CN115282909A - Production device and method of anion essence - Google Patents
Production device and method of anion essence Download PDFInfo
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- CN115282909A CN115282909A CN202210932623.7A CN202210932623A CN115282909A CN 115282909 A CN115282909 A CN 115282909A CN 202210932623 A CN202210932623 A CN 202210932623A CN 115282909 A CN115282909 A CN 115282909A
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- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/18—Stationary reactors having moving elements inside
- B01J19/1862—Stationary reactors having moving elements inside placed in series
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
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Abstract
The invention provides a device and a method for producing negative ion essence, and relates to the technical field of essence production. Mineral powder is conveyed into a first reaction component for reaction through a powder groove and a belt or pumping equipment arranged in the powder groove; the pumping equipment arranged here is a delivery pump, and then the powder is fully stirred with other substances by the first reaction component and then is transferred into the second reaction component by the pumping equipment to react.
Description
Technical Field
The invention relates to the technical field of essence production, in particular to a device and a method for producing negative ion essence.
Background
Essence is one of paints that can be applied firmly to the surface of an object to protect, decorate, mark, and other special purpose chemical mixture paints. The book of coating technology which is relatively authoritative in the Chinese coating world is defined as follows: the paint is a material which can be coated on the surface of an object by different construction processes to form a continuous solid film with firm adhesion and certain strength. The film thus formed is generally called a coating film, also called a paint film or a coating. The paint is composed of film forming matter, filler (pigment and filler), solvent and assistant. The components may be slightly changed according to the performance requirements, for example, the varnish has no pigment and filler, and the powder coating can have no solvent.
The production of the essence needs five steps of proportioning, dissolving, dispersing, inspecting and packaging, wherein the proportioning and the dispersing belong to the final essential link, and if the proportion of the proportioning is not accurate, the dispersing effect is not good, so that the quality of the essence is influenced to a great extent.
Dispersion process in the essence production must pack paint vehicle, pigment and can the even stirring, so could obtain high-quality essence, and present agitating unit passes through simple rapid mixing that carries on of puddler, and mixing efficiency is slow, and essence mixing quality can not be ensured moreover.
Disclosure of Invention
The invention aims to provide a production device of anion essence, which can rapidly mix and stir the essence for many times and ensure the dispersion quality of the essence.
The embodiment of the invention is realized by the following steps:
the embodiment of the application provides a production device of anion essence, including powder groove, first reaction unit and second reaction unit, the powder groove with first reaction unit's input intercommunication, first reaction unit's output with second reaction unit's input intercommunication, second reaction unit's output intercommunication has filling equipment.
In some embodiments of the present invention, the first reaction assembly includes a first tank, a high temperature reaction assembly, and a filter, a first stirring assembly is installed at the top of the first tank, an output shaft of the first stirring assembly penetrates through the first tank, a first stirring portion is disposed on the output shaft of the first stirring assembly, and the first tank, the high temperature reaction assembly, and the filter are sequentially communicated and then communicated with an input end of the second reaction assembly.
In some embodiments of the present invention, the number of the first reaction assemblies is two, and the two first reaction assemblies are arranged in parallel, and the filter in any one of the first reaction assemblies is communicated with the first tank in the other first reaction assembly, and the filter in the other first reaction assembly is communicated with the input end of the second reaction assembly.
In some embodiments of the present invention, the second reaction component includes a second tank, a second stirring component is installed at the top of the second tank, an output shaft of the second stirring component penetrates through the second tank, a second stirring portion is arranged on the output shaft of the second stirring component, and the first tank is communicated with the input end of the filling apparatus.
In some embodiments of the invention, the device further comprises two groups of auxiliary material filling assemblies, wherein any one group of auxiliary material filling assemblies is communicated with the first tank body communicated with the powder groove, and the other group of auxiliary material filling assemblies are respectively communicated with the output ends of the filters in the two first reaction assemblies.
