CN103588584A - Adhesive used for producing granular ammonium sulfate - Google Patents
Adhesive used for producing granular ammonium sulfate Download PDFInfo
- Publication number
- CN103588584A CN103588584A CN201310614637.5A CN201310614637A CN103588584A CN 103588584 A CN103588584 A CN 103588584A CN 201310614637 A CN201310614637 A CN 201310614637A CN 103588584 A CN103588584 A CN 103588584A
- Authority
- CN
- China
- Prior art keywords
- ammonium sulfate
- tackiness agent
- granular ammonium
- calcium carbonate
- product
- 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.)
- Pending
Links
Landscapes
- Fertilizers (AREA)
Abstract
The invention discloses an adhesive used for producing granular ammonium sulfate, the adhesive comprises the following components: pearl alum, calcium carbonate and monoammonium phosphate; the adhesive comprises the following components by mass percentage: 10-15% of calcium carbonate, 70-75% of pearl alum and 5-10% of monoammonium phosphate; the above adhesive is used for producing the granular ammonium sulfate; the provided method comprises the following advantages: 1)under the prerequisite that appearance and quality of the product are ensured, the nitrogen content of the granular ammonium sulfate product produced by a novel adhesive can ensure more than 19.5%, the product cost for per ton is decreased by 100 yuan, the economic benefit is obvious; and 2) the apparatus and the flow employed by the production method are current mature flow, change is less, and the investment risk is reduced.
Description
?
Technical field
The present invention relates to adhesive field, be specifically related to a kind of tackiness agent for the production of granular ammonium sulfate.
Background technology
Ammonium sulfate is the industrial raw material that is widely used in the industries such as chemical industry, dyeing and weaving, medicine, leather.In use there are many shortcomings in crystal ammonium sulfate as fertilizer sources: easily caking, poor fluidity, be difficult to realize mechanized application, and in application, easily form dust and run off.Granular ammonium sulfate good physical performance, does not play dirt, long-term storage prevented from caking, good fluidity during handling, easy spreading during fertilising, and can realize aircraft and broadcast fertilizer, reduce the loss, also can play slow releasing function simultaneously, the utilization ratio that improves fertilizer, is more and more subject to the especially welcome of foreign market of market.
Subordinate's Wengfu phosphate fertilizer plant of Wengfu Group Co., Ltd. and developed granular ammonium sulfate granulation novel process for 2009, has filled up a blank of domestic correlation technique.Granular ammonium sulfate product Han Dan Liang≤19.5 that Wengfu group produces for a long time, ton products with adhesive agent cost is about 150 yuan, effort through Wengfu phosphate fertilizer plant correlation technique, producers, develop a kind of new type bonding agent, guaranteeing under the prerequisite of granular ammonium sulfate product outer quality, ton products with adhesive agent cost drops to 50 yuan, and product per ton is saved 100 yuan, has created good economic benefit.
Summary of the invention
The object of the invention is provides a kind of new particulate ammonium sulfate production to use tackiness agent based on the market requirement.When guaranteeing product outer quality, granular ammonium sulfate product ton cost is declined 100 yuan/ton.
A kind of tackiness agent for the production of granular ammonium sulfate of the present invention, the main component of its tackiness agent is: Tai-Ace S 150, calcium carbonate, monoammonium phosphate; The mass percent of each composition of tackiness agent: calcium carbonate 10%~15%, Tai-Ace S 150 70%~75%, monoammonium phosphate 5%~10%.
Above-mentioned tackiness agent is when for the production of granular ammonium sulfate product, and effective proportioning of ammonium sulfate slurry and tackiness agent is for seeing the following form
Granular ammonium sulfate slurrying proportioning table:
Sequence number | Title | Specification | Pure amount (kg) |
1 | Tackiness agent | Mixture | 50? |
2 | Ammonium sulfate slurry | 20.7-0-22.3 | 1000? |
Add up to | ? | ? | 1050 |
This tackiness agent effectively utilizes the viscosity of material and the balling ratio that reaction heat improves product, during normal production, do not need to use steam or water to help granulation, reduced baked strength, can reduce costs, improve output, lower coal consumption, simultaneously can be according to market need to solve the even blending problem of available nutrient.
Above-mentioned tackiness agent in use, the ammonium sulfate slurry that upstream device is produced is mixed by a certain percentage with tackiness agent, send into granulation/drying machine spray granulating, work in-process obtain qualified 2mm-4mm product particle after broken, screening, washing, add as required tinting material, coating agent obtains granular ammonium sulfate product.
In aforesaid method, described in produce the ammoniumsulphate soln that raw material that granular ammonium sulfate product uses is phosphogypsum ammonium sulfate production processed, density: 1.24 g/ml-1.26g/ml, water ratio: 50%~58% N content: 20.5%-21.0%; In new type bonding agent, Tai-Ace S 150 is common industrial aluminum sulphate, and monoammonium phosphate is common fertilizer grade monoammonium phosphate, and calcium carbonate is upstream device byproduct (calcium carbonate content: 60%; Moisture content: 15%-20%).
Method provided by the invention has following advantage:
(1) the granular ammonium sulfate product that uses new type bonding agent to produce, is guaranteeing under the prerequisite of product outer quality, nitrogen content is guaranteed more than 19.5%, 100 yuan of ton cost decreases, remarkable in economical benefits;
(2) flow process that the device that this patent production method adopts and flow process are existing maturation, changes littlely, has reduced the risk of investing.
Embodiment
Be implemented in being mixed in groove of a belt stirrer, add ammonium sulfate slurry and tackiness agent simultaneously, density 1.24 g/ml-1.26g/ml of ammonium sulfate slurry, the ammonium sulfate slurry and the tackiness agent that enter the groove that is mixed carry out accurate proportioning metering.Preliminary mixed material pulp pumping to slurry circulation system is further mixed, and suitably heats slurry temperature is risen to 85 ℃-100 ℃.The slip preparing is sent into granulation/drying machine spray granulating
andthe high-temperature flue gas of approximately 550 ℃-600 ℃ dry, dry thermal source adopts coal-fired fluidizing furnace to produce.High-temperature gas is to whitewashing slip fluidized drying, the work in-process that obtain after dry are delivered to work in-process by bucket elevator and are sieved, after screening, 2mm-4mm particle enters the cooling and parcel of cooling cylinder and obtains product, >4mm particle after crusher in crushing with screening out 1mm-2mm particle as returning charge, return to granulation/drying machine.Dried tail gas is sent into Venturi scrubber scrubbing dust collection by exhaust fan through whirlwind depositing dust, and it is emptying that dedusting gas up to standard passes through aiutage.
Wengfu phosphate fertilizer plant of Wengfu Group Co., Ltd. is used the inventive method, utilize the granular ammonium device of a set of 200kt/a that the ammonium sulfate slurry of phosphogypsum ammonium sulfate production processed and phosphor ammonium slurry are produced to granular ammonium sulfate after proportioning, granulating and drying, fragmentation, screening, washing, painted parcel, formed the granular ammonium sulfate production throughput of 100kt/a at present.
[related data]
1. granular ammonium sulfate slurrying proportioning table:
Sequence number | Title | Specification | Pure amount (kg) |
1 | Tackiness agent | Mixture | 50? |
2 | Ammonium sulfate slurry | 20.7-0-22.3 | 1000? |
Add up to | ? | ? | 1050 |
2. use the product data after tackiness agent
The granular ammonium sulfate product situation that-28 days on the 21st June in 2013 produces:
Average nitrogen content (mathematics weighted mean): 20.53%
Date manufactured | Order of classes or grades at school | Quantity | Total nitrogen |
2013-6-28 | In vain | 233.5 | 19.86 |
2013-6-28 | Night | 183 | 21.18 |
2013-6-27 | In vain | 177 | 20.03 |
2013-6-27 | Night | 208.5 | 19.82 |
2013-6-26 | In vain | 186 | 19.59 |
2013-6-26 | Night | 179 | 19.54 |
2013-6-25 | In vain | 194 | 19.57 |
2013-6-25 | Night | 116 | 19.48 |
2013-6-24 | In vain | 181 | 20.22 |
2013-6-24 | Night | 191.5 | 20.04 |
2013-6-23 | In vain | 156 | 19.5 |
2013-6-23 | Night | 180 | 19.88 |
2013-6-22 | In vain | 196 | 19.72 |
2013-6-22 | Night | 158 | 19.97 |
2013-6-21 | In vain | 169.5 | 19.67 |
2013-6-21 | Night | 176 | 19.76 |
Ultimate production | 2885 | ||
Average nitrogen content | 19.86 |
Claims (2)
1. for the production of a tackiness agent for granular ammonium sulfate, it is characterized in that the main component of tackiness agent is: Tai-Ace S 150, calcium carbonate, monoammonium phosphate; The mass percent of each composition of tackiness agent: calcium carbonate 10%~15%, Tai-Ace S 150 70%~75%, monoammonium phosphate 5%~10%; Above-mentioned tackiness agent is when for the production of granular ammonium sulfate product, under effective proportioning of ammonium sulfate slurry and tackiness agent is shown in:
Granular ammonium sulfate slurrying proportioning:
Above-mentioned tackiness agent in use, the ammonium sulfate slurry that upstream device is produced is mixed by a certain percentage with tackiness agent, send into granulation/drying machine spray granulating, work in-process obtain qualified 2mm-4mm product particle after broken, screening, washing, add as required tinting material, coating agent obtains granular ammonium sulfate product.
2. a kind of tackiness agent for the production of granular ammonium sulfate according to claim 1, the ammoniumsulphate soln that to it is characterized in that producing raw material that granular ammonium sulfate product uses be phosphogypsum ammonium sulfate production processed, density: 1.24 g/ml-1.26g/ml, water ratio: 50%~58% N content: 20.5%-21.0%; In tackiness agent, Tai-Ace S 150 is common industrial aluminum sulphate, and monoammonium phosphate is common fertilizer grade monoammonium phosphate, and calcium carbonate is wherein calcium carbonate content of upstream device byproduct: 60%; Moisture content: 15%-20%.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201310614637.5A CN103588584A (en) | 2013-11-28 | 2013-11-28 | Adhesive used for producing granular ammonium sulfate |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201310614637.5A CN103588584A (en) | 2013-11-28 | 2013-11-28 | Adhesive used for producing granular ammonium sulfate |
Publications (1)
Publication Number | Publication Date |
---|---|
CN103588584A true CN103588584A (en) | 2014-02-19 |
Family
ID=50078946
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201310614637.5A Pending CN103588584A (en) | 2013-11-28 | 2013-11-28 | Adhesive used for producing granular ammonium sulfate |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN103588584A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107531583A (en) * | 2015-05-27 | 2018-01-02 | 蒂森克虏伯工业解决方案股份公司 | Ammonium sulfate is granulated |
CN109704863A (en) * | 2019-02-18 | 2019-05-03 | 湖北三宁化工股份有限公司 | A kind of bulky grain sulfur-containing nitrogen fertilizer and preparation method thereof |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101269823A (en) * | 2008-05-07 | 2008-09-24 | 瓮福(集团)有限责任公司 | Method for producing ammonium sulphate with phosphogypsum as raw material |
CN101575222A (en) * | 2009-06-05 | 2009-11-11 | 瓮福(集团)有限责任公司 | Method for producing ammonium sulphate grain products by using inorganic caking agent |
CN102464508A (en) * | 2010-10-29 | 2012-05-23 | 山东农大肥业科技有限公司 | Granulation binder of compound fertilizer and application method thereof |
-
2013
- 2013-11-28 CN CN201310614637.5A patent/CN103588584A/en active Pending
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101269823A (en) * | 2008-05-07 | 2008-09-24 | 瓮福(集团)有限责任公司 | Method for producing ammonium sulphate with phosphogypsum as raw material |
CN101575222A (en) * | 2009-06-05 | 2009-11-11 | 瓮福(集团)有限责任公司 | Method for producing ammonium sulphate grain products by using inorganic caking agent |
CN102464508A (en) * | 2010-10-29 | 2012-05-23 | 山东农大肥业科技有限公司 | Granulation binder of compound fertilizer and application method thereof |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107531583A (en) * | 2015-05-27 | 2018-01-02 | 蒂森克虏伯工业解决方案股份公司 | Ammonium sulfate is granulated |
CN109704863A (en) * | 2019-02-18 | 2019-05-03 | 湖北三宁化工股份有限公司 | A kind of bulky grain sulfur-containing nitrogen fertilizer and preparation method thereof |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN105110819B (en) | A method of sulfenyl urea compound fertilizer is produced using ammonia process of desulfurization by-product | |
CN103848670B (en) | A kind of with the technique of phosphorus ammonium thickened pulp One-step production high-concentration compound fertilizer | |
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 | |
CN104355734A (en) | Production method of ammonium sulfate-ammonium phosphate composite fertilizer | |
CN101648838B (en) | Method for producing granular ammonium sulfate by using crystalline ammonium sulfate or powdery ammonium sulfate | |
CN1266088C (en) | Direct urea solution spraying and pelletizing process of producing composite fertilizer | |
CN102503622A (en) | Process for producing urea sulfate ammoniated compound fertilizer | |
CN103044121B (en) | Production method of ammonium phosphate sulfate product | |
CN100371238C (en) | Method for producing diammonium phosphate by concentrating acid slime, and secondary ammoniation reactor | |
CN100354235C (en) | Spray pelleting process of compound fertilizer | |
CN102276362A (en) | high-concentration compound fertilizer | |
CN104803736A (en) | Technological method for steam-free compound fertilizer production | |
CN103360145A (en) | Technology of producing ammonium sulfate phosphate product from tailing slag | |
CN103396186A (en) | Technology and device for producing ammonium phosphate sulfate product with sewage treatment slag | |
CN101734970A (en) | Method for preparing urea ammonium phosphate by employing multi-level neutralization and acidic slurry concentration | |
CN103588584A (en) | Adhesive used for producing granular ammonium sulfate | |
CN103396222A (en) | Adhesive for producing granular ammonium sulfate | |
CN101973790B (en) | Method for producing granular diammonium phosphate with low concentration of nutrients by tailings | |
CN103626528A (en) | Method for producing granular ammonium sulphate by using phosphorus-containing wastewater | |
CN101337847B (en) | Method for preparing high-nitrogen sulfonyl azophoska compound fertilizer | |
CN103588543B (en) | Production method for multi-nutrient urea sulfuric acid sulfur-based composite fertilizer | |
CN101412646B (en) | Preparation of nitro azophoska compound fertilizer | |
CN102910955B (en) | Production method of ammonium sulphate phosphate products | |
CN109536704A (en) | Steel-making enrichment sludge complex adhesive and its preparation and application |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
C02 | Deemed withdrawal of patent application after publication (patent law 2001) | ||
WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20140219 |