CN101921149B - Filler-free synergistic compound fertilizer produced by urine syrup ammonia-acid method and production method thereof - Google Patents

Filler-free synergistic compound fertilizer produced by urine syrup ammonia-acid method and production method thereof Download PDF

Info

Publication number
CN101921149B
CN101921149B CN 201010264697 CN201010264697A CN101921149B CN 101921149 B CN101921149 B CN 101921149B CN 201010264697 CN201010264697 CN 201010264697 CN 201010264697 A CN201010264697 A CN 201010264697A CN 101921149 B CN101921149 B CN 101921149B
Authority
CN
China
Prior art keywords
fertilizer
urine
coating machine
granulation
weight part
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.)
Active
Application number
CN 201010264697
Other languages
Chinese (zh)
Other versions
CN101921149A (en
Inventor
罗斌
谢中平
孙锡林
陈勇
束维正
樊荣琦
郑兴来
刘洪滨
胡长青
李莉
刘晓晖
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.)
CNSG ANHUI HONG SIFANG FERTILIZER INDUSTRY CO., LTD.
Original Assignee
CNSG ANHUI HONG SIFANG 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 CNSG ANHUI HONG SIFANG Co Ltd filed Critical CNSG ANHUI HONG SIFANG Co Ltd
Priority to CN 201010264697 priority Critical patent/CN101921149B/en
Publication of CN101921149A publication Critical patent/CN101921149A/en
Application granted granted Critical
Publication of CN101921149B publication Critical patent/CN101921149B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Landscapes

  • Fertilizers (AREA)

Abstract

The invention discloses a filler-free synergistic compound fertilizer produced by a urine syrup ammonia-acid method to pelletize and a production method thereof. The production method thereof comprises the following steps: selecting raw materials according to the product formulation, and metering, crushing and evenly mixing the raw materials; adopting the urine syrup ammonia-acid revolving drum pelleting process, carrying out first-segment drying, second-segment cooling and coarse and fine screening on the mixture, and then feeding the screened mixture into a coating machine; utilizing the front end of the coating machine to spray fertilizer synergist by a continuous pulverization coating method, utilizing the middle end of the coating machine to spray pasty anti-blocking agent, and utilizing the tail end of the coating machine to add powdery anti-blocking agent; and adequately stirring and packaging to obtain the finished product. The filler-free synergistic compound fertilizer produced by the pelleting process of the urine syrup ammonia-acid method has small investment, simple operation, low production cost, obvious energy conservation effect, beautiful product appearance, good dissolubility and improved nutrient utilization ratio; and after the filler-free synergistic compound fertilizer is applied to crops, production and income are increased.

