CN205966109U - Comminuted system - Google Patents
Comminuted system Download PDFInfo
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- CN205966109U CN205966109U CN201620913152.5U CN201620913152U CN205966109U CN 205966109 U CN205966109 U CN 205966109U CN 201620913152 U CN201620913152 U CN 201620913152U CN 205966109 U CN205966109 U CN 205966109U
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Abstract
The utility model discloses a comminuted system, including the reaction cabin, controlling means that are equipped with feed inlet and discharge gate, reach all with controlling means electric connection's feedway, reaction liquid feeding device and rapid pressure reduction means, feedway with the feed inlet cooperation, reaction liquid feeding device with reaction cabin pipeline intercommunication, pressure reduction means includes step -down closure member rapidly, step -down closure member with the discharge gate sliding fit in reaction cabin. Send into the material when the back reaction under -deck and fully fuse the back with reaction liquid, make through step -down closure member and discharge gate sliding fit and react the under -deck rapid depressurization for the inside and the surface of material granule form great pressure difference within a definite time, thereby by its inside emergence " explosion ", with the less granule of the cracked one -tenth of the raw materials of great granule, so realize good crushing effect, can not cause the damage to the material simultaneously, protect its biological activity and active ingredient, and make simple process, the work safety, the reliability is high.
Description
Technical field
This utility model is related to crushing material technical field, particularly a kind of crushing material system.
Background technology
With the increasingly raising of people's living standard, how to seek the healthy topic becoming people's growing interest.Mirror
In this, the health promoting beverage that some plants and its extract make, the guarantor for example being made by Phaeoporus obliquus are also engendered on the market
Strong tea, health beverage etc..Such product main component has polysaccharide, inonotus obliquus, Inonqqus obliquus alcohol, multiple oxidation triterpeness
Compound, bolt bacterium acid etc., nutritional labeling is high, medicinal effects are good, is joined assistant raw material special component and combines, can effectively improve people
The vigor of body immunocyte, anticancer diffusion and recurrence, can effectively prevent carcinogenic absorption waiting harmful substance in gastrointestinal,
Body discharges can be promoted simultaneously, thus be welcome by suitable crowd.
Then determine above-mentioned health promoting beverage is worth the granule size that one of key factor is feed particles, and it is determined
Determine to extract the level of medicinal ingredient.Existing raw material is mostly produced using crushing technology, mainly have room temperature or cryogrinding,
Impact, shred, split broken and crushing etc. process, such technical matters and Making programme complex, thus result in and produce into
This is higher；Additionally, obtained Phaeoporus obliquus finished particle after pulverization process is larger, and granule can be caused damage, thus greatly
Reduce greatly biological activity, active constituent content and other characteristics of product.
Content of the invention
Based on this, this utility model is to overcome the defect of prior art, provides a kind of good crushing effect, can protect product
Product biological activity and effective ingredient, simple production process, low cost of manufacture and work safety, reliable crushing material system.
Its technical scheme is as follows：
A kind of crushing material system, including be provided with the reaction cabin of charging aperture and discharging opening, control device and all with described control
Feeding device, reaction liquid supplying device and rapid dropping equipment, described feeding device and described charging that device processed is electrically connected with
Mouth cooperation, described reaction liquid supplying device and described reaction cabin pipeline connection, described rapid dropping equipment includes blood pressure lowering opening and closing element,
Described blood pressure lowering opening and closing element is slidably matched with the discharging opening of described reaction cabin.
Wherein in an embodiment, described feeding device includes inlet valve, described inlet valve include valve rod and with described
The valve head that valve rod connects, described reaction cabin includes being provided with the reative cell of opening and the upper lid being connected with reative cell, described valve head and
Described opening can close fit, described charging aperture is arranged at described upper lid, forms charging logical between described upper lid and described valve head
Road, described charging aperture, described feeding-passage and the opening of described reative cell are sequentially communicated.
Wherein in an embodiment, described rapid dropping equipment includes the driving that force piece is connected with described force piece
Part and the described blood pressure lowering opening and closing element being connected with described actuator, described blood pressure lowering opening and closing element include slide bar and with described slide bar end
The closure member connecting, described reaction cabin is provided with pressure contact portion positioned at described discharge outlet, described closure member and described pressure contact portion snapping
Cooperation.