In some embodiments of the present invention, the auxiliary material filling assembly includes a filling tank, the filling tank is provided with a pipeline communicated therewith, and the filling tank is provided with a liquid level meter.
In some embodiments of the invention, the filter comprises two filter tubes arranged in pairs, the two filter tubes being in communication with each other.
In some embodiments of the present invention, a sedimentation tank and a light wave sterilization storage tank are sequentially disposed between the second tank and the input end of the filling apparatus.
In some embodiments of the present invention, a diaphragm pump is disposed between the first tank and the high temperature reaction assembly.
A production method of anion essence comprises the steps of putting mineral powder into a powder groove, and conveying the mineral powder into a first tank body in any one first reaction assembly through the powder groove; adding deionized water and a multifunctional auxiliary agent into the first tank body, and starting the first stirring assembly to stir;
pumping the uniformly stirred slurry into a high-temperature reaction room in a first reaction assembly, and performing nano carbonization active primary treatment;
filtering the primarily treated slurry, pumping the filtered slurry into the other first reaction assembly, and simultaneously injecting deionized water for stirring and cooling; then adding plant powder and multifunctional auxiliary agent for stirring;
pumping the uniformly stirred slurry into a high-temperature reaction assembly in the other first reaction assembly, and performing nano carbonization activity deep-level treatment;
filtering the slurry after deep-stage treatment, pumping the filtered slurry into a second tank body, and simultaneously injecting deionized water for stirring and cooling; when the water temperature is reduced, sequentially adding a wetting agent, a bactericide and a defoaming agent and stirring;
after stirring, putting the slurry in the tank body into a sedimentation tank for sedimentation; pumping the precipitated liquid into a storage tank of an optical wave sterilization chamber for optical wave sterilization;
the prepared liquid can be canned after light wave sterilization and disinfection.
Compared with the prior art, the embodiment of the invention has at least the following advantages or beneficial effects:
the embodiment of the application provides a production device of anion essence, including powder groove, first reaction unit and second reaction unit, the powder groove with first reaction unit's input intercommunication, first reaction unit's output with second reaction unit's input intercommunication, second reaction unit's output intercommunication has filling equipment. The production device provided by the technical scheme is mainly used for producing materials rich in plant anions, and can release anions as far as possible from mixed materials rich in anions; the pumping equipment arranged here is a delivery pump, then the first reaction component is used for fully stirring with other substances and then transmitting the mixture into the second reaction component through the pumping equipment for reaction, and the second reaction component is used for fully reacting through the steps and is packaged by filling equipment. After the series of flow operations, the error caused by manual operation can be avoided, the preparation precision of the powder product is improved, and the working efficiency is improved.
A production method of anion essence comprises the steps of putting mineral powder into a powder groove, and conveying the mineral powder into a first tank body in any one first reaction assembly through the powder groove; adding deionized water and a multifunctional auxiliary agent into the first tank body, and starting the first stirring component to stir;
pumping the uniformly stirred slurry into a high-temperature reaction room in a first reaction assembly, and performing nano carbonization active primary treatment;
filtering the primarily treated slurry, pumping the filtered slurry into the other first reaction component, and simultaneously injecting deionized water for stirring and cooling; then adding plant powder and multifunctional auxiliary agent for stirring;
pumping the uniformly stirred slurry into a high-temperature reaction assembly in the other first reaction assembly, and performing nano carbonization activity deep-level treatment;
filtering the slurry after deep-stage treatment, pumping the filtered slurry into a second tank body, and simultaneously injecting deionized water for stirring and cooling; when the water temperature is reduced, sequentially adding a wetting agent, a bactericide and a defoaming agent and stirring;
after stirring, putting the slurry in the tank body into a sedimentation tank for sedimentation; and pumping the precipitated liquid into a storage tank of an optical wave sterilizing room for optical wave sterilization. After the series of flow operations, the error caused by manual operation can be avoided, the preparation precision of the powder product is improved, and the working efficiency is improved.
Drawings
In order to more clearly illustrate the technical solutions of the embodiments of the present invention, the drawings needed to be used in the embodiments will be briefly described below, it should be understood that the following drawings only illustrate some embodiments of the present invention and therefore should not be considered as limiting the scope, and for those skilled in the art, other related drawings can be obtained according to the drawings without inventive efforts.
FIG. 1 is a schematic front view of the present invention;
FIG. 2 is a schematic structural view of a first reaction module according to the present invention;
FIG. 3 is a schematic view of a second reaction module according to the present invention.
Icon: 1. a powder groove; 2. a first reaction assembly; 3. a second reaction assembly; 4. filling equipment; 5. a sedimentation tank; 6. a light wave sterilization storage tank; 7. a filter tube; 8. a liquid level meter; 9. filling the tank; 201. a first stirring assembly; 202. a first tank; 203. a first stirring section; 204. a high temperature reaction assembly; 301. a second stirring assembly; 302. a second tank; 303. a second stirring section.
Detailed Description
In order to make the objects, technical solutions and advantages of the embodiments of the present invention clearer, the technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the drawings in the embodiments of the present invention, and it is obvious that the described embodiments are some, but not all, embodiments of the present invention. The components of embodiments of the present invention generally described and illustrated in the figures herein may be arranged and designed in a wide variety of different configurations.
Thus, the following detailed description of the embodiments of the present invention, presented in the figures, is not intended to limit the scope of the invention, as claimed, but is merely representative of selected embodiments of the invention. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present invention.
It should be noted that: like reference numbers and letters refer to like items in the following figures, and thus, once an item is defined in one figure, it need not be further defined and explained in subsequent figures.
In the description of the embodiments of the present invention, it should be noted that, if the terms "center", "upper", "lower", "left", "right", "vertical", "horizontal", "inner", "outer", etc. indicate an orientation or a positional relationship based on an orientation or a positional relationship shown in the drawings, or an orientation or a positional relationship which is usually arranged when the product of the present invention is used, it is only for convenience of description and simplification of the description, but does not indicate or imply that the device or the element referred to must have a specific orientation, be constructed and operated in a specific orientation, and thus, should not be construed as limiting the present invention.
Furthermore, the terms "horizontal", "vertical", "overhang" and the like do not require that the components be absolutely horizontal or overhang, but may be slightly inclined. For example, "horizontal" merely means that the direction is more horizontal than "vertical" and does not mean that the structure must be perfectly horizontal, but may be slightly inclined.
In the description of the embodiments of the present invention, "a plurality" represents at least 2.
In the description of the embodiments of the present invention, it should be further noted that unless otherwise explicitly stated or limited, the terms "disposed," "mounted," "connected," and "connected" should be interpreted broadly, and may be, for example, fixedly connected, detachably connected, or integrally connected; can be mechanically or electrically connected; they may be connected directly or indirectly through intervening media, or they may be interconnected between two elements. The specific meanings of the above terms in the present invention can be understood by those skilled in the art according to specific situations.
Examples
Referring to fig. 1-3, fig. 1 is a schematic front view of the present invention; FIG. 2 is a schematic structural view of a first reaction module 2 according to the present invention; FIG. 3 is a schematic view of the second reaction unit 3 according to the present invention.
The embodiment of the application provides a production device of anion essence, including powder groove 1, first reaction unit 2 and second reaction unit 3, powder groove 1 with first reaction unit 2's input intercommunication, first reaction unit 2's output with second reaction unit 3's input intercommunication, second reaction unit 3's output intercommunication has filling equipment 4. The production device provided by the technical scheme is mainly used for producing materials rich in plant anions, and can release anions as much as possible from mixed materials rich in anions, and the actual operation flow of the device is that mineral powder passes through the powder tank 1 and is transferred into the first reaction component 2 for reaction through a belt or pumping equipment arranged in the powder tank 1; the pumping equipment arranged here is a delivery pump, and then the first reaction component 2 fully stirs with other substances and transmits the mixture to the second reaction component 3 through the pumping equipment for reaction, and the second reaction component is fully reacted through the steps and packaged by the filling equipment 4. After the series of flow operations, the error caused by manual operation can be avoided, the preparation precision of the powder product is improved, and the working efficiency is improved. As shown in fig. 1, from left to right is the output direction.
In some embodiments of the present invention, the first reaction assembly 2 includes a first tank 202, a high temperature reaction assembly 204, and a filter, the first stirring assembly 201 is installed at the top of the first tank 202, an output shaft of the first stirring assembly 201 penetrates through the first tank 202, a first stirring portion 203 is arranged on the output shaft of the first stirring assembly 201, and the first tank 202, the high temperature reaction assembly 204, and the filter are sequentially communicated and then communicated with an input end of the second reaction assembly 3. The first tank 202 is arranged to provide a space for stirring and mixing the mineral substances transferred to the inner part of the first tank through the powder trough 1, and after the powder and other substances are filled, the first tank 202 is immediately started and provided with the first stirring assembly 201 at the top thereof to drive the stirring part arranged on the first stirring assembly 201, namely the spiral blade rotates in the first tank 202, so that the powder and other auxiliary substances are fully stirred, and the mixing quality of the powder, the auxiliary substances and the liquid is improved.
In some embodiments of the present invention, the first reaction modules 2 are two groups, and two groups of the first reaction modules 2 are arranged in parallel, and the filter in any one group of the first reaction modules 2 is communicated with the first tank 202 in another group of the first reaction modules 2, and the filter in another group of the first reaction modules 2 is communicated with the input end of the second reaction module 3. Can improve the stirring quality of the powder and the auxiliary materials and ensure that the substances prepared by the equipment exert the due quality.
After the stirring in the first tank 202 is completed, the slurry can be pumped into the high-temperature reaction component 204 through a diaphragm pump arranged at an opening at the lower end of the first tank 202 to be subjected to primary treatment of nano carbonization activity for 3 hours, then the slurry subjected to primary treatment is filtered by 120 meshes, and then the filtered slurry is pumped into the first tank 202 in the other group of first reaction components 2 through a diaphragm pump arranged at the output end of the filter, and 300 parts of deionized water is injected to be stirred and cooled; and when the water temperature is reduced to 60 ℃, adding 100 parts of the plant powder and 3 parts of the multifunctional auxiliary agent for stirring, wherein the stirring speed is controlled to be 1000 revolutions, and the stirring time is 30 minutes.
In some embodiments of the present invention, the second reaction assembly 3 includes a second tank 302, a second stirring assembly 301 is installed on the top of the second tank 302, an output shaft of the second stirring assembly 301 is inserted into the second tank 302, a second stirring portion 303 is provided on an output shaft of the second stirring assembly 301, and the first tank 202 is communicated with the input end of the filling apparatus 4. Filtering the slurry after deep-stage treatment for 220 meshes, pumping the filtered slurry into a second tank 302 in the second reaction assembly 3 through a diaphragm pump arranged at the output end of a filter in the second reaction assembly 3, and simultaneously injecting 200 parts of deionized water for stirring and cooling; and when the water temperature is reduced to 30 ℃, sequentially adding 3 parts of wetting agent, 2 parts of bactericide and 1 part of defoaming agent, controlling the stirring speed within 500 revolutions, and stirring for 20 minutes.
In some embodiments of the present invention, the present invention further includes two sets of auxiliary material filling assemblies, wherein any one set of auxiliary material filling assembly is communicated with the first tank 202 communicated with the powder tank 1, and the other set of auxiliary material filling assembly is respectively communicated with the output ends of the filters located in the two first reaction assemblies 2. The two auxiliary material filling assemblies are beneficial to technical operators, and auxiliary materials and other substances are added into the first tank body 202 and the second tank body 302, so that the substances which are uniformly stirred are fully reacted.