Description

Synergistic compound fertilizer and production method thereof that urine slurry propylhomoserin method is produced filler-free
Technical field
The present invention relates to technical field of fertilizers, specifically a kind of synergistic compound fertilizer of urinating slurry propylhomoserin method production filler-free.
Background technology
Fertilizer is the grain of plant, is extremely important capital goods in the agricultural sector, is the important leverage of agriculture production development and national food safety.Along with the continuous development of China's chemical fertilizer industry and agriculture production, compound manure has obtained developing rapidly in nearly decades as the more complete fertilizer of a kind of nutritive ingredient.
The production of present domestic compound manure exists the energy consumption height, pollutes problems such as many, that investment is big, composite fertilizer enterprise faces intense market competition, product has competitive edge and seems extremely important, the compound manure that contains weighting agent influences because being subjected to weighting agent, the product instantly-soluble is poor, be dissolved with residue, appearance color instability, raw material characteristics is obvious to the compound fertilizer granulating and the dry influence that contain weighting agent simultaneously, production energy consumption is big, the cost of goods manifactured height can not satisfy market to quality product and cost requirement.
In the face of increasingly serious global grain security problem, the raising fertilizer amount simple in order to increase grain yield must cause the excessive fertilization problem, main harm: the throughput that weakens the crops; The aggravation environmental pollution; Waste a large amount of narrow resources, development Synergistic type fertilizer can improve utilization rate of fertilizer, reduces rate of fertilizer application, alleviates environmental pollution, alleviates China's energy scarcity.
In order to improve composite fertilizer's quality, reduce production costs, improve utilization rate of fertilizer, improve product specification and the market competitiveness energetically, quality, production and application problem at the compound manure existence that contains weighting agent, comprehensive composite fertilizer produces and uses urine basic spray granulating, propylhomoserin granulation and the coating method coating process that atomizes continuously, the invention provides a kind of urinate synergistic compound fertilizer product innovation that the granulation of slurry propylhomoserin method produces filler-free and and manufacture method, agriculture production is of great significance, composite fertilizer's industrial development is also had very important effect.
Summary of the invention
The invention provides a kind of synergistic compound fertilizer and manufacture method thereof that filler-free is produced in the granulation of slurry propylhomoserin method of urinating, urine slurry propylhomoserin method technology is adopted in granulation, add fertilizer synergist and adopt atomizing coating method continuously, can accomplish in the production that granulation is effective, production efficiency is high, energy consumption is low, low cost of manufacture, it is pure white mellow and full smooth to make product appearance, solvability is good, no residue, the increasing both production and income of crop applying energy improves quality of agricultural product, strengthen crop anti-adversity, improve the soil.
Technical scheme of the present invention is:
A kind of synergistic compound fertilizer of urinating slurry propylhomoserin method production filler-free is characterized in that: from the raw material of following weight part:
Urea 5-40 weight part, ammonium chloride 6-20 weight part, ammonium sulfate 2-42 weight part, monoammonium phosphate 28-68 weight part, Repone K 12-53 weight part, vitriolate of tartar 10-58 weight part, Repone K fertiliser containing magnesium 7-35 weight part, potash magnesium sulphate fertilizer 5-45 weight part,
Select two or more raw material mix mixture, spray urine slurry 50-280 kilogram, liquefied ammonia 16-32 kilogram, dilute sulphuric acid 16-40 kilogram by mixture per ton during granulation, granulation work in-process spraying fertilizer synergist 3-6 kilogram per ton, paste anti-hard caking agent 0.8-1.2 kilogram, powdered anti-caking agent 2.0-3.0 kilogram during coating.
Described urine slurry propylhomoserin method is produced the synergistic compound fertilizer of filler-free, it is characterized in that: described urea contains N46.2%, ammonium chloride and contains that N23.6%, ammonium sulfate contain N20.5%, monoammonium phosphate contains N10%-11%, contains P 2O 543%-48%, Repone K contain K 2O60%, vitriolate of tartar contain K 2O50%, Repone K fertiliser containing magnesium contain K 2O22%, potash magnesium sulphate fertilizer contain K 2O22%.
Described urine slurry propylhomoserin method is produced the synergistic compound fertilizer of filler-free, it is characterized in that: described urine slurry is 95% urea soln for mass percentage concentration, and described dilute sulphuric acid mass percentage concentration is 50%-60%.
Described urine slurry propylhomoserin method is produced the synergistic compound fertilizer of filler-free, and it is characterized in that: described fertilizer synergist is poly aspartic acid.