Wherein in an embodiment, also include sealing member, described sealing member is arranged at described pressure contact portion and is opened with described
Closing member is fastened.
Wherein in an embodiment, described closure member is provided with first annular inclined-plane, and described sealing member is provided with the second annular
Inclined-plane, described first annular inclined-plane is cooperated with described second annular slope.
Wherein in an embodiment, also include the pressure indicating gage for pressure values in reaction cabin described in real-time monitoring.
Wherein in an embodiment, also include adjusting means, described adjusting means includes being arranged in described reaction cabin
Monitoring part with the described monitoring Volume Indicator that is connected of part and the eduction valve that is electrically connected with described control device, described instead
Cabin is answered to be provided with relief port, described eduction valve is connected with described relief port pipeline.
Wherein in an embodiment, also include material recycling device, described material recycling device includes and described discharging
Mouthful feed back cylinder connecting and be arranged at filtration members in described feed back cylinder, described filtration members are provided with multiple filtering holes.
Wherein in an embodiment, described material recycling device also includes trap, and described feed back cylinder is near described mistake
The side wall of filter part is provided with feedback outlet, and described feedback outlet is connected with described trap pipeline, and described trap and described feed
Device connects.
Wherein in an embodiment, described reaction liquid supplying device includes fluidsupply container, liquid feeding pipeline and flow-control
Valve, one end of described liquid feeding pipeline is connected with described fluidsupply container, and the other end of described liquid feeding pipeline is connected with described reaction cabin,
Described flow control valve is connected on described liquid feeding pipeline.
The beneficial effects of the utility model are：
Above-mentioned crushing material system is passed through described feeding device, described reaction liquid supplying device and described rapid blood pressure lowering dress
Put and be all electrically connected with described control device, thus improve the automatization level of system work, pass through described feed in addition
Device and the cooperation of described charging aperture, by described reaction liquid supplying device and described reaction cabin pipeline connection, when sending into reaction cabin
Fully merging after entering material and reactant liquor, being slidably matched so that reacting by described blood pressure lowering opening and closing element and described discharging opening afterwards
In cabin, rapid blood pressure lowering is so that form larger pressure difference between the inside of material particles and outer surface, thus by its internal occur " quick-fried
Fried ", the raw material of larger particles is fragmented into smaller particle, so realizes good crushing effect, material will not be caused simultaneously
Damage, protect its biological activity and effective ingredient, and the processing technology of this crushing material system is simple, work safety, reliability
High.
Brief description
Fig. 1 is the structural representation of the crushing material system described in this utility model embodiment.
Description of reference numerals：
100th, reaction cabin, 110, charging aperture, 120, discharging opening, 130, reative cell, 140, Shang Gai, 150, feeding-passage,
160th, pressure contact portion, 200, control device, 300, feeding device, 320, inlet valve, 322, valve rod, 324, valve head, 400, reactant liquor
Feedway, 420, fluidsupply container, 440, liquid feeding pipeline, 460, flow control valve, 500, rapid dropping equipment, 510, blood pressure lowering opens
Closing member, 512, slide bar, 514, closure member, 514a, first annular inclined-plane, 520, force piece, 530, actuator, 600, sealing member,
620th, the second annular slope, 700, pressure indicating gage, 800, adjusting means, 820, monitoring part, 840, Volume Indicator, 860, let out
Stream valve, 900, material recycling device, 920, feed back cylinder, 940, filtration members, 960, trap, 962, feedback outlet.
Specific embodiment
Below embodiment of the present utility model is described in detail：
As shown in figure 1, a kind of crushing material system, including the reaction cabin 100, the control that are provided with charging aperture 110 and discharging opening 120
Device 200 processed and the feeding device 300 being all electrically connected with described control device 200, reaction liquid supplying device 400 and rapid
Dropping equipment 500, described feeding device 300 is coordinated with described charging aperture 110, and described reaction liquid supplying device 400 is anti-with described
Answer cabin 100 pipeline connection, described rapid dropping equipment 500 includes blood pressure lowering opening and closing element 510, described blood pressure lowering opening and closing element 510 with described
The discharging opening 120 of reaction cabin 100 is slidably matched.
Above-mentioned crushing material system is passed through described feeding device 300, described reaction liquid supplying device 400 and described rapid
Dropping equipment 500 and being all electrically connected with described control device 200, is thus improved the automatization level of system work, leads in addition
Cross and described feeding device 300 is coordinated with described charging aperture 110, by described reaction liquid supplying device 400 and described reaction cabin 100
Pipeline connection, fully merges, afterwards by described blood pressure lowering opening and closing element after sending into material and reactant liquor into reaction cabin 100
510 are slidably matched with described discharging opening 120 makes rapid blood pressure lowering in reaction cabin 100 so that the inside of material particles and outer surface
Between form larger pressure difference, thus by its internal there is " blast ", the raw material of larger particles is fragmented into smaller particle, so
Realize good crushing effect, material will not be caused to damage simultaneously, protect its biological activity and effective ingredient, and this material powder
The processing technology of broken system is simple, work safety, and reliability is high.
In the present embodiment, illustrate taking Phaeoporus Obliquus as a example.Described reaction liquid supplying device 400 is used for described reaction
The liquid carbon dioxide of supply high pressure in cabin 100, its pressure is typically sized to several MPas to dozens of MPa.Work as pulverizing
Before technique starts, first by described feeding device 300 by a certain amount of, first pulverizing, Phaeoporus Obliquus that granule is larger pass through described
Charging aperture 110 is sent in described reaction cabin 100, makes described reactant liquor supply dress by described control device 200 output order afterwards
Put 400 a certain amount of liquid carbon dioxide is passed through in reaction cabin 100.The more described blood pressure lowering of diameter of cylindrical discharging opening 120
Opening and closing element 510 is big, and both are coaxially arranged, and Formation cross-section is the discharging gap of annular between the two, when two kinds participate in reaction
Material mutually merge after, control device 200 sends instruction at once so that described rapid dropping equipment 500 works, now, institute
State relatively described discharging opening 120 upward sliding of blood pressure lowering opening and closing element 510, expose the discharging gap of described discharging opening 120, now react
Air pressure in cabin 100 reduces rapidly.Additionally, above-mentioned crushing material system is also included in reaction cabin described in real-time monitoring 100
The pressure indicating gage 700 of pressure values.Display numerical value by observation pressure indicating gage 700 is extremely identical with optimum response pressure value
When, operator provide control device 200 and instruct, and now described blood pressure lowering opening and closing element 510 resets rapidly, with described discharging opening 120
Recompounding is airtight.Phaeoporus Obliquus granule in reaction cabin 100 can be exploded in it due to the effect of inside and outside pressure difference, from
And be fragmented into the less granule of size, thus realize the purpose pulverized.
Described reaction liquid supplying device 400 includes fluidsupply container 420, liquid feeding pipeline 440 and flow control valve 460, described
One end of liquid feeding pipeline 440 is connected with described fluidsupply container 420, the other end of described liquid feeding pipeline 440 and described reaction cabin 100
Connection, described flow control valve 460 is connected on described liquid feeding pipeline 440.Described fluidsupply container 420 is preferably high-pressure liquid two
Oxidation canister, certainly in other embodiments can also high-pressure liquid nitrogen tank.The outlet of liquid carbon dioxide tank and liquid feeding pipeline
440 wherein one end connects, and its exit is provided with electromagnetic valve, and electromagnetic valve is connected with control device 200 electricity row and by controlling
Device 200 controls being turned on and off of liquid carbon dioxide tank, and controllability is good, safe and reliable.Additionally, on the side wall of cylinder
It is preset with inlet opening, the other end of liquid feeding pipeline 440 is connected with inlet opening, further, described water influent pipeline is also equipped with
Flow control valve 460, so setting more flexible real-time control can be passed through the stream of the liquid carbon dioxide in reaction cabin 100
Amount, and then control the pressure size in reaction cabin 100, simultaneously with above-mentioned pressure indicating gage 700 cooperating it can be ensured that reacting
Reaction pressure in cabin 100 is in desired value scope, thus ensureing that the pulverizing reaction effect in reaction cabin 100 is good.
Wherein in an embodiment, described feeding device 300 includes inlet valve 320, and described inlet valve 320 includes valve rod
322 and the valve head 324 that is connected with described valve rod 322, described reaction cabin 100 include being provided with opening reative cell 130 and with anti-
Answer the upper lid 140 that room 130 connects, described valve head 324 and described opening can close fit, described charging aperture 110 is arranged at described
Upper lid 140, forms feeding-passage 150 between described upper lid 140 and described valve head 324, described charging aperture 110, described charging are logical
Road 150 is sequentially communicated with the opening of described reative cell 130.
In this embodiment, described feeding device 300 also includes motor and first reducing mechanism.When Phaeoporus Obliquus raw material enters
After reducing mechanism at the beginning of entering is processed into the larger granule of granularity, inlet valve 320 is lifted by now motor action upwards, to reveal
Go out the annulus of charging aperture 110, can be by the first larger granularity pulverized by the feed mechanism of similar conveyer belt or feeding tube
Phaeoporus Obliquus gradually sent in described reative cell 130 by described charging aperture 110, described feeding-passage 150.When the Phaeoporus Obliquus sent into
Response magnitude when meeting optimal values, motor inverts and so that inlet valve 320 is declined so that described valve head 324 is anti-with described
The opening answering room 130 closes.So setting can greatly improve the automaticity of crushing system, while improve production efficiency
Greatly improve economy.Preferably, the lower surface of described valve head 324 is provided with a ring annular groove, its shape and size with described
Columnar reative cell 130 matches, and thus can realize good obturation effect, it is to avoid excessive Phaeoporus Obliquus granule penetrates into anti-
Answer in room 130, affect crushing effect.
Described rapid dropping equipment 500 include actuator 530 that force piece 520 is connected with described force piece 520 and with
The described blood pressure lowering opening and closing element 510 that described actuator 530 connects, described blood pressure lowering opening and closing element 510 include slide bar 512 and with described cunning
The closure member 514 that bar 512 end connects, described reaction cabin 100 is located at and is provided with pressure contact portion 160 at described discharging opening 120, described closes
Component 514 is fastened with described pressure contact portion 160.
In the present embodiment, described blood pressure lowering opening and closing element 510 is blow-off valve, and above-mentioned reative cell 130 is similar to cylindrical structure, circle
The lower end of cylinder includes the conical section that sectional area is gradually reduced, and the cylindrical section being connected with conical section, cylindrical section and reaction cabin 100
Lower cover connect.Described discharging opening 120 is arranged at the centre of lower cover, discharging opening 120 with diameter greater than described slide bar 512
Diameter, thus described slide bar 512 relatively described discharging opening 120 can slide up and down under the driving effect of motor, simultaneously
Form the discharging gap of annular, so setting can be in order to go out to material between described discharging opening 120 and described slide bar 512
Material speed is limited, and improves the Modulatory character of system.Additionally, described closure member 514 is preferably becoming with described slide bar 512 one
Type, to guarantee having enough bonding strengths, improves dependability and the life-span of blood pressure lowering opening and closing element 510.Described pressure contact portion 160
It is the side wall circle ledge structure that cardiac prominence sets thereto along cylindrical section, the bottom surface of described closure member 514 can be with Step-edge Junction
Structure closely fastens, and so setting not only can ensure constant reaction pressure in reaction cabin 100 it is ensured that the crushing effect of material
Good, material can also be avoided simultaneously to leak, improve sealing property and the functional reliability of reaction cabin 100.
Further, above-mentioned crushing material system also includes sealing member 600, and described sealing member 600 is arranged at described crimping
Portion 160 is simultaneously fastened with described opening and closing element 510.In the present embodiment, described sealing member 600 is preferably rubber seal, will
It is installed at above-mentioned pressure contact portion 160, and with described closure member 514 press fit, sealing effectiveness not only can be improved further,
Simultaneously when described decompression opening and closing element 510 declines rapidly, may also operate as the effect of buffer shock-absorbing, it is to avoid with pressure contact portion 160
Stiff to hard rigid collision, eliminate collision and produce the hidden danger of structural damage.
Additionally, described closure member 514 is provided with first annular inclined-plane 514a, described sealing member 600 is provided with the second annular slope
620, described first annular inclined-plane 514a is cooperated with described second annular slope 620.So rubber can be increased close for setting
Seal and the contact area of closure member 514, thus improve the sealing property of blow-off valve further.
