CN106166465A - A kind of horizontal melted compound fertilizer air prilling device - Google Patents

A kind of horizontal melted compound fertilizer air prilling device Download PDF

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Publication number
CN106166465A
CN106166465A CN201610485134.6A CN201610485134A CN106166465A CN 106166465 A CN106166465 A CN 106166465A CN 201610485134 A CN201610485134 A CN 201610485134A CN 106166465 A CN106166465 A CN 106166465A
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CN
China
Prior art keywords
granulation tower
ejector
tower
air
air prilling
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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
Application number
CN201610485134.6A
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Chinese (zh)
Inventor
黄培钊
张建军
李秀旭
穆光远
刘法安
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.)
Shenzhen Batian Ecotypic Engineering Co Ltd
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Shenzhen Batian Ecotypic Engineering Co Ltd
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Publication date
Application filed by Shenzhen Batian Ecotypic Engineering Co Ltd filed Critical Shenzhen Batian Ecotypic Engineering Co Ltd
Priority to CN201610485134.6A priority Critical patent/CN106166465A/en
Publication of CN106166465A publication Critical patent/CN106166465A/en
Pending legal-status Critical Current

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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2/00Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic
    • B01J2/02Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic by dividing the liquid material into drops, e.g. by spraying, and solidifying the drops
    • B01J2/04Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic by dividing the liquid material into drops, e.g. by spraying, and solidifying the drops in a gaseous medium

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Fertilizers (AREA)

Abstract

The present invention provides a kind of horizontal melted compound fertilizer air prilling device, described air prilling equipment includes ejector and granulation tower, the nozzle of described ejector is positioned at the side within granulation tower, the horizontal plane of described nozzle spray angle upwards is 0 60 ° with the angle of horizontal plane, the height of described granulation tower is 10 40m, a length of 30 100m of described granulation tower.The air prilling device of the present invention sprays raw material from the side of granulation tower, makes raw material spray with the angle with horizontal plane, and range of jet is long, completes grain forming in horizontal tower, and the product uniformity obtained is preferable;Horizontal air prilling device tower body is relatively low, it is achieved that melt pelletization small-scale production, can realize producing melt pelletization compound fertilizer without enormous investment, save production cost.

