CN105854486A - Waste heat recycling type waste gas treating device for setting machine - Google Patents
Waste heat recycling type waste gas treating device for setting machine Download PDFInfo
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- CN105854486A CN105854486A CN201610358704.5A CN201610358704A CN105854486A CN 105854486 A CN105854486 A CN 105854486A CN 201610358704 A CN201610358704 A CN 201610358704A CN 105854486 A CN105854486 A CN 105854486A
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- 239000002912 waste gas Substances 0.000 title claims abstract description 44
- 239000002918 waste heat Substances 0.000 title claims abstract description 41
- 238000004064 recycling Methods 0.000 title abstract 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 193
- 239000007789 gas Substances 0.000 claims abstract description 70
- 239000007921 spray Substances 0.000 claims abstract description 52
- 238000004043 dyeing Methods 0.000 claims abstract description 13
- 238000007639 printing Methods 0.000 claims abstract description 13
- 239000000779 smoke Substances 0.000 claims abstract description 10
- 238000000926 separation method Methods 0.000 claims description 60
- 238000011084 recovery Methods 0.000 claims description 51
- 238000000746 purification Methods 0.000 claims description 14
- 239000004071 soot Substances 0.000 claims description 9
- 230000005484 gravity Effects 0.000 claims description 7
- 239000003517 fume Substances 0.000 claims description 6
- 238000004513 sizing Methods 0.000 claims description 5
- 238000012546 transfer Methods 0.000 claims description 5
- 238000005406 washing Methods 0.000 claims description 5
- 239000013589 supplement Substances 0.000 claims description 4
- 238000005192 partition Methods 0.000 claims description 3
- 241001061823 Plagopterus Species 0.000 claims description 2
- 239000012535 impurity Substances 0.000 claims description 2
- 239000002184 metal Substances 0.000 claims description 2
- 238000005507 spraying Methods 0.000 abstract description 11
- 239000000428 dust Substances 0.000 abstract description 9
- 230000000694 effects Effects 0.000 abstract description 6
- 238000004519 manufacturing process Methods 0.000 abstract description 6
- 238000000034 method Methods 0.000 abstract description 5
- 238000001914 filtration Methods 0.000 abstract description 3
- 230000008569 process Effects 0.000 abstract description 3
- 230000007613 environmental effect Effects 0.000 abstract description 2
- 238000009434 installation Methods 0.000 abstract description 2
- 230000003068 static effect Effects 0.000 abstract description 2
- 230000003247 decreasing effect Effects 0.000 abstract 1
- 235000019198 oils Nutrition 0.000 description 46
- 239000000835 fiber Substances 0.000 description 8
- 239000007788 liquid Substances 0.000 description 6
- 239000003595 mist Substances 0.000 description 6
- 238000004880 explosion Methods 0.000 description 4
- 239000002245 particle Substances 0.000 description 3
- 239000002351 wastewater Substances 0.000 description 3
- 238000009825 accumulation Methods 0.000 description 2
- 230000008859 change Effects 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 238000003912 environmental pollution Methods 0.000 description 2
- 239000004744 fabric Substances 0.000 description 2
- 230000000630 rising effect Effects 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 206010000369 Accident Diseases 0.000 description 1
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 238000000889 atomisation Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000005238 degreasing Methods 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000002360 explosive Substances 0.000 description 1
- 239000003546 flue gas Substances 0.000 description 1
- 238000002309 gasification Methods 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 230000017525 heat dissipation Effects 0.000 description 1
- 230000006698 induction Effects 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 235000019476 oil-water mixture Nutrition 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 238000004804 winding Methods 0.000 description 1
- 210000002268 wool Anatomy 0.000 description 1
Classifications
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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
-
- D—TEXTILES; PAPER
- D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
- D06C—FINISHING, DRESSING, TENTERING OR STRETCHING TEXTILE FABRICS
- D06C7/00—Heating or cooling textile fabrics
- D06C7/02—Setting
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2258/00—Sources of waste gases
- B01D2258/02—Other waste gases
- B01D2258/0283—Flue gases
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2259/00—Type of treatment
- B01D2259/65—Employing advanced heat integration, e.g. Pinch technology
- B01D2259/655—Employing advanced heat integration, e.g. Pinch technology using heat storage materials
- B01D2259/657—Employing advanced heat integration, e.g. Pinch technology using heat storage materials using latent heat, e.g. with phase change materials
Landscapes
- Engineering & Computer Science (AREA)
- Textile Engineering (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrostatic Separation (AREA)
- Treating Waste Gases (AREA)
Abstract
Description
技术领域 technical field
本发明涉及一种节能环保装置,主要是印染业定型机设备运行过程中产生的高温含油尘废气的余热回收利用、油烟油回收及净化处理设备。 The invention relates to an energy-saving and environment-friendly device, which is mainly used for waste heat recovery and utilization of high-temperature oily dust-containing waste gas generated during the operation of printing and dyeing industry setting machine equipment, oil fume oil recovery and purification treatment equipment.
