CN110339663A - A spray dust removal equipment with wind direction changing technology - Google Patents
A spray dust removal equipment with wind direction changing technology Download PDFInfo
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- CN110339663A CN110339663A CN201910739741.4A CN201910739741A CN110339663A CN 110339663 A CN110339663 A CN 110339663A CN 201910739741 A CN201910739741 A CN 201910739741A CN 110339663 A CN110339663 A CN 110339663A
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- 239000007921 spray Substances 0.000 title claims abstract description 106
- 239000000428 dust Substances 0.000 title claims abstract description 40
- 238000005516 engineering process Methods 0.000 title claims abstract description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 71
- 238000005507 spraying Methods 0.000 claims abstract description 5
- 238000001914 filtration Methods 0.000 claims description 2
- 230000006978 adaptation Effects 0.000 claims 1
- 230000000694 effects Effects 0.000 abstract description 5
- 238000004887 air purification Methods 0.000 abstract description 3
- 239000004576 sand Substances 0.000 abstract description 2
- 238000011084 recovery Methods 0.000 description 15
- 239000007789 gas Substances 0.000 description 8
- 238000000746 purification Methods 0.000 description 3
- 239000007788 liquid Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- 239000002912 waste gas Substances 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 1
- 230000000295 complement effect Effects 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000004927 fusion Effects 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 239000013049 sediment Substances 0.000 description 1
- 238000009987 spinning Methods 0.000 description 1
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D50/00—Combinations of methods or devices for separating particles from gases or vapours
- B01D50/60—Combinations of devices covered by groups B01D46/00 and B01D47/00
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Abstract
Description
技术领域technical field
本发明涉及喷淋除尘领域,尤其是一种具有风向变轨技术的喷淋除尘设备。The invention relates to the field of spray dust removal, in particular to a spray dust removal device with wind direction changing technology.
背景技术Background technique
现有一些用于棉绒粉尘处理的设备,为了达到国家要求的排放标准,势必会增加内部旋流板和喷淋头的数量,因此喷淋塔的高度普遍在五米以上,有些会达到七八米,这种高度对于标准厂房来说,根本放不下,限制了这种处理设备的实用性,同时,经处理后的气体粉尘浓度不理想,由于旋流板,喷淋头等增多,也加大了电能的损耗。Some existing equipment for lint dust treatment, in order to meet the emission standards required by the country, will inevitably increase the number of internal swirl plates and spray heads, so the height of the spray tower is generally more than five meters, and some will reach seven Eight meters, this height is too high for a standard factory building, which limits the practicability of this treatment equipment. At the same time, the concentration of gas dust after treatment is not ideal. Increased power loss.
发明内容Contents of the invention
针对现有技术存在的补足,本发明提供一种具有风向变轨技术的喷淋除尘设备,本设备可以大大降低喷淋塔的高度,降低粉尘排放浓度,同时将水资源循环使用,节能环保。Aiming at the complement of the existing technology, the present invention provides a spray dust removal equipment with wind direction changing technology. This equipment can greatly reduce the height of the spray tower, reduce the dust emission concentration, and at the same time recycle water resources, which is energy-saving and environmentally friendly.
本发明提供一种具有风向变轨技术的喷淋除尘设备,包括进气管、进水管、喷淋头、喷淋塔、排气管、回收水箱、水泵;所述的进气管与喷淋塔底部固定连接,所述的喷淋头与进水管连接,所述的水泵设置在进水管与回收水箱之间,所述的水泵可以将水送至喷淋头,所述的排气管设置在喷淋塔的顶部,粉尘气体进入喷淋塔并过滤处理后通过排气管排出去;其特征是:所述的喷淋头设置在进气管内,进水支管一端连接有进水管,另一端穿入进气管,喷淋头设置在进水支管上,可以360°喷射;所述的进气管与喷淋塔连接的端部设置有向下弯的弯头;所述的喷淋塔内设置有旋流板;所述的喷淋塔底部设置有排水口,通过排水管排到回收水箱。The invention provides a spray dust removal equipment with wind direction changing technology, which includes an air inlet pipe, a water inlet pipe, a spray head, a spray tower, an exhaust pipe, a recovery water tank, and a water pump; the air inlet pipe and the bottom of the spray tower Fixed connection, the sprinkler head is connected to the water inlet pipe, the water pump is set between the water inlet pipe and the recovery water tank, the water pump can send water to the sprinkler head, and the exhaust pipe is set in the sprayer At the top of the shower tower, the dust gas enters the spray tower and is discharged through the exhaust pipe after being filtered; the feature is: the spray head is set in the air intake pipe, one end of the water inlet branch pipe is connected to the water inlet pipe, and the other end is passed through into the air inlet pipe, and the spray head is arranged on the water inlet branch pipe, which can be sprayed at 360°; the end of the air inlet pipe connected to the spray tower is provided with a downwardly bent elbow; the spray tower is provided with A swirl plate; the bottom of the spray tower is provided with a drain outlet, which is discharged to the recovery water tank through a drain pipe.
