CN201404794Y - Novel tower-type air-cooling pelletizing device of full-melting compound fertilizer - Google Patents

Novel tower-type air-cooling pelletizing device of full-melting compound fertilizer Download PDF

Info

Publication number
CN201404794Y
CN201404794Y CN2009200458052U CN200920045805U CN201404794Y CN 201404794 Y CN201404794 Y CN 201404794Y CN 2009200458052 U CN2009200458052 U CN 2009200458052U CN 200920045805 U CN200920045805 U CN 200920045805U CN 201404794 Y CN201404794 Y CN 201404794Y
Authority
CN
China
Prior art keywords
tower
granulation
pelletizing
air
air exhauster
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.)
Expired - Fee Related
Application number
CN2009200458052U
Other languages
Chinese (zh)
Inventor
魏贵生
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to CN2009200458052U priority Critical patent/CN201404794Y/en
Application granted granted Critical
Publication of CN201404794Y publication Critical patent/CN201404794Y/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Landscapes

  • Fertilizers (AREA)

Abstract

The utility model relates to a novel tower-type air-cooling pelletizing device of a full-melting compound fertilizer, comprising a pelletizing tower (1) and a rotational pelletizing head (2), the height of the pelletizing tower (1) is 15-70m, the diameter of the tower is 6-18m, the rotational pelletizing head (2) is arranged at the central position at the top part of the inner side of the pelletizing tower (1), and the lower part of the pelletizing tower (1) is connected with a conical collector (4); the novel tower-type air-cooling pelletizing device is characterized in that: the top part ofthe pelletizing tower (1) is at least provided with a circle of exhaust fans (3), the air inlet of the exhaust fan (3) is communicated with the inner cavity of the pelletizing tower (1), and the distance L from the edge of the exhaust fans (3) at the outset ring to the inner wall of the pelletizing tower (1) is 0.9-2.5m; a circle of air windows (5), the height H of which is 1.2-3m, a conveying device (6) is arranged below the material outlet of the conical collector (4), and the material outlet of the conveying device (6) is provided with a revolving drum cooler (7). The novel tower-type air-cooling pelletizing device has the advantages of good pelletizing effect and convenient manufacturing and installation.

