CN203876114U - Tape casting machine with functions of heat energy recycling and waste gas treatment - Google Patents
Tape casting machine with functions of heat energy recycling and waste gas treatment Download PDFInfo
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- CN203876114U CN203876114U CN201320694702.5U CN201320694702U CN203876114U CN 203876114 U CN203876114 U CN 203876114U CN 201320694702 U CN201320694702 U CN 201320694702U CN 203876114 U CN203876114 U CN 203876114U
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- 239000002912 waste gas Substances 0.000 title claims abstract description 16
- 238000010345 tape casting Methods 0.000 title claims 4
- 238000004064 recycling Methods 0.000 title 1
- 239000007789 gas Substances 0.000 claims abstract description 27
- 238000005266 casting Methods 0.000 claims abstract description 17
- 239000007788 liquid Substances 0.000 claims abstract description 17
- 239000012528 membrane Substances 0.000 claims abstract description 16
- 238000003860 storage Methods 0.000 claims abstract description 12
- 238000011084 recovery Methods 0.000 claims abstract description 6
- 239000005416 organic matter Substances 0.000 claims description 7
- 239000000126 substance Substances 0.000 claims description 3
- 239000000919 ceramic Substances 0.000 abstract description 17
- 238000001035 drying Methods 0.000 abstract description 12
- 239000002002 slurry Substances 0.000 abstract description 9
- 238000004519 manufacturing process Methods 0.000 abstract description 6
- 239000012855 volatile organic compound Substances 0.000 abstract description 6
- 238000009833 condensation Methods 0.000 abstract description 5
- 230000005494 condensation Effects 0.000 abstract description 5
- 230000007613 environmental effect Effects 0.000 abstract description 2
- 150000002894 organic compounds Chemical class 0.000 abstract description 2
- 239000003990 capacitor Substances 0.000 abstract 1
- 238000001514 detection method Methods 0.000 abstract 1
- 239000000446 fuel Substances 0.000 abstract 1
- 238000004806 packaging method and process Methods 0.000 abstract 1
- 239000000758 substrate Substances 0.000 abstract 1
- 238000000034 method Methods 0.000 description 4
- 239000002699 waste material Substances 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 2
- 239000012466 permeate Substances 0.000 description 2
- 239000011230 binding agent Substances 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 239000002270 dispersing agent Substances 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 238000004377 microelectronic Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000005693 optoelectronics Effects 0.000 description 1
- 239000011368 organic material Substances 0.000 description 1
- 239000010815 organic waste Substances 0.000 description 1
- 239000004014 plasticizer Substances 0.000 description 1
- 231100000614 poison Toxicity 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000007650 screen-printing Methods 0.000 description 1
- 238000005245 sintering Methods 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 239000003440 toxic substance Substances 0.000 description 1
- 239000010891 toxic waste 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/10—Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
本实用新型涉及电子陶瓷生产设备,尤其涉及一种具有热能回收及废气处理功能的流延机,它主要由主动滚轮,从动滚轮,流延头,输送带,烘箱,热废气处理系统等组成。本实用新型将流延机干燥陶瓷浆料中产生的热废气通过换热器用于加热新鲜空气,并通过风机将新鲜热风通过风机鼓入烘箱;而废气中的挥发性有机物(VOCs)通过冷凝器初步冷凝后,经过膜组件,将废气中的挥发性有机物分离下来后,无害的透余气直接排空,分离下来的有机物经过进一步冷凝后放置在储液槽中。本实用新型适用于陶瓷基板,叠片式电容与电感,片式元器件,压电器件,红外线探测器件,燃料电池及集成电路的多层封装领域,与现有技术相比,具有节约能源,环境友好的优点。
The utility model relates to electronic ceramic production equipment, in particular to a casting machine with the functions of heat energy recovery and waste gas treatment, which is mainly composed of driving rollers, driven rollers, casting heads, conveyor belts, ovens, hot waste gas treatment systems, etc. . The utility model uses the hot waste gas produced in the drying ceramic slurry of the casting machine to heat the fresh air through the heat exchanger, and blows the fresh hot air into the oven through the fan; and the volatile organic compounds (VOCs) in the waste gas pass through the condenser After the initial condensation, the volatile organic compounds in the exhaust gas are separated through the membrane module, and the harmless residual air is directly emptied, and the separated organic compounds are further condensed and placed in the liquid storage tank. The utility model is suitable for multi-layer packaging fields of ceramic substrates, laminated capacitors and inductors, chip components, piezoelectric devices, infrared detection devices, fuel cells and integrated circuits. Compared with the prior art, the utility model has the advantages of saving energy, The advantages of environmental friendliness.
