CN112808018A - Two-dimensional film continuous production process and equipment based on electrophoresis strategy - Google Patents
Two-dimensional film continuous production process and equipment based on electrophoresis strategy Download PDFInfo
- Publication number
- CN112808018A CN112808018A CN202011541089.4A CN202011541089A CN112808018A CN 112808018 A CN112808018 A CN 112808018A CN 202011541089 A CN202011541089 A CN 202011541089A CN 112808018 A CN112808018 A CN 112808018A
- Authority
- CN
- China
- Prior art keywords
- dimensional
- electrophoresis
- porous substrate
- strategy
- production process
- 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.)
- Pending
Links
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D67/00—Processes specially adapted for manufacturing semi-permeable membranes for separation processes or apparatus
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D69/00—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
- B01D69/02—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor characterised by their properties
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2323/00—Details relating to membrane preparation
- B01D2323/35—Use of magnetic or electrical fields
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2323/00—Details relating to membrane preparation
- B01D2323/42—Details of membrane preparation apparatus
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The invention belongs to the technical field of preparation of nano separation membranes, and discloses a two-dimensional membrane continuous production process and equipment based on an electrophoresis strategy. The method specifically comprises the following steps: (1) the porous substrate is convoluted on a reel and is connected in sequence to enable the porous substrate to pass through an electrodeposition tank and a dryer in sequence; (2) dispersing the two-dimensional nanosheets in a solvent to obtain a two-dimensional nanosheet solution; (3) and (3) placing the two-dimensional nanosheet solution obtained in the step (2) in an electrodeposition tank, carrying out electrophoretic deposition on the porous substrate, drying the porous substrate by using a dryer, and carrying out convolution by using a scroll to collect a two-dimensional film so as to obtain the two-dimensional film. The method has the advantages of low cost, high efficiency, strong operability, and integration of film deposition, film forming, drying and packaging; the obtained two-dimensional film has strong binding capacity with a substrate, uniform thickness and good flexibility. The technical operation problem that the two-dimensional film can not be continuously prepared in a large range is solved.
Description
Technical Field
The invention belongs to the technical field of preparation of nano separation membranes, and particularly relates to a two-dimensional membrane continuous production process and equipment based on an electrophoresis strategy.
Background
Separation processes play an important role in industrial production, mainly in relation to gas phase separation, liquid phase separation and multi-phase separation. Currently, separation processes are mainly achieved by distillation or adsorption units. Such processes typically consume large amounts of energy and have large footprint, high maintenance and operating costs, and low efficiency. The supply and demand proportion of industrial production and chemical products is severely limited. Therefore, under the social background of rapid development of industrialization, a method for replacing the traditional separation means needs to be solved urgently.
At present, the membrane separation technology has the advantages of flexible operation, small occupied area, large operable area, low energy consumption, high separation efficiency, no phase change or chemical change in the operation process and the like, and becomes the most promising alternative separation technology at present. The technology is a process of selectively separating and purifying a system to be separated by using membrane materials with channels or mass transfer holes with different sizes under the condition of concentration gradient or external driving force.
Currently, the film materials are mainly classified into organic films and inorganic films, and the organic films are most widely applied in the field of commercialization due to the advantage of low price, but the corrosion resistance of the materials is poor. Compared with the inorganic film, the inorganic film has better corrosion resistance, but the cost is higher, and the preparation process is not comparable to an organic film system which can be continuously prepared. The currently emerging two-dimensional membranes have a nanoscale thickness, a centimeter-scale size and excellent separation efficiency, and are gradually exposed in the industrialized process. At present, the preparation method of the two-dimensional membrane mainly adopts vacuum-assisted suction filtration, and the requirement of large-scale continuous industrial preparation is severely limited.
Disclosure of Invention
In order to overcome the defects and shortcomings of the prior art and realize continuous production of two-dimensional film preparation, the invention aims to provide a two-dimensional film continuous production process and equipment based on an electrophoresis strategy.
