CN204865414U - Chemical fertilizer production dust collector - Google Patents
Chemical fertilizer production dust collector Download PDFInfo
- Publication number
- CN204865414U CN204865414U CN201520575357.2U CN201520575357U CN204865414U CN 204865414 U CN204865414 U CN 204865414U CN 201520575357 U CN201520575357 U CN 201520575357U CN 204865414 U CN204865414 U CN 204865414U
- Authority
- CN
- China
- Prior art keywords
- expansion chamber
- dust
- bag
- chemical fertilizer
- room
- 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 - Lifetime
Links
Landscapes
- Filtering Of Dispersed Particles In Gases (AREA)
Abstract
本实用新型公开了一种化肥生产除尘装置,包括沉降室、绞龙、袋式除尘室和引风机;沉降室左侧的顶部设有与含尘尾气管道连接入气口,沉降室内部与袋式除尘室连通,绞龙位于沉降室和袋式除尘室的下方并且贯穿于沉降室和袋式除尘室,沉降室和袋式除尘室的尾端分别设有清尘口,袋式除尘室的出口通过通风道与引风机连接,引风机的出口与排风管连接。本除尘装置降低了生产现场空气中的粉尘含量,改善了生产现场的工作环境,保障了操作工人的健康安全。同时也集中收集了粉尘物料,减少了工人的劳动强度,节约了生产成本。
The utility model discloses a dust removal device for chemical fertilizer production, which comprises a settling chamber, an auger, a bag-type dedusting chamber and an induced draft fan; The dust removal room is connected, and the auger is located below the settling chamber and the bag type dust removal room and runs through the settling room and the bag type dust removal room. It is connected with the induced draft fan through the ventilation channel, and the outlet of the induced draft fan is connected with the exhaust pipe. The dust removal device reduces the dust content in the air of the production site, improves the working environment of the production site, and ensures the health and safety of the operating workers. At the same time, dust materials are collected in a concentrated manner, which reduces the labor intensity of workers and saves production costs.
Description
技术领域technical field
本实用新型涉及一种化肥生产除尘装置。The utility model relates to a dust removal device for chemical fertilizer production.
背景技术Background technique
硝基复肥的生产除尘装置,原建设设计是利用旋风除尘进行对生产现场除尘,但旋风除尘效果不太明显,经过实际的试运行,塔上粉尘量过高,经测量空气中粉尘量达28mg/m3,不但污染现场操作环境,而且每小时都需要安排专人进行清理,增加了工人劳动强度,同时也严重影响工人的健康安全,严重的粉尘流失导致物料消耗的增加,为企业带来环保压力问题的同时成为制约生产的瓶颈问题。The original construction design of the dust removal device for the production of nitro compound fertilizer is to use cyclone dust removal to remove dust from the production site, but the effect of cyclone dust removal is not obvious. After actual trial operation, the amount of dust on the tower is too high. 28mg/m 3 , not only pollute the on-site operating environment, but also need to arrange special personnel to clean up every hour, which increases the labor intensity of workers, and also seriously affects the health and safety of workers. Environmental pressure has become a bottleneck restricting production at the same time.
实用新型内容Utility model content
本实用新型为了解决上述问题,提出了一种化肥生产除尘装置,本除尘装置降低了生产现场空气中的粉尘含量,改善了生产现场的工作环境,保障了操作工人的健康安全。同时也集中收集了粉尘物料,减少了工人的劳动强度,节约了生产成本。In order to solve the above problems, the utility model proposes a dust removal device for chemical fertilizer production. The dust removal device reduces the dust content in the air of the production site, improves the working environment of the production site, and ensures the health and safety of the operators. At the same time, dust materials are collected in a concentrated manner, which reduces the labor intensity of workers and saves production costs.
