CN106431581A - Organic liquid fertilizer based on concentrated biogas slurry as well as preparation and application methods thereof - Google Patents
Organic liquid fertilizer based on concentrated biogas slurry as well as preparation and application methods thereof Download PDFInfo
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- CN106431581A CN106431581A CN201610794632.9A CN201610794632A CN106431581A CN 106431581 A CN106431581 A CN 106431581A CN 201610794632 A CN201610794632 A CN 201610794632A CN 106431581 A CN106431581 A CN 106431581A
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- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05G—MIXTURES OF FERTILISERS COVERED INDIVIDUALLY BY DIFFERENT SUBCLASSES OF CLASS C05; MIXTURES OF ONE OR MORE FERTILISERS WITH MATERIALS NOT HAVING A SPECIFIC FERTILISING ACTIVITY, e.g. PESTICIDES, SOIL-CONDITIONERS, WETTING AGENTS; FERTILISERS CHARACTERISED BY THEIR FORM
- C05G5/00—Fertilisers characterised by their form
- C05G5/20—Liquid fertilisers
- C05G5/23—Solutions
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- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05B—PHOSPHATIC FERTILISERS
- C05B7/00—Fertilisers based essentially on alkali or ammonium orthophosphates
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Abstract
The invention belongs to the field of organic waste resource recovery and fertilizer production and in particular relates to an organic liquid fertilizer based on concentrated biogas slurry as well as preparation and application methods thereof. The preparation method comprises the following steps: (1) preparing an organic basic liquid fertilizer liquid: carrying out dispersive mixing on concentrated biogas slurry and phosphate fertilizers, thus obtaining the organic basic liquid fertilizer liquid; (2) preparing an organic basic nitrogen fertilizer liquid: carrying out dispersive mixing on concentrated biogas slurry and nitrogen fertilizers, thus obtaining the organic basic nitrogen fertilizer liquid; (3) preparing an organic basic chelate/complex trace element fertilizer liquid: carrying out dispersive mixing on concentrated biogas slurry and trace element fertilizers, thus obtaining the organic basic chelate/complex trace element fertilizer liquid; (4) preparing an organic liquid fertilizer primary liquid: carrying out dispersive mixing on the three kinds of liquids and an organic polymer dispersing emulsifier, thus obtaining the organic liquid fertilizer primary liquid; (5) preparing the organic liquid fertilizer based on concentrated biogas slurry: carrying out filtration and centrifugal separation on the organic liquid fertilizer primary liquid, thus obtaining the organic liquid fertilizer. The preparation method has the effect of achieving resource utilization of anaerobic digestion liquids of large-scale biogas projects. The prepared organic liquid fertilizer is applied as a special fertilizer for drop irrigation, soaking of seeds, seed dressing, root irrigation or foliage spray.
Description
Technical field
The invention belongs to organic waste resource recycling and field of fertilizer production are and in particular to a kind of being based on concentrates natural pond
The organic fertilizer of liquid and its methods for making and using same.
Background technology
Anaerobic fermentation residues are biogas slurry, the two-part mixture of biogas residue, i.e. anaerobic digestion solution.Mainly by partly undecomposed
Organic substance, microbial metabolic products and newborn microbial cells composition, its comprehensive utilization not only can avoid secondary pollution, also may be used
Bring good economy, ecological environment and social benefit.The annual anaerobic fermentation residues of China (biogas residue, biogas slurry) about 3.85 hundred million t,
How to guarantee that the sustainable development of biological fuel gas engineering and the biogas engineering built can normally run, solve anaerobic digestion solution
Process extremely urgent with Utilizing question.At present, aspect is utilized mainly to apply (also field) pattern using direct in anaerobic digestion solution.
Because the moisture of anaerobic digestion solution is high, it is not easy to storage, transports, anaerobic digestion solution natural pond extensive use of chemical fertilizer (Fertilizer Transformed) difficult to realize,
Not only become restriction large industrialized biogas engineering economic benefit, the bottleneck of sustainable commercialized running, also become its money of restriction
The technical bottleneck that sourceization recycles.
For speeding up to agricultural modernization, China widelys popularize implantation in large scale and water-fertilizer integral, and puts into a large amount of moneys
Gold guiding agricultural implements irrigation and water conservancy, and especially north drought area irrigating facility development is very fast, and such as spray, drip irrigation set
Apply, objectively require supporting with it, inexpensive liquid fertilizer.The liquid fertilizer passing through at present is mainly solid-state Water soluble fertilizer
Material, raw materials for production a great number of elements potassium main source is potassium dihydrogen phosphate and potassium nitrate, and other raw materials are carbamide, MAP, nitre
Sour ammonium, chelated microelements, various raw materials carry out blending, stirring can achieve.Water soluble fertilizer is that one kind is completely molten
In water polyelement composite fertilizer it is desirable to can promptly be dissolved in the water, be beneficial to crop and absorb rapidly, and it absorbs
Rate is of a relatively high, is more crucially matched in the facilities such as modern spray drop filling, it is possible to achieve water-fertilizer integral.Certainly, water solublity
The administration of fertilizer is easy, can carry out fertigation with irrigation water (including the modes such as sprinkling irrigation, drip irrigation), reach water-saving and save fertile province
The efficiency of work.Water soluble fertilizer can be containing the whole nutrients required for plant growth, can be according to process of crop growth
Nutritional need feature carry out the formula of science so that its utilization rate of fertilizer is 2-3 times of conventional composite chemical fertilizer, reduce fertile
The waste of material.Secondly, water soluble fertilizer is a quick-acting fertilizer, and grower can be allowed to see effect and the table of fertilizer quickly
Existing, can according to crop difference growing way, fertilizer formula be made adjustment at any time.However, the restriction of water soluble fertilizer at this stage because
Element is mainly raw materials for production and production method, and such as potash fertilizer raw material sources, in potassium dihydrogen phosphate and potassium nitrate, due to expensive, are made
Solid-state Water soluble fertilizer is become to hold at high price.Import solid-state Water soluble fertilizer price typically at 30,000 yuan per ton about, domestic also per ton
20000 yuan about.Water soluble fertilizer is expensive, on the higher industrial crops of economic worth more using or be used for foliage fertilizer, and general
There is dissolubility, contain the mechanical admixtures such as water-insoluble it is impossible to adapt to irrigating facility liquid manure one completely in logical agricultural basis chemical fertilizer
The needs changed.In addition, the problems such as chronic administration Water soluble fertilizer often results in local secondary salinization.
