CN200974819Y - Air-cooled crystallization granulating device for full-fusion composite fertilizer - Google Patents
Air-cooled crystallization granulating device for full-fusion composite fertilizer Download PDFInfo
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- CN200974819Y CN200974819Y CN200620125635.5U CN200620125635U CN200974819Y CN 200974819 Y CN200974819 Y CN 200974819Y CN 200620125635 U CN200620125635 U CN 200620125635U CN 200974819 Y CN200974819 Y CN 200974819Y
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- 239000003337 fertilizer Substances 0.000 title claims abstract description 23
- 238000002425 crystallisation Methods 0.000 title claims abstract description 11
- 230000008025 crystallization Effects 0.000 title claims abstract description 11
- 239000002131 composite material Substances 0.000 title 1
- 238000005469 granulation Methods 0.000 claims abstract description 32
- 230000003179 granulation Effects 0.000 claims abstract description 32
- 150000001875 compounds Chemical class 0.000 claims abstract description 21
- 239000000463 material Substances 0.000 claims description 4
- 238000006243 chemical reaction Methods 0.000 claims description 3
- 238000001816 cooling Methods 0.000 abstract description 14
- 239000002245 particle Substances 0.000 abstract description 8
- 239000002002 slurry Substances 0.000 abstract description 8
- 239000000428 dust Substances 0.000 abstract description 7
- 230000000694 effects Effects 0.000 abstract description 4
- 239000000203 mixture Substances 0.000 abstract 1
- 238000007493 shaping process Methods 0.000 abstract 1
- 238000000034 method Methods 0.000 description 10
- 238000005265 energy consumption Methods 0.000 description 7
- 238000004519 manufacturing process Methods 0.000 description 3
- 238000007664 blowing Methods 0.000 description 2
- 238000007710 freezing Methods 0.000 description 2
- 230000008014 freezing Effects 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 235000015097 nutrients Nutrition 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 238000009423 ventilation Methods 0.000 description 1
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
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Abstract
Description
技术领域technical field
本实用新型涉及一种复合肥的造粒装置,尤其是一种全熔融复合肥的风冷结晶造粒设备,具体地说是一种全熔融复合肥的风冷结晶造粒装置。The utility model relates to a compound fertilizer granulation device, in particular to an air-cooled crystallization granulation device for full-melt compound fertilizer, in particular to an air-cooled crystallization granulator for full-melt compound fertilizer.
背景技术Background technique
近年来,我国生产全熔融复合肥(即NPK复合肥)的生产工艺得到了很大的提高,传统的圆盘造粒、挤压造料、转鼓造粒等传统工艺已日臻成熟,但传统工艺存在效率低,成品外观差、能耗高等一系列问题,为此人们实用新型了塔式造粒新工艺,这种工艺制造出来的产品外观圆润,养分准确均匀,肥料利用率高,一经推出即大受欢迎。但这种工艺存在的主要问题是为了增加冷却效果,其塔身大都在100米以上,塔径也在12以上,投资大,造价高,占地面积大,对安全要求高,物料的输送和提升难度很大,能耗也比较高,为此,人们在塔高和能耗上做了大量研究,为此,中国专利021349711提出了一种低塔生产工艺及设备,中国专利200510038702.X提出了一种利用冷冻造粒的方法及其装置,它们在降低塔身高度上均有创造性意义。这二种方法及装置在实际使用中仍存在以下问题:一是增加了粉尘,而且粉尘容易与塔壁粘连,需定期停产清理;二是成品颗粒的外观度较差,无法与高塔相媲美,颗粒之间容易粘连;三是适应性差,每个造粒塔可造的复合肥的配方变化不能太大,否则将无法正常工作,不同配方的产品调节困难;四是投资仍然较大。正是由于上述原因,致使它们难以大面积推广使用。