为了实现上述目的,本实用新型采用如下技术方案:In order to achieve the above object, the utility model adopts the following technical solutions:
一种化肥生产除尘装置,包括沉降室、绞龙、袋式除尘室和引风机;沉降室左侧的顶部设有与含尘尾气管道连接的入气口,沉降室内部与袋式除尘室连通,绞龙位于沉降室和袋式除尘室的下方并且贯穿于沉降室和袋式除尘室,沉降室和袋式除尘室的尾端分别设有清尘口,袋式除尘室的出口通过通风道与引风机连接,引风机的出口与排风管连接。含尘尾气通过入气口进入除尘装置,依次通过沉降室、袋式除尘室,最后由引风机将净化后的尾气排出,在除尘设备内部沉降的粉尘由绞龙运送至清尘口排出。整个除尘过程简单、紧凑。A dust removal device for chemical fertilizer production, including a settling chamber, an auger, a bag-type dust removal chamber and an induced draft fan; the top of the left side of the settling chamber is provided with an air inlet connected to the dust-containing tail gas pipeline, and the inside of the settling chamber is communicated with the bag-type dust removal chamber. The auger is located below the settling chamber and the baghouse and runs through the settling chamber and the baghouse. The tail ends of the settling chamber and the baghouse are respectively equipped with dust cleaning ports, and the outlet of the baghouse passes through the air duct and The induced draft fan is connected, and the outlet of the induced draft fan is connected with the exhaust pipe. The dust-laden exhaust gas enters the dust removal device through the air inlet, passes through the settling chamber, the bag-type dust removal chamber in turn, and finally the purified exhaust gas is discharged by the induced draft fan. The whole dust removal process is simple and compact.
所述沉降室包括第一沉降室、第二沉降室、第三沉降室和滤尘板,沉降室为长方体,内部为空腔结构,从左到右依次为第一沉降室、第二沉降室和第三沉降室,相邻的两个沉降室用滤尘板隔开。多个沉降室和多个滤尘板构造的设置,能够减缓含尘尾气的流动速度,有助于提高沉降效果,加快沉降效率。The settling chamber includes a first settling chamber, a second settling chamber, a third settling chamber and a dust filter plate. The settling chamber is a cuboid with a cavity structure inside. From left to right are the first settling chamber, the second settling chamber and the In the third settling chamber, two adjacent settling chambers are separated by a dust filter plate. The setting of multiple settling chambers and multiple dust filter plate structures can slow down the flow velocity of the dust-laden exhaust gas, help to improve the settling effect and accelerate the settling efficiency.
所述袋式除尘室包括袋沉室和袋式除尘器,袋式除尘器安装在袋沉室的上方。袋式除尘器是一种高效的干式除尘器。它是依靠纤维滤料做成的滤袋,更主要的是通过滤袋表面上形成的粉尘层来净化气体的。适用范围广,除尘效率高,可达到99%以上。The baghouse includes a baghouse and a baghouse, and the baghouse is installed above the baghouse. The bag filter is a highly efficient dry dust collector. It is a filter bag made of fiber filter material, and more importantly, it purifies the gas through the dust layer formed on the surface of the filter bag. It has a wide range of applications and high dust removal efficiency, which can reach more than 99%.
所述沉降室和袋式除尘室的横截面上面为一长方形,下方为倒锥形,倒锥形底部为圆弧形。下部倒锥形和圆弧形的设计,可利用粉尘自身的重力作用自动收集到绞龙的运行路线上,无需另外提供动力。The cross section of the settling chamber and the bag-type dust removal chamber is a rectangle above, and an inverted cone below, and the bottom of the inverted cone is arc-shaped. The inverted cone and arc-shaped design of the lower part can use the gravity of the dust itself to automatically collect it on the running route of the auger without additional power.
所述滤尘板上设有若干通孔,同组使用的滤尘板,在沉降室至袋式除尘室的方向上滤尘板孔径依次减小。根据含尘尾气中的含尘量设计不同孔径的滤尘板,使滤尘板在不堵塞的前提下拥有更高的沉降效果。The dust filter plate is provided with a number of through holes, and the dust filter plates used in the same group, the pore diameter of the dust filter plate decreases successively in the direction from the settling chamber to the baghouse. Design dust filter plates with different apertures according to the dust content in the dusty exhaust gas, so that the dust filter plates have a higher settling effect without clogging.
所述滤尘板内部安装有超声波振动器。经过长时间的沉降,滤尘板上容易堆积粉尘,如果停机清理会造成不小的损失,安装超声波振动器可以对滤尘板进行自动清理,延长滤尘板的使用寿命。An ultrasonic vibrator is installed inside the dust filter plate. After a long period of settlement, dust is easy to accumulate on the dust filter plate. If it is shut down for cleaning, it will cause a lot of losses. Installing an ultrasonic vibrator can automatically clean the dust filter plate and prolong the service life of the dust filter plate.
