid gross mass;The degree of polymerization of polyethylene glycol is 6000;
(2) molar ratio of phenolic resin and waterglass is 8, and paste dries removal volatile ingredient under the conditions of 120 DEG C;
(3) heating furnace is warming up to 1500 DEG C and keeps the temperature 3 hours, carry out carbothermic reduction reaction;
(4) coarse dispersion keeps the temperature 4 hours under the conditions of 620 DEG C, makes remaining carbon removal, the material after reaction cools to the furnace Room temperature, then grind and Silicon Carbide Powder is made, 300~700 nanometers of partial size.
Embodiment 4
With embodiment 1, difference is method:
(1) mass concentration of hydrochloric acid is 5%;Hydrochloric acid accounts for the percent by volume 30% of waterglass, coupling agent account for waterglass and The 10.0% of hydrochloric acid total volume, polyethylene glycol are the 5% of waterglass and hydrochloric acid gross mass;The degree of polymerization of polyethylene glycol is 20000;
(2) molar ratio of phenolic resin and waterglass is 10, and paste dries removal volatile ingredient under the conditions of 200 DEG C;
(3) heating furnace is warming up to 1550 DEG C and keeps the temperature 2 hours, carry out carbothermic reduction reaction;
(4) coarse dispersion keeps the temperature 2 hours under the conditions of 650 DEG C, makes remaining carbon removal, the material after reaction cools to the furnace Room temperature, then grind and Silicon Carbide Powder is made, 350~850 nanometers of partial size.

Claims (5)

1. a kind of method that low temperature is synthetically prepared Silicon Carbide Powder, it is characterised in that the following steps are included:
(1) it prepares gel: preparing silicon source waterglass, hydrochloric, surfactant coupling agent and polyethylene glycol, wherein hydrochloric acid Mass concentration be 5~35%;Hydrochloric acid accounts for the percent by volume 1~30% of waterglass, and coupling agent accounts for waterglass and hydrochloric acid is overall Long-pending 0.01~10.0%, polyethylene glycol are the 0.01~10.0% of waterglass and hydrochloric acid gross mass;By waterglass, coupling agent, Polyethylene glycol and hydrochloric acid sequentially add in deionized water, stir evenly and gel is made;By gel after washing and alcohol is washed, filtering is obtained Obtain aqueous precursor gel;
(2) it prepares presoma powder: aqueous precursor gel is put into dehydrated alcohol, phenolic resin is added under agitation, make Phenolic resin dissolves in dehydrated alcohol, and aqueous precursor gel is dispersed, until whole materials form paste;Paste is placed in In baking oven, drying removal volatile ingredient, surplus material cool to room temperature with the furnace under the conditions of 65~200 DEG C, take out grinding and are made Presoma powder;Wherein the molar ratio of phenolic resin and waterglass is 0.5~10;
(3) it synthesizes: presoma powder being put into heating furnace, argon gas is passed through into heating furnace and drives away air, and keeps argon gas Circulation;Then heating furnace is warming up to 1400~1550 DEG C, keeps the temperature 2~5 hours, carry out carbothermic reduction reaction, after the reaction was completed It cools to room temperature with the furnace, obtains coarse dispersion;
(4) decarburization: coarse dispersion is placed in resistance furnace, is kept the temperature 2~8 hours under the conditions of 550~650 DEG C, is removed remaining carbon It removes, the material after reaction cools to room temperature with the furnace, then grinds and Silicon Carbide Powder is made.
2. the method that a kind of low temperature according to claim 1 is synthetically prepared Silicon Carbide Powder, it is characterised in that described Polyethylene glycol the degree of polymerization be 2000~20000.
3. the method that a kind of low temperature according to claim 1 is synthetically prepared Silicon Carbide Powder, it is characterised in that step (1) in, after the dosage of deionized water is with deionized water and mixed in hydrochloric acid, all dissolving waterglass, coupling agent and polyethylene glycol is It is quasi-.
4. the method that a kind of low temperature according to claim 1 is synthetically prepared Silicon Carbide Powder, it is characterised in that step (2) in, the dosage of dehydrated alcohol, which is subject to, dissolves whole phenolic resin.
5. the method that a kind of low temperature according to claim 1 is synthetically prepared Silicon Carbide Powder, it is characterised in that described Silicon Carbide Powder partial size be 200~1000 nanometers.
CN201811616833.5A 2018-12-27 2018-12-27 Method for preparing silicon carbide ceramic powder by low-temperature synthesis Active CN109437913B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201811616833.5A CN109437913B (en) 2018-12-27 2018-12-27 Method for preparing silicon carbide ceramic powder by low-temperature synthesis

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201811616833.5A CN109437913B (en) 2018-12-27 2018-12-27 Method for preparing silicon carbide ceramic powder by low-temperature synthesis

