CN101697295A - Method and equipment for utilizing catalytic heat energy of microwire enameling machine - Google Patents
Method and equipment for utilizing catalytic heat energy of microwire enameling machine Download PDFInfo
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- 230000003197 catalytic effect Effects 0.000 title claims abstract description 68
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- 238000007084 catalytic combustion reaction Methods 0.000 claims abstract description 20
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Abstract
Description
技术领域 technical field
本发明涉及漆包线覆涂漆膜烘焙干燥的方法和设备,特别是利用催化燃烧后的热能替代电能加热的漆包机工艺,尤其涉及微细线漆包机利用催化燃烧热能的工艺设备。The invention relates to a method and equipment for baking and drying an enameled wire coated paint film, in particular to an enamelling machine process using catalytic combustion heat energy instead of electric energy for heating, especially to a process equipment for a fine wire enamelling machine using catalytic combustion heat energy.
背景技术 Background technique
现有技术的漆包线生产行业中,为了降低成本,只能在节能方面挖掘潜力。In the enameled wire production industry of the prior art, in order to reduce costs, the potential can only be tapped in terms of energy saving.
一些漆包线制造厂家研究开发的节能型微线漆包线机烘炉,其废气回收利用装置中的催化燃烧室设置在炉膛固化区一端,漆包线溶剂被蒸发的气体经催化燃烧室燃烧,产生热气流,新鲜空气经热气流预热后顺流打入炉膛,节能效果不明显。Some enameled wire manufacturers research and develop energy-saving micro-wire enameled wire machine ovens. The catalytic combustion chamber in the exhaust gas recovery and utilization device is set at one end of the furnace curing area. After the air is preheated by the hot air flow, it flows into the furnace along the flow, so the energy saving effect is not obvious.
近来,众厂家陆续对现有设备进行技术改造,并申请了若干专利,例如:已经有02290021.7号中国实用新型专利,所公开的一种名为“节能型微线漆包机烘炉”的技术方案,该实用新型解决方案:一种节能型微线漆包机烘炉,包含炉膛、废气回收利用装置,其中,废气回收利用装置的入口设置在炉膛的蒸发区一端,出口通过循环风机、分风管与炉膛的固化区一端相连接。Recently, many manufacturers have successively carried out technical transformation on existing equipment and applied for several patents, for example: there is already a Chinese utility model patent No. 02290021.7, which discloses a technical solution called "energy-saving micro-wire enamelling machine oven" , the utility model solution: an energy-saving micro-wire enamelled machine oven, including a furnace and a waste gas recycling device, wherein the inlet of the waste gas recycling device is set at one end of the evaporation area of the furnace, and the outlet passes through a circulating fan and a distribution pipe It is connected to one end of the curing area of the furnace.
该方案虽然将废气回收产生的热气流逆向打入炉膛内腔,但单一入口距离炉膛的蒸发区路途遥远,在炉膛的蒸发区仍然需要电热管加热,因此,节能效果没有达到理想值。Although this solution injects the hot air flow generated by waste gas recovery into the inner cavity of the furnace in reverse, the single inlet is far away from the evaporation area of the furnace, and electric heating tubes are still needed for heating in the evaporation area of the furnace. Therefore, the energy saving effect has not reached the ideal value.
况且,该方案不适应加工微细线。Moreover, this scheme is not suitable for processing fine wires.
再如200910105133.4号中国发明专利申请,所公开的一种名为“一种漆包机合理分配催化燃烧热能的方法和设备”的技术方案,该方案虽然充分利用了催化燃烧热能,但其方案适只用于线径较粗的漆包线,在彼应用有比较理想的节能效果,但该方案因其微粒污染的问题并不适于微细线。Another example is the Chinese invention patent application No. 200910105133.4, which discloses a technical solution called "a method and equipment for rationally distributing catalytic combustion heat energy in an enameling machine". It is used for enameled wires with thicker wire diameters, which has an ideal energy-saving effect in that application, but this solution is not suitable for fine wires due to the problem of particle pollution.
对于微细线,微粒污染的问题已经是主要矛盾,必须加以根治。For fine wires, the problem of particle pollution is already the main contradiction and must be eradicated.
现有技术中,也有在微细线的出线口制作一个很小的热辐射板的技术,但其方案节能效果差的太远。In the prior art, there is also a technology of making a very small heat radiation plate at the outlet of the micro wire, but the energy saving effect of the solution is too poor.
发明内容 Contents of the invention
为了避开现有技术中存在的缺陷和不足之处,本发明提出一种微细线漆包机利用催化燃烧热能的方法和设备。In order to avoid the defects and deficiencies in the prior art, the present invention proposes a method and equipment for utilizing catalytic combustion heat energy in a fine wire enamelling machine.
本发明为了保证漆包线质量,不将有机废气燃烧后的循环热风引入炉体内,而是用循环热风加热很大面积的热辐射板,用洁净的辐射热来烘焙微细线。In order to ensure the quality of the enameled wire, the present invention does not introduce the circulating hot air after the organic waste gas is burned into the furnace body, but uses the circulating hot air to heat a large-area heat radiation plate, and uses clean radiant heat to bake the fine wire.
本发明为了降低电能消耗,在并排加工多根漆包线的前提下,在用电热管预工作一个多小时后,催化燃烧热能已经达到满足设备本身使用,就可以将主炉体的电热管电源断电。In order to reduce the consumption of electric energy, the present invention processes multiple enameled wires side by side, and after more than one hour of pre-work with the electric heating tube, the catalytic combustion heat energy has reached the requirement of the equipment itself, and the power supply of the electric heating tube of the main furnace body can be cut off .
为了达到上述目的,本发明通过采用以下技术方案来实现:In order to achieve the above object, the present invention realizes by adopting the following technical solutions:
实施微细线漆包机利用催化热能的方法,所述方法基于安装了主炉加热管的主炉体、循环风机、热交换器以及一次催化室的漆包机;所述主炉加热管用于预热工序;Implement the method of utilizing catalytic heat energy by the micro-wire enamelling machine, the method is based on the main furnace body, the circulation fan, the heat exchanger and the enamelling machine of the primary catalytic chamber installed with the main furnace heating pipe; the main furnace heating pipe is used for the preheating process ;
所述方法包括如下步骤:The method comprises the steps of:
A.首先在前炉空间和后炉空间的交界处设置有机废气入口,所述有机废气入口位于主炉体中部偏于前炉空间的位置,所述有机废气入口吸收由微细线上逸出的有机废气;A. First, an organic waste gas inlet is provided at the junction of the forehearth space and the back furnace space. The organic waste gas inlet is located in the middle of the main furnace body and is biased towards the forehearth space. The organic waste gas inlet absorbs the escaped gas from the fine line organic waste gas;
B.在前炉空间和后炉空间的上方设置前热辐射板和后热辐射板,所述前热辐射板和后热辐射板的长度不小于主炉空间长度的68%;B. Install a front heat radiation plate and a rear heat radiation plate above the front furnace space and the rear furnace space, and the length of the front heat radiation plate and the rear heat radiation plate is not less than 68% of the length of the main furnace space;
C.在有机废气入口上方设置一次催化室,在一次催化室的进口前方设置一次催化加热管,在一次催化室的出口处设置循环风机;C. Set a primary catalytic chamber above the inlet of the organic waste gas, set a primary catalytic heating pipe in front of the inlet of the primary catalytic chamber, and set a circulating fan at the outlet of the primary catalytic chamber;
D.有机废气在一次催化室催化燃烧形成循环热风;D. Organic waste gas is catalytically burned in the primary catalytic chamber to form circulating hot air;
E.接下来循环风机将催化燃烧后的循环热风送入循环热风道;E. Next, the circulating fan sends the circulating hot air after catalytic combustion into the circulating hot air channel;
F.接下来,循环热风进入以后热辐射板为底板的后热箱,然后循环热风通过连通管进入以前热辐射板为底板的前热箱;F. Next, the circulating hot air enters the rear heat box with the heat radiation plate as the bottom plate, and then the circulating hot air enters the front heat box with the heat radiation plate as the bottom plate through the connecting pipe;
G.接下来,循环热风从前热箱出来进入二次催化室,二次催化燃烧的热能在热交换器进行热交换,将由新风风机压入的新风加热,形成新热风;G. Next, the circulating hot air comes out from the front heat box and enters the secondary catalytic chamber. The heat energy of the secondary catalytic combustion is exchanged in the heat exchanger, and the fresh air pressed in by the fresh air fan is heated to form new hot air;
H.接下来新热风经新热风道由出风口喷出,进入前炉空间,对微细线进行烘焙,微细线上逸出的有机废气进入有机废气入口;H. Next, the new hot air is ejected from the air outlet through the new hot air channel, enters the forehearth space, and bakes the fine wire, and the organic waste gas escaping from the fine wire enters the organic waste gas inlet;
I.微细线向前运行,进入后炉空间,继续有有机废气从微细线上逸出,这部分有机废气也进入有机废气入口;I. The fine wire runs forward and enters the rear furnace space, and organic waste gas continues to escape from the fine wire, and this part of organic waste gas also enters the organic waste gas inlet;
J.观测催化燃烧热能是否达到独立运行状态,如未达到则向下运行步骤K;如果达到,则运行步骤L;J. Observe whether the catalytic combustion heat energy reaches the independent operation state, if not, then run step K downward; if it is reached, then run step L;
K.转步骤D。K. Go to step D.