所述沉降室内安装有静电除尘棒。含尘气体经过高压静电场时被电分离,尘粒与负离子结合带上负电后,趋向阳极表面放电而沉积,具有除尘效率高,除尘粒子粒径范围宽,结构简单的特点。Electrostatic dust removal rods are installed in the settling chamber. The dust-containing gas is electrically separated when it passes through a high-voltage electrostatic field. After the dust particles are combined with negative ions and charged with negative charges, they tend to discharge and deposit on the surface of the anode. It has the characteristics of high dust removal efficiency, wide particle size range and simple structure.
本实用新型的有益效果为:The beneficial effects of the utility model are:
(1)本实用新型解决了化肥生产过程中,空气内部粉尘量严重的问题;(1) The utility model solves the problem of serious dust in the air during the fertilizer production process;
(2)本实用新型改善了生产环境,减少了卫生清理的次数,节约了劳动力,减轻了工人的劳动强度并且保证了工人的健康安全;(2) The utility model improves the production environment, reduces the number of sanitation cleaning, saves labor, reduces the labor intensity of workers and ensures the health and safety of workers;
(3)本实用新型回收了大量可以作为原料回加的粉尘,降低了生产成本。(3) The utility model reclaims a large amount of dust that can be added back as raw materials, which reduces the production cost.
附图说明Description of drawings
图1是本实用新型整体结构示意图;Fig. 1 is a schematic diagram of the overall structure of the utility model;
图2是本实用新型的沉降室结构示意图;Fig. 2 is the structural representation of the settling chamber of the present utility model;
图3是本实用新型的袋式除尘室结构示意图;Fig. 3 is a schematic structural view of the bag-type dust removal chamber of the present invention;
图4是本实用新型的沉降室断面结构示意图;Fig. 4 is the schematic diagram of the section structure of the settling chamber of the present utility model;
其中,1、沉降室,2、绞龙,3、清尘口,4、袋式除尘室,5、引风机,6、排风管,7、通风道,8、入气口,11、第一沉降室,12、滤尘板,13、第二沉降室,14、第三沉降室,41、袋沉室,42、袋式除尘器。Among them, 1. Settling chamber, 2. Auger, 3. Dust cleaning port, 4. Baghouse, 5. Induced fan, 6. Exhaust pipe, 7. Air duct, 8. Air inlet, 11. First Settling chamber, 12, dust filter plate, 13, second settling chamber, 14, third settling chamber, 41, bag settling chamber, 42, bag filter.
具体实施方式:Detailed ways:
下面结合附图与实施例对本实用新型作进一步说明。Below in conjunction with accompanying drawing and embodiment the utility model is further described.
如图1所示,一种化肥生产除尘装置,包括沉降室1、绞龙2、袋式除尘室4和引风机5;沉降室1左侧的顶部设有与含尘尾气管道连接的入气口8,含尘尾气进入沉降室1发生沉降,沉降后的粉尘落到沉降室1的底部,沉降室1内部与袋式除尘室4连通,通过沉降室1的沉降大部分粉尘被消除,进入袋式除尘室4后粉尘再次进行沉降并落到袋式除尘室4的底部。绞龙2位于沉降室1和袋式除尘室4的下方并且贯穿于沉降室1和袋式除尘室4,沉降室1和袋式除尘室4的尾端分别设有清尘口3,通过绞龙2的转动,绞龙2上的螺旋叶片推动粉尘到达清尘口3,清尘口3与废料回收箱连接,粉尘落入废料箱。袋式除尘室4的出口通过通风道7与引风机5连接,为含尘尾气提供动力。最后处理后的含尘尾气通过排风管6排出。As shown in Figure 1, a dust removal device for chemical fertilizer production includes a settling chamber 1, an auger 2, a bag-type dust removal chamber 4 and an induced draft fan 5; the top of the left side of the settling chamber 1 is provided with an air inlet connected to a dusty tail gas pipeline 8. The dust-containing tail gas enters the settling chamber 1 and settles. The settled dust falls to the bottom of the settling chamber 1. The interior of the settling chamber 1 is connected with the bag filter chamber 4. Most of the dust is eliminated through the settling chamber 1 and enters the bag. After the bag type dust removal chamber 4, the dust settles again and falls to the bottom of the bag type dust removal chamber 4. The auger 2 is located below the settling chamber 1 and the baghouse 4 and runs through the settling chamber 1 and the baghouse 4. The tail ends of the settling chamber 1 and the baghouse 4 are respectively provided with a dust cleaning port 3. With the rotation of the dragon 2, the helical blades on the auger 2 push the dust to reach the dust removal port 3, and the dust removal port 3 is connected with the waste recycling bin, and the dust falls into the waste bin. The outlet of the baghouse 4 is connected with the induced draft fan 5 through the air passage 7, so as to provide power for the dusty tail gas. The dusty tail gas after the final treatment is discharged through the exhaust pipe 6 .
