CN107855088A - A kind of efficient, intelligence reactive crystallization equipment - Google Patents

A kind of efficient, intelligence reactive crystallization equipment Download PDF

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Publication number
CN107855088A
CN107855088A CN201711387448.3A CN201711387448A CN107855088A CN 107855088 A CN107855088 A CN 107855088A CN 201711387448 A CN201711387448 A CN 201711387448A CN 107855088 A CN107855088 A CN 107855088A
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CN
China
Prior art keywords
reactive crystallization
efficient
reactor
equipment according
intelligence
Prior art date
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Pending
Application number
CN201711387448.3A
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Chinese (zh)
Inventor
黄青山
朱全红
肖航
杨超
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Institute of Process Engineering of CAS
Qingdao Institute of Bioenergy and Bioprocess Technology of CAS
Original Assignee
Qingdao Institute of Bioenergy and Bioprocess Technology of CAS
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 Qingdao Institute of Bioenergy and Bioprocess Technology of CAS filed Critical Qingdao Institute of Bioenergy and Bioprocess Technology of CAS
Priority to CN201711387448.3A priority Critical patent/CN107855088A/en
Publication of CN107855088A publication Critical patent/CN107855088A/en
Pending legal-status Critical Current

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Classifications

    • 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
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D9/00Crystallisation
    • B01D9/0063Control or regulation
    • 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
    • B01J19/0006Controlling or regulating processes
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D9/00Crystallisation
    • B01D2009/0086Processes or apparatus therefor

Abstract

The invention discloses a kind of equipment that can efficiently, intelligently, accurately control reaction crystallization process, it includes:Agent set reactor, constant temperature water bath apparatus is provided with the outside of the agent set, feed arrangement is provided with the agent set top, agitating device, pH electrodes, conductance electrode are provided with the agent set top, the constant temperature water bath apparatus, feed arrangement, agitating device, pH electrodes and conductance electrode etc. are all connected with programmable logic controller (PLC) PLC automatic control system, automated intelligent control is realized, meanwhile, the granularity of product can be monitored in real time by online granulometry system.Overall structure of the present invention is simply clear, reaction crystallization process full-automatic measurement, feedback and control can be realized, artificial running cost and manual operation error are reduced, reaction crystallization process is carried out all the time under the reaction condition set, so as to ensure the quality of required product and stability.

