CN106395797B - Remove the carbon nanotubes purification system of metal ion - Google Patents

Remove the carbon nanotubes purification system of metal ion Download PDF

Info

Publication number
CN106395797B
CN106395797B CN201610768180.7A CN201610768180A CN106395797B CN 106395797 B CN106395797 B CN 106395797B CN 201610768180 A CN201610768180 A CN 201610768180A CN 106395797 B CN106395797 B CN 106395797B
Authority
CN
China
Prior art keywords
carbon nanotubes
container
acid
storage tank
heat exchanger
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.)
Active
Application number
CN201610768180.7A
Other languages
Chinese (zh)
Other versions
CN106395797A (en
Inventor
沈宇栋
顾灵锋
程阳
蔡峰烽
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.)
Wuxi Dongheng New Energy Technology Co Ltd
Original Assignee
Wuxi Dongheng New Energy Technology Co Ltd
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 Wuxi Dongheng New Energy Technology Co Ltd filed Critical Wuxi Dongheng New Energy Technology Co Ltd
Priority to CN201610768180.7A priority Critical patent/CN106395797B/en
Publication of CN106395797A publication Critical patent/CN106395797A/en
Application granted granted Critical
Publication of CN106395797B publication Critical patent/CN106395797B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01PINDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
    • C01P2006/00Physical properties of inorganic compounds
    • C01P2006/80Compositional purity

Abstract

Remove the carbon nanotubes purification system of metal ion, including fluid reaction bed, heat exchanger, acid storage tank, two grinders and two filter presses, the acid vapors of the fluid reaction bed discharge are passed through heat exchanger, the acid coolant of the heat exchanger discharge is passed through acid storage tank, the carbon nanotubes crude product of the fluid reaction bed discharge is passed through filter press, the acid solution of the filter press discharge is passed through acid storage tank, the carbon nanotubes crude product of the filter press discharge is passed through grinder, carbon nanotubes crude product after the grinder grinding passes through a grinder again, then pass to next filter press, obtain finished product carbon nanotubes.The present invention, carbon nanotubes crude product pass through the continuous grinder of twice, and removal impurity effect is good, and energy consumption is low.

Description

Remove the carbon nanotubes purification system of metal ion
Technical field
The present invention relates to the carbon nanotubes purification system for removing metal ion, belong to carbon nanotubes production technical field.
Background technology
Carbon nanotubes is a kind of tubular nanometer material being made of carbon atom.Tube wall contains multilayer carbon atom and is referred to as multi wall Carbon nanotubes(MWNT), it is referred to as single-walled carbon nanotube containing single layer of carbon atom(SWNT).Carbon nanotubes is since being found, and one It is directly of interest as researcher using its unique structure and excellent performance.Novel conductive/high-strength meet material, electronic device, Catalyst carrier material etc. has potential application prospect.
The preparation process of carbon nanotubes mainly has:Arc discharge method, laser ablation method, chemical vapour deposition technique, solid-phase thermal Solution, flame synthesis, electric glow discharge method and polymerisation synthetic method etc..Wherein, the application of chemical vapour deposition technique (CVD) The most extensively, this method is to allow gaseous alkanes by being attached with the template of catalyst granules, under conditions of 600~1200 DEG C, Gaseous hydrocarbon decomposes generation carbon nanotubes.One outstanding advantages of this method are that Residual reactants are gas, may exit off reaction System, obtains the higher carbon nanotubes of purity, while temperature also need not be very high, in contrast saves energy.However, CVD Method need to use transition-metal catalyst, and such as Fe, Co, Ni and its alloy are as catalyst.This causes prepared carbon nanometer Often the metal impurities containing high level, the presence of metal impurities can directly affect performance and the application of carbon nanotubes in pipe.
The technique that metal impurities are removed from carbon nanotubes is known as purifying.Carbon nanotubes can produce during purification reaction Acid mist and spent acid.At present, acid mist and spent acid not only cause problem of environmental pollution, but also increase all without by recycling Production cost.
Inventor has found by retrieval:Application No. 201510466039.7, entitled carbon nanotubes method of purification, The patent discloses a kind of carbon nanotubes method of purification, and the carbon nanotubes method of purification mainly includes the following steps that:A, in fixation During bed or fluid unit preparation carbon nanotubes or after the completion of preparation, reducing gas and/or inert gas are passed through, is specially Hydrogen and/or carbon dioxide, the temperature of reaction for 100 DEG C -800 DEG C it
Between, the reaction time is 3-60 minutes, and gas flow rate is between 0.06m3/h-1000m3/h;B, stop being passed through Reducing gas, drops to room temperature in the protection of inert gas, and inert gas is nitrogen and/or argon gas, that is, obtains purity as 99.5% Carbon nanotubes above.Carbon nanotubes method of purification of the present invention can remove impurity on the premise of carbon pipe is not injured, and have The advantages that technique is simple, easy to operate, and purification efficiency is high and cost is relatively low, is adapted to the carbon nanotubes purification of industrial mass. But in the patent, can not be fully whole by the oxidizing gas in fixed bed or fluid unit after being passed through inert gas Exclude, in fact, it is difficult to accomplish that carbon nanotubes can be cooled down in reducing gas and/or inert gas without by autoxidation, The purity of carbon nanotubes is caused not reach more than 99.5%.
Inventor also found by retrieval:Application No. 201210476918.4, a kind of entitled purified carbon nanometer The method of pipe, the invention discloses a kind of method of purifying carbon nano-tube, it includes the following steps:Extracted using soxhlet extraction Impurity in carbon nanotubes crude product:First extracted with acid with strong oxidizing property, then extracted with deionized water.The purifying carbon nano-tube of the invention Method with the acid with strong oxidizing property purifying carbon nano-tube of boiling temperature is in, treatment process is simple, processing time is short, eliminates pumping Filter, centrifugation etc. process and substantially increase the efficiency of purifying carbon nano-tube;Purification process damaged caused by carbon nanotubes it is small, it is pure Carbon nanotubes after change is heat-resist and has good reactivity and compatibility;And acid can be recycled and recycled, greatly Resource is saved greatly.Although the patent describes the partial impurities removed in carbon nanotubes crude product, but have no mention of how The impurity in acid with strong oxidizing property and deionized water is separated, it can be reused, is unfavorable for industrial mass production application.
The content of the invention
Above-mentioned in order to solve the problems, such as, the invention discloses a kind of carbon nanotubes for removing metal ion to purify system System, its concrete technical scheme are as follows:
Remove the carbon nanotubes purification system of metal ion, including fluid reaction bed, heat exchanger, acid storage tank, two grindings Machine and two filter presses, the place that the fluid reaction bed is used for carbon nanometer tube material powder and acid solution is reacted are described to change Hot device is used for the sour gas that cooling fluid reaction bed produces, and the acid storage tank is used to store the acid solution that heat exchanger cools down And the acid solution that filter press squeezes out, the filter press are used to extrude the liquid in carbon nanotubes crude product, the grinder For being uniformly mixed by carbon nanotubes crude product and with non-oxidizable acid solution,
The acid vapors of the fluid reaction bed discharge are passed through heat exchanger, and the acid coolant of the heat exchanger discharge is passed through Acid storage tank, the carbon nanotubes crude product of the fluid reaction bed discharge are passed through filter press, and the acid solution of the filter press discharge leads to Enter acid storage tank, the carbon nanotubes crude product of the filter press discharge is passed through grinder, and the carbon nanotubes after the grinder grinding is thick Product pass through a grinder again, then pass to next filter press, obtain finished product carbon nanotubes.
Air pump is provided with the acid storage tank, the air pump conveys air into acid storage tank from the bottom of acid storage tank, is used for Acid solution in acid storage tank is uniformly mixed.
The heat exchanger selects jacketed type exchanger, and the jacketed type exchanger includes container and chuck, the chuck bag Bottom and the surrounding of container are trapped among, gap is left between the chuck and container, the upper end of the chuck is provided with steam inlet, The lower end of the chuck is provided with cooling liquid outlet, and the top of the container is provided with liquid outlet, and the bottom of the container is set There is inlet,
Sour gas from fluid reaction bed is entered in chuck from steam inlet, is formed by the cooling effect of chuck Coolant, and from cooling liquid outlet discharge, be passed into acid storage tank, in the container injection be used for cooling jacket in gas it is molten Liquid, the bottom liquid inlet mouth of the solution from container in the container enter, and are discharged from the liquid outlet of container top.
Agitating device is provided with the container, the agitating device includes central actuating shaft, and the central actuating shaft passes through It extend into container through chuck, and is stretched out from the top of container, the central actuating shaft surrounding is provided with several paddles, Several described paddles are evenly distributed on the horizontal surrounding of central actuating shaft, and the paddle includes several one end and center The horizon bar that drive shaft is fixed, each horizon bar are fixed with several perpendicular vertical plates, and the vertical plate is in half Toroidal, adjacent vertical plate on the same horizon bar mutually stagger.
The through hole of several semicircular arcs is offered on the vertical plate, the circle where the through hole of the semicircular arc is with erecting Circle where straight panel is concentric circles.
The heat exchanger landfill is flushed in underground, the steam inlet with ground, and the top of the central actuating shaft passes through Driving device connects motor.
The inlet and cooling liquid outlet are located at around the bottom of central actuating shaft, and the liquid outlet is located at centre-driven Beside the top of axis.
The present invention operation principle be:
The present invention, carbon nanometer tube material powder and acid solution chemically react on fluid reaction bed, generate carbon nanotubes, Acid mist can be produced in the reaction process, is directly discharged in air, not only pollutes environment, while wastes industrial chemicals, by acid mist It is passed into heat exchanger, acid mist is cooled to acid solution, then the acid solution is passed into acid storage tank, the acid solution in adjustment acid storage tank PH, you can reuse.
The carbon nanotubes crude product generated on fluid reaction bed is input to filter press, and the acid solution of filter press extrusion is also transported to acid Storage tank, treats that industry reuses.Handle to obtain filter cake by filter press, then the filter cake is put into twice grinder, add Non-oxidizing acid, the metal impurities on carbon nanotubes crude product surface are rinsed out, which is also passed into acid storage tank, treat work again Industry uses.Obtained in grinder after removing impurity, more clean carbon nanotubes.Pass through grinder twice, impurity removes more Add thoroughly.
The beneficial effects of the invention are as follows:
1. the present invention, the carbon nanotubes crude product obtained from fluid reaction bed pass through the continuous grinder of twice, go to clean Matter effect is good, and energy consumption is low, reduces carbon nanotubes crude product and repeatedly passes through filter press, longevity of service, reduces carbon nanotubes The time of crude product cleaning;
2. the present invention, acid solution are recovered, treat industrial application again, avoid the wasting of resources;
3. it is of the invention, air pump is provided with acid storage tank, air pump conveys air into acid storage tank from the bottom of acid storage tank, can incite somebody to action Acid solution in acid storage tank is uniformly mixed, and is conducive to the PH of accurately adjustment acid solution;
4. the present invention, soil heat exchanging device of the heat exchanger landfill around underground, heat exchanger has the effect of insulation, sour gas In chuck, thermal energy fully by the liquid absorption in container, fully improves the heat utilization rate in sour gas, avoids industry body Thermal energy wastes;
5. it is of the invention, agitating device is provided with heat exchanger, agitating device flows the liquid agitation in container, with container The heat exchanger effectiveness of liquid in gas and container of the liquid of wall contact in constantly flow regime, increase chuck, is improved Heat exchange efficiency, also improves thermal energy and is absorbed and used rate;
6. the present invention, paddle offers several to fix multiple semicircular vertical plates on horizon bar on vertical plate The through hole of semicircular arc, in paddle rotary course, liquid is passed through from the through hole of semicircular arc, forms turbulent flow, liquid is under When being passed through in the through hole of the semicircular arc of one paddle, to change direction again, and liquid is stirred leaf and promotes towards chamber wall Flowing, liquid flowing are more uniform;Mutually staggering for adjacent vertical plate on the same horizon bar, adds liquid flow Dynamic path, allows liquid sufficient heat exchange in flow process.
Brief description of the drawings
Fig. 1 is the connection relationship diagram of the present invention,
Fig. 2 is the structure diagram of the jacketed type exchanger of the present invention,
Reference numerals list:1-central actuating shaft, 2-liquid outlet, 3-container, 4-steam inlet, 5-chuck, 6- Vertical plate, 7-horizon bar, 8-inlet, 9-cooling liquid outlet.
Embodiment
With reference to the accompanying drawings and detailed description, the present invention is furture elucidated.It should be understood that following embodiments are only For illustrating the present invention rather than limiting the scope of the invention.
Fig. 1 is the connection relationship diagram of the present invention, with reference to attached drawing as it can be seen that the carbon nanotubes purification of this removal metal ion System, including fluid reaction bed, heat exchanger, acid storage tank, two grinders and two filter presses, the fluid reaction bed are used for carbon The place that nanotube source powder and acid solution are reacted, the heat exchanger are used for the sour gas that cooling fluid reaction bed produces Body, the acid storage tank is for storing the acid solution that heat exchanger cools down and the acid solution that filter press squeezes out, the pressure Filter is used to extruding liquid in carbon nanotubes crude product, and the grinder is used for carbon nanotubes crude product and molten with non-oxidizing acid Liquid is uniformly mixed.
The acid vapors of the fluid reaction bed discharge are passed through heat exchanger, and the acid coolant of the heat exchanger discharge is passed through Acid storage tank, the carbon nanotubes crude product of the fluid reaction bed discharge are passed through filter press, and the acid solution of the filter press discharge leads to Enter acid storage tank, the carbon nanotubes crude product of the filter press discharge is passed through grinder, and the carbon nanotubes after the grinder grinding is thick Product pass through a grinder again, then pass to next filter press, obtain finished product carbon nanotubes.The acidity of fluid reaction bed discharge Steam is stored after being cooled down by heat exchanger by acid storage tank, treats industrial application again, and filter press extrudes the acid solution in carbon nanotubes crude product, Grinder cleaning removes the impurity on carbon nanotubes crude product.Carbon nanotubes crude product passes through the continuous grinder of twice, removes impurity Effect is good, and energy consumption is low, reduces carbon nanotubes crude product and repeatedly passes through filter press, longevity of service, it is thick to reduce carbon nanotubes The time of product cleaning.
Air pump is provided with the acid storage tank, the air pump conveys air into acid storage tank from the bottom of acid storage tank, is used for Acid solution in acid storage tank is uniformly mixed.Under the action of air stream, air stream agitates the acid solution in acid storage tank effect, acid Liquid is in continuous turbulence state, is conveniently adjusted to obtain accurate pH value.
Fig. 2 is the structure diagram of the jacketed type exchanger of the present invention, with reference to attached drawing as it can be seen that the heat exchanger selects chuck Formula heat exchanger, the jacketed type exchanger include container 3 and chuck 5, and the chuck 5 is enclosed in bottom and the surrounding of container 3, institute State and gap is left between chuck 5 and container 3, the upper end of the chuck 5 is provided with steam inlet 4, and the lower end of the chuck 5 is set There is cooling liquid outlet 9, the top of the container 3 is provided with liquid outlet 2, and the bottom of the container 3 is provided with inlet 8, comes from The sour gas of fluid reaction bed is entered in chuck 5 from steam inlet 4, and coolant is formed by the cooling effect of chuck 5, and Discharge, be passed into acid storage tank from cooling liquid outlet 9, solution of the injection for gas in cooling jacket 5, institute in the container 3 The bottom liquid inlet mouth 8 for stating the solution from container 3 in container 3 enters, and is discharged from the liquid outlet 2 at the top of container 3.From fluid reaction The acid vapors of bed are cooled into liquid, and the heat in steam is by liquid absorption in container 3, steam and the liquid flow in container 3 To on the contrary, improving heat exchanger effectiveness.
Agitating device is provided with the container 3, the agitating device includes central actuating shaft 1, the central actuating shaft 1 Penetrate chuck 5 to extend into container 3, and stretched out from the top of container 3,1 surrounding of central actuating shaft is provided with several Paddle, several described paddles are evenly distributed on the horizontal surrounding of central actuating shaft 1, the paddle include several one The horizon bar 7 that end is fixed with central actuating shaft 1, each horizon bar 7 are fixed with several perpendicular vertical plates 6, institute 6 semicircular in shape shape of vertical plate is stated, the through hole of several semicircular arcs is offered on the vertical plate 6, the semicircular arc leads to Circle where hole and the circle where vertical plate 6 are concentric circles.Paddle can flow the liquid agitation in container 3, liquid Inside carries out heat exchange, avoids that the fluid temperature close to container 3 wall is high, and the fluid temperature close to 3 center of container is low, allows container 3 In liquid can fully absorb thermal energy.Adjacent vertical plate 6 on the same horizon bar 7 mutually staggers.Strengthen container 3 The scrambling of middle liquid flowing, makes the liquid internal thermal energy in container 3 fully dispersed uniformly.
The heat exchanger landfill is flushed in underground, the steam inlet 4 with ground, and the top of the central actuating shaft 1 leads to Over-driving device connects motor.Avoid the thermal energy in heat exchanger by diffusion in atmosphere, soil is solid around heat exchanger again Surely it is ignorant of, and the good heat insulating of soil, after soil is heated to predetermined temperature by chuck 5, the thermal energy in steam is with regard to abundant By the liquid absorption in container 3.
The inlet 8 and cooling liquid outlet 9 are located at around the bottom of central actuating shaft 1, and the liquid outlet 2 is located at center Beside the top of drive shaft 1.Ensure that the longitudinal center of central actuating shaft 1 from 5 heat exchanger of chuck passes through.
Technological means disclosed in the present invention program is not limited only to the technological means disclosed in above-mentioned technological means, further includes Formed technical solution is combined by above technical characteristic.
It is complete by above-mentioned description, relevant staff using the above-mentioned desirable embodiment according to the present invention as enlightenment Various changes and amendments can be carried out without departing from the scope of the technological thought of the present invention' entirely.The technology of this invention Property scope is not limited to the content on specification, it is necessary to determines its technical scope according to right.