At present, there is a problem of that moisture content is high, it is big to be dehydrated difficulty in the extensive use of chemical fertilizer of anaerobic digestion solution natural pond using aspect, in application side
Face is still more extensive, also lacks necessary theory support.And anaerobic digestion solution natural pond extensive use of chemical fertilizer poor product quality, single varieties, profit
Low with rate, added value is not high, and industrialization process is slow.Anaerobic digestion solution is rich in bioactive substance (organic substance) and crop must
The full price nutrient element of palpus, has the slow fertilizer efficiency feature having both of speed.Wherein, humus material is conducive to the work of soil microorganism
The dynamic formation with soil aggregate, improves potential ability and the stability of fertilizer provision from soil;The nutrients such as nitrogen, phosphorus, potassium, calcium, magnesium unit
Element meets plant growth needs;Undegraded Organic substance provides N source and C source for soil microorganism, improves the biological of topsoil soils and lives
Property.Produce high efficiency organic-inorganic compound (conjunction) fertilizer, substrate, concentrate organic fertilizer etc. using biogas residue, biogas slurry, improve biogas residue, natural pond
Liquid scale process complete set technology system, not only can effectively solving Biogas Residues secondary pollution problem, realize resource
Change and utilize, promote traditional agriculture to produce and realize industrialization, commercialization and modernization, preserve the ecological environment, and agriculture can be promoted
Product safety production development, improves the international competitiveness of agricultural product.
Therefore, the organic liquid fertilizer with anaerobic fermentation residues as primary raw material for the exploitation, solves Water soluble fertilizer expensive
With the problems such as the secondary salinization of local to adapt to the needs of water-fertilizer integral, be to realize having of anaerobic fermentation residues high-value-use
Effect approach.Meanwhile, the composition of research anaerobic fermentation residues (biogas residue/biogas slurry), value, purposes and Land use systems, form biogas
The complete set technology system that engineering anaerobic digestion liquid scale is processed, determines the encouragement policy and Extension Model being suitable for China's national situation,
Promote circular agriculture construction, to realize biogas industry sustainable development significant.
Content of the invention
In order to solve above-mentioned technical problem, the invention provides a kind of preparation side based on the organic fertilizer concentrating biogas slurry
Method.Raw material includes concentrating biogas slurry, agricultural inorganic chemical fertilizer, organic polymer dispersion emulsifier.Technological equipment is by allocating reaction
The accessory such as kettle, hybrid reactor and matching pump, valve forms.Described preparation method comprises the following steps:
(1) prepare organic basis liquid fertilizer solution:Concentration biogas slurry is taken to mix with phosphate fertilizer, dispersion mixing under the conditions of 50~60 DEG C
15~30min, obtains final product described organic basis liquid fertilizer solution;
(2) prepare organic basis nitrogenous fertilizer solution:Concentration biogas slurry is taken to mix with nitrogenous fertilizer, dispersion mixing under the conditions of 50~60 DEG C
15~30min, obtains final product described organic basis nitrogenous fertilizer solution;
(3) prepare organic basis chela/complex state trace element fertilizer solution:Concentration biogas slurry is taken to mix with trace element fertilizer,
Dispersion mixing 60~120min under the conditions of 50~60 DEG C, obtains final product described organic basis chela/complex state trace element fertilizer solution;
(4) preparation is based on the organic fertilizer primary solution concentrating biogas slurry:By described organic basis liquid fertilizer solution, organic basis
Nitrogenous fertilizer solution, organic basis chela/complex state trace element fertilizer solution, potash fertilizer, moderate-element fertilizer and organic polymer dispersion and emulsion
Agent mixes, dispersion mixing 30~60min under the conditions of 50~60 DEG C, obtains final product described molten based on the organic fertilizer primary concentrating biogas slurry
Liquid;
(5) preparation is based on the organic fertilizer concentrating biogas slurry:Entered described based on the organic fertilizer primary solution concentrating biogas slurry
Row filter centrifugation separates, and sieve separates slag and is used for the solid fertilizer of organic and inorganic or soil conditioner raw material, the lower separating liquid of sieve is described
Based on the organic fertilizer concentrating biogas slurry.
Temperature conditionss in above-mentioned preparation method and dispersion mixing time are all that inventor is paying the base of creative work
On plinth, the optimized choice that carried out, it not only makes various materials fully be merged, and preferably plays the facilitation of complementation,
And so that the entirely stability of described organic fertilizer and fertilizer efficiency is all improved largely.The organic fertilizer that the method is produced has
High nutrition, speed slow in succession with disease-resistant antibacterial effect, section is fertile, water saving and ecological, environmental protective, improves the sustainable production energy of soil
Power, the yield and quality of crops, simple production process, practicality, beneficial to promote, achievable biogas industry anaerobic digestion solution fertilizer
Change, commercialization and high quality, solve the problems, such as that a large amount of anaerobic digestion solutions process the technical bottleneck with recycling.
Of the present invention concentration the application for a patent for invention by publication number CN105776611A, CN105884410A for the biogas slurry public affairs
The organic fertilizer base fluid opened, is biogas engineering anaerobic fermentation by-product anaerobic digestion solution through staged care, reversely concentration, high shear
The biogas slurry of dispersion and emulsion acquisition, biogas residue mixture.The preparation method of this organic fertilizer base fluid comprises the following steps:
1) the not digested decomposing organic matter of bulky grain, silt etc. are removed:Remove anaerobic digestion solution using hierarchical processing method
In the not digested decomposing organic matter of bulky grain, silt etc., obtain and eliminate the not digested decomposing organic matter of bulky grain, silt etc.