In recent years, the production process of producing full-melt compound fertilizer (ie NPK compound fertilizer) in my country has been greatly improved. The process has a series of problems such as low efficiency, poor appearance of the finished product, and high energy consumption. For this reason, people have developed a new tower granulation process. The products produced by this process have a round appearance, accurate and uniform nutrients, and high fertilizer utilization. Once launched That is, a big hit. However, the main problem of this process is that in order to increase the cooling effect, the tower body is mostly more than 100 meters, and the tower diameter is also more than 12. The investment is large, the cost is high, the floor area is large, and the safety requirements are high. It is very difficult to upgrade, and the energy consumption is relatively high. Therefore, people have done a lot of research on tower height and energy consumption. For this reason, Chinese patent 021349711 proposes a low-tower production process and equipment, and Chinese patent 200510038702.X proposes A method and device utilizing freezing granulation are proposed, and they all have creative significance in reducing the height of the tower body. These two methods and devices still have the following problems in actual use: one is that the dust is increased, and the dust is easy to stick to the tower wall, which requires regular shutdown and cleaning; the other is that the appearance of the finished particles is poor, which cannot be compared with the high tower , the particles are easy to stick together; the third is poor adaptability, the formula of the compound fertilizer that can be made by each prilling tower should not change too much, otherwise it will not work normally, and the adjustment of products with different formulas is difficult; the fourth is that the investment is still relatively large. Just because of above-mentioned reasons, cause them to be difficult to popularize and use on a large scale.
发明内容Contents of the invention
本实用新型的目的是针对现有的低塔造粒存在的成粒效果差、易产生粘壁粉尘和产品配比调节难度大的问题,实用新型一种成形好、投资少、能耗低的、适合于低塔使用的全熔融复合肥的风冷结晶造粒装置。The purpose of this utility model is to solve the problems of poor granulation effect, easy generation of sticky wall dust and difficult adjustment of product ratio in the existing low-tower granulation. , An air-cooled crystallization granulation device suitable for full-melt compound fertilizers used in low towers.
本实用新型的技术方案是:The technical scheme of the utility model is:
一种全熔融复合肥的风冷结晶造粒装置,包括造粒塔1、旋转造粒头2、风机3、抽风机4,该造料塔1的塔高为15-50米,塔径为6-12米,旋转造粒头2安装在造粒塔1内侧顶部中心位置处,其特征是所述的抽风机4安装在造粒塔1的顶部、旋转造粒头2的周围,抽风机4的进风口与造粒塔1的内腔相通;在距离旋转造粒头2垂直距离为4米以下(含4米)的造粒塔塔身上安装有3-5圈、每圈由若干台风机3组成的环形送风机组5,所述的环形送风机组5之间的距离为1.5-4米;An air-cooled crystallization granulation device for fully molten compound fertilizers, comprising a
所述的风机3的送风方向与水平面的夹角α为15-45度,与所在点塔径线之间的夹角β为80-85度。The included angle α between the air supply direction of the
所述的抽风机4垂直安装在造粒塔1的顶部,其数量为4-8台。The
每圈环形送风机组5由20-40台风机3组成,每圈环形送风机组5均安装有用于统一调节风量的变频调速器。Each circle of annular
本实用新型具有以下优点:The utility model has the following advantages:
1、本实用新型的方法工艺紧凑、产品成形好,投资少,能耗低,它通过在造粒成形塔中部安装多排横向切风鼓风装置及在塔顶安装多台抽风设备一方面产生向上的负压,另一方面快速将多余的热量排出塔外,大幅度减少了复合肥颗粒的固化时间,降低了造粒成形塔的高度和直径,可大大节省投资成本,减少运行成本。1. The method of the utility model has compact technology, good product forming, less investment, and low energy consumption. It is produced by installing multiple rows of transverse wind cutting and blowing devices in the middle of the granulation forming tower and installing multiple exhaust devices on the top of the tower. On the other hand, the upward negative pressure quickly discharges excess heat out of the tower, greatly reducing the curing time of compound fertilizer particles, reducing the height and diameter of the granulation forming tower, which can greatly save investment costs and reduce operating costs.