Description

The novel tower-type air-cooled prilling granulator of full-fusing composite fertilizer
Technical field
The utility model relates to a kind of granulation formation device of composite fertilizer, the wind-cooling crystallization granulation equipment of especially a kind of full-fusing composite fertilizer, the novel tower-type air-cooled prilling granulator of specifically a kind of full-fusing composite fertilizer.
Background technology
In recent years, the production technology that China produces full-fusing composite fertilizer (being NPK composite fertilizer) is greatly improved, it is ripe day by day that traditional handicrafts such as material, drum granulating are made in traditional disk granulation, extruding, but traditional handicraft exists efficient low, a series of problems such as finished product appearance poor, energy consumption height, and people have invented the tower granulation new technology for this reason, the produced product appearance of this technology is mellow and full, nutrient is accurately even, and the utilization rate of fertilizer height is promptly popular once releasing.But the subject matter that this technology exists is in order to increase cooling effect, its body of the tower is mostly more than 100 meters, tower diameter is also more than 12, investment is big, the cost height, floor space is big, to the safety requirements height, the conveying of material and lifting difficulty are very big, and energy consumption is also than higher, for this reason, people have done big quantity research on tower height and energy consumption, for this reason, Chinese patent 021349711 has proposed a kind of low tower production technology and equipment, Chinese patent 200510038702.X has proposed a kind of freezing process for granulating and device thereof of utilizing, and they are reducing all creative meaning on the body of the tower height.Still there are following problem in actual use in these two kinds of methods and device: the one, increased dust, and dust is easy and the adhesion of tower wall, needs regularly to stop production cleaning; The 2nd, the outward appearance degree of finished particle is relatively poor, can't compare favourably adhesion easily between the particle with high tower; The 3rd, bad adaptability, the prescription of the composite fertilizer that each granulation tower can be made changes can not be too greatly, otherwise can't operate as normal, and the product of different formulations is regulated difficulty; The 4th, invest still bigger.Just because of above-mentioned reason, cause them to be difficult to large tracts of land and promote the use of.At the problems referred to above, the applicant has applied for that to State Patent Office name is called " wind-cooling crystallization granulation method of full-fusing composite fertilizer and device thereof ", application number is that 200710004177.9 patent of invention has solved the problems referred to above to a certain extent, has promoted the manufacturing process and the level of China composite fertilizer greatly.But in actual use because the wind that air blast produces can cause certain turbulent flow in tower, influence the granulation effect, particle diameter is difficult to surpass more than 2 millimeters, and control accuracy had relatively high expectations, easily produce sticking wall dust, cause easy caking, the product proportioning is regulated problems such as difficulty, therefore must be improved.
Summary of the invention
The purpose of this utility model is the granulating weak effect that exists at existing tower granulation, easily produce sticking wall dust and product proportioning regulates the big problem of difficulty, design a kind of shaping well, small investment, energy consumption low, be suitable in the wind-cooling crystallization granulation device of the full-fusing composite fertilizer that uses of low tower.
The technical solution of the utility model is:
The wind-cooling crystallization granulation device of a kind of full-fusing composite fertilizer, comprise granulation tower 1 and rotating granulation head 2, the tower height of this granulation tower 1 is a 15-70 rice, tower diameter is a 6-18 rice, rotating granulation head 2 is installed in granulation tower 1 inside top center position, the bottom of making material tower 1 is connected with one taper (V-arrangement) or W shape structure (front view) gatherer 4, it is characterized in that being equipped with one at least at the top of described granulation tower 1 encloses air exhauster 3, the air inlet of this air exhauster 3 communicates with the inner chamber of granulation tower 1, and the distance L of Edge Distance granulation tower 1 inwall of outmost turns air exhauster 3 is 0.9-2.5m; In the bottom of granulation tower 1, to offer a circle height H be the air-inlet window 5 of 1.2-3m for the top of conical collector 4; Conveying device 6 is installed, the rotary drum cooler 7 that the discharge end of conveying device 6 is installed below the discharging opening of conical collector 4.
Granulation tower 1 top is equipped with the air exhauster 3 that a number of turns amount is no less than 8, and the diameter of every air exhauster is not less than 0.8 meter.
Louvered window leaf 8 is installed on described air-inlet window 5.
The charging aperture of described rotating granulation head 2 links to each other with the discharge end of slip breakdown of emulsion machine 9.
The beneficial effects of the utility model are:
1, thereby it is of the present utility model by changing the prilling process that traditional air blast delays the quick cooling formation of high temperature fluid column decrease speed particle, change the method for exhausting into, make cooling air stable the flowing that make progress at the bottom of the tower, not only can further prolong high temperature fluid column decrease speed, and because unstable airflow, the granulation effect is better than the air blast mode greatly, can obtain particle diameter in the composite fertilizer more than 2.5 millimeters, particle diameter can be steady in a long-term between the 2-4.5 millimeter, supporting rotary drum cooler makes the whole cooling of particle to the particle that falls dehumidifying wind cooling processing from cooling tower simultaneously, and is non-hygroscopic in the cooling procedure, prevented from caking is convenient to packing and transportation.
2, with existing in low tower compare with freezing tower and can reduce investment 50%-80%, production scale can be regulated as required simultaneously, and is changeable.