Description
技术领域 technical field
本实用新型涉及电子陶瓷生产设备,尤其涉及一种具有热能回收及废气处理功能的流延机。 The utility model relates to electronic ceramic production equipment, in particular to a casting machine with functions of heat energy recovery and waste gas treatment. the
背景技术 Background technique
电子陶瓷被广泛用于微电子技术、光电子与电力电子技术等领域,电子陶瓷浆料主要有无机陶瓷粉末与有机材料如粘结剂、增塑剂、分散剂和溶剂等组成,混合均匀后的电子陶瓷浆料需要经过流延、丝印、烧结等一系列工艺制成所需电子陶瓷,而流延工艺主要通过干燥手段制成陶瓷生坯。流延工艺主要的生产设备为流延机,现有的流延机干燥过程中产生的热废气直接排往大气,这样一方面浪费热能,另一方面陶瓷浆料干燥过程中产生大量的挥发性有机物(VOCs)多为剧毒物质,未经过任何处理直接排空严重污染环境。发明专利CN102338557A虽然考虑到利用热交换器回收热能,但是其干燥稳定后,烘箱内部既无新风进入也无热风排出,这样整个烘箱内部虽然温度达到要求,但是干燥湿度没有考虑,存在干燥不理想的可能;已公布专利CN201559281U虽然也考虑利用热交换器回收热能,但是其被烘箱内部排出的热风直接重新排入烘箱内部,没有考虑陶瓷浆料干燥过程中的火用值对干燥的影响,这样存在干燥效率低的弊端。 Electronic ceramics are widely used in the fields of microelectronics technology, optoelectronics and power electronics technology. Electronic ceramics slurry mainly consists of inorganic ceramic powder and organic materials such as binders, plasticizers, dispersants and solvents. The electronic ceramic slurry needs to go through a series of processes such as casting, screen printing, and sintering to make the required electronic ceramics, and the casting process mainly makes ceramic green bodies by drying. The main production equipment of the casting process is the casting machine. The hot waste gas generated during the drying process of the existing casting machine is directly discharged into the atmosphere, which wastes heat energy on the one hand, and produces a large amount of volatile gas during the drying process of the ceramic slurry on the other hand. Organic compounds (VOCs) are mostly highly toxic substances, which are directly emptied without any treatment and seriously pollute the environment. Although the invention patent CN102338557A considers the use of heat exchangers to recover heat energy, after the drying is stable, neither fresh air enters nor hot air is discharged inside the oven. In this way, although the temperature inside the oven meets the requirements, the drying humidity is not considered, and there is a problem of unsatisfactory drying. Possibly; although the published patent CN201559281U also considers the use of heat exchangers to recover heat energy, it is directly re-discharged into the oven by the hot air discharged from the inside of the oven, without considering the influence of the exergy value on the drying process of the ceramic slurry. The disadvantage of low drying efficiency. the
实用新型内容 Utility model content
本实用新型的目的在于提供本实用新型涉及电子陶瓷生产设备,尤其涉及一种新型的具有热能回收及废气处理功能的流延机,解决现有设备浪费能源且污染环境的缺陷。 The purpose of the utility model is to provide the utility model related to electronic ceramics production equipment, especially a new casting machine with functions of heat energy recovery and waste gas treatment, so as to solve the defects of energy waste and environmental pollution of existing equipment. the