2、与现有的低塔和冷冻塔相比可减少投资50%-70%,同时生产规模可根据需要调节,可大可小。2. Compared with the existing low tower and freezing tower, the investment can be reduced by 50%-70%. At the same time, the production scale can be adjusted according to the needs, which can be large or small.
3、可生产高中低不同浓度的复合肥,改变配方十分方便,配方比例范围大,对于不同配比的复合肥可通过变频调节器调节送风量将冷却时间调整到合适的范围,防止过冷和冷却不足现象的发生。3. It can produce compound fertilizers with different concentrations of high, medium and low. It is very convenient to change the formula, and the formula ratio range is large. For compound fertilizers with different ratios, the air supply volume can be adjusted through the frequency conversion regulator to adjust the cooling time to an appropriate range to prevent overcooling. and the occurrence of insufficient cooling.
4、不会产生粉尘粘壁现象,无需定期清理塔壁,复合肥浆料颗粒以涡旋状在塔身内缓慢下降可使得粉尘随颗粒一起下降,不会产生目前的扬尘现象。4. There will be no dust sticking to the wall, and there is no need to regularly clean the tower wall. The particles of the compound fertilizer slurry will slowly descend in the tower body in a vortex shape, so that the dust will fall together with the particles, and the current dust phenomenon will not occur.
5、产品的均匀度好,成品率可高达99%以上,且操控性能。5. The uniformity of the product is good, the yield rate can be as high as 99%, and the control performance is excellent.
6、可在全天候条件下工作,解决了现有的工艺存在的高温、高湿条件下无法正常生产的矛盾,可在高温高湿条件下全天候正常生产。6. It can work under all-weather conditions, which solves the contradiction that the existing process cannot produce normally under high-temperature and high-humidity conditions, and can work normally under high-temperature and high-humidity conditions around the clock.
7、能耗低,一方面降低了塔高,减少了物料输送的能耗,另一方面通过采用节能鼓风机,可大大减少能源损耗。7. Low energy consumption. On the one hand, the height of the tower is reduced, which reduces the energy consumption of material transportation. On the other hand, energy consumption can be greatly reduced by using energy-saving blowers.
附图说明Description of drawings
图1是本实用新型的结构示意图。Fig. 1 is the structural representation of the utility model.
图2是本实用新型的风机的水平方向安装角度示意图。Fig. 2 is a schematic diagram of the installation angle of the fan in the horizontal direction of the utility model.
具体实施方式Detailed ways
下面结构附图和实施例对本实用新型作进一步的说明。The following structural drawings and embodiments further illustrate the utility model.
一种全熔融复合肥的风冷结晶造粒装置,如图1、2所示,它包括造粒塔1、旋转造粒头2、风机3、抽风机4,该造料塔1的塔高为15-50米,塔径为6-12米,旋转造粒头2安装在造粒塔1内侧顶部中心位置处,在造粒塔1的顶部、旋转造粒头2的周围垂直安装有4-8台抽风机4,以便于将塔内的热量排出,抽风机4的进风口与造粒塔1的内腔相通;在距离旋转造粒头2垂直距离为4米以下(如4米位置处)的造粒塔塔身上安装有3-5圈、每圈由20-40台风机3组成的环形送风机组5,每台风机3的送风量和送风速度可根据复合肥的种类、冷却速度和产量参考相关设计手册进行选择,所述的环形送风机组5之间的距离以1.5-4米为宜。为了取得理想的涡旋效果,减缓料浆的下降速度,使从造粒头出来的浆料迅速冷却,因此风机3的送风方向应进行合理的控制,风机3的送风方向与水平面的夹角α可在15-45度之间选择,与所在安装点塔径线之间的夹角β可在80-85度之间选择。每个环形送风机组5均带有各自的风量调节装置(如变频调速器)以便于统一调节送风量。An air-cooled crystallization granulation device for full-melt compound fertilizer, as shown in Figures 1 and 2, it includes a
此外,具体实施时的送风量可根据产量和塔径加以确定。In addition, the air supply volume during specific implementation can be determined according to the output and tower diameter.