Description

A kind of efficient, intelligence reactive crystallization equipment
Technical field
The present invention relates to chemical reaction to crystallize automation control area, more particularly to a kind of reaction knot efficiently, intelligent Crystalline substance equipment.Quality control available for reactive crystallization in chemical industry, advanced material and medical product.
Background technology
The core of lithium ion battery is positive electrode, however, positive electrode current material precursor is in prepare with scale mistake The problems such as crystal tap density is small, size distribution is wide, pattern is defective, quality is unstable in journey be present, need to accurately monitor on-line, The reaction conditions such as charging rate, temperature, pH, electrical conductivity, speed of agitator in auto-control reaction system, to reach accurate control The reaction crystallization process of positive electrode material precursor.
It is entitled such as patent CN105183026B:A kind of automatic regulating system of crystallization reaction acid-base value, its feature Including:The pH electrodes of crystallization reaction acid-base value in the retort are detected in real time;The acid-base value that the pH electrodes are detected is received, And the ISM transmitters for presetting acid-base value threshold value are provided between the alkali lye secondary flow gauge and the retort, according to described The magnetic valve of the instruction automatic shutter of ISM transmitters.
It is entitled such as patent CN103551100B:A kind of continuous fast reaction crystallization improves the dress of crystal stability Put and method, its feature include:By two or more reaction solutions respectively from the different feeds tube pump of liquid jet impact feed arrangement Enter, reaction solution is sprayed in a manner of the collision that liquidates from nozzle enters tank reactor, in tank reactor in a manner of complete mixing flow Reaction nucleation is carried out, reaction solution flows into tubular reactor afterwards, and carry out crystal growth is flowed in a manner of laminar flow, then after Handle the crystal product stablized.
And for example patent CN104881062B, it is entitled:It is a kind of quickly to be controlled without toning crystallisation by cooling temperature of reaction kettle Method, its summary include:This method is added using refrigeration compressor, the electronics based on pulse width modulation power of variable ratio frequency changer regulation power Heat pipe, programmable controller, monitoring computer construction temperature control system.It is anti-that crystallization can be quantitatively adjusted using the invention Answer the rate of temperature fall of kettle solution, it is ensured that reach the cooling desired value specified without toning, so as to be carried for the cooling of crystallization processes regulation For a kind of convenient and reliable automation control method.
Current reactive crystallization automaton be auto-control a certain item operating condition, such as pH, temperature, no It can realize to all operationss condition on-line monitoring and automatically control.And realize the automatic control for so including all operationss condition System, is not the simple superposition of these single condition controls, but the control of various conditions is organically combined, and avoids in different bars Contradiction is produced in the control of part, and there is presently no the good control strategy of such a integrality.Importantly, in large arch dam In rate, opaque reactive crystallization system can real-time monitored crystal morphology and measure Lens capsule equipment there is not yet Arrive.
The content of the invention
For the existing reactive crystallization automaton a certain item operating condition that has been auto-control, and can not be in height The deficiency of real-time monitored crystal morphology and granularity in solid holdup, opaque reactive crystallization system, the invention provides a kind of high The reactive crystallization equipment of effect, intelligence, for monitoring and automatically controlling the charging rate of reaction crystallization process, temperature, pH, electricity on-line The all operationss condition such as condensate flow inside and outside conductance, speed of agitator and kettle, and in high solid concentration, opaque hot-die system The pattern and size distribution of middle on-line measurement crystal grain.
In order to solve the above problems, the invention provides following technical scheme:
A kind of efficient, intelligence reactive crystallization equipment, it is characterised in that including:
The reactor of reactive crystallization is carried out for saline solution, complex liquid, alkali lye and acid solution;
For keeping the constant temperature water bath apparatus of inside reactor constant temperature;
For the feed arrangement fed to reactor inside;
Agitating device for stirring inside reactor;
For detecting the pH measurement apparatus of reactive crystallization acid-base value in the reactor in real time;
For detecting the conductivity measuring apparatus of reactive crystallization electrical conductivity in the reactor in real time;