Above-mentioned crushing material system also includes adjusting means 800, and described adjusting means 800 includes being arranged at described reaction cabin
Monitoring part 820 in 100 electrically connects with the described monitoring Volume Indicator 840 that is connected of part 820 and with described control device 200
The eduction valve 860 connecing, described reaction cabin 100 is provided with relief port, and described eduction valve 860 is connected with described relief port pipeline.Wherein,
Above-mentioned crushing system can preset one group of optimal response parameter combination in control device 200, including pressure, liquid dioxy
Change the numerical value such as carbon capacity, by arranging described monitoring part 820 in reaction cabin 100 internal side wall, monitoring part 820 is preferably liquid level
Sensor, it with the liquid level of the liquid carbon dioxide in real-time monitoring reaction cabin 100, and Monitoring Data can be transmitted to appearance
Amount indicator 840 supplies staff to observe.When the liquid level of carbon dioxide is low compared with preset value or higher, accordingly permissible
By adjusting, flow control valve 460 increases supply liquid carbon dioxide or regulation eduction valve 860 reduces in reaction cabin 100
Liquid carbon dioxide carrying out flexible modulation, thus ensureing that the capability value participating in the liquid carbon dioxide of reaction is suitable, and then
Guarantee to pulverize the effect of reaction so that pulverizing the Phaeoporus Obliquus granular size obtaining to meet target requirement.
Additionally, above-mentioned crushing system also includes material recycling device 900, described material recycling device 900 include with described
Feed back cylinder 920 that discharging opening 120 connects and be arranged at filtration members 940 in described feed back cylinder 920, described filtration members 940 are provided with
Multiple filtering holes.Wherein, one end of described feed back cylinder 920 is connected with the lower cover of reaction cabin 100, so that described discharging opening 120 is located at
In cylinder lumen, other end docking finished product Phaeoporus Obliquus granule following process mechanism (the such as sorting equipment, packaging of feed back cylinder 920
Device etc.).In addition, described filtration members 940 are preferably filter screen in the present embodiment, filter screen are provided with multiple mesh and (filter
Hole), the size of mesh is matched with the Phaeoporus Obliquus granular size needing, thus filter screen is installed on the intracavity of feed back cylinder 920, can
To screen to the Phaeoporus Obliquus granule after grinding and processing, and then the Phaeoporus Obliquus granule that makes to meet the requirements carries out production through filter screen and makes
With, and the particulate blockage insufficiently pulverized, granule is larger is lived.So setting can greatly improve this material-pulverizing device
Functional reliability and effectiveness, improve the material suitability producing.
Further, described material recycling device 900 also includes trap 960, and described feed back cylinder 920 is near described filtration
The side wall of part 940 is provided with feedback outlet 962, and described feedback outlet 962 is connected with described trap 960 pipeline, and described trap
960 are connected with described feeding device 300.In the present embodiment, described feedback outlet 962 arranges the lower wall of described feed back cylinder 920
Place, in embodiment one, described feedback outlet 962 includes an opening, and the baffle plate with opening cooperation, during original state, baffle plate
Connect in opening gear, to avoid Phaeoporus Obliquus granule to fall in trap 960, thus reducing the material quantum of output of crushing system.Serve as
When accumulation has more large granular materials at filter screen, now open baffle plate, large granular materials can be fallen in trap 960；?
In embodiment two, described feedback outlet 962 is the multiple through holes being evenly arranged opening up at the lower wall of described feed back cylinder 920,
Through hole with diameter greater than large-sized Phaeoporus Obliquus granule, and then may insure undesirable larger particles fall in through hole
Enter in trap 960.Afterwards, Phaeoporus Obliquus granule big for the particle diameter of collection is delivered to feeding device 300 by described trap 960
Carry out reworking, so setting can be realized the circulation of Phaeoporus Obliquus material and fully processes, and greatly improve the utilization rate of raw material, from
And improve crushing material system economy.
Each technical characteristic of embodiment described above can arbitrarily be combined, for making description succinct, not to above-mentioned reality
The all possible combination of each technical characteristic applied in example is all described, as long as however, the combination of these technical characteristics is not deposited
In contradiction, all it is considered to be the scope of this specification record.
