CN107337498A - A kind of method, selenium-enriched organic fertilizer and its application that selenium-enriched organic fertilizer is produced using dregs of rice class material - Google Patents

A kind of method, selenium-enriched organic fertilizer and its application that selenium-enriched organic fertilizer is produced using dregs of rice class material Download PDF

Info

Publication number
CN107337498A
CN107337498A CN201710700919.5A CN201710700919A CN107337498A CN 107337498 A CN107337498 A CN 107337498A CN 201710700919 A CN201710700919 A CN 201710700919A CN 107337498 A CN107337498 A CN 107337498A
Authority
CN
China
Prior art keywords
selenium
protein
fertilizer
acid
dregs
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
CN201710700919.5A
Other languages
Chinese (zh)
Inventor
丁立朋
丁然
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.)
RIZHAO XURI COMPOSITE MATERIALS Co Ltd
Original Assignee
RIZHAO XURI COMPOSITE MATERIALS Co Ltd
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 RIZHAO XURI COMPOSITE MATERIALS Co Ltd filed Critical RIZHAO XURI COMPOSITE MATERIALS Co Ltd
Priority to CN201710700919.5A priority Critical patent/CN107337498A/en
Publication of CN107337498A publication Critical patent/CN107337498A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C05FERTILISERS; MANUFACTURE THEREOF
    • C05CNITROGENOUS FERTILISERS
    • C05C11/00Other nitrogenous fertilisers
    • CCHEMISTRY; METALLURGY
    • C05FERTILISERS; MANUFACTURE THEREOF
    • C05BPHOSPHATIC FERTILISERS
    • C05B7/00Fertilisers based essentially on alkali or ammonium orthophosphates

Abstract

The present invention relates to organic fertilizer manufacture technology field, there is provided a kind of method that selenium-enriched organic fertilizer is produced using dregs of rice class material.After dregs of rice class material physics defibrination, starched with phosphoroselenoate agent phosphorylation dregs of rice albuminoid slurry or its protein hydrolysate, prepare selenium-rich organic composite fertilizer, strong oxidizing property selenate, selenite be effectively prevent to the Oxidative demage of organic matter, avoid the forfeiture of se complementary effect caused by selenate, selenite are reduced to insoluble elemental selenium in itself, Organic nutrient has been sufficiently reserved, has improved selenium-rich fertilizer efficiency.The selenium-enriched organic fertilizer that the present invention is prepared can use as the outer fertilizer of the base fertilizer of various crop, top dressing and root, improve the utilization rate of selenium.

