CN108033476A - A kind of preparation method of nano-calcium carbonate - Google Patents

A kind of preparation method of nano-calcium carbonate Download PDF

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Publication number
CN108033476A
CN108033476A CN201810121235.4A CN201810121235A CN108033476A CN 108033476 A CN108033476 A CN 108033476A CN 201810121235 A CN201810121235 A CN 201810121235A CN 108033476 A CN108033476 A CN 108033476A
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calcium carbonate
nano
sweep
preparation
agitating paddle
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骆培成
丁莉
赵川川
邬斌
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Southeast University
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Southeast University
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    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01FCOMPOUNDS OF THE METALS BERYLLIUM, MAGNESIUM, ALUMINIUM, CALCIUM, STRONTIUM, BARIUM, RADIUM, THORIUM, OR OF THE RARE-EARTH METALS
    • C01F11/00Compounds of calcium, strontium, or barium
    • C01F11/18Carbonates
    • C01F11/181Preparation of calcium carbonate by carbonation of aqueous solutions and characterised by control of the carbonation conditions
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/0053Details of the reactor
    • B01J19/0066Stirrers
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/18Stationary reactors having moving elements inside
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B82NANOTECHNOLOGY
    • B82YSPECIFIC USES OR APPLICATIONS OF NANOSTRUCTURES; MEASUREMENT OR ANALYSIS OF NANOSTRUCTURES; MANUFACTURE OR TREATMENT OF NANOSTRUCTURES
    • B82Y30/00Nanotechnology for materials or surface science, e.g. nanocomposites
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01FCOMPOUNDS OF THE METALS BERYLLIUM, MAGNESIUM, ALUMINIUM, CALCIUM, STRONTIUM, BARIUM, RADIUM, THORIUM, OR OF THE RARE-EARTH METALS
    • C01F11/00Compounds of calcium, strontium, or barium
    • C01F11/18Carbonates
    • C01F11/182Preparation of calcium carbonate by carbonation of aqueous solutions and characterised by an additive other than CaCO3-seeds
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01FCOMPOUNDS OF THE METALS BERYLLIUM, MAGNESIUM, ALUMINIUM, CALCIUM, STRONTIUM, BARIUM, RADIUM, THORIUM, OR OF THE RARE-EARTH METALS
    • C01F11/00Compounds of calcium, strontium, or barium
    • C01F11/18Carbonates
    • C01F11/182Preparation of calcium carbonate by carbonation of aqueous solutions and characterised by an additive other than CaCO3-seeds
    • C01F11/183Preparation of calcium carbonate by carbonation of aqueous solutions and characterised by an additive other than CaCO3-seeds the additive being an organic compound

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Geology (AREA)
  • Inorganic Chemistry (AREA)
  • Nanotechnology (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Physics & Mathematics (AREA)
  • Health & Medical Sciences (AREA)
  • Composite Materials (AREA)
  • Condensed Matter Physics & Semiconductors (AREA)
  • General Physics & Mathematics (AREA)
  • Materials Engineering (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • General Health & Medical Sciences (AREA)
  • Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)

Abstract

The present invention provides a kind of preparation method of the nano-calcium carbonate using the self-priming agitating paddle in sweep short blade surface.This method prepares nano-calcium carbonate using the self-priming agitating paddle in sweep short blade surface, in the presence of dispersant, by calcium hydroxide slurry and carbon dioxide gas precursor reactant.Using the pH value of pH measuring probes (8) the measurement reaction solution of installation in stirred autoclave (1), when pH value is less than 8, stirring motor (4) and CO are closed2Intake valve (6), stops reaction.Slurries after the completion of reaction are discharged by blow-off valve (9), reaction solution obtains nano-calcium carbonate powder-product by centrifuging, wash, after drying.Nano-calcium carbonate prepared by the method according to the invention is relative to the nano-calcium carbonate obtained in the prior art, and evenly, particle disperses more preferably for particle diameter smaller, particle diameter distribution, in addition, carbonization time greatly shortens.

