CN109892221A - The efficient recycling and processing equipment of one plant nutrient liquor and method - Google Patents

The efficient recycling and processing equipment of one plant nutrient liquor and method Download PDF

Info

Publication number
CN109892221A
CN109892221A CN201910148245.1A CN201910148245A CN109892221A CN 109892221 A CN109892221 A CN 109892221A CN 201910148245 A CN201910148245 A CN 201910148245A CN 109892221 A CN109892221 A CN 109892221A
Authority
CN
China
Prior art keywords
nutrient solution
unit
plant
nutrition liquid
quartz sand
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CN201910148245.1A
Other languages
Chinese (zh)
Inventor
李婷
艾为党
张良长
李家练
张岍
武重阳
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Shenzhen Greenhouse Interplanetary Space Science And Technology Research Institute
China Astronaut Research and Training Center
Original Assignee
Shenzhen Greenhouse Interplanetary Space Science And Technology Research Institute
China Astronaut Research and Training Center
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Shenzhen Greenhouse Interplanetary Space Science And Technology Research Institute, China Astronaut Research and Training Center filed Critical Shenzhen Greenhouse Interplanetary Space Science And Technology Research Institute
Priority to CN201910148245.1A priority Critical patent/CN109892221A/en
Publication of CN109892221A publication Critical patent/CN109892221A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P60/00Technologies relating to agriculture, livestock or agroalimentary industries
    • Y02P60/20Reduction of greenhouse gas [GHG] emissions in agriculture, e.g. CO2
    • Y02P60/21Dinitrogen oxide [N2O], e.g. using aquaponics, hydroponics or efficiency measures

Abstract

The present invention relates to the efficient recycling and processing equipment of a plant nutrient liquor and methods, including circulating cultivation frame, standing reservoir case, nutrient solution mother liquor supply unit, quartz sand-activated carbon adsorption retention unit and high-strength ultraviolet light mineralization unit;Nutrient solution mother liquor supply unit is connect with standing reservoir case;The outlet of standing reservoir case is connect by the first infusion branch and the second infusion branch with circulating cultivation frame import, and the outlet of circulating cultivation frame is connect with standing reservoir case import, to carry out the circulation of plant nutrition liquid;First infusion branch curb nutrient input send direction to be successively arranged quartz sand-activated carbon adsorption retention unit and high-strength ultraviolet light mineralization unit;The present invention can supplement the nutrient of plant nutrition liquid;It is degraded and is removed using plant nutrition liquid regenerative system, and to crop residues decomposition suspended matter, root system secretion organic matter, harmful microorganism and the variant viral in plant nutrition liquid, effectively avoided crop from continuous cropping obstacle occur, ensure plant efficient growth.