Described urine slurry propylhomoserin method is produced the synergistic compound fertilizer of filler-free, it is characterized in that: described paste anti-hard caking agent is made up of machinery oil, stearylamine, distearyl dimethyl ammonium chloride, and the weight proportion of each component is machinery oil: stearylamine: distearyl dimethyl ammonium chloride=10: (2.5-5.0): (0.6-2.5).
Described urine slurry propylhomoserin method is produced the synergistic compound fertilizer of filler-free, it is characterized in that: described powdered anti-caking agent is made up of diatomite, attapulgite, sodium lauryl sulphate, polyacrylamide, and the weight proportion of each component is diatomite: attapulgite: sodium lauryl sulphate: polyacrylamide=10: (6-10): (0.4-1.6): (0.2-1.4).
The production method that described urine slurry propylhomoserin method is produced the synergistic compound fertilizer of filler-free is characterized in that: may further comprise the steps:
(1) material pulverize, mixing: take by weighing urea, ammonium chloride, ammonium sulfate, monoammonium phosphate, Repone K, vitriolate of tartar, Repone K fertiliser containing magnesium, potash magnesium sulphate fertilizer by formula rate, broken and mix after send in the rotary drum granulator;
(2) urine slurry propylhomoserin method granulation: in tablets press, the granulation material is sprayed an amount of urine slurry earlier, again liquefied ammonia and dilute sulphuric acid are sprayed the granulation material behind tubular reactor;
(4) dry, cooling, screening: the particle after the granulation is carried out one section drying, two sections coolings and thickness screening, and the qualified particle of screening back granularity enters in the special coating machine, and macrobead returns fragmentation, and particulate returns granulation;
(5) synergistic agent and anti-hard caking agent coating: fertilizer synergist is delivered to the coating machine front end evenly sprays through air atomizing, coating machine middle-end atomizing spraying paste anti-hard caking agent, the terminal powdered anti-caking agent that adds of coating machine;
(6), packing: the fertilizer that coating is good mixes, packs through abundant, gets finished product.
Advantage of the present invention is as follows:
1, the present invention only needs to increase tubular reactor, tail gas generated by granulation washing device and propylhomoserin measuring apparatus at crude urine base spray granulating compound fertilizer facility and gets final product, and less investment, and is easy to operate;
2, urine slurry propylhomoserin method rotary drum prilling process is adopted in granulation, need not to increase granulation weighting agent and amendment, reduces product batching cost;
3, urine slurry propylhomoserin method rotary drum prilling process is adopted in granulation, and the chemical reaction that takes full advantage of stock yard improves prilling temperature, improves material characteristic, makes it to reach the granulation operating mode of the best, and the material returning charge improves plant capacity than reducing, and reduces production costs;
4, urine slurry propylhomoserin method rotary drum prilling process is adopted in granulation, does not use steam, water granulation, and the propylhomoserin reaction produces a large amount of heats, reduces material moisture, alleviates drying load, and coal consumption, power consumption reduce significantly, and energy-saving effect is remarkable;
5, add fertilizer synergist and adopt atomizing coating method continuously, the mode of filming adopts the continuous atomizing of special nozzle to film, and has improved the spraying homogeneity, effectively reduces the fertilizer synergist consumption;
6, fertilizer synergist and N-P-K content can be regulated as required in the prepared product;
7, prepared product particle is pure white, smooth, mellow and full, the intensity height, and moisture is low, does not lump, and not efflorescence is dissolved no residue, and can also be improved plant recovery of nutrient, and the increasing both production and income of crop applying energy improves quality of agricultural product, strengthens crop anti-adversity, improves the soil.
Description of drawings
Fig. 1 is process flow sheet of the present invention.
Embodiment
Embodiment 1
Total nutrient (N+P 2O 5+ K 2O) 〉=51%, specification is the synergistic compound fertilizer of the chloride type filler-free of 17-17-17, and concrete technological operation step is as follows:
(1) measures 33.5 kilograms of Repone K respectively and (contain K 2O-60%), 42.1 kilograms of monoammonium phosphates (contain N-10%, contain P 2O 5-48%), 13.0 kilograms of ammonium chlorides (containing N-23.6%), 11.4 urea (containing N-46.2%), with the above-mentioned raw materials fragmentation, mix, get mixture and send in the rotary drum granulator;
(2) mixture per ton sprays 159.1 kilograms of urine slurries, 26.1 kilograms of liquefied ammonia, 22.7 kilograms of dilute sulphuric acids in the tablets press;
(3) adopt one section drying, two sections coolings and thickness screening, the qualified particle of screening back granularity enters in the special coating machine, and macrobead returns fragmentation, and particulate returns granulation;
(4) to the qualified particle of screening back granularity per ton, 3 kilograms of fertilizer synergists are delivered to the coating machine front end evenly to spray through air atomizing, 1.1 kilograms of coating machine middle-end atomizing spraying paste anti-hard caking agents, the weight proportion of each component of paste anti-hard caking agent is machinery oil: stearylamine: distearyl dimethyl ammonium chloride=10: 2.6: 1.0, terminal 2.8 kilograms of the powdered anti-caking agents that add of coating machine, the weight proportion of each component of powdered anti-caking agent is diatomite: attapulgite: sodium lauryl sulphate: polyacrylamide=10: 9: 0.8: 0.4;
(5) the abundant mixing of the fertilizer that coating is good, packing get finished product.
Embodiment 2
Total nutrient (N+P 2O 5+ K 2O) 〉=48%, specification is the synergistic compound fertilizer of the chloride type filler-free of 25-13-10, and concrete technological operation step is as follows:
(1) measures 21.1 kilograms of Repone K respectively and (contain K 2O-60%), 37.4 kilograms of monoammonium phosphates (contain N-11%, contain P 2O 5-44%), 10.2 kilograms of ammonium chlorides (containing N-23.6%), 31.3 kilograms of urea (containing N-46.2%), with the above-mentioned raw materials fragmentation, mix, get mixture, send in the rotary drum granulator;
(2) mixture per ton sprays 217.6 kilograms of urine slurries, 28.5 kilograms of liquefied ammonia, 27.3 kilograms of dilute sulphuric acids in the tablets press;
(3) adopt one section drying, two sections coolings and thickness screening, the qualified particle of screening back granularity enters in the special coating machine, and macrobead returns fragmentation, and particulate returns granulation;
(4) to the qualified particle of screening back granularity per ton, 4 kilograms of fertilizer synergists are delivered to the coating machine front end evenly to spray through air atomizing, 1.2 kilograms of coating machine middle-end atomizing spraying paste anti-hard caking agents, the weight proportion of each component of paste anti-hard caking agent is machinery oil: stearylamine: distearyl dimethyl ammonium chloride=10: 4.2: 1.4, terminal 2.6 kilograms of the powdered anti-caking agents that add of coating machine, the weight proportion of each component of powdered anti-caking agent is diatomite: attapulgite: sodium lauryl sulphate: polyacrylamide=10: 6.7: 0.5: 0.5;
(5) the abundant mixing of the fertilizer that coating is good, packing get finished product.
Embodiment 3
Total nutrient (N+P 2O 5+ K 2O) 〉=45%, specification is the synergistic compound fertilizer of 15-15-15 potassium sulfate type filler-free, and concrete technological operation step is as follows:
(1) measures 36.2 kilograms of vitriolate of tartar respectively and (contain K 2O-50%), 41.5 kilograms of monoammonium phosphates (contain N-11%, contain P 2O 5-44%), 22.3 kilograms of ammonium sulfate (containing N-20.5%), with the above-mentioned raw materials fragmentation, mix, get mixture, send in the rotary drum granulator;
(2) mixture per ton sprays 191.5 kilograms of urine slurries, 27.7 kilograms of liquefied ammonia, 23.4 kilograms of dilute sulphuric acids in the tablets press;
(3) adopt one section drying, two sections coolings and thickness screening, the qualified particle of screening back granularity enters in the special coating machine, and macrobead returns fragmentation, and particulate returns granulation;
(4), to the qualified particle of screening back granularity per ton, 5 kilograms of fertilizer synergists are delivered to the coating machine front end evenly to spray through air atomizing, 0.9 kilogram of coating machine middle-end atomizing spraying paste anti-hard caking agent, the weight proportion of each component of paste anti-hard caking agent is machinery oil: stearylamine: distearyl dimethyl ammonium chloride=10: 3.0: 1.2, terminal 2.5 kilograms of the powdered anti-caking agents that add of coating machine; The weight proportion of each component of powdered anti-caking agent is diatomite: attapulgite: sodium lauryl sulphate: polyacrylamide=10: 8.8: 0.5: 1.0;
(5), the abundant mixing of fertilizer, packing that coating is good, get finished product.
Embodiment 4
Total nutrient (N+P 2O 5+ K 2O) 〉=48%, specification is the synergistic compound fertilizer of 14-20-14 potassium sulfate type filler-free, and concrete technological operation step is as follows:
(1) measures 30.9 kilograms of vitriolate of tartar respectively and (contain K 2O-50%), 11.1 kilograms of potash magnesium sulphate fertilizers (contain K 2O-22%), 58.0 kilograms of monoammonium phosphates (contain N-11%, contain P 2O 5-44%), with the above-mentioned raw materials fragmentation, mix, gets mixture, send in the rotary drum granulator;
(2) mixture per ton sprays 246.9 kilograms of urine slurries, 30.9 kilograms of liquefied ammonia, 24.7 kilograms of dilute sulphuric acids in the tablets press;
(3) adopt one section drying, two sections coolings and thickness screening, the qualified particle of screening back granularity enters in the special coating machine, and macrobead returns fragmentation, and particulate returns granulation;
(4) to the qualified particle of screening back granularity per ton, 4 kilograms of fertilizer synergists are delivered to the coating machine front end evenly to spray through air atomizing, 1.1 kilograms of coating machine middle-end atomizing spraying paste anti-hard caking agents, the weight proportion of each component of paste anti-hard caking agent is machinery oil: stearylamine: distearyl dimethyl ammonium chloride=10: 4.8: 1.8, terminal 2.6 kilograms of the powdered anti-caking agents that add of coating machine, the weight proportion of each component of powdered anti-caking agent is diatomite: attapulgite: sodium lauryl sulphate: polyacrylamide=10: 9.5: 0.7: 0.4;
(5) the abundant mixing of the fertilizer that coating is good, packing get finished product.

Claims (2)

1. urinate the synergistic compound fertilizer that slurry propylhomoserin method is produced filler-free for one kind, it is characterized in that: from the raw material of following weight part:
Urea 5-40 weight part, ammonium chloride 6-20 weight part, ammonium sulfate 2-42 weight part, monoammonium phosphate 28-68 weight part, Repone K 12-53 weight part, vitriolate of tartar 10-58 weight part, Repone K fertiliser containing magnesium 7-35 weight part, potash magnesium sulphate fertilizer 5-45 weight part,
Select two or more raw material mix mixture, spray urine slurry 50-280 kilogram, liquefied ammonia 16-32 kilogram, dilute sulphuric acid 16-40 kilogram by mixture per ton during granulation, granulation work in-process spraying fertilizer synergist 3-6 kilogram per ton, paste anti-hard caking agent 0.8-1.2 kilogram, powdered anti-caking agent 2.0-3.0 kilogram during coating; Described urea contains N46.2%, ammonium chloride and contains that N23.6%, ammonium sulfate contain N20.5%, monoammonium phosphate contains N10%-11%, contains P 2O 543%-48%, Repone K contain K 2O60%, vitriolate of tartar contain K 2O50%, Repone K fertiliser containing magnesium contain K 2O22%, potash magnesium sulphate fertilizer contain K 2O22%; Described urine slurry is 95% urea soln for mass percentage concentration; Described dilute sulphuric acid mass percentage concentration is 50%-60%; Described fertilizer synergist is poly aspartic acid; Described paste anti-hard caking agent is made up of machinery oil, stearylamine, distearyl dimethyl ammonium chloride, and the weight proportion of each component is machinery oil: stearylamine: distearyl dimethyl ammonium chloride=10: (2.5-5.0): (0.6-2.5); Described powdered anti-caking agent is made up of diatomite, attapulgite, sodium lauryl sulphate, polyacrylamide, and the weight proportion of each component is diatomite: attapulgite: sodium lauryl sulphate: polyacrylamide=10: (6-10): (0.4-1.6): (0.2-1.4).
2. the described urine of claim 1 is starched the production method that the propylhomoserin method is produced the synergistic compound fertilizer of filler-free, it is characterized in that: may further comprise the steps:
(1) material pulverize, mixing: take by weighing urea, ammonium chloride, ammonium sulfate, monoammonium phosphate, Repone K, vitriolate of tartar, Repone K fertiliser containing magnesium, potash magnesium sulphate fertilizer by formula rate, broken and mix after send in the rotary drum granulator;
(2) urine slurry propylhomoserin method granulation: in tablets press, the granulation material is sprayed an amount of urine slurry earlier, again liquefied ammonia and dilute sulphuric acid are sprayed the granulation material behind tubular reactor;
(4) dry, cooling, screening: the particle after the granulation is carried out one section drying, two sections coolings and thickness screening, and the qualified particle of screening back granularity enters in the special coating machine, and macrobead returns fragmentation, and particulate returns granulation;
(5) synergistic agent and anti-hard caking agent coating; Fertilizer synergist is delivered to the coating machine front end evenly sprays through air atomizing, coating machine middle-end atomizing spraying paste anti-hard caking agent, the terminal powdered anti-caking agent that adds of coating machine;
(6), packing: the fertilizer that coating is good mixes, packs through abundant, gets finished product.
CN 201010264697 2010-08-24 2010-08-24 Filler-free synergistic compound fertilizer produced by urine syrup ammonia-acid method and production method thereof Active CN101921149B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 201010264697 CN101921149B (en) 2010-08-24 2010-08-24 Filler-free synergistic compound fertilizer produced by urine syrup ammonia-acid method and production method thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 201010264697 CN101921149B (en) 2010-08-24 2010-08-24 Filler-free synergistic compound fertilizer produced by urine syrup ammonia-acid method and production method thereof

Publications (2)

Publication Number Publication Date
CN101921149A CN101921149A (en) 2010-12-22
CN101921149B true CN101921149B (en) 2013-08-07