Description

It is a kind of using dregs of rice class material produce the method for selenium-enriched organic fertilizer, selenium-enriched organic fertilizer and its Using
Technical field
It is more particularly to a kind of to produce selenium-enriched organic fertilizer using dregs of rice class material the present invention relates to organic fertilizer manufacture technology field Method, selenium-enriched organic fertilizer and its application.
Background technology
The existing selenium hardening agent produced used in the technology of selenium-enriched organic fertilizer is mainly selenic acid and sub- selenium with strong oxidizing property Acid.Selenic acid and selenite, all with strong oxidizing property, can destroy organic either in alkalescence, neutrality or under acid state Many nutriments such as the amino acid in fertilizer, itself are reduced to insoluble elemental selenium and reduce se complementary effect.Either in acid Under property, alkalescence or neutral state, selenite can be by Glycine Oxidation, and selenite radical is reduced to mulberry simple substance in itself Selenium.The oxidation reaction speed pole of the selenite amino acid stronger to reproducibility such as cysteine, vitamin C, sulfhydryl compound It hurry up, selenite radical is reduced to grey black elemental selenium.The presence of these redox reactions, the amino in organic fertilizer was both destroyed Many nutriments such as acid, selenic acid and selenite are reduced to insoluble elemental selenium and lose se complementary effect again in itself.
Se-enriched bio-organic fertilizer and preparation method thereof as disclosed in patent CN101717294B, it is extracted with dregs of beans enzyme hydrolysis Amino acid, the amino acid extracted is prepared into chelating selenium, chelated zinc, chela with sodium selenite, zinc sulfate, ferrous sulfate chelating respectively Iron is closed, gained chelating liquid compounding boric acid, calcium ions and magnesium ions antagonist prepare organic trace element composite fertilizer.Its selenite radical used Easily obtained amino acid, vitamin C, phenolic compound can be aoxidized, itself is reduced to elemental selenium.This was both destroyed Many nutriments such as amino acid, vitamin C in organic fertilizer, selenite are reduced to insoluble elemental selenium and lost again in itself Lose se complementary effect.
The content of the invention
In view of this, the invention provides a kind of method that selenium-enriched organic fertilizer is produced using dregs of rice class material.It is prepared by this method The selenium-rich organic composite fertilizer gone out, strong oxidizing property selenate, selenite are effectively prevent to the Oxidative demage of organic matter, is avoided The forfeiture of se complementary effect caused by selenate, selenite are reduced to insoluble elemental selenium in itself, has been sufficiently reserved organic battalion Form point, improve selenium-rich fertilizer efficiency.
In order to solve the above-mentioned technical problem, technical scheme is as follows:
The invention provides a kind of method that selenium-enriched organic fertilizer is produced using dregs of rice class material, comprise the following steps:
(1) by dregs of rice class material defibrination, protein milk is obtained;
(2) protein milk is mixed with the phosphoroselenoate agent of the protein milk solid masses 2~500%, in temperature It is that 0~100 DEG C and pH value carry out phosphorylation reaction under conditions of 7~12, the reaction time is 2~6h, obtains phosphorylated protein Slurry;
(3) pH value for adjusting the phosphorylated protein slurry is 7~9, and selenium-enriched organic fertilizer is obtained after centrifugal filtration.
Preferably, the phosphoroselenoate agent is phosphoroselenoate and its salt, seleno polyphosphoric acid and its salt, the oxidation of seleno ten four The one or more of phosphorus and seleno POCl3;The seleno polyphosphoric acid is that seleno tripolyphosphate, the polyphosphoric acid of seleno four, seleno are more Polyphosphoric acid or seleno cyclic polyphosphoric acid;The salt is ammonium salt, sylvite or sodium salt.
Preferably, citric acid, the quality of the citric acid are additionally added in the protein milk and/or phosphorylated protein slurry It independently is the 0.1~10% of the protein milk and/or phosphorylated protein slurry solid masses.
Preferably, urea, the urea quality are additionally added in the solution before phosphorylation reaction and/or after phosphorylation reaction It independently is the 0~300% of the protein milk or phosphorylated protein slurry solid masses.
Preferably, also include after the centrifugal filtration:The liquid material drying-granulating that the centrifugal filtration is obtained.
Preferably, in the above method of the invention, the protein milk replaces with the water that the protein milk obtains after hydrolysis Solve protein milk.
Wherein, the hydrolysis includes acid, alkali or enzyme hydrolysis.
Preferably, the step of acid or basic hydrolysis protein milk includes:By the protein milk and the protein milk quality 0.05%~5% acid or alkali mixing, degrade 2~48h at 50~105 DEG C, is centrifuged after cooling, removes residue, is made Acid or the protein hydrolysate of base catalysis slurry.
Preferably, the step of protein hydrolysis slurry includes:By the protein milk and the protein milk solid masses 0.05%~5% protease mixing, digested under being 7~12 in pH value, hydrolysis temperature is 20~80 DEG C, enzymolysis time 2 ~72h, centrifuged after enzyme deactivation cooling, remove residue, obtain the protein hydrolysate slurry of enzymatic.
Present invention also offers the selenium-enriched organic fertilizer that the above method is prepared.
Present invention also offers the application of above-mentioned selenium-enriched organic fertilizer, the selenium-enriched organic fertilizer is diluted with water 100~10000 Times, it is fertile outside base fertilizer, top dressing or root as crop.Fertilization mode is using spreading manuer in holes, enter by the way of ditch spread, drip irrigation or foliage spray OK, present invention preferably employs the mode of drip irrigation to apply fertilizer.