The technical scheme for solving the technical problems is as follows:
a two-dimensional film continuous production process based on an electrophoresis strategy is characterized by comprising the following steps:
(1) the porous substrate is convoluted on a reel and is connected in sequence to enable the porous substrate to pass through an electrodeposition tank and a dryer in sequence;
(2) dispersing the two-dimensional nanosheets in a solvent to obtain a two-dimensional nanosheet solution;
(3) and (3) placing the two-dimensional nanosheet solution obtained in the step (2) in an electrodeposition tank, carrying out electrophoretic deposition on the porous substrate, drying the porous substrate by using a dryer, and carrying out convolution by using a scroll to collect a two-dimensional film so as to obtain the two-dimensional film.
Preferably, the porous substrate is a substrate with good uniform conductivity, the pore diameter of the porous substrate is 1 nm-10 μm, and the thickness of the porous substrate is 1 μm-250 μm.
Preferably, the two-dimensional nanosheets are two-dimensional nanosheet material having charged properties; further preferably, the two-dimensional nanosheet material with charged properties is MXene, 2D-MOF, 2D-COF, 2D-TDMs, 2D-MoS22D-molecular sieve, 2D-silylene, 2D-phospholene, 2D-boron nitride, 2D-C3N4、2D-WS2One kind of (1).
Preferably, the solvent in step (2) is an aqueous solvent or an organic solvent; further preferably, the aqueous solvent is pure water or a salt solution, and the organic solvent is one or more of ethanol, methanol, isopropanol, DMF and DMSO.
Preferably, the pH of the two-dimensional nanosheet solution in the step (2) is 2-14.
Preferably, in the step (3), the voltage of the electrophoretic deposition is 1-48V, the current of the electrophoretic deposition is 1-30 mA, and the time of the electrophoretic deposition is 1S-1 h. Setting according to different two-dimensional nanosheet solution systems.
Preferably, the convolution speed of the scroll in the step (3) is 1 rpm-365 rpm; the adjustment is made according to the deposition time of different two-dimensional materials.
Preferably, the temperature of the dryer in the step (3) is 25-250 ℃; and the adjustment is carried out according to the properties and the system of the dried two-dimensional film.
Preferably, in order to improve the bonding force between the substrate and the two-dimensional membrane, the porous substrate material in step (1) may be pretreated with an acid, an alkali, a surfactant, and a cross-linking agent according to the properties of the two-dimensional membrane.
The apparatus for the continuous production process of the two-dimensional film based on the electrophoresis strategy is shown in fig. 1, and comprises: a first reel 1-1, a second reel 1-2, a third reel 1-3, a fourth reel 1-4, an electrodeposition bath 3, a conductive plate 4, a dryer 5;
the first reel 1-1, the second reel 1-2, the third reel 1-3 and the fourth reel 1-4 are connected with the porous substrate 2, and the porous substrate 2 is made to pass through an electrodeposition tank 3 and a dryer 5 in sequence;
the first scroll 1-1, the second scroll 1-2, the third scroll 1-3, the fourth scroll 1-4 are connected with one pole of a power supply to be used as working electrodes, the conductive plate 4 is arranged in the electrodeposition tank 3, and the conductive plate 4 is connected with the other side of the power supply to be used as a counter electrode.
Preferably, the conductive plate 4 is placed at the bottom of the electrodeposition bath 3, and the conductive plate 4 is a uniformly conductive plate.
Preferably, the porous substrate 2 is uniformly convoluted on a first reel 1-1, passes through an electrodeposition bath 3 and a dryer 4, and is collected by convolution on a reel 1-4.
Compared with the prior art, the invention has the following advantages and beneficial effects:
1. the method is based on an electrophoresis mode to quickly form the film, and combines a roll-to-roll method and an electrophoresis technology for the first time to quickly prepare the two-dimensional film.
2. Compared with the traditional suction filtration, the process has higher film forming speed and has the advantage of continuous preparation compared with a single electrodeposition method.
Drawings
FIG. 1 is a schematic view of the apparatus.
Detailed Description
The present invention is described in further detail with reference to examples, but the embodiments and the scope of the present invention are not limited thereto.
Example 1
An apparatus for a two-dimensional film continuous production process based on an electrophoresis strategy,
the apparatus used is shown in fig. 1 and comprises:
a first reel 1-1, a second reel 1-2, a third reel 1-3, a fourth reel 1-4, an electrodeposition bath 3, a conductive plate 4, a dryer 5;
wherein, a first scroll 1-1, a second scroll 1-2, a third scroll 1-3, a fourth scroll 1-4 are connected with the porous substrate 2, and the porous substrate 2 is made to pass through an electrodeposition tank 3 and a dryer 5 in sequence;
the first scroll 1-1, the second scroll 1-2, the third scroll 1-3, the fourth scroll 1-4 and the power supply one pole connected as the working electrode, the conductive plate 4 is placed at the bottom of the electrodeposition tank 3, the conductive plate 4 is a uniform conductive plate, the conductive plate 4 is connected with the other side of the power supply as the counter electrode.
Example 2
A two-dimensional film continuous production process based on an electrophoresis strategy,
the apparatus of example 1 was used, comprising the following steps:
step 1, connecting all reels with electrodes, fixedly connecting and convoluting a stainless steel mesh (2500 meshes) porous substrate with the average pore diameter of 0.25 mu m and the thickness of 2 mu m on a first reel 1-1 through conductive adhesive, and enabling the porous substrate to pass through an electrodeposition tank 3 and a dryer 5 through a second reel 1-2, a third reel 1-3 and a fourth reel 1-4; the overlapping size of the adjacently deposited porous substrates is controlled to be within 0.5 cm. The conductive paste is used to connect the substrates to each other to facilitate uniform deposition of the two-dimensional film on the substrates during the electro-deposition process.
And 3, setting the temperature of the dryer to 80 ℃, and ensuring that the film can be completely dried at the current reel rotating speed.
And 4, collecting the dried film by a 1-4 reel to obtain the final two-dimensional film coiled material.
Compared with the traditional suction filtration, the electrodeposition can quickly form a film within 2min to reach the same thickness of the film obtained by the suction filtration method, and the time for frequently replacing the substrate material is saved after the electrodeposition is combined with a roll-to-roll process, so that the time can be saved by more than 60 percent compared with the film formed by single electrodeposition.
In a more specific embodiment of the present invention, the pretreatment process of the substrate and the electrodeposition solution in step 1 is: and sequentially placing the substrate into dilute hydrochloric acid or dilute sodium hydroxide, absolute ethyl alcohol and deionized water, respectively soaking and carrying out ultrasonic treatment for 5-10 min, airing, uniformly curling on a scroll, and connecting by using a conductive adhesive. Dispersing two-dimensional nanosheet powder in deionized water, and performing ultrasonic treatment for 6 h.
When the binding force between the substrate and the two-dimensional film is smaller than the friction force applied to the substrate by the scroll, the scroll drives the copper foil to rotate together, the process can better keep the integrity of the loaded two-dimensional film coiled material, and prevent cracks from generating in the rolling collection process to influence the film thickness.
The above description is only for the purpose of illustrating the preferred embodiments of the present invention and is not to be construed as limiting the invention, and any modifications, equivalents, improvements and the like that fall within the spirit and principle of the present invention are intended to be included therein.
Claims (10)
1. A two-dimensional film continuous production process based on an electrophoresis strategy is characterized by comprising the following steps:
(1) the porous substrate is convoluted on a reel and is connected in sequence to enable the porous substrate to pass through an electrodeposition tank and a dryer in sequence;
(2) dispersing the two-dimensional nanosheets in a solvent to obtain a two-dimensional nanosheet solution;
(3) and (3) placing the two-dimensional nanosheet solution obtained in the step (2) in an electrodeposition tank, carrying out electrophoretic deposition on the porous substrate, drying the porous substrate by using a dryer, and carrying out convolution by using a scroll to collect a two-dimensional film so as to obtain the two-dimensional film.
2. The continuous production process of two-dimensional membrane based on electrophoresis strategy as claimed in claim 1, wherein the porous substrate in step (1) is a substrate with good uniform conductivity, the pore diameter of the porous substrate is 1 nm-10 μm, and the thickness of the porous substrate is 1 μm-250 μm.
3. The electrophoresis strategy-based two-dimensional film continuous production process according to claim 1, wherein in the step (2), the two-dimensional nanosheets are two-dimensional nanosheet materials with charged properties.
4. The continuous production process of two-dimensional film based on electrophoresis strategy as claimed in claim 3, wherein the two-dimensional nanoplatelets with charged property are MXene, 2D-MOF, 2D-COF, 2D-TDMs, 2D-MoS22D-molecular sieve, 2D-silylene, 2D-phospholene, 2D-boron nitride, 2D-C3N4、2D-WS2One kind of (1).
5. The two-dimensional membrane continuous production process based on electrophoresis strategy as claimed in claim 1, wherein the solvent in step (2) is water solvent or organic solvent.
6. The two-dimensional membrane continuous production process based on the electrophoresis strategy as claimed in claim 5, wherein the aqueous solvent is pure water or a salt solution, and the organic solvent is one or more of ethanol, methanol, isopropanol, DMF, and DMSO.
7. The continuous production process of two-dimensional film based on electrophoresis strategy as claimed in claim 1, wherein in step (3), the voltage of the electrophoretic deposition is 1-48V, the current of the electrophoretic deposition is 1-30 mA, and the time of the electrophoretic deposition is 1S-1 h.
8. The continuous production process of two-dimensional film based on electrophoresis strategy as claimed in claim 1, wherein the convolution speed of the scroll in step (3) is 1-365 rpm.
9. The continuous production process of two-dimensional film based on electrophoresis strategy as claimed in claim 1, wherein the temperature of the dryer in step (3) is 25-250 ℃.
10. The apparatus for the continuous production process of two-dimensional film based on electrophoresis strategy according to any claim 1-9, characterized by comprising: the device comprises a first reel, a second reel, a third reel, a fourth reel, an electrodeposition tank, a conductive plate and a dryer;
the first reel, the second reel, the third reel and the fourth reel are connected with the porous substrate, and the porous substrate is enabled to pass through an electrodeposition tank and a dryer in sequence;
the first scroll, the second scroll, the third scroll and the fourth scroll are connected with one pole of a power supply to be used as working electrodes, the conductive plate is arranged in the electro-deposition tank, and the conductive plate is connected with the other side of the power supply to be used as a counter electrode.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202011541089.4A CN112808018A (en) | 2020-12-23 | 2020-12-23 | Two-dimensional film continuous production process and equipment based on electrophoresis strategy |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202011541089.4A CN112808018A (en) | 2020-12-23 | 2020-12-23 | Two-dimensional film continuous production process and equipment based on electrophoresis strategy |
Publications (1)
Publication Number | Publication Date |
---|---|
CN112808018A true CN112808018A (en) | 2021-05-18 |
Family
ID=75853678
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN202011541089.4A Pending CN112808018A (en) | 2020-12-23 | 2020-12-23 | Two-dimensional film continuous production process and equipment based on electrophoresis strategy |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN112808018A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN114522543A (en) * | 2022-01-19 | 2022-05-24 | 华南理工大学 | Ultrathin two-dimensional Cu-TCPP film and preparation method thereof |
CN114534509A (en) * | 2022-01-19 | 2022-05-27 | 华南理工大学 | Two-dimensional metal organic framework film and electrophoretic deposition preparation method thereof |
CN114592197A (en) * | 2022-01-20 | 2022-06-07 | 华南理工大学 | Two-dimensional g-C3N4Nano-sheet membrane, electrochemical preparation method thereof and application thereof in ion separation |
Citations (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6887361B1 (en) * | 2001-03-22 | 2005-05-03 | The Regents Of The University Of California | Method for making thin-film ceramic membrane on non-shrinking continuous or porous substrates by electrophoretic deposition |
CN1905215A (en) * | 2005-07-26 | 2007-01-31 | 中国科学院化学研究所 | Process for preparing TiO2 nanocrystal porous film electrode by low-temp. electrophoresis sedimentation |
CN205044040U (en) * | 2015-09-25 | 2016-02-24 | 惠州易晖能源科技股份有限公司 | Volume to volume dip plating membrane system |
CN106669432A (en) * | 2016-12-20 | 2017-05-17 | 华南理工大学 | Method for preparing metal organic framework membrane by utilizing stainless steel mesh modified by electro-deposition method |
CN107689401A (en) * | 2017-09-14 | 2018-02-13 | 旭科新能源股份有限公司 | A kind of volume to volume package system and method for flexible thin-film solar cell |
CN208406652U (en) * | 2017-10-17 | 2019-01-22 | 深圳市科源光科技有限公司 | A kind of polymeric membrane for separation automatic assembly line |
CN109603569A (en) * | 2019-01-14 | 2019-04-12 | 北京化工大学 | The film forming apparatus and method for the composite membrane that continuous preparative separation layer is PDMS |
CN109666964A (en) * | 2019-01-16 | 2019-04-23 | 华南理工大学 | A kind of method that electrophoretic deposition quickly prepares two-dimentional MXene film |
CN109701397A (en) * | 2019-01-16 | 2019-05-03 | 华南理工大学 | A kind of application of the two-dimentional MXene film of electrophoretic deposition preparation in ion rejection |
CN110451671A (en) * | 2019-08-22 | 2019-11-15 | 北京正和顺汽车部件有限公司 | The self-circulating water processing unit of electrophoretic painting |
CN111041542A (en) * | 2019-11-22 | 2020-04-21 | 上海交通大学 | Composite metal wire with composite electroplated nano carbon metal film and preparation method thereof |
CN111675210A (en) * | 2020-07-07 | 2020-09-18 | 北京石墨烯技术研究院有限公司 | Graphene production system |
-
2020
- 2020-12-23 CN CN202011541089.4A patent/CN112808018A/en active Pending
Patent Citations (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6887361B1 (en) * | 2001-03-22 | 2005-05-03 | The Regents Of The University Of California | Method for making thin-film ceramic membrane on non-shrinking continuous or porous substrates by electrophoretic deposition |
CN1905215A (en) * | 2005-07-26 | 2007-01-31 | 中国科学院化学研究所 | Process for preparing TiO2 nanocrystal porous film electrode by low-temp. electrophoresis sedimentation |
CN205044040U (en) * | 2015-09-25 | 2016-02-24 | 惠州易晖能源科技股份有限公司 | Volume to volume dip plating membrane system |
CN106669432A (en) * | 2016-12-20 | 2017-05-17 | 华南理工大学 | Method for preparing metal organic framework membrane by utilizing stainless steel mesh modified by electro-deposition method |
CN107689401A (en) * | 2017-09-14 | 2018-02-13 | 旭科新能源股份有限公司 | A kind of volume to volume package system and method for flexible thin-film solar cell |
CN208406652U (en) * | 2017-10-17 | 2019-01-22 | 深圳市科源光科技有限公司 | A kind of polymeric membrane for separation automatic assembly line |
CN109603569A (en) * | 2019-01-14 | 2019-04-12 | 北京化工大学 | The film forming apparatus and method for the composite membrane that continuous preparative separation layer is PDMS |
CN109666964A (en) * | 2019-01-16 | 2019-04-23 | 华南理工大学 | A kind of method that electrophoretic deposition quickly prepares two-dimentional MXene film |
CN109701397A (en) * | 2019-01-16 | 2019-05-03 | 华南理工大学 | A kind of application of the two-dimentional MXene film of electrophoretic deposition preparation in ion rejection |
CN110451671A (en) * | 2019-08-22 | 2019-11-15 | 北京正和顺汽车部件有限公司 | The self-circulating water processing unit of electrophoretic painting |
CN111041542A (en) * | 2019-11-22 | 2020-04-21 | 上海交通大学 | Composite metal wire with composite electroplated nano carbon metal film and preparation method thereof |