Claims (5)

1. the carbon nanotubes purification system of metal ion is removed, it is characterized in that including fluid reaction bed, heat exchanger, acid storage tank, two A grinder and two filter presses, the place that the fluid reaction bed is used for carbon nanometer tube material powder and acid solution is reacted, The heat exchanger is used for the sour gas that cooling fluid reaction bed produces, and the acid storage tank is used to store what heat exchanger cooled down The acid solution that acid solution and filter press squeeze out, the filter press is used to extrude the liquid in carbon nanotubes crude product, described Grinder is used to be uniformly mixed by carbon nanotubes crude product and with non-oxidizable acid solution, the acid steaming of the fluid reaction bed discharge Vapour is passed through heat exchanger, and the acid coolant of the heat exchanger discharge is passed through acid storage tank, the carbon nanometer of the fluid reaction bed discharge Pipe crude product is passed through filter press, and the acid solution of the filter press discharge is passed through acid storage tank, the carbon nanotubes of the filter press discharge Crude product is passed through grinder, and the carbon nanotubes crude product after the grinder grinding passes through a grinder, then passes to next again Filter press, obtains finished product carbon nanotubes;
Air pump is provided with the acid storage tank, the air pump conveys air into acid storage tank from the bottom of acid storage tank, for by acid Acid solution in storage tank is uniformly mixed;
Agitating device is provided with the container, the agitating device includes central actuating shaft, and the central actuating shaft penetrates Chuck is extend into container, and is stretched out from the top of container, and the central actuating shaft surrounding is provided with several paddles, if The dry paddle is evenly distributed on the horizontal surrounding of central actuating shaft, and the paddle includes several one end and driven with center The horizon bar that moving axis is fixed, each horizon bar are fixed with several perpendicular vertical plates, and the vertical plate is in semicircle Shape, adjacent vertical plate on the same horizon bar mutually stagger.
2. the carbon nanotubes purification system according to claim 1 for removing metal ion, it is characterized in that the heat exchanger selects With jacketed type exchanger, the jacketed type exchanger includes container and chuck, and the chuck is enclosed in bottom and the surrounding of container, Gap is left between the chuck and container, the upper end of the chuck is provided with steam inlet, and the lower end of the chuck is provided with Cooling liquid outlet, the top of the container are provided with liquid outlet, and the bottom of the container is provided with inlet, from fluid reaction The sour gas of bed is entered in chuck from steam inlet, forms coolant by the cooling effect of chuck, and go out from coolant Mouth discharge, is passed into acid storage tank, solution of the injection for gas in cooling jacket in the container, molten in the container Liquid enters from the bottom liquid inlet mouth of container, is discharged from the liquid outlet of container top.
3. the carbon nanotubes purification system according to claim 2 for removing metal ion, it is characterized in that on the vertical plate The through hole of several semicircular arcs is offered, the circle where the through hole of the semicircular arc and the circle where vertical plate are concentric Circle.
4. the carbon nanotubes purification system according to claim 3 for removing metal ion, it is characterized in that the heat exchanger is filled out Underground is embedded in, the steam inlet is flushed with ground, and motor is connected via drive in the top of the central actuating shaft.
5. it is according to claim 4 remove metal ion carbon nanotubes purification system, it is characterized in that the inlet and Cooling liquid outlet is located at around the bottom of central actuating shaft, and the liquid outlet is located at beside the top of central actuating shaft.
CN201610768180.7A 2016-08-31 2016-08-31 Remove the carbon nanotubes purification system of metal ion Active CN106395797B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201610768180.7A CN106395797B (en) 2016-08-31 2016-08-31 Remove the carbon nanotubes purification system of metal ion

