CN102898221A - Preparation method of nitrogen-phosphorus-potassium compound fertilizer - Google Patents

Preparation method of nitrogen-phosphorus-potassium compound fertilizer Download PDF

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CN102898221A
CN102898221A CN2012104572744A CN201210457274A CN102898221A CN 102898221 A CN102898221 A CN 102898221A CN 2012104572744 A CN2012104572744 A CN 2012104572744A CN 201210457274 A CN201210457274 A CN 201210457274A CN 102898221 A CN102898221 A CN 102898221A
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nitrogen
phosphorus
compound fertilizer
potassium
preparation
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CN102898221B (en
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戴贵芝
刘国良
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Shandong Leguan Crop Nutrition Co.,Ltd.
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Daiwei Agricultural Science & Technology Development LLC
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Abstract

The invention discloses a preparation method of a nitrogen-phosphorus-potassium compound fertilizer. The method comprises the steps of: enabling excessive sulfuric acid to react with potassium chloride in a reaction tank in the condition of warming up to generate potassium bisulfate slurry containing excessive sulfuric acid, mixing the potassium bisulfate slurry containing excessive sulfuric acid with a monoammonium phosphate solution, adding the potassium bisulfate slurry and the monoammonium phosphate solution as well as synthesis ammonia into a reactor together, so as to generate compound fertilizer slurry containing nitrogen-phosphorus-potassium in the condition of warming up, adding the mixed solution of the material containing nitrogen-phosphorus-potassium after reaction and nitric acid as well as water into a granulator, simultaneously adding the synthesis ammonia so as to generate compound fertilizer particles containing the nitrogen-phosphorus-potassium in the condition of warming up, drying, cooling and screening the compound fertilizer particles. The preparation method has the advantages that the potassium chloride is subjected to dechlorination with the excessive sulfuric acid, and biuret is not produced in the low-temperature combination reaction. The fertilizer contains nitrate nitrogen and ammonium nitrogen, and is quick in effect in the early stage and stable in release in the later stage.

