CN207899175U - A kind of hot investment casting roasting kiln flue purification system - Google Patents
A kind of hot investment casting roasting kiln flue purification system Download PDFInfo
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- 238000005495 investment casting Methods 0.000 title claims abstract description 8
- 238000000746 purification Methods 0.000 title claims abstract description 8
- 239000000428 dust Substances 0.000 claims abstract description 46
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 36
- 239000000779 smoke Substances 0.000 claims abstract description 24
- 239000012717 electrostatic precipitator Substances 0.000 claims abstract description 18
- 238000006303 photolysis reaction Methods 0.000 claims abstract description 12
- 238000001816 cooling Methods 0.000 claims description 15
- 239000005457 ice water Substances 0.000 claims description 6
- 239000007789 gas Substances 0.000 abstract description 16
- 230000005684 electric field Effects 0.000 abstract description 10
- 230000015843 photosynthesis, light reaction Effects 0.000 abstract description 10
- 230000000694 effects Effects 0.000 abstract description 6
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 abstract description 5
- 239000003546 flue gas Substances 0.000 abstract description 5
- 230000005484 gravity Effects 0.000 abstract description 3
- 239000002245 particle Substances 0.000 abstract description 3
- 238000002485 combustion reaction Methods 0.000 description 7
- 238000007599 discharging Methods 0.000 description 6
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 3
- QGJOPFRUJISHPQ-UHFFFAOYSA-N Carbon disulfide Chemical compound S=C=S QGJOPFRUJISHPQ-UHFFFAOYSA-N 0.000 description 3
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 3
- 230000007613 environmental effect Effects 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 2
- QMMFVYPAHWMCMS-UHFFFAOYSA-N Dimethyl sulfide Chemical compound CSC QMMFVYPAHWMCMS-UHFFFAOYSA-N 0.000 description 2
- LSDPWZHWYPCBBB-UHFFFAOYSA-N Methanethiol Chemical compound SC LSDPWZHWYPCBBB-UHFFFAOYSA-N 0.000 description 2
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 2
- 238000003915 air pollution Methods 0.000 description 2
- 230000007547 defect Effects 0.000 description 2
- WQOXQRCZOLPYPM-UHFFFAOYSA-N dimethyl disulfide Chemical compound CSSC WQOXQRCZOLPYPM-UHFFFAOYSA-N 0.000 description 2
- 239000004744 fabric Substances 0.000 description 2
- 229910000037 hydrogen sulfide Inorganic materials 0.000 description 2
- 238000002347 injection Methods 0.000 description 2
- 239000007924 injection Substances 0.000 description 2
- 238000005507 spraying Methods 0.000 description 2
- GETQZCLCWQTVFV-UHFFFAOYSA-N trimethylamine Chemical compound CN(C)C GETQZCLCWQTVFV-UHFFFAOYSA-N 0.000 description 2
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 description 1
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 1
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 description 1
- 239000000809 air pollutant Substances 0.000 description 1
- 231100001243 air pollutant Toxicity 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 239000004753 textile Substances 0.000 description 1
- 239000012855 volatile organic compound Substances 0.000 description 1
- 239000002912 waste gas Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- 239000008096 xylene Substances 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
- Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
- Y02A50/2351—Atmospheric particulate matter [PM], e.g. carbon smoke microparticles, smog, aerosol particles, dust
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/25—Process efficiency
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- Treating Waste Gases (AREA)
- Electrostatic Separation (AREA)
Abstract
本实用新型公开了一种精密铸造焙烧炉窑烟道净化系统,包括炉窑,先将炉窑内的带蜡烟雾送入冷却塔中进行降温,然后用袋式除尘器既能过滤掉烟雾中的颗粒大、比重大的粉尘,又能过滤掉烟雾中较细小粉尘。顺接用水膜除尘器进一步提高除尘效果,当然水膜除尘器更重要的是对烟雾再次进行降温冷却,所以需要附加冰水机组,从而烟雾中水蒸气的比例就会大大减小为后续静电除尘器服务,如果水蒸气过多,静电除尘器就无法正常发挥效应了,所以冰水机组的增设非常有必要。接下来静电除尘器利用高压电场使烟气发生电离,气流中的粉尘荷电在电场作用下与气流分离。最后一步用UV光解空气净化器裂解恶臭气体。最终可以放心的向大气排放了。
The utility model discloses a flue purification system of a precision casting roasting kiln, which comprises a kiln. The dust with large particles and large specific gravity can filter out the finer dust in the smoke. Followed by the water film dust collector to further improve the dust removal effect. Of course, the water film dust collector is more important to cool down the smoke again, so it is necessary to add a chiller unit, so that the proportion of water vapor in the smoke will be greatly reduced for subsequent electrostatic dust removal If there is too much water vapor, the electrostatic precipitator will not be able to function normally, so it is very necessary to add chillers. Next, the electrostatic precipitator uses a high-voltage electric field to ionize the flue gas, and the charged dust in the airflow is separated from the airflow under the action of the electric field. The last step is to crack the malodorous gas with UV photolysis air purifier. Finally, it can be released to the atmosphere with confidence.
