CN202390333U - Compound fertilizer production device dispensing with fillers - Google Patents
Compound fertilizer production device dispensing with fillers Download PDFInfo
- Publication number
- CN202390333U CN202390333U CN 201120549084 CN201120549084U CN202390333U CN 202390333 U CN202390333 U CN 202390333U CN 201120549084 CN201120549084 CN 201120549084 CN 201120549084 U CN201120549084 U CN 201120549084U CN 202390333 U CN202390333 U CN 202390333U
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- jet pipe
- tablets press
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Abstract
The utility model belongs to the field of production of compound fertilizers dispensing with fillers, and in particular relates to a compound fertilizer production device dispensing with fillers. The device has a simple structure and a high granulation rate, operates stably, does not discharge wastewater and dispenses with fillers. The device comprises a semi-sealed chamber movably installed on one side of a granulator, wherein the semi-sealed chamber is connected with a drying system, a screening system, a cooling system, a wrapping system and a packaging system via a pipeline; a gas outlet is arranged at the top of the semi-sealed chamber and is connected with a deduster, a washer, an acid preparation tank and the other side of the granulator via a pipeline; the acid preparation tank is connected with a dilute sulfuric acid spray pipe; a gaseous ammonia storage tank is connected with a gaseous ammonia spray pipe; a liquid ammonia storage tank is connected with a liquid ammonia spray pipe; and a batching system is connected with the other side of the granulator. The device has the following advantages: the produced compound fertilizers have good instant solubility, low moisture content and low cost, do not have residues after being dissolved, and can not pollute the environment.
Description
Technical field
The utility model belongs to the production field of filler-free composite fertilizer, be specifically related to a kind of simple in structure, stable, balling ratio is high, the production equipment of the filler-free composite fertilizer of non-wastewater discharge and filler-free.
Background technology
China is maximum in the world compound manure production at present and uses country; Compound manure is as a kind of more comprehensive fertilizer of function ratio that contains at least two kinds of nutrients in nitrogen, phosphorus, the potassium; More and more received user's favor, just the efficient in order to guarantee that composite fertilizer produces adds the weighting agents such as clay that bonding or batching effect are arranged in the time of often need in drum granulating production, dropping into raw material; These weighting agents not only influence the visual appearance of product; Can cause simultaneously the complex fertilizer product instantly-soluble poor, be dissolved with residue, water cut and increase, caused production cost to increase, also environment has been caused pollution.
Summary of the invention
The purpose of the utility model be to overcome defective of the prior art and provide a kind of simple in structure, stable, balling ratio is high, non-wastewater discharge, filler-free, the compound manure instantly-soluble produced are good, the no residue of dissolving, water cut are low, the production equipment of cost filler-free composite fertilizer low and that can not pollute environment.
The purpose of the utility model is achieved in that and comprises that semitight cavity, the described semitight cavity bottom installed with tablets press one side activity link to each other with dehumidification system, screening system, cooling system, baggage systems and packaging system through pipeline successively; Described semitight cavity upper part sealing; Lower part communicates with tablets press; The top of described semitight cavity is provided with pneumatic outlet; Described pneumatic outlet through pipeline successively with fly-ash separator, washer, the opposite side of complex acid jar and tablets press links to each other, the pipeline between described washer and the complex acid jar is provided with threeway; One end of described threeway links to each other with the opposite side of tablets press is inner through pipeline, and described complex acid jar links to each other with the inner dilute sulphuric acid jet pipe of tablets press through pipeline; Described gas ammonia storage tank links to each other with the inner gas ammonia jet pipe of the opposite side of tablets press, and described liquid ammonia storage tank links to each other with the inner liquefied ammonia jet pipe of the opposite side of tablets press, and described feed proportioning system links to each other with the opposite side of tablets press; Described complex acid tank top is provided with emptying pipe.The shower nozzle of described dilute sulphuric acid jet pipe and liquefied ammonia jet pipe adopts the uneven distribution method to arrange.Four shower nozzles of layout in the end 1/3rd that described dilute sulphuric acid jet pipe links to each other with the complex acid jar are arranged three shower nozzles in the centre 1/3rd, two shower nozzles of terminal 1/3rd interior layouts.Four shower nozzles of layout in the end 1/3rd that described liquefied ammonia jet pipe links to each other with liquid ammonia storage tank are arranged three shower nozzles in the centre 1/3rd, two shower nozzles of terminal 1/3rd interior layouts.Described dilute sulphuric acid jet pipe, the shower nozzle that is provided with on gas ammonia jet pipe and the liquefied ammonia jet pipe be installed in positive apparent direction and tablets press radially vertical surface be on the position at 42 degree angles.
The utlity model has simple in structure, stable, balling ratio is high, non-wastewater discharge, filler-free, the compound manure instantly-soluble produced are good, the no residue of dissolving, water cut are low, cost advantage low and that can not pollute environment.
Description of drawings
Fig. 1 is the utility model principle schematic.
Fig. 2 is the installation site synoptic diagram of the utility model tablets press inner nozzle.