For automatically controlling the FPGA of the conditions such as the charging rate of reactive crystallization, temperature, pH, electrical conductivity, speed of agitator Controller PLC automatic control system;
For monitoring the online granulometry system of reactive crystallization granularity and pattern on-line;
Saline solution needed for reactive crystallization, complex liquid, alkali lye and acid solution are sent into by tank reactor by feed arrangement, pass through constant temperature Water bath device control temperature in the kettle keeps constant, reactant in kettle is sufficiently mixed uniformly by agitating device, is measured by pH PH and electrical conductivity and PLC automatic control system is fed back in device and conductivity measuring apparatus measurement kettle, automatically controlled by PLC and be The addition speed for auto-control saline solution, complex liquid, alkali lye and the acid solution of uniting, makes pH and electrical conductivity in kettle be maintained at suitable reactive crystallization Condition, be sent into online grain after the pretreatment such as dilute, tile from the crystalline product of the overfall overflow of continuous production discharging Measuring system is spent, to observe crystal size and pattern.
Further, the constant temperature water bath apparatus includes thermal resistance, water-bath chuck, circulating cooling water coil, circulating pump, kettle Interior condenser tube.
Further, the peripherally disposed baffle plate of reactor inwall, baffle number are 2-8.
Further, the kettle interior condenser tube is combined into one with baffle plate.
Further, the feed arrangement includes material liquid tank and corresponding feed pump.
Further, the agitating device includes agitating paddle, belt, stirring motor and automatic speed measuring device.
Further, the pH measurement apparatus includes pH electrodes, electrode protection set and is connected with pH electrodes automatic aobvious Show instrument etc., pH measurement ranges are 0-14.
Further, the conductivity measuring apparatus includes conductance electrode, electrode protection set and is connected with conductance electrode Meter of Automatic Display.
Further, the automatic control control system and some feed pumps, pH electrodes, conductance electrode, thermal resistance, condenser pipe, Stirring motor, online granulometry system etc. are connected.
Further, the online granulometry system includes high definition photographic system, measuring platform and supporting computer, and granularity is surveyed It is 1-10000 μm to measure scope.
It is compared with the prior art, the present invention has advantages below:
It is provided by the invention it is a kind of efficiently, intelligence reactive crystallization equipment be a set of Automatic Control continuous production device, energy Enough charging rates monitored on-line and regulate and control reactive crystallization, temperature, pH, electrical conductivity, speed of agitator, the operation such as condensed water inside and outside kettle Condition, it is whole without manually operated.Meanwhile a kind of efficient, intelligence reactive crystallization equipment provided by the invention carries high-resolution The photographic means of rate, can high solid concentration, it is nontransparent in the case of online observation product shape characteristic and size distribution Situation, convenient adjustment operating parameter in time, to ensure crystal mass.So as to ensure reaction crystallization process all the time to the full extent Carried out under stable reaction condition, generate good pattern, uniform particle sizes, the crystal of product stabilization.
Brief description of the drawings
Fig. 1 is the block schematic illustration of the present invention.
Fig. 2 is the structural representation of agent set of the present invention.
Wherein, 1 is salt flow container, and 2 be alkali liquid tank, and 3 be complexing flow container, and 4 be acid solution tank, and 5 be baffle plate, and 6 be agitating device, 7 It is pH electrodes for conductance electrode, 8,9 be constant temperature water bath apparatus, and 10 be reactor, and 11 be online granulometry system, and 12 be PLC Automatic control system.
Embodiment
Embodiment one
Reaction bottom liquid is added in 10 L reactors, including 9.5 L pure water, by 6:2:The nickel sulfate of 2 molar ratio weighing, Cobaltous sulfate and manganese sulfate solid totally 623 g, 0.3 L ammoniacal liquor and 192 g sodium hydrate solids etc..By 6:2:2 molar ratio The mixing salt solution of nickel sulfate, cobaltous sulfate and manganese sulfate that concentration is 0.8 mol/L adds the mol/L of salt flow container 1,1.4 hydrogen-oxygen Change the ammonia spirit addition complexing flow container 3 that sodium solution adds the mol/L of alkali liquid tank 2,1, compound concentration is that 1 mol/L sulfuric acid is molten Liquid adds acid solution tank 4.The inwall of reactor 10 sets baffle plate 5, peripherally disposed 4, reduces the directed flow of liquid, strengthens Turbulence.PLC automatic control system 12 is the Automatic Centering Control of whole device, and various operating parameters are received by front-end probe Signal simultaneously provides respective feedback and is adjusted.Revolution speed is fed by controlling, to adjust charging rate.Can by conductance electrode 7 Realize that the charging rate of saline solution and complex liquid controls the electrical conductivity in