CN205368170U - Organic water -culturing nutrient solution preparation facilities - Google Patents
Organic water -culturing nutrient solution preparation facilities Download PDFInfo
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- CN205368170U CN205368170U CN201521091721.4U CN201521091721U CN205368170U CN 205368170 U CN205368170 U CN 205368170U CN 201521091721 U CN201521091721 U CN 201521091721U CN 205368170 U CN205368170 U CN 205368170U
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- nutrient solution
- nutritional solution
- fermentation
- preparation facilities
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/40—Bio-organic fraction processing; Production of fertilisers from the organic fraction of waste or refuse
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Abstract
The utility model relates to an organic agriculture cultivates technical field, especially relates to an organic water -culturing nutrient solution preparation facilities. The utility model provides an organic water -culturing nutrient solution preparation facilities, including fermented mechanism, stock solution mechanism, sanitizing means and filtering mechanism. The fermentation production water -culturing nutrient solution of fermentation mechanism stoste, the inside germ of nutrient solution stoste can be killed to nutrient solution stoste behind sanitizing means, can effectively prevent to use this nutrient solution to carry out the vegetables emergence disease of cultivating, and the solid particle thing filtering in filtering mechanism is with nutrient solution stoste can prevent nutrient solution stoste plug the pipe simultaneously, and the raw materials that adopts at the in -process of preparing in -process organotrophy liquid is nature raw material, the advantage of cultivation and nutrient solution cultivation merges organically, has overcome traditional organic soil and has cultivated native communicable disease problem occurred frequently, has widened organic vegetable's cultivation mode, improve the quality of water planting vegetables simultaneously, avoided the emergence of water planting vegetables nitrate enrichment.
Description
Technical field
This utility model relates to organic technical field of agricultural cultivation, particularly relates to a kind of sized organic hydroponic nutritional solution preparation facilities.
Background technology
Organic agriculture follows continuable development principle in agricultural product production process, without the fertilizer of synthetic, pesticide, growth regulator in production estimation process, do not adopt technique for gene engineering and product thereof, adopt the technological means of sustainable development, maintain continual and steady mode of agriculture.By being in that organic agriculture production process decreases the use of pesticide, chemical fertilizer, it is to avoid the pollution residual of agricultural product, it is possible to the safety and environmental protection food of output high-quality, be conducive to people's health, reduce disease and occur.Especially in recent years, along with the raising of people's living standard, the demand of organic farm products increases year by year.But, owing to the pattern of farming in farmland is comparatively single, particularly under the facility condition of relative closure, soil easily accumulates pathogenic microorganism and harmful substance, constrains the raising of the yield and quality of organic farm products to a certain extent.
Soilless culture can break away from the constraint of soil, it also avoid continuous cropping obstacle and infectious disease that soil cultivation occurs simultaneously, decreases using of pesticide, reduces agriculture production cost while improving quality of vegetable.Water planting is to develop a kind of form faster in cultivation technique without soil, and its core is to utilize nutritional solution to replace soil, creates suitable rhizospheric environment for crop, makes crop growth period shortening, yield and quality improve.And the fertilizer preparation of the multiplex chemosynthesis of nutritional solution used by water planting forms, migrate in the nutritional solution speed of diffusion of nutrient is far longer than soil, and leaf vegetables crop mostly is nitrophilous crop, therefore the phenomenon ubiquity that nutrient fluid cultivation vegetable nitrate exceeds standard.
Therefore, for the problems referred to above, it is necessary to the production that a kind of technology is capable of under organic conditions mill water culture nutrient solution, organic farming and nutriculture are integrated, under organic conditions, realizes the cultivating superior high-yield of pot-herb.
Utility model content
(1) to solve the technical problem that
The technical problems to be solved in the utility model is: provide a kind of sized organic hydroponic nutritional solution preparation facilities, utilize this device can carry out the preparation of water planting organic nutrient solution for cultivating, it is that the leaf vegetables water planting production realized under organic farming pattern provides safeguard simultaneously, thus overcoming the tradition organic soil cultivation mode dependence to cultivation medium, fundamentally contain the outburst of cultivating soil spreading venereal diseases insect pest.
