CN205043171U - Industrial production system of liquid phase nanometer elargol body - Google Patents
Industrial production system of liquid phase nanometer elargol body Download PDFInfo
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- CN205043171U CN205043171U CN201520799842.8U CN201520799842U CN205043171U CN 205043171 U CN205043171 U CN 205043171U CN 201520799842 U CN201520799842 U CN 201520799842U CN 205043171 U CN205043171 U CN 205043171U
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Abstract
The utility model discloses an industrial production system of liquid phase nanometer elargol body, always control unit, the automatic ratio unit of solvent, automatic unit, the solvent self -heating unit of stirring of solvent including the computer, wherein, the automatic ratio unit of solvent includes the solvent memory, and the solvent memory divide into four at least solvent memory areas, and every solvent memory area is provided with controller I, solvent outflow passageway, sets up flowmeter and control switch on solvent outflow passageway, and flowmeter and control switch are connected with controller I respectively, automatically, stir the unit includes controller II, motor, stirring rod, agitator to the solvent, solvent self -heating unit includes solvent ratios container, container self -heating system, heating system controller unit, the unit connection is all always controlled with the computer to controller I, controller II, heating system controller unit. The utility model discloses making nanometer silvering solution body ratio process convenient and fast more, having saved the cost of labor, degree of automation is high.
Description
Technical field
The utility model relates to suitability for industrialized production system, is applied in the suitability for industrialized production of liquid phase nano silver colloid, is specifically related to a kind of suitability for industrialized production system of liquid phase nano silver colloid.
Background technology
Nanometer technology is the technology studied character and the application of material in nano-scale range and process.1 nanometer equals 10
-9rice.Mainly study in the world and explore between the material of 0.1 nanometer to 100 nanometers.Nanometer technology has been widely used in medicine, comprises pharmaceutical carrier, cell dyeing, cell separation, clinical diagnosis and sterilizing.
Metal comprises silver, copper, mercury, zinc all have anti-microbial property.Family dependents of military personel in the liberated areas's property can not be obtained by the bacterium of these metal process, Nano Silver belongs to metal nano material, because it has very large surface area, so have very high surface energy, surface-active and good catalytic performance, in existing technology, liquid phase nano silver colloid solvent is produced out, but preparing the preparation technology in nano silver colloid dissolving agent process normally by manually completing, automaticity is not high, so not only lost labor's cost, and in the process preparing solvent, the proportioning of the amount of each composition may have deviation.
Utility model content
The technical problems to be solved in the utility model is the suitability for industrialized production system providing a kind of liquid phase nano silver colloid, realizes the automation preparation of nano silver colloid, saves cost of labor, avoid manually preparing the deviation that in the process of solvent, each composition of proportioning may cause.
For solving the problems of the technologies described above, the utility model by the following technical solutions:
A suitability for industrialized production system for liquid phase nano silver colloid, comprises computer Master Control Unit, solvent automatic mixing unit, solvent automatic stirring unit, solvent Automatic-heating unit;
Wherein, described solvent automatic mixing unit comprises solvent memory, described solvent memory is divided at least four for storing the solvent memory block of different solvents, each solvent memory block is provided with controller I, solvent flow pass, the flowmeter be arranged on solvent flow pass, the gauge tap be arranged on solvent flow pass, described flowmeter and gauge tap are connected with controller I respectively, and controller I is connected with computer Master Control Unit;
Described solvent automatic stirring unit comprises controller II, the motor be connected with controller II, the stirring rod be connected with motor, is connected to the agitator of described stirring rod end, and described controller II is connected with computer Master Control Unit;
Described solvent Automatic-heating unit comprises solvent burden ratio container, container automatic heating system, the heating-system-controller unit that is connected with container automatic heating system, and described heating-system-controller unit is also connected with computer Master Control Unit.
The suitability for industrialized production system of liquid phase nano silver colloid, also comprises the vertical supporting frame being fixed on solvent burden ratio container both sides, and to be positioned at above solvent burden ratio container and to connect the cross-brace frame on the top of described both sides vertical supporting frame; Described solvent automatic mixing unit and solvent automatic stirring unit are all fixed on the cross-brace frame that is positioned at above solvent burden ratio container.
Described vertical supporting frame is by the liftable bracing frame of lifting controller unit controls, and described lifting controller unit is connected with computer Master Control Unit.
Described solvent burden ratio container is placed on ground or work top by pad.
The agitator of solvent automatic stirring unit vertically to stretch in solvent burden ratio container and is positioned at the central authorities of solvent burden ratio container.
Described stirring rod adopts cylindrical glass stirring rod.
Agitator adopts circular glass to stir cutterhead.
Container automatic heating system comprises and is arranged on temperature sensor on solvent burden ratio container and electric heater, and described temperature sensor and electric heater are connected with heating-system-controller unit respectively.