Embodiment
Like Fig. 1, shown in 2; The utility model comprises that semitight cavity 6, described semitight cavity 6 bottoms of installing with tablets press 1 one side activities link to each other with dehumidification system 2, screening system 3, cooling system 4, baggage systems 5 and packaging system 17 through pipeline successively; Described semitight cavity 6 upper part sealing; Lower part communicates with tablets press 1, and the top of described semitight cavity 6 is provided with pneumatic outlet 7, described pneumatic outlet 7 through pipeline successively with fly-ash separator 8, washer 9; Complex acid jar 10 links to each other with the opposite side of tablets press 1; Pipeline between described washer 9 and the complex acid jar 10 is provided with threeway, and an end of described threeway links to each other with the opposite side of tablets press 1 is inner through pipeline, and described complex acid jar 10 links to each other with tablets press 1 inner dilute sulphuric acid jet pipe 15 through pipeline; Described gas ammonia storage tank 12 links to each other with the inner gas ammonia jet pipe 16 of the opposite side of tablets press 1, and described liquid ammonia storage tank 13 links to each other with the inner liquefied ammonia jet pipe 11 of the opposite side of tablets press 1, and described feed proportioning system 14 links to each other with the opposite side of tablets press 1; Described complex acid jar 10 tops are provided with emptying pipe.The shower nozzle of described dilute sulphuric acid jet pipe 15 and liquefied ammonia jet pipe 11 adopts the uneven distribution method to arrange.Four shower nozzles of layout in the end 1/3rd that described dilute sulphuric acid jet pipe 15 links to each other with complex acid jar 10 are arranged three shower nozzles in the centre 1/3rd, two shower nozzles of terminal 1/3rd interior layouts.Four shower nozzles of layout in the end 1/3rd that described liquefied ammonia jet pipe 11 links to each other with liquid ammonia storage tank 13 are arranged three shower nozzles in the centre 1/3rd, two shower nozzles of terminal 1/3rd interior layouts.The shower nozzle that is provided with on the described dilute sulphuric acid jet pipe 15, gas ammonia jet pipe 16 and liquefied ammonia jet pipe 11 be installed in positive apparent direction and tablets press 1 radially vertical surface be on the position at 42 degree angles.
As shown in Figure 1, main raw materials such as urea, monoammonium phosphate, Repone K, ammonium chloride proportionally carry out getting into after the proportioning in feed proportioning system in the tablets press 1 in the utility model, and gas ammonia, liquefied ammonia, the dilute sulphuric acid of having allocated concentration also proportionally are driven in the tablets press; Regulate the washing water yield that gets in the tablets press 1 simultaneously, make under tablets press 1 70～80 ℃ of interior temperature of charge, water cut 2.3～3.5% conditions, bond each other, push between each material; Form compound fertilizer granules; Qualified particle gets into dehumidification system 2 with underproof particle and carries out drying, and the compound fertilizer granules that dehumidification system 2 comes out through screening system 3, is removed irrational compound fertilizer granules successively; Qualified particle gets into cooling system 4 coolings; Get into baggage systems 5 then, superscribe the agent of one deck anti-caking, get into packaging system 17 at last at particle surface.
Tablets press 1 rotation semitight cavity 6 does not rotate in the utility model, and solid materials gets into semitight cavity 6 backs and gets into dehumidification system 2, screening system 3, cooling system 4 successively through pipeline, baggage systems 5 and packaging system 17; Because the sealing of semitight cavity 6 upper part can not get in the tablets press 1 so contain the gas of dust once more; The gas that contains dust gets into fly-ash separator 8 backs and gets in the washers 9, and through washing back emptying up to standard, a washing water part gets into complex acid jar 10, and to be used for configuration concentration be 60% dilute sulphuric acid, and another part gets in the tablets press and is used to increase granulation humidity; The dilute sulphuric acid that configures in the complex acid jar 10 gets in the tablets press 1; Gas ammonia in the gas ammonia storage tank 12 gets into the bottom of tablets press 1, apart from 1.2 meters of imports.
As shown in Figure 2; Concentration is 60% dilute sulphuric acid in the tablets press 1; The shower nozzle of gas ammonia jet pipe 16 and liquefied ammonia jet pipe 11 is positioned at position, tablets press lower middle; Shower nozzle and tablets press radially vertical surface are 42 degree angles, and this angle can either satisfy the sour granulation demand of spray, can well avoid material to get into jet pipe again and result in blockage.
Claims (5)
1. the production equipment of a filler-free composite fertilizer; Comprise that semitight cavity (6), described semitight cavity (6) bottom of installing with tablets press (1) one side activity link to each other with dehumidification system (2), screening system (3), cooling system (4), baggage systems (5) and packaging system (17) through pipeline successively; It is characterized in that: the sealing of described semitight cavity (6) upper part; Lower part communicates with tablets press (1); The top of described semitight cavity (6) is provided with pneumatic outlet (7); Described pneumatic outlet (7) through pipeline successively with fly-ash separator (8), washer (9), complex acid jar (10) links to each other with the opposite side of tablets press (1), the pipeline between described washer (9) and the complex acid jar (10) is provided with threeway; One end of described threeway links to each other with the opposite side of tablets press (1) is inner through pipeline, and described complex acid jar (10) links to each other with the inner dilute sulphuric acid jet pipe (15) of tablets press (1) through pipeline; Described gas ammonia storage tank (12) links to each other with the inner gas ammonia jet pipe (16) of the opposite side of tablets press (1); Described liquid ammonia storage tank (13) links to each other with the inner liquefied ammonia jet pipe (11) of the opposite side of tablets press (1), and described feed proportioning system (14) links to each other with the opposite side of tablets press (1); Described complex acid jar (10) top is provided with emptying pipe.
2. the production equipment of filler-free according to claim 1 composite fertilizer is characterized in that: the shower nozzle of described dilute sulphuric acid jet pipe (15) and liquefied ammonia jet pipe (11) adopts the uneven distribution method to arrange.
3. the production equipment of filler-free according to claim 2 composite fertilizer; It is characterized in that: arrange four shower nozzles in the end 1/3rd that described dilute sulphuric acid jet pipe (15) links to each other with complex acid jar (10); Arrange three shower nozzles in middle 1/3rd, arrange two shower nozzles in the end 1/3rd.
4. the production equipment of filler-free according to claim 2 composite fertilizer; It is characterized in that: arrange four shower nozzles in the end 1/3rd that described liquefied ammonia jet pipe (11) links to each other with liquid ammonia storage tank (13); Arrange three shower nozzles in middle 1/3rd, arrange two shower nozzles in the end 1/3rd.
5. the production equipment of filler-free according to claim 1 composite fertilizer; It is characterized in that: the shower nozzle that described dilute sulphuric acid jet pipe (15), gas ammonia jet pipe (16) and liquefied ammonia jet pipe (11) go up to be provided be installed in positive apparent direction and tablets press (1) radially vertical surface be on the position at 42 degree angles.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201120549084 CN202390333U (en) | 2011-12-26 | 2011-12-26 | Compound fertilizer production device dispensing with fillers |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201120549084 CN202390333U (en) | 2011-12-26 | 2011-12-26 | Compound fertilizer production device dispensing with fillers |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202390333U true CN202390333U (en) | 2012-08-22 |
Family
ID=46665271
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201120549084 Expired - Lifetime CN202390333U (en) | 2011-12-26 | 2011-12-26 | Compound fertilizer production device dispensing with fillers |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202390333U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103694064A (en) * | 2013-12-12 | 2014-04-02 | 广西地源之本肥业有限公司 | Automatic compound fertilizer granulation assembly system |
| CN103694062A (en) * | 2013-12-12 | 2014-04-02 | 广西地源之本肥业有限公司 | Continuous feeding assembly system for pelletizing compound fertilizer |
| CN103694063A (en) * | 2013-12-12 | 2014-04-02 | 广西地源之本肥业有限公司 | Compound fertilizer granulation assembly system |
| CN103694061A (en) * | 2013-12-12 | 2014-04-02 | 广西地源之本肥业有限公司 | Anti-overpressure compound fertilizer granulation assembly system |
-
2011
- 2011-12-26 CN CN 201120549084 patent/CN202390333U/en not_active Expired - Lifetime
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103694064A (en) * | 2013-12-12 | 2014-04-02 | 广西地源之本肥业有限公司 | Automatic compound fertilizer granulation assembly system |
| CN103694062A (en) * | 2013-12-12 | 2014-04-02 | 广西地源之本肥业有限公司 | Continuous feeding assembly system for pelletizing compound fertilizer |
| CN103694063A (en) * | 2013-12-12 | 2014-04-02 | 广西地源之本肥业有限公司 | Compound fertilizer granulation assembly system |
| CN103694061A (en) * | 2013-12-12 | 2014-04-02 | 广西地源之本肥业有限公司 | Anti-overpressure compound fertilizer granulation assembly system |
| CN103694061B (en) * | 2013-12-12 | 2016-06-22 | 广西地源之本肥业有限公司 | Anti-overvoltage compound fertilizer granulating assembly system |
| CN103694063B (en) * | 2013-12-12 | 2016-06-29 | 广西地源之本肥业有限公司 | Compound fertilizer granulating assembly system |
| CN103694064B (en) * | 2013-12-12 | 2017-01-18 | 河北百斗嘉肥料有限公司 | Automatic compound fertilizer granulation assembly system |
| CN103694062B (en) * | 2013-12-12 | 2017-04-12 | 广西地源之本肥业有限公司 | Continuous feeding assembly system for pelletizing compound fertilizer |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CP03 | Change of name, title or address | ||
| CP03 | Change of name, title or address |
Address after: 453731 Xinxiang Economic Development Zone, Henan Province (Xiaoji Town) Patentee after: Henan Xinlianxin Chemical Industry Group Co., Ltd. Address before: 453731 Henan Xinxiang Economic Development Zone Xiaoji Town Henan Xinlianxin Chemical Fertilizer Co., Ltd. Patentee before: Henan XInlianxin Fertiliser Limited Company |
|
| CX01 | Expiry of patent term | ||
| CX01 | Expiry of patent term |
Granted publication date: 20120822 |