kettle in automated intelligent control reactor 10, makes solution in kettle It is maintained at the degree of supersaturation for being adapted to crystallization.Similarly, the charging rate of acid solution and alkali lye is automatically controlled by pH electrodes 8 to control It is 10.5 that pH is constant in reactor 10, and control accuracy is ± 0.02.The kettle interior condenser tube being arranged on inside baffle plate 5 can be to reactor Material temperature controlling in 10, the temperature runaway of liquid is prevented, using also including thermal resistance, water-bath chuck, circulating cooling water coil and circulating pump Constant temperature water bath apparatus 9 accurately control reactor temperature be 50oC, temperature-controlled precision are ± 0.1oC.Agitating device 6 is set Speed of agitator is 700 r/min, and the actual speed of agitating paddle is measured with hall principle.It can be read in real time by Meter of Automatic Display Take rotating speed, temperature, electrical conductivity, pH numerical value.From the product of the overfall outflow of continuous production discharging, through over sampling, dilution, put down Online granulometry system 11 is put into after the pretreatment such as paving to be taken pictures, analyzed, so as to realize the online survey of Lens capsule Amount, then feeds back to PLC automatic control system 12, according to the intelligent control for establishing control strategy and carrying out in real time operating parameter, makes Particle size range is at 10-100 μm.
Embodiment two
In 2 m3Reaction bottom liquid is added in reactor, including 1940 L pure water, by 8:1:The sulfuric acid of 1 molar ratio weighing Nickel, cobaltous sulfate and manganese sulfate solid totally 124.6 kg, 60 L ammoniacal liquor and 38.4 kg sodium hydrate solids etc..By 8:1:1 mole Mixing salt solution than nickel sulfate, cobaltous sulfate and manganese sulfate that compound concentration is 0.8 mol/L adds the mol/L of salt flow container 1,1.4 Sodium hydroxide solution add alkali liquid tank 2,1 mol/L ammonia spirit and add complexing flow container 3, compound concentration is 1 mol/L's Sulfuric acid solution adds acid solution tank 4.The inwall of reactor 10 sets baffle plate 5, peripherally disposed 8, reduces the oriented flow of liquid It is dynamic, strengthen turbulence.PLC automatic control system 12 is the Automatic Centering Control of whole device, and various behaviour are received by front-end probe Make the signal of parameter and provide respective feedback to be adjusted.Revolution speed is fed by controlling, to adjust charging rate.Pass through conductance Electrode 7, which can be realized, automatically controls in reactor 10 charging rate of saline solution and complex liquid to control the electrical conductivity in kettle, makes in kettle Solution is maintained at the degree of supersaturation for being adapted to crystallization.Similarly, automatically controlled by pH electrodes 8 charging rate of acid solution and alkali lye come It is 11.5 that pH is constant in control reactor 10, and control accuracy is ± 0.02.The kettle interior condenser tube being arranged on inside baffle plate 5 can be to anti- Material temperature controlling in kettle 10 is answered, prevents the temperature runaway of liquid, using also including thermal resistance, water-bath chuck, circulating cooling water coil and follow It is 75 that the constant temperature water bath apparatus 9 of ring pump, which accurately controls reactor temperature,oC, temperature-controlled precision are ± 0.1oC.Agitating device is set 6 speed of agitator is 900 r/min, and the actual speed of agitating paddle is measured with hall principle.Can be real by Meter of Automatic Display When read rotating speed, temperature, electrical conductivity, pH numerical value.From the product of the overfall outflow of continuous production discharging, through over sampling, dilute Release, tile etc. and being put into online granulometry system 11 after pretreatment and taken pictures, analyzed, so as to realize Lens capsule Line measure, then feed back to PLC automatic control system 12, according to establish control strategy carry out in real time operating parameter intelligence control System, makes particle size range at 10-100 μm.
Overall structure of the present invention is simply clear, can realize the full-automatic intelligent control of reaction crystallization process, reduces people Work running cost and manual operation error, reaction crystallization process is set to be carried out all the time under the reaction condition set, so as to ensure The quality and stability and continuity of product.
A kind of efficient, intelligence reactive crystallization equipment provided by the present invention is described in detail above.Herein Apply specific case to be set forth embodiments of the present invention, the explanation of above example is only intended to help and understands this The core concept of invention.It should be pointed out that for those skilled in the art, the principle of the invention is not being departed from Under the premise of, some improvements and modifications can also be made, these improvements and modifications also should be regarded as protection scope of the present invention, this implementation The available prior art of each part being not known in example is realized.

