CN104406210A - Cooking fume treating device - Google Patents
Cooking fume treating device Download PDFInfo
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- CN104406210A CN104406210A CN201410670468.1A CN201410670468A CN104406210A CN 104406210 A CN104406210 A CN 104406210A CN 201410670468 A CN201410670468 A CN 201410670468A CN 104406210 A CN104406210 A CN 104406210A
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- hot water
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- 239000003517 fume Substances 0.000 title claims abstract description 51
- 238000010411 cooking Methods 0.000 title claims abstract description 16
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 30
- 238000009833 condensation Methods 0.000 claims abstract description 21
- 230000005494 condensation Effects 0.000 claims abstract description 21
- 238000011282 treatment Methods 0.000 claims abstract description 19
- 239000007789 gas Substances 0.000 claims abstract description 13
- KRHYYFGTRYWZRS-UHFFFAOYSA-M Fluoride anion Chemical compound [F-] KRHYYFGTRYWZRS-UHFFFAOYSA-M 0.000 claims abstract description 10
- 238000003860 storage Methods 0.000 claims abstract description 10
- 239000000523 sample Substances 0.000 claims abstract description 7
- 239000003795 chemical substances by application Substances 0.000 claims abstract 3
- 238000010438 heat treatment Methods 0.000 claims description 5
- 239000000779 smoke Substances 0.000 claims 5
- 229920002521 macromolecule Polymers 0.000 claims 2
- 239000007921 spray Substances 0.000 claims 2
- 239000012855 volatile organic compound Substances 0.000 abstract description 15
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 abstract description 11
- 239000003546 flue gas Substances 0.000 abstract description 11
- 229920000642 polymer Polymers 0.000 abstract description 9
- 239000012756 surface treatment agent Substances 0.000 abstract description 7
- 238000004140 cleaning Methods 0.000 abstract description 4
- 238000010521 absorption reaction Methods 0.000 abstract description 3
- 238000012856 packing Methods 0.000 abstract description 2
- 239000003921 oil Substances 0.000 description 34
- 235000019198 oils Nutrition 0.000 description 34
- 238000000034 method Methods 0.000 description 17
- 239000003344 environmental pollutant Substances 0.000 description 10
- 231100000719 pollutant Toxicity 0.000 description 10
- 239000000126 substance Substances 0.000 description 7
- 238000005516 engineering process Methods 0.000 description 6
- 238000000746 purification Methods 0.000 description 6
- 239000012530 fluid Substances 0.000 description 5
- 239000007788 liquid Substances 0.000 description 5
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 4
- 239000002245 particle Substances 0.000 description 4
- 238000012545 processing Methods 0.000 description 4
- 238000005338 heat storage Methods 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- 238000009835 boiling Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000008157 edible vegetable oil Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000004924 electrostatic deposition Methods 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 238000011044 inertial separation Methods 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- 238000005507 spraying Methods 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 1
- 150000001335 aliphatic alkanes Chemical class 0.000 description 1
- 150000001336 alkenes Chemical class 0.000 description 1
- 150000004945 aromatic hydrocarbons Chemical class 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000000284 extract Substances 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 238000011221 initial treatment Methods 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 239000013618 particulate matter Substances 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 239000004071 soot Substances 0.000 description 1
- 238000004381 surface treatment Methods 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 238000004227 thermal cracking Methods 0.000 description 1
- 238000005979 thermal decomposition reaction Methods 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- 235000015112 vegetable and seed oil Nutrition 0.000 description 1
- 239000008158 vegetable oil Substances 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24C—DOMESTIC STOVES OR RANGES ; DETAILS OF DOMESTIC STOVES OR RANGES, OF GENERAL APPLICATION
- F24C15/00—Details
- F24C15/20—Removing cooking fumes
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Treating Waste Gases (AREA)
- Ventilation (AREA)
Abstract
一种饮食业油烟处理装置,由集气罩、引风机、旋风分离器、油烟冷凝箱和热泵装置组成,,引风机、旋风分离器与油烟冷凝箱通过管道串联连接,内壁采用氟化物高分子表面处理剂进行喷涂处理,旋风分离器内部设有吸收填料,底部设有排污阀a;油烟冷凝箱顶部设有排气管,底部设有排污阀b;热泵装置由压缩机、蒸发器、风机、膨胀阀、冷凝器和蓄热水箱组成,蓄热水箱内部设有循环水泵并与冷凝器进行换热,蓄热水箱外部设有温控探头和热水出水管。本发明的优点是:该装置采用热泵换热,节约电能,降低运行费用;采用氟化物高分子表面处理剂对烟气冷凝箱做处理,能够最大限度减少清洗次数;能够回收挥发性有机化合物并提供热水。
A cooking fume treatment device in the catering industry, which consists of a gas collecting hood, an induced draft fan, a cyclone separator, a fume condensation box and a heat pump device. The induced draft fan, the cyclone separator and the fume condensation box are connected in series through pipes, and the inner wall is made of fluoride polymer surface The treatment agent is sprayed, the cyclone separator is equipped with absorption packing, and the bottom is equipped with a drain valve a; the top of the oil fume condensation box is equipped with an exhaust pipe, and the bottom is equipped with a drain valve b; the heat pump device consists of a compressor, an evaporator, a fan, It consists of an expansion valve, a condenser and a hot water storage tank. A circulating water pump is installed inside the hot storage tank to exchange heat with the condenser. A temperature control probe and a hot water outlet pipe are installed outside the hot water storage tank. The advantages of the present invention are: the device uses a heat pump to exchange heat, saves electric energy, and reduces operating costs; uses a fluoride polymer surface treatment agent to treat the flue gas condensation box, which can minimize the number of cleanings; can recover volatile organic compounds and Hot water is provided.
Description
技术领域 technical field
本发明涉及环保技术中的污染物治理与节能减排,特别是一种饮食业油烟处理装置。 The invention relates to pollutant treatment and energy saving and emission reduction in environmental protection technology, in particular to a cooking fume treatment device for catering industry. the
背景技术 Background technique
饮食业油烟是指食物烹饪加工过程中挥发的油脂、有机质及其加热分解或裂解产物,其中污染物可大致分为三类:固态颗粒、微型液滴和气态可挥发性有机污染物(Volatile Organic Compounds,VOC)。我国的餐饮业油烟排放量、污染物排放种类与菜系、规模等条件关系密切,污染物种类包括烷烃、烯烃、芳香烃和含氧化合物等等。随着社会的发展和服务业的长足进步,餐饮业油烟已成为城市大气不可忽视的污染源。2010年我国精制食用植物油产量3878.54×104t,其中城镇居民平均每人每年购买食用植物油8.84kg,农村为6.31kg,则居民每年消耗植物油1015.57×104t。烹饪油烟VOCs排放因子为5.03g/kg,则每年仅家庭烹饪可产生VOCs5.1×104t。 Catering fume refers to the volatilized oil, organic matter and thermal decomposition or cracking products during food cooking and processing. The pollutants can be roughly divided into three categories: solid particles, micro-droplets and gaseous volatile organic compounds (Volatile Organic Compounds). , VOC). my country's catering industry's soot emissions and types of pollutant emissions are closely related to the cuisine, scale and other conditions. The types of pollutants include alkanes, olefins, aromatic hydrocarbons, and oxygen-containing compounds. With the development of society and the great progress of the service industry, cooking fumes from the catering industry have become a pollution source that cannot be ignored in cities. In 2010, the output of refined edible vegetable oil in China was 3878.54×10 4 t, among which urban residents purchased an average of 8.84kg of edible vegetable oil per person per year, and 6.31kg in rural areas, and residents consumed 1015.57×10 4 t of vegetable oil per year. If the VOCs emission factor of cooking fumes is 5.03g/kg, only household cooking can produce 5.1×10 4 t of VOCs per year.
我国早在2001年出台《饮食业油烟排放标准(试行)》(GB18483-2001),对饮食业单位油烟的最高允许排放浓度和油烟净化设备的最低去除率进行了规定。但“试行”多年仍无更加细致的标准出台,也在一定程度上说明了该类污染源控制的复杂性和治理技术的不成熟,社会急需一种适合大面积推广应用的饮食业油烟污染物治理的成熟技术。 As early as 2001, my country promulgated the "Catering Fume Emission Standard (Trial)" (GB18483-2001), which stipulated the maximum allowable emission concentration of cooking fume and the minimum removal rate of cooking fume purification equipment in the catering industry. However, no more detailed standards have been issued after many years of "trial implementation", which also explains to a certain extent the complexity of the control of this type of pollution source and the immature treatment technology. Mature technology. the
现有的油烟治理技术有惯性分离法、普通过滤法、活性炭吸附法、液体洗涤法、静电沉积法等多种工艺,均具有各自的局限性。如惯性分离法和过滤法中,由于油烟中颗粒物粘度大,清洗维护工作相当困难;活性炭吸附法必须经常更换滤料,运行成本较高;液体洗涤法和静电沉积法则分别易产生废水及臭氧等二次污染,未能彻底解决污染问题。另外,上述技术均只注重于颗粒物的去除,而对烟气中的VOC物质作用较小,污染物去除不彻底。因此,从油烟成分的物理化学性质进行分析,开发一种油烟净化方法,低能耗高效率地去除气、液、固三态污染物质,同时不产生二次污染,具有极其重要的现实意义。 The existing oil fume control technologies include inertial separation method, ordinary filtration method, activated carbon adsorption method, liquid washing method, electrostatic deposition method and other processes, all of which have their own limitations. For example, in the inertial separation method and the filtration method, due to the high viscosity of the particles in the oil fume, the cleaning and maintenance work is quite difficult; the activated carbon adsorption method must frequently replace the filter material, and the operating cost is high; the liquid washing method and the electrostatic deposition method are easy to produce waste water and ozone, etc. Secondary pollution, failed to completely solve the pollution problem. In addition, the above technologies only focus on the removal of particulate matter, but have little effect on VOC substances in the flue gas, and the removal of pollutants is not complete. Therefore, it is of extremely important practical significance to analyze the physical and chemical properties of oil fume components and develop a method for oil fume purification that can remove gas, liquid, and solid pollutants with low energy consumption and high efficiency without causing secondary pollution. the
由于饮食业油烟中的污染物质主要包括微型液固颗粒和VOC物质,VOC的定义为熔点低于室温而沸点在50-260℃之间的挥发性有机化合物,因此,采用特制的热泵系统将废气中的温度抽离,将废气降低至一定温度使VOC物质冷凝成为液态,结合一定的物理净化方式,整合出一套处理系统,完成对饮食业油烟的深度处理,同时提供温度用来产出热水供用户使用。这是一种新型、高效同时环境友好的油烟清洁技术,同时产生热水。 Since the pollutants in the oil fume of the catering industry mainly include microscopic liquid-solid particles and VOC substances, VOC is defined as a volatile organic compound whose melting point is lower than room temperature and boiling point is between 50-260°C. The temperature is extracted, the exhaust gas is lowered to a certain temperature to condense the VOC substances into a liquid state, combined with a certain physical purification method, a set of treatment system is integrated to complete the advanced treatment of cooking fumes in the catering industry, and at the same time provide temperature to produce hot water for supply user use. This is a new, efficient and environmentally friendly oil fume cleaning technology, while generating hot water. the
发明内容 Contents of the invention
本发明的目的是针对上述存在问题,提供一种饮食业油烟处理装置, The purpose of the present invention is to address the above problems, to provide a cooking fume treatment device,
本发明的技术方案: Technical scheme of the present invention:
一种饮食业油烟处理装置,由集气罩、引风机、旋风分离器、油烟冷凝箱和热泵装置组成,集气罩位于灶台上方,引风机、旋风分离器与油烟冷凝箱通过管道串联连接,旋风分离器内壁采用氟化物高分子表面处理剂进行喷涂处理,旋风分离器内部设有吸收填料,底部设有排污阀a;油烟冷凝箱顶部设有排气管,底部设有排污阀b;热泵装置由压缩机、蒸发器、风机、膨胀阀、冷凝器和蓄热水箱组成,其中蒸发器、膨胀阀和冷凝器位于油烟冷凝箱内与油烟直接接触,同样采用氟化物高分子表面处理剂进行喷涂处理,蓄热水箱内部设有循环水泵并通过循环管道与冷凝器进行换热,蓄热水箱外部设有温控探头和热水出水管。 An oil fume treatment device for the catering industry, which consists of an air collecting hood, an induced draft fan, a cyclone separator, an oil fume condensation box and a heat pump device. The air collecting hood is located above the stove, and the induced draft fan, the cyclone separator and the oil fume condensation box are connected in series through pipelines. The inner wall of the cyclone separator is sprayed with a fluoride polymer surface treatment agent. The cyclone separator is equipped with an absorption filler and a drain valve a at the bottom; an exhaust pipe is installed on the top of the oil fume condensation box, and a drain valve b is installed at the bottom; the heat pump The device is composed of compressor, evaporator, fan, expansion valve, condenser and hot water storage tank. The evaporator, expansion valve and condenser are located in the oil fume condensation box and are in direct contact with the oil fume. Fluoride polymer surface treatment agent is also used For spraying treatment, there is a circulating water pump inside the hot water storage tank and heat exchange with the condenser through a circulating pipe, and a temperature control probe and a hot water outlet pipe are installed outside the hot water storage tank. the
所述灶台发热功率与集气罩投影面积的比例为1.67×108J/h: 1.1m2。 The ratio of the heating power of the stove to the projected area of the gas collecting hood is 1.67×10 8 J/h: 1.1m 2 .
所述热泵装置的压缩机工质为R134a。 The compressor working fluid of the heat pump device is R134a. the
本发明的优点是: The advantages of the present invention are:
该装置中烟气冷凝箱采用热泵装置换热,在达到去除要求的前提下,节约电能,降低运行费用;采用氟化物高分子表面处理剂对烟气冷凝箱做处理,能够最大限度减少清洗次数;能够回收挥发性有机化合物并提供热水。 The flue gas condensation box in the device uses a heat pump device for heat exchange, which saves electricity and reduces operating costs on the premise of meeting the removal requirements; the flue gas condensation box is treated with a fluoride polymer surface treatment agent, which can minimize the number of cleanings ; capable of recovering volatile organic compounds and providing hot water.
附图说明 Description of drawings
图1为饮食业油烟二级处理装置示意图。 Figure 1 is a schematic diagram of a secondary treatment device for oil fume in the catering industry. the
图2为热泵装置结构示意图。 Fig. 2 is a schematic diagram of the structure of the heat pump device. the
图中:1.灶台, 2.集气罩, 3.引风机, 4.旋风分离器, 5.油烟冷凝箱,6.热泵式换热器, 7.排污阀a 8.排气管, 9.排污阀b 10.压缩机, In the figure: 1. Cooktop, 2. Gas collecting hood, 3. Induced fan, 4. Cyclone separator, 5. Oil fume condensation box, 6. Heat pump heat exchanger, 7. Drain valve a 8. Exhaust pipe, 9. Drain valve b 10. Compressor,
11.蒸发器, 12.风机, 13.膨胀阀, 14.冷凝器, 15.温控探头, 11. Evaporator, 12. Fan, 13. Expansion valve, 14. Condenser, 15. Temperature control probe,
16.蓄热水箱, 17.热水出水管。 16. Hot water storage tank, 17. Hot water outlet pipe.
具体实施方式 Detailed ways
下面结合具体实施例对本发明进行进一步描述,但本发明的保护范围并不仅限于此。 The present invention will be further described below in conjunction with specific examples, but the protection scope of the present invention is not limited thereto. the
实施例: Example:
一种饮食业油烟处理装置,如图1、2所示,由集气罩2、引风机3、旋风分离器4、油烟冷凝箱5和热泵装置6组成,集气罩位于灶台1上方,引风机3、旋风分离器4与油烟冷凝箱5通过管道串联连接,旋风分离器4内壁采用氟化物高分子表面处理剂进行喷涂处理,旋风分离器内部设有吸收填料,底部设有排污阀a7;油烟冷凝箱5顶部设有排气管8,底部设有排污阀b9;热泵装置由压缩机10、蒸发器11、风机12、膨胀阀13、冷凝器14、温控探头15和蓄热水箱16组成,其中蒸发器11、膨胀阀13和冷凝器14位于油烟冷凝箱5内与油烟直接接触,同样采用氟化物高分子表面处理剂进行喷涂处理,蓄热水箱5内部设有循环水泵并通过循环管道与冷凝器14进行换热,蓄热水箱5外部设有温控探头15和热水出水管17。 An oil fume treatment device for the catering industry, as shown in Figures 1 and 2, consists of an air collecting hood 2, an induced draft fan 3, a cyclone separator 4, an oil fume condensation box 5, and a heat pump device 6. The air collecting hood is located above the stove 1, and the induced Fan 3, cyclone separator 4 and oil fume condensation box 5 are connected in series through pipelines, the inner wall of cyclone separator 4 is sprayed with fluoride polymer surface treatment agent, the interior of cyclone separator is provided with absorption packing, and the bottom is provided with sewage valve a7; The top of the oil fume condensation box 5 is provided with an exhaust pipe 8, and the bottom is provided with a drain valve b9; the heat pump device consists of a compressor 10, an evaporator 11, a fan 12, an expansion valve 13, a condenser 14, a temperature control probe 15 and a heat storage tank 16 components, wherein the evaporator 11, expansion valve 13 and condenser 14 are located in the oil fume condensation tank 5 and are in direct contact with the oil fume. The fluoride polymer surface treatment agent is also used for spraying treatment. The inside of the heat storage tank 5 is equipped with a circulating water pump and Heat is exchanged with the condenser 14 through the circulation pipe, and a temperature control probe 15 and a hot water outlet pipe 17 are provided outside the heat storage tank 5 .
该实施例中,灶台发热功率与集气罩投影面积的比例为1.67×108J/h: 1.1m2;热泵装置的压缩机工质为R134a。 In this embodiment, the ratio of the heating power of the stove to the projected area of the gas collecting hood is 1.67×10 8 J/h: 1.1m 2 ; the working fluid of the compressor of the heat pump device is R134a.
该装置的工作方法: How the device works:
首先对油烟进行有序收集,然后对油烟进行旋风分离以去除颗粒态污染物,最终进入热泵冷凝系统,将烟气温度冷凝至主要VOC污染物的沸点以下,使VOC物质变为液态,完成对烟气的深度净化。热泵系统在冷凝烟气的同时,将烟气的温度抽提用于产生热水,供用户使用。具体方法如下: First, the oil fume is collected in an orderly manner, and then the oil fume is cyclone separated to remove particulate pollutants, and finally enters the heat pump condensing system to condense the temperature of the flue gas below the boiling point of the main VOC pollutants, so that the VOC substances become liquid and complete the purification process. Deep purification of flue gas. While condensing the flue gas, the heat pump system extracts the temperature of the flue gas to generate hot water for users. The specific method is as follows:
1)首先对油烟进行收集 1) First collect the oil fume
在厨房灶台上方合适位置设置捕集型上部集气罩,每个基准灶台发热功率为1.67×108J/h,对应的集气罩投影面积为1.1m2,同理大型单位则按照此基准增加集气罩面积,其他规定参考GB18483-2001《饮食业油烟排放标准(试行)》,设置引风机一端与集气罩连接,一端为排放管道与处理设备连接,引风机的风量按照标准设计,当灶台工作时开启引风机,油烟将被有序收集进入排放管道,进入后续的处理装置。 Set up a trapping upper gas collection hood at a suitable position above the kitchen stove. The heating power of each reference stove is 1.67×10 8 J/h, and the corresponding projected area of the gas collection hood is 1.1m 2 . This benchmark increases the area of the gas collecting hood. For other regulations, refer to GB18483-2001 "Catering Fume Emission Standard (Trial)". One end of the induced draft fan is connected to the gas collecting hood, and the other end is connected to the discharge pipe and the processing equipment. The air volume of the induced draft fan is designed according to the standard. , When the cooktop is working, the induced draft fan is turned on, and the oil fume will be collected in an orderly manner into the discharge pipe and then into the subsequent processing device.
2)上述经收集的油烟进入由旋风分离器组成的一级处理装置,内部采用特制高分子表面处理剂进行喷涂处理,以降低油类物质的粘附。油烟经管道由下部进入分离器,在螺旋上升过程中,油烟中的重组分在离心力的作用下,与分离器锥体碰撞后被截留,最终在锥斗中富集,积累一定时间后可以通过锥斗底部的阀门排放出系统。经过一级净化的油烟上升进入排放管,进入后续的处理装置。 2) The above-mentioned collected oil fume enters the first-stage treatment device composed of cyclone separator, and the interior is sprayed with a special polymer surface treatment agent to reduce the adhesion of oil substances. The oil fume enters the separator from the lower part through the pipeline. During the spiral rising process, the heavy components in the oil fume are intercepted after colliding with the cone of the separator under the action of centrifugal force, and finally enriched in the cone bucket. After accumulating for a certain period of time, they can pass through the separator. A valve at the bottom of the cone discharges out of the system. The oil fume after primary purification rises into the discharge pipe and enters the subsequent processing device. the
3)二级处理装置由热泵系统及其保护装置组成,为适应烟气工作环境,需要对热泵装置暴露在烟气中的组件:蒸发器、冷凝器、膨胀阀进行保护,采用氟化物高分子表面处理,置于二级装置进气口内,用于截留一级处理中未被分离的油滴或颗粒物,此种做法能够较好地保护热泵系统的换热器短时间内受到污染而降低热传递效率。热泵换热器在换热过程中,蒸发器吸收烟气热量提供给蒸发器内部的压缩机工质,冷凝器中的工质将热量输送给需要加热的水。经过预处理后的油烟被风机抽入热泵系统,冷凝降温后排出,冷风与油烟混合进一步降低整个箱体中油烟的温度,从而使VOC物质液化,被截留在箱体内部,最终从箱体中锥斗排出系统,经冷凝后的温度则达标排放。热水产出采用循环进水加热的方式运行,水箱出水温度可以在35-70℃之间调节,由温控探头控制,热水产量由配风量及压缩机、工质选择相关。 3) The secondary treatment device is composed of a heat pump system and its protection device. In order to adapt to the flue gas working environment, it is necessary to protect the components of the heat pump device exposed to the flue gas: evaporator, condenser, and expansion valve, and use fluoride polymer Surface treatment, placed in the air inlet of the secondary device, is used to intercept oil droplets or particles that have not been separated in the primary treatment. This method can better protect the heat exchanger of the heat pump system from being polluted in a short time and reduce heat loss. transfer efficiency. During the heat exchange process of the heat pump heat exchanger, the evaporator absorbs the flue gas heat and provides it to the compressor working fluid inside the evaporator, and the working fluid in the condenser delivers heat to the water that needs to be heated. After pretreatment, the oil fume is drawn into the heat pump system by the fan, and then discharged after condensation and cooling. The cold air and the oil fume are mixed to further reduce the temperature of the oil fume in the entire box, so that the VOC substances are liquefied, trapped inside the box, and finally discharged from the box. Cone bucket discharge system, the temperature after condensation is up to the standard discharge. The hot water output is operated by circulating water inlet heating. The water outlet temperature of the water tank can be adjusted between 35-70°C, controlled by the temperature control probe. The hot water output is related to the air distribution volume, compressor, and working fluid selection. the
试验装置处理效果如表1所示: The treatment effect of the test device is shown in Table 1:
综上所述,本发明所述的一种饮食业油烟二级处理方法及装置,能够高效地去除油烟中的污染物质,不产生二次污染,运行稳定,并同时回收热能,产出热水供用户使用,具有极其重要的应用价值。 To sum up, the method and device for secondary treatment of cooking fumes in the catering industry described in the present invention can efficiently remove pollutants in the cooking fumes without causing secondary pollution, operate stably, recover heat energy at the same time, and produce hot water for supply It is used by users and has extremely important application value.
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105890003A (en) * | 2016-04-28 | 2016-08-24 | 湖南理工学院 | Non-cleaning smoke exhaust ventilator |
| CN112097301A (en) * | 2020-11-03 | 2020-12-18 | 江苏省泗洪中学 | A comprehensive range hood |
| CN112665215A (en) * | 2021-01-26 | 2021-04-16 | 常州大学 | Flue gas recovery type cold-heat exchange cold-storage and heat-storage system for cafeteria |
| CN116255696A (en) * | 2023-03-07 | 2023-06-13 | 南京一阳环保科技有限公司 | Common flue waste gas cooling and filtering device |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2090492U (en) * | 1991-03-05 | 1991-12-11 | 汤健中 | Wall soot exhauster |
| JPH07139807A (en) * | 1993-11-12 | 1995-06-02 | Kajima Corp | Kitchen waste heat recovery device |
| CN2859302Y (en) * | 2004-04-29 | 2007-01-17 | 陈胜华 | Cyclone separate smoke extractor |
| CN201611164U (en) * | 2009-12-31 | 2010-10-20 | 杭州真心热能电器有限公司 | Integrator of air-source water heater and range hood |
| CN102052761A (en) * | 2010-12-27 | 2011-05-11 | 天津市职业大学 | Heat pump system capable of washing kitchen exhaust smoke and taking kitchen exhaust smoke as heat source |
| CN102261688A (en) * | 2011-06-24 | 2011-11-30 | 孙道林 | Cyclone cooking hood |
| CN202993315U (en) * | 2012-09-27 | 2013-06-12 | 夏涛 | Kitchen heat energy recycling device |
-
2014
- 2014-11-21 CN CN201410670468.1A patent/CN104406210A/en active Pending
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2090492U (en) * | 1991-03-05 | 1991-12-11 | 汤健中 | Wall soot exhauster |
| JPH07139807A (en) * | 1993-11-12 | 1995-06-02 | Kajima Corp | Kitchen waste heat recovery device |
| CN2859302Y (en) * | 2004-04-29 | 2007-01-17 | 陈胜华 | Cyclone separate smoke extractor |
| CN201611164U (en) * | 2009-12-31 | 2010-10-20 | 杭州真心热能电器有限公司 | Integrator of air-source water heater and range hood |
| CN102052761A (en) * | 2010-12-27 | 2011-05-11 | 天津市职业大学 | Heat pump system capable of washing kitchen exhaust smoke and taking kitchen exhaust smoke as heat source |
| CN102261688A (en) * | 2011-06-24 | 2011-11-30 | 孙道林 | Cyclone cooking hood |
| CN202993315U (en) * | 2012-09-27 | 2013-06-12 | 夏涛 | Kitchen heat energy recycling device |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105890003A (en) * | 2016-04-28 | 2016-08-24 | 湖南理工学院 | Non-cleaning smoke exhaust ventilator |
| CN112097301A (en) * | 2020-11-03 | 2020-12-18 | 江苏省泗洪中学 | A comprehensive range hood |
| CN112665215A (en) * | 2021-01-26 | 2021-04-16 | 常州大学 | Flue gas recovery type cold-heat exchange cold-storage and heat-storage system for cafeteria |
| CN116255696A (en) * | 2023-03-07 | 2023-06-13 | 南京一阳环保科技有限公司 | Common flue waste gas cooling and filtering device |
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