背景技术 Background technique
随着我国工业持续快速的发展,工业生产也给环境带来了一定程度的污染,特别是废气问题,如果不加以净化处理,直接排放到大气中,将严重危害到人们的健康。 With the continuous and rapid development of my country's industry, industrial production has also brought a certain degree of pollution to the environment, especially the problem of exhaust gas. If it is not purified and treated, it will be directly discharged into the atmosphere, which will seriously endanger people's health.
印染行业的定型机排放的废气是高温热气体,其温度在180℃左右。废气含有油烟气、尘和织物纤维等各种有害成份。如果把废气直接排放到大气中,既不环保,也不节能,所以现在的定型机废气都要求达标排放,以节约能源和减少环境污染。 The waste gas emitted by the setting machine in the printing and dyeing industry is a high-temperature hot gas, and its temperature is about 180 °C. Exhaust gas contains various harmful components such as oil fume, dust and fabric fibers. If the exhaust gas is directly discharged into the atmosphere, it is neither environmentally friendly nor energy-saving. Therefore, the exhaust gas of the current setting machine is required to meet the standard discharge in order to save energy and reduce environmental pollution.
针对目前的定型机废气处理,大多数印染企业只是简单地将废气由风机从管道正吸入式送入过滤网,经过滤网的简单分离后,就直接排放在大气中。其设备简陋,过滤效果差,排到大气中的气体含有大量纤维粉尘和烟油等成份,烟气为蓝灰色气体。不仅如此,废气处理系统的引风系统风道过长、直径大、可燃可爆性气体容量大、油渍及纤维粉尘易在风道壁上积存。而且多台定型机所产生的废气先通过引风系统风道一并集中到集风箱内,再将存于集风箱内的废气引入净化装置进行处理排放。这样的处理过程存在很大隐患,当废气浓度达到爆炸极限或着火条件时,一旦遇有静电火花或明火及热量聚集过多而产生的自燃明火时就会发生爆炸或火灾事故。 For the current exhaust gas treatment of setting machines, most printing and dyeing enterprises simply suck the exhaust gas from the pipeline into the filter screen through the fan, and discharge it directly into the atmosphere after simple separation by the filter screen. The equipment is simple, the filtering effect is poor, and the gas discharged into the atmosphere contains a lot of fiber dust and smoke oil, and the smoke is blue-gray gas. Not only that, the air duct of the air induction system of the exhaust gas treatment system is too long, the diameter is large, the capacity of flammable and explosive gas is large, and oil stains and fiber dust are easy to accumulate on the wall of the air duct. Moreover, the waste gas generated by multiple setting machines is first collected into the wind collecting box through the air duct of the induced draft system, and then the waste gas stored in the wind collecting box is introduced into the purification device for treatment and discharge. There are great hidden dangers in such a treatment process. When the exhaust gas concentration reaches the explosion limit or fire conditions, an explosion or fire accident will occur in case of static sparks or open flames and self-igniting open flames caused by excessive heat accumulation.