Thick biogas residue and biogas slurry;
2) reversely concentrate:By step 1) the thick biogas residue that obtains and biogas slurry airtight, equipped with heating and dispersing mixer
Container in contact dispersion mixing 15-30min, obtain solid content be 10-30 mass % reverse concentrated solution;
3) activate bioactive substance:By step 2) the reverse concentrated solution that obtains enters high cut disperse emulsification device, carries out
High frequency high cut disperse emulsification processes 60~120min, obtains high physiologically active anaerobic digestion and concentrates biogas slurry;
4) filtration separation:Using 170 mesh or 200 mesh filtering centrifuge to step 3) the high physiologically active anaerobism that obtains disappears
Change concentration biogas slurry and carry out filter centrifugation separation, the siftage of acquisition is high physiologically active organic fertilizer base fluid, that is, of the present invention
Concentrate biogas slurry.
The invention provides a kind of prepare the synthesizer that described organic fertilizer is adopted, this device is also present invention preparation
The technological process of organic fertilizer, 1~in this synthesizer No. 3 allotment reactor except volume difference in addition to, remaining relevant configuration
(including dog-house, dispersing mixer, material inlet valve, discharge valve, underflow pump, control chamber, scale liquidometer etc.) all same;This
Outward, the relevant configuration of hybrid reactor is also essentially identical with 1~No. 3 allotment reactor, and only volume is different with effect;And,
The control chamber all same of each reactor above, is used to control underflow pump, electric heater and the dispersion of the configuration of each reactor
The unlatching of blender, and the setting of time and temperature;In addition, 1~No. 3 allotment reactor is all by pipeline, respective discharging
The material inlet valve of valve, underflow pump and hybrid reactor is attached;Hybrid reactor passes through pipeline, discharge valve, underflow pump
It is attached with filtering centrifuge.
Based on above-mentioned synthesizer, described step (1)~(5) employ following preferred version:
Specifically described step (1) is:Using No. 1 allotment reactor, open material inlet valve, start underflow pump, add institute
State concentration biogas slurry 100wt% that solid content is 5-30wt%, close material inlet valve and underflow pump;Start dispersing mixer, open
Dog-house, throws in phosphate fertilizer powder material, and injected volume is the described 60-85wt% concentrating biogas slurry, closes dog-house, persistently disperses mixed
Close;Start heater heat temperature raising, treat that material is warming up to 50-60 DEG C, and maintain this temperature dispersion mixing 15-30min, stop adding
Heat and dispersion mixing, obtain grade [(4.1~5.1)-(16.5~20.2) -0] or [(5.6~6.9)-(15.8~19.3) -0]
Organic basis liquid fertilizer solution;Preferably, described phosphate fertilizer raw material is MAP (11-44-0) or Diammonium phosphate (DAP) (15-42-0)
One or two.
Grade of the present invention refers to the nutrient content of compound (conjunction) fertilizer or organic fertilizer, requires to join in national standard
Box-like expression.For example, MAP grade (11-44-0) is to be represented with formula, and wherein N content is 11%, P2O5Content is
44%th, K2O content is 0%, and organic basis liquid fertilizer grade [(4.1~5.1)-(16.5~20.2) -0] is to be represented with formula,
Wherein N content is 4.1~5.1%, P2O5Content is 16.5~20.2%, K2O content is 0.
Specifically described step (2) is:Using No. 2 allotment reactors, open material inlet valve, start underflow pump, add institute
State concentration biogas slurry 100wt% that solid content is 5-30wt%, close material inlet valve and underflow pump;Start dispersing mixer, open
Dog-house, throws in nitrogenous fertilizer powder material, and injected volume is the described 60-85wt% concentrating biogas slurry, closes dog-house, persistently disperses mixed
Close;Start heater heat temperature raising, treat that material is warming up to 50-60 DEG C, and maintain this temperature dispersion mixing 15-30min, stop adding
Heat and dispersion mixing, obtain organic basis nitrogenous fertilizer that grade is [(17.3~21.1) -0-0] or [(12.8~15.6) -0-0] molten
Liquid;Preferably, described nitrogenous fertilizer is carbamide (46-0-0) or ammonium nitrate (34-0-0).
Specifically described step (3) is:Using No. 3 allotment reactors, open material inlet valve, start underflow pump, add institute
State concentration biogas slurry 100wt% that solid content is 5-30wt%, close material inlet valve and underflow pump;Start dispersing mixer, open
Dog-house, throws in trace element fertilizer powder material, and injected volume is the described 5-10wt% concentrating biogas slurry, closes dog-house, continues
Dispersion mixing;Start heater heat temperature raising, treat that material is warming up to 50-60 DEG C, and maintain this temperature dispersion mixing 60-
120min, stops heating and dispersion mixing, obtains organic basis chela/complex state that grade is [0-0-0+ (3.4~5.5) TE] micro-
Secondary element liquid fertilizer solution;Preferably, described trace element fertilizer is manganese sulfate [0-0-0-30 (Mn)], zinc sulfate [0-0-0-21
(Zn)], Borax [0-0-0-11 (B)], ammonium molybdate [0-0-0-54 (Mo)], copper sulfate [0-0-0-24 (Cu)], ferrous sulfate [0-
One or more of 0-0-18 (Fe)].
