CN214361737U - Electrolytic water and fertilizer treatment equipment - Google Patents
Electrolytic water and fertilizer treatment equipment Download PDFInfo
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- CN214361737U CN214361737U CN202120344092.0U CN202120344092U CN214361737U CN 214361737 U CN214361737 U CN 214361737U CN 202120344092 U CN202120344092 U CN 202120344092U CN 214361737 U CN214361737 U CN 214361737U
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Abstract
The utility model discloses an electrolytic liquid manure processing equipment, include: an equipment housing; an electrolysis module, a finished product tank and a solution tank; the electrolytic module comprises at least two electrolytic tanks, and each electrolytic tank comprises a solution electrolytic cavity and a finished product electrolytic cavity; a pure water adding pipeline I is connected between the solution tank and the pure water adding port I, and a pure water adding pipeline II is connected between the finished product tank and the pure water adding port II; the equipment shell is provided with a solution adding port, and a solution adding pipeline is connected between the solution tank and the solution adding port; a filling pipeline is connected between the finished product tank and the filling port; the solution tank is connected with a solution drainage pipeline, the finished product tank is connected with a finished product drainage pipeline, and the solution drainage pipeline and the finished product drainage pipeline are connected with a drainage port through a connecting pipeline; a solution circulating pipeline is connected between the electrolysis module and the solution tank, and a finished product circulating pipeline is connected between the electrolysis module and the finished product tank. The utility model provides a can circulate the electrolysis to pure water and electrolyte solution, make off-the-shelf pH value up to standard.
Description
Technical Field
The utility model belongs to the technical field of electrolysis liquid manure equipment, more specifically say, the utility model relates to an electrolysis liquid manure processing equipment.
Background
The electrolyzed water is also called electrolyzed ionic water and oxidation-reduction potential water, and refers to a process of generating hydrogen and oxygen by direct current electrolysis of water. In 1869, since the invention of dc generators, hydrogen gas was produced by electrolytic water technology. In 1931, the first water electrolysis equipment was developed in japan and applied to the medical field; by 1960, the application of the electrolyzed water gradually develops from the medical field to the daily life field; among them, the present ones include the apparatus for electrolyzing water and fertilizer suitable for the agricultural production field. The emergence of agricultural water and fertilizer electrolysis equipment reduces the pollution of industry to the environment, and marks the arrival of 'zero chemical agricultural era' for agriculture. The agricultural electrolytic water and fertilizer treatment equipment can be used in the fields of industrial planting, cultivation, deep processing of agricultural products and the like.
The production efficiency of the existing water and fertilizer electrolysis equipment is low, and the pH value of the electrolyzed finished product is difficult to reach the standard and is qualified. Therefore, the electrolytic water and fertilizer treatment equipment which can be used for continuous electrolytic production, has high electrolytic production efficiency and high standard reaching rate of finished products is needed.
SUMMERY OF THE UTILITY MODEL
An object of the present invention is to solve at least the above problems and/or disadvantages and to provide at least the advantages which will be described later.
To achieve these objects and other advantages in accordance with the purpose of the invention, there is provided an electrolytic water and fertilizer treatment apparatus including:
an equipment housing;
the electrolytic module is arranged inside the equipment shell, and a finished product tank and a solution tank are also arranged inside the equipment shell; the electrolytic module comprises at least two electrolytic tanks, each electrolytic tank comprises a solution electrolytic cavity and a finished product electrolytic cavity, and the solution electrolytic cavity and the finished product electrolytic cavity are separated by an ion exchange membrane;
the equipment shell is provided with a pure water adding port I and a pure water adding port II, a pure water adding pipeline I is connected between the solution tank and the pure water adding port I, and a pure water adding pipeline II is connected between the finished product tank and the pure water adding port II;
the equipment shell is provided with a solution adding port, and a solution adding pipeline is connected between the solution tank and the solution adding port;
the equipment shell is provided with a filling opening, and a filling pipeline is connected between the finished product tank and the filling opening;
the equipment shell is provided with a water outlet, the solution tank is connected with a solution drainage pipeline, the finished product tank is connected with a finished product drainage pipeline, and the solution drainage pipeline and the finished product drainage pipeline are connected with the water outlet through a connecting pipeline;
a solution circulating pipeline is connected between a solution electrolysis cavity of the electrolytic cell and the solution tank, and a finished product circulating pipeline is connected between a finished product electrolysis cavity of the electrolytic cell and the finished product tank.
Preferably, the structure of the addition pipeline I comprises: two ends of the pure water adding pipeline I are respectively connected with the solution tank and the pure water adding port I, and a pure water adding electromagnetic valve I is arranged on the pure water adding pipeline I;
the structure of the pure water adding pipeline II comprises: and two ends of the pure water adding pipeline II are respectively connected with the finished product tank and the pure water adding port II, and a pure water adding electromagnetic valve II is arranged on the pure water adding pipeline II.
Preferably, the solution adding line has a structure including: and the two ends of the solution adding pipeline are respectively connected with the solution tank and the solution adding port, and a solution adding pump is arranged on the solution adding pipeline.
Preferably, the structure of the filling line comprises: and two ends of the filling pipeline are respectively connected with the finished product tank and the filling port, and a filling pump is arranged on the filling pipeline.
Preferably, the equipment shell is provided with an exhaust port, and an exhaust pipeline is connected between the finished product tank and the exhaust port.
Preferably, the equipment shell is provided with an overflow port, and the solution tank and the finished product tank are connected with the overflow port through overflow pipelines.
Preferably, wherein the solution drain line has a structure including: the two ends of the solution drainage pipeline are respectively connected with the solution tank and the connecting pipeline, and a solution drainage electromagnetic valve is arranged on the solution drainage pipeline;
the structure of the finished product drainage pipeline comprises: and the two ends of the finished product drainage pipeline are respectively connected with the finished product tank and the connecting pipeline, and a finished product drainage electromagnetic valve is arranged on the finished product drainage pipeline.
Preferably, wherein the solution circulation line has a structure including: the solution circulating pipeline is respectively connected with the solution electrolysis cavity and the solution tank, and a solution circulating pump is arranged on the solution circulating pipeline;
the structure of the finished product circulation pipeline comprises: and the finished product circulating pipeline is respectively connected with the finished product electrolysis cavity and the finished product tank, and a finished product circulating pump is arranged on the finished product circulating pipeline.
Preferably, an observation operation panel is arranged on the equipment shell, and the observation operation panel structurally comprises a touch screen, a solution tank pH meter, a finished product tank pH meter and a plurality of operation buttons;
the equipment shell is hinged with a front door, and a front door observation window is arranged on the front door.
Preferably, a pipeline approach switch I is installed at a position, close to the electrolysis module, of the solution circulation pipeline; and a pipeline approach switch II is arranged at the position, close to the electrolysis module, of the finished product circulating pipeline.
The utility model discloses at least, include following beneficial effect: the utility model provides an electrolysis liquid manure treatment facility is through a plurality of electrolysis tanks that set up to dispose corresponding solution circulating line and finished product circulating line, can use a plurality of electrolysis tanks to carry out circulation electrolysis respectively simultaneously to electrolyte solution and pure water, make finished product pH value in the finished product jar up to standard, electrolysis production efficiency is high. When the agent A is produced, a sodium chloride solution is used as an electrolyte solution, and after circular electrolysis, the pH value of a finished product can reach 1.6 +/-0.2; when the agent B is produced, a potassium carbonate solution is used as an electrolyte solution, and after circular electrolysis, the pH value of a finished product can reach 13.2 +/-0.2. The utility model can produce agricultural liquid manure with specific pH value through the difference of the configured electrolyte solution. Utility model adopts the modular design simultaneously, and each accessory can independently be dismantled the maintenance. The utility model can realize continuous cycle production, and improve the production efficiency of water and fertilizer electrolysis.
Additional advantages, objects, and features of the invention will be set forth in part in the description which follows and in part will become apparent to those having ordinary skill in the art upon examination of the following or may be learned from practice of the invention.
Description of the drawings:
FIG. 1 is a schematic side view of an electrolytic water and fertilizer treatment apparatus provided by the present invention;
FIG. 2 is a schematic view of the internal structure of the electrolytic water and fertilizer treatment device provided by the present invention;
FIG. 3 is a schematic view of a cross-sectional structure of the electrolytic water and fertilizer treatment device provided by the present invention;
fig. 4 is the external structure schematic diagram of the electrolytic water and fertilizer treatment device provided by the utility model.
The specific implementation mode is as follows:
the present invention is further described in detail below with reference to the drawings so that those skilled in the art can implement the invention with reference to the description.
It will be understood that terms such as "having," "including," and "comprising," as used herein, do not preclude the presence or addition of one or more other elements or groups thereof.
It should be noted that in the description of the present invention, the terms indicating the orientation or the positional relationship are based on the orientation or the positional relationship shown in the drawings, and are only for convenience of describing the present invention and simplifying the description, and do not indicate or imply that the indicated device or element must have a specific orientation, be constructed in a specific orientation, and be operated, and thus should not be construed as limiting the present invention. Furthermore, the terms "first" and "second" are used for descriptive purposes only and are not to be construed as indicating or implying relative importance.
In the description of the present invention, unless otherwise explicitly specified or limited, the terms "mounted," "disposed," "sleeved/connected," "connected," and the like are to be construed broadly, such as "connected," which may be a fixed connection, a detachable connection, or an integral connection, a mechanical connection, an electrical connection, a direct connection, an indirect connection via an intermediate medium, or a connection between two elements, and those skilled in the art will understand the specific meaning of the terms in the present invention in a specific context.
Furthermore, in the present disclosure, unless explicitly stated or limited otherwise, a first feature may be "on" or "under" a second feature in direct contact with the first and second features, or in indirect contact with the first and second features through an intermediate. Also, a first feature "on," "over," and "above" a second feature may be directly or diagonally above the second feature, or may simply indicate that the first feature is at a higher level than the second feature. A first feature being "under," "below," and "beneath" a second feature may be directly under or obliquely under the first feature, or may simply mean that the first feature is at a lesser elevation than the second feature.
As shown in fig. 1-4: the utility model discloses an electrolytic liquid manure processing equipment, include:
an apparatus casing 1;
the electrolytic module 2 is arranged inside the equipment shell 1, and a finished product tank 3 and a solution tank 4 are also arranged inside the equipment shell 1; the electrolytic module 2 comprises two electrolytic cells 21, each electrolytic cell 21 comprises a solution electrolytic cavity 211 and a finished product electrolytic cavity 212, and the solution electrolytic cavity 211 and the finished product electrolytic cavity 212 are separated by an ion exchange membrane;
the equipment shell is provided with a pure water adding port I101 and a pure water adding port II 102, a pure water adding pipeline I is connected between the solution tank 4 and the pure water adding port I101, and a pure water adding pipeline II is connected between the finished product tank 3 and the pure water adding port II 102;
the equipment shell 1 is provided with a solution adding port 103, and a solution adding pipeline is connected between the solution tank 4 and the solution adding port 103;
the equipment shell 1 is provided with a filling opening 104, and a filling pipeline is connected between the finished product tank 3 and the filling opening 104;
the equipment shell 1 is provided with a water outlet 105, the solution tank 4 is connected with a solution drainage pipeline, the finished product tank 3 is connected with a finished product drainage pipeline, and the solution drainage pipeline and the finished product drainage pipeline are connected with the water outlet 105 through a connecting pipeline 5;
a solution circulating pipeline is connected between the solution electrolysis cavity 211 of the electrolysis bath 21 and the solution tank 4, and a finished product circulating pipeline is connected between the finished product electrolysis cavity 212 of the electrolysis bath 21 and the finished product tank 3. In fig. 2, the two electrolytic cells 21 are respectively connected with the solution circulation pipeline and the finished product circulation pipeline in a pipeline converging manner.
In the above technical solution, the structure of the adding pipeline i includes: two ends of the pure water adding pipeline I6 are respectively connected with the solution tank 4 and the pure water adding port I101, and a pure water adding electromagnetic valve I is arranged on the pure water adding pipeline I6;
the structure of the pure water adding pipeline II comprises: and two ends of the pure water adding pipeline II 8 are respectively connected with the finished product tank 3 and the pure water adding port II 102, and a pure water adding electromagnetic valve II is arranged on the pure water adding pipeline II 8.
In the above technical solution, the solution adding pipeline has a structure including: and a solution adding pipe 10 having both ends connected to the solution tank 4 and the solution adding port 103, respectively, wherein the solution adding pipe 10 is provided with a solution adding pump 11.
In the above technical solution, the structure of the filling pipeline includes: and two ends of the filling pipeline 12 are respectively connected with the finished product tank 3 and the filling port 104, and a filling pump 121 is arranged on the filling pipeline.
In the above technical solution, the apparatus housing 1 is provided with an exhaust port 106, and an exhaust pipeline 13 is connected between the finished product tank 3 and the exhaust port 103.
In the above technical solution, the apparatus housing 1 is provided with an overflow port 107, and the solution tank 4 and the finished product tank 3 are connected with the overflow port 107 through an overflow pipe 14.
In the above technical solution, the solution drain line has a structure including: a solution drainage pipeline 15, two ends of which are respectively connected with the solution tank 4 and the connecting pipeline 5, wherein a solution drainage electromagnetic valve is arranged on the solution drainage pipeline 15;
the structure of the finished product drainage pipeline comprises: and two ends of the finished product drainage pipeline 16 are respectively connected with the finished product tank 3 and the connecting pipeline 5, and a finished product drainage electromagnetic valve is arranged on the finished product drainage pipeline 16. The waste water in the solution tank 4 and the finished product tank 3 is intensively discharged through a connecting pipe 5.
In the above technical solution, the solution circulation line has a structure including: a solution circulation pipeline 17 connected to the solution electrolysis chamber 211 and the solution tank 4, respectively, and the solution circulation pipeline 17 is provided with a solution circulation pump 171;
the structure of the finished product circulation pipeline comprises: and a finished product circulating pipeline 18 which is respectively connected with the finished product electrolysis cavity 212 and the finished product tank 3, and a finished product circulating pump 181 is arranged on the finished product circulating pipeline 18.
In the technical scheme, an observation operation panel 111 is arranged on the equipment shell 1, and the observation operation panel structurally comprises a touch screen, a solution tank pH instrument, a finished product tank pH instrument and a plurality of operation buttons; the solution tank pH meter and the finished product tank pH meter are respectively used for detecting the pH values of the solution in the solution tank and the finished product in the finished product tank.
The equipment shell is hinged with a front door 112, and a front door observation window 113 is arranged on the front door.
In the technical scheme, a pipeline approach switch I is arranged at the position, close to the electrolysis module 2, of the solution circulating pipeline 17; and a pipeline approach switch II is arranged at the position of the finished product circulating pipeline 18 close to the electrolysis module 2.
The working principle of the above-mentioned equipment is specifically explained below with reference to the embodiments:
example 1:
when the agent A is produced, adding a prepared sodium chloride solution into a solution tank through a solution adding port and a solution adding pipeline, and adding pure water into a finished product tank through a pure water adding port II and a pure water adding pipeline II; wherein the sodium chloride solution can be automatically pumped into the solution tank by the solution adding pump. Sodium chloride solution in the solution tank is pumped into the solution electrolysis cavity 211 through a solution circulating pipeline by a solution circulating pump, an electrode in the solution electrolysis cavity 211 is used as a negative electrode to electrolyze the sodium chloride solution, pure water in the finished product tank is pumped into the finished product electrolysis cavity 212 through a finished product circulating pipeline by a finished product circulating pump, and the electrode in the finished product electrolysis cavity 212 is used as a positive electrode to electrolyze the pure water; and, the sodium chloride solution circulates between the solution electrolysis chamber 211 and the solution tank 4 through a solution circulation line, and the pure water circulates between the finished product tank 3 and the finished product electrolysis chamber 212 through a finished product circulation line, so as to realize circulation electrolysis of the sodium chloride solution and the pure water. And the pipeline proximity switch I and the pipeline proximity switch II are used for indicating whether the sodium chloride solution and the finished product are circulated in place.
The pH value of the sodium chloride solution is changed from neutral to strong alkaline, namely after the production is started, the pH values in the solution tank 4 and the solution electrolysis cavity 211 are gradually changed from about 7-8 to more than 13, and the pH values in the finished product electrolysis cavity 212 and the finished product tank 3 are gradually changed from neutral to acidic. After production is stopped, the electrolyte solution and the finished product in the electrolytic bath 21 automatically flow back to the solution tank and the finished product tank, respectively. And when the pH value of the finished product in the finished product tank reaches the standard, filling the finished product in the finished product tank into an external tank body through a filling pipeline. After the finished product is filled, pure water is respectively added into the solution tank and the finished product tank through the pure water adding port I and the pure water adding port II so as to maintain the pH values in the solution tank and the finished product tank and ensure that the electrolytic bath 21 is protected by water immersion. And the solution in the solution tank and the solution in the finished product tank are discharged through a solution drainage pipeline and a finished product drainage pipeline respectively. The overflow pipeline and the overflow port are used for discharging redundant liquid in the solution tank and the finished product tank, and the exhaust port and the exhaust pipeline are used for exhausting gas in the finished product tank. When the agent A is produced, all doors and windows of equipment are required to be closed for production, and the agent A is matched with waste gas treatment equipment for use, so that the waste gas is prevented from leaking outwards and affecting the environment and the body health.
Example 2:
when the agent B is produced, the prepared potassium carbonate solution is added into the solution tank 4 through the solution adding port and the solution adding pipeline, and pure water is added into the finished product tank through the pure water adding port II and the pure water adding pipeline II; wherein the potassium carbonate solution may be automatically pumped into the solution tank 4 by a solution addition pump. Potassium carbonate solution in the solution tank is pumped into the solution electrolysis cavity 211 through a solution circulating pipeline by a solution circulating pump, an electrode in the solution electrolysis cavity 211 is used as a positive electrode to electrolyze the potassium carbonate solution, pure water in the finished product tank 3 is pumped into the finished product electrolysis cavity 212 through a finished product circulating pipeline by a finished product circulating pump, and an electrode in the finished product electrolysis cavity 212 is used as a negative electrode to electrolyze the pure water; in addition, the potassium carbonate solution circulates between the solution electrolysis cavity 211 and the solution tank through the solution circulation pipeline, and the finished product circulates between the finished product tank and the finished product electrolysis cavity 212 through the finished product circulation pipeline, so that the circulating electrolysis of the potassium carbonate solution and the pure water is realized. And the pipeline proximity switch I and the pipeline proximity switch II are used for indicating whether the potassium carbonate solution and the finished product are circulated in place.
The pH value of the potassium carbonate solution is changed from alkalinity to neutrality, namely after the production is started, the pH values in the solution tank 4 and the solution electrolysis cavity 211 are gradually changed from about 12 to about 7, and the pH values in the finished product electrolysis cavity 212 and the finished product tank 3 are gradually changed from neutrality to alkalinity. After production is stopped, the electrolyte solution and the finished product in the electrolytic bath 21 automatically flow back to the solution tank and the finished product tank, respectively. And when the pH value of the finished product in the finished product tank reaches the standard, filling the finished product in the finished product tank into an external tank body through a filling pipeline. After the finished product is filled, pure water is respectively added into the solution tank and the finished product tank through the pure water adding port I and the pure water adding port II so as to maintain the pH values in the solution tank and the finished product tank and ensure that the electrolytic bath 21 is protected by water immersion. And the solution in the solution tank and the solution in the finished product tank are discharged through a solution drainage pipeline and a finished product drainage pipeline respectively. The overflow pipeline and the overflow port are used for discharging redundant liquid in the solution tank and the finished product tank, and the exhaust port and the exhaust pipeline are used for exhausting gas in the finished product tank.
The number of apparatuses and the scale of the process described here are intended to simplify the description of the present invention. Applications, modifications and variations of the present invention will be apparent to those skilled in the art.
While the embodiments of the invention have been described above, it is not intended to be limited to the details shown, or described, but rather to cover all modifications, which would come within the scope of the appended claims, and all changes which come within the meaning and range of equivalency of the art are therefore intended to be embraced therein.
Claims (10)
1. An electrolytic water and fertilizer treatment apparatus, comprising:
an equipment housing;
the electrolytic module is arranged inside the equipment shell, and a finished product tank and a solution tank are also arranged inside the equipment shell; the electrolytic module comprises at least two electrolytic tanks, each electrolytic tank comprises a solution electrolytic cavity and a finished product electrolytic cavity, and the solution electrolytic cavity and the finished product electrolytic cavity are separated by an ion exchange membrane;
the equipment shell is provided with a pure water adding port I and a pure water adding port II, a pure water adding pipeline I is connected between the solution tank and the pure water adding port I, and a pure water adding pipeline II is connected between the finished product tank and the pure water adding port II;
the equipment shell is provided with a solution adding port, and a solution adding pipeline is connected between the solution tank and the solution adding port;
the equipment shell is provided with a filling opening, and a filling pipeline is connected between the finished product tank and the filling opening;
the equipment shell is provided with a water outlet, the solution tank is connected with a solution drainage pipeline, the finished product tank is connected with a finished product drainage pipeline, and the solution drainage pipeline and the finished product drainage pipeline are connected with the water outlet through a connecting pipeline;
a solution circulating pipeline is connected between a solution electrolysis cavity of the electrolytic cell and the solution tank, and a finished product circulating pipeline is connected between a finished product electrolysis cavity of the electrolytic cell and the finished product tank.