In some embodiments of the present invention, the auxiliary material filling assembly includes a filling tank 9, a pipeline communicated with the filling tank 9 is disposed on the filling tank 9, and a liquid level meter 8 is disposed in the filling tank 9. The liquid level meter 8 is convenient for measure the auxiliary materials added into the filling tank 9, the technical personnel can control the quality of the prepared materials, the processing efficiency is improved, and the processing speed is increased.
In some embodiments of the invention, the filter comprises two filter tubes 7 arranged in pairs, the two filter tubes 7 communicating with each other. The two filter pipes 7 which are communicated through the pipeline can improve the filtering quality and the filtering efficiency of the liquid, and the two filter pipes 7 can also avoid the blockage of the single filter pipe 7 and the influence on the use of the equipment.
In some embodiments of the present invention, a sedimentation tank 5 and a light wave sterilization storage tank 6 are sequentially disposed between the second tank 302 and the input end of the filling apparatus 4. Putting the slurry in the tank body into a sedimentation tank 5 for sedimentation for 60 minutes; and pumping the precipitated liquid into a storage tank of an optical wave sterilizing and disinfecting room for optical wave sterilization and disinfection for 30 minutes.
In some embodiments of the present invention, a diaphragm pump is disposed between the first tank 202 and the high temperature reaction module 204.
A production method of anion essence comprises the steps of putting mineral powder into a powder trough 1, and conveying the mineral powder into a first tank 202 in any one first reaction assembly 2 through the powder trough 1; adding deionized water and a multifunctional additive into the first tank 202, and starting the first stirring component 201 to stir;
pumping the uniformly stirred slurry into a high-temperature reaction room in the first reaction assembly 2 for nano carbonization activity primary treatment;
filtering the primarily treated slurry, pumping the filtered slurry into the other first reaction component 2, and simultaneously injecting deionized water for stirring and cooling; then adding plant powder and multifunctional auxiliary agent for stirring;
pumping the uniformly stirred slurry into the high-temperature reaction component 204 in the other first reaction component 2 for nano carbonization activity deep-level treatment;
filtering the slurry after deep-stage treatment, pumping the filtered slurry into the second tank 302, and simultaneously injecting deionized water for stirring and cooling; when the water temperature is reduced, sequentially adding a wetting agent, a bactericide and a defoaming agent and stirring;
after stirring, putting the slurry in the tank body into a sedimentation tank 5 for sedimentation; pumping the precipitated liquid into a storage tank of an optical wave sterilization chamber for optical wave sterilization;
the prepared liquid can be canned after light wave sterilization and disinfection.
Detailed preparation steps comprise:
the first step is as follows: putting 100 parts of mineral powder into a powder trough 1, and conveying the mineral powder into a tank body of a high-speed dispersion machine through the powder trough 1; and simultaneously adding 500 parts of deionized water and 3 parts of multifunctional auxiliary agent, starting the high-speed dispersion machine, controlling the rotating speed at 1200 revolutions, and stirring for 30 minutes.
The second step is that: pumping the evenly stirred slurry to a high-temperature reaction room through a diaphragm pump, and carrying out primary treatment of nano carbonization activity for 3 hours.
The third step: filtering the primarily treated slurry by 120 meshes, pumping the filtered slurry into a tank body of a high-speed dispersion machine through a diaphragm pump, and simultaneously injecting 300 parts of deionized water for stirring and cooling; and when the water temperature is reduced to 60 ℃, adding 100 parts of the plant powder and 3 parts of the multifunctional auxiliary agent for stirring, wherein the stirring speed is controlled to be 1000 revolutions, and the stirring time is 30 minutes.
The fourth step: pumping the evenly stirred slurry to a high-temperature reaction room through a diaphragm pump, and carrying out nano carbonization activity deep-level treatment for 3 hours.