Publications (2)

Publication Number Publication Date
CN109437913A true CN109437913A (en) 2019-03-08
CN109437913B CN109437913B (en) 2021-08-24

Family

ID=65538477

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201811616833.5A Active CN109437913B (en) 2018-12-27 2018-12-27 Method for preparing silicon carbide ceramic powder by low-temperature synthesis

Country Status (1)

Country Link
CN (1) CN109437913B (en)

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS56140079A (en) * 1980-03-28 1981-11-02 Nippon Steel Corp Indefinite form refractory composition for vibration molding
CN101786622A (en) * 2010-01-20 2010-07-28 中国科学院山西煤炭化学研究所 Preparation method of silicon carbide nano-wire
CN101804981A (en) * 2010-04-01 2010-08-18 中国科学院山西煤炭化学研究所 Method for preparing hollow silicon carbide nano material
CN102432013A (en) * 2011-10-08 2012-05-02 中国科学院山西煤炭化学研究所 Preparation method of beta-nano-SiC
CN107963631A (en) * 2017-12-12 2018-04-27 宁波爱克创威新材料科技有限公司 Nanometer silicon carbide and preparation method thereof
CN108314050A (en) * 2018-03-12 2018-07-24 鲁东大学 A kind of preparation method of the nanometer silicon carbide particle of efficient absorption organic dyestuff

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS56140079A (en) * 1980-03-28 1981-11-02 Nippon Steel Corp Indefinite form refractory composition for vibration molding
CN101786622A (en) * 2010-01-20 2010-07-28 中国科学院山西煤炭化学研究所 Preparation method of silicon carbide nano-wire
CN101804981A (en) * 2010-04-01 2010-08-18 中国科学院山西煤炭化学研究所 Method for preparing hollow silicon carbide nano material
CN102432013A (en) * 2011-10-08 2012-05-02 中国科学院山西煤炭化学研究所 Preparation method of beta-nano-SiC
CN107963631A (en) * 2017-12-12 2018-04-27 宁波爱克创威新材料科技有限公司 Nanometer silicon carbide and preparation method thereof
CN108314050A (en) * 2018-03-12 2018-07-24 鲁东大学 A kind of preparation method of the nanometer silicon carbide particle of efficient absorption organic dyestuff

Also Published As

Publication number Publication date
CN109437913B (en) 2021-08-24

Similar Documents

Publication Publication Date Title
CN108840683B (en) Process for preparing zirconium nitride ceramic microspheres and zirconium nitride ceramic microspheres
CN110421113A (en) A kind of ceramsite sand prepared by regenerating used waste and the precoated sand prepared by the ceramsite sand
CN103359736A (en) Method for purifying and preparing silicon carbide powder from crystalline silicon cutting waste mortar
CN1834016A (en) Process for producing fine alpha-alumina particles
CN106006584A (en) Preparation method of hexagonal boron nitride powder
CN103754891A (en) Method for preparing hafnium boride powder by using boron/carbothermic method
CN106540733A (en) A kind of method for preparing graphite phase carbon nitride material
CN103011869B (en) High-abrasion-resistance refractory liner material and preparation method thereof
CN104556073A (en) Process for purifying inorganic nonmetallic minerals
CN1174171A (en) Magnesium hydroxide and method of preparing water suspension
CN103864048A (en) Method for preparing large high-power carbon electrode by using semi-graphitized anthracite
CN109437913A (en) A kind of method that low temperature is synthetically prepared Silicon Carbide Powder
CN102491779A (en) Method for improving poriness of alumina ceramic mold core
CN109437921A (en) The method for being synthetically prepared silicon nitride ceramics powder based on the modified low temperature in surface
CN103086704A (en) Preparation method of high-porosity mineral-based ceramic membrane support
CN102153144A (en) Method for preparing calcium ferroaluminates
JP2010013293A (en) Method for producing aluminum titanate-based ceramic powder
CN1159226C (en) Process for preparing rare-earth nano oxide by ball grinding and solid-phase chemical reaction
CN112299408A (en) Diamond tool preparation method based on warm compaction forming
CN102275919A (en) Preparation method of superfine niobium carbide powder
CN102268581B (en) Preparation method of superfine tantalum-niobium carbide solid solution powder
CN102489218A (en) Method for granulating and forming silicon carbide fine powder and silicon carbide granule
CN101565491B (en) Thermoplastic liquid phenolic resin and preparation method thereof
CN109502563A (en) A kind of method that low temperature is synthetically prepared silicon nitride ceramics powder
CN108147777A (en) It is a kind of to be pressed into method with heating tube using recycling synthesizing cubic boron nitride solid waste and prepare superelevation

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant