CN102285824A - Process for preparing compound fertilizer by utilizing iminodiacetonitrile waste liquid - Google Patents

Process for preparing compound fertilizer by utilizing iminodiacetonitrile waste liquid Download PDF

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Publication number
CN102285824A
CN102285824A CN2010102042852A CN201010204285A CN102285824A CN 102285824 A CN102285824 A CN 102285824A CN 2010102042852 A CN2010102042852 A CN 2010102042852A CN 201010204285 A CN201010204285 A CN 201010204285A CN 102285824 A CN102285824 A CN 102285824A
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CN
China
Prior art keywords
granulating
waste liquid
drying machine
iminodiacetonitrile
raw material
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CN2010102042852A
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Chinese (zh)
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张新
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Individual
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Individual
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Priority to CN2010102042852A priority Critical patent/CN102285824A/en
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A40/00Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
    • Y02A40/10Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
    • Y02A40/20Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses

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  • Fertilizers (AREA)

Abstract

The invention discloses a process for preparing a compound fertilizer by utilizing iminodiacetonitrile waste liquid. The raw material comprises the following components of: ammonium sulfate, potassium sulfate, monoammonium phosphate, calcium hydrophosphate, calcium hydroxide and magnesium sulfate. The preparation method comprises the following steps of: pumping the iminodiacetonitrile waste liquid into an ingredient pool, and adding the calcium hydrophosphate to react; sequentially adding the ammonium sulfate, the potassium sulfate, the monoammonium phosphate, the calcium hydrophosphate and the magnesium sulfate, completely dissolving and stirring, granulating, drying, and feeding back unqualified grains to be re-granulated; and adding a waste water and water gas reutilization process to the process disclosed by the invention. The iminodiacetonitrile waste liquid is taken as the raw material in the process disclosed by the invention, thus the purposes of turning harm into good and protecting environment are realized. Secondary pollution is not generated, no three wastes exhaust and the yield is stable during the whole production.

Description

Utilize the technology of iminodiacetonitrile waste liquid production composite fertilizer
Technical field
The present invention relates to a kind of production technique of composite fertilizer.
Background technology
Have also in China's chemical fertilizers production that nitrogen is many, phosphorus is few, the phenomenon of potassium deficiency.China's fertilizer amount is big, rank first in the world, but its utilization rate of fertilizer is low, in applying the fertilizer in soil, the loss of chemical fertilizer of 40%-60% is arranged approximately, not only causes the huge wasting of resources, and causes ecological environment of soil to worsen.According to statistics, at present China has more than 2,000 ten thousand hectares of arable lands to be polluted, and causes grain about 5,000,000,000 kilograms of the underproduction on year-on-year basis.In China, per kilogram fertilizer increases food crop output not as good as 1/2nd of world standard.Simultaneously, owing to use mineral manure in a large number for a long time, soil with organic matter reduces year by year, thereby destroys the ecotope of soil, causes arable soil to harden, crop production reduction, and quality reduces.For this reason, China agricultural sector has proposed to develop compound organic and inorganic fertilizer, to improve this phenomenon.
According to above-mentioned situation, for adapting to the needs of modern agricultural development, the development of chemical fertilizer must be from ecological agriculture technological standpoint, develop and to make increasing crop yield, make increasing peasant income, improve crop quality, pollution-free, the non-harmful fertilizer variety that can improve the soil again, this is the required of developing modern agriculture, is that benefit future generations offspring's institute wants.
Compound organic and inorganic fertilizer makes crop yield, makes increasing peasant income, can improve crop quality, can improve the soil again, and test shows that effect of increasing production is better than general inorganic compound fertilizer greatly through agricultural section.
Again and, iminodiacetonitrile nitrile waste liquid is the project of the disposal of three wastes, its complicated component; iminodiacetonitrile nitrile waste liquid is the raffinate of production iminodiacetonitrile nitrile; be the dark red thickness aqueous solution, proportion is 1.18-1.25, and directly discharging will cause severe contamination; processing costs is very high; if can adopt special process technology to be recycled with this liquid as nitrogen and organic raw material, then can reach and turn harm into good; turn waste into wealth the purpose of protection environment.
Summary of the invention
In order to overcome the above problem, the invention provides a kind of iminodiacetonitrile waste liquid that utilizes and produce compound fertilizer production technology.
Present technique comprises the usage ratio and the complete processing of its raw material, and the usage ratio of its raw material is: wherein, per 1 cube volume imino-waste liquid diethyl is equipped with following raw material, and its raw material weight ratio is:
Ammonium sulfate: 40%~50%
Vitriolate of tartar: 10%~20%
Monoammonium phosphate: 10%~16%
Secondary calcium phosphate: 60%~70%
Calcium hydroxide: 0.2%~0.4%
Sal epsom: 0.2%~0.4%
Its production technique is:
A. the iminodiacetonitrile waste liquid is pumped into dosing chamber, and add secondary calcium phosphate, reacted 20~40 minutes;
B. add ammonium sulfate, vitriolate of tartar, monoammonium phosphate, secondary calcium phosphate, sal epsom then successively, and through fully dissolving and stirring 30~60 minutes;
C. mixture after being mixed is pumped into the whitewashing pond; Proportion reaches 1.32-1.34
D. when the hot blast that provides in the granulating and drying machine reaches more than 360 ℃, temperature of charge reaches 70 ℃ in the dryer, and the mixture in the whitewashing pond is sprayed into granulating and drying machine, and in granulating and drying machine granulating and carry out warm air drying; Not granulated fine powder or granule are sifted out, and send and return the whitewashing pond;
The grain that e. will be shaped continues dry, and making its water content is 0~5%;
F. after drying, grain is transported to sieve apparatus, sieves out the spherolite that diameter is 2-4.2mm, undesirable grain and fine powder are carried out break process and return granulating and drying machine granulation again;
J. the particle after will screening enters cooler and cools off;
H. after the cooling, the packing warehouse-in is finished the production of composite fertilizer;
I. will collect by the hot blast of granulating and drying machine, and carry out dedusting, and enter washing machine after the dedusting again and carry out scrubbing dust collection, after dust content wherein is less than GB, discharge;
G. the washings that hot blast is washed is through recycling, and when wherein concentration reaches proportion after 1: 16, returns to dosing chamber and utilizes;
The present invention utilizes the iminodiacetonitrile waste liquid as starting material; the iminodiacetonitrile waste liquid is the project of the disposal of three wastes; iminodiacetonitrile component of effluent complexity; directly discharging will cause severe contamination, and processing costs is very high, and this technology is with the raw material of this liquid as nitrogen and organic matter; recycled; reach and turn harm into good, turn waste into wealth, the purpose of protection environment.
This device produces tail gas and contains low amounts of dust, adopts tornado dust collector to remove wherein about 80%, is recovered in the granulating system, and all the other dust of about 20% make tail gas reach emission standard after chimney enters in the atmosphere after the washer washing.
Washing water recycle, reach finite concentration after, add dosing chamber and recycle.There is not other discharge of wastewater.
Do not produce secondary pollution in the whole process of production, three-waste free discharge, and stable yield, outward appearance is even, smooth, glossy.
Embodiment
Be example by the iminodiacetonitrile waste liquid that utilizes 1 cube volume, produce in the following manner:
A. 1 cube volume iminodiacetonitrile waste liquid is pumped into dosing chamber, and add 20~30kg calcium hydroxide, reacted 20~40 minutes;
B. the secondary calcium phosphate, the 20~30kg sal epsom that add 320~380kg ammonium sulfate, 100~150kg vitriolate of tartar, 80~120kg monoammonium phosphate, 100~150kg fertilizer grade then successively, and through fully dissolving and stirring 30~60 minutes;
C. mixture after being mixed is pumped into the whitewashing pond;
D. when the hot blast that provides in the granulating and drying machine reaches 70 ℃, the mixture in the whitewashing pond is sprayed into granulating and drying machine, and in granulating and drying machine granulating and carry out warm air drying; Not granulated fine powder or granule are sifted out, and send and return the whitewashing pond;
The grain that e. will be shaped continues dry, and making its water content is 0~5%;
F. after drying, grain is transported to sieve apparatus, sieves out the spherolite that diameter is 2-4.2mm, undesirable grain and fine powder are carried out break process and return granulating and drying machine granulation again;
J. the particle after will screening enters cooler and cools off;
H. after the cooling, the packing warehouse-in is finished the production of composite fertilizer;
I. will collect by the hot blast of granulating and drying machine, and carry out dedusting, and enter washing machine after the dedusting again and carry out scrubbing dust collection, after dust content wherein is less than GB, discharge;
G. the washings that hot blast is washed is through recycling, and after wherein concentration reaches (1: 16), returns to dosing chamber and utilizes.
Foregoing is invented the description that tries example to this patent, and obviously, patent of the present invention is not limited thereto, and on this basis to the various remodeling that the present invention did, does not all exceed the present invention.