(2) technical scheme
In order to solve above-mentioned technical problem, this utility model provides a kind of sized organic hydroponic nutritional solution preparation facilities, including the fermentation mechanism for fermented organic material, for storing the liquid storage mechanism of nutritional solution stock solution, described fermentation mechanism is connected with described liquid storage mechanism by pipeline, is additionally provided with disinfecting mechanism and filter mechanism on described pipeline.
Preferably, it is provided with the agitator for stirring organic materials in described fermentation mechanism.
Preferably, described disinfecting mechanism is ultraviolet ray disinfector, and described ultraviolet ray disinfector is between fermentation mechanism and filter mechanism.
Preferably, the pipeline between described ultraviolet ray disinfector and fermentation mechanism is additionally provided with switch valve.
Preferably, described filter mechanism includes the first filter element, the second filter element and the 3rd filter element that set gradually.
Preferably, described first filter element is sand and gravel filter, and its filtering accuracy is 0.5mm, and described second filter element and the 3rd filter element are laminated filter, the filtering accuracy of described second filter element is 0.1mm, and the filtering accuracy of described 3rd filter element is 0.02mm.
Preferably, also including driving mechanism, described driving mechanism is for being delivered to the nutritional solution stock solution produced of fermenting in fermentation mechanism in liquid storage mechanism.
Preferably, described liquid storage mechanism is fluid reservoir, and described driving mechanism is the vacuum pump being connected with described fluid reservoir.
Preferably, the exit of described fluid reservoir is provided with check valve.
(3) beneficial effect
Technique scheme of the present utility model has the advantage that this utility model provides a kind of sized organic hydroponic nutritional solution preparation facilities, including fermentation mechanism, liquid storage mechanism, disinfecting mechanism and filter mechanism.Fermentation generation mill water culture nutrient solution stock solution is carried out by adding organic materials in fermentation mechanism, nutritional solution stock solution can kill the pathogenic bacteria within nutritional solution stock solution after disinfecting mechanism, can effectively prevent the vegetable generation disease using this nutritional solution to carry out cultivating, through filter mechanism, the solid particulate matter in nutritional solution stock solution is filtered simultaneously, it is possible to prevent nutritional solution stock solution blocking pipeline, to ensure that what water planting worked is smoothed out；And the raw material adopted in the process of organic nutrient solution for cultivating in preparation process is natural material, the addition of prosthetic synthetic, the advantage of organic farming and nutrient fluid cultivation is merged, overcome the problem that tradition organic soil cultivating soil infectious disease is occurred frequently, widen the cultivation mode of organic vegetable；Improve the quality of vegetable aquaculture, it is to avoid the generation of vegetable aquaculture nitrate enrichment simultaneously.
Accompanying drawing explanation
This utility model is above-mentioned and/or the advantage of additional aspect is from conjunction with will be apparent from easy to understand the accompanying drawings below description to embodiment, wherein:
Fig. 1 is the structural representation of the sized organic hydroponic nutritional solution preparation facilities described in this utility model embodiment.
Wherein, in Fig. 1, corresponding relation between accompanying drawing labelling and component names is:
1, fermentation mechanism, 2, agitator, 3, pipeline, 4, switch valve, 5, disinfecting mechanism, 6, filter mechanism, 7, fluid reservoir, 8, vacuum pump, 9, check valve.
Detailed description of the invention
In description of the present utility model, it is necessary to explanation, unless otherwise clearly defined and limited, term " installation ", " being connected ", " connection " should be interpreted broadly, for instance, it is possible to it is fixing connection, it is also possible to be removably connect, or connect integratedly；Can be mechanically connected, it is also possible to be electrical connection；Can be joined directly together, it is also possible to be indirectly connected to by intermediary, it is possible to be the connection of two element internals.For the ordinary skill in the art, it is possible to concrete condition understands above-mentioned term concrete meaning in this utility model.Additionally, in description of the present utility model, except as otherwise noted, " multiple " are meant that two or more.
For making the purpose of this utility model embodiment, technical scheme and advantage clearly, below in conjunction with the accompanying drawing in this utility model embodiment, technical scheme in this utility model embodiment is clearly and completely described, obviously, described embodiment is a part of embodiment of the present utility model, rather than whole embodiments.Based on the embodiment in this utility model, the every other embodiment that those of ordinary skill in the art obtain under the premise not making creative work, broadly fall into the scope of this utility model protection.