The utility model is being prepared in nano silver colloid dissolving agent process without the need to by manually completing preparation technology, avoid the deviation manually prepared each composition of proportioning in dissolving agent process and may cause, make Nano Silver liquid proportion process more convenient, save cost of labor, and automaticity is high; The vertical supporting bar of solvent memory block is Collapsible structure simultaneously, can, according to the height of the size adjustment solvent memory block of solvent burden ratio container, be a kind of innovative intelligent nano silver colloid preparation system; Follow-up laser particle size analyzer (LPSA), ultraviolet-visible absorption spectroscopy instrument (UV-V), transmission electron microscope (TEM), X-ray diffraction (LPSA), the infrared spectrum (FTIR) etc. of carrying out can be facilitated to carry out analyzing and measuring.
Accompanying drawing explanation
Fig. 1 is schematic block circuit diagram of the present utility model.
Fig. 2 is structural representation of the present utility model.
Detailed description of the invention
Below in conjunction with the drawings and specific embodiments, the utility model is described in further detail.
See Fig. 1 and Fig. 2, the suitability for industrialized production system of a kind of liquid phase nano silver colloid of the present embodiment, comprises computer Master Control Unit 14, solvent automatic mixing unit, solvent automatic stirring unit, solvent Automatic-heating unit; Wherein:
Computer Master Control Unit 14 adopts industrial computer or PC.
Solvent automatic mixing unit comprises solvent memory 1, and described solvent memory 1 is divided into four order arrangements and solvent memory block for storing different solvents: A district, B district, D district, E district; Each solvent memory block is provided with controller unit I 2,3,5,6, solvent flow pass 7,8,9,10, and be arranged on the flowmeter on solvent flow pass 7,8,9,10, the gauge tap be arranged on solvent flow pass 7,8,9,10, described flowmeter and gauge tap are connected with controller unit I 2,3,5,6 respectively, and controller unit I 2,3,5,6 is connected with computer Master Control Unit 14.
Solvent automatic stirring unit, be arranged between the B district of solvent memory block and D district, comprise controller unit II 4, the motor be connected with controller unit II 4, the cylindrical stirring rod 11 be connected with motor, the circular glass that is connected to described stirring rod 11 end stir cutterhead 12, described controller unit II 4 is connected with computer Master Control Unit 14.The stirring cutterhead 12 of solvent automatic stirring unit vertically to stretch in solvent burden ratio container 15 and is positioned at the central authorities of solvent burden ratio container 15.
Solvent Automatic-heating unit comprises solvent burden ratio container 15, container automatic heating system, the heating-system-controller unit 13 that is connected with container automatic heating system, and described heating-system-controller unit 13 is connected with computer Master Control Unit 14.Container automatic heating system comprises and is arranged on temperature sensor on solvent burden ratio container 15 and electric heater, and temperature sensor and electric heater are all connected with heating-system-controller unit 13; The real time temperature of solution in temperature sensor Real-Time Monitoring solvent burden ratio container 15, energising and the power-off of electric heater is controlled by heating-system-controller unit 13, realize the adjustment of temperature, simultaneous computer Master Control Unit 14 can show the temperature information that heating-system-controller unit 13 feeds back.
Solvent automatic mixing unit and solvent automatic stirring unit are all fixed on the cross-brace frame 17 that is positioned at above solvent burden ratio container 15, and cross-brace frame 17 is connected with the top of the vertical supporting frame 18,19 being fixed on solvent burden ratio container 15 both sides.Described vertical supporting frame 18,19 is that lifting controller unit is connected with computer Master Control Unit 14 by the liftable bracing frame of lifting controller unit controls, liftable bracing frame be embodied as prior art, drive lifting by hydraulic-driven or motor.Solvent burden ratio container 15 is placed on ground or work top by pad 16.
Operation principle of the present utility model:
Solvent manning inputs the amount of the required each solvent be equipped with to computer Master Control Unit 14, by computer Master Control Unit 14 by signal transmission to each solvent memory block of solvent burden ratio unit: A district, B district, D district, the controller I 2 that E district is arranged, 3, 5, 6, controller unit I 2, 3, 5, 6 according to the different order from the signal received by computer Master Control Unit 14, open each solvent flow pass 7, 8, 9, gauge tap on 10, controller unit I 2, 3, 5, 6 receive flow meter signal, control the opening and closing of gauge tap on coordinative solvent flow pass, the corresponding solvent that each solvent memory block is released adds in solvent burden ratio container 15, realize the accurate control of dosage, complete solution ratio.The controller unit II 4 of solvent automatic stirring unit drives according to the signal control motor received from computer Master Control Unit 14 and stirs cutterhead 12 fast rotational, is fully mixed by solution.By container automatic heating system, the solution in solvent burden ratio container 15 is heated receive the instruction of computer Master Control Unit 14 at heating-system-controller unit 13 after.Liftable bracing frame 18,19 can according to required configuration quantity of solvent number and the size of solvent burden ratio container 15, regulated the height of the position of the solvent memory 1 be positioned on cross-brace frame 17 by the instruction of lifting controller unit receiving computer Master Control Unit 14.Schematic block circuit diagram of the present utility model as shown in Figure 1.The utility model process operation simple and fast, solution ratio accuracy is high, automaticity is high, and facilitates follow-up laser particle size analyzer (LPSA), uv-visible absorption spectra instrument (UV-V), transmission electron microscope (TEM), X-ray diffraction (LPSA), the infrared spectrum (FTIR) etc. of carrying out to carry out analyzing and measuring.