Specifically described step (4) is:Open 1,2, No. 3 allotment reactor discharge valves and hybrid reactor charging respectively
Valve, starts respective underflow pump, respectively by described organic basis liquid fertilizer solution, organic basis nitrogenous fertilizer solution, organic basis chelating
State/complex state trace element fertilizer solution presses 1:1:1 ratio is measured respectively, is pumped into hybrid reactor, obtains grade and is
The mixed liquor of [(5.6~9.3)-(5.3~6.7) -0+ (1.1~1.8) TE];1,2, No. 3 allotment reactor discharge valves of closing,
Hybrid reactor material inlet valve and underflow pump;Start the dispersing mixer of hybrid reactor, open dog-house, throw in potash fertilizer first
Powder material, its injected volume is the 10-50% of described mixed liquor, secondly throws in moderate-element fertilizer powder material, and its injected volume is
The 0-30% of described mixed liquor, finally throws in organic polymer dispersion emulsifier powder material, and its injected volume is described mixed liquor
1-3%, close dog-house, continue dispersion mixing;Start the heater heat temperature raising of hybrid reactor, treat that material is warming up to
50-60 DEG C, and maintain this temperature dispersion mixing 30-60min, stop heating and dispersion mixing, obtain grade be [(5.1~
10.2)-(4.8~5.2)-(4.2~13.8)-(0~3.4) Ca- (0~1.3) Mg+ (1.0~1.8) TE] based on concentrate natural pond
The organic fertilizer primary solution of liquid;Preferably, described potash fertilizer be potassium sulfate (0-0-50), potassium chloride [0-0-60)] or potassium nitrate
One or more of (13-0-46);And/or, described moderate-element fertilizer is calcium nitrate [12-0-0-17 (Ca)] or magnesium sulfate
One of [0-0-0-10 (Mg)] or two kinds;And/or, described machine macromolecule dispersion emulsifier is xanthan gum or hydroxyl fiber
Element it is preferred that described hydroxylated cellulose be hydroxypropyl methyl cellulose or hydroxyethylmethyl-cellulose or hydroxyethyl cellulose or
One or more of hydroxymethyl cellulose.
Specifically described step (5) is:Open described hybrid reactor discharge valve, start underflow pump, be based on described
The organic fertilizer primary solution concentrating biogas slurry is pumped in 170 or 200 mesh filtering centrifuges carrying out filtration separation, described filtration
Slag is separated on the sieve of centrifuge and is used for that organic and inorganic is solid fertile or soil conditioner raw material, the lower separating liquid of sieve be described based on dense
The organic fertilizer of contracting biogas slurry, wherein insoluble matter grain diameter≤0.089mm or 0.0740mm is it can be ensured that meet spray, drip irrigation equipment
Requirement.
1~No. 3 allotment reactor in the method for the invention and hybrid reactor are each equipped with heater and disperse mixed
Clutch, difference is only different with physical and chemical process in volume, and the operation of repeat step (1) to (5) can achieve based on concentration
The continuous prodution of the organic fertilizer of biogas slurry.
The method of the invention, described dispersing mixer is batch (-type) prompt stream dispersing mixer, and the prompt stream of described batch (-type)
The rotor speed of dispersing mixer is 2900rpm;And, heater of the present invention is electric heater.Described batch (-type) is prompt
Flow dispersing mixer under the rotor of high-speed rotation drives, by the water-insoluble in mixing liquid material in kettle in rotor guide chamber
In the presence of produce one strong liquid vertical circulation, force water-insoluble in mixing liquid material and liquid vertical circulation
In kettle, overall circulation, reaches mixing macroscopically;Meanwhile, the rotor of high-speed rotation produces microcosmic mixing shearing to be reached
Turbulent flow, the liquid processing through microcosmic turbulent mixture is dispersed to each corner in space in kettle with the circulation of overall liquor stream,
The water-insoluble in described mixing liquid material is forced to be thoroughly dispersed mixing, this dispersion mixing mode has and is substantially better than it
The dispersion mixing that its hybrid mode is brought.
The method of the invention, concentrate in described step (1)~(3) biogas slurry all preferably solid content be 10%~20% dense
Contracting biogas slurry.
Based on above-mentioned preparation method, the invention provides the organic fertilizer that a kind of said method is obtained, its grade is [(5.1
~10.2)-(4.8~5.2)-(4.2~13.8)-(0~3.4) Ca- (0~1.3) Mg+ (1.0~1.8) TE].
Finally, present invention also offers application in solanaceous vegetables/cultivation of fruit tree for the above-mentioned organic fertilizer, that is,:By institute
State 300~500 times of organic fertilizer dilute and be used for drip irrigation special fertilizer;Or, by described organic fertilizer dilute 800~1000
Times, for soaking seed, dressing seed, pouring root or foliage-spray special fertilizer.
The technique scheme of the present invention has the advantages that:
(1) a kind of organic fertilizer based on concentration biogas slurry of the present invention, removes in its component and sends out containing higher plant growth
Educate outside required N P and K a great number of elements, calcium and magnesium sulfur moderate-element and various trace elements, also contain high biological active substanceies, be
High concentration, stable suspension fertilizers.Due to concentrating the coordinative role of the organic acid such as the aminoacid in biogas slurry, humic acid, make
Organically combine between various inorganic nutrients nutrients, mutually promote, action compensating, effectively increase the utilization rate of chemical fertilizer.Apply
With this organic fertilizer can improved soil environment, increase soil breathability, adjust soil acidity or alkalinity, formed loose sum stable
Soil aggregate structure;Increase water holding, the fertilizer-preserving ability of soil, prevent erosion, provide for crop root loose, swelling
Growing environment;Strengthen crop root vigor, improve the chlorophyll content of plant, promote photosynthesis, promote crop, flower bud, really
The growth of (bell), minimizing comes off, and improves and the interior quality improving fruit (seed) and exterior quality, improves the unit plane of crop
Long-pending yield, has improved soil concurrently and stimulates crop growth dual function.Apply this organic fertilizer and can eliminate chronic administration no
It is hardened that machine chemical fertilizer causes to soil, improves crop anti-adversity (as drought resisting, cold-resistant, resistant to lodging, disease and insect resistance invasion and attack ability),
And unharmful substance residual, belong to ecology, environmental protection, multi-Functional Fertilizers.
(2) of the present invention a kind of based on concentrate biogas slurry organic fertilizer, with anaerobic fermentation residues pass through staged care,
The concentration biogas slurry of the method preparation of back flush, reversely concentration and high cut disperse emulsification is Organic Ingredientss, crude protein therein,
Organic component content, value, range of application and the ecologies such as aminoacid, humic acidss (especially fulvic acid), auximone
Environmental safety is all improved largely compared with anaerobic fermentation residues before processing, for effectively utilizing the high physiology concentrating in biogas slurry
Active substance and scientific formula create condition.Due to avoiding high-temperature process, therefore decrease energy resource consumption.