Claims (10)

  1. A kind of 1. efficient, intelligence reactive crystallization equipment, it is characterised in that including:
    The reactor of reactive crystallization is carried out for saline solution, complex liquid, alkali lye and acid solution;
    For keeping the constant temperature water bath apparatus of constant temperature inside reactor;
    For the feed arrangement fed to reactor inside;
    Agitating device for stirring inside reactor;
    For detecting the pH measurement apparatus of reactive crystallization acid-base value in the reactor in real time;
    For detecting the conductivity measuring apparatus of reactive crystallization electrical conductivity in the reactor in real time;
    For automatically controlling the FPGA of the conditions such as the charging rate of reactive crystallization, temperature, pH, electrical conductivity, speed of agitator Controller PLC automatic control system;
    For monitoring the online granulometry system of reactive crystallization granularity and pattern on-line;
    Saline solution needed for reactive crystallization, complex liquid, alkali lye and acid solution are sent into by tank reactor by feed arrangement, pass through constant temperature Water bath device control temperature in the kettle keeps constant, reactant in kettle is sufficiently mixed uniformly by agitating device, is measured by pH PH and electrical conductivity and PLC automatic control system is fed back in device and conductivity measuring apparatus measurement kettle, automatically controlled by PLC and be The addition speed for auto-control saline solution, complex liquid, alkali lye and the acid solution of uniting, makes pH and electrical conductivity in kettle be maintained at suitable reactive crystallization Condition, from continuous production discharging overfall overflow crystalline product through over sampling, dilution, tiling etc. pre-process after be fed in Line granulometry system, to observe crystal size and pattern.
  2. 2. efficient, intelligence reactive crystallization equipment according to claim 1, it is characterised in that the constant temperature water bath apparatus Including thermal resistance, water-bath chuck, circulating cooling water coil, circulating pump, kettle interior condenser tube.
  3. 3. efficient, intelligence reactive crystallization equipment according to claim 1, it is characterised in that the reactor inwall edge Circumferencial direction sets baffle plate, and baffle number is 2-8.
  4. 4. efficient, the intelligent reactive crystallization equipment according to Claims 2 or 3, it is characterised in that the kettle interior condenser tube It is combined into one with baffle plate.
  5. 5. efficient, intelligence reactive crystallization equipment according to claim 1, it is characterised in that the feed arrangement includes Material liquid tank and corresponding feed pump.
  6. 6. efficient, intelligence reactive crystallization equipment according to claim 1, it is characterised in that the agitating device includes Agitating paddle, belt, stirring motor and automatic speed measuring device.
  7. 7. efficient, intelligence reactive crystallization equipment according to claim 1, it is characterised in that the pH measurement apparatus bag PH electrodes, electrode protection set and Meter of Automatic Display for being connected with pH electrodes etc. are included, pH measurement ranges are 0-14.
  8. 8. efficient, intelligence reactive crystallization equipment according to claim 1, it is characterised in that the conductivity measurement dress Put including conductance electrode, electrode protection set and the Meter of Automatic Display being connected with conductance electrode.
  9. 9. efficient, intelligence reactive crystallization equipment according to claim 1, it is characterised in that the automatic control control system It is connected with some feed pumps, pH electrodes, conductance electrode, thermal resistance, condenser pipe, stirring motor, online granulometry system etc..
  10. 10. efficient, intelligence reactive crystallization equipment according to claim 1, it is characterised in that the online granulometry System includes high definition photographic system, measuring platform and supporting computer, and granulometry scope is 1-10000 μm.
CN201711387448.3A 2017-12-20 2017-12-20 A kind of efficient, intelligence reactive crystallization equipment Pending CN107855088A (en)

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Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108203114A (en) * 2018-04-11 2018-06-26 宜春市鼎鑫高能科技有限公司 A kind of system of brine crystallization lithium carbonate suitable for industrial automation production
CN108745252A (en) * 2018-07-09 2018-11-06 北京市计量检测科学研究院 A kind of micro Nano material preparation facilities
CN108905262A (en) * 2018-06-12 2018-11-30 崇义章源钨业股份有限公司 The system and method for ammonium para-tungstate crystal automation control
CN109116893A (en) * 2018-09-30 2019-01-01 镇江华智睿安物联科技有限公司 A kind of width Cheng Wendu is adjusted and the device of pH measurement
CN109187641A (en) * 2018-08-10 2019-01-11 中国原子能科学研究院 A kind of device of research ionic crystal reaction nucleation kinetics
CN109182742A (en) * 2018-09-28 2019-01-11 中国恩菲工程技术有限公司 Rare-earth precipitation device
CN109187854A (en) * 2018-08-10 2019-01-11 中国原子能科学研究院 The measuring method of reaction solution extension rate when studying ionic crystal reaction nucleation rate
CN109942655A (en) * 2019-04-29 2019-06-28 宜昌东阳光药业股份有限公司 A kind of continuous crystallisation process of erythromycin thiocyanate crude product
CN110160919A (en) * 2019-07-04 2019-08-23 中国科学院青岛生物能源与过程研究所 A kind of on-line measurement device of grain graininess and pattern
CN111154827A (en) * 2020-01-22 2020-05-15 金河生物科技股份有限公司 Method for producing oxytetracycline

Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1271185A (en) * 2000-05-08 2000-10-25 许开华 Preparation method and equipment of the anode material for lithium ion cell
CN103551100A (en) * 2013-10-31 2014-02-05 华南理工大学 Device and method for improving stability of crystals by using continuous and rapid reactive crystallization
CN104888682A (en) * 2015-05-27 2015-09-09 张四清 Environment-friendly chemical tank capable of automatically injecting water
CN105183026A (en) * 2015-08-26 2015-12-23 宁波金和锂电材料有限公司 Automatic adjustment system for adjusting pH value of crystallization reaction
CN105561624A (en) * 2016-01-29 2016-05-11 太仓市微贯机电有限公司 Reactor equipment for spherical crystals
CN205308324U (en) * 2015-12-30 2016-06-15 安泰科技股份有限公司 Reaction system of preparation lithium ion secondary cell cathode material precursor
CN205353799U (en) * 2016-01-19 2016-06-29 宁波金和锂电材料有限公司 Governing system of crystallization reaction pH valve
CN106549150A (en) * 2016-11-07 2017-03-29 多氟多(焦作)新能源科技有限公司 A kind of preparation method of nickel manganese cobalt complex hydroxide and the reactor for preparing nickel manganese cobalt complex hydroxide
CN106573794A (en) * 2014-08-01 2017-04-19 苹果公司 High-density precursor for manufacture of composite metal oxide cathodes for li-ion batteries
CN206435198U (en) * 2016-12-31 2017-08-25 北京当升材料科技股份有限公司 A kind of synthesis device of precursor of lithium ionic cell positive material