Compared with prior art, the present invention has advantages below:
(i), the present invention is to dregs of rice class material using Organic nutrients such as defibrination technology extraction dregs of rice proteinoid, and speed is fast, effect Rate is high, and energy consumption is low, low to destruction of organic material rate.
Dregs of rice class matter protein content is very high, but is wrapped in by cellulose cell wall, is unfavorable for acid, the hydrolysis of alkali and enzyme carries Take.The nutritional ingredient temperature of acid-base catalysis hydrolysis extraction dregs of rice class material is high, and the time is longer.Enzyme hydrolysis condition is gentle, but because there is fibre The parcel of cell membrane is tieed up, and hydrolysis rate is slower, hydrolysis time length.Dregs of rice class material can be with rapid extraction protein etc. after defibrination Organic nutrient, the time is short, efficiency high, and organic nutrient substance is not destroyed substantially.Defibrination has abolished cellulose cell wall To the parcel of the Organic nutrients such as protein, the nutritional ingredients such as protein, polypeptide are extracted in water so that these nutrients The hydrolysis of matter is carried out in homogeneous phase aqueous solution, and speed is accelerated, and hydrolysis efficiency is high, and hydrolysis is more thorough.
(ii), protein, polypeptide and amino acid produce selenium-rich organic composite fertilizer with phosphoroselenoate agent phosphorylation, avoid strong Oxidation and itself reduction of the selenate, selenite of oxidisability to Organic nutrient, avoid Organic nutrient Destroy and selenate, selenite are reduced to insoluble elemental selenium and caused by se complementary effect forfeiture.
Protein, polypeptide and amino acid can be modified with phosphorylation, dissolubility, foaming capacity after protein phosphorylation, breast Change ability, moisture holding capacity and solution viscosity are all greatly improved.The present invention using seleno polyphosphoric acid, the tetraphosphine oxide of seleno ten, The phosphoroselenoate such as seleno phosphorous oxychloride agent carries out the phosphorylation of protein and hydrolysate.Phosphoroselenoate agent is in neutral and alkali environment In with protein, polypeptide, amino acid carry out phosphorylation reaction, generate corresponding phosphoroselenoate compound.The phosphoroselenoate of generation Thing is stable in, in alkaline solution.Contain substantial amounts of nitrogen, phosphorus, potassium and trace elements of selenium in product, there is fertilizer well Effect.Selenium atom can be easily absorbed by crops with Phosphorylated products, have good selenium-supply function, therefore may be used as selenium-supply Organic fertilizer.The use of phosphoroselenoate agent of the present invention, the selenate of strong oxidizing property, selenite are effectively prevent to organic matter Oxidative demage, Organic nutrient is sufficiently reserved, has improved fertilizer efficiency.Meanwhile eliminate selenate again, selenite is reduced For the decline of se complementary effect caused by insoluble elemental selenium.Meanwhile the selenium in the selenophosphates in product can readily with Phosphate is absorbed by crops, and improves the utilization rate of selenium.
Embodiment
The invention provides a kind of method that selenium-enriched organic fertilizer is produced using dregs of rice class material, comprise the following steps:
(1) by dregs of rice class material defibrination, protein milk is obtained;
(2) protein milk is mixed with the phosphoroselenoate agent of the protein milk solid masses 2~500%, in temperature It is that 0~100 DEG C and pH value carry out 2~6h of phosphorylation reaction under conditions of 7~12, obtains phosphorylated protein slurry;
(3) pH value for adjusting the phosphorylated protein slurry is 7~9, and selenium-enriched organic fertilizer is obtained after centrifugal filtration.
Dregs of rice class material in the present invention is residue after the oil expression such as soybean, cottonseed, vegetable seed, benne, tea seed, commonly referred to as Dregs of beans, rapeseed dregs, cotton dregs, benne are broken, tea seed cake etc..
Dregs of rice class matter protein content is very high, but is wrapped up by cellulose cell wall, acid and alkali hydrolysis extraction organic nutrient substance Temperature is high, time length, easily causes the destruction of nutriment.Enzyme hydrolysis condition is gentle, but because there is the parcel of cellulose cell wall, and Hydrolysis rate is slower, hydrolysis time length, and enzymolysis is not thorough.The present invention is used dregs of rice class material defibrination, realizes protein and fiber The separation of plain cell membrane, quickly the nutritional ingredient of dregs of rice class material is extracted in water, protein milk is made.Organic nutrient substance dissociates Thoroughly, to organic nutrient substance substantially without destruction.
The present invention is not particularly limited to the mode of dregs of rice class material defibrination, is using the conventional defibrination mode in this area Can.It is preferred that physics defibrination is carried out using fiberizer.It can be the fiberizer of plane mill or taper rubbing disc.Further It is preferred that physics defibrination is carried out using 200~1000mm of grinding wheel diameter high-density paste mill.Physics refining process is with short production cycle, battalion It is low to form a point recovery rate height, destructive rate, production efficiency height.
In the present invention, dregs of rice class material is before defibrination is carried out, and first dregs of rice class material absorbs water complete, in order to defibrination, The intracellular matters such as protein, fat in dregs of rice class material fully dissociate during defibrination.The present invention is to dregs of rice class thing The water sucting mode of matter is not particularly limited, it is preferred to use the mode of water vapour boiling or water immersion is absorbed water.It is excellent in the present invention The time for selecting dregs of rice class material water vapour boiling is 10~90min, more preferably 20~80min;Or dregs of rice class material is soaked in water Fully absorbed water overnight.Dregs of rice class material after absorbing water completely is subjected to defibrination, obtains protein milk.Obtained protein milk is directly used In preparing selenium-enriched organic fertilizer, or selenium-enriched organic fertilizer is prepared after acid, alkali or enzymatic hydrolysis.
In the present invention, obtained protein milk is subjected to acid, alkali or enzymatic hydrolysis, to obtain the protein of small molecule, more Peptide and amino acid, be advantageous to crop absorption.
In the present invention, using acid or during basic hydrolysis protein milk, the addition of acid or alkali is the protein milk quality 0.05%~5%, more preferably 0.1~4%, more preferably 1~3%.In the present invention, acid, the reaction temperature of basic hydrolysis For 50 DEG C~105 DEG C, preferably 60~90 DEG C.Before heating, citric acid is preferably added in protein milk, is played in hydrolytic process Disinfection, prevent the effect of smell pollution.Wherein, the addition of citric acid is the 0.1%~10% of protein milk solid masses, It is further 2%~5%.
In the present invention, sour species used is not limited, preferably sulfuric acid, phosphoric acid and hydrochloric acid;In the present invention, to used The species of alkali does not limit, preferably potassium oxide, the inorganic weak acid salt of potassium hydroxide and potassium, such as potassium carbonate, saleratus, four boron Sour sodium, kodalk, borax etc..
The time of protein milk and acid or alkali reaction is 2~48h, more preferably 12~36h.Reaction cools after terminating, and centrifuges Separation, residue is removed, acid or the protein hydrolysate slurry of base catalysis is made.
In the present invention, it is preferred to use protease carries out catalyzing hydrolysis to protein milk.The mild condition of enzymatic hydrolysis, nutrition Thing destructive rate is low, and hydrolysis is thorough.
The present invention is not limited the species of enzyme used, preferably vegetable protein hydrolase.The addition of the protease The 0.05~5% of preferably described protein milk solid masses, more preferably 0.1~4%, more preferably 0.5~3%.
In the present invention, the reaction temperature of albumen enzymatic hydrolysis is 20 DEG C~80 DEG C, more preferably 35~60 DEG C, protease The reaction time of catalyzing hydrolysis is 2~72h, more preferably 12~48h.After hydrolysis terminates, hydrolyzate is warming up to 80~100 DEG C Enzyme is inactivated, after being cooled to normal temperature, obtains the protein hydrolysate slurry of enzymatic.
The present invention reacts the protein milk being prepared and/or protein hydrolysate slurry with phosphoroselenoate agent, and preparing selenium-rich has Machine fertilizer.Control 0~100 DEG C of the temperature of phosphorylation reaction, 30~60 DEG C of preferable temperature;Control the pH value of phosphorylation reaction for 7~ 12, more preferably 8~11.Protein milk and/or protein hydrolysate slurry are mixed with phosphoroselenoate agent, carry out phosphorus under these conditions Acidification reaction.
In the present invention, the addition of phosphoroselenoate agent for protein milk and/or protein hydrolysate starch solid masses 2~ 500%, preferably 10%~200%, more preferably 20%~100%.
In the present invention, the feed postition of the phosphoroselenoate agent be able to can also be used by the way of being directly added into Phosphoroselenoate agent is first dissolved in after phosphoric acid to the mode added.For strong water suction, can be with water, the seleno of amino vigorous reaction The phosphoric acid agent such as tetraphosphine oxide of seleno ten, seleno POCl3 etc., it is preferred to use these phosphoroselenoate agents are first dissolved in into phosphoric acid The mode added afterwards, in case vigorous reaction causes the loss of nutritional ingredient.The preferred concentration of the phosphoric acid solution be 5~ 75%, more preferably 25~60%.The phosphoroselenoate agent is dissolved in after phosphoric acid solution, has actually occurred polymerisation, raw Into seleno polyphosphoric acid.
In the present invention, the phosphoroselenoate agent is phosphoroselenoate and its salt, and seleno polyphosphoric acid and its salt, seleno ten aoxidize The one or more of four phosphorus, seleno POCl3;The seleno polyphosphoric acid is seleno tripolyphosphate, the polyphosphoric acid of seleno four, seleno Polyphosphoric acids;The salt is the salt soluble in water such as its ammonium salt, sylvite and sodium salt.Specific kind of the present invention to phosphoroselenoate agent Class is not particularly limited, using any one or a few in mentioned kind.
In the present invention, the pH value of phosphorylation reaction is controlled 7~12.Before phosphoric acid agent addition, first egg is adjusted with alkali The pH starched in vain is alkalescence.Wherein, the addition of alkali is 1.05~1.2 times of the total acid equivalent of phosphoric acid agent.Alkali in the protein milk Feed postition preferably under conditions of to keep reacting liquid pH value be 7~12, the mode that is synchronously added with phosphoroselenoate agent.To The phosphoric acid solution of phosphoroselenoate agent or phosphoroselenoate agent is slowly added into mixed liquor, the pH value for ensureing reaction solution is 7~12.
In the present invention, the preferably time of phosphorylation reaction is 2~6h, more preferably 3~5h.After reaction terminates, phosphorus is obtained Acidified protein is starched.Gained phosphorylated protein starches non-oxidative, in, stable in alkaline solution, and contains substantial amounts of phosphorus, potassium and micro- Secondary element selenium, there is good fertilizer efficiency.
In the present invention, preferably add urea in protein milk and/or protein hydrolysate slurry and prepare selenium-enriched organic fertilizer.Urea adds Entering can add or added after phosphorylation before phosphorylation.The addition of urea is that the protein milk is consolidated The 0~300% of weight, more preferably 50~200%.
The present invention is preferably also added into citric acid in obtained phosphorylated protein slurry.Due to protein in dregs of rice class material, The contents of organic matter such as fat are higher, and processing procedure easily rots, and release stench.The present invention adds lemon in reaction solution Lemon acid is used for antisepsis and sterilization deodorizing, improves the bin stability of product.The addition of citric acid is phosphorylated protein in the present invention Starch the 0.1~10% of solid masses, preferably 0.5%~5%, more preferably 1%~3%.
The pH value for adjusting reaction solution is 7~9, centrifugal filtration, removes residue, obtains selenium-enriched organic fertilizer.
Any residue obtained in the present invention can be used as soil conditioner after drying, also can together with animal wastes decomposed system Standby organic fertilizer.
In the present invention, the method for adjusting reacting liquid pH value is not particularly limited, preferably adjusted with the acid, the alkali that have fertilizer efficiency Reaction solution is to required pH value.Wherein, acid preferably phosphoric acid and sulfuric acid;Alkali is preferably the salt of weak acid of potassium oxide, potassium hydroxide or potassium, More preferably potassium carbonate, potassium hydroxide, dipotassium tetraborate, potassium metaborate, borax etc..
The present invention is not particularly limited to the mode of separation of solid and liquid, it is preferred to use the mode of centrifugal filtration.
The selenium-enriched organic fertilizer that the present invention is prepared can also be made as granular fertilizer.By the selenium-enriched organic fertilizer of liquid through being granulated Technique is granulated, you can prepares granular pattern selenium-enriched organic fertilizer.During granulation, other kinds of fertilizer can also be added, such as With preparing selenium-rich urea together with urea mother liquor.The present invention is not particularly limited to the technique of granulation, using the routine in this area Prilling.
The selenium-enriched organic fertilizer that the present invention is prepared can be used as the outer fertilizer of base fertilizer, top dressing and root.It is diluted with water 100~10000 Times, more preferably 500~2000 times administrations for being used for low selenium crop, the particularly administration of crop, obtain selenium-rich for poor selenium Agricultural product.Fertilization mode is by the way of cave-applied fertilizer burial, pick ditch fertilising burial mode, the mode of drip irrigation and foliage spray side Formula.For Different Crop, applied using optimal fertilization mode.Can for the fruit tree of growth period length, Chinese yam, green onion, ginger and garlic, tealeaves etc. Include applying fertilizer by the way of foliage spray using any fertilization mode.Present invention preferably employs the mode of drip irrigation to apply fertilizer.Particularly pair In tealeaves, using continuous drip irrigation, the stable selenium-rich organic tea of Se content can be obtained.
According to crop is different and soil Se content, selenium-enriched organic fertilizer mu dosage of the present invention is 2~20kg/ times, preferably 5~ 15kg/ times, Se content, the yield and quality of crop can be effectively improved.For graininess organic fertilizer, can be dissolved in after water by upper Method use is stated, directly can also be applied fertilizer by the way of conventional.
Above-mentioned selenium-enriched organic fertilizer provided by the invention can not dissolve in transition metal ions and heavy metal ion reaction generation The precipitation of water, reduce se complementary effect.Therefore, selenium-enriched organic fertilizer of the invention avoids and transition metal ions or a huge sum of money in fertilising Category ion is mixed to be applied or uses with.
For the object, technical solutions and advantages of the present invention are more clearly understood, the present invention is entered with reference to embodiment Row detailed description, but they can not be interpreted as limiting the scope of the present invention.
Embodiment 1
1 physics defibrination
By dregs of rice class material water vapour boiling 60min, with fiberizer physics defibrination, refining concentration 25%, protein milk is made.
2 protein milk enzyme hydrolysis
The parts by weight of protein milk 1000 in step 1,300,000 enzyme activity are added by the amount of the solid masses 0.5% in protein milk Alkali protease, with mass fraction be 30% potassium hydroxide solution adjust pH to 10.0~11.0, controlling reaction temperature be 45~ 50 DEG C, under pH value 10~11, hydrolyze 16h.Reaction solution is warming up into 85 DEG C inactivates enzyme, after being cooled to normal temperature, obtains enzymatic water Solve protein milk.
3 phosphorylations produce selenium-rich organic composite fertilizer
Gained enzymatic hydrolysis protein milk in step 2, the saturated solution of 312 parts by weight potassium hydroxide is added, adds 200 weights Part urea is measured, under conditions of keeping reacting liquid temperature to be not higher than 40 DEG C, is slowly added into the selenizing four of 200 parts by weight, 50% 6 oxygen four The phosphoric acid solution of phosphorus (tetraphosphine oxide of four seleno ten), be 10~12 to reacting liquid pH value, keep reaction temperature not higher than 40 DEG C and Under conditions of pH value is 9~12,6h is reacted.Fully after dissolving, the parts by weight of citric acid 3 are added, with potassium hydroxide saturated solution Reacting liquid pH value is adjusted to 7, centrifugal filtration obtains selenium-rich organic composite fertilizer.
Content of each nutritional ingredient in the compoiste fertilizer solids is respectively in gained organic Se-rich composite fertilizer:Ammonia Base acid content of peptides 8.7%, Se content 6.4%, potassium content 23.6%, nitrogen content 10.2%, phosphorus content 6.0%, and remain The a variety of nutriments and trace element of dregs of beans, it is high-quality selenium-rich organic composite fertilizer.
Embodiment 2
1 physics defibrination
Dregs of rice class material is soaked in water overnight, ensures that water suction is complete.With fiberizer physics defibrination, protein milk is obtained.