为了提高经济效益,在较大规模的印染企业,已经对现有的定型机的废气进行了综合治理,主要包括回收废气余热及废气中的烟油,然后通过净化器雾化洗涤或高压静电装置净化废气而达标排放。根据实际调查,考虑到实际定型机的操作及印染企业防火防爆要求,目前已有的余热回收设备并不能充分利用高温废气热能,经热回收后的废气送到净化器,在净化器内洗涤净化,净化器出来的油水混合液温度仍然较高,在70℃左右,需要使用风机和散热器来冷却才能循环使用水,冷却后的热风排掉,使得有价值的热能直接浪费。另外,废气余热回收与烟油回收不能同时实现,现有烟油回收器内凝结的水珠和油珠一般通过导管排到地沟里,造成浪费和二次污染。 In order to improve economic benefits, in large-scale printing and dyeing enterprises, the exhaust gas of the existing setting machine has been comprehensively treated, mainly including recovering the waste heat of the exhaust gas and the smoke oil in the exhaust gas, and then atomizing and washing through the purifier or high-voltage electrostatic device Purify exhaust gas and meet emission standards. According to the actual survey, considering the operation of the actual setting machine and the fire and explosion protection requirements of printing and dyeing enterprises, the existing waste heat recovery equipment cannot make full use of the heat energy of high-temperature exhaust gas. After heat recovery, the exhaust gas is sent to the purifier, where it is washed and purified , The temperature of the oil-water mixture from the purifier is still high, around 70°C, it needs to be cooled by fans and radiators to circulate the water, and the hot air after cooling is discharged, which makes the valuable heat energy directly wasted. In addition, waste gas waste heat recovery and e-liquid recovery cannot be realized at the same time. The water droplets and oil droplets condensed in the existing e-liquid recovery device are generally discharged into the ditch through conduits, causing waste and secondary pollution.
总体上,现有废气处理设备分散,管道长、散热面积大,管道粘油滴油,部分设备占地大,热回收率低,烟油回收率差。 In general, the existing exhaust gas treatment equipment is scattered, with long pipelines and large heat dissipation areas, oily and dripping pipelines, some equipment occupy a large area, low heat recovery rate, and poor smoke oil recovery rate.
发明内容 Contents of the invention
为了克服现有技术高温废气余热回收效率不高,油烟油回收率低及废气处理系统复杂等缺陷,本发明的目的在于提供一种定型机废气处理及余热回收装置,定型机的高温废气的余热能够得到有效提高,同时增加油烟油回收率和增强废气净化效果。 In order to overcome the defects of the prior art such as low recovery efficiency of high-temperature waste gas waste heat, low oil recovery rate and complex waste gas treatment system, the purpose of the present invention is to provide a device for waste gas treatment and waste heat recovery of a setting machine. It can be effectively improved, and at the same time, the recovery rate of soot oil is increased and the effect of exhaust gas purification is enhanced.
为达到上述目的,本发明采用的技术方案为: In order to achieve the above object, the technical scheme adopted in the present invention is:
一种余热回收式定型机废气处理装置,包括余热回收装置、废气净化装置以及烟油回收装置,其中: A waste heat recovery type waste gas treatment device for a sizing machine, including a waste heat recovery device, a waste gas purification device and a smoke oil recovery device, wherein:
余热回收装置为长方形的箱体,箱体内通过金属板分为上下两层,上层为水路,下层为高温废气流路,箱体内垂直方向布置有热管,余热回收装置的高温废气流路一侧设有进风口,进风口前设有滤网,另一侧设有热风出口; The waste heat recovery device is a rectangular box. The box is divided into upper and lower layers by metal plates. The upper layer is the water channel, and the lower layer is the high-temperature exhaust gas flow channel. Heat pipes are arranged vertically in the box. There is an air inlet, with a filter screen in front of the air inlet, and a hot air outlet on the other side;
废气净化装置包括过滤塔、喷雾头、喷淋头和高压静电装置,过滤塔为筒体结构,其内自下而上布置有喷雾头、喷淋头、一级高压静电装置和二级高压静电装置,余热回收装置的热风出口通过管道连接过滤塔下部的废气进口; The exhaust gas purification device includes a filter tower, a spray head, a spray head and a high-voltage electrostatic device. The filter tower is a cylindrical structure, and a spray head, a spray head, a first-level high-voltage electrostatic device and a second-level high-voltage electrostatic device are arranged from bottom to top. device, the hot air outlet of the waste heat recovery device is connected to the exhaust gas inlet at the lower part of the filter tower through a pipeline;