As shown in Figure 1, this utility model provides a kind of sized organic hydroponic nutritional solution preparation facilities, including the fermentation mechanism 1 for fermented organic material, for storing the liquid storage mechanism of nutritional solution stock solution, described fermentation mechanism 1 is connected with described liquid storage mechanism by pipeline 3, is additionally provided with disinfecting mechanism 5 and filter mechanism 6 on described pipeline 3.The sized organic hydroponic nutritional solution preparation facilities that this utility model provides, fermentation generation mill water culture nutrient solution stock solution is carried out by adding organic materials in fermentation mechanism 1, nutritional solution stock solution can kill the pathogenic bacteria within nutritional solution stock solution after disinfecting mechanism 5, can effectively prevent the vegetable generation disease using this nutritional solution to carry out cultivating, through filter mechanism 6, the solid particulate matter in nutritional solution stock solution is filtered simultaneously, it is possible to prevent nutritional solution stock solution blocking pipeline 3, to ensure that what water planting worked is smoothed out；And the raw material adopted in the process of organic nutrient solution for cultivating in preparation process is natural material, the addition of prosthetic synthetic, the advantage of organic farming and nutrient fluid cultivation is merged, overcome the problem that tradition organic soil cultivating soil infectious disease is occurred frequently, widen the cultivation mode of organic vegetable；Improve the generation of vegetable aquaculture nitrate enrichment simultaneously.
Wherein, fermentation mechanism 1 is for the initial fermentation of organic materials, alternatively, described organic materials bean cake, plant ash and bone meal mix according to the ratio of 2:1:1, concrete sweat is: first joined by organic materials in fermentation mechanism 1, it is added into 1/5 place of fermentation mechanism 1, it is subsequently adding clear water, add the clear water of 5 times of volumes, fermentation process can be carried out, the time of fermentation is generally 5-7 days, alternatively, fermentation can be stirred to interpolation microbial bacterial agent in fermentation mechanism 1 to accelerate fermentation progress, so fermentation period can be foreshortened to 3-5 days.
In the nutritional solution of fermentation generation, appropriate quick lime is put into again after fermentation ends, alternatively, the ratio that the dosage putting into quick lime adds 10g quick lime generally according to every liter of water adds quick lime, the pathogenic microorganism put in the nutritional solution that quick lime utilizes the disinfective action of quick lime that fermentation is produced on the one hand kills process, and still further aspect utilizes the poisonous and harmful substances that the alkalescence of quick lime promotes sweat to generate to decompose；After sterilization, valve can be opened, start vacuum pump 8, fluid reservoir 7 is formed negative pressure, the nutritional solution produced at the effect bottom fermentation of negative pressure passes sequentially through ultra violet sterilizer, filter element enters into stock solution and stores unit, can complete the sterilization to nutritional solution stock solution and filtration.
Wherein, in described fermentation mechanism 1, agitator 2 is installed, for during the fermentation material being stirred, it is made fully to ferment, preferably, described disinfecting mechanism 5 is ultraviolet ray disinfector, described ultraviolet ray disinfector is between fermentation mechanism 1 and filter mechanism 6, nutritional solution for fermentation is produced carries out secondary sterilization, to guarantee the pathogenic microorganism of the nutritional solution that fermentation produces effectively is killed, simultaneously the pipeline 3 between described ultraviolet ray disinfector and fermentation mechanism 1 is additionally provided with switch valve 4, for controlling nutritional solution stock solution to the circulation in car pipe.
Alternatively, sized organic hydroponic nutritional solution preparation facilities also includes driving mechanism, described driving mechanism is for being delivered in liquid storage mechanism by the nutritional solution stock solution that fermentation in fermentation mechanism 1 produces, preferably, described liquid storage mechanism is fluid reservoir 7, and described driving mechanism is the vacuum pump 8 being connected with described fluid reservoir 7, negative pressure is formed by inhaling in fluid reservoir 7 by vacuum pump 8, so that nutritional solution stock solution smoothly enters in fluid reservoir 7, to accelerate the rate of filtration, improve filter efficiency.And, it is provided with check valve 9 in the exit of described fluid reservoir 7, the exit of fluid reservoir 7 lower end is located at by described check valve 9, can prevent gas in vacuum pump 8 start-up course from entering in fluid reservoir 7 from lower end leakage fluid dram, guarantee formation vacuum in fluid reservoir 7, it should be noted that the reserved outlet connecting vacuum pump 8 not above above fluid reservoir 7 of the liquid level of fluid reservoir 7, during to prevent vacuum pump 8 from running, nutritional solution stock solution is sucked vacuum pump 8.
