CN110124423A - A kind of novel energy-conserving air purifier - Google Patents
A kind of novel energy-conserving air purifier Download PDFInfo
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- CN110124423A CN110124423A CN201810131383.4A CN201810131383A CN110124423A CN 110124423 A CN110124423 A CN 110124423A CN 201810131383 A CN201810131383 A CN 201810131383A CN 110124423 A CN110124423 A CN 110124423A
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Abstract
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技术领域technical field
本发明涉及一种工业用环保设备技术领域,尤其涉及一种新型节能空气净化器。The invention relates to the technical field of industrial environmental protection equipment, in particular to a novel energy-saving air purifier.
背景技术Background technique
随着人类进入二十一世纪,工业化的飞速发展以及多品种污染物的无序排放,已经使地球环境受到了严重影响,部分地区已经到了令人难以生存的地步,虽然国家已三令五申,控制排放,整治环境。国内常用的空气净化器的种类、原理和特性如下:As mankind enters the 21st century, the rapid development of industrialization and the disorderly discharge of various pollutants have seriously affected the global environment, and some areas have reached the point where it is difficult to survive. Although the country has repeatedly issued orders to control emissions , Renovate the environment. The types, principles and characteristics of commonly used air purifiers in China are as follows:
1.机械式除尘器1. Mechanical dust collector
采用这种形式除尘的有以下几种:There are several types of dust removal in this form:
a.重力除尘器;b.惯性除尘器;c.旋风除尘器;d.多管旋风除尘器。a. Gravity dust collector; b. Inertial dust collector; c. Cyclone dust collector; d. Multi-tube cyclone dust collector.
以上四种除尘器,都是以独立形式存在,其原理都一样,利用粉尘自身重量,在高速旋转过程中自然下落,达到除尘目的。但它们都有一个共同的弱点,那就是微粒粉尘都无法除净,烟尘就更不用说,它们都只能适用于矿山、冶金及多颗粒粉尘的地方。The above four dust collectors all exist in an independent form, and their principles are the same, using the weight of the dust itself to fall naturally during the high-speed rotation to achieve the purpose of dust removal. But they all have a common weakness, that is, the particulate dust cannot be removed, not to mention the smoke dust, and they can only be used in mines, metallurgy and multi-particle dust.
2.湿式除尘器2. Wet dust collector
采用这种形式除尘的有以下几种:There are several types of dust removal in this form:
a.喷淋洗涤器;b.文丘里除尘器;c.自激式除尘器;d.水膜除尘器;a. Spray scrubber; b. Venturi dust collector; c. Self-excited dust collector; d. Water film dust collector;
以上四种除尘器,也都是以独立形式存在的,它们的原理也都是利用气流通过水帘(有逆向和顺向)把较大粉尘过滤下来,同样无法除净微粒粉尘,而且运动阻力大,对正常排放有一定的阻碍作用;The above four dust collectors also exist in an independent form, and their principle is to use the airflow to pass through the water curtain (with reverse and forward directions) to filter the larger dust, and it is also impossible to remove the fine dust, and the movement resistance is large. , has a certain hindering effect on normal discharge;
3.过滤式除尘器3. Filter dust collector
采用这种形式的一般最常用的有颗粒层除尘器和袋式除尘器两种,一般也是以独立形式存在的,其特点是开始微小的粉尘也不能过滤,可一段时间后(1小时)通风阻力加大,影响正常排放,微粒粉尘倒排。In this form, the most commonly used ones are granular layer dust collector and bag dust collector, which generally exist in an independent form. Its characteristic is that the tiny dust cannot be filtered at the beginning, and it can be ventilated after a period of time (1 hour). The increased resistance will affect the normal discharge, and the particulate dust will be discharged backwards.
4.静电除尘器4. Electrostatic precipitator
这种除尘器是利用电场原理捕捉灰尘,效果虽好,但价格昂贵,营运成本也相当高,一般只适用于大企业、大污染源的净化除尘。This kind of dust collector uses the principle of electric field to capture dust. Although the effect is good, it is expensive and the operating cost is also quite high. Generally, it is only suitable for the purification and dust removal of large enterprises and large pollution sources.
5.火力发电厂的除尘,用的是一整套系统设备,其中包括除硫及其它有害元素,其原理也是将静电除尘和喷淋式除尘并用,再经过复杂的除硫工艺,这些设备不仅规模庞大,而且造价高昂,整套设备将高达数千万元之多。5. The dust removal of the thermal power plant uses a complete set of system equipment, including the removal of sulfur and other harmful elements. Huge and expensive, the whole set of equipment will cost tens of millions of yuan.