2 phosphorylations produce selenium-rich organic composite fertilizer
The gained parts by weight of protein milk 1000 in step 1, under conditions of 60 DEG C of reacting liquid temperature is kept, add 546 weight The saturated solution of part potassium carbonate, is slowly added into the phosphoric acid solution of the seleno POCl3 of 300 parts by weight 25%, is to reacting liquid pH value 12, keep reaction temperature to be 60 DEG C and under conditions of pH value is 8~10, react 4h.The parts by weight of citric acid 50 are added, are adjusted with phosphoric acid Section reacting liquid pH value is adjusted to 8, centrifugal filtration.Filtrate after filtering is granulated together with urea mother liquor, obtains selenium-rich organic composite fertilizer.
Embodiment 3
1 physics defibrination
By dregs of rice class material vapors boiling 45min, with fiberizer physics defibrination, protein milk is made.
2 protein milk enzyme hydrolysis
The parts by weight of protein milk 1000 in step 1, neutral compound protein is added by the 4.5% of protein milk solid part quality Enzyme, it is that 30% potassium hydroxide solution adjusts pH to 8.0, water under conditions of controlling reaction temperature is 55 DEG C, pH value is 8 with mass fraction Solve 48h.Reaction solution is warming up into 90 DEG C inactivates enzyme, after being cooled to normal temperature, obtains protein hydrolysis slurry.
3 phosphorylations produce selenium-rich organic composite fertilizer
Gained protein hydrolysis slurry, adds 100 parts by weight of urea in step 2, adds the saturation of 317 weight parts potassium bicarbonates Solution, the phosphoric acid solution of the phosphorus of 150 parts by weight, 6,0%0 selenizing four is slowly added into, is 8 to reacting liquid pH value, holding reaction temperature is Under conditions of 80 DEG C and pH value are 7.5~8.5,2h is reacted.The parts by weight of citric acid 5 are added, reacting liquid pH value is adjusted to 9, from The heart filters, and is granulated Hou get selenium-rich organics composite fertilizer.
Embodiment 4
1 physics defibrination
By dregs of rice class material vapors boiling 60min, with the large-scale high-density paste mill physics defibrination of paper-making pulping, albumen is made Slurry.
2 protein milk acid-catalyzed hydrolysis
The parts by weight of protein milk 1000 in step 1,2.5% phosphoric acid of addition protein milk quality, 0.5% sulfuric acid, 1% Citric acid.85 DEG C are warming up to, hydrolysis 12h.Reaction finishes, and is cooled to normal temperature, obtains acid protein hydrolysats slurry.
3 phosphorylations produce selenium-rich organic composite fertilizer
Gained acid protein hydrolysats slurry in step 2, the urea of acid protein hydrolysats slurry quality 300% is added, by 300 parts by weight hydrogen The phosphoric acid solution of the saturated solution of potassium oxide and the seleno tripolyphosphate of 180 parts by weight 50%, is synchronously added to sour water solution under stirring In protein milk, two kinds of material charging rates are adjusted, charging process remains reacting liquid pH value between 10~12.Feed Finish, holding reacting liquid pH value is 8~10, reaction temperature reacts 1h under conditions of being 95 DEG C.Reaction is finished, and reacting liquid pH value is adjusted To 8, centrifugal filtration, Hou get selenium-rich organics composite fertilizer is granulated.
Embodiment 5
1 physics defibrination
By dregs of rice class material vapors boiling 50min, with the large-scale high-density paste mill physics defibrination of paper-making pulping, albumen is made Slurry.
2 protein milk alkali catalyzed hydrolysis
The parts by weight of protein milk 1000 in step 1, add 5% potassium hydroxide of protein milk quality, protein milk solid matter The citric acid of amount 10%.105 DEG C are warming up to, hydrolysis 24h.Reaction finishes, and is cooled to normal temperature, obtains basic hydrolysis protein milk.
3 phosphorylations produce selenium-rich organic composite fertilizer
Gained basic hydrolysis protein milk in step 2, the urea of basic hydrolysis protein milk quality 100% is added, by 300 parts by weight hydrogen The saturated solution of potassium oxide and 180 parts by weight seleno tripolyphosphates, are synchronously added in basic hydrolysis protein milk under stirring, adjustment two Kind material charging rate, charging process remain reacting liquid pH value between 9~11.Charging finishes, and keeps reacting liquid pH value 6h is reacted under conditions of being 20 DEG C for 8~10, reaction temperature.Reaction is finished, and reacting liquid pH value is adjusted into 7, centrifugal filtration, is granulated Hou get selenium-rich organics composite fertilizer.
Embodiment 6
In June, 2015 is sub in sunshine mountain and sea day tourism and resort zone by gained organic Se-rich composite fertilizer in embodiment 1 to September Young tea leaves leaf Specialty Co-operative Organization Tea planting carries out effect test.Tealeaves fertilizing method:Every mu of tealeaves composite fertilizer's consumption 15kg, water are dilute 500 times are released, in tea row fertigation, is picked tea-leaves after 5 days.Blank control drip irrigation same amount water, the same period pick tea-leaves.After testing, fertilization area Tealeaves Se content is 9.6mg/kg dry teas, and check plot tealeaves Se content is 1.2mg/kg dry teas.The stronger fragrance of tealeaves fragrance.
Organic Se-rich composite fertilizer produced by the invention Se content is high, and inorganic fertilizer efficiency composition and Organic nutrient enrich.Make Organic Se-rich composite fertilizer produced by the invention can effectively improve tealeaves Se content, and energy improving quality, is high-quality selenium-rich organic Composite fertilizer.
Described above is only the preferred embodiment of the present invention, it is noted that for the ordinary skill people of the art For member, under the premise without departing from the principles of the invention, some improvements and modifications can also be made, these improvements and modifications also should It is considered as protection scope of the present invention.