The fifth step: filtering the slurry treated at the deep stage for 220 meshes, pumping the filtered slurry into a low-speed dispersion machine tank body through a diaphragm pump, and simultaneously injecting 200 parts of deionized water for stirring and cooling; and when the water temperature is reduced to 30 ℃, sequentially adding 3 parts of wetting agent, 2 parts of bactericide and 1 part of defoaming agent, controlling the stirring speed within 500 revolutions, and stirring for 20 minutes.
And a sixth step: after stirring, putting the slurry in the tank body into a sedimentation tank 5 for sedimentation for 60 minutes; and pumping the precipitated liquid into a storage tank of an optical wave sterilizing and disinfecting room for optical wave sterilization and disinfection for 30 minutes.
The seventh step: the prepared liquid can be canned after light wave sterilization and disinfection.
And, the low speed dispersion machine set therein is the second reaction module 3, the high speed dispersion machine set therein is the first reaction module 2, and the high temperature reaction chamber is the high temperature reaction module 204.
To sum up, the embodiment of the application provides a production device of anion essence, including powder silo 1, first reaction unit 2 and second reaction unit 3, powder silo 1 with the input intercommunication of first reaction unit 2, the output of first reaction unit 2 with the input intercommunication of second reaction unit 3, the output intercommunication of second reaction unit 3 has filling equipment 4. The production device provided by the technical scheme is mainly used for producing materials rich in plant anions, and can release anions as far as possible from mixed materials rich in anions, and the actual operation flow of the device is that mineral powder is firstly transmitted into the first reaction component 2 for reaction through the powder tank 1 and a belt or pumping equipment arranged in the powder tank 1; the pumping equipment arranged here is a delivery pump, and then the first reaction component 2 fully stirs with other substances and transmits the mixture to the second reaction component 3 through the pumping equipment for reaction, and the second reaction component is fully reacted through the steps and packaged by the filling equipment 4. After the series of flow operations, the error caused by manual operation can be avoided, the preparation precision of the powder product is improved, and the working efficiency is improved.
A production method of anion essence comprises the steps of putting mineral powder into a powder trough 1, and conveying the mineral powder into a first tank 202 in any one first reaction assembly 2 through the powder trough 1; adding deionized water and a multifunctional additive into the first tank 202, and starting the first stirring component 201 to stir;
pumping the uniformly stirred slurry into a high-temperature reaction room in the first reaction component 2, and performing nano carbonization active primary treatment;
filtering the primarily treated slurry, pumping the filtered slurry into the other first reaction component 2, and simultaneously injecting deionized water for stirring and cooling; then adding plant powder and multifunctional auxiliary agent for stirring;
pumping the uniformly stirred slurry into the high-temperature reaction component 204 in the other first reaction component 2 for nano carbonization activity deep-level treatment;
filtering the slurry after deep-stage treatment, pumping the filtered slurry into the second tank 302, and simultaneously injecting deionized water for stirring and cooling; when the water temperature is reduced, sequentially adding a wetting agent, a bactericide and a defoaming agent and stirring;
after stirring, putting the slurry in the tank body into a sedimentation tank 5 for sedimentation; and pumping the precipitated liquid into a storage tank of an optical wave sterilizing room for optical wave sterilization. After the series of flow operations, the error caused by manual operation can be avoided, the preparation precision of the powder product is improved, and the working efficiency is improved.
The above is only a preferred embodiment of the present invention, and is not intended to limit the present invention, and various modifications and changes will occur to those skilled in the art. Any modification, equivalent replacement, or improvement made within the spirit and principle of the present invention should be included in the protection scope of the present invention.
Claims (10)
1. The utility model provides a production device of anion essence which characterized in that, includes powder groove, first reaction unit and second reaction unit, the powder groove with first reaction unit's input intercommunication, first reaction unit's output with second reaction unit's input intercommunication, second reaction unit's output intercommunication has filling equipment.