L.催化燃烧热能达到正常循环后,主炉加热管、一次催化加热管、二次催化加热管全部或部分被断电;L. After the catalytic combustion heat reaches a normal cycle, all or part of the main furnace heating tube, the primary catalytic heating tube, and the secondary catalytic heating tube are cut off;
M.转步骤D。M. Go to step D.
在实现上述方法的各步骤中,对主炉加热管、一次催化加热管、二次催化加热管、前热箱、后热箱、循环热风道、循环风机、一次催化室、热交换器、二次催化室、新热风道外部皆设置保温部。In each step of realizing the above method, the main furnace heating tube, the primary catalytic heating tube, the secondary catalytic heating tube, the front hot box, the rear hot box, the circulating hot air duct, the circulating fan, the primary catalytic chamber, the heat exchanger, the secondary The secondary catalytic chamber and the exterior of the new hot air duct are equipped with heat preservation parts.
在上述方法的步骤C中,所述连通管为一只以上,间隔排列于有机废气入口中。In step C of the above method, there are more than one connecting pipes arranged at intervals in the organic waste gas inlet.
上述方法中,所述前热辐射板和后热辐射板采用金属板。In the above method, the front heat radiation plate and the rear heat radiation plate are metal plates.
设计制造一种实现上述方法的微细线漆包机利用催化热能的设备,该设备基于安装了主炉加热管、一次催化加热管的主炉体、循环风机、热交换器以及一次催化室;Design and manufacture a device for utilizing catalytic heat energy in a micro-wire enamelling machine that realizes the above method. The device is based on a main furnace body equipped with a main furnace heating tube, a primary catalytic heating tube, a circulating fan, a heat exchanger, and a primary catalytic chamber;
所述设备还包括:The device also includes:
一有机废气入口,位于前炉空间和后炉空间的交界,偏于前炉空间的位置,所述有机废气入口吸收由微细线上逸出的有机废气;An organic waste gas inlet, located at the junction of the forehearth space and the back furnace space, offset from the position of the forehearth space, the organic waste gas inlet absorbs the organic waste gas escaping from the fine line;
一前热辐射板和一后热辐射板设置在前炉空间和后炉空间的上方;A front heat radiation plate and a rear heat radiation plate are arranged above the front furnace space and the rear furnace space;
所述前热辐射板和后热辐射板的长度不小于主炉空间长度的68%;The length of the front heat radiation plate and the rear heat radiation plate is not less than 68% of the length of the main furnace space;
一个一次催化室在有机废气入口上方设置,在一次催化室的进口前方设置一次催化加热管,在一次催化室的出口处设置循环风机;A primary catalytic chamber is arranged above the inlet of the organic waste gas, a primary catalytic heating pipe is arranged in front of the inlet of the primary catalytic chamber, and a circulating fan is arranged at the outlet of the primary catalytic chamber;
一循环热风道连接循环风机将催化燃烧后的循环热风送入后热箱。A circulating hot air duct is connected with a circulating fan to send the catalytically combusted circulating hot air into the rear hot box.
所述后热辐射板是后热箱的底板,所述前热辐射板是前热箱的底板。The rear heat radiation plate is the bottom plate of the rear heat box, and the front heat radiation plate is the bottom plate of the front heat box.
所述前热箱和后热箱之间有至少一个连通管,循环热风通过从其间通过。There is at least one communication pipe between the front heat box and the rear heat box, through which circulating hot air passes.
所述主炉加热管、一次催化加热管、前热箱、后热箱、循环热风道、循环风机、一次催化室外部皆设置保温部。The main furnace heating pipe, the primary catalytic heating pipe, the front heating box, the rear heating box, the circulating hot air duct, the circulating fan and the primary catalytic chamber are all equipped with heat preservation parts.
与现有技术相比较,本发明的微细线漆包机利用催化热能的方法和设备,专门用于加工0.05mm左右的漆包线,由于充分利用了催化热能,而且彻底杜绝了有机废气与漆包线的接触,从而保证了漆包线的质量。Compared with the prior art, the micro-wire enamelling machine of the present invention utilizes the method and equipment of catalytic heat energy, and is specially used for processing enameled wires of about 0.05 mm in diameter. Since the catalytic heat energy is fully utilized, and the contact between organic waste gas and enameled wires is completely eliminated, Thereby ensuring the quality of the enameled wire.
本发明的突出技术贡献是采用了超大面积的热辐射板,将催化热能充分地加热热辐射板,又合理地确定了有机废气入口的位置,以及合理地驱动有机废气的流动。所以本发明有突出的节能效果:每天耗电仅为300度,较同类设备相比,节电30%以上。The outstanding technical contribution of the present invention is the use of a super-large-area heat radiation plate, which can fully heat the heat radiation plate with catalytic heat energy, reasonably determine the position of the organic waste gas inlet, and reasonably drive the flow of the organic waste gas. Therefore, the present invention has an outstanding energy-saving effect: the daily power consumption is only 300 degrees, and compared with similar equipment, it can save more than 30% of electricity.
附图说明 Description of drawings
图1是本发明的微细线漆包机利用催化热能的方法和设备的原理示意图。Fig. 1 is a schematic diagram of the method and equipment for utilizing catalytic heat energy in the micro-wire enamelling machine of the present invention.
图中标号:100微细线。The reference number in the figure: 100 fine lines.
1循环风机,2一次催化室,3新风风机。1 circulating fan, 2 primary catalytic chamber, 3 fresh air fan.
4热交换器,5二次催化室。4 heat exchangers, 5 secondary catalytic chambers.
9主炉体,11循环风机电机,12循环热风道,13后热箱。9 main furnace body, 11 circulating fan motor, 12 circulating hot air passage, 13 rear hot box.
14后热辐射板,15连通管,16前热箱16。14 rear heat radiation panels, 15 connecting pipes, 16
17前热辐射板,18有机废气入口。17 front heat radiation panels, 18 organic waste gas inlets.
41新热风道,42出风口。41 new hot air duct, 42 air outlet.
51二次催化加热管,52主炉加热管,53一次催化加热管。51 secondary catalytic heating tube, 52 main furnace heating tube, 53 primary catalytic heating tube.
61前炉空间,62后炉空间,64保温部。61 front furnace space, 62 rear furnace space, 64 heat preservation department.
具体实施方式 Detailed ways
下面结合附图与具体实施方式对本发明作进一步详细描述:Below in conjunction with accompanying drawing and specific embodiment the present invention is described in further detail:
如图1所示最佳实施例,The preferred embodiment shown in Figure 1,
实施一种微细线漆包机利用催化热能的方法,所述方法基于安装了主炉加热管52的主炉体、循环风机1、热交换器4以及一次催化室2的漆包机;所述主炉加热管52用于预热工序;Carry out a kind of method that micro-wire enamelling machine utilizes catalytic heat energy, described method is based on the enamelling machine that the main furnace body of main
所述方法包括如下步骤:The method comprises the steps of:
A.首先在前炉空间61和后炉空间62的交界处设置有机废气入口18,所述有机废气入口18位于主炉体中部偏于前炉空间61的位置,所述有机废气入口18吸收由微细线100上逸出的有机废气;A. First, an organic
B.在前炉空间61和后炉空间62的上方设置前热辐射板17和后热辐射板14,所述前热辐射板17和后热辐射板14的长度不小于主炉空间长度的68%;B. Set the front
C.在有机废气入口18上方设置一次催化室2,在一次催化室2的进口前方设置一次催化加热管53,在一次催化室2的出口处设置循环风机1;C. Set a primary catalytic chamber 2 above the organic
D.有机废气在一次催化室2催化燃烧形成循环热风;D. The organic waste gas is catalytically burned in the primary catalytic chamber 2 to form circulating hot air;
E.接下来循环风机1将催化燃烧后的循环热风送入循环热风道12;E. Next, the circulation fan 1 sends the circulation hot air after the catalytic combustion into the circulation
F.接下来,循环热风进入以后热辐射板14为底板的后热箱13,然后循环热风通过连通管15进入以前热辐射板17为底板的前热箱16;F. Next, the circulating hot air enters the
G.接下来,循环热风从前热箱16出来进入二次催化室5,二次催化燃烧的热能在热交换器4进行热交换,将由新风风机3压入的新风加热,形成新热风;G. Next, the circulating hot air enters the secondary catalytic chamber 5 from the front
H.接下来新热风经新热风道41由出风口42喷出,进入前炉空间61,对微细线100进行烘焙,微细线100上逸出的有机废气进入有机废气入口18;H. Next, the new hot air is ejected from the
I.微细线100向前运行,进入后炉空间62,继续有有机废气从微细线100上逸出,这部分有机废气也进入有机废气入口18;I. The
J.观测催化燃烧热能是否达到独立运行状态,如未达到则向下运行步骤K;如果达到,则运行步骤L;J. Observe whether the catalytic combustion heat energy reaches the independent operation state, if not, then run step K downward; if it is reached, then run step L;
K.转步骤D。K. Go to step D.