如图2所示,沉降室1包括第一沉降室11、第二沉降室13、第三沉降室14和滤尘板12,分为三级,并且由滤尘板12隔开。沉降室1为长方体,内部为空腔结构,从左到右依次为第一沉降室11、第二沉降室13和第三沉降室14。相邻的两个沉降室1用滤尘板12隔开。同组使用的滤尘板12,在沉降室至袋式除尘室的方向上滤尘板孔径依次减小,含尘尾气进入沉降室1后,依次通过第一、二、三沉降室。经过滤尘板12的阻挡,使大部分的粉尘落到沉降室1的底部。As shown in FIG. 2 , the settling chamber 1 includes a first settling chamber 11 , a second settling chamber 13 , a third settling chamber 14 and a dust filter plate 12 , which are divided into three stages and separated by the dust filter plate 12 . The settling chamber 1 is a cuboid with a cavity structure inside, and from left to right there are first settling chamber 11 , second settling chamber 13 and third settling chamber 14 . Two adjacent settling chambers 1 are separated by a dust filter plate 12 . For the dust filter plates 12 used in the same group, the pore diameters of the dust filter plates decrease successively in the direction from the settling chamber to the baghouse, and after the dust-laden tail gas enters the settling chamber 1, it passes through the first, second, and third settling chambers in sequence. After being blocked by the dust filter plate 12, most of the dust falls to the bottom of the settling chamber 1.
作为一种改进,沉降室1内安装静电除尘棒,含尘尾气中的粉尘由于快速运动和高温容易产生静电,不容易沉降,安装静电除尘棒后会与粉尘的电性中和,加速粉尘的沉降。As an improvement, an electrostatic dust removal rod is installed in the settling chamber 1. The dust in the dusty tail gas is prone to static electricity due to fast movement and high temperature, and is not easy to settle. After the electrostatic dust removal rod is installed, it will be electrically neutralized with the dust, and the dust will be accelerated. settlement.
作为一种改进,滤尘板12内部安装超声波振动器,在滤尘板12净化含尘尾气过程中,超声波振动器震动,减少粉尘在滤尘板12上的堆积,增加滤尘板12的使用寿命,延长滤尘板12的使用周期。As an improvement, an ultrasonic vibrator is installed inside the dust filter plate 12. When the dust filter plate 12 purifies the dusty exhaust gas, the ultrasonic vibrator vibrates to reduce the accumulation of dust on the dust filter plate 12, increase the service life of the dust filter plate 12, and prolong the dust filter. The life cycle of the board 12.
如图3所示,袋式除尘室4分为上下两部分,分别为袋式除尘器42和袋沉室41。含尘尾气经过沉降室1的过滤后进入袋式除尘室4,在袋沉室41内进行短暂的降尘,进入袋式除尘器42进行进一步的除尘。As shown in FIG. 3 , the baghouse 4 is divided into upper and lower parts, which are respectively a baghouse 42 and a baghouse 41 . The dust-laden tail gas enters the bag filter chamber 4 after being filtered by the settling chamber 1 , conducts short-term dust reduction in the bag filter chamber 41 , and enters the bag filter 42 for further dust removal.