Family

ID=43336395

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 201010264697 Active CN101921149B (en) 2010-08-24 2010-08-24 Filler-free synergistic compound fertilizer produced by urine syrup ammonia-acid method and production method thereof

Country Status (1)

Country Link
CN (1) CN101921149B (en)

Families Citing this family (20)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102173937A (en) * 2011-01-27 2011-09-07 中盐安徽红四方股份有限公司 Composite nitrogen fertilizer and production method thereof
CN102241545A (en) * 2011-03-09 2011-11-16 山东远东国际生物化工股份有限公司 Process for producing polypeptide composite fertilizer by using ammonia-acid method
CN102153409A (en) * 2011-03-15 2011-08-17 长江师范学院 Pickle prolonged-effect-time compound fertilizer and preparation method thereof
CN102336599B (en) * 2011-06-23 2013-11-06 安徽省司尔特肥业股份有限公司 Technological method for producing high-density composite fertilizer by ammonia-acid method
CN102424616B (en) * 2011-09-09 2013-09-04 广东拉多美化肥有限公司 Full water-soluble urea-based composite fertilizer and preparation method thereof
CN102515921A (en) * 2011-12-26 2012-06-27 河南心连心化肥有限公司 Filler-free compound fertilizer
CN102617243A (en) * 2012-04-16 2012-08-01 瓮福(集团)有限责任公司 Production formula of granular chloramine nitrogen fertilizer and preparation method thereof
CN102674985A (en) * 2012-06-15 2012-09-19 云南天和地农业营养科技有限责任公司 Novel agricultural compound fertilizer
CN103044144B (en) * 2013-01-05 2014-05-07 杨彪 Preparation method of organic chelate fertilizer
CN103011941B (en) * 2013-01-05 2014-03-05 杨彪 Production method of compound fertilizer
CN103664369B (en) * 2013-12-05 2015-12-30 中盐安徽红四方股份有限公司 A kind of synergy loss controlling fertilizer and preparation method thereof
CN103787781A (en) * 2014-02-27 2014-05-14 王东 High-efficiency anti-seepage fertilizer and preparation method thereof
CN104649826A (en) * 2015-02-09 2015-05-27 山西大学 Method for preparing anti-caking slow-release fertilizer from magnesium slag
CN104692958A (en) * 2015-03-17 2015-06-10 河北盛龙农业科技有限公司 Corn compound fertilizer and preparation method thereof
CN105948994A (en) * 2016-05-16 2016-09-21 安徽省龙晨肥业有限公司 Urea-based compound fertilizer containing high-activity minerals
CN107151186A (en) * 2017-07-12 2017-09-12 烟台市昊星晟信息技术有限公司 A kind of method for preventing fertilizer agglomeration
CN112028697A (en) * 2020-08-03 2020-12-04 安徽省旌一农业旅游发展有限公司 Process for preventing and controlling caking of compound fertilizer
CN114230417A (en) * 2021-12-20 2022-03-25 安徽辉隆集团五禾生态肥业有限公司 High-sulfur-based compound fertilizer, processing technology and processing equipment thereof
CN114181021A (en) * 2021-12-23 2022-03-15 安徽辉隆集团五禾生态肥业有限公司 Potassium fulvate type compound fertilizer containing medium and trace metal elements and preparation process thereof
CN115259955A (en) * 2022-08-05 2022-11-01 安徽辉隆集团五禾生态肥业有限公司 Potassium sulfate type compound fertilizer, preparation method and special extrusion screening pulverizer

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101265128A (en) * 2008-04-16 2008-09-17 江苏华昌化工股份有限公司 Method for preparing particle nitrogen fertilizer
CN101684051A (en) * 2008-09-27 2010-03-31 河南财鑫实业化工有限责任公司 Production process of organic-inorganic compound fertilizer
CN101792354A (en) * 2010-04-07 2010-08-04 中盐安徽红四方股份有限公司 Color drought-resistance water-retention sustained-release compound fertilizer and method for producing same

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101265128A (en) * 2008-04-16 2008-09-17 江苏华昌化工股份有限公司 Method for preparing particle nitrogen fertilizer
CN101684051A (en) * 2008-09-27 2010-03-31 河南财鑫实业化工有限责任公司 Production process of organic-inorganic compound fertilizer
CN101792354A (en) * 2010-04-07 2010-08-04 中盐安徽红四方股份有限公司 Color drought-resistance water-retention sustained-release compound fertilizer and method for producing same

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
"尿素熔融喷浆造粒工艺生产复合肥";许洪兴;《磷肥与复肥》;20030920;第18卷(第5期);第45-47页 *
许洪兴."尿素熔融喷浆造粒工艺生产复合肥".《磷肥与复肥》.2003,第18卷(第5期),第45-47页.

Also Published As

Publication number Publication date
CN101921149A (en) 2010-12-22

Similar Documents

Publication Publication Date Title
CN101921149B (en) Filler-free synergistic compound fertilizer produced by urine syrup ammonia-acid method and production method thereof
CN101717289B (en) Method for producing Nitrogen-Phosphorus-Potassium compound fertilizer by ammonia and acid tubular reactor
CN101792354B (en) Color drought-resistance water-retention sustained-release compound fertilizer and method for producing same
CN102093113B (en) Production method of readily available and controlled release composite fertilizer containing three nitrogen elements
CN101570455B (en) Method for preparing particle ammonium sulfate product by organic-inorganic binder
CN102040427A (en) Method for producing chlorine-based high phosphorus compound fertilizer by ammoniation method
CN102153392B (en) Production method of novel slow release urea-formaldehyde compound fertilizer
CN101575222B (en) Method for producing ammonium sulphate grain products by using inorganic caking agent
CN102173937A (en) Composite nitrogen fertilizer and production method thereof
CN102276362B (en) High-concentration compound fertilizer
CN102241545A (en) Process for producing polypeptide composite fertilizer by using ammonia-acid method
CN106365778A (en) High-strength compound fertilizer and preparation method of same
CN101983957A (en) Method for producing nitrogen-fixing potassium slow-release compound fertilizer with mesh inner membrane by using ammonia-acid method
CN101638347B (en) Fertilizer special for peanuts and preparation method thereof
CN104418637A (en) Colorful slowly-releasing compound fertilizer and preparation method thereof
CN103058751B (en) Preparation method for special slow-release long-acting compound fertilizer for corn
CN202139174U (en) Equipment for producing high-concentration compound fertilizers
CN109485506A (en) Containing there are many wheat special complex fertilizers of phosphorus element and preparation method thereof
CN104355772A (en) Preparation method and preparation device of compound fertilizer
CN105646106A (en) Humic acid type functionality organic-inorganic compound fertilizer and preparing method thereof
CN104591894A (en) Preparation method of controlled release type fertilizer
CN103086804A (en) Stable lumbrukinase granulated fertilizer and preparation method thereof
CN101638343B (en) Special corn fertilizer and preparation method thereof
CN101337847B (en) Method for preparing high-nitrogen sulfonyl azophoska compound fertilizer
CN105110859A (en) Multi-element high-phosphorus compound fertilizer and preparation method thereof

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
C41 Transfer of patent application or patent right or utility model
TR01 Transfer of patent right

Effective date of registration: 20150625

Address after: 231602 north side of No. five road, circular economy demonstration park, Anhui, Hefei

Patentee after: CNSG ANHUI HONG SIFANG FERTILIZER INDUSTRY CO., LTD.

Address before: 230022 No. 12 Qi Road, Hefei, Anhui

Patentee before: CNSG Anhui Hong Sifang Co., Ltd.

PE01 Entry into force of the registration of the contract for pledge of patent right

Denomination of invention: Filler-free synergistic compound fertilizer produced by urine syrup ammonia-acid method and production method thereof

Effective date of registration: 20180413

Granted publication date: 20130807

Pledgee: Huizhou merchant bank, Hefei Taihu Road Branch

Pledgor: CNSG ANHUI HONG SIFANG FERTILIZER INDUSTRY CO., LTD.

Registration number: 2018340000108

PE01 Entry into force of the registration of the contract for pledge of patent right
PC01 Cancellation of the registration of the contract for pledge of patent right

Date of cancellation: 20180625

Granted publication date: 20130807

Pledgee: Huizhou merchant bank, Hefei Taihu Road Branch

Pledgor: CNSG ANHUI HONG SIFANG FERTILIZER INDUSTRY CO., LTD.

Registration number: 2018340000108

PC01 Cancellation of the registration of the contract for pledge of patent right