L.催化燃烧热能达到正常循环后,主炉加热管52、一次催化加热管53、二次催化加热管51全部或部分被断电;L. After the catalytic combustion heat reaches a normal cycle, the main
M.转步骤D。M. Go to step D.
在实现上述方法的各步骤中,对主炉加热管52、一次催化加热管53、二次催化加热管51、前热箱16、后热箱13、循环热风道12、循环风机1、一次催化室2、热交换器4、二次催化室5、新热风道41外部皆设置保温部64。In each step of realizing above-mentioned method, main
在步骤C中,所述连通管15为一只以上,间隔排列于有机废气入口18中。In step C, there are more than one
所述前热辐射板17和后热辐射板14采用金属板。The front
设计制造一种微细线漆包机利用催化热能的设备,所述设备基于安装了主炉加热管52、一次催化加热管53的主炉体9、循环风机1、热交换器4以及一次催化室2;Design and manufacture a kind of equipment for micro-wire enamelling machine to use catalytic heat energy. The equipment is based on the
所述设备包括:The equipment includes:
一有机废气入口18,位于前炉空间61和后炉空间62的交界,偏于前炉空间61的位置,所述有机废气入口18吸收由微细线100上逸出的有机废气;An organic
一前热辐射板17和一后热辐射板14设置在前炉空间61和后炉空间62的上方;A front
所述前热辐射板17和后热辐射板14的长度不小于主炉空间长度的68%;The length of the front
一个一次催化室2在有机废气入口18上方设置,在一次催化室2的进口前方设置一次催化加热管53,在一次催化室2的出口处设置循环风机1;A primary catalytic chamber 2 is set above the organic
一循环热风道12连接循环风机1将催化燃烧后的循环热风送入后热箱13。A circulating
所述后热辐射板14是后热箱13的底板,所述前热辐射板17是前热箱16的底板。The rear
所述前热箱16和后热箱13之间有至少一个连通管15,循环热风通过从其间通过。There is at least one
所述主炉加热管52、一次催化加热管53、前热箱16、后热箱13、循环热风道12、循环风机1、一次催化室2外部皆设置保温部64。The main
综上所述,本发明突破了一个禁区,即:在微细线漆包机中如何实现以催化热能为主进行烘焙,因为此时是要完全屏蔽有机废气,以杜绝其中的超细微粒粘附在漆包线上,影响漆包线质量。To sum up, the present invention breaks through a forbidden area, that is, how to achieve baking based on catalytic heat energy in the fine wire enamelling machine, because at this time, the organic waste gas must be completely shielded to prevent the ultrafine particles from adhering to the surface. Enameled wire affects the quality of enameled wire.
本发明的微细线漆包机利用催化热能的方法和设备,专门用于加工0.05mm左右的漆包线,由于充分利用了催化热能,而且彻底杜绝了有机废气与漆包线的接触,从而保证了漆包线的质量。The micro-wire enamelling machine of the present invention utilizes the method and equipment of catalytic heat energy, and is specially used for processing enameled wires of about 0.05 mm in diameter. Since the catalytic heat energy is fully utilized, and the contact between organic waste gas and enameled wires is completely eliminated, the quality of enameled wires is guaranteed.