Preferably, described filter mechanism 6 includes setting gradually the first filter element, the second filter element and the 3rd filter element, described first filter element is sand and gravel filter, its filtering accuracy is 0.5mm (namely can filter the solid particulate matter of more than particle diameter 0.5mm), described second filter element and the 3rd filter element are laminated filter, the filtering accuracy of described second filter element is 0.1mm, and the filtering accuracy of described 3rd filter element is 0.02mm；Filter mechanism is arranged to the mode of three-stage filtration, it is possible to ensure filtering accuracy, it is ensured that enter the nutritional solution stock solution in fluid reservoir 7 and will not be mixed with the solid particulate matter of big particle diameter, to prevent the blocking of liquid-transport pipe-line 3.
It should be noted that, the nutritional solution stock solution being stored in fluid reservoir 7 needs its electrical conductivity and pH are adjusted before for raise crop, typically via adding clear water-reducible scheme, the EC value of stock solution is adjusted in the scope of 1.0-1.2ms/m, by the method for addition acetic acid by the pH regulator of diluted nutritional solution to the scope of 5.5-6.5, namely can be used for culturing vegetable.
Process embodiments of the invention being produced nutritional solution stock solution below in conjunction with accompanying drawing 1 is described in detail.
According to the ratio of 3:1:1 by bean cake, plant ash, bone meal mix homogeneously, join in fermentation mechanism 1, the clear water of about 5 times of volumes is added again in fermentation mechanism 1, it is eventually adding microbial bacterial agent, fermentation process can be carried out, needing the nutritional solution that fermentation is produced by turn on agitator 2 to be stirred during the fermentation, general stirring frequency is 10 minutes/hour.In the nutritional solution produced that ferments, add 5 kilograms of quick lime after fermentation ends, continue stirring, until the nutritional solution that quick lime and fermentation produce is thoroughly mixed.It is then turned on vacuum pump 8 and carries out the sterilization of nutritional solution, the filtration that fermentation produces, prepare the stock solution of organic nutrient solution for cultivating, regulate EC and the pH value of stock solution successively simultaneously, normally due to nutritional solution stock solution is concentrated solution, its EC (refers to the concentration of soluble-salt in solution), and value is higher, therefore by adding the method for clear water, the EC value of nutritional solution is regulated to the scope of 1.0-1.2, by adding the method for brewing vinegar, the pH value of nutritional solution is regulated to the scope of 5.5-6.5, namely can be used for the production of sized organic hydroponic Caulis et Folium Lactucae Sativae.Compared with tradition organic soil cultivation, utilizing organic nutrient solution for cultivating prepared by this device and method to carry out water planting Caulis et Folium Lactucae Sativae production, it is possible to the listing phase shifts to an earlier date more than 5 days, the growth uniformity is also significantly greater than organic soil cultivation.
In sum, this utility model provides a kind of sized organic hydroponic nutritional solution preparation facilities, including fermentation mechanism, liquid storage mechanism, disinfecting mechanism and filter mechanism.Fermentation generation mill water culture nutrient solution stock solution is carried out by adding organic materials in fermentation mechanism, nutritional solution stock solution can kill the pathogenic bacteria within nutritional solution stock solution after disinfecting mechanism, can effectively prevent the vegetable generation disease using this nutritional solution to carry out cultivating, through filter mechanism, the solid particulate matter in nutritional solution stock solution is filtered simultaneously, it is possible to prevent nutritional solution stock solution blocking pipeline, to ensure that what water planting worked is smoothed out；And the raw material adopted in the process of organic nutrient solution for cultivating in preparation process is natural material, the addition of prosthetic synthetic, the advantage of organic farming and nutrient fluid cultivation is merged, overcome the problem that tradition organic soil cultivating soil infectious disease is occurred frequently, widen the cultivation mode of organic vegetable；Improve the quality of vegetable aquaculture, it is to avoid the generation of vegetable aquaculture nitrate enrichment simultaneously.
Last it is noted that above example is only in order to illustrate the technical solution of the utility model, it is not intended to limit；Although this utility model being described in detail with reference to previous embodiment, it will be understood by those within the art that: the technical scheme described in foregoing embodiments still can be modified by it, or wherein portion of techniques feature is carried out equivalent replacement；And these amendments or replacement, do not make the essence of appropriate technical solution depart from the spirit and scope of each embodiment technical scheme of this utility model.
Claims (9)
1. a sized organic hydroponic nutritional solution preparation facilities, it is characterized in that: include the fermentation mechanism (1) for fermented organic material, for storing the liquid storage mechanism of nutritional solution stock solution, described fermentation mechanism (1) is connected with described liquid storage mechanism by pipeline (3), is additionally provided with disinfecting mechanism (5) and filter mechanism (6) on described pipeline (3).
2. sized organic hydroponic nutritional solution preparation facilities according to claim 1, it is characterised in that: it is provided with the agitator (2) for stirring organic materials in described fermentation mechanism (1).
3. sized organic hydroponic nutritional solution preparation facilities according to claim 1, it is characterized in that: described disinfecting mechanism (5) is ultraviolet ray disinfector, described ultraviolet ray disinfector is positioned between fermentation mechanism (1) and filter mechanism (6).
4. sized organic hydroponic nutritional solution preparation facilities according to claim 3, it is characterised in that: the pipeline (3) between described ultraviolet ray disinfector and fermentation mechanism (1) is additionally provided with switch valve (4).
5. sized organic hydroponic nutritional solution preparation facilities according to claim 1, it is characterised in that: described filter mechanism (6) includes the first filter element, the second filter element and the 3rd filter element that set gradually.
6. sized organic hydroponic nutritional solution preparation facilities according to claim 5, it is characterized in that: described first filter element is sand and gravel filter, its filtering accuracy is 0.5mm, described second filter element and the 3rd filter element are laminated filter, the filtering accuracy of described second filter element is 0.1mm, and the filtering accuracy of described 3rd filter element is 0.02mm.
7. sized organic hydroponic nutritional solution preparation facilities according to claim 1, it is characterised in that: also including driving mechanism, described driving mechanism is for being delivered to the nutritional solution stock solution that fermentation in fermentation mechanism (1) produces in liquid storage mechanism.
8. sized organic hydroponic nutritional solution preparation facilities according to claim 7, it is characterised in that: described liquid storage mechanism is fluid reservoir (7), and described driving mechanism is the vacuum pump (8) being connected with described fluid reservoir (7).
9. sized organic hydroponic nutritional solution preparation facilities according to claim 8, it is characterised in that: the exit of described fluid reservoir (7) is provided with check valve (9).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521091721.4U CN205368170U (en) | 2015-12-24 | 2015-12-24 | Organic water -culturing nutrient solution preparation facilities |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521091721.4U CN205368170U (en) | 2015-12-24 | 2015-12-24 | Organic water -culturing nutrient solution preparation facilities |
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| CN205368170U true CN205368170U (en) | 2016-07-06 |
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| CN201521091721.4U Expired - Fee Related CN205368170U (en) | 2015-12-24 | 2015-12-24 | Organic water -culturing nutrient solution preparation facilities |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106905009A (en) * | 2017-02-24 | 2017-06-30 | 北京农业智能装备技术研究中心 | Vegetables straw processing system and method |
| CN107969312A (en) * | 2017-12-09 | 2018-05-01 | 佛山市高明区菜花园农业科技有限公司 | Nutrient solution preparation facilities is used in a kind of water culture plantation |
-
2015
- 2015-12-24 CN CN201521091721.4U patent/CN205368170U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106905009A (en) * | 2017-02-24 | 2017-06-30 | 北京农业智能装备技术研究中心 | Vegetables straw processing system and method |
| CN107969312A (en) * | 2017-12-09 | 2018-05-01 | 佛山市高明区菜花园农业科技有限公司 | Nutrient solution preparation facilities is used in a kind of water culture plantation |
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| Date | Code | Title | Description |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160706 Termination date: 20161224 |
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| CF01 | Termination of patent right due to non-payment of annual fee |