Description

A kind of horizontal melted compound fertilizer air prilling device
Technical field
The invention belongs to fertilizer equipment and manufacture field, be specifically related to a kind of horizontal melted compound fertilizer air prilling device.
Background technology
Process of granulation in compounded fertilizer of granulated production process mainly have granulating method, fluidization process, squeezing and pressing method, melting oil cold process, Melted air-cooling.And melting the cool method of air, also referred to as tower granulation method, it is divided into force ventilated low tower method (general Within high 60m) and the high tower method (general high more than 60m) of gravity-flow ventilation.
CN1213964C discloses the method that the low tower pelletize of a kind of melting charge slurry produces granulated multicomponent composite fertilizer, and it includes Following steps: a, compound fertilizer raw material Hybrid Heating is melted;B, melting charge slurry are by the low tower tower using tower height to be 15-45m The rotary prilling sprayer on top sprays and enters in granulation tower;C, spray in tower to point multilamellar between bottom in the middle part of granulation tower and send Wind, makes slip drop to slowly at the bottom of tower under the drag effect of ascending air during tower top declines and complete pelletize.Step The low tower using tower height to be 30m in rapid b.Described granulation tower is square column type or the cylinder of inner hollow, when being square, tower bottom Size length × a width of 4-20m × 4-20m, time rounded, a diameter of 4-20m at the bottom of tower.This technology uses at high top of tower melted multiple Hefei raw material sprays high tower natural cooling with comminutor again, and structure is complicated, and investment energy consumption is high.
Summary of the invention
For solving the problems referred to above, the present invention provides a kind of horizontal melted compound fertilizer air prilling device, only needs to accommodate The rewinding mouth of compound fertilizer granules, and this programme compound fertilizer melting charge slurry is melted without making high tower on the ground, can be very big Saving compound fertilizer melt pelletization cost.
The specific scheme is that a kind of horizontal melted compound fertilizer air prilling device, described air prilling equipment includes ejector And granulation tower, the nozzle of described ejector is positioned at the side within granulation tower, the horizontal plane of described nozzle spray angle upwards Being 0-60 ° with the angle of horizontal plane, the height of described granulation tower is 10-40m, a length of 30-100m of described granulation tower.
Preferably, the horizontal plane of described nozzle spray angle upwards is 0-45 ° with the angle of horizontal plane, described granulation tower Height be 20-40m, a length of 40-50m of described granulation tower.
Preferably, described nozzle is 0-40m with the height of the bottom of pelletize.
Preferably, the bottom of described granulation tower is provided with rewinding mouth, and described rewinding mouth is for receiving the fertilizer of ejector ejection Granule, 0.01-0.8 times of a length of granulation tower length of described rewinding mouth.
Preferably, described rewinding mouth is positioned at bottom bottom to the ejector place wall of the granulation tower wall relative with ejector At 0-100m.
Preferably, being provided with screening plant bottom described rewinding mouth, described screening plant includes that sieving plate, finished particle export Exporting with seed particles, the outlet of described finished particle for transferring out air prilling equipment, described crystal seed by fertilizer finished particle Particle outlet connects ejector, for being transported to ejector by the seed particles of sieving plate.
Preferably, the number of described rewinding mouth is 1-10.
Preferably, the bottom of described granulation tower is 0-30 ° with the angle of horizontal plane.
Preferably, the side that described granulation tower is relative with ejector is provided with cool air inlet, is used for inputting cold air and makes spray Shoot material slurry cooling, and the top of described granulation tower is provided with cold-air vent.
Beneficial effects of the present invention:
1) advantage of the invention is that and spray raw material from the side of granulation tower, make raw material spray with the angle with horizontal plane Going out, range of jet is long, completes grain forming in horizontal tower, and the product uniformity obtained is preferable;
2) the horizontal air prilling device of the present invention is used, from the little granular compound fertilizer of ejector ejection is in granulation tower Starting after being raised to peak to fall, cold air enters from the right side of granulation tower in the process, and left side is flowed out, and accelerates these little Grain compound fertilizer cooling and solidifying;
3) the horizontal air prilling device tower body of the present invention is relatively low, it is achieved that melt pelletization small-scale production, without great number Investment can realize producing melt pelletization compound fertilizer;
4) compound fertilizer's melting charge slurry of the present invention is melted under tower, extremely low to tower body requirement of strength, can save greatly Compound fertilizer's melt pelletization cost.
Accompanying drawing explanation
Fig. 1 is the profile of horizontal melted compound fertilizer air prilling device, and wherein 1 is ejector, and 2 is granulation tower, and 3 for receiving Material mouth, 4 is cool air inlet, and 5 is cold-air vent, and 6 is high pressure gas entrance, and 7 is melting charge slurry entrance, and 8 is injector nozzle.
Detailed description of the invention
Below the detailed description of the invention of the present invention is described further:
A kind of horizontal melted compound fertilizer air prilling device, described air prilling equipment includes ejector 1 and granulation tower 2, The nozzle 8 of described ejector is positioned at the side within granulation tower 2, the horizontal plane of described nozzle 8 spray angle upwards and level The angle in face is 30 °, and the height of described granulation tower is 25m, a length of 50m of described granulation tower;Described nozzle and the end of pelletize The height in portion is 5m;The bottom of described granulation tower is provided with rewinding mouth 3, and described rewinding mouth 3 is for receiving the fertilizer of ejector 1 ejection Granule, 0.1 times of a length of granulation tower 2 length of described rewinding mouth 3, the i.e. width of necking material are 5m;Described rewinding mouth Number is 3, described rewinding mouth be positioned at 0m bottom bottom to the ejector place wall of the granulation tower wall relative with ejector, 10m, At 20m;Being provided with screening plant bottom described rewinding mouth, described screening plant includes the outlet of sieving plate, finished particle and crystal seed Grain outlet, the outlet of described finished particle for transferring out air prilling equipment by fertilizer finished particle, and described seed particles exports Connect ejector, for ejector will be transported to by the seed particles of sieving plate;The bottom of described granulation tower and horizontal plane Angle is 0 °;The side that described granulation tower 2 is relative with ejector 1 is provided with cool air inlet 4, is used for inputting cold air and makes jetting material Slurry cooling, the top of described granulation tower is provided with cold-air vent 5.
Melted compound fertilizer slip enters ejector 1 through melting charge slurry entrance 7, from the high pressure gas of high pressure gas entrance 6 ejection Melting charge slurry punching press is mixed by body, by ejector 1 with the angle that angle is 30 ° of horizontal plane upwards spray angle Yu horizontal plane Being injected to granulation tower 2, the little granular compound fertilizer that melting charge slurry sprays from ejector is from the beginning of rising to after peak in granulation tower Falling to rewinding mouth 3, cold air enters from the cool air inlet 4 on the right side of granulation tower in the process, and the cold air in left side goes out Mouth 5 flows out, and accelerates these little granular compound fertilizers cooling and solidifying;Raw material is made to spray with the angle with horizontal plane, range of jet Long, horizontal tower completes grain forming, the product uniformity obtained is preferable;Horizontal air prilling device tower body is relatively low, it is achieved Melt pelletization small-scale production, can realize producing melt pelletization compound fertilizer without enormous investment;The compound fertilizer of the present invention melts Melting material slurry is melted under tower, extremely low to tower body requirement of strength, can save compound fertilizer's melt pelletization cost greatly.
The announcement of book and teaching according to the above description, those skilled in the art in the invention can also be to above-mentioned embodiment party Formula changes and revises.Therefore, the invention is not limited in detailed description of the invention disclosed and described above, to invention A little modifications and changes should also be as falling in the scope of the claims of the present invention.Although additionally, this specification employing Some specific terms, but these terms are merely for convenience of description, and the present invention does not constitute any restriction.