本实用新型未涉及部分均与现有技术相同。The parts not involved in the utility model are all the same as the prior art.
与本实用新型相配套的方法包括以下步骤:The method matched with the utility model comprises the following steps:
第一步,将全熔融状态下的复合肥料浆从位于塔高为15-50,塔径为6-12米的造粒塔的顶部的旋转造粒头中喷出;In the first step, the compound fertilizer slurry in the fully molten state is sprayed from the rotary granulation head located at the top of the prilling tower with a tower height of 15-50 meters and a tower diameter of 6-12 meters;
第二步,在离造粒头垂直距离为4米以下(含4米)位置的造粒塔塔身周围安装第一组向塔内吹风的冷却风机,使每台风机的出风方向与水平面的夹角为15-45度,与直径夹角为80-85度的方向向塔向输送冷却用风,控制送风速度为2-10米/秒,风压为100-400Pa,以保证冷却速度,并通过风机的合理配置(即调整风机送风的方向、角度)使由风机送风的冷却用风在塔内形成涡旋状空气幕,从而减缓旋转造粒头中喷出的颗粒状料浆的下降速度,使料浆的各个面与风机送来的冷却用风充分接触,使其表面快速结晶;与此同时在造粒塔顶上安装起通风和产生负压的抽风机,将塔内浆料的热量快速抽出塔外;The second step is to install the first group of cooling fans blowing into the tower around the prilling tower body at a position of less than 4 meters (including 4 meters) from the prilling head, so that the air outlet direction of each fan is in line with the horizontal plane. The included angle is 15-45 degrees, and the direction with the diameter of 80-85 degrees is used to deliver cooling air to the tower. The air supply speed is controlled at 2-10 m/s, and the air pressure is 100-400 Pa to ensure cooling. Speed, and through the reasonable configuration of the fan (that is, adjusting the direction and angle of the fan's air supply), the cooling wind blown by the fan forms a vortex-shaped air curtain in the tower, thereby slowing down the granularity ejected from the rotating granulation head. The descending speed of the slurry makes each surface of the slurry fully contact with the cooling wind sent by the fan, so that the surface crystallizes rapidly; at the same time, an exhaust fan for ventilation and negative pressure is installed on the top of the prilling tower to The heat of the slurry in the tower is quickly drawn out of the tower;
第三步,在距第一组冷却风机下方每隔为1.5-4米设置一组、共设计两组或两组以上的、与第二步相同的冷却风机组,以使经第一冷却风机组冷却后基本成形的晶粒进一步冷却,沉降到塔底后,在塔底得到粒状复合肥;The third step is to set up a set of 1.5-4 meters apart from the first group of cooling fans, and design two or more sets of cooling fans that are the same as the second step, so that the first cooling air After the unit is cooled, the basically formed grains are further cooled, and after settling to the bottom of the tower, granular compound fertilizer is obtained at the bottom of the tower;
第四步,将上述第三步得到的粒状复合肥通过输送带送出塔外进行自然冷却即可。In the fourth step, the granular compound fertilizer obtained in the third step above is sent out of the tower through a conveyor belt for natural cooling.
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2010148983A1 (en) * | 2009-06-26 | 2010-12-29 | Dai Liangyu | Method for pelleting spherical fine particle of sodium nitrate |
| CN117146281A (en) * | 2023-10-30 | 2023-12-01 | 江苏大恒环境技术有限公司 | Ash discharging device for salt-containing waste liquid incinerator |
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2006
- 2006-12-05 CN CN200620125635.5U patent/CN200974819Y/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2010148983A1 (en) * | 2009-06-26 | 2010-12-29 | Dai Liangyu | Method for pelleting spherical fine particle of sodium nitrate |
| CN117146281A (en) * | 2023-10-30 | 2023-12-01 | 江苏大恒环境技术有限公司 | Ash discharging device for salt-containing waste liquid incinerator |
| CN117146281B (en) * | 2023-10-30 | 2024-03-05 | 江苏大恒环境技术有限公司 | Ash discharging device for salt-containing waste liquid incinerator |
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