Description

A kind of preparation method of nano-calcium carbonate
Technical field
The present invention relates to one kind to use the self-priming agitating paddle in sweep short blade surface, anti-by carrying out being carbonized in stirred tank The method that nano-calcium carbonate should be prepared.
Background technology
The increase of Carbon Dioxide in Air gas content causes Global Temperature to raise, and environment is continuous worsening.However, research table Dependence of person of good sense's class to fuel such as kerosene will cause continuing to increase for carbon dioxide gas content in air.Reduce two in air Carbon oxide gas content has become the much-talked-about topic of global concern.Reduce the method master of the content of Carbon Dioxide in Air gas To include chemical absorption method, Physical Absorption method, membrane filter method and absorption method etc..Pass through gas-liquid preparation of nanometer calcium carbonate by carbonization Method is then that a kind of method of Carbon Dioxide in Air gas is utilized by chemical absorption method.
Nano-calcium carbonate is to grow up the 1980s, and particle diameter is less than a kind of Novel super-thin solid of 100nm Powder particle.Since nano-calcium carbonate compared with other nano-particles has the properties of many uniquenesses such as thermal conductivity, lubricity, anti-oxidant Property, dissolving and decomposition temperature is higher and heat endurance is high, so nano-calcium carbonate is in rubber, plastics, papermaking, coating, ink It is all very extensive Deng field application.
Chinese invention patent CN 1442363A disclose the side that a kind of supergravity reactor prepares microwhisker like calcium carbonate Method.This method is in the presence of chemical additives, using calcium hydroxide and carbon dioxide as raw material, utilizes supergravity reactor height Speed rotates the much bigger gravity environment of the ratio terrestrial gravitation produced, and carburizing reagent is effectively controlled on molecular scale and was crystallized Journey, is made the crystal whisker-shaped calcium carbonate that particle diameter is small, is evenly distributed.But reaction unit design is complicated, equipment investment is big, energy consumption Height, hardly possible cleaning is unfavorable to follow-up continuous production, and production cost will be improved for industrial production.
Chinese invention patent CN 101967310A disclose one kind in membrane reactor prepare with low viscosity and it is medium touch Become the method for performance nano-calcium carbonate.This method calcined lime stone, digest after obtained calcium hydroxide slurry be put into film In scattered carbonization reactor, under the conditions of existing for chemical additives, it is passed through carbon dioxide and carries out reaction preparation with low Viscosity and medium thixotropic property nano-calcium carbonate.The nano-calcium carbonate particle diameter that this method is prepared is small and particle diameter distribution is uniform.But It is to prepare nano-calcium carbonate using the reactor there is the problem of of high cost, equipment easily blocks, and industrialized production is difficult.
Chinese invention patent CN 104556184A disclose a kind of production method of industrial sedimentation type nano-calcium carbonate.Should The calcium hydroxide suspension of preparation is added in autoclave by method, then passes to carbon dioxide, controls titanium dioxide Carbon flow is certain value, prepares that particle diameter distribution is relatively narrow and stable quality by way of high pressure self-priming, the higher nanometer of purity Calcium carbonate granule.But since this method self-priming speed is slower, longer the time required to reaction, production efficiency is relatively low, thus it is uncomfortable Preferably it is applied to industrial production.
The purpose of the present invention is utilize the self-priming stirring in sweep short blade surface in Chinese patent (CN 103768980A) Paddle is stirred to increase mass transfer rate, under the action of dispersant, is made calcium hydroxide slurry and carbon dioxide gas precursor reactant, is obtained It is small to obtain particle diameter, the relatively narrow and well dispersed nano-calcium carbonate of particle diameter distribution.
The content of the invention
Technical problem:The object of the present invention is to provide a kind of preparation method of nano-calcium carbonate.It is mainly used for solving existing Nano-calcium carbonate preparation process present in reaction speed is slow, energy consumption is big, particle diameter is big, particle diameter distribution is uneven, particle coagulation The problems such as serious.Compared with prior art, it is stirred using the self-priming agitating paddle in sweep short blade surface and adds mass transfer speed Rate, the nano-calcium carbonate particle diameter prepared is small, and particle diameter distribution is relatively narrow and well dispersed, and in addition, the reaction time is shorter.