3, can produce the composite fertilizer of high, normal, basic variable concentrations, it is very convenient to change prescription, the formula rate scope is big, composite fertilizer for different proportionings can will adjust to suitable scope cool time by variable frequency adjustment device adjusting exhausting amount, prevented that cold-peace from cooling off the not generation of foot phenomenon, and realized simultaneously the convenient of particle diameter regulated.
4, can not produce the dust wall sticking phenomenon, need not periodic cleaning tower wall,, therefore can not produce the dust wall sticking phenomenon because the wind of air exhauster rises along wall.
5, the good evenness of product, yield rate can be up to more than 99%, and handling good.
6, can under all weather conditions, work, solved under high temperature that existing processes exists, the super-humid conditions can't ordinary production contradiction, can be under hot and humid condition round-the-clock ordinary production.
7, energy consumption is low, has reduced tower height on the one hand, has reduced the energy consumption of mass transport, by adopting energy-conservation air exhauster, can significantly reduce energy loss on the other hand.
8, the utility model is equipped with the breakdown of emulsion machine slip is carried out fragmentation, and the emulsification exquisiteness helps increasing the surface tension of temperature of high temperature slurry, improves the granulating effect, increases particle diameter and granulating ratio (more than 99%).
9, it is low to the utlity model has cost, makes that installation, debugging and operation maintenance are convenient, the advantage of good energy-conserving effect.
Description of drawings
Fig. 1 is the structural representation of device of the present utility model.
Fig. 2 is the top view of granulation tower of the present utility model.
The specific embodiment
Following structure drawings and Examples are further described the utility model.
Shown in Fig. 1-2.
The wind-cooling crystallization granulation device of a kind of full-fusing composite fertilizer, comprise granulation tower 1, rotating granulation head 2, air exhauster 3, conveying device 6 (can adopt belt conveyor to be realized) and rotary drum cooler 7, as shown in Figure 1, the tower height of granulation tower 1 can be between the 15-70 rice, tower diameter can be between the 6-18 rice, rotating granulation head 2 is installed in granulation tower 1 inside top center position, in order to improve the granulation effect, also can make the slurry that enters rotating granulation head 2 be introduced into breakdown of emulsion machine 9 (can adopt the stainless steel high speed agitator or be that the relevant device that 1000-5000 changes is realized from the market purchasing rotating speed directly) during concrete enforcement carries out breakdown of emulsion and handles, the bottom of making material tower 1 is connected with one taper (being seen as V-arrangement from the front) or biconial (promptly being seen as W shape from the front) gatherer 4, one circle or a few circle air exhauster 3 is installed at the top of described granulation tower 1, the number of turns of air exhauster 3 can be determined according to the power of tower diameter and every air exhauster, the air exhauster of inner ring should be avoided rotating granulation head 2 pairing positions, at least should the air exhauster 3 that one number of turns amount is no less than 8 be installed in the position of distance granulation tower 1 inwall 0.9-2.5 during concrete enforcement, the diameter of every air exhauster 3 should be greater than 80 centimetres (as shown in Figure 2), the air inlet of air exhauster 3 communicates with the inner chamber of granulation tower 1, and the distance L of Edge Distance granulation tower 1 inwall of outmost turns air exhauster 3 is 0.9-2.5m; In the bottom of granulation tower 1, to offer a circle height H be the air-inlet window 5 of 1.2-3m for the top of conical collector 4, louvered window leaf 8 is installed on the air-inlet window 5, the pane of air-inlet window 5 can be replaced by the pillar that supports granulation tower 1, and in order to improve the air intake effect, air-inlet window 5 is the bigger the better in principle; Because the temperature of compound fertilizer granules that falls into conical collector 4 from granulation tower 1 is generally more than 55 degrees centigrade, therefore in order to prevent the caking in the natural cooling process, the utility model also is equipped with a conveying device 6 below the discharging opening of conical collector 4 (can adopt the belt conveyor of normal wind or other is board-like, wheel conveyer is realized), by conveying device 6 particle being sent into the rotary drum cooler 7 that is positioned at its discharge end one side rapidly (can be directly from market purchasing, customization or design voluntarily, when designing voluntarily with directly through being not more than 1.6 meters, length is no more than 20 meters and is advisable) in lower the temperature, dehumidifying (utilizing dehumidified air to exchange realization) is sent into follow-up baling line after treatment again through rotary drum cooler 7 cooled compound fertilizer granules and is packed and get final product.Air exhauster 3 preferably adopts the frequency control air exhauster during concrete enforcement, on its drive motors frequency converter is installed, and its power can be selected according to the maximum quantity of wind of every air exhauster.
Below be two concrete design example; but protection of the present utility model is not limited in this two design example; those skilled in the art can carry out a series of equivalence design with reference to summary of the invention of the present utility model, the specific embodiment and two following design example, and these all are considered to belong among the protection domain of the present utility model.
11 meters of tower diameter (internal diameter) Ф of example 1. design granulation towers, 40 meters of effective depths (prilling head to tower at the bottom of), 48 meters of total heights.Using diameter altogether is 1 meter 16 of air exhausters and to become a circle evenly to be installed in apart from the inner wall of tower distance L be 1 meter position, and the actual motion production capacity is 10 tons/hour, 90% above particle diameter 〉=2.5 millimeter.
12 meters of tower diameter (internal diameter) Ф of example 2. design granulation towers, 45 meters of effective depths (prilling head to tower at the bottom of), 54 meters of total heights.Using diameter altogether is 1 meter 20 of air exhausters and to become a circle to be installed in apart from the inner wall of tower distance L be 1.2 meters position, and the actual motion production capacity is 16 tons/hour, 90% above particle diameter 〉=2.5 millimeter.
The utility model does not relate to the part prior art that maybe can adopt same as the prior art to be realized.