Description

A kind of preparation method of nitrogen-phosphorus-potassium compound fertilizer
Technical field
The invention belongs to the manufacture method of chemical fertilizer, definite saying is a kind of preparation method of nitrogen-phosphorus-potassium compound fertilizer.
Background technology
At present the method for manufacturing technology of nitrogen-phosphorus-potassium compound fertilizer is because the temperature of chemical reaction is higher, and produces easily biuret, can cause damage to soil.Therefore, how reducing biuret in the production process produces and just to have become root problem that the nitrogen-phosphorus-potassium compound fertilizer manufacturing need to solve.For this reason, the present inventor has done in earnest research, has proposed goal of the invention of the present invention.
Summary of the invention
Goal of the invention of the present invention puts forward in order to overcome the deficiency that produces biuret in the present nitrogen-phosphorus-potassium compound fertilizer manufacturing.A kind of preparation method of nitrogen-phosphorus-potassium compound fertilizer namely is provided.
Technical solution of the present invention is to realize like this; the preparation method of this nitrogen-phosphorus-potassium compound fertilizer; it is characterized in that the method may further comprise the steps: excess sulfuric acid and Repone K are reacted under Elevated Temperature Conditions in reactive tank; generation contains the sal enixum slip of excess sulfuric acid; the sal enixum slip that will contain excess sulfuric acid mixes with monoammonium phosphate liquid; jointly join sal enixum slip and monoammonium phosphate solution and synthetic ammonia in the reactor; under the condition that heats up, generate the composite fertilizer's slip that contains nitrogen phosphorus potassium; contain the material of nitrogen phosphorus potassium and the mixing solutions of nitric acid and water joins in the tablets press with reacted; add simultaneously synthetic ammonia; under the condition that heats up, form the compound fertilizer granules that contains nitrogen phosphorus potassium, with compound fertilizer granules through super-dry; cooling; screening.
Useful technique effect of the present invention is: Repone K is with excessive sulfuric acid dechlorination, and the low temperature combination reaction does not produce biuret.Contain nitric nitrogen in the fertilizer, early stage is quick-acting, and the later stage discharges stable.
Embodiment
The below provides specific embodiment, and structure of the present invention and use are elaborated.
Embodiment 1, excess sulfuric acid and Repone K are reacted under Elevated Temperature Conditions in reactive tank, generate the sal enixum slip that contains excess sulfuric acid, sulfuric acid with the Elevated Temperature Conditions that Repone K reacts is: in 80~130 ℃ of temperature ranges.Sulfuric acid uses the vitriol oil, and preferably concentration surpasses 90% sulfuric acid.200 kilograms of the sal enixum slips that will contain excess sulfuric acid mix with 80 kilograms of monoammonium phosphate liquid, and the specific gravity control of monoammonium phosphate solution is: 1.10~1.40.Sal enixum slip and monoammonium phosphate solution and 80 kilograms of synthetic ammonia are joined in the reactor jointly, and reactor preferably uses the cross tubular reactor.Generate the composite fertilizer's slip that contains nitrogen phosphorus potassium under the condition that heats up, will contain the material of nitrogen phosphorus potassium and the mixing solutions of nitric acid and water and join in the tablets press, the specific gravity control of aqueous nitric acid is: 1.10~1.55.Add simultaneously synthetic ammonia, under the condition that heats up through granulation time of 1~5 minute.Formation contains the compound fertilizer granules of nitrogen phosphorus potassium, compound fertilizer granules through super-dry, be cooled to and sieve when the material particles surface temperature reaches 50~60 ℃ of temperature.
Embodiment 2,
Excess sulfuric acid and Repone K are reacted under Elevated Temperature Conditions in reactive tank, generate the sal enixum slip that contains excess sulfuric acid, the Elevated Temperature Conditions of sulfuric acid and Repone K reaction is: in 80~130 ℃ of temperature ranges.Sulfuric acid uses the vitriol oil, and preferably concentration surpasses 90% sulfuric acid.240 kilograms of the sal enixum slips that will contain excess sulfuric acid mix with 100 kilograms of monoammonium phosphate liquid, and the specific gravity control of monoammonium phosphate solution is: 1.10~1.40.Sal enixum slip and monoammonium phosphate solution and 100 kilograms of synthetic ammonia are joined in the reactor jointly, and reactor preferably uses the cross tubular reactor.Generate the composite fertilizer's slip that contains nitrogen phosphorus potassium under the condition that heats up, will contain the material of nitrogen phosphorus potassium and the mixing solutions of nitric acid and water and join in the tablets press, the specific gravity control of aqueous nitric acid is: 1.10~1.55.Add simultaneously synthetic ammonia, under the condition that heats up through granulation time of 2~15 minutes.Formation contains the compound fertilizer granules of nitrogen phosphorus potassium, compound fertilizer granules through super-dry, be cooled to and sieve when the material particles surface temperature reaches 50~60 ℃ of temperature.
Excess sulfuric acid and Repone K are reacted under Elevated Temperature Conditions in reactive tank, generate the sal enixum slip that contains excess sulfuric acid, the Elevated Temperature Conditions of sulfuric acid and Repone K reaction is: in 80~130 ℃ of temperature ranges.Sulfuric acid uses the vitriol oil, and preferably concentration surpasses 90% sulfuric acid.300 kilograms of the sal enixum slips that will contain excess sulfuric acid mix with 120 kg monoammonium phosphate liquid, and the specific gravity control of monoammonium phosphate solution is: 1.10~1.40.Sal enixum slip and monoammonium phosphate solution and 120 kg synthetic ammonia are joined in the reactor jointly, and reactor preferably uses the cross tubular reactor.Generate the composite fertilizer's slip that contains nitrogen phosphorus potassium under the condition that heats up, will contain the material of nitrogen phosphorus potassium and the mixing solutions of nitric acid and water and join in the tablets press, the specific gravity control of aqueous nitric acid is: 1.10~1.55.Add simultaneously synthetic ammonia, under the condition that heats up through granulation time of 5~30 minutes.Formation contains the compound fertilizer granules of nitrogen phosphorus potassium, compound fertilizer granules through super-dry, be cooled to and sieve when the material particles surface temperature reaches 50~60 ℃ of temperature.

Claims (9)