烟油回收装置包括油水收集装置和油水分离箱,一次油水收集装置设置于喷雾头下部,二次油水收集装置设置于喷淋头下部,一次油水收集装置和二次油水收集装置均采用环形倒置漏斗状布置于过滤塔内,一次油水收集装置通过管道连接一次油水分离箱顶部,一次油水收集装置的底部高于一次油水分离箱顶部,使位于一次油水收集装置内的油水由重力回流到一次油水分离箱;二次油水收集装置通过管道连接二次油水分离箱顶部,二次油水收集装置的底部高于二次油水分离箱顶部,使位于二次油水收集装置内的油水由重力回流到二次油水分离箱; The smoke oil recovery device includes an oil-water collection device and an oil-water separation box. The primary oil-water collection device is set at the lower part of the spray head, and the secondary oil-water collection device is set at the lower part of the spray head. Both the primary oil-water collection device and the secondary oil-water collection device use annular inverted funnels The primary oil-water collection device is connected to the top of the primary oil-water separation tank through pipes, and the bottom of the primary oil-water collection device is higher than the top of the primary oil-water separation tank, so that the oil and water in the primary oil-water collection device flow back to the primary oil-water separation tank by gravity. tank; the secondary oil-water collection device is connected to the top of the secondary oil-water separation box through pipelines, and the bottom of the secondary oil-water collection device is higher than the top of the secondary oil-water separation box, so that the oil and water in the secondary oil-water collection device flow back to the secondary oil-water by gravity separation box;
高温废气经滤网粗滤除去大杂物,利用热管高效传热原理,高温废气被热管冷却进入过滤塔,余热回收装置上层的冷水被加热后用于补充印染所需热水;废气被喷雾头雾化洗涤,废气中的油烟油及挥发性气体随水落入一次油水收集装置;雾化后的废气经喷淋头喷淋水除雾后,大部分水二次油水收集装置收集;喷淋后的废气由一级高压静电装置和二级高压静电装置捕获细小的油烟和除去部分废气中的臭气,净化后的达标废气从过滤塔的顶部经排气管道排入大气。 The high-temperature exhaust gas is filtered through the filter to remove large impurities. Using the principle of high-efficiency heat transfer of the heat pipe, the high-temperature exhaust gas is cooled by the heat pipe and enters the filter tower. The cold water on the upper layer of the waste heat recovery device is heated and used to supplement the hot water required for printing and dyeing; Atomized washing, soot oil and volatile gas in the exhaust gas fall into the primary oil-water collection device with water; after the atomized exhaust gas is sprayed by the spray head to demist, most of the water is collected by the secondary oil-water collection device; The final exhaust gas is captured by the first-level high-voltage electrostatic device and the second-level high-voltage electrostatic device to capture fine oil fumes and remove part of the odor in the exhaust gas. The purified exhaust gas is discharged into the atmosphere from the top of the filter tower through the exhaust pipe.
本发明中,余热回收装置上层内设有导流板,使冷水在余热回收装置上层内作“S”形流动,导流节数可以采用2节、4节甚至多节;热管上半部分浸没在水中,出水管路安装温度控制阀,进水管路安装浮球阀。 In the present invention, a guide plate is provided in the upper layer of the waste heat recovery device, so that the cold water flows in an "S" shape in the upper layer of the waste heat recovery device, and the number of guide nodes can be 2, 4 or even more; In the water, a temperature control valve is installed in the water outlet pipeline, and a float valve is installed in the water inlet pipeline.
本发明中,位于余热回收装置下层的热管采用缠绕翅片形式置于高温废气流路中。 In the present invention, the heat pipes located in the lower layer of the waste heat recovery device are placed in the high-temperature exhaust gas flow path in the form of wound fins.
本发明中,喷雾头采用多个,喷雾面覆盖整个过滤塔的横截面。 In the present invention, multiple spray heads are used, and the spray surface covers the cross section of the entire filter tower.
本发明中,喷淋头采用多个,喷淋面覆盖整个过滤塔的横截面。 In the present invention, multiple spray heads are used, and the spray surface covers the entire cross section of the filter tower.
本发明中,喷雾头和喷淋头分别通过管道与相应的水泵连接。 In the present invention, the spray head and the shower head are respectively connected with corresponding water pumps through pipelines.
本发明中,一级油水分离箱和二级油水分离箱内均设有高于水液面的隔板,底部开孔,通过所述孔连接水泵,由水泵将水输送至喷雾头或喷淋头;一次油水分离箱或二级油水分离箱均设有油水分离箱进水阀、油水分离箱排水阀和手动控制阀门。 In the present invention, both the first-stage oil-water separation tank and the second-stage oil-water separation tank are provided with partitions higher than the water level, and holes are opened at the bottom, and a water pump is connected through the hole, and the water is delivered to the spray head or spray nozzle by the water pump. Head; primary oil-water separation tank or secondary oil-water separation tank is equipped with oil-water separation tank inlet valve, oil-water separation tank drain valve and manual control valve.
本发明中,一次油水分离箱和二次油水分离箱之间设置溢流管。 In the present invention, an overflow pipe is arranged between the primary oil-water separation box and the secondary oil-water separation box.
由于由定型机排出的高温废气中含油烟油和布纤维,在进入余热回收箱体前安装粗滤装置,在粗滤装置的滤网分离下,大纤维尘得到初步过滤,从而避免大纤维与油滴粘贴在换热管上,增加换热热阻,降低换热效果,同时也可以避免大纤维与油滴的长期聚集而导致的着火爆炸危险。另外,该滤网易于拆卸,便于维护人员经常更换。 Since the high-temperature exhaust gas discharged from the setting machine contains oily smoke oil and cloth fibers, a coarse filter device is installed before entering the waste heat recovery box. Under the separation of the filter screen of the coarse filter device, the large fiber dust is preliminarily filtered, thereby avoiding the large fiber and oil Droplets are pasted on the heat exchange tubes to increase the heat transfer resistance and reduce the heat transfer effect. At the same time, it can also avoid the danger of fire and explosion caused by the long-term accumulation of large fibers and oil droplets. In addition, the filter screen is easy to disassemble, which is convenient for maintenance personnel to replace frequently.
为了将高温废气的热能有效回收,同时又要使得换热器简单且易于维护,余热回收箱体采用上下分层设计,利用热管冷端置于箱体下层用于高温废气换热,吸收废气热能,降低废气温度。热管吸收的废气热能通过热管高效导热将热量传至箱体上层热端,热管热端与冷水换热,将加热后冷水用于预热印染所需热水。为了提高热管与废气换热效率,热管冷端即下半部分采用强化缠绕翅片;而为了提高热管与冷水换热效率,长方形箱体上层水侧采用导流板,使冷水在余热回收装置内作“之”形流动,增加换热时间,提高出水温度。另外,出水管路安装温度控制阀,待温度达到设定值时,启动水泵排水,从而使得出水温度稳定。进水管路安装浮球控制阀,液位低于设定值时,打开阀门进水,保证水侧液位维持一定高度。通过热管换热的方法,使得高温废气能够高效预热补充印染所需的热水,有利于印染企业的能源得到综合利用,同时降低烟气进入净化过滤筒体的温度,提高油烟油回收率,避免了环境污染。 In order to effectively recover the heat energy of high-temperature exhaust gas, and at the same time make the heat exchanger simple and easy to maintain, the waste heat recovery box is designed with upper and lower layers, and the cold end of the heat pipe is placed in the lower layer of the box for heat exchange of high-temperature exhaust gas and absorption of exhaust gas heat energy. , to reduce the exhaust gas temperature. The heat energy of the waste gas absorbed by the heat pipe is transferred to the hot end of the upper layer of the cabinet through the efficient heat conduction of the heat pipe, and the hot end of the heat pipe exchanges heat with the cold water, and the heated cold water is used for preheating the hot water required for printing and dyeing. In order to improve the heat exchange efficiency between the heat pipe and the exhaust gas, the cold end of the heat pipe, that is, the lower part, adopts reinforced winding fins; and in order to improve the heat exchange efficiency between the heat pipe and the cold water, the upper water side of the rectangular box adopts a deflector to make the cold water flow in the waste heat recovery device Make a "Zigzag" shape flow, increase the heat exchange time, and increase the outlet water temperature. In addition, a temperature control valve is installed in the water outlet pipeline. When the temperature reaches the set value, the water pump is started to drain water, so that the temperature of the water outlet is stable. The water inlet pipeline is equipped with a float control valve. When the liquid level is lower than the set value, the valve is opened to enter water to ensure that the liquid level on the water side maintains a certain height. Through the heat exchange method of the heat pipe, the high-temperature exhaust gas can be efficiently preheated to supplement the hot water required for printing and dyeing, which is conducive to the comprehensive utilization of energy in printing and dyeing enterprises, and at the same time reduces the temperature of the flue gas entering the purification filter cylinder, and improves the oil recovery rate. Environmental pollution is avoided.
为了提高废气中油烟油回收效率,废气净化装置采用圆柱形筒体过滤塔,筒体过滤塔内自下而上配有喷雾头、喷淋头和两级高压静电装置。含有粉尘颗粒及油烟油的气体穿过由喷雾装置形成的水雾层后,粉尘及油烟油受到集聚而吸附在油雾吸附层上,由于重力作用含油或者含尘大颗粒沉降在喷雾头下方的一次油水收集装置中。同时由于废气使部分水雾气化,废气温度进一步降低。置于喷雾头上方的喷淋头形成水幕,能够有效将上升的废气油滴和较小雾滴进一步富集在水中,并由二次油水收集装置收集。经过两次水处理的废气仍有少量有害不溶性气体,例如臭气,通过两次高压静电装置,提高废气的最终净化效率,最终将废气处理致排放标准。 In order to improve the recovery efficiency of soot oil in the exhaust gas, the exhaust gas purification device adopts a cylindrical filter tower, which is equipped with a spray head, a spray head and a two-stage high-voltage electrostatic device from bottom to top. After the gas containing dust particles and soot oil passes through the water mist layer formed by the spray device, the dust and soot oil are accumulated and adsorbed on the oil mist adsorption layer. Due to the action of gravity, the oily or dusty large particles settle under the spray head. In the primary oil and water collection device. At the same time, due to the gasification of part of the water mist by the exhaust gas, the temperature of the exhaust gas is further reduced. The spray head placed above the spray head forms a water curtain, which can effectively further enrich the rising exhaust gas oil droplets and smaller mist droplets in the water, and collect them by the secondary oil-water collection device. After two times of water treatment, the waste gas still has a small amount of harmful insoluble gas, such as odor. After passing through the high-voltage electrostatic device twice, the final purification efficiency of the waste gas is improved, and the waste gas is finally treated to the emission standard.
为了将油烟油有效回收,在过滤塔中设置倾斜状的油水收集装置,收集喷雾和喷淋的形成的含油废水。含油废水经过管路,分别进入油水分离箱。油水分离箱中间设置隔断,利用烟油密度低于水的原理,烟油自动排入含油侧。在油水分离箱底部有管路与水泵连接,水泵将分离出来的水圧送至喷雾头或者喷淋头,继续洗涤吸收废气中的油烟油。由于喷雾需要较多水分蒸发,喷淋使得喷雾造成的上升水滴继续沉降,二次油水分离箱收集的废水往往多于所需的喷淋水,采用溢流管将二次油水分离箱多余的水溢流至一次油水分离箱。同时为了保证油水分离箱中的水的除油效果稳定,设置进出口水阀,用于定期换水。 In order to effectively recover the fume oil, an inclined oil-water collection device is installed in the filter tower to collect the oily wastewater formed by spraying and spraying. The oily waste water passes through the pipeline and enters the oil-water separation tank respectively. A partition is set in the middle of the oil-water separation box. Using the principle that the density of e-liquid is lower than that of water, the e-liquid is automatically discharged into the oil-containing side. At the bottom of the oil-water separation tank, there is a pipeline connected to the water pump, and the water pump sends the separated water to the spray head or shower head to continue washing and absorbing the soot oil in the exhaust gas. Since spraying requires more water to evaporate, spraying makes the rising water droplets caused by spraying continue to settle, and the waste water collected by the secondary oil-water separation box is often more than the required spray water. The overflow pipe is used to drain the excess water from the secondary oil-water separation box. Overflow to the primary oil-water separation tank. At the same time, in order to ensure the stable degreasing effect of the water in the oil-water separation tank, an inlet and outlet water valve is set for regular water change.
本发明的有益效果在于:运用本技术开发的产品经实测,热能回收率85%,粉尘净化效率99%,油雾去除率99%。由此可见,本发明能够有效回收定型机高温废气热能,提高了油烟油的回收率,降低了整套设备制造和安装成本。结构紧凑,占地小,节能,节水,便于制造、安装和维护,可实现达标排放,以达到环保的功效。该设备也适用于过饱和蒸汽并产生含油、含尘气体的生产制造行业。 The beneficial effect of the present invention is that: the product developed by using this technology has a thermal energy recovery rate of 85%, a dust purification efficiency of 99%, and an oil mist removal rate of 99%. It can be seen that the present invention can effectively recover the heat energy of the high-temperature waste gas of the setting machine, improve the recovery rate of soot oil, and reduce the manufacturing and installation costs of the whole set of equipment. Compact structure, small footprint, energy-saving, water-saving, easy to manufacture, install and maintain, can achieve discharge standards, in order to achieve the effect of environmental protection. This equipment is also suitable for the manufacturing industry where supersaturated steam produces oily and dusty gas.
附图说明 Description of drawings
图1为本发明的一种结构示意图: Fig. 1 is a kind of structural representation of the present invention:
图中标号:1是滤网,2是余热回收装置,3是热管,4是过滤塔,5是喷雾头,6是二次油水收集装置,7是喷淋头,8是一级高压静电装置,9是二级高压静电装置,10喷淋水泵,11是二次油水分离箱,12是溢流管,13是二次油水分离箱进水阀,14是二次油水分离箱排水阀,15是一次油水分离箱排水阀,16是一次油水分离箱,17是一次油水分离箱进水阀,18是喷雾头阀门,19是一次油水收集装置,20是导流板。 Numbers in the figure: 1 is the filter screen, 2 is the waste heat recovery device, 3 is the heat pipe, 4 is the filter tower, 5 is the spray head, 6 is the secondary oil and water collection device, 7 is the spray head, 8 is the first-level high-voltage electrostatic device , 9 is the secondary high-voltage electrostatic device, 10 is the spray pump, 11 is the secondary oil-water separation box, 12 is the overflow pipe, 13 is the water inlet valve of the secondary oil-water separation box, 14 is the drain valve of the secondary oil-water separation box, 15 16 is an oil-water separation box drain valve, 17 is an oil-water separation box inlet valve, 18 is a spray nozzle valve, 19 is an oil-water collection device, and 20 is a deflector.
具体实施方式 detailed description
下面结合附图对本发明的结构设计原理和工作原理作进一步详细说明。 The structural design principle and working principle of the present invention will be described in further detail below in conjunction with the accompanying drawings.
实施例1:在定型机的顶部设置平台或支架来安放定型机废气处理及余热回收装置,将废气余热回收装置的进气口与定型机的排气口连接,进气口有滤网1过滤随废气排出的大颗粒杂物,例如毛纤维,经过粗滤处理过的高温废气进入余热回收装置2与热管3进行换热。利用热管高效传热原理,热管加热流经的冷水,被加热后的冷水用于补充印染所需热水。 Example 1: Set up a platform or bracket on the top of the sizing machine to place the waste gas treatment and waste heat recovery device of the sizing machine, connect the air inlet of the waste gas and waste heat recovery device to the exhaust port of the sizing machine, and filter the air inlet with a filter 1 The large-particle debris discharged with the exhaust gas, such as wool fibers, and the high-temperature exhaust gas that has been coarsely filtered enter the waste heat recovery device 2 to exchange heat with the heat pipe 3 . Utilizing the efficient heat transfer principle of the heat pipe, the heat pipe heats the cold water flowing through it, and the heated cold water is used to supplement the hot water required for printing and dyeing.
高温废气被热管3冷却后,温度降低,继续进入过滤塔4。废气在过滤塔4中首先被喷雾头5雾化洗涤,在喷雾头5雾化洗涤中充分使废气中的油烟油及其它挥发性气体固化随水落下,被一次油水收集装置19收集。同时一部分雾滴气化,降低废气温度。雾化洗涤后的废气经喷淋头7喷淋水除雾后,大部分水分被而二次油水收集装置6收集。废气通过喷雾、喷淋逐级降温、净化,降温后的废气温度在50℃以下。通过两次水除油后的废气再由一级高压静电装置8和二级高压静电装置9两次捕获细小的油烟和除去部分废气中的臭气,并且在此温度下,高压静电装置将不会附着油滴,长期保持很高的净化效率,净化后的达标废气经排气管道排入大气。 After the high-temperature waste gas is cooled by the heat pipe 3, the temperature drops and continues to enter the filter tower 4. In the filter tower 4, the waste gas is first atomized and washed by the spray head 5. During the atomization and washing process of the spray head 5, the soot oil and other volatile gases in the waste gas are solidified and fall with the water, and are collected by the primary oil-water collection device 19. At the same time, part of the mist is gasified to reduce the temperature of the exhaust gas. After the atomized and washed waste gas is sprayed with water by the spray head 7 to demist, most of the water is collected by the secondary oil and water collection device 6 . The exhaust gas is cooled and purified step by step through spraying and spraying, and the temperature of the exhaust gas after cooling is below 50°C. After the waste gas has been deoiled by water for two times, the first-level high-voltage electrostatic device 8 and the second-level high-voltage electrostatic device 9 capture the fine oil fume and remove part of the odor in the waste gas twice, and at this temperature, the high-voltage electrostatic device will not It will adhere to oil droplets and maintain a high purification efficiency for a long time. The purified waste gas that meets the standard is discharged into the atmosphere through the exhaust pipe.
喷雾收集的油水沉积在一次油水收集装置19的凹槽内,最后通过过滤塔4壳体的排水口,经过管路重力回流到一次油水分离箱16内。喷淋收集的油水沉积在二次油水收集装置6的凹槽内,最后通过过滤塔4壳体的排水口,经过管路重力回流到二次油水分离箱11内。 The oil and water collected by the spray is deposited in the groove of the primary oil and water collecting device 19, and finally passes through the drain of the shell of the filter tower 4, and flows back into the primary oil and water separation tank 16 through the pipeline gravity. The oil and water collected by spraying is deposited in the groove of the secondary oil and water collecting device 6, and finally passes through the drain of the shell of the filter tower 4, and flows back into the secondary oil and water separation tank 11 through the pipeline gravity.
二次油水分离箱11和一次油水分离箱16的构造大致相同,采用隔离板,利用油比水轻的原理,将收集的废油排入油侧,实现油水分离。在油水分离箱内有过滤网过滤杂物,下端有出水口连接水泵。二次油水分离箱11和一次油水分离箱16分别通过喷淋水泵10、喷雾头阀门18将油水分离箱内的水重新循环供给喷雾头5、喷淋头7以洗涤废气。 The structure of the secondary oil-water separation box 11 and the primary oil-water separation box 16 is roughly the same, using a separation plate, and using the principle that oil is lighter than water, the collected waste oil is discharged into the oil side to realize oil-water separation. In the oil-water separation box, there is a filter screen to filter sundries, and a water outlet is connected to the water pump at the lower end. The secondary oil-water separation tank 11 and the primary oil-water separation tank 16 respectively recirculate the water in the oil-water separation tank to the spray head 5 and the spray head 7 through the spray water pump 10 and the spray head valve 18 to wash the waste gas.
由于二次油水收集装置6收集得到的油水明显多于喷淋头7的喷淋水量,因此二次油水分离箱11的回水量多于泵出水量。而一次油水收集装置19收集得到的油水明显少于喷雾头5的喷雾水量,因此一次油水收集箱16的回水量少于喷淋水量。综合考虑,采用溢流管12调节两台油水收集装置的水量,使得一次油水收集装置19不需要频繁补水,从而达到节约用水的目的。 Since the oil-water collected by the secondary oil-water collection device 6 is obviously more than the spray water volume of the spray head 7, the return water volume of the secondary oil-water separation tank 11 is more than the pumped water volume. And the oil-water collected by the primary oil-water collecting device 19 is obviously less than the spraying water quantity of the spray head 5, so the return water quantity of the primary oil-water collecting box 16 is less than the spraying water quantity. Considering comprehensively, the overflow pipe 12 is used to adjust the water volume of the two oil-water collection devices, so that the primary oil-water collection device 19 does not need to replenish water frequently, thereby achieving the purpose of saving water.
另外,考虑到用于洗涤废气的水不能长时间使用,否则会降低除油效率,因此油水分离装置的水需要定期更换。在两台油水收集装置前后分别安装一次油水分离箱进水阀17、二次油水分离箱进水阀13和一次油水分离箱排水阀15、二次油水分离箱排水阀14,实现定期换水目的。 In addition, considering that the water used to wash the exhaust gas cannot be used for a long time, otherwise the oil removal efficiency will be reduced, so the water in the oil-water separation device needs to be replaced regularly. Install the water inlet valve 17 of the primary oil-water separation box, the water inlet valve 13 of the secondary oil-water separation box, the drain valve 15 of the primary oil-water separation box, and the drain valve 14 of the secondary oil-water separation box before and after the two oil-water collection devices, so as to realize the purpose of regular water change .
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