以上介绍的所有除尘设备,不仅价格不低,而且多为单一使用,效果都受到了一定局限,营运成本也不低。且由于中国国情特殊,南北东西差距很大,大小企业分布不均,排放的污染源也差异很大。鉴于这些原因,国家级大型企业可以安装大型净化设备(或进口设备),而这些设备价格一般都在几百上千万元以上,这对大中型企业来说,或许可以承受,而对一般中小企业来说,这样的设备就很难接受了,特别是小企业,而且是劳动密集型的小企业,更难接受这样的设备。事实上,我国的很多污染物,相当一部分都是这些企业排放的。因此,寻求一种规模不大、价格不高、适应性广而净化效果明显、营运成本低的小型空气净化器,是中国现阶段控制和治理大气污染的最有效途径。All the dust removal equipment introduced above are not only not cheap, but most of them are single-use, the effect is limited to a certain extent, and the operating cost is not low. Moreover, due to China's special national conditions, there is a large gap between the north and the south, and the distribution of large and small enterprises is uneven, and the pollution sources emitted are also very different. In view of these reasons, large state-level enterprises can install large-scale purification equipment (or imported equipment), and the price of these equipment is generally more than tens of millions of yuan, which may be affordable for large and medium-sized enterprises, but for general small and medium-sized For enterprises, it is difficult to accept such equipment, especially small enterprises, and labor-intensive small enterprises, it is even more difficult to accept such equipment. In fact, many pollutants in our country are discharged by these enterprises. Therefore, seeking a small-scale air purifier with small scale, low price, wide adaptability, obvious purification effect and low operating cost is the most effective way to control and treat air pollution in China at this stage.
本申请人曾经申请过专利公开号为CN200710134903.9、公开日为2009.10.28的中国发明专利工业用小型空气净化器,本申请人发现曾经的空气净化器在水气揉和的速度与效率方面在长期使用的过程中没有达到预期的效果,并且粉尘回收以及水资源回收的存在效率低下,频繁更换集尘箱以及水箱中的水源,故新申请旨在解决该净化器的效率问题,在水气揉和装置和旋风分离装置之间的导风管中设置了气流阀门,形成了工业废气与水雾的高效混合紊流腔,并且在气流阀门两边形成压强差,在增加揉和效率的同时加快了气流在导风管中的流速,提高了净化的效率,将所述集尘箱通过振动器控制振动,有效的解决旋风分离器过滤的粉尘及固体颗粒通过筒体内壁滑落至集尘箱产生的粉尘堆积问题,再加上压滤盘的压滤,更好的提高了集尘箱的集尘和过滤的效率。The applicant once applied for a small industrial air purifier with the patent publication number of CN200710134903.9 and the publication date of 2009.10.28. The applicant found that the air purifier used to knead water and air in terms of speed and efficiency In the process of long-term use, the expected effect has not been achieved, and the efficiency of dust recovery and water resource recovery is low, and the water source in the dust collection box and water tank is frequently replaced. Therefore, the new application aims to solve the efficiency problem of the purifier. An air flow valve is set in the air guide pipe between the air kneading device and the cyclone separation device, forming an efficient mixing turbulence chamber for industrial waste gas and water mist, and forming a pressure difference on both sides of the air flow valve, while increasing the kneading efficiency Speed up the flow rate of the airflow in the air guide pipe, improve the purification efficiency, control the vibration of the dust box through the vibrator, effectively solve the problem that the dust and solid particles filtered by the cyclone separator slide down to the dust box through the inner wall of the cylinder The dust accumulation problem, coupled with the pressure filtration of the filter plate, better improves the dust collection and filtration efficiency of the dust collection box.
发明内容Contents of the invention
一种新型节能空气净化器,包括动力装置、密封连接的导风管、风机、水气揉合装置、旋风分离器以及集尘箱、水箱和水泵,其特征在于,所述导风管一端设有与污染排放设备排放口连接的接口,另一端与所述强力风机进风口密封连接;A new type of energy-saving air purifier, including a power unit, a sealed air guide pipe, a fan, a water-air kneading device, a cyclone separator, a dust collection box, a water tank and a water pump, is characterized in that one end of the air guide pipe is set There is an interface connected to the discharge port of the pollution discharge equipment, and the other end is sealed and connected to the air inlet of the powerful fan;
所述导风管上至少设置有气流阀门,所述气流阀门设置在所述水气揉合装置和所述旋风分离器之间的通道中且靠近所述水气揉合装置一侧,所述气流阀门通过包裹在外廓的密封圈与所述导风管内壁连密封连接,所述气流阀门包括与所述导风管内壁轮廓形状相同的外箍以及连接在所述外箍内圈上的多个风阻片、多个所述风阻片闭合形成密闭的阻风面,所述风阻片远离所述水气揉合装置一端设置有限位片。The air guide pipe is provided with at least an airflow valve, and the airflow valve is arranged in the channel between the water-air kneading device and the cyclone separator and is close to the side of the water-air kneading device. The airflow valve is tightly connected with the inner wall of the air guide pipe through the sealing ring wrapped on the outer contour. A wind resistance sheet and a plurality of wind resistance sheets are closed to form an airtight wind resistance surface, and the end of the wind resistance sheet away from the water-air kneading device is provided with a limiting sheet.
由此,所述气流阀门的设置使得在所述气流阀门与所述水气揉合装置之间形成了一个体积更小,密度更大的混合腔,让工业废气和通过所述水泵将所述水箱内的水充分且更有效率的混合,使的混合之后的气体质量更大,由于所述气流阀门的存在使得所述风机在使用过程中在所述气流阀门的两端形成压强差,当混合腔中的压强升高到一定的值后,所述气流阀门上设置的所述风阻片在压强差的作用下向所述旋风分离器的方向打开,形成了一个形状小于所述导风管的通气孔,让重度混合的气体快速的通过所述气流阀门,在所述气流阀门和所述旋风分离器之间形成一个激流紊流腔,造成废气与水气的二次混合,且重度混合的气体更快的进入所述旋风分离器中,当积累在混合腔内的混合气体进入激流紊流腔后,所述气流阀门两端的压强差逐渐降低,所述风阻片闭合回位,所述限位片在所述风阻片回位的过程中起到了有效的定位作用,防止混合腔负压造成的倒吸问题。Thus, the setting of the air flow valve makes a mixing chamber with smaller volume and higher density formed between the air flow valve and the water-air kneading device, so that the industrial waste gas and the The water in the water tank is fully and more efficiently mixed, so that the gas quality after mixing is greater. Due to the existence of the air flow valve, the fan forms a pressure difference at both ends of the air flow valve during use. After the pressure in the mixing chamber rises to a certain value, the air resistance plate provided on the air flow valve opens toward the direction of the cyclone separator under the action of the pressure difference, forming a shape smaller than the air duct. The vent hole allows the heavily mixed gas to quickly pass through the airflow valve, forming a turbulent flow chamber between the airflow valve and the cyclone separator, resulting in secondary mixing of exhaust gas and water vapor, and severe mixing The gas enters the cyclone separator faster, and when the mixed gas accumulated in the mixing chamber enters the torrent turbulence chamber, the pressure difference between the two ends of the air flow valve gradually decreases, the wind resistance plate is closed and returned, and the The limiting plate plays an effective positioning role in the process of returning the air resistance plate, and prevents the suction problem caused by the negative pressure in the mixing chamber.
作为本发明的优选,所述水气揉合装置包括揉合管道、揉轮、揉合喷头和揉和阀门,所述揉合管道两端分别与所述风机的出风口和所述旋风分离器的进风口密封连接,所述揉合管道设有一个直径上游较大、下游较小的锥形部,所述揉轮包括揉轮头和多条叶片,所述揉轮头形状为圆台和圆锥台的结合体,多条所述叶片沿径向螺旋设置于所述揉轮头表面,所述揉轮头可转动地设置在所述锥形部中,所述揉轮头中心轴向设有轴孔和转轴,所述转轴与所述动力装置传动连接,多个所述揉合喷头设置在所述锥形部并沿气流方向倾斜指向所述揉轮头,所述锥形部的锥度角δ小于所述圆锥台的锥度角θ;As a preference of the present invention, the water-air kneading device includes a kneading pipeline, a kneading wheel, a kneading nozzle and a kneading valve, and the two ends of the kneading pipeline are respectively connected to the air outlet of the fan and the cyclone separator The air inlet is sealed and connected. The kneading pipeline is provided with a tapered part with a larger diameter upstream and a smaller downstream. The kneading wheel includes a kneading wheel head and a plurality of blades. A combination of platforms, a plurality of blades are arranged radially and spirally on the surface of the kneading wheel head, the kneading wheel head is rotatably arranged in the tapered part, and the center of the kneading wheel head A shaft hole and a rotating shaft, the rotating shaft is in transmission connection with the power device, a plurality of kneading nozzles are arranged on the tapered part and point to the kneading wheel head obliquely along the airflow direction, the taper angle of the tapered part δ is less than the taper angle θ of the truncated cone;
所述旋风分离器设有一个上大下小的倒圆锥台形筒体,所述筒体上端面封闭,中心插入有排风管,所述排风管中设有除味层,所述水气揉合装置连接在所述筒体的上部,所述筒体内腔顶部还设有分离喷头,所述集尘箱设置在所述筒体下端的正下方。The cyclone separator is provided with an inverted truncated cone-shaped cylinder with a large upper part and a smaller lower part. The upper end of the cylindrical body is closed, and an exhaust pipe is inserted in the center. The deodorization layer is arranged in the exhaust pipe, and the water vapor The kneading device is connected to the upper part of the barrel, the top of the inner cavity of the barrel is also provided with a separation nozzle, and the dust collection box is arranged directly below the lower end of the barrel.
作为本发明的优选,所述叶片与所述揉轮头轴线的螺旋角度20°≤α≤25°,所述叶片与所述揉轮头表面的倾斜角20°≤β≤25°,所述锥形部的锥度角33°≤δ≤42°,所述圆锥台的锥度角35°≤θ≤45°;所述筒体的锥度为28°~35°。As a preference of the present invention, the helical angle between the blade and the axis of the kneading wheel head is 20°≤α≤25°, the inclination angle between the blade and the surface of the kneading wheel head is 20°≤β≤25°, the The taper angle of the tapered part is 33°≤δ≤42°, the taper angle of the truncated cone is 35°≤θ≤45°; the taper of the barrel is 28°-35°.
由此,所述排风管插入后下端离筒体底部的高度与所述排风管下端所处位置所述筒体的横截面直径之比为 0.85~1.15,所述排风管下端所处位置所述筒体的横截面直径与所述排风管直径之比为1.6~1.8。Therefore, the ratio of the height of the lower end of the exhaust pipe from the bottom of the cylinder to the cross-sectional diameter of the cylinder where the lower end of the exhaust pipe is located is 0.85 to 1.15, and the lower end of the exhaust pipe is located The ratio of the cross-sectional diameter of the cylinder to the diameter of the exhaust pipe is 1.6-1.8.
作为本发明的优选,所述揉合喷头沿气流方向倾斜指向所述揉轮头圆台和圆锥台的结合部;所述揉合喷头和所述分离喷头为雾化喷头。As a preference of the present invention, the kneading nozzle is obliquely directed to the junction of the truncated cone and the truncated cone of the kneading wheel head along the airflow direction; the kneading nozzle and the separation nozzle are atomizing nozzles.
作为本发明的优选,所述圆锥台的锥度角θ=40°,所述叶片与所述揉轮头轴线的螺旋角度α=23°;所述叶片与所述揉轮头表面的倾斜角β=22°,所述锥形部的锥度角δ=38°;所述筒体的锥度为30°,所述排风管下端离筒体底部的高度与排风管下端所处位置筒体的横截面直径之比为1,所述排风管下端所处位置筒体的横截面直径与排风管直径之比为1.7;所述揉合喷头沿气流方向倾斜指向所述揉轮头圆台和圆锥台的结合部并与所述揉轮头轴线成45°。As a preference of the present invention, the taper angle θ=40° of the truncated cone, the helix angle α=23° between the blade and the axis of the kneading wheel head; the inclination angle β between the blade and the surface of the kneading wheel head =22°, the taper angle δ=38° of the tapered part; the taper of the cylinder is 30°, the height of the lower end of the exhaust pipe from the bottom of the cylinder is the same as the height of the cylinder at the lower end of the exhaust pipe. The ratio of the cross-sectional diameter is 1, and the ratio of the cross-sectional diameter of the cylinder at the lower end of the exhaust pipe to the diameter of the exhaust pipe is 1.7; The junction of the truncated cone is 45° with the axis of the kneading wheel head.
作为本发明的优选,所述水箱、所述水泵、所述揉合喷头和所述分离喷头通过水管连接构成喷淋系统。As a preference of the present invention, the water tank, the water pump, the kneading nozzle and the separation nozzle are connected through water pipes to form a spraying system.
作为本发明的优选,所述水箱设置在所述集尘箱的下方,所述水箱和所述集尘箱之间设有细滤网回收喷淋水构成循环利用系统。As a preference of the present invention, the water tank is arranged below the dust collection box, and a fine filter is provided between the water tank and the dust collection box to recover the spray water to form a recycling system.
作为本发明的优选,所述集尘箱连接有振动器。As a preference of the present invention, the dust box is connected with a vibrator.
由此,通过振动器来控制所述集尘箱的振动,来解决所述旋风分离器过滤的粉尘及固体颗粒通过所述筒体内壁滑落至所述集尘箱产生的粉尘堆积问题,能够更好的收集粉尘以及对含有水分的粉尘进行过滤,所述水箱包括回收水箱和水源箱,所述回收水箱设置在所述集尘箱与所述水源箱之间,所述回收水箱设置有出水口,所述水源箱设置有进水口,由于考虑到一些工业废气或者粉尘的温度较高,故而将一部分的热量传递给了水气中,通过回收水箱将热量进行第二部的回收。Therefore, the vibration of the dust box is controlled by the vibrator to solve the problem of dust accumulation caused by the dust and solid particles filtered by the cyclone separator sliding down to the dust box through the inner wall of the cylinder, which can be more efficient. Good for collecting dust and filtering dust containing moisture, the water tank includes a recycling water tank and a water source tank, the recycling water tank is arranged between the dust collection tank and the water source tank, and the recycling water tank is provided with a water outlet , the water source tank is provided with a water inlet, and due to the high temperature of some industrial waste gas or dust, a part of the heat is transferred to the water vapor, and the heat is recovered in the second part through the recovery water tank.
作为本发明的优选,所述旋风分离器还包括压滤盘,所述压滤盘与所述旋风分离器的转动轴连接。As a preference of the present invention, the cyclone separator further includes a filter press disc, and the filter press disc is connected with the rotation shaft of the cyclone separator.
由此,所述压滤盘的直径小于等于所述旋风分离器出尘口直径,所述压滤盘在所述转动轴的带动下进行下压,对所述集尘箱中的收集物进行压滤,实现更好的喷淋水回收,限定压滤盘大小将压滤盘对粉尘落下的影响降到最低。Thus, the diameter of the filter press disc is less than or equal to the diameter of the dust outlet of the cyclone separator, and the filter press disc is pressed down under the drive of the rotating shaft to collect the collected objects in the dust box. Press filtration to achieve better spray water recovery, and limit the size of the filter disc to minimize the impact of the filter disc on dust fall.
作为本发明的优选,所述导风管的内壁与外壁的夹层中设置有温差发电芯片。As a preference of the present invention, a thermoelectric power generation chip is arranged in the interlayer between the inner wall and the outer wall of the air duct.
由此,所述温差发电芯片为现有的技术,可以将进入该净化器的高温度废气中的热量进行初步的回收为电能。Therefore, the thermoelectric power generation chip is an existing technology, which can initially recover the heat in the high-temperature exhaust gas entering the purifier into electrical energy.
本发明具有以下有益效果:The present invention has the following beneficial effects:
本发明适用性很强,有很大的发展前景,与现有技术相比,本发明设计的一种新型空气净化器,在水气揉和装置和旋风分离装置之间的导风管中设置了气流阀门,形成了工业废气与水雾的高效混合紊流腔,并且在气流阀门两边形成压强差,在增加揉和效率的同时加快了气流在导风管中的流速,提高了净化的效率,将所述集尘箱通过振动器控制振动,有效的解决旋风分离器过滤的粉尘及固体颗粒通过筒体内壁滑落至集尘箱产生的粉尘堆积问题,再加上压滤盘的压滤,更好的提高了集尘箱的集尘和过滤的效率。The present invention has strong applicability and great development prospects. Compared with the prior art, a novel air purifier designed by the present invention is installed in the air guide pipe between the water-gas kneading device and the cyclone separation device. The airflow valve is installed to form an efficient mixing turbulence chamber for industrial waste gas and water mist, and a pressure difference is formed on both sides of the airflow valve, which increases the kneading efficiency and speeds up the flow rate of the airflow in the air duct, improving the efficiency of purification , the vibration of the dust collection box is controlled by a vibrator, which effectively solves the problem of dust accumulation caused by the dust and solid particles filtered by the cyclone separator slipping through the inner wall of the cylinder to the dust collection box, plus the pressure filtration of the filter plate, The dust collection and filtration efficiency of the dust collection box is better improved.
下面通过附图和实施例,对本发明的技术方案做进一步的详细描述。The technical solutions of the present invention will be described in further detail below with reference to the accompanying drawings and embodiments.
附图说明Description of drawings
图1为本发明局部放大图;Fig. 1 is a partial enlarged view of the present invention;
图2为气流阀门的结构示意图;Fig. 2 is the structural representation of air flow valve;
图3为本发明主视结构示意图;Fig. 3 is a schematic diagram of the main view structure of the present invention;
图4为本发明左视结构示意图;Fig. 4 is a schematic view of the left view structure of the present invention;
图5为图3旋风分离器A-A结构剖视图;Fig. 5 is a cross-sectional view of the structure of Fig. 3 cyclone separator A-A;
图6为揉轮立体示意图;Fig. 6 is a three-dimensional schematic diagram of a kneading wheel;
图7为揉轮主视图;Figure 7 is a front view of the kneading wheel;
图8为揉轮左视图。Figure 8 is a left side view of the kneading wheel.
具体实施方式Detailed ways
以下结合附图对本发明作进一步详细说明。The present invention will be described in further detail below in conjunction with the accompanying drawings.
如图1、2、4和5所示,一种新型节能空气净化器,包括动力装置1、密封连接的导风管2、风机3、水气揉合装置4、旋风分离器5以及集尘箱6、水箱7和水泵8,其特征在于,所述导风管2一端设有与污染排放设备排放口连接的接口21,另一端与所述强力风机3进风口密封连接,所述导风管2上至少设置有气流阀门21,所述气流阀门21设置在所述水气揉合装置4和所述旋风分离器5之间的通道中且靠近所述水气揉合装置4一侧,所述气流阀门21通过包裹在外廓的密封圈22与所述导风管2内壁连密封连接,所述气流阀门21包括与所述导风管2内壁轮廓形状相同的外箍211以及连接在所述外箍211内圈上的多个风阻片212、多个所述风阻片212闭合形成密闭的阻风面213,所述风阻片212远离所述水气揉合装置4一端设置有限位片214,所述气流阀门21的设置使得在所述气流阀门21与所述水气揉合装置4之间形成了一个体积更小,密度更大的混合腔,让工业废气和通过所述水泵8将所述水箱7内的水充分且更有效率的混合,使的混合之后的气体质量更大,由于所述气流阀门21的存在使得所述风机3在使用过程中在所述气流阀门21的两端形成压强差,当混合腔中的压强升高到一定的值后,所述气流阀门21上设置的所述风阻片212在压强差的作用下向所述旋风分离器5的方向打开,形成了一个形状小于所述导风管2的通气孔,让重度混合的气体快速的通过所述气流阀门21,在所述气流阀门21和所述旋风分离器5之间形成一个激流紊流腔,造成废气与水气的二次混合,且重度混合的气体更快的进入所述旋风分离器5中,当积累在混合腔内的混合气体进入激流紊流腔后,所述气流阀门21两端的压强差逐渐降低,所述风阻片212闭合回位,所述限位片214在所述风阻片212回位的过程中起到了有效的定位作用,防止混合腔负压造成的倒吸问题,所述风阻片212的至少为3个,以保证足够的通气孔大小,并且沿所述气流阀门2的圆心圆周分布,每两个所述风阻片212之间设置有所述限位片214。As shown in Figures 1, 2, 4 and 5, a new type of energy-saving air purifier includes a power unit 1, a sealed air duct 2, a fan 3, a water-air kneading device 4, a cyclone separator 5 and a dust collector Tank 6, water tank 7 and water pump 8 are characterized in that one end of the air guide pipe 2 is provided with an interface 21 connected to the discharge port of the pollution discharge equipment, and the other end is sealed and connected with the air inlet of the powerful fan 3, and the air guide pipe At least an airflow valve 21 is provided on the pipe 2, and the airflow valve 21 is arranged in the channel between the water-air kneading device 4 and the cyclone separator 5 and is close to the side of the water-air kneading device 4, The airflow valve 21 is connected to the inner wall of the air guide pipe 2 in a sealed manner through a sealing ring 22 wrapped in the outer contour. A plurality of wind resistance pieces 212 on the inner ring of the outer hoop 211, and a plurality of the wind resistance pieces 212 are closed to form an airtight wind resistance surface 213, and the end of the wind resistance pieces 212 far away from the water-air kneading device 4 is provided with a limit piece 214 , the setting of the air flow valve 21 makes a mixing chamber with smaller volume and higher density formed between the air flow valve 21 and the water-air kneading device 4, allowing the industrial waste gas to be mixed with the water pump 8 The water in the water tank 7 is fully and more efficiently mixed, so that the gas quality after the mixing is greater. Due to the existence of the air flow valve 21, the fan 3 is in use at both ends of the air flow valve 21. When the pressure in the mixing chamber rises to a certain value, the wind resistance sheet 212 provided on the airflow valve 21 opens toward the direction of the cyclone separator 5 under the action of the pressure difference, forming A vent hole with a shape smaller than that of the air guide pipe 2 is provided to allow the heavily mixed gas to quickly pass through the air flow valve 21, forming a torrent turbulent flow chamber between the air flow valve 21 and the cyclone separator 5, The secondary mixing of exhaust gas and water gas is caused, and the heavily mixed gas enters the cyclone separator 5 faster. When the mixed gas accumulated in the mixing chamber enters the turbulent flow chamber, the air flow valve 21 at both ends The pressure difference gradually decreases, the air resistance sheet 212 is closed and returned, and the limiting sheet 214 plays an effective positioning role during the return process of the air resistance sheet 212, preventing the suction problem caused by the negative pressure in the mixing chamber. There are at least three wind resistance pieces 212 to ensure sufficient air hole size, and they are distributed along the center and circumference of the airflow valve 2 , and the limiting pieces 214 are arranged between every two wind resistance pieces 212 .
如图2、3、6、7和8所示,本实施例中,所述水气揉合装置4包括揉合管道41、揉轮42、揉合喷头43和揉和阀门44,所述揉合管道41两端分别与所述风机3的出风口和所述旋风分离器5的进风口密封连接,所述揉合管道41设有一个直径上游较大、下游较小的锥形部411,所述揉轮42包括揉轮头421和多条叶片422,所述揉轮头421形状为圆台和圆锥台的结合体,多条所述叶片422沿径向螺旋设置于所述揉轮头421表面,所述揉轮头421可转动地设置在所述锥形部411中,所述揉轮头421中心轴向设有轴孔和转轴,所述转轴与所述动力装置1传动连接,多个所述揉合喷头43设置在所述锥形部411并沿气流方向倾斜指向所述揉轮头421,所述锥形部411的锥度角δ小于所述圆锥台的锥度角θ,所述旋风分离器5设有一个上大下小的倒圆锥台形筒体51,所述筒体51上端面封闭,中心插入有排风管52,所述排风管52中设有除味层521,所述水气揉合装置4连接在所述筒体51的上部,所述筒体51内腔顶部还设有分离喷头53,所述集尘箱6设置在所述筒体51下端的正下方;揉轮头421和多条叶片422,揉轮头421形状为圆台和圆锥台的结合体,多条叶片422沿径向均匀成螺旋设置在揉轮头421表面,揉轮头 421中心轴向设有轴孔和转轴,转轴一端动密封从揉合管道41 中穿出并通过轴承和轴承座安装在轴承座支座上,轴承座支座固定在水箱7上,转轴上设有皮带轮与动力装置传动连接,揉轮 42在动力装置如电机的驱动下高速旋转As shown in Figures 2, 3, 6, 7 and 8, in this embodiment, the water-air kneading device 4 includes a kneading pipeline 41, a kneading wheel 42, a kneading nozzle 43 and a kneading valve 44. The two ends of the mixing pipeline 41 are respectively sealed and connected to the air outlet of the fan 3 and the air inlet of the cyclone separator 5, and the kneading pipeline 41 is provided with a tapered portion 411 with a larger diameter upstream and a smaller downstream diameter, The kneading wheel 42 includes a kneading wheel head 421 and a plurality of blades 422, the shape of the kneading wheel head 421 is a combination of a circular truncated cone and a conical truncated cone, and a plurality of the kneading wheel heads 422 are spirally arranged on the kneading wheel head 421 in the radial direction On the surface, the kneading wheel head 421 is rotatably arranged in the tapered part 411, and the central axis of the kneading wheel head 421 is provided with a shaft hole and a rotating shaft. The two kneading nozzles 43 are arranged on the conical portion 411 and point to the kneading wheel head 421 obliquely along the airflow direction, the taper angle δ of the conical portion 411 is smaller than the taper angle θ of the truncated cone, and the The cyclone separator 5 is provided with an inverted truncated cone-shaped cylinder 51 with a large upper part and a smaller lower part. The upper end of the cylindrical body 51 is closed, and an exhaust pipe 52 is inserted in the center. The deodorization layer 521 is arranged in the exhaust pipe 52. The water-air kneading device 4 is connected to the upper part of the cylinder body 51, and the top of the cylinder body 51 is provided with a separation nozzle 53, and the dust collection box 6 is arranged directly below the lower end of the cylinder body 51. Knead the wheel head 421 and a plurality of blades 422, and the wheel head 421 is shaped as a combination of a truncated cone and a truncated cone, and a plurality of blades 422 are arranged on the surface of the wheel head 421 evenly in the radial direction, and the center axis of the wheel head 421 is kneaded. A shaft hole and a rotating shaft are provided, and the dynamic seal at one end of the rotating shaft passes through the kneading pipeline 41 and is installed on the bearing seat through the bearing and the bearing seat. The bearing seat is fixed on the water tank 7, and the rotating shaft is provided with a pulley and a power The device is connected by transmission, and the kneading wheel 42 rotates at a high speed under the drive of a power device such as a motor
本实施例中,所述叶片422与所述揉轮头421轴线的螺旋角度20°≤α≤25°,所述叶片422与所述揉轮头421表面的倾斜角20°≤β≤25°,所述锥形部411的锥度角33°≤δ≤42°,所述圆锥台的锥度角35°≤θ≤45°;所述筒体51的锥度为28°~35°,所述排风管52插入后下端离筒体底部的高度与所述排风管52下端所处位置所述筒体51的横截面直径之比为 0.85~1.15,所述排风管52下端所处位置所述筒体51的横截面直径与所述排风管52直径之比为1.6~1.8;所述揉合喷头43沿气流方向倾斜指向所述揉轮头421圆台和圆锥台的结合部;所述揉合喷头43和所述分离喷头53为雾化喷头。In this embodiment, the helical angle between the blade 422 and the axis of the kneading wheel head 421 is 20°≤α≤25°, and the inclination angle between the blade 422 and the surface of the kneading wheel head 421 is 20°≤β≤25° , the taper angle of the tapered part 411 is 33°≤δ≤42°, the taper angle of the truncated cone is 35°≤θ≤45°; the taper of the cylinder 51 is 28°~35°, the row The ratio of the height of the lower end of the air duct 52 from the bottom of the barrel to the cross-sectional diameter of the barrel 51 where the lower end of the exhaust duct 52 is located is 0.85 to 1.15. The ratio of the cross-sectional diameter of the cylinder body 51 to the diameter of the exhaust pipe 52 is 1.6 to 1.8; the kneading nozzle 43 is obliquely directed to the junction of the kneading wheel head 421 and the truncated cone along the airflow direction; The kneading nozzle 43 and the separation nozzle 53 are atomizing nozzles.
本实施例中,所述圆锥台的锥度角θ=40°,所述叶片422与所述揉轮头421轴线的螺旋角度α=23°;所述叶片422与所述揉轮头421表面的倾斜角β=22°,所述锥形部411的锥度角δ=38°;所述筒体51的锥度为30°,所述排风管52下端离筒体底部的高度与排风管下端所处位置筒体的横截面直径之比为1,所述排风管52下端所处位置筒体的横截面直径与排风管直径之比为1.7;所述揉合喷头43沿气流方向倾斜指向所述揉轮头421圆台和圆锥台的结合部并与所述揉轮头421轴线成45°。In the present embodiment, the taper angle θ=40° of the truncated cone, the helical angle α=23° between the blade 422 and the axis of the kneading wheel head 421; The inclination angle β=22°, the taper angle δ=38° of the tapered portion 411; the taper of the cylinder 51 is 30°, and the height of the lower end of the exhaust pipe 52 from the bottom of the cylinder is equal to that of the lower end of the exhaust pipe. The ratio of the cross-sectional diameter of the cylinder at the position is 1, and the ratio of the cross-sectional diameter of the cylinder at the lower end of the exhaust pipe 52 to the diameter of the exhaust pipe is 1.7; the kneading nozzle 43 is inclined along the airflow direction Point to the junction of the kneading wheel head 421 and the conical truncated truncated cone, and form a 45° angle with the axis of the kneading wheel head 421 .
本实施例中,所述水箱7、所述水泵8、所述揉合喷头43和所述分离喷头53通过水管连接构成喷淋系统,所述水箱7设置在所述集尘箱6的下方,所述水箱7和所述集尘箱6之间设有细滤网9回收喷淋水构成循环利用系统。In this embodiment, the water tank 7, the water pump 8, the kneading nozzle 43 and the separation nozzle 53 are connected through water pipes to form a spray system, and the water tank 7 is arranged below the dust collection box 6, A fine filter screen 9 is arranged between the water tank 7 and the dust collection box 6 to recycle the spray water to form a recycling system.
本实施例中,所述集尘箱6连接有振动器,通过振动器来控制所述集尘箱6的振动,来解决所述旋风分离器5过滤的粉尘及固体颗粒通过所述筒体51内壁滑落至所述集尘箱6产生的粉尘堆积问题,能够更好的收集粉尘以及对含有水分的粉尘进行过滤,所述水箱7包括回收水箱和水源箱,所述回收水箱71设置在所述集尘箱6与所述水源箱之间,所述回收水箱设置有出水口,所述水源箱设置有进水口,由于考虑到一些工业废气或者粉尘的温度较高,故而将一部分的热量传递给了水气中,通过回收水箱将热量进行第二部的回收。In this embodiment, the dust collection box 6 is connected with a vibrator, and the vibration of the dust collection box 6 is controlled by the vibrator to solve the problem that the dust and solid particles filtered by the cyclone separator 5 pass through the cylinder 51 The problem of dust accumulation caused by the sliding of the inner wall to the dust collection box 6 can better collect dust and filter the dust containing moisture. The water tank 7 includes a recovery water tank and a water source tank. Between the dust collection box 6 and the water source box, the water recovery tank is provided with a water outlet, and the water source box is provided with a water inlet. Due to the high temperature of some industrial waste gas or dust, a part of the heat is transferred to the In the water vapor, the heat is recovered in the second part through the recovery water tank.
本实施例中,所述旋风分离器5还包括压滤盘,所述压滤盘与所述旋风分离器5的转动轴连接,所述压滤盘的直径小于等于所述旋风分离器5出尘口直径,所述压滤盘在所述转动轴的带动下进行下压,对所述集尘箱6中的收集物进行压滤,实现更好的喷淋水回收,限定压滤盘大小将压滤盘对粉尘落下的影响降到最低。In this embodiment, the cyclone separator 5 further includes a filter press disc, which is connected to the rotation shaft of the cyclone separator 5, and the diameter of the filter press disc is less than or equal to the output of the cyclone separator 5. The diameter of the dust port, the pressure filter plate is pressed down under the drive of the rotating shaft, and the collected matter in the dust box 6 is press-filtered to achieve better spray water recovery, and the size of the filter press plate is limited Minimize the impact of the filter plate on dust fall.
本实施例中,所述导风管2的内壁与外壁的夹层中设置有温差发电芯片,所述温差发电芯片为现有的技术,可以将进入该净化器的高温度废气中的热量进行初步的回收为电能。In this embodiment, the interlayer between the inner wall and the outer wall of the air guide pipe 2 is provided with a thermoelectric power generation chip. The thermoelectric power generation chip is an existing technology, which can preliminarily convert the heat in the high-temperature exhaust gas entering the purifier. recovered as electrical energy.
上面所述的实施例仅是对本发明的优选实施方式进行描述,并非对本发明的构思和范围进行限定。在不脱离本发明设计构思的前提下,本领域普通人员对本发明的技术方案做出的各种变型和改进,均应落入到本发明的保护范围,本发明请求保护的技术内容,已经全部记载在权利要求书中。The above-mentioned embodiments are only descriptions of preferred implementations of the present invention, and are not intended to limit the concept and scope of the present invention. Under the premise of not departing from the design concept of the present invention, various modifications and improvements made by ordinary persons in the art to the technical solution of the present invention shall fall within the scope of protection of the present invention, and the technical content claimed in the present invention has been fully described in the claims.
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| CN206823369U (en) * | 2017-04-12 | 2018-01-02 | 沈阳味丹生物科技有限公司 | Cyclone separator |
| CN206762468U (en) * | 2017-05-12 | 2017-12-19 | 辽宁基伊环保科技股份有限公司 | A kind of new double-cyclone high-efficiency dehydration demister |
| CN208757184U (en) * | 2018-02-09 | 2019-04-19 | 浙江管工智能机械设备有限公司 | A kind of novel energy-conserving air purifier |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN114345105A (en) * | 2021-12-29 | 2022-04-15 | 山东理工职业学院 | An environmentally friendly pharmaceutical waste gas treatment equipment |
| CN114345105B (en) * | 2021-12-29 | 2024-04-16 | 山东理工职业学院 | Environment-friendly pharmacy exhaust treatment equipment |
| CN115077085A (en) * | 2022-04-28 | 2022-09-20 | 青岛海尔空调器有限总公司 | Fresh air filtering joint, fresh air pipe and fresh air conditioner |
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