Claims (8)
1. a suitability for industrialized production system for liquid phase nano silver colloid, is characterized in that: comprise computer Master Control Unit, solvent automatic mixing unit, solvent automatic stirring unit, solvent Automatic-heating unit;
Wherein, described solvent automatic mixing unit comprises solvent memory, described solvent memory is divided at least four for storing the solvent memory block of different solvents, each solvent memory block is provided with controller I, solvent flow pass, the flowmeter be arranged on solvent flow pass, the gauge tap be arranged on solvent flow pass, described flowmeter and gauge tap are connected with controller I respectively, and controller I is connected with computer Master Control Unit;
Described solvent automatic stirring unit comprises controller II, the motor be connected with controller II, the stirring rod be connected with motor, is connected to the agitator of described stirring rod end, and described controller II is connected with computer Master Control Unit;
Described solvent Automatic-heating unit comprises solvent burden ratio container, container automatic heating system, the heating-system-controller unit that is connected with container automatic heating system, and described heating-system-controller unit is also connected with computer Master Control Unit.
2. the suitability for industrialized production system of liquid phase nano silver colloid according to claim 1, it is characterized in that: also comprise the vertical supporting frame being fixed on solvent burden ratio container both sides, and to be positioned at above solvent burden ratio container and to connect the cross-brace frame on the top of described both sides vertical supporting frame; Described solvent automatic mixing unit and solvent automatic stirring unit are all fixed on the cross-brace frame that is positioned at above solvent burden ratio container.
3. the suitability for industrialized production system of liquid phase nano silver colloid according to claim 2, is characterized in that: described vertical supporting frame is by the liftable bracing frame of lifting controller unit controls, and described lifting controller unit is connected with computer Master Control Unit.
4. the suitability for industrialized production system of liquid phase nano silver colloid according to claim 1 and 2, is characterized in that: described solvent burden ratio container is placed on ground or work top by pad.
5. the suitability for industrialized production system of liquid phase nano silver colloid according to claim 1, is characterized in that: the agitator of solvent automatic stirring unit vertically to stretch in solvent burden ratio container and is positioned at the central authorities of solvent burden ratio container.
6. the suitability for industrialized production system of liquid phase nano silver colloid according to claim 1, is characterized in that: described stirring rod adopts cylindrical glass stirring rod.
7. the suitability for industrialized production system of liquid phase nano silver colloid according to claim 1 or 5, is characterized in that: agitator adopts circular glass to stir cutterhead.
8. the suitability for industrialized production system of liquid phase nano silver colloid according to claim 1, it is characterized in that: container automatic heating system comprises and is arranged on temperature sensor on solvent burden ratio container and electric heater, and described temperature sensor and electric heater are connected with heating-system-controller unit respectively.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520799842.8U CN205043171U (en) | 2015-10-16 | 2015-10-16 | Industrial production system of liquid phase nanometer elargol body |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520799842.8U CN205043171U (en) | 2015-10-16 | 2015-10-16 | Industrial production system of liquid phase nanometer elargol body |
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| Publication Number | Publication Date |
|---|---|
| CN205043171U true CN205043171U (en) | 2016-02-24 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520799842.8U Expired - Fee Related CN205043171U (en) | 2015-10-16 | 2015-10-16 | Industrial production system of liquid phase nanometer elargol body |
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| CN (1) | CN205043171U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106908434A (en) * | 2017-03-20 | 2017-06-30 | 上海镭立激光科技有限公司 | Using the device of ultraviolet Raman spectrometer real-time control spherical silver powder preparation process |
-
2015
- 2015-10-16 CN CN201520799842.8U patent/CN205043171U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106908434A (en) * | 2017-03-20 | 2017-06-30 | 上海镭立激光科技有限公司 | Using the device of ultraviolet Raman spectrometer real-time control spherical silver powder preparation process |
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| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160224 Termination date: 20161016 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |