CN101033158A - Method of manufacturing endoplasm tower type fused mass granulating slow and control release composite fertilizer - Google Patents
Method of manufacturing endoplasm tower type fused mass granulating slow and control release composite fertilizer Download PDFInfo
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- CN101033158A CN101033158A CN 200710097403 CN200710097403A CN101033158A CN 101033158 A CN101033158 A CN 101033158A CN 200710097403 CN200710097403 CN 200710097403 CN 200710097403 A CN200710097403 A CN 200710097403A CN 101033158 A CN101033158 A CN 101033158A
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Abstract
This invention discloses a manufacturing method for an endoplasm-type tower melter prilling slow control released compound manure characterizing in matching a certain proportion of heated P, K and humic acid solid powder in an urea melting solution and adding slow control release reagent to mix them with the solution to composite them to a low temperature co-melt body quickly with a fluid performance under the action of its own temperature and mechanical mixing, then prilling by a prilling tower spraying technology, and sprayed drops in the falling process exchange heat with the rising airflow to get cold quickly and solidified so as to form the endoplasm-type slow control released compound manure, which is to melt a slow-controlled release agent BG-3 with the material completely to distribute them in the manure uniformly and control releasing nutrient according to the needs of plants to increase usability of chemical fertilizers.
Description
Slow, control release composite fertilizer manufacture method technical field that technical field the invention belongs to is specifically related to the manufacture method of a kind of endoplasm tower type fused mass granulating slow, control release composite fertilizer.
Slow, the control release composite fertilizer of the present domestic production of background technology belong to Envelope type mostly, its technology be material after granulation, oven dry, cooling, screening, will delay again, controlled-release material is wrapping to the granulated fertilizer surface.This product membrane wrapping thickness in process of production is difficult to control, and it is consistent with the fertilizer efficiency burst size of coated fertilizer to cause the needed fertilizer amount of the different process of growth of farm crop to be difficult to.
Summary of the invention the purpose of this invention is to provide a kind ofly can control the endoplasm tower type fused mass granulating slow that the fertilizer nutrient discharges, the manufacture method of control release composite fertilizer according to the plant growth needs.
Endoplasm tower type fused mass granulating slow of the present invention; the production technique of control release composite fertilizer is to improve realization on the basis of existing technology; its production principle is to allocate a certain proportion of phosphorus through heating in the urea liquation into; the solid-state pulverulent material of potassium and humic acid; add slow simultaneously; control-released agent (is called for short: BG-3); it is mixed with fused solution; under the temperature of fusion self and mechanical agitation, be combined into low temperature eutectic rapidly with certain flowing property; adopt prilling tower sprinkling pelleting technology to carry out granulation then; carry out heat exchange with the airflow that rises and cool off rapidly and solidifies in prilling tower in the process that falls of spray tear drop, just having formed the endoplasm type delays; control release composite fertilizer.
Slow, the controlled release mechanism of endoplasm tower type fused mass granulating slow, control release composite fertilizer are: BG-3 is made of hydrophilic nano material and biodegradation type material; with the fertilizer adhesive moulding; make both may command diffusions of release of fertilizer nutrient, the also degraded of may command endoplasm section bar material.
Its process technology scheme main points are as follows:
1, is heated to 70-75 ℃ first BG-3 is added in the BG-3 fusion groove, be atomised to urea surface in the urea melting device with volume pump again, with BG-3 and urea fusion together, form the mixture of urea and BG-3, then mixture is beaten to the tempering tank of prilling tower top with pump, the BG-3 add-on is 0.3～0.4% of a weight of urea;
2, the mixture, monoammonium phosphate, Repone K, stopping composition and the humic acid that in tempering tank, add urea and BG-3, its weight proportion is respectively 40～65,10～40,10～40,10～38 and 2～2.5, behind thorough mixing, add 0.7～0.8%BG-3 of above-mentioned material gross weight again in tempering tank, BG-3 is heated to 70-75 ℃ in advance;
3, material behind thorough mixing, adopts tablets press to spray in the prilling tower in tempering tank, and naturally cooling solidify to form particle.
Described monoammonium phosphate phosphoric acid hydrogen calcium replaces, and described Repone K can replace with vitriolate of tartar.
Described stopping composition can be phosphogypsum, calcium powder, ammonium chloride or ammonium sulfate.
The endoplasm tower type fused mass granulating slow that the inventive method is produced, the effect of having a mind to that control release composite fertilizer is slow with the Envelope type that prior art is produced, control release composite fertilizer is compared are:
1, production technique is simple, only needs original production equipment and technology simply transformed to get final product;
2, humic acid has slightly acidic, wetting ability, adsorptivity and complexing, can with urea, phosphorus, middle trace element etc. interacts, growth to plant has tangible stimulating activity, also improve the soil simultaneously, improve the mineral fertilizer utilization ratio, humic acid mixes with urea can also play the effect that suppresses urase and nitrification inhibitor, therefore fertilizer had slow-release function, can change simultaneously the appearance color of product again, owing to add humic acid, can prolong the retention time of nitrogen in soil, and phosphorus played the part slow releasing function, and increased the slow release effect of fertilizer, can also play certain effect of improving the soil simultaneously;
3, can reduce the urea fusing point behind the adding BG-3, reduce the generation of objectionable impurities biuret, and help reducing energy consumption, save cost;
4, the product particle of this explained hereafter is smooth, mellow and full, and it is coffee-like that outward appearance is, and each particle all has shrinkage cavity, has natural anti-false sign, and the nitrogenous proportioning height of this product, nutrient is even, moisture content is low, and prevented from caking is convenient to mechanized application;
5, the product of this explained hereafter dissolution rate in soil is moderate, and the absorption and the utilization of the crop nutrient of being more convenient for have changed the common fertilizer nutrient and discharged the characteristics of too concentrating, and improve fertilizer utilization ratio greatly.
Endoplasm type of the present invention is slow, control release composite fertilizer is with slow, control-released agent BG-3, fully and the material fusion, be evenly distributed among the fertilizer, can control the release of nutrient according to the needs that crop absorbs nutrient, reach and improve the chemical fertilizer utilization ratio, alleviate the purpose of chemical fertilizer soil, river pollution.
Appended drawings is a process flow diagram of the present invention.
Embodiment
The technology point of embodiment 1 production endoplasm tower type fused mass granulating slow, control release composite fertilizer is as follows:
1, adds BG-3 in the urea melting operation, BG-3 fusion groove, volume pump are installed in the batch house, spiral nozzle is installed in the volume pump outlet, and shower nozzle connects pressurized air, earlier BG-3 is heated to 70 ℃, with the urea surface of volume pump in shower nozzle is atomised to the urea melting device, with BG-3 and urea fusion together, its objective is and reduce the urea fusing point, and form the mixture of urea and BG-3, then mixture is beaten to the tempering tank of tower top with pump, the weight proportion of BG-3 and urea is 0.3%;
2, in tempering tank, add the urea of 40 weight parts and the mixture of BG-3, the monoammonium phosphate of 10 weight parts, the Repone K of 40 weight parts, the phosphogypsum stopping composition of 10 weight parts and the humic acid of 2 weight parts, adding total whitewashing amount weight proportion again in tempering tank is 0.8%BG-3, BG-3 is the BG-3 fusion groove of being installed by the prilling tower below, volume pump, the BG-3 dashpot is installed in the prilling tower top, in the dashpot outlet magnetic flow meter is installed, to be heated to 70 ℃ in the BG-3 fusion groove of BG-3 below prilling tower earlier on the technology, beat to the BG-3 dashpot of prilling tower top with volume pump, overflow is to tempering tank then again;
3, above-mentioned material behind thorough mixing, adopts tablets press to spray in the prilling tower in tempering tank, and naturally cooling solidify to form particle.
Embodiment 2 is heated to 75 ℃ according to embodiment 1 with BG-3, and the BG-3 in the technology point 1 and the weight proportion of urea are 0.4%; Urea in the technology point 2 and the mixture of BG-3, monoammonium phosphate, Repone K, phosphogypsum stopping composition and humic acid, its weight proportion is respectively 65,40,10,38 and 2.5, and adding total whitewashing amount weight proportion in tempering tank is 0.7%BG-3.
Embodiment 3 is according to embodiment 1, according to embodiment 1, and urea in the technology point 2 and the mixture of BG-3, monoammonium phosphate, Repone K, phosphogypsum stopping composition and humic acid, its weight proportion is respectively 50,30,20,28 and 2.2.
Embodiment 4 is according to embodiment 1, monoammonium phosphate with secondary calcium phosphate replace, Repone K with vitriolate of tartar replace, the stopping composition calcium powder.
Embodiment 5 is according to embodiment 1, stopping composition ammonium chloride.
Embodiment 6 is according to embodiment 1, stopping composition ammonium sulfate.
Claims (3)
1, the manufacture method of a kind of endoplasm tower type fused mass granulating slow, control release composite fertilizer is characterized in that being undertaken by following technology:
1), is heated to 70-75 ℃ first BG-3 is added in the BG-3 fusion groove, be atomised to urea surface in the urea melting device with volume pump again, with BG-3 and urea fusion together, form the mixture of urea and BG-3, then mixture is beaten to the tempering tank of prilling tower top with pump, the BG-3 add-on is 0.3～0.4% of a weight of urea;
2) mixture, monoammonium phosphate, Repone K, stopping composition and the humic acid that, in tempering tank, add urea and BG-3, its weight proportion is respectively 40～65,10～40,10～40,10～38 and 2～2.5, behind thorough mixing, add 0.7～0.8% BG-3 of above-mentioned material gross weight again in tempering tank, BG-3 is heated to 70-75 ℃ in advance;
3), material behind thorough mixing, adopts tablets press to spray in the prilling tower in tempering tank, naturally cooling solidify to form particle.
2, the manufacture method of endoplasm tower type fused mass granulating slow according to claim 1, control release composite fertilizer is characterized in that said monoammonium phosphate phosphoric acid hydrogen calcium replaces, and said Repone K can replace with vitriolate of tartar.
3, the manufacture method of endoplasm tower type fused mass granulating slow according to claim 1, control release composite fertilizer is characterized in that said stopping composition can be phosphogypsum, calcium powder, ammonium chloride or ammonium sulfate.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
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| CNB2007100974032A CN100467431C (en) | 2007-05-09 | 2007-05-09 | Method of manufacturing endoplasm tower type fused mass granulating slow and control release composite fertilizer |
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| CNB2007100974032A CN100467431C (en) | 2007-05-09 | 2007-05-09 | Method of manufacturing endoplasm tower type fused mass granulating slow and control release composite fertilizer |
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| CN101033158A true CN101033158A (en) | 2007-09-12 |
| CN100467431C CN100467431C (en) | 2009-03-11 |
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Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN102503640A (en) * | 2011-10-29 | 2012-06-20 | 史丹利化肥股份有限公司 | Special functional melt granulated humic acid fertilizer and production method thereof |
| CN102674935A (en) * | 2012-06-04 | 2012-09-19 | 史丹利化肥股份有限公司 | High-efficiency ultra-concentration chlorine-based compound fertilizer and production method thereof |
| CN102795911A (en) * | 2012-08-29 | 2012-11-28 | 史丹利化肥股份有限公司 | Water-soluble humic-acid-contained fertilizer specially for cherries and production method of fertilizer |
| CN103910577A (en) * | 2014-04-04 | 2014-07-09 | 成都新柯力化工科技有限公司 | Slowly-soluble fertilizer and preparation method thereof |
| CN103922854A (en) * | 2014-04-30 | 2014-07-16 | 成都新柯力化工科技有限公司 | Water-retaining slow-soluble fertilizer and preparation method thereof |
| CN104276906A (en) * | 2014-09-17 | 2015-01-14 | 湖北祥云(集团)化工股份有限公司 | Humic acid synergistic slow-release compound fertilizer and preparation method thereof |
| CN111939835A (en) * | 2020-08-21 | 2020-11-17 | 陶娟 | Preparation method of organic compound fertilizer |
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| CN103396242A (en) * | 2013-08-08 | 2013-11-20 | 徐庆海 | Production process and device for organization of inorganic fertilizers |
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2007
- 2007-05-09 CN CNB2007100974032A patent/CN100467431C/en not_active Expired - Fee Related
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102503640A (en) * | 2011-10-29 | 2012-06-20 | 史丹利化肥股份有限公司 | Special functional melt granulated humic acid fertilizer and production method thereof |
| CN102674935A (en) * | 2012-06-04 | 2012-09-19 | 史丹利化肥股份有限公司 | High-efficiency ultra-concentration chlorine-based compound fertilizer and production method thereof |
| CN102674935B (en) * | 2012-06-04 | 2015-02-11 | 史丹利化肥股份有限公司 | High-efficiency ultra-concentration chlorine-based compound fertilizer and production method thereof |
| CN102795911A (en) * | 2012-08-29 | 2012-11-28 | 史丹利化肥股份有限公司 | Water-soluble humic-acid-contained fertilizer specially for cherries and production method of fertilizer |
| CN103910577A (en) * | 2014-04-04 | 2014-07-09 | 成都新柯力化工科技有限公司 | Slowly-soluble fertilizer and preparation method thereof |
| CN103910577B (en) * | 2014-04-04 | 2015-06-10 | 成都新柯力化工科技有限公司 | Slowly-soluble fertilizer and preparation method thereof |
| CN103922854A (en) * | 2014-04-30 | 2014-07-16 | 成都新柯力化工科技有限公司 | Water-retaining slow-soluble fertilizer and preparation method thereof |
| CN104276906A (en) * | 2014-09-17 | 2015-01-14 | 湖北祥云(集团)化工股份有限公司 | Humic acid synergistic slow-release compound fertilizer and preparation method thereof |
| CN104276906B (en) * | 2014-09-17 | 2016-06-22 | 湖北祥云(集团)化工股份有限公司 | A kind of Humic acid synergistic type slow-release compound fertilizer and preparation method thereof |
| CN111939835A (en) * | 2020-08-21 | 2020-11-17 | 陶娟 | Preparation method of organic compound fertilizer |
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| CN100467431C (en) | 2009-03-11 |
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