Claims (6)

1, the novel tower-type air-cooled prilling granulator of a kind of full-fusing composite fertilizer, comprise granulation tower (1) and rotating granulation head (2), the tower height of this granulation tower (1) is a 15-70 rice, tower diameter is a 6-18 rice, rotating granulation head (2) is installed in granulation tower (1) inside top center position, the bottom of making material tower (1) is connected with one gatherer (4), it is characterized in that being equipped with one at least at the top of described granulation tower (1) encloses air exhauster (3), the air inlet of this air exhauster (3) communicates with the inner chamber of granulation tower (1), and the distance L of Edge Distance granulation tower (1) inwall of outmost turns air exhauster (3) is 0.9-2.5m; In the bottom of granulation tower (1), to offer a circle height H be the air-inlet window (5) of 1.2-3m for the top of conical collector (4); Discharging opening below at conical collector (4) is equipped with conveying device (6), the rotary drum cooler (7) that the discharge end of conveying device (6) is installed.
2, prilling granulator according to claim 1 is characterized in that granulation tower (1) top is equipped with the air exhauster (3) that a number of turns amount is no less than 8, and the diameter of every air exhauster is not less than 0.8 meter.
3, prilling granulator according to claim 1 is characterized in that being equipped with louvered window leaf (8) on described air-inlet window (5).
4, prilling granulator according to claim 1 is characterized in that the charging aperture of described rotating granulation head (2) links to each other with the discharge end of slip breakdown of emulsion machine (9).
5, prilling granulator according to claim 1 is characterized in that on the drive motors of described air exhauster (3) frequency converter being housed.
6, prilling granulator according to claim 1 is characterized in that described gatherer (4) is taper or or W shape structure.
CN2009200458052U 2009-05-13 2009-05-13 Novel tower-type air-cooling pelletizing device of full-melting compound fertilizer Expired - Fee Related CN201404794Y (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2009200458052U CN201404794Y (en) 2009-05-13 2009-05-13 Novel tower-type air-cooling pelletizing device of full-melting compound fertilizer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2009200458052U CN201404794Y (en) 2009-05-13 2009-05-13 Novel tower-type air-cooling pelletizing device of full-melting compound fertilizer

Publications (1)

Publication Number Publication Date
CN201404794Y true CN201404794Y (en) 2010-02-17

Family

ID=41675715

Family Applications (1)

Application Number Title Priority Date Filing Date
CN2009200458052U Expired - Fee Related CN201404794Y (en) 2009-05-13 2009-05-13 Novel tower-type air-cooling pelletizing device of full-melting compound fertilizer

Country Status (1)

Country Link
CN (1) CN201404794Y (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101555181B (en) * 2009-05-13 2012-06-27 魏贵生 Novel tower-type air-cooled prilling device for full-melting compound fertilizers

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101555181B (en) * 2009-05-13 2012-06-27 魏贵生 Novel tower-type air-cooled prilling device for full-melting compound fertilizers

Similar Documents

Publication Publication Date Title
CN100450979C (en) Full- fusing wind-cooling crystallization granulation method and device for composite fertilizer
CN207287366U (en) A kind of composite heat transfer comminutor
CN106140048B (en) Integral type solid phase viscosity-increasing reactor and the system and method cut into slices with its production high visocity nylon
CN102580347B (en) Continuous crystallization method of tetraacetylethylenediamine
CN109395659A (en) A kind of sainfoin plantation with screening function releases the fertile prilling granulator of control with long-acting
CN204151247U (en) A kind of for the prilling granulator after nitrophosphate fertilizer evaporation technology
CN208187181U (en) A kind of band sieves the cooling equipment of compound fertilizer production with tower granulation production of effect
CN101555181B (en) Novel tower-type air-cooled prilling device for full-melting compound fertilizers
CN201404794Y (en) Novel tower-type air-cooling pelletizing device of full-melting compound fertilizer
CN204469663U (en) Pivoted arm scraper at the bottom of high tower compound fertilizer tower
CN206167979U (en) Empty cold crystallization ware of calcium nitrate
CN210367481U (en) Compound fertilizer production prilling granulator
CN209696836U (en) A kind of fourth element Tower-type melt granulation compound fertilizer process units
CN200974819Y (en) Air-cooled crystallization granulating device for full-fusion composite fertilizer
CN109161404A (en) One kind being used for downdraft straw charring charcoal gas combined production device and its production method
CN204787921U (en) Reverse -flow fodder cooling device
CN201983596U (en) Hot air supplier used for powder process spray drying tower
CN105481532A (en) Multidimensional extruding granulation method based on addition of organic binder and apparatus thereof
CN101580413B (en) Systematic integration optimization method based on high tower fused melt granulated compound fertilizer technology
CN206865989U (en) A kind of pelleting agent, which suspends, dries burnishing device
CN210584825U (en) Functional multistage compound thoughtlessly fertile granulator
CN216879212U (en) Granulation drying device for superphosphate
CN212076892U (en) Material cooling device for compound fertilizer production
CN208998464U (en) A kind of organic fertilizer process units
CN214933504U (en) Potassium citrate production is with defeated material equipment

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
C17 Cessation of patent right
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20100217

Termination date: 20130513