Claims (9)

1. a horizontal melted compound fertilizer air prilling device, it is characterised in that described air prilling equipment include ejector and Granulation tower, the nozzle of described ejector is positioned at the side within granulation tower, the horizontal plane of described nozzle spray angle upwards with The angle of horizontal plane is 0-60 °, and the height of described granulation tower is 10-40m, a length of 30-100m of described granulation tower.
Air prilling device the most according to claim 1, it is characterised in that the horizontal plane of described nozzle jet angle upwards Degree is 0-45 ° with the angle of horizontal plane, and the height of described granulation tower is 20-40m, a length of 40-50m of described granulation tower.
Air prilling device the most according to claim 1, it is characterised in that described nozzle with the height of the bottom of pelletize is 0-40m。
Air prilling device the most according to claim 1, it is characterised in that the bottom of described granulation tower is provided with rewinding mouth, Described rewinding mouth is for receiving the fertiliser granulates of ejector ejection, the 0.01-0.8 of a length of granulation tower length of described rewinding mouth Times.
Air prilling device the most according to claim 1, it is characterised in that, described rewinding mouth is positioned at relative with ejector Granulation tower wall bottom to ejector place wall bottom 0-100m at.
Air prilling device the most according to claim 4, it is characterised in that be provided with screening plant bottom described rewinding mouth, Described screening plant includes the outlet of sieving plate, finished particle and seed particles outlet, and the outlet of described finished particle is for by fertilizer Finished particle transfers out air prilling equipment, and the outlet of described seed particles connects ejector, for by by the crystal seed of sieving plate Granule is transported to ejector.
Air prilling device the most according to claim 4, it is characterised in that the number of described rewinding mouth is 1-10.
Air prilling device the most according to claim 1, it is characterised in that the bottom of described granulation tower and the folder of horizontal plane Angle is 0-30 °.
Air prilling device the most according to claim 1, it is characterised in that the side that described granulation tower is relative with ejector Being provided with cool air inlet, be used for inputting cold air and make injection slip lower the temperature, the top of described granulation tower is provided with cold-air vent.
CN201610485134.6A 2016-06-28 2016-06-28 A kind of horizontal melted compound fertilizer air prilling device Pending CN106166465A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201610485134.6A CN106166465A (en) 2016-06-28 2016-06-28 A kind of horizontal melted compound fertilizer air prilling device

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Application Number Priority Date Filing Date Title
CN201610485134.6A CN106166465A (en) 2016-06-28 2016-06-28 A kind of horizontal melted compound fertilizer air prilling device

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CN106166465A true CN106166465A (en) 2016-11-30

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Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1517179A (en) * 2003-01-17 2004-08-04 Jfe金属材料株式会社 Manufacturing method of high-carbon chromium iron slag grinded by wind power and sand-blast material
CN202122935U (en) * 2011-05-20 2012-01-25 安徽泰达新材料股份有限公司 Novel pelleting equipment for trimellitic anhydride
CN102974269A (en) * 2012-12-12 2013-03-20 长沙凯瑞重工机械有限公司 Dry type granulating system for sulfonium
CN103706290A (en) * 2013-11-19 2014-04-09 南通新邦化工科技有限公司 New drum-type granulating method and granulating device
CN103922370A (en) * 2014-04-30 2014-07-16 刘清山 Method and device for preparing granular magnesium chloride
CN206121680U (en) * 2016-06-28 2017-04-26 深圳市芭田生态工程股份有限公司 Prilling granulator sprays in horizontal melting compound fertilizer

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1517179A (en) * 2003-01-17 2004-08-04 Jfe金属材料株式会社 Manufacturing method of high-carbon chromium iron slag grinded by wind power and sand-blast material
CN202122935U (en) * 2011-05-20 2012-01-25 安徽泰达新材料股份有限公司 Novel pelleting equipment for trimellitic anhydride
CN102974269A (en) * 2012-12-12 2013-03-20 长沙凯瑞重工机械有限公司 Dry type granulating system for sulfonium
CN103706290A (en) * 2013-11-19 2014-04-09 南通新邦化工科技有限公司 New drum-type granulating method and granulating device
CN103922370A (en) * 2014-04-30 2014-07-16 刘清山 Method and device for preparing granular magnesium chloride
CN206121680U (en) * 2016-06-28 2017-04-26 深圳市芭田生态工程股份有限公司 Prilling granulator sprays in horizontal melting compound fertilizer

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Application publication date: 20161130