本发明的突出技术贡献是采用了超大面积的热辐射板,将催化热能充分地加热热辐射板,又合理地确定了有机废气入口的位置,以及合理地驱动有机废气的流动。所以本发明有突出的节能效果:每天耗电仅为300度,较同类设备相比,节电30%以上。The outstanding technical contribution of the present invention is the use of a super-large-area heat radiation plate, which can fully heat the heat radiation plate with catalytic heat energy, reasonably determine the position of the organic waste gas inlet, and reasonably drive the flow of the organic waste gas. Therefore, the present invention has an outstanding energy-saving effect: the daily power consumption is only 300 degrees, and compared with similar equipment, it can save more than 30% of electricity.
以上内容是结合具体的优选实施方式对本发明所作的进一步详细说明,不能认定本发明的具体实施只局限于这些说明。对于本发明所属技术领域的普通技术人员来说,在不脱离本发明构思的前提下,还可以做出若干简单推演或替换,都应当视为属于本发明的保护范围。The above content is a further detailed description of the present invention in conjunction with specific preferred embodiments, and it cannot be assumed that the specific implementation of the present invention is limited to these descriptions. For those of ordinary skill in the technical field of the present invention, without departing from the concept of the present invention, some simple deduction or replacement can be made, which should be regarded as belonging to the protection scope of the present invention.
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Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102368412A (en) * | 2011-09-14 | 2012-03-07 | 吴江市神州机械有限公司 | Cyclic baking method of enamelled wire and oven for realizing method |
| CN102543321A (en) * | 2011-11-14 | 2012-07-04 | 周开勇 | An energy-saving and environment-friendly vertical enamelled oven and its control method |
| CN102867597A (en) * | 2012-08-20 | 2013-01-09 | 东莞泽龙线缆有限公司 | A method for setting the return air volume of a multi-line enamelling machine for energy saving and emission reduction and its equipment structure |
| CN107385162A (en) * | 2017-09-04 | 2017-11-24 | 马鞍山钢铁股份有限公司 | A kind of cold rolling vertical type continuous annealing furnace radiation tubular construction |
| CN114937534A (en) * | 2022-04-01 | 2022-08-23 | 卫辉市云波漆包线有限公司 | Energy-concerving and environment-protective enamelling machine |
| CN117316549A (en) * | 2023-10-16 | 2023-12-29 | 无锡市瑞球科技有限公司 | Vertical enameled wire wind circulating device |
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2009
- 2009-10-16 CN CN2009101107823A patent/CN101697295B/en not_active Expired - Fee Related
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102368412A (en) * | 2011-09-14 | 2012-03-07 | 吴江市神州机械有限公司 | Cyclic baking method of enamelled wire and oven for realizing method |
| CN102543321A (en) * | 2011-11-14 | 2012-07-04 | 周开勇 | An energy-saving and environment-friendly vertical enamelled oven and its control method |
| CN102543321B (en) * | 2011-11-14 | 2013-06-26 | 周开勇 | Energy-saving environment-friendly vertical enamelled baking oven and control method thereof |
| CN102867597A (en) * | 2012-08-20 | 2013-01-09 | 东莞泽龙线缆有限公司 | A method for setting the return air volume of a multi-line enamelling machine for energy saving and emission reduction and its equipment structure |
| CN102867597B (en) * | 2012-08-20 | 2014-06-18 | 东莞泽龙线缆有限公司 | Method and equipment structure for setting energy-saving emission-reduction return air volume of multi-wire enamelling machine |
| CN107385162A (en) * | 2017-09-04 | 2017-11-24 | 马鞍山钢铁股份有限公司 | A kind of cold rolling vertical type continuous annealing furnace radiation tubular construction |
| CN114937534A (en) * | 2022-04-01 | 2022-08-23 | 卫辉市云波漆包线有限公司 | Energy-concerving and environment-protective enamelling machine |
| CN114937534B (en) * | 2022-04-01 | 2023-05-05 | 卫辉市云波漆包线有限公司 | Energy-saving and environment-friendly enameling machine |
| CN117316549A (en) * | 2023-10-16 | 2023-12-29 | 无锡市瑞球科技有限公司 | Vertical enameled wire wind circulating device |
| CN117316549B (en) * | 2023-10-16 | 2024-03-26 | 无锡市瑞球科技有限公司 | Vertical enameled wire wind circulating device |
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