Description

The efficient recycling and processing equipment of one plant nutrient liquor and method
Technical field
The invention belongs to the efficient recycling processing technique field of water planting crops plant nutrition liquid more particularly to a kind of plant nutrients The efficient recycling and processing equipment of liquid and method.
Background technique
One of in such a way that hydroponic plant cultivation mode is closed system implants Efficient Cultivation, plant nutrition liquid supply The microelements such as a great number of elements such as nitrogen, phosphorus needed for plant growth, potassium and boron, zinc, manganese.Appoint meeting the following Long-term Manned Spaceflight In the closed system of business, resource is carried to reduce, and reduce waste discharge as far as possible, need to realize the long-term efficient of plant nutrition liquid Circulating and recovering.Plant nutrition liquid recycles for a long time faces two problems: first is that in plant nutrition liquid nutrient missing, shadow It rings plant normal growth and forms complete life cycle;Second is that since secretions from plant roots and crop residues decomposition substance are tired Long-pending, organic matter accumulation in confined space waste water circulatory system phegma, and a large amount of harmful microorganisms are bred, and plant is caused to generate Continuous cropping obstacle, cause yield reduce, quality deteriorate, bearing status be deteriorated the phenomenon that.To solve the above problems, realizing closed system Middle hydroponic plant plant nutrition liquid recycles, and ensures long-effect plant healthy growth, need to establish a set of based on closed loop water body The technique and device of the efficient reuse of the plant nutrition liquid of flowing.
Summary of the invention
The object of the present invention is to provide the efficient recycling and processing equipment of a plant nutrient liquor and methods, to solve above-mentioned technology Problem.
The present invention provides the efficient recycling and processing equipments of a plant nutrient liquor, including circulating cultivation frame, standing reservoir Case, nutrient solution mother liquor supply unit, quartz sand-activated carbon adsorption retention unit and high-strength ultraviolet light mineralization unit;
Nutrient solution mother liquor supply unit is connect with standing reservoir case, for feeding plant growth into standing reservoir case Required a great number of elements and microelement;
The outlet of standing reservoir case is connect by the first infusion branch and the second infusion branch with circulating cultivation frame import, is followed The outlet of ring cultivating stand is connect with standing reservoir case import, to carry out the circulation of plant nutrition liquid;
First infusion branch curb nutrient input send direction to be successively arranged quartz sand-activated carbon adsorption retention unit and high-strength purple Outer smooth mineralization unit retains unit by quartz sand-activated carbon adsorption and high-strength ultraviolet light mineralization unit is combined to plant nutrient Crop residues decomposition suspended matter, root system secretion organic matter, harmful microorganism and variant viral in liquid are degraded and are removed;The Two infusion branches are to surmount pipe;
Quartz sand-activated carbon adsorption retention unit and the import for surmounting pipe are equipped with for switching the first infusion branch and second The solenoid valve of infusion branch;Nutrient solution mother liquor supply unit is equipped with the solenoid valve for controlling mother liquor output;
Phosphate, nitrate, organic matter on-line computing model are installed, phosphate, nitrate are online in standing reservoir case Monitor is connect with the solenoid valve of nutrient solution mother liquor supply unit, and organic matter on-line computing model and the first infusion branch and second are defeated The solenoid valve of liquid branch connects.
Further, quartz sand-activated carbon adsorption retention unit is along nutrient solution conveying direction by quartzy sand filter blanket, particle Quartz sand-activated carbon filter that active carbon filtering layer is constituted.
Further, quartzy sand filter blanket is made of the quartz sand that partial size is 0.8-1.2mm, height 15cm;Particle is living Property charcoal filtering layer by partial size be 16~32 mesh granular activated carbon constitute, height 60cm.
Further, nutrient solution mother liquor supply unit is additionally provided with the metering pump for measuring nutrient solution mother liquor output quantity.
Further, standing reservoir case is equipped with nutrient solution sample tap.
The present invention also provides the application efficient recycling and processing equipment Treatment for Reuse plant nutrition liquids of above-mentioned plant nutrition liquid Method, comprising:
When phosphate, nitrate on-line computing model monitor phosphate and nitrate concentration lower than setting value, pass through battalion It is micro- that nutrient solution mother liquor feeds nitrogen, phosphorus needed for unit feeds plant growth to standing reservoir case, potassium a great number of elements and boron, zinc, manganese Secondary element.
Further, this method further include:
When nutrient solution cycle period is more than 20 days or nutrient solution organic matter on-line monitoring concentration is more than 20mg/L, make to seek After nutrient solution comes out from standing reservoir case, it is introduced into quartz sand-activated carbon adsorption retention unit, enters high-strength ultraviolet light mineralising afterwards Unit, finally water outlet reenters circulating cultivation frame;
When nutrient solution cycle period is less than 20 days, and nutrient solution organic matter on-line monitoring concentration is less than 30mg/L, Make nutrient solution from standing reservoir case come out after, directly enter circulating cultivation frame by surmounting pipe.
According to the above aspect of the present invention, being fed by the efficient recycling and processing equipment of plant nutrition liquid and method using plant nutrition liquid System supplements the nutrient of plant nutrition liquid;Using plant nutrition liquid regenerative system, cut by quartz sand-activated carbon adsorption Unit, high-strength ultraviolet light mineralization unit are stayed, is combined organic to the crop residues decomposition suspended matter in plant nutrition liquid, root system secretion Object, harmful microorganism and variant viral are degraded and are removed, and crop is effectively avoided continuous cropping obstacle occur, ensure that plant efficient is raw It is long.
The above description is only an overview of the technical scheme of the present invention, in order to better understand the technical means of the present invention, And can be implemented in accordance with the contents of the specification, the following is a detailed description of the preferred embodiments of the present invention and the accompanying drawings.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of the efficient recycling and processing equipment of plant nutrition liquid of the present invention.
Figure label:
1- circulating cultivation frame;2- standing reservoir case;3- nutrient solution mother liquor feeds unit;4- quartz sand-activated carbon adsorption Retain unit;41- quartz sand filter blanket;42- granular activated carbon filtering layer;The high-strength ultraviolet light mineralization unit of 5-;6- surmounts pipe;7- electromagnetism Valve.
Specific embodiment
With reference to the accompanying drawings and examples, specific embodiments of the present invention will be described in further detail.Implement below Example is not intended to limit the scope of the invention for illustrating the present invention.
Join shown in Fig. 1, present embodiments provides the efficient recycling and processing equipment of a plant nutrient liquor, including circulating cultivation frame 1, standing reservoir case 2, nutrient solution mother liquor supply unit 3 (plant nutrition liquid make-up system), quartz sand-activated carbon adsorption retention Unit 4 and high-strength ultraviolet light mineralization unit 5 (plant nutrition liquid regenerative system);
Nutrient solution mother liquor supply unit 3 is connect with standing reservoir case 2, for feeding plant into standing reservoir case 2 A great number of elements and microelement needed for growth;
The outlet of standing reservoir case 2 is connect by the first infusion branch and the second infusion branch with 1 import of circulating cultivation frame, The outlet of circulating cultivation frame 1 is connect with 2 import of standing reservoir case, to carry out the circulation of plant nutrition liquid;
First infusion branch curb nutrient input send direction to be successively arranged quartz sand-activated carbon adsorption retention unit 4 and high-strength Ultraviolet light mineralization unit 5 retains unit 4 by quartz sand-activated carbon adsorption and high-strength ultraviolet light mineralization unit 5 is combined to plant Crop residues decomposition suspended matter, root system secretion organic matter, harmful microorganism and variant viral in nutrient solution are degraded and are gone It removes;Second infusion branch is to surmount pipe 6;
Quartz sand-activated carbon adsorption retention unit 4 and the import for surmounting pipe 6 are equipped with for switching the first infusion branch and the The solenoid valve 7 of two infusion branches;Nutrient solution mother liquor supply unit 3 is equipped with the solenoid valve (not shown) for controlling mother liquor output;
Phosphate, nitrate, organic matter (TOC) on-line computing model (not shown), phosphoric acid are installed in standing reservoir case 2 Salt, nitrate on-line computing model and nutrient solution mother liquor supply unit solenoid valve connect, organic matter on-line computing model and first defeated The solenoid valve 7 of liquid branch and the second infusion branch connects.
Plant nutrient is supplemented using plant nutrition liquid make-up system by the efficient recycling and processing equipment of the plant nutrition liquid The nutrient of liquid;Using plant nutrition liquid regenerative system, unit, high-strength ultraviolet light are retained by quartz sand-activated carbon adsorption Mineralization unit is combined to crop residues decomposition suspended matter, root system secretion organic matter, harmful microorganism and the change in plant nutrition liquid Different virus is degraded and is removed, and crop is effectively avoided continuous cropping obstacle occur, ensures plant efficient growth.
In the present embodiment, quartz sand-activated carbon adsorption retention unit 4 is along nutrient solution conveying direction by quartzy sand filter blanket 41, quartz sand-activated carbon filter (quartz sand-activated-charcoal column) that granular activated carbon filtering layer 42 is constituted.