Claims (11)

  1. A kind of 1. method that selenium-enriched organic fertilizer is produced using dregs of rice class material, it is characterised in that:Comprise the following steps:
    (1) by dregs of rice class material defibrination, protein milk is obtained;
    (2) protein milk is mixed with the phosphoroselenoate agent of the protein milk solid masses 2~500%, temperature be 0~ 100 DEG C carry out phosphorylation reaction with pH value under conditions of 7~12, and the reaction time is 2~6h, obtain phosphorylated protein slurry;
    (3) pH value for adjusting the phosphorylated protein slurry is 7~9, and selenium-enriched organic fertilizer is obtained after centrifugal filtration.
  2. 2. according to the method for claim 1, it is characterised in that:The phosphoroselenoate agent is phosphoroselenoate and its salt, selenium For the one or more of polyphosphoric acid and its salt, the tetraphosphine oxide of seleno ten and seleno POCl3;The seleno polyphosphoric acid is seleno Tripolyphosphate, the polyphosphoric acid of seleno four, seleno polyphosphoric acids or seleno cyclic polyphosphoric acid;The salt is ammonium salt, sylvite or sodium salt.
  3. 3. according to the method for claim 1, it is characterised in that:In the protein milk and/or phosphorylated protein slurry also Citric acid is added, the quality of the citric acid independently is the protein milk and/or the phosphorylated protein starches solid masses 0.1~10%.
  4. 4. according to the method for claim 1, it is characterised in that:It is molten before phosphorylation reaction and/or after phosphorylation reaction Urea is additionally added in liquid, the quality of the urea independently is the 0 of the protein milk or phosphorylated protein slurry solid masses ~300%.
  5. 5. according to the method for claim 1, it is characterised in that:Also include after the centrifugal filtration:By the centrifugal filtration Obtained liquid material drying-granulating.
  6. 6. according to the method described in Claims 1 to 5 any one, it is characterised in that:The protein milk replaces with the albumen Starch the protein hydrolysate slurry obtained after hydrolysis.
  7. 7. according to the method for claim 6, it is characterised in that the hydrolysis includes acid, alkali or enzyme hydrolysis.
  8. 8. according to the method for claim 7, it is characterised in that the acid includes the step of basic hydrolysis protein milk:By institute State protein milk to mix with the acid or alkali of the protein milk quality 0.05%~5%, degrade 2~48h at 50~105 DEG C, cooling After centrifuge, remove residue, be made acid or base catalysis protein hydrolysate slurry.
  9. 9. according to the method for claim 7, it is characterised in that the step of protein hydrolysis are starched includes:By the egg White slurry mixes with the protease of the protein milk solid masses 0.05%~5%, is digested, digested under being 7~12 in pH value Temperature is 20~80 DEG C, 2~72h of enzymolysis time, is centrifuged after enzyme deactivation cooling, removes residue, obtain the hydrolysis egg of enzymatic White slurry.
  10. 10. the selenium-enriched organic fertilizer being prepared according to claim 1~9 any one methods described.
  11. 11. the application of selenium-enriched organic fertilizer described in claim 10, it is characterised in that:The selenium-enriched organic fertilizer is diluted with water 100~ 10000 times use, fertilizer outside base fertilizer, top dressing or root as crop.
CN201710700919.5A 2017-08-16 2017-08-16 A kind of method, selenium-enriched organic fertilizer and its application that selenium-enriched organic fertilizer is produced using dregs of rice class material Pending CN107337498A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201710700919.5A CN107337498A (en) 2017-08-16 2017-08-16 A kind of method, selenium-enriched organic fertilizer and its application that selenium-enriched organic fertilizer is produced using dregs of rice class material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201710700919.5A CN107337498A (en) 2017-08-16 2017-08-16 A kind of method, selenium-enriched organic fertilizer and its application that selenium-enriched organic fertilizer is produced using dregs of rice class material