(3) the preparation method operation of organic fertilizer of the present invention is simple, and cycle is short can be applicable to large-scale production.Usual
In the case of be immiscible based on partial solid phase and the liquid phase in the organic fertilizer concentrating biogas slurry, especially inorganic nutrients are all adopted
With the inorganic chemical fertilizer of agricultural grade, affected by factors such as itself dissolubility and self-contained inorganic impurities again,
Cause the unstability of organic fertilizer system.The present invention dissipates hybrid mode due to employing batch (-type) victory flow point, can be by each reaction
Mixing liquid in kettle efficiently, rapidly and uniformly obtains stable to another continuous phase from a phase or multiple distributed mutually
High-quality product.Thus it is possible to produce going out multiple types, the polyfunctional organic liquid fertilizer based on concentration biogas slurry, to meet
Different soils, the needs of Different Crop, reduces cost, reach the purpose of increasing both production and income.
(4) organic fertilizer of the present invention, improving trace element based on the organic acid chelated microelement concentrating in biogas slurry has
Effect state content, the dispersion and emulsion effect based on high-molecular organic materials such as xanthan gum, hydroxylated celluloses makes in described organic fertilizer
Water-insoluble be in suspension, relatively steady state.Therefore, the organic liquid fertilizer based on concentration biogas slurry of the present invention
There is higher physiologically active and higher stability.Wherein, the Organic substances such as the small-molecular-weight aminoacid that contains, fulvic acid are permissible
Keep its product pH, NPK element and the superfluous stability closing state trace element, and plant roots can be promoted as growth regulator again
The growth of system, stimulates the growth of plant, promotes photosynthesis.
(5) organic fertilizer of the method for the invention preparation contains various bioactivators, in organic acid therein
Gibberellins in butanoic acid and phytohormone, heteroauxing and vitamin B12 have obvious inhibitory action to pathogenic bacteria.Ammonia therein
Have direct effect with ammonium salt and some antibiotic to the pest and disease damage of crop, and pollution-free, no residual hazard, no Drug resistance and be described as
" biomass pesticides ".In terms of suppression pathogen, anaerobic fermentation residues are to escherichia coli, Salmonella paratyphi and bacillus rhusiopathiae suises
Significantly inhibit effect in pathogenic bacterium.
(6) organic fertilizer of the method for the invention preparation, humic acid therein, aminoacid, vitamin and phytohormone,
Root fertilising, foliage dressing etc. can be carried out as organic liquid fertilizer to fruit trees and vegetables, and the proline wherein containing, Caulis et Folium Lini
The materials such as acid, fulvic acid, can be greatly improved the frost resistance of fruit trees and vegetables.
(7) the organic fertilizer test of continuous 6 years of the method for the invention preparation shows, the more untapped soil of soil
The content of organic matter increases by 58.4%, and density declines 16.1%, and voidage increases by 12.9%, and mellow soil layer thickens 8cm, and crumb structure obtains
Arrive improvement.The increase of wherein voidage, is conducive to breathability and the water penetration of soil, so that soil water-reataining fertilizer-keeping ability is strengthened,
Improve soil physical properties.It is applied to vegetable, flowers and special crop seedling nutritious soil or nutritive cube substrate, comprehensive nutrition,
Can widely produce.Also can apply with other fertilizer simultaneously, such as can be made into corruption phosphate fertilizer in natural pond with the mixture of ground phosphate rock, right
Phosphorus shortage soil has notable production-increasing function, is used in mixed way, with nitrogenous fertilizer, the loss that can reduce nitrogen.
(8) the sieve low suspension state being 170 or 200 mesh sieves based on the organic liquid fertilizer concentrating biogas slurry that the present invention produces
Fluid product, insoluble matter solid granulates particle diameter≤0.089mm or 0.0740mm is it can be ensured that meet spray, the requirement of drip irrigation equipment.
Brief description
Fig. 1 is the structural representation of synthesizer described in the embodiment of the present invention;
Wherein, 1, No. 1 allotment reactor;2nd, No. 2 allotment reactors;3rd, No. 3 allotment reactors;4th, hybrid reactor;5、
Filtering centrifuge;6th, batch (-type) prompt stream dispersing mixer;7th, material inlet valve;8th, discharge valve;9th, underflow pump;10th, control chamber (temperature
Degree/stirring/pump);11st, scale liquidometer.
Specific embodiment
With reference to the accompanying drawings and examples embodiments of the present invention are described in further detail.Following examples are used for
The present invention is described, but can not be used for limiting the scope of the present invention.Following examples are all based on described in described reaction unit
Flow chart is carrying out and to illustrate.Wherein, term " No. 1 ", " No. 2 ", " No. 3 " are only used for describing purpose, and it is not intended that referring to
Show or imply relative importance.Concentration biogas slurry in following examples is all prepared from using content of the invention methods described.
Embodiment 1
As shown in figure 1, present embodiments provide a kind of prepare the synthesizer that described organic fertilizer is adopted, this device
The technological process that the present invention prepares organic fertilizer, 1~in this synthesizer No. 3 allotment reactor except volume difference in addition to,
Remaining relevant configuration (includes dog-house, dispersing mixer 6, material inlet valve 7, discharge valve 8, underflow pump 9, control chamber 10, scale
Liquidometer 11 etc.) all same;Additionally, the relevant configuration of hybrid reactor 4 is also essentially identical with 1~No. 3 allotment reactor, difference
It is only that volume is different with effect;And, control chamber 10 all same of each reactor above, it is used to control each reactor
The unlatching of the underflow pump 9, electric heater and dispersing mixer 6 of configuration, and the setting of time and temperature;In addition, 1~No. 3 tune
Join reactor to be all attached by pipeline, respective discharge valve 8, underflow pump 9 and the material inlet valve 7 of hybrid reactor 4;Mixed
Close reactor 4 to be attached with filtering centrifuge 5 by pipeline, discharge valve 8, underflow pump 9.