为了实现上述的目的,采用如下的技术方案:一种具有热能回收及废气处理功能的流延机,由主动滚轮,从动滚轮,流延头,输送带,烘箱,热废气处理系统等组成,主从动滚轮带动输送带运动,输送带载送陶瓷浆料进入烘箱内被干燥,被干燥后的陶瓷生坯被载送出烘箱;干燥过程中产生的热废气经由热废气处理系统处理。所述的热废气系统包括过滤器、风机、换热器、冷凝器、膜组件、储液槽等部件;所述过滤器一端与大气相连,另一端与换热器入口相连;所述换热器有两个通道,其中第一个通道一端与第一号抽风机出风口相连,另一端与第一号冷凝器进料口相连,第二个通道一端与过滤器出口相连,另一端与第二号抽风机入口相连;烘箱具有进风口和出风口,第二风机出口与烘箱进风口相连,第一抽风机 入口与烘箱出风口相连,所述热废气处理系统将加热的新鲜空气从烘箱两端鼓入,烘箱干燥的废气从底部被抽入热废气处理系统中。 In order to achieve the above purpose, the following technical solution is adopted: a casting machine with functions of heat energy recovery and exhaust gas treatment, which is composed of driving rollers, driven rollers, casting heads, conveyor belts, ovens, thermal exhaust gas treatment systems, etc. The driving and driven rollers drive the conveyor belt to move, and the conveyor belt carries the ceramic slurry into the oven to be dried, and the dried ceramic green body is carried out of the oven; the hot exhaust gas generated during the drying process is treated by the thermal exhaust gas treatment system. The hot exhaust gas system includes filters, fans, heat exchangers, condensers, membrane modules, liquid storage tanks and other components; one end of the filter is connected to the atmosphere, and the other end is connected to the inlet of the heat exchanger; the heat exchange The condenser has two channels, one end of the first channel is connected to the outlet of the No. 1 exhaust fan, the other end is connected to the inlet of the No. The inlet of the No. 2 exhaust fan is connected; the oven has an air inlet and an air outlet, the outlet of the second fan is connected with the air inlet of the oven, the inlet of the first exhaust fan is connected with the outlet of the oven, and the hot exhaust gas treatment system transfers heated fresh air from both sides of the oven. The end is blown in, and the oven-dried exhaust gas is drawn into the hot exhaust gas treatment system from the bottom. the
所述热废气处理系统包含可以分离有机物的冷凝器,有机物冷凝成液态后置于储液槽中。 The hot exhaust gas treatment system includes a condenser capable of separating organic matter, and the organic matter is condensed into a liquid state and placed in a liquid storage tank. the
所述废气处理系统还包含膜组件,所述膜组件包含一层或一层以上的透过膜,可透过有机物。 The exhaust gas treatment system further includes a membrane module, and the membrane module includes one or more layers of permeable membranes, which can permeate organic matter. the
进一步地,所述热废气处理系统还包括第二冷凝器,所述第二冷凝器的进气口与所述膜组件出气口相连。 Further, the hot exhaust gas treatment system further includes a second condenser, the inlet of the second condenser is connected to the outlet of the membrane module. the
进一步地,本方案的优选连接方式为:所述过滤器一端与大气相连,另一端与换热器入口相连;所述换热器有两个通道,其中第一个通道一端与第一抽风机出风口相连,另一端与第一号冷凝器进料口相连,第二个通道一端与过滤器出口相连,另一端与第二号抽风机入风口相连;烘箱具有进风口和出风口,第二号抽风机出口与烘箱进风口相连,第一抽风机入口与烘箱出风口相连;所述第一号冷凝器出口与膜组件入口相连;所述膜组件出口与第三号抽风机入口相连;所述第三号抽风机出口与第二号冷凝器入口相连,所述第二号冷凝器包含两个出口,其中第一出口与储液槽相连,第二出口直接连接大气。 Further, the preferred connection mode of this solution is: one end of the filter is connected to the atmosphere, and the other end is connected to the inlet of the heat exchanger; the heat exchanger has two channels, and one end of the first channel is connected to the first exhaust fan. The air outlet is connected, and the other end is connected with the inlet of the No. 1 condenser. One end of the second channel is connected with the filter outlet, and the other end is connected with the air inlet of the No. 2 exhaust fan; the oven has an air inlet and an air outlet. The outlet of the No. exhaust fan is connected with the air inlet of the oven, the inlet of the first exhaust fan is connected with the outlet of the oven; the outlet of the No. 1 condenser is connected with the inlet of the membrane module; the outlet of the membrane module is connected with the inlet of the No. 3 exhaust fan; The outlet of the No. 3 exhaust fan is connected to the inlet of the No. 2 condenser, and the No. 2 condenser includes two outlets, wherein the first outlet is connected to the liquid storage tank, and the second outlet is directly connected to the atmosphere. the
上述方案中,所述过滤器选用粗效过滤器加中效过滤器组合的形式,有必要时可选用高效或精密级过滤器。 In the above solution, the filter is a combination of a coarse-effect filter and a medium-effect filter, and if necessary, a high-efficiency or precision filter can be selected. the
上述方案中,所述烘箱内部具有热源装置,可加热空气,热源装置采用PID温控调节方法,所述热废气处理系统位于烘箱侧面。 In the above scheme, there is a heat source device inside the oven, which can heat the air. The heat source device adopts a PID temperature control adjustment method, and the hot waste gas treatment system is located on the side of the oven. the
上述方案中,所述换热器优选换热系数高的换热器,本实用新型优选板式换热器。 In the above solution, the heat exchanger is preferably a heat exchanger with a high heat transfer coefficient, and the plate heat exchanger is preferred in the present invention. the
上述方案中,所述膜组件具有不同的透过膜,可透过生产中遇到的各类有机物;透过的有机物均需通过冷凝器冷凝后放置于储液槽中,透余气直接排空。 In the above solution, the membrane module has different permeable membranes, which can permeate various organic substances encountered in production; the permeated organic substances need to be condensed by the condenser and placed in the liquid storage tank, and the residual air can be directly discharged null. the
上述方案中,所述储液槽中的有机物将透过焚烧方法处理。 In the above scheme, the organic matter in the liquid storage tank will be treated by incineration. the
与现有技术相比,本实用新型更环保节能,通过换热器将热废气中的热用于加热新鲜空气,该热新鲜空气被鼓入烘箱中,由于烘箱由于具有PID温控调节系统,因此鼓入烘箱中的热能可以减少烘箱功率消耗从而节省电能;热废气中含有的大量挥发性有机物通过冷凝→膜透过→冷凝这一步骤后,透余的无害气体直接排往大气,而剩余的高体积含量的液态挥发性有机物被冷凝后储存起来,这些有毒废物可以通过燃烧等的办法处理,从而保证电子陶瓷生产过程的环保要求。 Compared with the prior art, the utility model is more environmentally friendly and energy-saving. The heat in the hot exhaust gas is used to heat the fresh air through the heat exchanger, and the hot fresh air is blown into the oven. Since the oven has a PID temperature control and adjustment system, Therefore, the heat energy blown into the oven can reduce the power consumption of the oven and save electric energy; after a large amount of volatile organic compounds contained in the hot exhaust gas pass through the steps of condensation→membrane permeation→condensation, the remaining harmless gas is directly discharged to the atmosphere, while The remaining liquid volatile organic compounds with high volume content are condensed and stored, and these toxic wastes can be disposed of by burning or other methods, so as to ensure the environmental protection requirements of the electronic ceramics production process. the
附图说明 Description of drawings
图1、2为本实用新型的结构示意图。 Fig. 1, 2 are structural representations of the utility model. the
具体实施方式 Detailed ways
下面结合附图对本实用新型作进一步的描述。 Below in conjunction with accompanying drawing, the utility model is further described. the
本实用新型原理如图1、图2所示。主动滚轮3带动从动滚轮1运动,输送带2安装主从动滚轮上,陶瓷浆料通过流延头7均匀涂布于输送带2上,输送带载送浆料进入烘箱5中被干燥,干燥完成后,成型生坯被载送出烘箱,干燥浆料过程中产生的热废气从通道6通过风机17被鼓出,被鼓出的热废气通入换热器16中,换热器16将通过过滤器15的新鲜空气加热,被加热的新鲜空气通过风机9从烘箱两端被鼓入烘箱中。 The utility model principle is as shown in Figure 1 and Figure 2. The driving roller 3 drives the driven roller 1 to move, the conveyor belt 2 is installed on the driving roller, the ceramic slurry is evenly coated on the conveyor belt 2 through the casting head 7, and the conveyor belt carries the slurry into the oven 5 to be dried. After the drying is completed, the formed green body is carried out of the oven, and the hot waste gas generated during the drying of the slurry is blown out from the channel 6 through the fan 17, and the blown out hot waste gas is passed into the heat exchanger 16, and the heat exchanger 16 will The fresh air passing through the filter 15 is heated, and the heated fresh air is blown into the oven from both ends of the oven by the fan 9 . the
图2为热废气处理系统,烘箱8内部有热源可以加热空气,风机9不断的往烘箱8内部鼓入新鲜空气,烘箱内部工作后产生的热废气由第一风机17抽出,第一风机17抽出的热废气被鼓入换热器16中,换热器16利用热废气将通过过滤器15的新鲜空气加热,被加热的新鲜热空气被第二风机9鼓入烘箱8,此为热回收过程;通过换热器的废气被通入第一冷凝器10中实现初步冷凝,初步冷凝后的废气通过膜组件11,透余气直接排空,剩余的高含量有机废气被第三风机14抽出第二通过冷凝器13后,进一步冷凝成液态后放置在储液槽12中,透余气继续排空,放置于储液槽中的废液留待进一步无害化处理。 Fig. 2 is a hot exhaust gas treatment system. There is a heat source inside the oven 8 to heat the air. The fan 9 blows fresh air into the oven 8 continuously. The hot exhaust gas generated after the oven works is drawn out by the first fan 17, The hot exhaust gas is blown into the heat exchanger 16, and the heat exchanger 16 uses the hot exhaust gas to heat the fresh air passing through the filter 15, and the heated fresh hot air is blown into the oven 8 by the second fan 9, which is a heat recovery process The exhaust gas passing through the heat exchanger is passed into the first condenser 10 to realize preliminary condensation, the exhaust gas after preliminary condensation passes through the membrane module 11, and the residual air is directly emptied, and the remaining high-content organic waste gas is drawn out by the third fan 14. 2. After passing through the condenser 13, it is further condensed into a liquid state and placed in the liquid storage tank 12, and the residual air is continuously emptied, and the waste liquid placed in the liquid storage tank is left for further harmless treatment. the
以上所述仅是本实用新型的优选实例。应当指出对于本领域的普通技术员来说,在本实用新型所提供的技术启示下,还可以做出其它等同变型或改进,也应当视为本实用新型的保护范围。 The above are only preferred examples of the present utility model. It should be pointed out that for those skilled in the art, under the technical inspiration provided by the utility model, other equivalent modifications or improvements can also be made, which should also be regarded as the protection scope of the utility model. the
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
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CN109263076A (en) * | 2018-11-07 | 2019-01-25 | 河南龙都天仁生物材料有限公司 | Lamination equipment |
CN113194758A (en) * | 2018-12-18 | 2021-07-30 | 菲利普莫里斯生产公司 | Method for producing sheets of material containing alkaloids |
CN114871078A (en) * | 2022-05-18 | 2022-08-09 | 三一技术装备有限公司 | Fresh air system of oven |
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2013
- 2013-11-06 CN CN201320694702.5U patent/CN203876114U/en not_active Expired - Fee Related
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109263076A (en) * | 2018-11-07 | 2019-01-25 | 河南龙都天仁生物材料有限公司 | Lamination equipment |
CN113194758A (en) * | 2018-12-18 | 2021-07-30 | 菲利普莫里斯生产公司 | Method for producing sheets of material containing alkaloids |
CN113194758B (en) * | 2018-12-18 | 2023-02-17 | 菲利普莫里斯生产公司 | Method for producing sheets of material containing alkaloids |
CN114871078A (en) * | 2022-05-18 | 2022-08-09 | 三一技术装备有限公司 | Fresh air system of oven |
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