如图4所示,沉降室1和袋式除尘室4的横截面上面为一长方形,下方为倒锥形,倒锥形底部为圆弧形,恰好与绞龙2配合安装。含尘尾气沉降下来的粉尘落到沉降室1和袋式除尘室4的底部,再经倒锥形的底面滑入圆弧形粉槽,由绞龙2的转动推动粉料运动之清尘口3。As shown in Figure 4, the cross-section of the settling chamber 1 and the baghouse 4 is a rectangle at the top, an inverted cone at the bottom, and an arc-shaped bottom of the inverted cone, which fits well with the auger 2 for installation. The dust settled by the dusty tail gas falls to the bottom of the settling chamber 1 and the bag dust chamber 4, and then slides into the arc-shaped powder chute through the inverted conical bottom surface, and the rotation of the auger 2 pushes the dust-cleaning port of the powder movement. 3.
上述虽然结合附图对本实用新型的具体实施方式进行了描述,但并非对本实用新型保护范围的限制,所属领域技术人员应该明白,在本实用新型的技术方案的基础上,本领域技术人员不需要付出创造性劳动即可做出的各种修改或变形仍在本实用新型的保护范围以内。Although the specific implementation of the utility model has been described above in conjunction with the accompanying drawings, it does not limit the protection scope of the utility model. Those skilled in the art should understand that on the basis of the technical solution of the utility model, those skilled in the art do not need to Various modifications or deformations that can be made with creative efforts are still within the protection scope of the present utility model.
Claims (7)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520575357.2U CN204865414U (en) | 2015-07-31 | 2015-07-31 | Chemical fertilizer production dust collector |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520575357.2U CN204865414U (en) | 2015-07-31 | 2015-07-31 | Chemical fertilizer production dust collector |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204865414U true CN204865414U (en) | 2015-12-16 |
Family
ID=54809850
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520575357.2U Expired - Lifetime CN204865414U (en) | 2015-07-31 | 2015-07-31 | Chemical fertilizer production dust collector |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204865414U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107649393A (en) * | 2017-09-20 | 2018-02-02 | 贵州贵天下茶业有限责任公司 | A kind of wild black tea dust pelletizing system and dust removal method |
-
2015
- 2015-07-31 CN CN201520575357.2U patent/CN204865414U/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107649393A (en) * | 2017-09-20 | 2018-02-02 | 贵州贵天下茶业有限责任公司 | A kind of wild black tea dust pelletizing system and dust removal method |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN109663449A (en) | A kind of wet type inertial dust separator | |
| CN204919443U (en) | Sweeping machine dust pelletizing system and have its sweeping machine | |
| CN104888571A (en) | Industrial flue gas dust removal device | |
| CN103252146B (en) | A kind of vertical electrostatic precipitator integrating gravity, cyclone dust collection | |
| CN105126552B (en) | A kind of screw concrete formula dedusting recovery system | |
| CN104056720B (en) | A kind of compound type dust remover | |
| CN102553732A (en) | Backflow circulation cyclone separator | |
| CN204901803U (en) | Production boiler | |
| CN204767913U (en) | Sack cleaner based on intelligent control device | |
| CN101518703B (en) | Inertial dust precollecting air flow uniform distribution device | |
| CN204672560U (en) | A kind of Sound-proof material granulated slag separator | |
| CN208032127U (en) | A kind of bag filter with part flow arrangement | |
| CN104128058A (en) | Vertical electrical dust collector integrating gravity and cyclone dust removal | |
| CN105128153B (en) | A kind of concrete concentrated dust collecting system | |
| CN104128056A (en) | Horizontal electrical dust collector integrating gravity and cyclone dust removal | |
| CN205240752U (en) | Dust removal selection by winnowing pipe tobacco recovery unit | |
| CN203235383U (en) | Horizontal electrostatic precipitator integrating gravity and cyclone dust removal | |
| CN103263815B (en) | Horizontal electric dust collector with integrated gravity cyclone dust collection function | |
| CN204530574U (en) | Road sweeper and its dust removal system | |
| CN204637882U (en) | A kind of vehicle carried dust cleaning apparatus | |
| CN202162143U (en) | Dedusting type vibrating screen | |
| CN208098851U (en) | A kind of sintering machine exhausting is responsible for the attachment device into head electric precipitator | |
| CN201669012U (en) | A flow guide device for a long bag type bag filter | |
| CN209490635U (en) | A kind of deduster | |
| CN201030328Y (en) | Compound electrostatic precipitator |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term | ||
| CX01 | Expiry of patent term |
Granted publication date: 20151216 |