Embodiment 2
Present embodiments provide a kind of method that organic fertilizer is prepared using embodiment 1 described device, as shown in figure 1, its
Comprise the steps:
(1) open the material inlet valve 7 of No. 1 allotment reactor, start its underflow pump 9, add the concentration that solid content is 10%
Biogas slurry 1000kg, closes material inlet valve 7.Start its dispersing mixer 6, open dog-house, throw in MAP (11-44-0) powder
Body raw material 850kg (concentrates the 85% of biogas slurry), closes dog-house, continues dispersion mixing.Start electric heater heat temperature raising, treat thing
Material is warming up to 60 DEG C, and maintains this temperature to continue dispersion mixing 30min, stops heating and dispersion mixing, obtains grade [5.1-
20.2-0] organic basis liquid fertilizer solution.
(2) open No. 2 allotment reactor material inlet valves 7, start underflow pump 9, add the concentration natural pond of described solid content 10%
Liquid 1000kg, closes material inlet valve 7.Start dispersing mixer 6, open dog-house, throw in carbamide (46-0-0) powder material
850kg (concentrates the 85% of biogas slurry), closes dog-house, continues dispersion mixing.Start electric heater heat temperature raising, treat that material heats up
To 60 DEG C, and maintain this temperature to continue dispersion mixing 30min, stop heating and dispersion mixing, obtain grade [21.1-0-0]
Organic basis nitrogenous fertilizer solution.
(3) open No. 3 allotment reactor material inlet valves 7, start underflow pump 9, add the concentration natural pond of described solid content 10%
Liquid 1000kg, closes material inlet valve 7.Start dispersing mixer 6, open dog-house, throw in trace element fertilizer powder material.Its
In, manganese sulfate [0-0-0-30 (Mn)] 50kg (concentrates the 5% of biogas slurry), and zinc sulfate [0-0-0-21 (Zn)] 50kg (concentrates biogas slurry
5%), Borax [0-0-0-11 (B)] 50kg the 5% of biogas slurry (concentrate), ammonium molybdate [0-0-0-54 (Mo)] 50kg (concentrate biogas slurry
5%), close dog-house, continue dispersion mixing.Start electric heater heat temperature raising, treat that material is warming up to 60 DEG C, and maintain this
Temperature dispersion mixes 90min, stops heating and dispersion mixing, obtains the organic of grade [0-0-0+5.5TE (Mn, Zn, B, Mo)]
Basic chela/complex state trace element liquid fertilizer solution.
(4) open 1,2, No. 3 compounding kettle discharge valves and mixing kettle material inlet valve 7 respectively, start respective underflow pump 9, by 3
Number compounding kettle organic basis liquid fertilizer solution [5.1-20.2-0] 1000kg, No. 2 compounding kettle organic basis nitrogenous fertilizer solution [21.1-0-
0] 1000kg, organic basis chelated microelements fertilizer solution [0-0-0+5.5TE (Mn, Zn, B, Mo)] 1000kg pump respectively
Enter hybrid reactor 4, close 1,2, No. 3 compounding kettle discharge valves 7, mixing kettle material inlet valve 8 and underflow pump 9.Start dispersion
Blender 6, opens dog-house, throws in potash fertilizer powder material 500kg (the 50% of mixed liquor), wherein, potassium sulfate (0-0- first
50) 200kg, potassium chloride (0-0-60) 300kg.Secondly throw in xanthan gum powder material 30kg (the 3% of mixed liquor), or hydroxyl is fine
The plain powder material 30kg (the 3% of mixed liquor) of dimension, closes dog-house, continues dispersion mixing.Start electric heater heat temperature raising, treat
Material is warming up to 60 DEG C, and maintains this temperature dispersion mixing 90min, stops heating and dispersion mixing, obtains grade [7.5-5.8-
8.0+1.6TE] based on concentrate biogas slurry organic fertilizer primary solution.
(5) open hybrid reactor 4 discharge valve 8, start underflow pump 9, by the base of grade [7.5-5.8-8.0+1.6TE]
It is pumped into 170 or 200 mesh filtering centrifuges 5 in the organic fertilizer primary solution concentrating biogas slurry and carries out filtration separation, sieve divides
From slag for soil conditioning raw material, the lower separating liquid of sieve is the described organic liquid fertilizer based on concentration biogas slurry.
Application:By 300~500 times of described organic fertilizer dilute, it is applied to liquid manure in solanaceous vegetables/cultivation of fruit tree
Integrated drop irrigation special fertilizer.
Embodiment 3
Present embodiments provide the method that another kind prepares organic fertilizer using embodiment 1 described device, as shown in figure 1,
It comprises the steps:
(1) open No. 1 allotment reactor material inlet valve 7, start underflow pump 9, add the concentration natural pond of described solid content 20%
Liquid 1000kg, closes material inlet valve 7.Start dispersing mixer 6, open dog-house, throw in Diammonium phosphate (DAP) (15-42-0) powder body former
Material 600kg (concentrates the 60% of biogas slurry), closes dog-house, continues dispersion mixing.Start electric heater heat temperature raising, treat material liter
Temperature is to 50 DEG C, and maintains this temperature to continue dispersion mixing 15min, stops heating and dispersion mixing, obtains grade [5.6-15.8-
0] organic basis liquid fertilizer solution.
(2) open No. 2 allotment reactor material inlet valves 7, start underflow pump 9, add the concentration natural pond of described solid content 20%
Liquid 1000kg, closes material inlet valve 7.Start dispersing mixer 6, open dog-house, throw in carbamide (46-0-0) powder material
600kg (concentrates the 60% of biogas slurry), closes dog-house, continues dispersion mixing.Start electric heater heat temperature raising, treat that material heats up
To 60 DEG C, and maintain this temperature to continue dispersion mixing 15min, stop heating and dispersion mixing, obtain grade [17.3-0-0]
Organic basis nitrogenous fertilizer solution.