1. the preparation method of a nitrogen-phosphorus-potassium compound fertilizer is characterized in that the method may further comprise the steps:
One, excess sulfuric acid and Repone K are reacted under Elevated Temperature Conditions in reactive tank, generate the sal enixum slip that contains excess sulfuric acid,
The sal enixum slip that two, will contain excess sulfuric acid mixes with monoammonium phosphate liquid,
Three, the sal enixum slip in the step 2 and monoammonium phosphate solution and synthetic ammonia are joined in the reactor jointly, under the condition that heats up, generate the composite fertilizer's slip that contains nitrogen phosphorus potassium,
Four, contain the material of nitrogen phosphorus potassium and the mixing solutions of nitric acid and water joins in the tablets press with reacted in the step 3, add simultaneously synthetic ammonia, under the condition that heats up, form the compound fertilizer granules that contains nitrogen phosphorus potassium,
Five, with the compound fertilizer granules in the step 4 through super-dry, cooling, screening.
2. according to the preparation method of a kind of nitrogen-phosphorus-potassium compound fertilizer claimed in claim 1, it is characterized in that the Elevated Temperature Conditions of said sulfuric acid and Repone K reaction is: in 80~130 ℃ of temperature ranges.
3. according to the preparation method of a kind of nitrogen-phosphorus-potassium compound fertilizer claimed in claim 1, it is levied the proportion that is said aqueous nitric acid and is: 1.10~1.55.
4. according to the preparation method of a kind of nitrogen-phosphorus-potassium compound fertilizer claimed in claim 1, it is characterized in that the blending ratio of the said sal enixum that contains excess sulfuric acid, monoammonium phosphate, synthetic ammonia is: sal enixum: monoammonium phosphate: synthetic ammonia=2.0~3.0: 0.8~1.2: 0.8~1.2.
5. according to the preparation method of a kind of nitrogen-phosphorus-potassium compound fertilizer claimed in claim 1, it is characterized in that said drying, be cooled to when the material particles surface temperature reaches 50~60 ℃ of temperature and sieve.
6. according to the preparation method of a kind of nitrogen-phosphorus-potassium compound fertilizer claimed in claim 1, it is characterized in that the proportion of said monoammonium phosphate solution is: 1.10~1.40.
7. according to the preparation method of a kind of nitrogen-phosphorus-potassium compound fertilizer claimed in claim 1, it is characterized in that said reactor is the cross tubular reactor.
8. according to the preparation method of a kind of nitrogen-phosphorus-potassium compound fertilizer claimed in claim 1, it is characterized in that the temperature under the said granulation Elevated Temperature Conditions is the surface temperature of material, temperature range is 60~90 ℃.
, according to the preparation method of a kind of nitrogen-phosphorus-potassium compound fertilizer claimed in claim 1, it is characterized in that the said granulation time is 1~30 minute.
CN201210457274.4A 2012-11-15 2012-11-15 Preparation method of nitrogen-phosphorus-potassium compound fertilizer Active CN102898221B (en)

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Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104725138A (en) * 2015-03-23 2015-06-24 戴威农业科技发展股份有限公司 Carbon matrix compound fertilizer and preparation method thereof
CN104761343A (en) * 2015-03-23 2015-07-08 戴威农业科技发展股份有限公司 Carbon-based composite fertilizer and preparation method thereof
CN105315037A (en) * 2014-08-05 2016-02-10 中化山东肥业有限公司 Process for producing high potassium nitro fertilizer by gunite method
TWI628156B (en) * 2015-07-07 2018-07-01 台灣肥料股份有限公司 Nitro compound fertilizer and preparation method thereof
CN109608247A (en) * 2019-01-22 2019-04-12 盘锦冠桥复合肥科技服务有限公司 A kind of production method of novel ammonification S-based compound fertilizer

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111423270A (en) * 2020-03-25 2020-07-17 贵州省草业研究所 Base fertilizer for pasture planting and preparation method thereof

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101328090A (en) * 2008-04-18 2008-12-24 中国-阿拉伯化肥有限公司 Method for producing nitro-sulfur-based nitrogen and potassium compound fertilizer
CN102010267A (en) * 2010-10-19 2011-04-13 戴威肥业(山东)有限公司 Preparation method of nitrocompound fertilizer

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101328090A (en) * 2008-04-18 2008-12-24 中国-阿拉伯化肥有限公司 Method for producing nitro-sulfur-based nitrogen and potassium compound fertilizer
CN102010267A (en) * 2010-10-19 2011-04-13 戴威肥业(山东)有限公司 Preparation method of nitrocompound fertilizer

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105315037A (en) * 2014-08-05 2016-02-10 中化山东肥业有限公司 Process for producing high potassium nitro fertilizer by gunite method
CN104725138A (en) * 2015-03-23 2015-06-24 戴威农业科技发展股份有限公司 Carbon matrix compound fertilizer and preparation method thereof
CN104761343A (en) * 2015-03-23 2015-07-08 戴威农业科技发展股份有限公司 Carbon-based composite fertilizer and preparation method thereof
TWI628156B (en) * 2015-07-07 2018-07-01 台灣肥料股份有限公司 Nitro compound fertilizer and preparation method thereof
CN109608247A (en) * 2019-01-22 2019-04-12 盘锦冠桥复合肥科技服务有限公司 A kind of production method of novel ammonification S-based compound fertilizer

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Patentee after: Shandong Leguan Crop Nutrition Co.,Ltd.

Address before: 262700 north of 600m Road West of the intersection of Shouyao road and maze Road, sunjiaji street, Shouguang City, Weifang City, Shandong Province

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