Technical solution:A kind of preparation method of nano-calcium carbonate of the present invention utilizes the self-priming stirring in sweep short blade surface Paddle prepares nano-calcium carbonate, in the presence of dispersant, by calcium hydroxide slurry and carbon dioxide gas precursor reactant, its specific steps For:
1) calcium hydroxide slurry configured is added in stirred autoclave, in stirred tank equipped with sweep short blade surface certainly Reacting slurry, by the constant temperature circulating medium in chuck, is heated or cooled to the temperature of setting by suction agitating paddle, then will be disperseed Agent adds stirred autoclave, opens stirring motor, after the dispersant in reacting slurry is uniformly dispersed, closes stirring motor;
2) inert gas breather valve is opened, it is P that inert gas to pressure is passed through into stirred autoclave1Afterwards, inertia is closed Gas ventilation valve, while open CO2Intake valve, adjusts constant pressure regulating valve, gas reactor stagnation pressure P is maintained at steady state value;
3) stirring motor is opened, and by the rotating speed of the rotational speed regulation of the self-priming agitating paddle in sweep short blade surface to agitating paddle N, at this time in kettle ullage inert gas and CO2Mixed gas is automatically drawn under liquid level, forms substantial amounts of minute bubbles distribution In reaction paste, the pH value of reaction solution is measured using the pH measuring probes installed in stirred autoclave, when pH value is less than 8, Close stirring motor and CO2Intake valve, stops reaction;
4) slurries after the completion of reaction are discharged by blow-off valve, reaction solution obtains nanometer by centrifuging, wash, after drying Calcium carbonate powder product.
Wherein:
The used self-priming agitating paddle in sweep short blade surface includes fixed disk, sweep, terminal pad and short blade, fixed Disk, sweep, terminal pad and short blade, wherein, the top of connection sweep below fixed disk, the lower part connection terminal pad of sweep, Short blade is connected below terminal pad.
The temperature control set in the step 1) is 0 DEG C to 60 DEG C.
The temperature of the setting is preferably 15 DEG C to 45 DEG C.
Calcium hydroxide slurry mass concentration described in the step 1) is 0.01wt% to 20wt%.
The calcium hydroxide slurry mass concentration is preferably 2wt% to 10wt%.
The dispersant of addition is sucrose, sulfuric acid, nitric acid, phosphoric acid or their mixture in the step 1), its addition For the 0.01wt% to 5wt% of reactant gross mass.Preferably 1wt% to 2wt%.
Inert gas in the step 2) is and CO2And Ca (OH)2The nonreactive gas of slurry.Preferably air Or nitrogen.
Inert gas to the pressure that is passed through is P1With gas reactor stagnation pressure P, the CO of expression2Gaseous phase volume divide rate (1- P1/ P) scope be not less than 0.1%.Preferred scope is 5%-40%.
The condition that the rotating speed N of agitating paddle described in the step 3) should meet is:N × D is more than 10, and wherein D is sweep (11) the corresponding diameter of a circle of inswept 1 circle of extension.Preferably N × D is more than 20.
Beneficial effect:Due to the use of the self-priming agitating paddle in sweep short blade surface in the present invention, pass through the agitating paddle Stirring action mass transfer enhancement process, shortens the carburizing reagent time, and production efficiency improves, the grain diameter smaller produced, It is more evenly distributed, disperses more preferable
Brief description of the drawings
Fig. 1 is the carbonizing plant schematic diagram that the present invention prepares nano-calcium carbonate;
Fig. 2 is the structure diagram of the self-priming agitating paddle in sweep short blade surface of the present invention;
Fig. 3 is the grain size distribution of nano-calcium carbonate prepared by embodiment 1;
Fig. 4 is the grain size distribution of nano-calcium carbonate prepared by embodiment 2.
Have in figure:Stirred autoclave 1, self-priming agitating paddle 2, chuck 3, stirring motor 4, inert gas breather valve 5, CO2 Intake valve 6, constant pressure regulating valve 7, pH measuring probes 8, blow-off valve 9, fixed disk 10, sweep 11, terminal pad 12, short blade 13.
Embodiment
