CN104311181B - Preparation method of special fertilizer for honey peaches - Google Patents

Preparation method of special fertilizer for honey peaches Download PDF

Info

Publication number
CN104311181B
CN104311181B CN201410478298.7A CN201410478298A CN104311181B CN 104311181 B CN104311181 B CN 104311181B CN 201410478298 A CN201410478298 A CN 201410478298A CN 104311181 B CN104311181 B CN 104311181B
Authority
CN
China
Prior art keywords
special fertilizer
honey peach
dihydrogen phosphate
filtrate
phosphoric acid
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.)
Expired - Fee Related
Application number
CN201410478298.7A
Other languages
Chinese (zh)
Other versions
CN104311181A (en
Inventor
陈肖虎
廖吉星
李军旗
喻茂
高贵龙
吴俊良
薛涛
苏涛
曾舒
陈双龙
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.)
Guizhou Kailin Group Co Ltd
Original Assignee
Guizhou University
Guizhou Kailin Group Co Ltd
Guizhou Kexin Chemical and Metallurgical 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 Guizhou University, Guizhou Kailin Group Co Ltd, Guizhou Kexin Chemical and Metallurgical Co Ltd filed Critical Guizhou University
Priority to CN201410478298.7A priority Critical patent/CN104311181B/en
Publication of CN104311181A publication Critical patent/CN104311181A/en
Application granted granted Critical
Publication of CN104311181B publication Critical patent/CN104311181B/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C05FERTILISERS; MANUFACTURE THEREOF
    • C05BPHOSPHATIC FERTILISERS
    • C05B7/00Fertilisers based essentially on alkali or ammonium orthophosphates
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B25/00Phosphorus; Compounds thereof
    • C01B25/16Oxyacids of phosphorus; Salts thereof
    • C01B25/26Phosphates
    • C01B25/30Alkali metal phosphates
    • C01B25/305Preparation from phosphorus-containing compounds by alkaline treatment
    • CCHEMISTRY; METALLURGY
    • C05FERTILISERS; MANUFACTURE THEREOF
    • C05DINORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C; FERTILISERS PRODUCING CARBON DIOXIDE
    • C05D9/00Other inorganic fertilisers
    • C05D9/02Other inorganic fertilisers containing trace elements

Abstract

The invention relates to the technical field of chemical industry, and discloses a preparation method of a special fertilizer for honey peaches. The method comprises the following steps: analyzing the ratio of nutritional elements required by the growth of honey peaches by researching the amounts of absorption of all the nutritional elements from soil in the growth process of honey peaches, reacting phosphoric acid with carbomite to generate an intermediate, introducing ammonia gas into the intermediate to produce ammonium dihydrogen phosphate, crystallizing parts of ammonium dihydrogen phosphate to precipitate, adjusting the ratio of nutritional elements in a reaction solution to meet the growth of honey peaches, and adding other nutritional elements required by honey peaches in order to prepare the special fertilizer for honey peaches. The preparation method has the advantages of full utilization of raw materials, good quality of the prepared ammonium dihydrogen phosphate, and low cost of the prepared special fertilizer for honey peaches.

Description

A kind of compound method of honey peach special fertilizer
Technical field
The present invention relates to chemical technology field, more particularly to a kind of compound method of honey peach special fertilizer.
Background technology
Honey peach belongs to a kind of spherical edible fruits, and honey peach has the functions such as skin Caring, clearing stomach, lung moistening, eliminating the phlegm.It The content of protein doubles than Fructus Mali pumilae, Fructus Vitis viniferae, seven times more than pear;The content of ferrum three times more than Fructus Mali pumilae, five times more than pear, Have the good reputation of " queen in fruit ".There is plantation China more.Rich in multivitamin, wherein vitamin C highest.Honey peach Pterostyrax in Defoliation small arbor plant, general height of tree 3-4 rice.Dryness is weak, and tree crown is opened a business.Sapling up-growth is vigorous, and growth branch reaches more than 1 meter within 1 year. Bud has prematureness, and tree crown is formed soon.Start result early, 2~3 years beginning results of field planting, 6~7 years Dasheng fruiting periods, 15~20 years After be fade-in aging, the life-span is shorter, and general management can also keep high yield in preferable 25~30 years.Honey peach is nutritious, meat Sweet juice is many, containing abundant irony, can increase human body hemoglobin quantity, ancients say:Often eat Fructus Persicae energy " beneficial appearance ", reason may Here.The contribution of Fructus Persicae, except Fructus Persicae meat energy Yangxuemeiyan, central Semen Persicae also has the effect of blood circulation promoting and blood stasis dispelling, antiasthmatic-antitussive.The traditional Chinese medical science Have a prescription, entitled five kernel soup, can loosening bowel to relieve constipation, promoting blood circulation to remove obstruction in the collateral, composition exactly Semen Persicae, Fructus Cannabiss, Semen Pruni, Semen Platycladi and Semen Armeniacae Amarum, for constipation due to dry stool, the people of liver-heat blood stasis and amenorrhea is particularly helpful.It should be noted that although semen juglandiss can be invigorated blood circulation, But during feminine menstrual, through measuring excessive or period inedibility of passing through.Meanwhile, the natural gum that peach tree flows out is also wonderful simply Medicine, can strong nourish, and can adjust blood sugar level again.Every hectogram Fructus Persicae contains 0.8 gram of protein, 0.1 gram of fat, 7 grams of saccharide, slightly fibre Dimension 4.1 grams, 0.5 gram of ash, 8 milligrams of calcium, 20 milligrams of phosphorus, 1.0 milligrams of ferrum, 0.01 milligram of carotene, 0.01 milligram of thiamine, 0.02 milligram of Vitamin E, 0.7 milligram of nicotinic acid, 6 milligrams of vitamin C, still have multiple volatile oil and organic acid.
The yield of honey peach to be improved, the selection getting hold of opportunity, consumption and the fertilizer type of fertilising is crucial, fertilizer In formula rationally, fertilising cost can not only be reduced, and the yield of crop can be lifted.The honey peach of plantation applies fertilizer at present is Based on farm manure, supplemented by carbamide.Farm manure and carbamide can meet the needs that honey peach grows at short notice, but life-time service Soil compaction can be made, soil property is hardening, destroy Soil structure.Meanwhile, the nutrient formula of this kind of fertilizer is unreasonable, can cause fertilizer Waste, and be difficult to promote the stable high yield of honey peach.Application for a patent for invention number discloses " honey peach for 201210244944.4 Special fertilizer ", this fertilizer is fertilizer and chemical fertilizer mixes, and contained nutrient is abundanter, but fertilizer efficiency is shorter, and fertilizer Utilization rate be 20-30%, cause the waste of substantial amounts of nutrient.There is presently no the production finding honey peach dedicated fertilizer The patent documentation of method or report.
Ammonium dihydrogen phosphate, is also called MAP, is a kind of chemicals, a kind of crystal of white, and heating can be resolved into Ammonium metaphosphate.Ammonium dihydrogen phosphate can serve as the fireproof agent of fertilizer and timber, paper, fabric it can also be used to pharmacy and ruminate dynamic Thing feed additive.At present, prepare the monoammonium phosphate double decomposition of ammonium dihydrogen phosphate employing.It is by water, potassium chloride, carbonic acid Hydrogen ammonium feeds intake in proportion, is subsequently adding the phosphoric acid of ormal weight, after being sufficiently stirred for, adjusts pH value, after heating concentrates, cooled crystallization, Product is obtained final product, centrifugation is mother liquid obtained to concentrate the as nitrogenous, multi-elements composite fertilizer such as phosphorus, potassium after centrifugation, drying.This work Skill does not have three waste discharge, and production cost is low compared with neutralisation, crystallization process, extraction, ion exchange.But product quality is not so good as neutralization Method, extraction, ion exchange, only do agricultural, and therefore, the value of its product can be significantly less than other methods.But, crystallization Method, in all have waste liquid to discharge during legal, extraction and ion exchange potassium dihydrogen phosphate preparation, dirt is caused to environment Dye.
The improvement of above technology still has larger problem and difficulty, and its process regulation is bad, then can be in reaction Middle other products of generation, such as ammonium dihydrogen phosphate can generate ammonium metaphosphate in heating, lead to the yield of ammonium dihydrogen phosphate relatively low, with When, also have substantial amounts of waste material discharge in whole production technology it is difficult to solve the zero-emission problem of pollutant;And, phosphorus Acid dihydride ammonium product is also difficult to separate out completely during crystallization separates out, but is in the saturated solution of saturation all the time, Then content is larger in the solution to make ammonium dihydrogen phosphate, if depth crystallization separates out, the ammonium dihydrogen phosphate product obtaining Purity is poor, the quality of impact ammonium dihydrogen phosphate product.
Production method with regard to ammonium dihydrogen phosphate has a lot, and for example, number of patent application is disclosed in 201210194632.7 " method producing industrial phosphoric acid ammonium dihydrogen ", it employed technical scheme comprise that:The first step adds a certain amount of in phosphoric acid by wet process Phosphate ore pulp reaction standing a period of time carries out preliminary desulfurization, after then taking supernatant to add barium salt and sodium salt defluorinate, is passed through ammonia It is neutralized, refilters and obtain ammonium phosphate solution, then by the phosphoric acid hybrid reaction after this ammonium phosphate solution and extraction, condensing crystallizing is just Obtain ammonium dihydrogen phosphate.The biphosphate ammonium concentration that the method is produced is higher, but its production technology is complex, produces into This is higher, and has waste liquid to discharge, to environment.
Content of the invention
In view of this, it is an object of the invention to provide a kind of compound method of honey peach special fertilizer, to solve existing fertilizer In material, nutrient collocation does not meet the demand to nutrient for the honey peach, leads to the fertilizer that honey peach is applied by honey peach Absorbance is relatively low, and some of them element compound remains in soil, changes the structure of soil, pollutes environment.Meanwhile, solve During preparation ammonium dihydrogen phosphate product, biphosphate crystalline ammonium separates out the substantial amounts of ammonium dihydrogen phosphate that not exclusively can cause Waste, biphosphate crystalline ammonium excessively can bring a large amount of impurity into ammonium dihydrogen phosphate product again, so that ammonium dihydrogen phosphate is produced The relatively low technical problem of the purity of product.
The present invention solves above-mentioned technical problem by the following technical programs:
A kind of compound method of honey peach special fertilizer, comprises the following steps:
(1) prepare intermediate:First add phosphoric acid in reactor, and the temperature of phosphoric acid is increased to 100-140 DEG C, so Add phosphoamide to make itself and phosphoric acid carry out synthetic reaction in backward reactor, after reaction 170-190min, temperature is cooled to 15- Crystallize after 30 DEG C, then centrifugation obtains intermediate, described phosphoric acid is (1.2-1.4) with the mol ratio of phosphoamide:1;
(2) prepare ammonium dihydrogen phosphate:The intermediate obtaining in step (1) is sent in reactor, and logical into reactor Enter ammonia, ammonia is (1.8-2) with the mol ratio of intermediate:1, the control response time is 40-60min, and reaction temperature is 15-25 DEG C, and adjust pH value for 8.5-9.5, after reaction terminates, the slip of acquisition is added to circulation crystallization in cooler crystallizer, simultaneously Detection and analysis filtrate, when in filtrate, nitrogen and the ratio of the quality of phosphorus are (7-9):(1.5-2.5), when, stop crystallizing and filtering, will The filter cake arriving obtains ammonium dihydrogen phosphate product after drying;
(3) prepare honey peach special fertilizer:The compound adding potassium in the filtrate filtering ammonium dihydrogen phosphate in step (2) is adjusted Whole nitrogen content is 7-9%, phosphorus content is 1.5-2.5%, potassium content is 12-13%, then adds middle and trace element in filtrate Compound, finally sends into filtrate in baker, for 4 DEG C/min, temperature is increased to 26-30 DEG C with programming rate, filtrate is dried It is 3-4% to moisture, you can prepared honey peach special fertilizer.
Described intermediate is urea phosphate.
In described step (1), by phosphoric acid with phosphoamide with mol ratio for 1.3:1 is added to mixing in reactor, controls reaction Temperature is 120 DEG C, after reaction 180min, temperature is cooled to after 20 DEG C centrifugation again and obtains intermediate.
In described step (2), when intermediate is reacted with ammonia, mixing speed is 200r/min, and the response time is 50min, instead The pH value answering solution is 9.
Described middle trace compound is calcium sulfate, zinc sulfate, magnesium sulfate, Borax and manganese sulfate.
Described intermediate is 1 with the mol ratio of ammonia:1.9.
It is warming up to 28 DEG C, after 40min is dried using programming rate for 4 DEG C/min when being dried in described step (3), adjust water Content is divided to be 3.5%.
In described honey peach special fertilizer nitrogen content be 8%, phosphorus content be 2%, potassium content be 12.5%.
The beneficial effects of the present invention is:
(1) in traditional ammonium dihydrogen phosphate preparation technology, although MAP double decomposition does not have three waste discharge, production cost Low compared with neutralisation, crystallization process, extraction, ion exchange.But product quality is not so good as neutralisation, extraction, ion exchange, Only do agricultural, therefore, the value of its product can be significantly less than other methods.But, crystallization process, in legal, extraction and Waste liquid is all had to discharge, to environment during ion exchange potassium dihydrogen phosphate preparation.The present invention adopt phosphoric acid with After phosphoamide reaction, then reacted with ammonia with reaction product, then so that biphosphate crystalline ammonium is separated out, by detecting in filtrate Nitrogen, the degree to control crystallization for the content of phosphorus composition, filtrate is used for producing honey peach special fertilizer.Ammonium dihydrogen phosphate crystallization degree Less, so the ammonium dihydrogen phosphate purity making is higher.Meanwhile, by filtrate reclaim be used for prepare honey peach special fertilizer so that The production cost of honey peach special fertilizer is relatively low.
(2) by the present invention in that preparing ammonium dihydrogen phosphate, and then in adjustment reactant liquor, nitrogen, the content of phosphorus meet honey peach life Long required ratio, the honey peach special fertilizer produced more fully can be absorbed by honey peach, with minimum fertilizers input, produces Go out most honey peachs, there is significant economic worth.
(3) reactant liquor is separated out a part of ammonium dihydrogen phosphate by the present invention, then again that filtrate is special for preparing honey peach Fertilizer, does not have tail washings to discharge pollution environment, has the significant value of environmental protection.
(4) the honey peach special fertilizer of the present invention is compound state chemical mixed fertilizer, by parameter in production technology, that is, being exactly temperature The control of degree, material concentration and proportioning is so that after phosphoric acid and urea reaction, generate urea phosphate product, urea phosphate product itself There is stronger acidity, and be that the compound state being combined together to form by way of coordinate bond is multiple between phosphoric acid and carbamide Salt, is also fertile as crop in conventional art, and crop the absorbance of this compound state double salt is compared carbamide, ammonium carbonate, All preferably a kind of compound state special fertilizer of the unitary such as ammonium nitrate, binary fertilizer absorbance, however, this compound state double salt is in phosphoric acid In the environment of presence, it may occur that the decomposition polymerisation of complexity of complexity is so that urea phosphate is formed at a temperature of 80-250 DEG C (H2PO4)-(H2NCONH3)+Two ions, (H2NCONH3)+Ion is close with phosphoric acid, and the environment for 80-160 DEG C in temperature Under, formedIntermediate-ion and dihydrogen phosphate, and form coordinate bond between C and O, this Plant intermediate-ion and can chelate formation multielement intermediate-ion with centering element compound, and then can continue to negatively charged with other The compound of lotus or ion form chelate, improve constituent content in double salt, and then can adjust the double salt of this ion presence In nutrient content, meanwhile, this chelate can be hydrolyzed again and by crop, and then can effectively for a long time for crop provide Fertilizer efficiency.
Specific embodiment
Those skilled in the art understands, the present invention will be further described below in conjunction with embodiment for convenience. Embodiment is only the illustration to this invention, is not limitation of the invention, does not make the step illustrating in embodiment It is all prior art, here is not described in detail.
The present invention carries out research and discussion by the mechanism that phosphoric acid and phosphoamide are reacted, and combines prior art literature Solve, phosphoric acid and phosphoamide react generation urea phosphate, its molecular formula is:CO(NH2)2.H3PO4, in the environment of higher temperature, Chemical bond between H and O in phosphoric acid can dialysis, hydrion and carbamide combine to form the ionic state containing positive charge so that phosphorus Sour urea forms the ion double salt that a kind of positive and negative charge phase attracts, its mechanism structural response following expression:CO(NH2)2.H3PO4→ (H2PO4)-.(H2NCONH3)+.
Urea phosphate ion double salt phosphoric acid presence in the environment of, (H therein2NCONH3)+Cation is close with phosphoric acid, shape Become the intermediate-ion of C → O coordinate bond, as (CO5PN2H8)+, and then make in urea phosphate intermediate containing substantial amounts of (H2PO4)-and (CO5PN2H8)+Ion, when adding excessive and appropriate potassium ion, dihydrogen phosphate forms phosphorus with potassium ion Acid dihydride ammonium crystal is precipitated, unnecessary potassium ion and (CO5PN2H8)+Ionic reaction, and displace part NH4 +So that solution In contain (CO5PNH4K)+Double salt ion, and by testing and analyzing and controlling the content of N in solution, P, K element, dry in heating Dry can be prepared by containing N, P, K element compound state composite fertilizer.
The present invention relates to main chemical reactions equation be:
Reaction equation one:
CO(NH2)2+H3PO4→CO(NH2)2.H3PO4
Reaction equation two:
Reaction equation three:
Wherein, the dotted line between carbon atom and oxygen atom represents there is coordinate bond between C atom and O atom.
The production method of the present invention is described further with embodiment below:
Embodiment one
A kind of compound method of honey peach special fertilizer, comprises the steps:
(1) prepare intermediate:First add phosphoric acid in reactor, and the temperature of phosphoric acid is increased to 100 DEG C, Ran Houxiang Add phosphoamide to make itself and phosphoric acid carry out synthetic reaction in reactor, after reaction 190min, temperature be cooled to crystallization after 15 DEG C, Centrifugation obtains intermediate again, and described phosphoric acid is 1.2 with the mol ratio of phosphoamide:1;
(2) prepare ammonium dihydrogen phosphate:The intermediate obtaining in step (1) is sent in reactor, and logical into reactor Enter ammonia, ammonia is 1.8 with the mol ratio of intermediate:1, the control response time is 40min, and mixing speed is 200r/min, instead Answer temperature to be 15 DEG C, and adjust pH value for 8.5, after reaction terminates, the slip of acquisition is added to circulation knot in cooler crystallizer Crystalline substance, tests and analyzes filtrate simultaneously, when in filtrate, nitrogen and the ratio of the quality of phosphorus are 7:When 1.5, stop crystallizing and filtering, by obtain Filter cake obtains ammonium dihydrogen phosphate product after drying;
(3) prepare honey peach special fertilizer:The compound adding potassium in the filtrate filtering ammonium dihydrogen phosphate in step (2) is adjusted Whole nitrogen content is 7%, phosphorus content is 1.5%, potassium content is 12%, then adds middle and trace element compound in filtrate, finally Filtrate is sent in baker, for 4 DEG C/min, temperature is increased to 26 DEG C with programming rate, filtrate is dried to moisture be 4%, you can prepared honey peach special fertilizer.
Embodiment two
(1) prepare intermediate:First add phosphoric acid in reactor, and the temperature of phosphoric acid is increased to 140 DEG C, Ran Houxiang Add phosphoamide to make itself and phosphoric acid carry out synthetic reaction in reactor, after reaction 190min, temperature be cooled to crystallization after 30 DEG C, Centrifugation obtains intermediate again, and described phosphoric acid is 1.4 with the mol ratio of phosphoamide:1;
(2) prepare ammonium dihydrogen phosphate:The intermediate obtaining in step (1) is sent in reactor, and logical into reactor Enter ammonia, ammonia is 2 with the mol ratio of intermediate:1, the control response time is 60min, and mixing speed is 200r/min, reaction Temperature is 25 DEG C, and adjusts pH value for 9.5, after reaction terminates, the slip of acquisition is added to circulation crystallization in cooler crystallizer, Test and analyze filtrate, when in filtrate, nitrogen and the ratio of the quality of phosphorus are 9 simultaneously:When 2.5, stop crystallizing and filtering, by the filter obtaining Cake obtains ammonium dihydrogen phosphate product after drying;
(3) prepare honey peach special fertilizer:The compound adding potassium in the filtrate filtering ammonium dihydrogen phosphate in step (2) is adjusted Whole nitrogen content is 9%, phosphorus content is 2.5%, potassium content is 13%, then adds middle and trace element compound in filtrate, finally Filtrate is sent in baker, for 4 DEG C/min, temperature is increased to 30 DEG C with programming rate, filtrate is dried to moisture be 3%, you can prepared honey peach special fertilizer.
Embodiment three
(1) prepare intermediate:First add phosphoric acid in reactor, and the temperature of phosphoric acid is increased to 120 DEG C, Ran Houxiang Add phosphoamide to make itself and phosphoric acid carry out synthetic reaction in reactor, after reaction 180min, temperature be cooled to crystallization after 20 DEG C, Centrifugation obtains intermediate again, and described phosphoric acid is 13 with the mol ratio of phosphoamide:1;
(2) prepare ammonium dihydrogen phosphate:The intermediate obtaining in step (1) is sent in reactor, and logical into reactor Enter ammonia, ammonia is 1.9 with the mol ratio of intermediate:1, the control response time is 50min, and reaction temperature is 20 DEG C, and adjusts PH value is 9, after reaction terminates, the slip of acquisition is added to circulation crystallization in cooler crystallizer, tests and analyzes filtrate simultaneously, when In filtrate, nitrogen and the ratio of the quality of phosphorus are 8:When 2, stop crystallizing and filtering, obtain ammonium dihydrogen phosphate after the filter cake obtaining is dried and produce Product;
(3) prepare honey peach special fertilizer:The compound adding potassium in the filtrate filtering ammonium dihydrogen phosphate in step (2) is adjusted Whole nitrogen content is 8%, phosphorus content is 2%, potassium content is 12.5%, then adds middle and trace element compound in filtrate, finally Filtrate is sent in baker, for 4 DEG C/min, temperature is increased to 28 DEG C with programming rate, filtrate is dried to moisture be 3.5%, you can prepared honey peach special fertilizer.
With reference to test example to the technique effect of technical solution of the present invention and the ammonium dihydrogen phosphate product that produced Quality is verified:
Test example one
According to HG/T3466-2012《People's Republic of China's chemical industry standard》The detection of chemical reagent ammonium dihydrogen phosphate is real Proved recipe method, detects to the quality of the product that embodiments of the invention one, embodiment two and embodiment three are produced, its Result is as shown in table 1.
Table 1 produces the quality measurements of ammonium dihydrogen phosphate product for embodiments of the invention:
As can be seen from the above table, the various parameters of the ammonium dihydrogen phosphate product that technical scheme is produced exceed Feed grade ammonium dihydrogen phosphate required standard, the purity of product is also higher, has significant progressive.
Test example two
Four mu of kinds of plantation are the honey peach of lake brocade YULU, cultivate honey peach tree according to common planting technology and extremely contain fruit Phase, this four mu of honey peachs are randomly divided into four groups, every group 1 mu, are numbered experimental group one, experimental group two, experimental group three and respectively Contrast groups, in the budding period fertilising 15kg/ mu of honey peach, Post flowering fertilising 12kg/ mu, fruit expanding period fertilising 15kg/ mu, reality Test group one administration is the fertilizer of the embodiment of the present invention one, and what experimental group two was applied is the fertilizer of the embodiment of the present invention two, experiment What group three was applied is the fertilizer of the embodiment of the present invention three, and what contrast groups were applied is the nitrogenous fertilizer that plantation honey peach is commonly used.Result is as follows Table:
Yield (kg)/mu Single average quality (g)
Experimental group one 1276 151
Experimental group two 1290 151
Experimental group three 1321 153
Contrast groups 1211 146
This honey peach special fertilizer be can be seen that by above-mentioned statistical result and can not only improve the yield of honey peach moreover it is possible to improve The quality of honey peach, is suitable to promote the use of.

Claims (8)

1. a kind of compound method of honey peach special fertilizer it is characterised in that:Comprise the following steps:
(1) prepare intermediate:First add phosphoric acid in reactor, and the temperature of phosphoric acid is increased to 100-140 DEG C, Ran Houxiang Add phosphoamide to make itself and phosphoric acid carry out synthetic reaction in reactor, after reaction 170-190min, temperature is cooled to 15-30 DEG C After crystallize, then centrifugation obtains intermediate, and described phosphoric acid is (1.2-1.4) with the mol ratio of phosphoamide:1;
(2) prepare ammonium dihydrogen phosphate:The intermediate obtaining in step (1) is sent in reactor, and is passed through ammonia into reactor Gas, ammonia is (1.8-2) with the mol ratio of intermediate:1, the control response time is 40-60min, and reaction temperature is 15-25 DEG C, And adjust pH value for 8.5-9.5, after reaction terminates, the slip of acquisition is added to circulation crystallization in cooler crystallizer, examines simultaneously Cls analysis filtrate, when in filtrate, nitrogen and the ratio of the quality of phosphorus are (7-9):(1.5-2.5), when, stop crystallizing and filtering, will obtain Filter cake dry after ammonium dihydrogen phosphate product;
(3) prepare honey peach special fertilizer:The compound adjustment nitrogen of potassium is added in the filtrate filtering ammonium dihydrogen phosphate in step (2) Content is 7-9%, phosphorus content is 1.5-2.5%, potassium content is 12-13%, then adds middle and trace element chemical combination in filtrate Thing, finally by filtrate send into baker in, for 4 DEG C/min, temperature is increased to 26-30 DEG C with programming rate, by filtrate dry to Moisture is 3-4%, you can prepared honey peach special fertilizer.
2. honey peach special fertilizer according to claim 1 compound method it is characterised in that:Described intermediate is phosphoric acid Urea.
3. honey peach special fertilizer according to claim 1 compound method it is characterised in that:In described step (1), by phosphorus Acid and phosphoamide are with mol ratio for 1.3:1 is added to mixing in reactor, and controlling reaction temperature is 120 DEG C, after reaction 180min, will Temperature be cooled to 20 DEG C after again centrifugation obtain intermediate.
4. honey peach special fertilizer according to claim 1 compound method it is characterised in that:In described step (2), middle When body is reacted with ammonia, mixing speed is 200r/min, and the response time is 50min, and the pH value of reaction solution is 9.
5. honey peach special fertilizer according to claim 1 compound method it is characterised in that:Described middle trace element Compound is calcium sulfate, zinc sulfate, magnesium sulfate, Borax and manganese sulfate.
6. honey peach special fertilizer according to claim 1 compound method it is characterised in that:Described intermediate and ammonia Mol ratio is 1:1.9.
7. honey peach special fertilizer according to claim 1 compound method it is characterised in that:It is dried in described step (3) Shi Caiyong programming rate is warming up to 28 DEG C, after 40min is dried for 4 DEG C/min, and adjustment moisture is 3.5%.
8. honey peach special fertilizer according to claim 1 compound method it is characterised in that:In described honey peach special fertilizer Nitrogen content is 8%, phosphorus content is 2%, potassium content is 12.5%.
CN201410478298.7A 2014-09-19 2014-09-19 Preparation method of special fertilizer for honey peaches Expired - Fee Related CN104311181B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201410478298.7A CN104311181B (en) 2014-09-19 2014-09-19 Preparation method of special fertilizer for honey peaches

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201410478298.7A CN104311181B (en) 2014-09-19 2014-09-19 Preparation method of special fertilizer for honey peaches

Publications (2)

Publication Number Publication Date
CN104311181A CN104311181A (en) 2015-01-28
CN104311181B true CN104311181B (en) 2017-02-08

Family

ID=52366531

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201410478298.7A Expired - Fee Related CN104311181B (en) 2014-09-19 2014-09-19 Preparation method of special fertilizer for honey peaches

Country Status (1)

Country Link
CN (1) CN104311181B (en)

Family Cites Families (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
BE760491A (en) * 1970-01-09 1971-05-27 Ugine Kuhlmann PROCESS FOR OBTAINING NEW REACTION PRODUCTS OF PHOSPHORIC ACID, UREA AND AMMONIA, AND THEIR APPLICATIONS AS FERTILIZERS
FR2264774B1 (en) * 1974-03-19 1977-06-17 Azote & Prod Chim
US4456463A (en) * 1982-10-15 1984-06-26 Stoller Enterprises, Inc. Ammonia stabilized high analysis liquid fertilizers
CN100534959C (en) * 2005-04-07 2009-09-02 中北大学 Multiple nutrient macromolecule slow release fertilizer and its preparation method and uses
CN101054321A (en) * 2006-04-13 2007-10-17 魏兆峰 Special compound fertilizer for peach
CN102040544A (en) * 2010-11-15 2011-05-04 中化重庆涪陵化工有限公司 Method for continuously producing feed grade urea phosphate by using wet purified phosphoric acid
CN102557774A (en) * 2010-12-13 2012-07-11 吴鲁智 Formula of special formula fertilizer (containing 36% of total nutrients of N, P and K) for peach trees
CN103664273A (en) * 2012-09-02 2014-03-26 句容市农业技术推广中心 Special-purpose fertilizer for peach trees
CN103803518A (en) * 2014-01-24 2014-05-21 贵阳中化开磷化肥有限公司 Method for preparing monopotassium phosphate by using wet-process phosphoric acid
CN103787293A (en) * 2014-01-24 2014-05-14 贵阳中化开磷化肥有限公司 Method for preparing sodium dihydrogen phosphate by utilizing phosphoric acid by wet process
CN103787294A (en) * 2014-01-24 2014-05-14 贵阳中化开磷化肥有限公司 Method of preparing trisodium phosphate by using wet-process phosphoric acid
CN103754853A (en) * 2014-01-24 2014-04-30 贵阳中化开磷化肥有限公司 Method for preparing disodium hydrogen phosphate from wet-process phosphoric acid
CN104016323A (en) * 2014-05-20 2014-09-03 贵阳中化开磷化肥有限公司 Production method for monoammonium phosphate
CN104003909B (en) * 2014-06-06 2016-08-31 云南江磷集团股份有限公司 The preparation method of urea phosphate