喷淋头设置在进气管内,水能大部分与棉绒粉尘混合,并沉淀在喷淋塔的底部,减少粉尘从喷淋塔排出的可能性,从而降低粉尘排出浓度。The sprinkler head is set in the air intake pipe, most of the water can be mixed with the lint dust and settle at the bottom of the spray tower, reducing the possibility of dust being discharged from the spray tower, thereby reducing the concentration of dust discharge.
进一步的设置是,所述的进气管设置有一次进气管和二次进气管,所述的喷淋塔设置有一次喷淋塔和二次喷淋塔;所述的进气管与一次喷淋塔的底部连接;所述的二次进气管一端连接在一次喷淋塔的顶部,一端连接在二次喷淋塔的底部;所述的排气管设置在二次喷淋塔的顶部;所述的一次进气管和二次进气管均设置有喷淋头。Further setting is, described air intake pipe is provided with primary air intake pipe and secondary air intake pipe, and described spray tower is provided with primary spray tower and secondary spray tower; Described air intake pipe and primary spray tower connected at the bottom; one end of the secondary air inlet pipe is connected to the top of the primary spray tower, and one end is connected to the bottom of the secondary spray tower; the exhaust pipe is arranged on the top of the secondary spray tower; Both the primary air intake pipe and the secondary air intake pipe are provided with sprinklers.
通过设置二次进气管和二次喷淋塔,增加粉尘在设备内的缓冲容积和时间,因此增加粉尘沉淀的可能性,有了二次喷淋,则一次喷淋塔的高度可以下比之前只有一次的处理的设备低,同时促进粉尘与谁混合,减少排出。By setting the secondary air inlet pipe and the secondary spray tower, the buffer volume and time of dust in the equipment are increased, so the possibility of dust precipitation is increased. With the secondary spray, the height of the primary spray tower can be lower than before Only one treatment equipment is low, and at the same time, it promotes the mixing of dust and reduces discharge.
进一步的,所述的喷淋塔内部设置有喷淋头。Further, a spray head is arranged inside the spray tower.
进一步的,所述喷淋头可以设置两个以上,所述的的旋流板可以设置两个以上,并且旋流板可同时正向设置或者同时反向设置。Further, more than two shower heads may be provided, more than two swirl plates may be provided, and the swirl plates may be arranged forwardly or backwardly at the same time.
进一步的,所述的回收水箱内部设置有过滤网,过滤网设置水平和竖直两块,横向长度与回收水箱宽度适配,过滤板将回收水箱隔成过滤出来的干净的水可以通过水泵进入进水管,进行循环利用。Further, the inside of the recovery water tank is provided with a filter screen, the filter screen is set in two pieces horizontally and vertically, the horizontal length is adapted to the width of the recovery water tank, and the filter plate separates the recovery water tank into filtered clean water that can enter through the water pump Inlet pipe for recycling.
通过上述方案设置,进气管经多层,即多路进水支管上的喷淋头360°无死角喷淋后,会行程泥沙俱下及强劲撞击想象,粉尘会从进气管的出口四处冲出,通过工艺改进,结构优化,在进气管出口设置弯头,从而改变方向,使泥沙充分溶解在喷淋塔的底部中,除尘效果及空气净化率显著提高;经过方案改进后,其效果是喷淋塔体制作上进一步矮化,降低成本,打破传统喷淋除尘系统在塔体设置需要多层正反旋流板,以用于延缓风速,提高除尘效果的惯例。Through the above scheme setting, the intake pipe passes through multiple layers, that is, after the spray head on the multi-channel water inlet branch pipe sprays 360° without dead angle, it will travel with mud and sand and strong impact imagination, and the dust will rush out from the outlet of the intake pipe. The process is improved, the structure is optimized, and an elbow is installed at the outlet of the air inlet pipe to change the direction, so that the sediment can be fully dissolved in the bottom of the spray tower, and the dust removal effect and air purification rate are significantly improved; after the program improvement, the effect is that the spray The production of the tower body is further dwarfed, the cost is reduced, and the traditional sprinkler dust removal system needs to be equipped with multi-layer positive and negative swirl plates on the tower body to delay the wind speed and improve the dust removal effect.
通过降低设备高度,适合有些厂房较低的场合,同时废气排放浓度远远优于国家标准,同时旋流板原先在一次喷淋塔内设置两层,必须正反设置的,现在一次喷淋塔内可以只设置一层,如果设置两层,也不需要同时正反设置。By reducing the height of the equipment, it is suitable for some occasions with low workshops. At the same time, the exhaust gas emission concentration is far superior to the national standard. At the same time, the swirl plate was originally installed with two layers in the primary spray tower, which must be set upside down. Now the primary spray tower Only one layer can be set inside, if two layers are set, there is no need to set the front and back at the same time.