The present invention is a kind of method for preparing nano-calcium carbonate using the self-priming agitating paddle in sweep short blade surface, will be configured Good calcium hydroxide slurry is added in stirred autoclave 1, and the self-priming agitating paddle 2 in sweep short blade surface is housed in stirred tank, is led to The constant temperature circulating medium in chuck 3 is crossed, reacting slurry is heated or cooled, then dispersant is added in stirred autoclave, Stirring motor 4 is opened, after reacting slurry dispersant is uniformly dispersed, closes stirring motor 4.Inert gas breather valve 5 is opened, to Inert gas is passed through in stirred autoclave 1 to P1Afterwards, inert gas breather valve 5 is closed, while opens CO2Intake valve 6, is adjusted permanent Regulating valve 7 is pressed, gas reactor stagnation pressure is maintained at certain pressure P.Stirring motor 4 is opened, and by sweep short blade surface self-priming The rotational speed regulation of formula agitating paddle 2 to certain rotating speed, at this time in kettle ullage inert gas and CO2Mixed gas is automatically drawn into Under liquid level, form substantial amounts of minute bubbles and be distributed in reaction paste.Surveyed using the pH measuring probes 8 of installation in stirred autoclave 1 The pH value of quantitative response liquid, when pH value is less than 8, closes stirring motor 4 and CO2Intake valve 6, stops reaction.After the completion of reacting Slurries discharged by blow-off valve 9, reaction solution by centrifuging, wash, it is dry after obtain nano-calcium carbonate powder-product.According to this Nano-calcium carbonate prepared by the method for invention is relative to the nano-calcium carbonate obtained in the prior art, particle diameter smaller, particle diameter point Evenly, particle disperses more preferably cloth, in addition, carbonization time greatly shortens.
Embodiment 1:
The calcium hydroxide slurry 8L that the concentration configured is 6wt% is added into a high 300mm, the stirring of diameter 200mm In reaction kettle 1, the self-priming agitating paddle 2 in sweep short blade surface is housed in stirred tank.The sweep horizontal cross-section of the agitating paddle for 4 × The rectangle of 2mm, is highly 200mm;The length of short blade and high respectively 20mm and 15mm, thickness 1mm.By in chuck 3 Constant temperature circulating medium, reacting slurry is heated to 40 DEG C, then the dispersant of 0.2wt% is added into stirred autoclave, unlatching is stirred Motor 4 is mixed, after reacting slurry dispersant is uniformly dispersed, closes stirring motor 4.Inert gas breather valve 5 is opened, it is anti-to stirring Answer and inert gas is passed through in kettle 1 to after 0.2MPa, close inert gas breather valve 5, while open CO2Intake valve 6, adjusts constant pressure Regulating valve 7, makes gas reactor stagnation pressure be maintained at 0.5MPa.Stirring motor 4 is opened, and by the self-priming stirring in sweep short blade surface The rotational speed regulation of paddle 2 to 240rpm, at this time in kettle ullage inert gas and CO2Mixed gas is automatically drawn under liquid level, Substantial amounts of minute bubbles are formed to be distributed in reaction paste.Reaction solution is measured using the pH measuring probes 8 of installation in stirred autoclave 1 PH value, when pH value is less than 8, close stirring motor 4 and CO2Intake valve 6, stops reaction.Slurries after the completion of reaction are led to Cross blow-off valve 9 to discharge, reaction solution obtains nano-calcium carbonate powder-product by centrifugation, freeze-drying.Transmission electricity is carried out to product Mirror is tested and counts grain diameter, and the statistical result of particle diameter distribution is shown in Fig. 3.
Embodiment 2:
The calcium hydroxide slurry 30L that the concentration configured is 7wt% is added into a high 1200mm, diameter 800mm's stirs Mix in reaction kettle 1, the self-priming agitating paddle 2 in sweep short blade surface is housed in stirred tank.The sweep horizontal cross-section of the agitating paddle is The rectangle of 16 × 8mm, is highly 850mm;The length of short blade and high respectively 80mm and 60mm, thickness 3mm.Pass through chuck Constant temperature circulating medium in 3,10 DEG C are cooled to by reacting slurry, then the dispersant of 1wt% is added stirred autoclave, and unlatching is stirred Motor 4 is mixed, after reacting slurry dispersant is uniformly dispersed, closes stirring motor 4.Inert gas breather valve 5 is opened, it is anti-to stirring Answer and inert gas is passed through in kettle 1 to after 0.2MPa, close inert gas breather valve 5, while open CO2Intake valve 6, adjusts constant pressure Regulating valve 7, makes gas reactor stagnation pressure be maintained at 0.3MPa.Stirring motor 4 is opened, and by the self-priming stirring in sweep short blade surface The rotational speed regulation of paddle 2 to 100rpm, at this time in kettle ullage inert gas and CO2Mixed gas is automatically drawn under liquid level, Substantial amounts of minute bubbles are formed to be distributed in reaction paste.Reaction solution is measured using the pH measuring probes 8 of installation in stirred autoclave 1 PH value, when pH value is less than 8, close stirring motor 4 and CO2Intake valve 6, stops reaction.Slurries after the completion of reaction are led to Cross blow-off valve 9 to discharge, reaction solution is by centrifugation, the nano-calcium carbonate powder-product being dried to obtain.Transmission electron microscope is carried out to product Test and count grain diameter, the statistical result of particle diameter distribution is shown in Fig. 4.