Also Published As

Publication number Publication date
CN104311181A (en) 2015-01-28

Similar Documents

Publication Publication Date Title
CN104291903B (en) A kind of method for preparing dendrobium candidum nutrition fertilizer
CN104291306B (en) A kind of compound method of Caulis et Folium Brassicae junceae nutrition fertilizer
CN104311181B (en) Preparation method of special fertilizer for honey peaches
CN103319263B (en) Calcium-containing liquid manure and preparation method thereof
CN104557213A (en) Method for preparing special fertilizer for day-lily buds and producing byproduct sodium dihydrogen phosphate
CN104310332B (en) A kind of method of the preparation of cockscomb special fertilizer
CN104291290B (en) A kind of method preparing the special enhancing fertilizer of ammonium dihydrogen phosphate co-production Bulbus Allii Cepae
CN104291904B (en) A kind of compound method of mung bean special fertilizer
CN104310343B (en) A kind of production method preparing ammonium dihydrogen phosphate by-product Fructus Pruni pseudocerasi special fertilizer
CN104326462B (en) A kind of production method preparing calcium dihydrogen phosphate by-product red bean special fertilizer
CN104261938B (en) Production method for preparation of calcium dihydrogen phosphate and by-production of special fertilizer for cauliflowers
CN104229766B (en) Production method for preparing monocalcium phosphate byproduct used as special fertilizer for chives
CN104310338B (en) Method for preparing ammonium dihydrogen phosphate and preparing special fertilizer for honeysuckle flower as byproduct
CN104291307B (en) Method for preparing monocalcium phosphate and fertilizer for garlic
CN104276551B (en) A kind of production method preparing Secondary ammonium phosphate by-product oat special fertilizer
CN104310354B (en) A kind of compound method of special fertilizer for carrot
CN104310337B (en) A kind of method preparing ammonium dihydrogen phosphate by-product Chinese sorghum special fertilizer
CN106631537A (en) Selenium methionine chelate humic acid additive for paste foliar fertilizer for pear trees
CN104310353B (en) A kind of method preparing sodium dihydrogen phosphate by-product Fructus Rosae Normalis special fertilizer
CN104310339B (en) A kind of method preparing Fructus Mali pumilae nutrition fertilizer
CN104310355B (en) A kind of method preparing potassium dihydrogen phosphate by-product special fertilizer for pitaya
CN104310348B (en) A kind of method preparing potassium dihydrogen phosphate co-production Fertilizer Special for Bamboos
CN105906451A (en) Dragon fruit high-yield fertilizer and manufacturing method thereof
CN104310350B (en) Method for preparing special fertilizer for pears, and preparing potassium dihydrogen phosphate as byproduct
CN104291298B (en) A kind of method preparing Caulis et Folium Brassicae capitatae special enhancing fertilizer

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C41 Transfer of patent application or patent right or utility model
TA01 Transfer of patent application right

Effective date of registration: 20160906

Address after: 550000 Huaxi District, Guizhou, Guiyang

Applicant after: Guizhou University

Applicant after: Phosphorylcholine group limited-liability company is opened in Guizhou

Applicant after: Guizhou Ke Xinhua smelting company limited

Address before: 550000 Huaxi District, Guizhou, Guiyang

Applicant before: Guizhou University

Applicant before: Zhonghuakai Phosphorous Chemical Fertilizer Co., Ltd., Guiyang

Applicant before: Guizhou Ke Xinhua smelting company limited

C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20170208

Termination date: 20200919

CF01 Termination of patent right due to non-payment of annual fee