Embodiment described above only have expressed several embodiments of the present utility model, and its description is more concrete and detailed,
But therefore can not be interpreted as the restriction to utility model patent scope.It should be pointed out that the common skill for this area
For art personnel, without departing from the concept of the premise utility, some deformation can also be made and improve, these broadly fall into
Protection domain of the present utility model.Therefore, the protection domain of this utility model patent should be defined by claims.
Claims (10)
1. a kind of crushing material system it is characterised in that include be provided with the reaction cabin of charging aperture and discharging opening, control device and
Feeding device, reaction liquid supplying device and the rapid dropping equipment being all electrically connected with described control device, described feeding device
With the cooperation of described charging aperture, described reaction liquid supplying device and described reaction cabin pipeline connection, described rapid dropping equipment includes
Blood pressure lowering opening and closing element, described blood pressure lowering opening and closing element is slidably matched with the discharging opening of described reaction cabin.
2. crushing material system according to claim 1 is it is characterised in that described feeding device includes inlet valve, described
Inlet valve includes valve rod and the valve head being connected with described valve rod, described reaction cabin include being provided with opening reative cell and with reaction
The upper lid that room connects, described valve head and described opening can close fit, described charging aperture is arranged at described upper lid, described upper lid with
Form feeding-passage, described charging aperture, described feeding-passage and the opening of described reative cell are sequentially communicated between described valve head.
3. crushing material system according to claim 1 it is characterised in that described rapid dropping equipment include force piece,
The actuator being connected with described force piece and the described blood pressure lowering opening and closing element being connected with described actuator, described blood pressure lowering opening and closing element bag
Include slide bar and the closure member being connected with described slide bar end, described reaction cabin is provided with pressure contact portion positioned at described discharge outlet, described
Closure member is fastened with described pressure contact portion.
4. it is characterised in that also including sealing member, described sealing member is arranged crushing material system according to claim 3
It is fastened in described pressure contact portion and with described opening and closing element.
5. crushing material system according to claim 4 is it is characterised in that described closure member is provided with first annular inclined-plane,
Described sealing member is provided with the second annular slope, and described first annular inclined-plane is cooperated with described second annular slope.
6. the crushing material system according to any one of claim 1 to 5 is it is characterised in that also include for real-time monitoring
The pressure indicating gage of pressure values in described reaction cabin.
7. the crushing material system according to any one of claim 1 to 5 is it is characterised in that also including adjusting means, described
Adjusting means include being arranged at the Volume Indicator that the monitoring part in described reaction cabin is connected with described monitoring part and with described
The eduction valve that control device is electrically connected with, described reaction cabin is provided with relief port, and described eduction valve is connected with described relief port pipeline.
8. the crushing material system according to any one of claim 1 to 5 is it is characterised in that also include material recycling device,
Described material recycling device is included the feed back cylinder being connected with described discharging opening and is arranged at filtration members in described feed back cylinder, institute
State filtration members and be provided with multiple filtering holes.
9. crushing material system according to claim 8 is it is characterised in that described material recycling device also includes reclaiming
Part, described feed back cylinder is provided with feedback outlet near the side wall of described filtration members, and described feedback outlet is connected with described trap pipeline,
And described trap is connected with described feeding device.
10. crushing material system according to claim 1 is it is characterised in that described reaction liquid supplying device includes feed flow
Container, liquid feeding pipeline and flow control valve, one end of described liquid feeding pipeline is connected with described fluidsupply container, described liquid feeding pipeline
The other end is connected with described reaction cabin, and described flow control valve is connected on described liquid feeding pipeline.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620913152.5U CN205966109U (en) | 2016-08-19 | 2016-08-19 | Comminuted system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620913152.5U CN205966109U (en) | 2016-08-19 | 2016-08-19 | Comminuted system |
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| CN205966109U true CN205966109U (en) | 2017-02-22 |
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| CN201620913152.5U Active CN205966109U (en) | 2016-08-19 | 2016-08-19 | Comminuted system |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110681445A (en) * | 2018-09-21 | 2020-01-14 | 昆明田康科技有限公司 | Plant water and preparation method thereof |
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2016
- 2016-08-19 CN CN201620913152.5U patent/CN205966109U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110681445A (en) * | 2018-09-21 | 2020-01-14 | 昆明田康科技有限公司 | Plant water and preparation method thereof |
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