Claims (10)

1. a kind of preparation method of nano-calcium carbonate, it is characterised in that this method utilizes the self-priming agitating paddle in sweep short blade surface Nano-calcium carbonate is prepared, in the presence of dispersant, by calcium hydroxide slurry and carbon dioxide gas precursor reactant, its specific steps For:
1) calcium hydroxide slurry configured is added in stirred autoclave (1), in stirred tank equipped with sweep short blade surface certainly Reacting slurry, by the constant temperature circulating medium in chuck (3), is heated or cooled to the temperature of setting by suction agitating paddle (2), then Dispersant is added into stirred autoclave, opens stirring motor (4), after the dispersant in reacting slurry is uniformly dispersed, closing is stirred Mix motor (4);
2) inert gas breather valve (5) is opened, is P to inert gas to pressure is passed through in stirred autoclave (1)1Afterwards, inertia is closed Gas ventilation valve (5), while open CO2Intake valve (6), adjusts constant pressure regulating valve (7), gas reactor stagnation pressure P is maintained at permanent Definite value;
3) stirring motor (4) is opened, and the rotational speed regulation of the self-priming agitating paddle in sweep short blade surface (2) to agitating paddle is turned Fast N, at this time in kettle ullage inert gas and CO2Mixed gas is automatically drawn under liquid level, forms substantial amounts of minute bubbles point It is distributed in reaction paste, using the pH value of pH measuring probes (8) the measurement reaction solution of installation in stirred autoclave (1), works as pH value During less than 8, stirring motor (4) and CO are closed2Intake valve (6), stops reaction;
4) slurries after the completion of reaction are discharged by blow-off valve (9), reaction solution obtains nanometer by centrifuging, wash, after drying Calcium carbonate powder product.
A kind of 2. preparation method of nano-calcium carbonate according to claim 1, it is characterised in that:The used short leaf of sweep The self-priming agitating paddle in piece surface (2) includes fixed disk (10), sweep (11), terminal pad (12) and short blade (13), fixed disk (10), sweep (11), terminal pad (12) and short blade (13), wherein, the top of connection sweep (11) below fixed disk (10), The lower part of sweep (11) connects terminal pad (12), and short blade (13) is connected below terminal pad (12).
A kind of 3. preparation method of nano-calcium carbonate according to claim 1, it is characterised in that:Setting in the step 1) Fixed temperature control is 0 DEG C to 60 DEG C.
A kind of 4. preparation method of nano-calcium carbonate according to claim 3, it is characterised in that:The temperature of the setting Preferably 15 DEG C to 45 DEG C.
A kind of 5. preparation method of nano-calcium carbonate according to claim 1, it is characterised in that:Described in the step 1) Calcium hydroxide slurry mass concentration be 0.01wt% to 20wt%.
A kind of 6. preparation method of nano-calcium carbonate according to claim 5, it is characterised in that:The calcium hydroxide slurry Liquid mass concentration is preferably 2wt% to 10wt%.
A kind of 7. preparation method of nano-calcium carbonate according to claim 1, it is characterised in that:Addition in the step 1) Dispersant be sucrose, sulfuric acid, nitric acid, phosphoric acid or their mixture, its addition is the 0.01wt% of reactant gross mass To 5wt%.
A kind of 8. preparation method of nano-calcium carbonate according to claim 1, it is characterised in that:It is lazy in the step 2) Property gas is and CO2And Ca (OH)2The nonreactive gas of slurry.
A kind of 9. preparation method of nano-calcium carbonate according to claim 1, it is characterised in that:Described is passed through indifferent gas Body to pressure is P1With gas reactor stagnation pressure P, the CO of expression2Gaseous phase volume divide rate (1-P1/ P) scope be not less than 0.1%.
A kind of 10. preparation method of nano-calcium carbonate according to claim 1, it is characterised in that:Institute in the step 3) The condition that stating the rotating speed N of agitating paddle should meet is:N × D is more than 10, and wherein D is the corresponding circle of inswept 1 circle of sweep (11) extension Diameter.
CN201810121235.4A 2018-02-07 2018-02-07 A kind of preparation method of nano-calcium carbonate Pending CN108033476A (en)