Patent Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1271185A (en) * 2000-05-08 2000-10-25 许开华 Preparation method and equipment of the anode material for lithium ion cell
CN103551100A (en) * 2013-10-31 2014-02-05 华南理工大学 Device and method for improving stability of crystals by using continuous and rapid reactive crystallization
CN106573794A (en) * 2014-08-01 2017-04-19 苹果公司 High-density precursor for manufacture of composite metal oxide cathodes for li-ion batteries
CN104888682A (en) * 2015-05-27 2015-09-09 张四清 Environment-friendly chemical tank capable of automatically injecting water
CN105183026A (en) * 2015-08-26 2015-12-23 宁波金和锂电材料有限公司 Automatic adjustment system for adjusting pH value of crystallization reaction
CN205308324U (en) * 2015-12-30 2016-06-15 安泰科技股份有限公司 Reaction system of preparation lithium ion secondary cell cathode material precursor
CN205353799U (en) * 2016-01-19 2016-06-29 宁波金和锂电材料有限公司 Governing system of crystallization reaction pH valve
CN105561624A (en) * 2016-01-29 2016-05-11 太仓市微贯机电有限公司 Reactor equipment for spherical crystals
CN106549150A (en) * 2016-11-07 2017-03-29 多氟多(焦作)新能源科技有限公司 A kind of preparation method of nickel manganese cobalt complex hydroxide and the reactor for preparing nickel manganese cobalt complex hydroxide
CN206435198U (en) * 2016-12-31 2017-08-25 北京当升材料科技股份有限公司 A kind of synthesis device of precursor of lithium ionic cell positive material

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
刘家棋 等: "《分离过程与技术》", 31 December 2001, 天津大学出版社 *
陈志平等: "《搅拌与混合设备设计选用手册》", 31 May 2004, 化学工业出版社 *

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108203114A (en) * 2018-04-11 2018-06-26 宜春市鼎鑫高能科技有限公司 A kind of system of brine crystallization lithium carbonate suitable for industrial automation production
CN108905262A (en) * 2018-06-12 2018-11-30 崇义章源钨业股份有限公司 The system and method for ammonium para-tungstate crystal automation control
CN108745252A (en) * 2018-07-09 2018-11-06 北京市计量检测科学研究院 A kind of micro Nano material preparation facilities
CN109187641A (en) * 2018-08-10 2019-01-11 中国原子能科学研究院 A kind of device of research ionic crystal reaction nucleation kinetics
CN109187854A (en) * 2018-08-10 2019-01-11 中国原子能科学研究院 The measuring method of reaction solution extension rate when studying ionic crystal reaction nucleation rate
CN109182742A (en) * 2018-09-28 2019-01-11 中国恩菲工程技术有限公司 Rare-earth precipitation device
CN109116893A (en) * 2018-09-30 2019-01-01 镇江华智睿安物联科技有限公司 A kind of width Cheng Wendu is adjusted and the device of pH measurement
CN109942655A (en) * 2019-04-29 2019-06-28 宜昌东阳光药业股份有限公司 A kind of continuous crystallisation process of erythromycin thiocyanate crude product
CN109942655B (en) * 2019-04-29 2020-05-12 宜昌东阳光药业股份有限公司 Continuous crystallization method of erythromycin thiocyanate crude product
CN110160919A (en) * 2019-07-04 2019-08-23 中国科学院青岛生物能源与过程研究所 A kind of on-line measurement device of grain graininess and pattern
CN111154827A (en) * 2020-01-22 2020-05-15 金河生物科技股份有限公司 Method for producing oxytetracycline
CN111154827B (en) * 2020-01-22 2021-11-05 金河生物科技股份有限公司 Method for producing oxytetracycline

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