In the present embodiment, quartzy sand filter blanket 41 is made of the quartz sand that partial size is 0.8-1.2mm, height 15cm; Granular activated carbon filtering layer 42 is made of the granular activated carbon that partial size is 16~32 mesh, height 60cm.
In the present embodiment, nutrient solution mother liquor supply unit 3 is additionally provided with the metering for measuring nutrient solution mother liquor output quantity Pump (not shown).
In the present embodiment, standing reservoir case 2 is equipped with nutrient solution sample tap (not shown).
The present embodiment is additionally provided using the efficient recycling and processing equipment Treatment for Reuse plant nutrition liquid of above-mentioned plant nutrition liquid Method, comprising:
Plant nutrition liquid initially enters plant nutrition liquid storage tank by circulating cultivation frame, when phosphate, nitrate are supervised online When survey instrument monitors phosphate and nitrate concentration lower than setting value, 3 solenoid valve of unit is fed by nutrient solution mother liquor and is beaten automatically It opens, a great number of elements and boron, zinc, manganese etc. such as nitrogen, phosphorus, potassium needed for feeding plant growth to standing reservoir case 2 by metering pump Microelement.
In the present embodiment, this method further include:
After nutrient solution comes out from standing reservoir case 2, it is divided into two infusion paths, path 1: when nutrient solution cycle period is super Spend 20 days or nutrient solution organic matter on-line monitoring concentration be when being more than 20mg/L, make nutrient solution from standing reservoir case 2 out after, It is introduced into quartz sand-activated carbon adsorption retention unit 4, enters high-strength ultraviolet light mineralization unit 5 afterwards, finally water outlet, which reenters, follows Ring cultivating stand 1.
Path 2: when nutrient solution cycle period is less than 20 days, and nutrient solution organic matter on-line monitoring concentration is less than When 30mg/L, make nutrient solution from standing reservoir case 2 come out after, directly by surmount pipe 6 enter circulating cultivation frame 1.
After nutrient solution comes out from standing reservoir case 2, according to 1 situation of path, initially enters quartz sand-activated carbon adsorption and cut Unit 4 is stayed, in this unit, the big partial size suspended matter that quartzy sand filter blanket 41 falls off retention removal because of plant root exudation, with Granular activated carbon is on the one hand by the partial organic substances (such as phenolic acid class, humic acids), micro heavy in Adsorption nutrient solution afterwards Metal ion and a small amount of pathogen;On the other hand the smaller suspended matter of partial size is removed into further retention.Quartz sand-activity carbon filtration 43 hydraulic detention time of pond is 15min.When the head loss of filtering layer reaches 30cm, carries out air-water and alternately backwash, gas punching 60s, air water rush 2min, and water rushes 60s, and whole process carries out 2 times.When TOC removal rate is reduced to 15% or less in unit water outlet, Replace granular activated carbon filtering layer 42.Unit 4 is retained by quartz sand-activated carbon adsorption, the removal rate of suspended matter reaches in nutrient solution To 90% or more, concentration of suspension is discharged in 5mg/L or less;TOC removal rate reaches 30% or more.
Nutrient solution is after quartz sand-activated carbon adsorption retention outflow of unit 4, into high-strength ultraviolet light mineralization unit 5, at this In unit, the advantage for making full use of high-strength UV energy density high increases the generating rate of hydroxyl radical free radical, improves reaction speed Rate, is difficult in efficient mineralization plant nutrition liquid to be tightly held by activated carbon or the organic matter of rhizosphere microbial degradation.High-strength ultraviolet light mine The photon flux for changing high-strength ultraviolet light employed in unit 5 is 3.13 × 10-6einstein·cm-2·s-1(intensity is roughly equal to 1000mW/cm2), it more than two orders of magnitude higher than ultraviolet ray intensity used in traditional advanced oxidation processes, utilizes high-intensitive purple The high feature of outer optical energy density reinforces the yield of hydroxyl radical free radical in advanced oxidation reaction, anti-to improve advanced oxidation with this The reaction rate and oxidability answered, thus effectively remove secretions from plant roots, crop residues decomposition object etc. be difficult to it is active The organic matter of charcoal absorption and microbial degradation synchronizes effectively control harmful microorganism and breeds, finally effectively avoids continuous cropping obstacle.This 1~2min of hydraulic detention time of unit.By high-strength ultraviolet light mineralization unit 5, in nutrient solution TOC removal rate reach 95% with On, TOC concentration reaches 5mg/L or less;Turbidity reaches 5NTU hereinafter, concentration of suspension reaches 10mg/L or less.
The present invention has the following technical effect that