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110183126A (en) * 2019-06-06 2019-08-30 长沙紫宸科技开发有限公司 A method of carbonate cementitious material is prepared by raw material of lime stone
CN111606344A (en) * 2020-04-28 2020-09-01 广西夏阳环保科技有限公司 Method for preparing nano calcium carbonate with high specific surface area
CN112023871A (en) * 2020-08-28 2020-12-04 安徽同益净化科技有限公司 CO (carbon monoxide)2Method for preparing nano calcite VOCs adsorbent by diffusion method
CN113877500A (en) * 2021-10-09 2022-01-04 江西华明纳米碳酸钙有限公司 Stirring formula nanometer calcium carbonate preparation equipment

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1453216A (en) * 2002-04-26 2003-11-05 北京化工大学 Eddy flow process of preparing ultramicro calcium carbonate precipitate
CN102897815A (en) * 2012-11-08 2013-01-30 广西华纳新材料科技有限公司 Nano-calcium carbonate carbonization reaction kettle
CN102963918A (en) * 2012-11-08 2013-03-13 广西华纳新材料科技有限公司 Carbonation reaction method of nano calcium carbonate
CN103768980A (en) * 2014-01-20 2014-05-07 东南大学 Long-paddle short-blade composite stirrer

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1453216A (en) * 2002-04-26 2003-11-05 北京化工大学 Eddy flow process of preparing ultramicro calcium carbonate precipitate
CN102897815A (en) * 2012-11-08 2013-01-30 广西华纳新材料科技有限公司 Nano-calcium carbonate carbonization reaction kettle
CN102963918A (en) * 2012-11-08 2013-03-13 广西华纳新材料科技有限公司 Carbonation reaction method of nano calcium carbonate
CN103768980A (en) * 2014-01-20 2014-05-07 东南大学 Long-paddle short-blade composite stirrer

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110183126A (en) * 2019-06-06 2019-08-30 长沙紫宸科技开发有限公司 A method of carbonate cementitious material is prepared by raw material of lime stone
CN110183126B (en) * 2019-06-06 2022-02-18 长沙紫宸科技开发有限公司 Method for preparing carbonate cementing material by taking limestone as raw material
CN111606344A (en) * 2020-04-28 2020-09-01 广西夏阳环保科技有限公司 Method for preparing nano calcium carbonate with high specific surface area
CN112023871A (en) * 2020-08-28 2020-12-04 安徽同益净化科技有限公司 CO (carbon monoxide)2Method for preparing nano calcite VOCs adsorbent by diffusion method
CN113877500A (en) * 2021-10-09 2022-01-04 江西华明纳米碳酸钙有限公司 Stirring formula nanometer calcium carbonate preparation equipment
CN113877500B (en) * 2021-10-09 2023-02-07 江西华明纳米碳酸钙有限公司 Stirring formula nanometer calcium carbonate preparation equipment

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Application publication date: 20180515