Description
技术领域technical field
本实用新型涉及环保设备技术领域,更具体地说是一种精密铸造焙烧炉窑烟道净化系统。The utility model relates to the technical field of environmental protection equipment, in particular to a flue purification system of a precision casting roasting furnace and kiln.
背景技术Background technique
排蜡窑在工业烧结制品应用中比较广泛,但是它的缺陷比较明显就是环境污染严重,主要来源于烟雾随意排放,由此国家相关部门出台了《工业炉窑大气污染物排放标准》(GB9078-1996)来限制企业无环保意识的这种行为。Wax discharge kiln is widely used in industrial sintered products, but its obvious defect is serious environmental pollution, which mainly comes from the random discharge of smoke. Therefore, the relevant national departments have issued the "Emission Standard of Air Pollutants for Industrial Furnaces" (GB9078- 1996) to limit the behavior of enterprises without environmental awareness.
但也有企业很用心,着力于解决排蜡窑烟雾排放的问题研究,其中湖南某企业的实用新型专利CN201510124951.4就公开了一种排蜡烟雾处理炉,该排蜡烟雾处理炉包括炉体、喷火组件及用于排出排蜡窑中废气的排蜡烟筒,所述排蜡烟筒上设有第一阀门,所述第一阀门将所述排蜡烟筒分隔形成与排蜡窑连接的第一排气段和将气体排出至排蜡窑外的第二排气段;所述炉体上设有第一燃烧腔室,所述第一燃烧腔室的进气口与所述排蜡烟筒的第一排气段连通,所述第一燃烧腔室的出气口与所述排蜡烟筒的第二排气段连通;所述炉体上设有供室外空气进入所述第一燃烧腔室中的第一气孔;所述喷火组件的喷火口设于所述第一燃烧腔室中。However, there are also companies that are very attentive and focus on solving the problem of smoke emission from the wax discharge kiln. Among them, the utility model patent CN201510124951.4 of an enterprise in Hunan discloses a wax discharge smoke treatment furnace. The wax discharge smoke treatment furnace includes a furnace body, The fire-spraying assembly and the wax-discharging chimney for discharging the waste gas in the wax-discharging kiln. The wax-discharging chimney is provided with a first valve, and the first valve separates the wax-discharging chimney to form a first valve connected to the wax-discharging kiln. Exhaust section and the second exhaust section that discharges the gas to the outside of the wax discharge kiln; the furnace body is provided with a first combustion chamber, and the air inlet of the first combustion chamber is connected to the gas outlet of the wax discharge chimney The first exhaust section communicates, and the air outlet of the first combustion chamber communicates with the second exhaust section of the wax exhaust chimney; the furnace body is provided with a vent for the outside air to enter the first combustion chamber The first air hole; the flame injection port of the flame injection assembly is located in the first combustion chamber.
该实用新型专利技术的设计主要是针对蜡的炉内循环燃烧,从而降低对空排蜡,降低大气污染的目的。其主要是解决炉窑内空气中蜡燃烧不充分的问题,解决对空排蜡的问题,但是其中排放的气体中还含有大量的颗粒粉尘以及有害气体等等其它废弃物,没有很好地得到解决。The design of this utility model patent technology is mainly aimed at the circular combustion of wax in the furnace, thereby reducing the wax discharge to the air and reducing air pollution. It mainly solves the problem of insufficient wax combustion in the air in the kiln, and solves the problem of wax discharge to the air, but the discharged gas also contains a large amount of particulate dust and harmful gases and other wastes, which have not been well obtained solve.
实用新型内容Utility model content
本实用新型的目的在于克服现有技术以上缺陷,提供一种排放气体无味感、无人体不适感、实现无害化安全排放、降低大气污染、实现节能环保理念的精密铸造焙烧炉窑烟道净化系统。The purpose of the utility model is to overcome the above defects of the prior art, and provide a precision casting roasting kiln flue purification that has no odor, no discomfort to the human body, realizes harmless and safe discharge, reduces air pollution, and realizes the concept of energy saving and environmental protection. system.
为了达到以上目的,本实用新型是通过以下技术方案实现的:一种精密铸造焙烧炉窑烟道净化系统,包括一炉窑,其特征在于,所述炉窑的排烟管连接有一冷却塔,所述冷却塔再连接有一袋式除尘器,所述袋式除尘器再连接有一水膜除尘器,所述水膜除尘器再连接有一静电除尘器,所述静电除尘器再连接有一UV光解空气净化器,所述UV光解空气净化器最后连接有一高空烟囱。In order to achieve the above purpose, the utility model is achieved through the following technical solutions: a precision casting roasting furnace flue purification system, including a furnace, characterized in that the smoke exhaust pipe of the furnace is connected to a cooling tower, The cooling tower is connected with a bag filter, and the bag filter is connected with a water film filter, and the water film filter is connected with an electrostatic precipitator, and the electrostatic filter is connected with a UV photolysis filter. An air purifier, the UV photolysis air purifier is finally connected with a high-altitude chimney.
作为优选,所述水膜除尘器旁侧还连接有一冰水机组。As a preference, a chiller unit is also connected to the side of the water film dust collector.
本实用新型先将炉窑内的带蜡烟雾送入冷却塔中进行降温,冷却塔是风机干式换热冷却方式。然后用袋式除尘器既能过滤掉烟雾中的颗粒大、比重大的粉尘,又能过滤掉烟雾中较细小粉尘。顺接用水膜除尘器进一步提高除尘效果,当然水膜除尘器更重要的是对烟雾再次进行降温冷却,一般控制在20℃左右为佳,所以需要附加冰水机组,从而烟雾中水蒸气的比例就会大大减小为后续静电除尘器服务,如果水蒸气过多,静电除尘器就无法正常发挥效应了,所以冰水机组的增设非常有必要。接下来静电除尘器利用高压电场使烟气发生电离,气流中的粉尘荷电在电场作用下与气流分离。最后一步用UV光解空气净化器裂解恶臭气体。最终可以放心的向大气排放了。The utility model sends the waxy smoke in the kiln to the cooling tower for cooling, and the cooling tower is a fan dry heat exchange cooling method. Then use the bag filter to filter out the large and specific dust in the smoke, and filter out the finer dust in the smoke. Followed by the water film dust collector to further improve the dust removal effect. Of course, the more important thing for the water film dust collector is to cool down the smoke again. Generally, it is better to control it at about 20°C, so it is necessary to add an ice water unit to increase the proportion of water vapor in the smoke. It will greatly reduce the service for the subsequent electrostatic precipitator. If there is too much water vapor, the electrostatic precipitator will not be able to function normally, so the addition of chilled water units is very necessary. Next, the electrostatic precipitator uses a high-voltage electric field to ionize the flue gas, and the charged dust in the airflow is separated from the airflow under the action of the electric field. The last step is to crack the malodorous gas with UV photolysis air purifier. Finally, it can be released to the atmosphere with confidence.
以下涉及到的组件进行名词解释:袋式除尘器是一种干式滤尘装置,它适用于捕集细小、干燥、非纤维性粉尘,滤袋采用纺织的滤布或非纺织的毡制成,利用纤维织物的过滤作用对含尘气体进行过滤,当含尘气体进入袋式除尘器后,颗粒大、比重大的粉尘,由于重力的作用沉降下来,落入灰斗,含有较细小粉尘的气体在通过滤料时,粉尘被阻留,使气体得到净化。The components involved are explained below: the bag filter is a dry dust filter device, which is suitable for collecting fine, dry, non-fibrous dust. The filter bag is made of textile filter cloth or non-woven felt. The dust-containing gas is filtered by the filter function of the fiber fabric. When the dust-containing gas enters the bag filter, the dust with large particles and specific gravity settles down due to the action of gravity and falls into the ash hopper, while the gas containing finer dust When passing through the filter material, the dust is blocked and the gas is purified.
水膜除尘器是含尘气体由筒体下部顺切向引入,旋转上升,尘粒受离心力作用而被分离,抛向筒体内壁,被筒体内壁流动的水膜层所吸附,随水流到底部锥体,经排尘口卸出。水膜层的形成是由布置在筒体的上部几个喷嘴、将水顺切向喷至器壁。这样,在筒体内壁始终覆盖一层旋转向下流动的很薄水膜,达到提高除尘效果的目的。The water film dust collector is that the dust-containing gas is introduced tangentially from the lower part of the cylinder, rotates up, and the dust particles are separated by centrifugal force, thrown to the inner wall of the cylinder, absorbed by the water film layer flowing on the inner wall of the cylinder, and flow to the bottom with the water The inner cone is discharged through the dust outlet. The water film layer is formed by several nozzles arranged on the upper part of the cylinder, spraying water tangentially to the wall of the device. In this way, the inner wall of the cylinder is always covered with a layer of very thin water film that rotates and flows downwards, so as to achieve the purpose of improving the dust removal effect.
静电除尘器是利用高压电场使烟气发生电离,气流中的粉尘荷电在电场作用下与气流分离。The electrostatic precipitator uses a high-voltage electric field to ionize the flue gas, and the dust charge in the airflow is separated from the airflow under the action of the electric field.
UV光解空气净化器是利用特制的高能高臭氧UV紫外线光束照射恶臭气体,裂解恶臭气体的装置。裂解恶臭气体如:氨、三甲胺、硫化氢、甲硫氢、甲硫醇、甲硫醚、二甲二硫、二硫化碳和苯乙烯,硫化物H2S、VOC类,苯、甲苯、二甲苯的分子键,使呈游离状态的污染物分子与臭氧氧化结合成小分子无害或低害的化合物,如CO2、H2O等。The UV photolysis air purifier is a device that uses a special high-energy high-ozone UV ultraviolet light beam to irradiate the malodorous gas and crack the malodorous gas. Cracking malodorous gases such as: ammonia, trimethylamine, hydrogen sulfide, methyl sulfide, methyl mercaptan, methyl sulfide, dimethyl disulfide, carbon disulfide and styrene, sulfide H2S, VOC, benzene, toluene, xylene molecules Bond, so that the pollutant molecules in the free state are oxidized and combined with ozone to form small molecular harmless or low-harm compounds, such as CO2, H2O, etc.
冰水机组四个主要组成部分:压缩机、蒸发器、冷凝器和膨胀阀,从而实现了机组制冷制热效果。The ice water unit has four main components: compressor, evaporator, condenser and expansion valve, thus realizing the cooling and heating effect of the unit.
有益效果:本实用新型先将炉窑内的带蜡烟雾送入冷却塔中进行降温。然后用袋式除尘器既能过滤掉烟雾中的颗粒大、比重大的粉尘,又能过滤掉烟雾中较细小粉尘。顺接用水膜除尘器进一步提高除尘效果,当然水膜除尘器更重要的是对烟雾再次进行降温冷却,一般控制在20℃左右为佳,所以需要附加冰水机组,从而烟雾中水蒸气的比例就会大大减小为后续静电除尘器服务,如果水蒸气过多,静电除尘器就无法正常发挥效应了,所以冰水机组的增设非常有必要。接下来静电除尘器利用高压电场使烟气发生电离,气流中的粉尘荷电在电场作用下与气流分离。最后一步用UV光解空气净化器裂解恶臭气体。最终可以放心的向大气排放了。Beneficial effects: the utility model first sends the waxy smoke in the kiln to the cooling tower for cooling. Then use the bag filter to filter out the large and specific dust in the smoke, and filter out the finer dust in the smoke. Followed by the water film dust collector to further improve the dust removal effect. Of course, the more important thing for the water film dust collector is to cool down the smoke again. Generally, it is better to control it at about 20°C, so it is necessary to add an ice water unit to increase the proportion of water vapor in the smoke. It will greatly reduce the service for the subsequent electrostatic precipitator. If there is too much water vapor, the electrostatic precipitator will not be able to function normally, so the addition of chilled water units is very necessary. Next, the electrostatic precipitator uses a high-voltage electric field to ionize the flue gas, and the charged dust in the airflow is separated from the airflow under the action of the electric field. The last step is to crack the malodorous gas with UV photolysis air purifier. Finally, it can be released to the atmosphere with confidence.
附图说明Description of drawings
图1为本实用新型的结构示意图。Fig. 1 is the structural representation of the utility model.
图中:1-炉窑,2-排烟管,3-冷却塔,4-袋式除尘器,5-水膜除尘器,6-冰水机组,7-静电除尘器,8-UV光解空气净化器,9-高空烟囱。In the figure: 1-Kiln, 2-Exhaust pipe, 3-Cooling tower, 4-Bag dust collector, 5-Water film dust collector, 6-Ice water unit, 7-Electrostatic precipitator, 8-UV photolysis Air cleaner, 9-high-altitude chimney.
具体实施方式Detailed ways
为了使本实用新型的技术手段、创作特征与达成目的易于明白理解,以下结合具体实施例进一步阐述本实用新型。In order to make the technical means, creative features and objectives of the present invention easy to understand, the present invention will be further described below in conjunction with specific embodiments.
实施例:如图1所示,一种精密铸造焙烧炉窑烟道净化系统,包括一炉窑1,炉窑1的排烟管2连接有一冷却塔3,冷却塔3再连接有一袋式除尘器4,袋式除尘器4再连接有一水膜除尘器5,水膜除尘器5旁侧还连接有一冰水机组6。水膜除尘器5再连接有一静电除尘器7,静电除尘器7再连接有一UV光解空气净化器8,UV光解空气净化器8最后连接有一高空烟囱9。Embodiment: As shown in Fig. 1, a kind of flue purification system of precision casting roasting furnace kiln comprises a furnace kiln 1, and the exhaust pipe 2 of furnace kiln 1 is connected with a cooling tower 3, and cooling tower 3 is connected with a bag type dedusting Device 4, bag filter 4 is connected with a water film dust collector 5 again, and water film dust collector 5 side is also connected with a chilled water unit 6. The water film dust collector 5 is connected with an electrostatic precipitator 7, and the electrostatic precipitator 7 is connected with a UV photolysis air cleaner 8, and the UV photolysis air cleaner 8 is finally connected with a high-altitude chimney 9.
使用:本实用新型先将炉窑内的带蜡烟雾送入冷却塔中进行降温。然后用袋式除尘器既能过滤掉烟雾中的颗粒大、比重大的粉尘,又能过滤掉烟雾中较细小粉尘。顺接用水膜除尘器进一步提高除尘效果,当然水膜除尘器更重要的是对烟雾再次进行降温冷却,一般控制在20℃左右为佳,所以需要附加冰水机组,从而烟雾中水蒸气的比例就会大大减小为后续静电除尘器服务,如果水蒸气过多,静电除尘器就无法正常发挥效应了,所以冰水机组的增设非常有必要。接下来静电除尘器利用高压电场使烟气发生电离,气流中的粉尘荷电在电场作用下与气流分离。最后一步用UV光解空气净化器裂解恶臭气体。最终可以放心的向大气排放了。Use: the utility model sends the waxy smoke in the kiln to the cooling tower to cool down. Then use the bag filter to filter out the large and specific dust in the smoke, and filter out the finer dust in the smoke. Followed by the water film dust collector to further improve the dust removal effect. Of course, the more important thing for the water film dust collector is to cool down the smoke again. Generally, it is better to control it at about 20°C, so it is necessary to add an ice water unit to increase the proportion of water vapor in the smoke. It will greatly reduce the service for the subsequent electrostatic precipitator. If there is too much water vapor, the electrostatic precipitator will not be able to function normally, so the addition of chilled water units is very necessary. Next, the electrostatic precipitator uses a high-voltage electric field to ionize the flue gas, and the charged dust in the airflow is separated from the airflow under the action of the electric field. The last step is to crack the malodorous gas with UV photolysis air purifier. Finally, it can be released to the atmosphere with confidence.
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107737507A (en) * | 2017-12-05 | 2018-02-27 | 诸暨市裘健机械厂 | A kind of hot investment casting roasting kiln flue cleaning system |
| CN110986606A (en) * | 2019-12-10 | 2020-04-10 | 山东建筑大学 | A fire test furnace cooling and purification system and method |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107737507A (en) * | 2017-12-05 | 2018-02-27 | 诸暨市裘健机械厂 | A kind of hot investment casting roasting kiln flue cleaning system |
| CN110986606A (en) * | 2019-12-10 | 2020-04-10 | 山东建筑大学 | A fire test furnace cooling and purification system and method |
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