(3) open No. 3 allotment reactor material inlet valves 7, start underflow pump 9, add the concentration natural pond of described solid content 20%
Liquid 1000kg, closes material inlet valve 7.Start dispersing mixer 6, open dog-house, throw in trace element fertilizer powder material.Its
In, manganese sulfate [0-0-0-30 (Mn)] 30kg (concentrates the 3% of biogas slurry), and zinc sulfate [0-0-0-21 (Zn)] 30kg (concentrates biogas slurry
3%), Borax [0-0-0-11 (B)] 30kg the 3% of biogas slurry (concentrate), ammonium molybdate [0-0-0-54 (Mo)] 30kg (concentrate biogas slurry
3%), close dog-house, continue dispersion mixing.Start electric heater heat temperature raising, treat that material is warming up to 50 DEG C, and maintain this
Temperature dispersion mixes 60min, stops heating and dispersion mixing, obtains the organic of grade [0-0-0+3.4TE (Mn, Zn, B, Mo)]
Basic chela/complex state trace element liquid fertilizer solution.
(4) open 1,2, No. 3 compounding kettle discharge valves and mixing kettle material inlet valve 7 respectively, start respective underflow pump 9, by 3
Number compounding kettle organic basis liquid fertilizer solution [5.6-15.8-0] 1000kg, No. 2 compounding kettle organic basis nitrogenous fertilizer solution [17.3-0-
0] 1000kg, organic basis chelated microelements fertilizer solution [0-0-0+3.4TE (Mn, Zn, B, Mo)] 1000kg pump respectively
Enter hybrid reactor 4, close 1,2, No. 3 compounding kettle discharge valves 7, mixing kettle material inlet valve 8 and underflow pump 9.Start dispersion
Blender 6, opens dog-house, throws in potassium nitrate (13-0-46) powder material 500kg (the 50% of mixed liquor) first;Secondly throw
Put moderate-element fertilizer powder material, wherein, calcium nitrate [12-0-0-17 (Ca)] 300kg (the 30% of mixed liquor), magnesium sulfate [0-
0-0-10 (Mg)] 200kg (the 20% of mixed liquor);Finally throw in xanthan gum powder material 10kg (the 1% of mixed liquor), or hydroxyl
Cellulose powder material 10kg (the 1% of mixed liquor), closes dog-house, continues dispersion mixing.Start electric heater heat temperature raising,
Treat that material is warming up to 50 DEG C, and maintain this temperature dispersion mixing 30min, stop heating and dispersion mixing, obtain grade [9.1-
5.1-5.8-1.3Ca-0.5Mg+1.4TE] based on concentrate biogas slurry organic fertilizer primary solution.
(5) open hybrid reactor discharge valve 8, start underflow pump 9, by grade [9.1-5.1-5.8-1.3Ca-0.5Mg
+ 1.4TE] be pumped into 170 or 200 mesh filtering centrifuges 5 and filtered based on the organic fertilizer primary solution concentrating biogas slurry
Separate, sieve separates slag for soil conditioning raw material, the lower separating liquid of sieve is the described organic liquid fertilizer based on concentration biogas slurry.
Application:By 500~800 times of described organic fertilizer dilute, it is applied to leaching in solanaceous vegetables/cultivation of fruit tree
Kind, seed dressing, pouring root and foliage-spray special fertilizer.
Embodiments of the invention in order to example and description for the sake of and be given, and be not exhaustively or by this
Bright it is limited to disclosed form.Many modifications and variations are obvious for the ordinary skill in the art.Choosing
Selecting and describe embodiment is in order to the principle of the present invention and practical application are more preferably described, and makes those of ordinary skill in the art
It will be appreciated that the present invention is thus design is suitable to the various embodiments with various modifications of special-purpose.
Claims (10)
1. a kind of preparation method based on the organic fertilizer concentrating biogas slurry is it is characterised in that comprise the following steps:
(1) prepare organic basis liquid fertilizer solution:Take concentration biogas slurry to mix with phosphate fertilizer, under the conditions of 50~60 DEG C dispersion mixing 15~
30min, obtains final product described organic basis liquid fertilizer solution;
(2) prepare organic basis nitrogenous fertilizer solution:Take concentration biogas slurry to mix with nitrogenous fertilizer, under the conditions of 50~60 DEG C dispersion mixing 15~
30min, obtains final product described organic basis nitrogenous fertilizer solution;
(3) prepare organic basis chela/complex state trace element fertilizer solution:Concentration biogas slurry is taken to mix with trace element fertilizer, Ran Hou
Dispersion mixing 60~120min under the conditions of 50~60 DEG C, obtains final product described organic basis chela/complex state trace element fertilizer solution;
(4) preparation is based on the organic fertilizer primary solution concentrating biogas slurry:By described organic basis liquid fertilizer solution, organic basis nitrogenous fertilizer
Solution, organic basis chela/complex state trace element fertilizer solution, potash fertilizer, moderate-element fertilizer and organic polymer dispersion emulsifier mix
Close, dispersion mixing 30~60min under the conditions of 50~60 DEG C, obtain final product the described organic fertilizer primary solution based on concentration biogas slurry;
(5) preparation is based on the organic fertilizer concentrating biogas slurry:Carried out described based on the organic fertilizer primary solution concentrating biogas slurry
Filter centrifugation, sieve separates slag and is used for organic and inorganic solid fertilizer or soil conditioner raw material, and the lower separating liquid of sieve is described
Based on the organic fertilizer concentrating biogas slurry.
2. according to claim 1 method it is characterised in that described step (1) be specially:Using No. 1 allotment reactor, beat
Open material inlet valve, start underflow pump, add concentration biogas slurry 100wt% that described solid content is 5-30wt%, close material inlet valve
And underflow pump;Start dispersing mixer, open dog-house, throw in phosphate fertilizer powder material, injected volume is the described 60- concentrating biogas slurry
85wt%, closes dog-house, continues dispersion mixing;Start heater heat temperature raising, treat that material is warming up to 50-60 DEG C, and maintain
This temperature dispersion mix 15-30min, stop heating and dispersion mixing, obtain grade be [(4.1~5.1)-(16.5~20.2)-
0] or [(5.6~6.9)-(15.8~19.3) -0] organic basis liquid fertilizer solution;
Preferably, described phosphate fertilizer is one or two of MAP (11-44-0) or Diammonium phosphate (DAP) (15-42-0).