Publications (1)

Publication Number Publication Date
CN107337498A true CN107337498A (en) 2017-11-10

Family

ID=60214194

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201710700919.5A Pending CN107337498A (en) 2017-08-16 2017-08-16 A kind of method, selenium-enriched organic fertilizer and its application that selenium-enriched organic fertilizer is produced using dregs of rice class material

Country Status (1)

Country Link
CN (1) CN107337498A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109485499A (en) * 2018-12-03 2019-03-19 上海农乐生物制品股份有限公司 A kind of preparation method of low lead organic slow-release plant nitrogen fertilizer
CN116530375A (en) * 2023-05-11 2023-08-04 宜春市科学院(江西富硒产业研究院) Planting method of selenium-enriched vegetables

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20080302151A1 (en) * 2007-06-11 2008-12-11 Timothy Allan Stemwedel Soluble Liquid Fertilizer for Organic Agriculture Derived From Soy Meal
CN101595977A (en) * 2008-06-02 2009-12-09 浙江医药股份有限公司新昌制药厂 Be of value to the formula food and the application thereof of eyes duration of photopic vision
CN103570445A (en) * 2012-08-02 2014-02-12 青岛海大生物集团有限公司 Preparation method of phosphorylation enteromorpha oligosaccharide powder fertilizer

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20080302151A1 (en) * 2007-06-11 2008-12-11 Timothy Allan Stemwedel Soluble Liquid Fertilizer for Organic Agriculture Derived From Soy Meal
CN101595977A (en) * 2008-06-02 2009-12-09 浙江医药股份有限公司新昌制药厂 Be of value to the formula food and the application thereof of eyes duration of photopic vision
CN103570445A (en) * 2012-08-02 2014-02-12 青岛海大生物集团有限公司 Preparation method of phosphorylation enteromorpha oligosaccharide powder fertilizer

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109485499A (en) * 2018-12-03 2019-03-19 上海农乐生物制品股份有限公司 A kind of preparation method of low lead organic slow-release plant nitrogen fertilizer
CN116530375A (en) * 2023-05-11 2023-08-04 宜春市科学院(江西富硒产业研究院) Planting method of selenium-enriched vegetables

Similar Documents

Publication Publication Date Title
CN104072232A (en) Environment-friendly chemical fertilizer
CN108484303A (en) A kind of environment protecting plant foliar fertilizer and preparation method thereof
CN104261904A (en) Trace element sucrose complex fertilizer additive, and preparation method and application thereof
CN104291903A (en) Method for preparing dendrobium officinale nutrient fertilizer
CN107337498A (en) A kind of method, selenium-enriched organic fertilizer and its application that selenium-enriched organic fertilizer is produced using dregs of rice class material
CN103467751B (en) The extracting method of humic acids in alcohol tank liquid fermented sludge
CN107739249A (en) Saline and alkaline region industrial crops improvement calcium boron clear liquid fertilizer and preparation method thereof
CN105541519A (en) Efficient chelating state liquid fertilizer
CN108059548A (en) A kind of Nutrition Soil planted for succulent and preparation method thereof
CN102503719B (en) Preparation method of strong-acidic water-soluble fertilizer special for alkaline soil
CN109251082A (en) A kind of humic acid foliar fertilizer and preparation method thereof
CN106187499A (en) A kind of nursery stock fertilizer with bacteriostasis
CN106431692A (en) Amino acid calcium water-soluble fertilizer and preparation method thereof
CN109134106A (en) A kind of organic water-soluble fertilizer preparation method for material for alleviating granulated sugar tangerine yellows
CN105272541A (en) Preparation method of abundant-nutrition special soilless culture fertilizer for cherry tomato
CN107857606A (en) A kind of ureaformaldehyde modifying agent and its preparation method and application
CN103708905A (en) Compound fertilizer special for organic selenium-enriched tea
CN105924283B (en) A kind of preparation method of colourless organic water-soluble fertilizer
CN106278570A (en) A kind of nursery stock rejuvenation fertilizer
CN104557213A (en) Method for preparing special fertilizer for day-lily buds and producing byproduct sodium dihydrogen phosphate
CN107500856A (en) A kind of method, selenium-enriched organic fertilizer and its application that Enteromorpha fast liquefying is produced to selenium-enriched organic fertilizer
CN106631537A (en) Selenium methionine chelate humic acid additive for paste foliar fertilizer for pear trees
CN108101670A (en) A kind of preparation method of environment-protecting type organic fertilizer
CN108033843A (en) Organic cake fertilizer of seaweed bio and preparation method thereof
CN106748215A (en) A kind of special paste foliage fertilizer additives of pear tree for adding rare earth modified shitosan

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
RJ01 Rejection of invention patent application after publication

Application publication date: 20171110