2. The apparatus for producing anion essence according to claim 1, wherein the first reaction assembly comprises a first tank, a high temperature reaction assembly and a filter, a first stirring assembly is installed at the top of the first tank, an output shaft of the first stirring assembly penetrates through the first tank, a first stirring portion is arranged on the output shaft of the first stirring assembly, and the first tank, the high temperature reaction assembly and the filter are communicated in sequence and then communicated with an input end of the second reaction assembly.
3. The apparatus for producing anion essence according to claim 2, wherein the first reaction components are two groups, and the two groups of first reaction components are arranged in parallel, and the filter in any one group of first reaction components is communicated with the first tank in the other group of first reaction components, and the filter in the other group of first reaction components is communicated with the input end of the second reaction component.
4. The apparatus for producing anion essence according to claim 3, wherein the second reaction component comprises a second tank, a second stirring component is installed on the top of the second tank, an output shaft of the second stirring component penetrates through the second tank, a second stirring part is arranged on the output shaft of the second stirring component, and the first tank is communicated with the input end of the filling device.
5. The device for producing the negative ion essence according to claim 4, further comprising two sets of auxiliary material filling assemblies, wherein any one set of auxiliary material filling assembly is communicated with the first tank communicated with the powder groove, and the other set of auxiliary material filling assembly is respectively communicated with the output ends of the filters in the two first reaction assemblies.
6. The device for producing the negative ion essence according to claim 5, wherein the auxiliary material filling assembly comprises a filling tank, the filling tank is provided with a pipeline communicated with the filling tank, and the filling tank is internally provided with a liquid level meter.
7. The apparatus for producing an anion essence according to claim 6, wherein the filter comprises two filter pipes which are arranged in pair, and the two filter pipes are communicated with each other.
8. The apparatus for producing anion essence according to claim 4, wherein a sedimentation tank and an optical wave sterilization storage tank are sequentially arranged between the second tank and the input end of the filling equipment.
9. The apparatus for producing anion essence according to claim 8, wherein a diaphragm pump is arranged between the first tank and the high temperature reaction component.
10. A production method of anion essence, which is characterized in that,
mineral powder is put into a powder groove and conveyed into a first tank body in any one first reaction assembly through the powder groove; adding deionized water and a multifunctional auxiliary agent into the first tank body, and starting the first stirring assembly to stir;
pumping the uniformly stirred slurry into a high-temperature reaction room in a first reaction assembly, and performing nano carbonization active primary treatment;
filtering the primarily treated slurry, pumping the filtered slurry into a first tank body in another first reaction assembly, and simultaneously injecting deionized water for stirring and cooling; then adding plant powder and multifunctional auxiliary agent for stirring;
pumping the uniformly stirred slurry into a high-temperature reaction assembly in the other first reaction assembly, and performing nano carbonization activity deep-level treatment;
filtering the slurry after deep-stage treatment, pumping the filtered slurry into a second tank body, and simultaneously injecting deionized water for stirring and cooling; when the water temperature is reduced, sequentially adding a wetting agent, a bactericide and a defoaming agent and stirring;
after stirring, putting the slurry in the tank body into a sedimentation tank for sedimentation; pumping the precipitated liquid into a storage tank of an optical wave sterilization room for optical wave sterilization;
the prepared liquid can be canned after light wave sterilization and disinfection.
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| CN202210932623.7A CN115282909A (en) | 2022-08-04 | 2022-08-04 | Production device and method of anion essence |
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| CN202210932623.7A CN115282909A (en) | 2022-08-04 | 2022-08-04 | Production device and method of anion essence |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN117884079A (en) * | 2024-03-18 | 2024-04-16 | 优牌生物医药科技(上海)有限公司 | Essence reduction equipment and preparation method thereof |
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2022
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN117884079A (en) * | 2024-03-18 | 2024-04-16 | 优牌生物医药科技(上海)有限公司 | Essence reduction equipment and preparation method thereof |
| CN117884079B (en) * | 2024-03-18 | 2024-05-07 | 优牌生物医药科技(上海)有限公司 | Essence reduction equipment and preparation method thereof |
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Application publication date: 20221104 |