3. according to claim 2 method it is characterised in that described step (2) be specially:Using No. 2 allotment reactors, beat
Open material inlet valve, start underflow pump, add concentration biogas slurry 100wt% that described solid content is 5-30wt%, close material inlet valve
And underflow pump;Start dispersing mixer, open dog-house, throw in nitrogenous fertilizer powder material, injected volume is the described 60- concentrating biogas slurry
85wt%, closes dog-house, continues dispersion mixing;Start heater heat temperature raising, treat that material is warming up to 50-60 DEG C, and maintain
This temperature dispersion mix 15-30min, stop heating and dispersion mixing, obtain grade be [(17.3~21.1) -0-0] or
Organic basis nitrogenous fertilizer solution of [(12.8~15.6) -0-0];
Preferably, described nitrogenous fertilizer is carbamide (46-0-0) or ammonium nitrate (34-0-0).
4. according to claim 3 method it is characterised in that described step (3) be specially:Using No. 3 allotment reactors, beat
Open material inlet valve, start underflow pump, add concentration biogas slurry 100wt% that described solid content is 5-30wt%, close material inlet valve
And underflow pump;Start dispersing mixer, open dog-house, throw in trace element fertilizer powder material, injected volume is described concentration natural pond
The 5-10wt% of liquid, closes dog-house, continues dispersion mixing;Start heater heat temperature raising, treat that material is warming up to 50-60 DEG C,
And maintain this temperature dispersion mixing 60-120min, stop heating and dispersion mixing, obtaining grade is [0-0-0+ (3.4~5.5)
TE] organic basis chela/complex state trace element liquid fertilizer solution;
Preferably, described trace element fertilizer is manganese sulfate [0-0-0-30 (Mn)], zinc sulfate [0-0-0-21 (Zn)], Borax [0-
0-0-11 (B)] or one or more of ammonium molybdate [0-0-0-54 (Mo)].
5. according to claim 4 method it is characterised in that described step (4) be specially:Open 1,2, No. 3 allotments respectively
Reactor discharge valve and hybrid reactor material inlet valve, start respective underflow pump, respectively will described organic basic liquid fertilizer solution,
Organic basis nitrogenous fertilizer solution, organic basis Chelating state/complex state trace element fertilizer solution press 1:1:1 ratio is measured respectively, pump
It is fed into hybrid reactor, obtain the mixed liquor that grade is [(5.6~9.3)-(5.3~6.7) -0+ (1.1~1.8) TE];Close
Close 1,2, No. 3 allotment reactor discharge valves, hybrid reactor material inlet valve and underflow pump;The dispersion starting hybrid reactor mixes
Clutch, opens dog-house, throws in potash fertilizer powder material first, its injected volume is the 10-50% of described mixed liquor, in secondly throwing in
Secondary element fertilizer powder material, its injected volume is the 0-30% of described mixed liquor, finally throws in organic polymer dispersion emulsifier powder
Body raw material, its injected volume is the 1-3% of described mixed liquor, closes dog-house, continues dispersion mixing;Start adding of hybrid reactor
Hot device heat temperature raising, treats that material is warming up to 50-60 DEG C, and maintains this temperature dispersion mixing 30-60min, stops heating and disperses
Mixing, obtaining grade is [(5.1~10.2)-(4.8~5.2)-(4.2~13.8)-(0~3.4) Ca- (0~1.3) Mg+ (1.0
~1.8) TE] based on concentrate biogas slurry organic fertilizer primary solution;
Preferably, described potash fertilizer be potassium sulfate (0-0-50), one of potassium chloride [0-0-60)] or potassium nitrate (13-0-46)
Or it is multiple;And/or, described moderate-element fertilizer is in calcium nitrate [12-0-0-17 (Ca)] or magnesium sulfate [0-0-0-10 (Mg)]
One or two;And/or, described machine macromolecule dispersion emulsifier is xanthan gum or hydroxylated cellulose.
6. according to claim 5 method it is characterised in that described step (5) be specially:Open described hybrid reactor to go out
Material valve, starts underflow pump, is pumped into 170 or 200 mesh filtrations by described based on the organic fertilizer primary solution concentrating biogas slurry
Carry out filtration separation in centrifuge, the sieve of described filtering centrifuge separates slag and is used for the solid fertilizer of organic and inorganic or soil conditioner
Raw material, the lower separating liquid of sieve is the described organic liquid fertilizer based on concentration biogas slurry.
7. according to claim 2~6 any one methods described it is characterised in that described dispersing mixer is the prompt stream of batch (-type)
Dispersing mixer, and the rotor speed of described batch (-type) prompt stream dispersing mixer is 2900rpm, described heater is electrical heating
Device.
8. according to claim 1~7 any one methods described it is characterised in that it is 10% that described concentration biogas slurry is solid content
~20% concentration biogas slurry.
9. the organic fertilizer that a kind of claim 1~8 any one methods described is obtained.
10. application in solanaceous vegetables/cultivation of fruit tree for the organic fertilizer described in claim 9 is it is characterised in that have described
300~500 times of machine liquid fertilizer dilute is used for drip irrigation special fertilizer;Or, by described 800~1000 times of use of organic fertilizer dilute
In seed soaking, seed dressing, pouring root or foliage-spray special fertilizer.
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CN108586085A (en) * | 2018-07-13 | 2018-09-28 | 梁山菱花生物科技有限公司 | A kind of production method of amino-acid trace element Water soluble fertilizer |
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CN109809839A (en) * | 2019-03-26 | 2019-05-28 | 中国科学院广州能源研究所 | It is a kind of to match fertile system suitable for biogas slurry Liquid Fertilizer |
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