(1) high efficiency.High-strength ultraviolet light photons flux used by high-strength ultraviolet light mineralization unit of the invention is 3.13 ×10-6einstein·cm-2·s-1(intensity is roughly equal to 1000mW/cm2), than ultraviolet light used in traditional advanced oxidation processes More than high two orders of magnitude of intensity, the yield of hydroxyl radical free radical improves hundreds of times in reaction, can make the thorough mineralising of organic matter, no longer Other intermediate products are generated, the continuous cropping obstacle for effectively avoiding organic matter or in which product from causing, and make the mineralization of organic material time Shorten tens times.Compared with Conventional UV light technology, the TOC of initial concentration 25mg/L is made to reach 95% removal rate by 15min It shorten to 1min.
(2) stability.Quartz sand of the present invention-activated carbon adsorption retention and high-strength ultraviolet mineralising combination technique are main Small by environmental influence based on physical and chemical reaction, antigen water variation water quality impact load ability is strong, can effective guarantee Stability of the circulation technology in closed system.
(3) compactedness.The present invention mainly uses quartz sand-activated carbon adsorption retention unit+high-strength ultraviolet light mineralization unit, Quartz sand-activated carbon process that leading portion uses, because of granular activated carbon specific surface area with higher, adsorption capacity is strong, and general Haydite filter tank compare, filter tank volume can reduce one third;The high-strength ultraviolet lamp technique that back segment uses, because of its ultrahigh in efficiency, Hydraulic detention time only needs 1min, reaction monomers only 15L.For these reasons, the present invention is easily integrated compact integrated set Standby, suitable for space resources anxiety manned space flight closed system.
(4) long-term effect.The present invention is excited mainly by electric current using ultraviolet lamp and generates high-throughput electronics, with conventional nanofiltration, The membrane filtration process such as reverse osmosis, resin ion exchange process are different, and high-strength ultraviolet light mineralization unit mainly passes through big rain It is carbon dioxide and water by the thorough mineralising of organic matter, ultraviolet lamp is hardly damaged under normal circumstances, has without physically or chemically regenerating There is long-term effect.
Below by specific example, invention is further described in detail.
According to the continuous 240 days practical operation situations of the vertical cultivated system of closed system, plant nutrition liquid accumulation is not handled The water quality situation of 20d is that TOC concentration is 25~30mg/L, and ammonia nitrogen concentration is 1~5mg/L, and turbidity is 4~10NTU, and suspended matter is dense Degree is 30~50mg/L.During the test of continuous operation, after plant nutrition liquid circulation, standing reservoir case is initially entered, is led to Nitrate and the automatic monitoring nutrient solution water quality condition of phosphate on-line monitoring probe in overnutrition liquid storage bin, when in nutrient solution When a great number of elements needed for the plant growths such as nitrogen, phosphorus, potassium starts deficiency, plant nutrition liquid make-up system automatically turns on supply mould Formula starts to supplement plant nutrient by peristaltic pump (metering pump).Plant nutrition liquid is after storage tank outflow, outlet pipe section dress There are online TOC and ammonia nitrogen on-line monitoring probe, when TOC concentration is more than 20mg/L or the nutrient solution accumulation cycle time is more than 20d When, then pipe electromagnetic valve automatically turns on, and nutrient solution enters plant nutrition liquid regenerative system;When TOC concentration be no more than 25mg/L, or When the nutrient solution accumulation cycle time is no more than 20d, plant nutrition liquid is directly back to plant circulating cultivation frame by passing through pipe.
After plant nutrition liquid enters plant nutrition liquid regenerative system, quartz sand-activated-charcoal column is first passed around, in reactor Interior hydraulic detention time is 15min, and mainly oil removal, absorbed portion organic matter, micro heavy are removed in retention in this unit Ion and highly charged ions.Then, nutrient solution enters high-strength ultraviolet light mineralization unit, and the hydraulic detention time in reactor is 1min, by the high advantage of the energy density of high-strength ultraviolet light, by organic matters such as secretions from plant roots, crop residues decomposition objects It is converted into carbon dioxide and water within the very short time, synchronizes effectively control harmful microorganism quantity, finally the effective company of avoiding Make obstacle.After being handled by plant nutrition liquid regenerative system, effluent quality reaches TOC concentration < 5mg/L, ammonia nitrogen concentration < 1mg/ L, turbidity < 1NTU, concentration of suspension < 10mg/L.Ensure that nutrient solution at least can continuously recycle 360d or more.
The above is only a preferred embodiment of the present invention, it is not intended to restrict the invention, it is noted that for this skill For the those of ordinary skill in art field, without departing from the technical principles of the invention, can also make it is several improvement and Modification, these improvements and modifications also should be regarded as protection scope of the present invention.

Claims (7)

1. the efficient recycling and processing equipment of a plant nutrient liquor, which is characterized in that including circulating cultivation frame, standing reservoir case, Nutrient solution mother liquor feeds unit, quartz sand-activated carbon adsorption retention unit and high-strength ultraviolet light mineralization unit;
The nutrient solution mother liquor supply unit is connect with the standing reservoir case, for feeding into the standing reservoir case A great number of elements needed for plant growth and microelement;
The standing reservoir case outlet is connected by the first infusion branch and the second infusion branch and the circulating cultivation frame import It connects, the circulating cultivation frame outlet is connect with the standing reservoir case import, to carry out the circulation of plant nutrition liquid;
The first infusion branch curb nutrient input send direction to be successively arranged the quartz sand-activated carbon adsorption retention unit and height Strong ultraviolet light mineralization unit retains unit and high-strength ultraviolet light mineralization unit joint pair by the quartz sand-activated carbon adsorption Crop residues decomposition suspended matter, root system secretion organic matter, harmful microorganism and variant viral in plant nutrition liquid are degraded And removal;The second infusion branch is to surmount pipe;
The quartz sand-activated carbon adsorption retention unit and the import for surmounting pipe be equipped with for switch the first infusion branch and The solenoid valve of second infusion branch;The nutrient solution mother liquor supply unit is equipped with the solenoid valve for controlling mother liquor output;
Phosphate, nitrate, organic matter on-line computing model, the phosphate, nitrate are installed in the standing reservoir case On-line computing model is connect with the solenoid valve of nutrient solution mother liquor supply unit, the organic matter on-line computing model and described first The solenoid valve connection of infusion branch and the second infusion branch.
2. the efficient recycling and processing equipment of plant nutrition liquid according to claim 1, which is characterized in that the quartz sand-work Property charcoal absorption retention unit be the quartz sand-work being made of along nutrient solution conveying direction quartzy sand filter blanket, granular activated carbon filtering layer Property carbon filtering pool.
3. the efficient recycling and processing equipment of plant nutrition liquid according to claim 2, which is characterized in that the quartz sand filter blanket It is made of the quartz sand that partial size is 0.8-1.2mm, height 15cm;The granular activated carbon filtering layer is 16~32 mesh by partial size Granular activated carbon constitute, height 60cm.
4. the efficient recycling and processing equipment of plant nutrition liquid according to claim 1, which is characterized in that the nutrient solution mother liquor Supply unit is additionally provided with the metering pump for measuring nutrient solution mother liquor output quantity.
5. the efficient recycling and processing equipment of plant nutrition liquid according to claim 1, which is characterized in that the standing reservoir Case is equipped with nutrient solution sample tap.
6. a kind of application efficient recycling and processing equipment Treatment for Reuse plant of plant nutrition liquid described in any one of claim 1 to 5 The method of nutrient solution characterized by comprising
When the phosphate, nitrate on-line computing model monitor phosphate and nitrate concentration lower than setting value, pass through institute State nutrient solution mother liquor feed unit to standing reservoir case feed plant growth needed for nitrogen, phosphorus, potassium a great number of elements and boron, zinc, Manganese microelement.
7. the method for Treatment for Reuse plant nutrition liquid according to claim 6, which is characterized in that further include:
When nutrient solution cycle period is more than 20 days or nutrient solution organic matter on-line monitoring concentration is more than 20mg/L, make nutrient solution After coming out from standing reservoir case, it is introduced into the quartz sand-activated carbon adsorption retention unit, enters the high-strength ultraviolet light afterwards Mineralization unit, finally water outlet reenters the circulating cultivation frame;
When nutrient solution cycle period is less than 20 days, and nutrient solution organic matter on-line monitoring concentration is less than 30mg/L, make to seek After nutrient solution comes out from standing reservoir case, directly by the pipe that surmounts into the circulating cultivation frame.
CN201910148245.1A 2019-02-27 2019-02-27 The efficient recycling and processing equipment of one plant nutrient liquor and method Pending CN109892221A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201910148245.1A CN109892221A (en) 2019-02-27 2019-02-27 The efficient recycling and processing equipment of one plant nutrient liquor and method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201910148245.1A CN109892221A (en) 2019-02-27 2019-02-27 The efficient recycling and processing equipment of one plant nutrient liquor and method

Publications (1)

Publication Number Publication Date
CN109892221A true CN109892221A (en) 2019-06-18

Family

ID=66945761

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201910148245.1A Pending CN109892221A (en) 2019-02-27 2019-02-27 The efficient recycling and processing equipment of one plant nutrient liquor and method

Country Status (1)

Country Link
CN (1) CN109892221A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN115024212A (en) * 2022-07-07 2022-09-09 东北农业大学 Nutrient solution cascade recycling circulation system applying soilless culture and control method thereof

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN201830730U (en) * 2010-08-31 2011-05-18 中国科学院植物研究所 Vegetable culture device capable of utilizing natural light source and being assembled detachably
CN202285744U (en) * 2011-09-06 2012-07-04 中国农业科学院农业环境与可持续发展研究所 Solid-carried nano TiO2 photocatalysis device
CN104719113A (en) * 2015-03-23 2015-06-24 上海交通大学 Lettuce cultivation system for promoting accumulation of antioxidant substances and cultivation method thereof
CN105638507A (en) * 2016-01-11 2016-06-08 北京航空航天大学 System achieving automatic control and circulating utilization of plant nutrient solution

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN201830730U (en) * 2010-08-31 2011-05-18 中国科学院植物研究所 Vegetable culture device capable of utilizing natural light source and being assembled detachably
CN202285744U (en) * 2011-09-06 2012-07-04 中国农业科学院农业环境与可持续发展研究所 Solid-carried nano TiO2 photocatalysis device
CN104719113A (en) * 2015-03-23 2015-06-24 上海交通大学 Lettuce cultivation system for promoting accumulation of antioxidant substances and cultivation method thereof
CN105638507A (en) * 2016-01-11 2016-06-08 北京航空航天大学 System achieving automatic control and circulating utilization of plant nutrient solution

Non-Patent Citations (8)

* Cited by examiner, † Cited by third party
Title
刘向辉等: "紫外线杀灭营养液中黄瓜枯萎病病菌试验研究", 《中国农学通报》 *
宋卫堂等: "紫外线-臭氧组合式营养液消毒机的设计及灭菌性能试验", 《农业工程学报》 *
庞丹丹: "高强光光催化的性能研究及应用", 《中国优秀硕士学位论文全文数据库 工程科技I辑》 *
李东星等: "植物工厂营养液循环再利用装备的研究应用", 《农业工程》 *
李秀婷: "《现代啤酒生产工艺》", 30 June 2013, 中国农业大学出版社 *
王学刚等: "《水处理工程实验》", 31 October 2016, 冶金工业出版社 *
苗秀杰: "《成长路上 北京市中小学生金鹏科技论坛活动》", 31 March 2016, 武汉大学出版社 *
陈亚萍等: "《城市水处理工程技术》", 31 August 2008, 黄河水利出版社 *

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN115024212A (en) * 2022-07-07 2022-09-09 东北农业大学 Nutrient solution cascade recycling circulation system applying soilless culture and control method thereof

Similar Documents

Publication Publication Date Title
CN104430134B (en) A kind of energy-efficient industrial circulating water high-density cultivation system saved land
KR101197244B1 (en) A Device for Treating Wastewater Comprising Nitrogen and Phosphorus and A Method for the Same
US11865498B2 (en) Membrane system to treat leachate and methods of treating leachate
US6635177B2 (en) Reclaiming water and usable brine concentrate from domestic sewage
EP2417243B1 (en) Photobioreactor and method for cultivating biomass by means of photosynthesis
CN105145455B (en) Industrial circulating water is breeded fish water treatment system
KR101611275B1 (en) The bioengineering method and apparatus to remove tritium in water
CN105010206B (en) Closed type industrial circulating water fish-cultivating method
CN108271730A (en) A kind of low-carbon zero-emission industrial circulating water cultivating system based on anaerobic denitrifying
CN107405573A (en) System and method for handling dilution waste water
CN108640274A (en) A kind of waste water circulation utilized device of integrated plant culture
CN105165678B (en) A kind of method of sturgeon breeding
CN109892221A (en) The efficient recycling and processing equipment of one plant nutrient liquor and method
CN201990579U (en) Bilayer biology-sand filter
CN107998746A (en) A kind of aquaculture original position filter method and device
CN105060648A (en) Industrial circulating water fish-culture denitrification zero-emission system
US11192810B2 (en) Waste treatment systems and methods
CN111333444A (en) Efficient treatment method for anaerobic fermentation substrate of fruit and vegetable waste
CN103613214A (en) Movable type biogas slurry concentrating integrated equipment
CN110316886A (en) A kind of garbage percolation liquid treating system and method
US20220055927A1 (en) Desalination of water using a complexing agent attached to a magnetic nanoparticle
CN204305874U (en) A kind of energy-efficient industrial circulating water high-density cultivation system saved land
CN209815887U (en) Biogas slurry high-power concentration system
CN208667344U (en) A kind of organophosphorus pesticide pollution soil heterotopic repair system
CN105000761A (en) Method for removing nitrogen elements in high-density fish culture circulating water

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
RJ01 Rejection of invention patent application after publication

Application publication date: 20190618

RJ01 Rejection of invention patent application after publication