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201610768180.7A CN106395797B (en) 2016-08-31 2016-08-31 Remove the carbon nanotubes purification system of metal ion

Publications (2)

Publication Number Publication Date
CN106395797A CN106395797A (en) 2017-02-15
CN106395797B true CN106395797B (en) 2018-04-24

Family

ID=58003211

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201610768180.7A Active CN106395797B (en) 2016-08-31 2016-08-31 Remove the carbon nanotubes purification system of metal ion

Country Status (1)

Country Link
CN (1) CN106395797B (en)

Also Published As

Publication number Publication date
CN106395797A (en) 2017-02-15

Similar Documents

Publication Publication Date Title
CN104961123B (en) A kind of native graphite ore deposit peels off method of purification
JP2006517900A (en) Process and apparatus for producing precipitated silica from rice husk ash
KR101727939B1 (en) Surface treating method using Tayler Reactor
CN104176723A (en) Small-tube-diameter carbon nano-tube purification device and small-tube-diameter carbon nano-tube purification method
JP7431796B2 (en) Boron nitride purification method and equipment
CN1137861C (en) Waste water treatment process by super-critical aqueous oxidation
CN206089049U (en) Go to carbon nanotube purification system that mixes in succession
CN102633350B (en) Method for recycling excessive oxygen and carbon dioxide in supercritical water oxidation system
CN114560765B (en) Industrial production method of crotonic acid by adopting microchannel reactor
CN113416151B (en) Preparation method of pure acetonitrile for chromatographic analysis and production equipment thereof
CN106395797B (en) Remove the carbon nanotubes purification system of metal ion
CN206089045U (en) Carbon nanotube purification system of recovered acid
CN206089047U (en) Heat recovery's tubule footpath carbon nanotube purification system
CN206089046U (en) Tubule footpath carbon nanotube purification system
CN206089048U (en) Get rid of metal ion's carbon nanotube purification system
CN112225200A (en) Method and device for continuously preparing high-purity carbon nano tube
CN106167257B (en) The pipe with small pipe diameter CNT purification system of energy recovery
CN105000745B (en) A kind of sulfur Gas Fields produced water treatment system
CN206188392U (en) Carbon nanotube purification system
CN106167259B (en) The Carbon nanotube purification system of precipitate metal ion
CN105174581B (en) A kind of sulfur Gas Fields produced water treatment technique
CN206089051U (en) Carbon nanotube purification system of multistage retrieval and utilization of heat energy
CN106365150A (en) Carbon nano tube purification system for recycling acid liquor in different stages
CN103482587A (en) Purification recovery process of waste sulfuric acid rich in organic impurity
CN1594615A (en) Sodium purifying process and purification system thereof

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant
PE01 Entry into force of the registration of the contract for pledge of patent right
PE01 Entry into force of the registration of the contract for pledge of patent right

Denomination of invention: Purification system of carbon nanotubes for removing metal ions

Effective date of registration: 20200824

Granted publication date: 20180424

Pledgee: Bank of Jiangsu Co.,Ltd. Wuxi Shanbei sub branch

Pledgor: WUXI DONGHENG NEW ENERGY TECHNOLOGY Co.,Ltd.

Registration number: Y2020320010125