Claims (1)

1. utilize the technology of iminodiacetonitrile waste liquid production composite fertilizer, it is characterized in that, wherein, per 1 cube volume imino-waste liquid diethyl is equipped with following raw material, and its raw material weight ratio is:
Ammonium sulfate: 40%~50%
Vitriolate of tartar: 10%~20%
Monoammonium phosphate: 10%~16%
Secondary calcium phosphate: 60%~70%
Calcium hydroxide: 0.2%~0.4%
Sal epsom: 0.2%~0.4%
Its production technique is:
A. the iminodiacetonitrile waste liquid is pumped into dosing chamber, and add calcium hydroxide, reacted 20~40 minutes;
B. add ammonium sulfate, vitriolate of tartar, monoammonium phosphate, secondary calcium phosphate, sal epsom then successively, and through fully dissolving and stirring 30~60 minutes;
C. mixture after being mixed is pumped into the whitewashing pond;
D. when the hot blast that provides in the granulating and drying machine reaches 360 ℃, the mixture in the whitewashing pond is sprayed into granulating and drying machine, and in granulating and drying machine granulating and carry out warm air drying; Not granulated fine powder or granule are sifted out, and send and return the whitewashing pond;
The grain that e. will be shaped continues dry, and making its water content is 0~5%;
F. after drying, grain is transported to sieve apparatus, sieves out the spherolite that diameter is 2-4.2mm, undesirable grain and fine powder are carried out break process and return granulating and drying machine granulation again;
J. the particle after will screening enters cooler and cools off;
H. after the cooling, the packing warehouse-in is finished the production of composite fertilizer;
I. will collect by the hot blast of granulating and drying machine, and carry out dedusting, and enter washing machine after the dedusting again and carry out scrubbing dust collection, after dust content wherein is less than GB, discharge;
G.. the washings that hot blast is washed is through recycling, and when wherein concentration reaches proportion after 1: 16, returns to dosing chamber and utilizes.
CN2010102042852A 2010-06-21 2010-06-21 Process for preparing compound fertilizer by utilizing iminodiacetonitrile waste liquid Pending CN102285824A (en)

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CN2010102042852A CN102285824A (en) 2010-06-21 2010-06-21 Process for preparing compound fertilizer by utilizing iminodiacetonitrile waste liquid

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CN102285824A true CN102285824A (en) 2011-12-21

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103483031A (en) * 2012-06-14 2014-01-01 川化股份有限公司 Method for preparing amino acid complex by using iminodiacetonitrile waste water

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101391911A (en) * 2008-11-07 2009-03-25 四川天正化工有限责任公司 Method for preparing organic fertilizer by using aminonitrile waste liquid

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101391911A (en) * 2008-11-07 2009-03-25 四川天正化工有限责任公司 Method for preparing organic fertilizer by using aminonitrile waste liquid

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
曹慧等: "亚氨基二乙腈项目环境影响评价关注的环境问题", 《安徽农业科学》 *
汪家铭: "亚氨基二乙腈发展概况及市场前景", 《江苏化工》 *

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103483031A (en) * 2012-06-14 2014-01-01 川化股份有限公司 Method for preparing amino acid complex by using iminodiacetonitrile waste water

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Application publication date: 20111221