2. The electrolytic water and fertilizer treatment apparatus according to claim 1, wherein the structure of the addition pipeline i comprises: two ends of the pure water adding pipeline I are respectively connected with the solution tank and the pure water adding port I, and a pure water adding electromagnetic valve I is arranged on the pure water adding pipeline I;
the structure of the pure water adding pipeline II comprises: and two ends of the pure water adding pipeline II are respectively connected with the finished product tank and the pure water adding port II, and a pure water adding electromagnetic valve II is arranged on the pure water adding pipeline II.
3. The electrolytic water-fertilizer treatment apparatus of claim 1, wherein the solution addition line is structured to include: and the two ends of the solution adding pipeline are respectively connected with the solution tank and the solution adding port, and a solution adding pump is arranged on the solution adding pipeline.
4. The electrolyzed water fertilizer treatment apparatus as defined in claim 1, wherein the filling line has a structure comprising: and two ends of the filling pipeline are respectively connected with the finished product tank and the filling port, and a filling pump is arranged on the filling pipeline.
5. The electrolyzed water fertilizer treatment apparatus according to claim 1, wherein the apparatus housing is provided with an exhaust port, and an exhaust duct is connected between the product tank and the exhaust port.
6. The electrolytic water-fertilizer treatment apparatus of claim 1, wherein the apparatus housing is provided with an overflow port, and the solution tank and the product tank are connected to the overflow port through an overflow pipe.
7. The electrolyzed water fertilizer treatment apparatus as defined in claim 1, wherein the solution drain line has a structure comprising: the two ends of the solution drainage pipeline are respectively connected with the solution tank and the connecting pipeline, and a solution drainage electromagnetic valve is arranged on the solution drainage pipeline;
the structure of the finished product drainage pipeline comprises: and the two ends of the finished product drainage pipeline are respectively connected with the finished product tank and the connecting pipeline, and a finished product drainage electromagnetic valve is arranged on the finished product drainage pipeline.
8. The electrolytic water-fertilizer treatment apparatus of claim 1, wherein the solution circulation line is structured to include: the solution circulating pipeline is respectively connected with the solution electrolysis cavity and the solution tank, and a solution circulating pump is arranged on the solution circulating pipeline;
the structure of the finished product circulation pipeline comprises: and the finished product circulating pipeline is respectively connected with the finished product electrolysis cavity and the finished product tank, and a finished product circulating pump is arranged on the finished product circulating pipeline.
9. The electrolytic water and fertilizer treatment apparatus according to claim 1, wherein an observation operation panel is provided on the apparatus casing, and the observation operation panel has a structure including a touch screen, a solution tank pH meter, a finished tank pH meter, and a plurality of operation buttons;
the equipment shell is hinged with a front door, and a front door observation window is arranged on the front door.
10. The electrolytic water and fertilizer treatment apparatus according to claim 8, wherein a pipe approach switch i is installed in the solution circulation pipe near the electrolysis module; and a pipeline approach switch II is arranged at the position, close to the electrolysis module, of the finished product circulating pipeline.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202120344092.0U CN214361737U (en) | 2021-02-05 | 2021-02-05 | Electrolytic water and fertilizer treatment equipment |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202120344092.0U CN214361737U (en) | 2021-02-05 | 2021-02-05 | Electrolytic water and fertilizer treatment equipment |
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| CN214361737U true CN214361737U (en) | 2021-10-08 |
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| CN202120344092.0U Active CN214361737U (en) | 2021-02-05 | 2021-02-05 | Electrolytic water and fertilizer treatment equipment |
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| CN (1) | CN214361737U (en) |
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2021
- 2021-02-05 CN CN202120344092.0U patent/CN214361737U/en active Active
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