附图说明Description of drawings
图1是本发明实施例的结构示意图。Fig. 1 is a schematic structural diagram of an embodiment of the present invention.
附图标记:1、一次进气管;2、水泵;3、进水管;4、喷淋头;5、一次喷淋塔;6、旋流板;7、二次进气管;8、排气管;9、二次喷淋塔;10、排水管;11、弯头;12、过滤网;13、回收水箱;31、进水支管。Reference signs: 1, primary air intake pipe; 2, water pump; 3, water inlet pipe; 4, spray head; 5, primary spray tower; 6, swirl plate; 7, secondary air intake pipe; 8, exhaust pipe 9. Secondary spray tower; 10. Drainage pipe; 11. Elbow; 12. Filter screen; 13. Recycling water tank;
具体实施方式Detailed ways
下面结合图1对本发明的技术方案作进一步详细说明,但不限于本说明。The technical solution of the present invention will be described in further detail below in conjunction with FIG. 1 , but is not limited to this description.
一种具有风向变轨技术的喷淋除尘设备包括进气管、进水管3、喷淋头4、喷淋塔、排气管8、回收水箱13、水泵2;所述的进气管与喷淋塔底部固定连接,所述的喷淋头4与进水管3连接,所述的水泵2设置在进水管3与回收水箱13之间,所述的水泵2可以将水送至喷淋头4,所述的排气管8设置在喷淋塔的顶部,粉尘气体进入喷淋塔并过滤处理后通过排气管8排出去;其特征是:所述的喷淋头4设置在进气管内,进水支管31一端连接有进水管3,另一端穿入进气管,喷淋头4设置在进水支管31的端部;所述的进气管与喷淋塔连接的端部设置有向下弯的弯头11;所述的喷淋塔内设置有旋流板6;所述的喷淋塔底部设置有排水口,通过排水管10排到回收水箱13。由于强劲的气流冲入进气管,在粉尘还未沉淀在喷淋塔底部,就会由于冲力使部分废液或废气上升到喷淋塔顶部,造成未充分融合,因此设置弯头11可以吸收更多的废液废气,使之沉淀;将喷淋头4设置在进气管,可以在进气的时候就充分融合,对喷淋塔要求就可以降低,所以高度上就不需要那么高。A spray dedusting equipment with wind direction changing technology includes air inlet pipe, water inlet pipe 3, spray head 4, spray tower, exhaust pipe 8, recovery water tank 13, water pump 2; described air inlet pipe and spray tower The bottom is fixedly connected, the sprinkler head 4 is connected to the water inlet pipe 3, the water pump 2 is arranged between the water inlet pipe 3 and the recovery water tank 13, and the water pump 2 can send water to the sprinkler head 4, so The exhaust pipe 8 described above is arranged on the top of the spray tower, and the dust gas enters the spray tower and is discharged through the exhaust pipe 8 after being filtered; One end of the water branch pipe 31 is connected with the water inlet pipe 3, and the other end penetrates into the air inlet pipe. The spray head 4 is arranged at the end of the water inlet branch pipe 31; An elbow 11; a swirl plate 6 is arranged in the spray tower; a drain is arranged at the bottom of the spray tower, which is discharged to the recovery water tank 13 through the drain pipe 10. Due to the strong airflow rushing into the intake pipe, before the dust settles at the bottom of the spray tower, part of the waste liquid or waste gas will rise to the top of the spray tower due to the momentum, resulting in insufficient fusion. Therefore, the installation of elbow 11 can absorb more dust. If there is a lot of waste liquid and waste gas, it will be precipitated; if the sprinkler head 4 is set in the air intake pipe, it can be fully integrated when the air is inhaled, and the requirements for the spray tower can be reduced, so the height does not need to be so high.
作为优选的,进气管设置有一次进气管1和二次进气管7,所述的喷淋塔设置有一次喷淋塔5和二次喷淋塔9;所述的进气管与一次喷淋塔5的底部连接;所述的二次进气管7一端连接在一次喷淋塔5的顶部,一端连接在二次喷淋塔9的底部;所述的排气管8设置在二次喷淋塔9的顶部;所述的一次进气管1和二次进气管7均设置有喷淋头4。As preferably, the air intake pipe is provided with a primary air intake pipe 1 and a secondary air intake pipe 7, and the spray tower is provided with a primary spray tower 5 and a secondary spray tower 9; The bottom of 5 is connected; one end of the secondary air inlet pipe 7 is connected to the top of the primary spray tower 5, and one end is connected to the bottom of the secondary spray tower 9; the exhaust pipe 8 is arranged on the secondary spray tower 9; the primary air intake pipe 1 and the secondary air intake pipe 7 are all provided with a spray head 4.
作为优选的,所述的喷淋塔内部设置有喷淋头4。Preferably, a spray head 4 is arranged inside the spray tower.
作为优选的,进气管和喷淋塔内部的喷淋头4可以各设置2个以上,同时,喷淋塔内部的旋流板6也可以根据喷淋塔的高度设置2个以上。As preferably, more than 2 spray heads 4 inside the air inlet pipe and the spray tower can be provided respectively, and at the same time, more than 2 swirl plates 6 inside the spray tower can also be provided according to the height of the spray tower.
目前现有设备喷淋塔高度一般为6-8米,一次喷淋塔5内部旋流板6要4-5个,还要正反设置,排出尾气为10mg/m3 左右,本实施例中,通过改进后,喷淋塔高度可以控制在1.5-3米高度,喷淋塔内部旋流板6设置1-2个即可,且无需正反设置,节能环保,同时尾气排放浓度优于国家标准(10mg/m3)5倍以上,达到1.7mg/m3 。At present, the height of the spray tower of the existing equipment is generally 6-8 meters. There are 4-5 swirl plates 6 inside the spray tower 5, and the front and back are also arranged. The exhaust gas is about 10 mg/m3. In this embodiment, After the improvement, the height of the spray tower can be controlled at a height of 1.5-3 meters, and only 1-2 swirl plates 6 inside the spray tower can be installed, and there is no need for positive and negative settings, which is energy-saving and environmentally friendly. At the same time, the concentration of exhaust gas emission is better than the national standard (10mg/m3) more than 5 times, reaching 1.7mg/m3.
更进一步的设置是,回收水箱13内部设置有过滤网12,过滤网12设置水平和竖直两块,横向长度与回收水箱13宽度适配,过滤出来的干净的水可以通过水泵2进入进水管3,进行循环利用。A further setting is that a filter screen 12 is provided inside the recovery water tank 13, and the filter screen 12 is provided with two pieces, horizontal and vertical, and the horizontal length is adapted to the width of the recovery water tank 13, and the filtered clean water can enter the water inlet pipe through the water pump 2 3. Recycle.
本套喷淋除尘设备可以配合前端集尘器和后端回收装置配合使用,集尘器设置在本套喷淋除尘设备前端,回收装置设置在陪喷淋除尘设备后端,通过集尘器收集重颗粉尘,含尘气体净化率可80%左右,然后喷淋除尘设备净化处理,可使含尘气体净化率93%以上,整套除尘系统工作流程为:风机通过风管连接开花机生产线(或其它气流纺生产线)送风至集尘器,对重颗粒粉尘回收分离处理,含微尘气体进入微尘喷淋除尘设备,在进气管经多层360度逆向喷淋处理,通过风向变轨及两级过滤实现微尘处理净化,空气净化达标排放的目标,泥浆进入回收水箱经泥回收装置处理,垃圾排出,水继续做循环喷淋用,底部工作一段时间后产生的於泥,由回收装置中的自动清於系统清除,避免了水箱中水长时间循环使用变质发臭。This set of spray dust removal equipment can be used in conjunction with front-end dust collector and rear-end recovery device. For heavy dust, the dust-containing gas purification rate can be about 80%, and then the spray dust removal equipment can purify the dust-containing gas with a purification rate of more than 93%. Other air spinning production lines) send air to the dust collector to recover and separate the heavy particle dust. The two-stage filtration realizes the goal of fine dust treatment and purification, and the air purification reaches the standard discharge. The mud enters the recovery water tank and is processed by the mud recovery device, and the garbage is discharged. The water continues to be used for circulating spraying. The mud generated after working for a period of time at the bottom is recovered by the recovery device. The automatic cleaning in the water tank is cleared by the system, which avoids the deterioration and odor of the water in the water tank for a long time.
当然,以上仅为本发明较佳实施方式,并非以此限定本发明的使用范围,因此,凡是在本发明原理上做等效改变、组合更改以及部分相同的技术特征数量增减,而没有做出实质性特点的,均应包含在本发明的保护范围内。Of course, the above are only preferred embodiments of the present invention, and are not intended to limit the application scope of the present invention. Therefore, any equivalent change, combination change, and increase or decrease in the number of some of the same technical features on the principle of the present invention are not made. Those with substantive features should be included in the protection scope of the present invention.
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| CN112337297A (en) * | 2019-12-23 | 2021-02-09 | 福州集丫科技有限公司 | Waste gas purification device for paper mill |
| CN115540138A (en) * | 2022-08-03 | 2022-12-30 | 南通名涂环境工程有限公司 | Air purification device with humidification effect |
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Application publication date: 20191018 |