CN111675210A (en) * | 2020-07-07 | 2020-09-18 | 北京石墨烯技术研究院有限公司 | Graphene production system |
Non-Patent Citations (2)
Title |
---|
JUNJIE DENG: "Fast electrophoretic preparation of large-area two-dimensional titanium carbide membranes for ion sieving", 《CHEMICAL ENGINEERING JOURNAL》 * |
王湛: "《膜分离技术基础》", 30 June 2006, 北京化学工业出版社 * |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN114522543A (en) * | 2022-01-19 | 2022-05-24 | 华南理工大学 | Ultrathin two-dimensional Cu-TCPP film and preparation method thereof |
CN114534509A (en) * | 2022-01-19 | 2022-05-27 | 华南理工大学 | Two-dimensional metal organic framework film and electrophoretic deposition preparation method thereof |
CN114592197A (en) * | 2022-01-20 | 2022-06-07 | 华南理工大学 | Two-dimensional g-C3N4Nano-sheet membrane, electrochemical preparation method thereof and application thereof in ion separation |
CN114592197B (en) * | 2022-01-20 | 2024-01-12 | 华南理工大学 | Two-dimensional g-C 3 N 4 Nanosheet film, electrochemical preparation method thereof and application of nanosheet film in ion separation |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN112808018A (en) | Two-dimensional film continuous production process and equipment based on electrophoresis strategy | |
CN105883781B (en) | A kind of preparation method of large area redox graphene film | |
CN103897093B (en) | Graphene/polymkeric substance composite aquogel film and preparation method thereof | |
CN112435867B (en) | Preparation method of flexible self-supporting MXene/CuS supercapacitor electrode material | |
CN113457448B (en) | Preparation method of double-layer MXene film based on different interlayer distances | |
CN106245104A (en) | A kind of method preparing Graphene based on electrochemical process stripping dual graphite electrodes | |
CN109824043B (en) | Method for improving speed of bubbling transfer of graphene by regulating flexibility of transfer medium layer | |
CN105719852A (en) | Preparation method for three-dimensional nano-porous graphene/manganese dioxide composite electrode material | |
CN107221447B (en) | A kind of graphene flexible compound electrode, preparation method and flexible super capacitor | |
CN106548877A (en) | Carbon nano pipe array/polyaniline/ceria composite electrode and its preparation method and application | |
CN112421017B (en) | Preparation method of binder-free water-based zinc ion battery positive electrode composite material | |
CN104961124A (en) | Method for manufacturing graphene paper | |
CN110380058A (en) | A kind of flexible current-collecting body and its preparation method and application | |
CN111217361B (en) | Method for preparing graphene nanosheet through electrochemical cathode stripping | |
CN109019686A (en) | A kind of preparation method and application of airsetting glue vanadium disulfide nano material | |
CN110808180B (en) | Preparation method of miniature asymmetric super capacitor, miniature asymmetric super capacitor and application thereof | |
CN105702935A (en) | Preparation method of multilayer anode with porous carbon composite material | |
CN105551834B (en) | Low-temperature and low-pressure preparation method of flexible dye-sensitized solar cell | |
CN107104001A (en) | A kind of method for improving specific capacitance in graphenic surface adsorption of hydrolyzation polyimide molecule | |
CN109772179B (en) | Method for preparing film by utilizing electrodeposition cobalt hydroxide nanosheet | |
CN109036877B (en) | Preparation method of porous graphene/transition metal chalcogenide film | |
CN107946079B (en) | Preparation of flexible full-printing quantum dot sensitized solar cell | |
CN108039290A (en) | A kind of method that electrode of super capacitor is prepared based on volume to volume printing technology | |
CN109346333A (en) | A kind of preparation method of carbon/glass fabric electrode of super capacitor | |
CN107665996A (en) | Three-dimensional porous nickel doughnut electrode material, preparation method and the battery based on the electrode |
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 |