CN107261657A - 一种工业滤袋除尘器 - Google Patents

一种工业滤袋除尘器 Download PDF

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CN107261657A
CN107261657A CN201710522457.2A CN201710522457A CN107261657A CN 107261657 A CN107261657 A CN 107261657A CN 201710522457 A CN201710522457 A CN 201710522457A CN 107261657 A CN107261657 A CN 107261657A
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carbon
parts
basket strainer
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leaching
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CN107261657B (zh
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单素梅
朱彦加
朱靓靓
吴健健
张瑜
李素英
付译鋆
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Jiangsu Lingfulong Environmental Engineering Co Ltd
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Abstract

本发明公开了一种工业滤袋除尘器，包括除尘器的本体，本体的一端设置入口，另一端设置除尘袋，本体内部设置浸碳除尘网，其中浸碳除尘网两端设置导线接头，浸碳除尘网与入口之间的本体内部设置有电晕线。本发明提供的工业滤袋除尘器利用浸碳除尘网作为电极和除尘载体，能够最大限度地发挥除尘效果，不仅通过静电除尘能够吸附尘粒，同时作为除尘网自身也能够发挥除尘作用，进而提高了除尘效果。同时通过将丙纶纱线进行改性与浸碳，实现了滤网性能与电极性能的同时实现。

Description

一种工业滤袋除尘器
技术领域
本发明属于滤袋除尘领域，具体一种工业滤袋除尘器。
背景技术
袋式除尘器在工业生产中广泛使用，由于其结构简单易于维护，在实际使用过程中得到了广泛的好评。现有的袋式除尘器大都由滤袋框和除尘袋的组合构成，并且，现有的袋式空气过滤器只采用一层滤袋过滤的方式，其过滤效果有限，不能够高效完成灰尘较多、颗粒较大的空气过滤作业，且在过滤灰尘较多、颗粒较大的气流时，除尘袋很容易发生堵塞，导致除尘袋的除尘周期有限，除尘袋上沉积的灰尘不易去除干净。同时除尘袋在过滤过程中由于其本身机械性能有限，导致了过滤高强气流中的灰尘时，除尘袋在长期使用过程中，尤其是在高温条件下长期使用过程中，除尘袋的寿命有限，过滤性能逐步下降。
发明内容
本发明的目的在于提供一种工业滤袋除尘器，通过静电除尘结合后期的布袋除尘最大限度地去除尘粒，同时通过浸碳除尘网的改性，实现除尘与浸碳效果的同时提升。
本发明通过以下技术方案实现：
本发明提供了一种工业滤袋除尘器，包括除尘器的本体，本体的一端设置入口，另一端设置除尘袋，本体内部设置浸碳除尘网，其中浸碳除尘网两端设置导线接头，浸碳除尘网与入口之间的本体内部设置有电晕线。
进一步地，所述的工业滤袋除尘器，本体上设置有插槽，浸碳除尘网以可拆卸的方式插入插槽。
进一步地，所述的工业滤袋除尘器，除尘袋与本体以可拆卸方式连接。
进一步地，所述的工业滤袋除尘器，浸碳除尘网与入口之间的本体底部设置储尘仓，储尘仓上设置有仓门。
进一步地，所述的工业滤袋除尘器，浸碳除尘网由以下重量份计的组分制备而成：环氧树脂6-8份，聚二甲基硅氧烷3-8份，聚氧乙烯脂肪酸酯1-3份，碳粉15-20份，二异氰酸酯4-8份，2,6-二叔丁基对甲酚0.5-1份，酚醛树脂4-7份，苯乙烯2-5份，丙纶纱线20-30份，聚醚二元醇2-5份和溶剂300-350份。
更进一步地，环氧树脂可为双酚A型环氧树脂；溶剂可为甲苯、正丁醇或异丁醇。
更进一步地，浸碳除尘网的制备方法如下：
步骤1，将环氧树脂粉碎至粒径200μm以下，得到环氧树脂粉末；
步骤2，将环氧树脂粉末与丙纶纱线混合，得纱线混合物，再在表面涂刷聚醚二元醇和聚二甲基硅氧烷的混合物，然后热压成型；
步骤3，将碳粉分散于溶剂中，加入聚氧乙烯脂肪酸酯，混合后在氮气保护条件下加入二异氰酸酯，2,6-二叔丁基对甲酚，酚醛树脂和苯乙烯，混合后得到浸碳混合液；
步骤4，将步骤2热压成型后的纱线浸入步骤3得到的浸碳混合液中，35-40℃下反应130-150分钟，然后再在60-70℃条件下反应250-280分钟，降至室温，取出纱线，烘干，得到浸碳纱线；
步骤5，将浸碳纱线进行织网，得到浸碳除尘网。
更进一步地，步骤4中烘干的温度可为80-100℃。
本发明提供的工业滤袋除尘器利用浸碳除尘网作为电极和除尘载体，能够最大限度地发挥除尘效果，不仅通过静电除尘能够吸附尘粒，同时作为除尘网自身也能够发挥除尘作用，进而提高了除尘效果。
本发明提供的静电除尘能够有效的进行前期的尘粒的过滤和去除，很好的避免了后期除尘袋除尘过程中由于大量尘粒造成的堵塞。
本发明还提供了浸碳除尘网及其制备方法，该浸碳除尘网具有良好的综合性能，不仅增强了滤网的机械性能，同时经涂覆后的滤网表面水滴角达到了126°以上，同时显著提升了滤网的拉伸断裂强度。滤网上的灰尘能够较为容易的被清除，延长了滤网使用寿命。
本发明提供的浸碳除尘网，通过将丙纶纱线进行改性，使得其更加容易与后期浸碳混合液中的组分共聚来提高碳粉与纱线的结合力。丙纶纱线混合改性后，在后期浸碳过程中，浸碳混合液中的二异氰酸酯，2,6-二叔丁基对甲酚，酚醛树脂和苯乙烯在共聚改性的过程中，通过低温(35-40℃)改性嫁接与高温(60-70℃)共聚反应，能够与改性后的丙纶纱线共聚结合，从而牢固地将碳附着在纱线表面，形成复合共聚体，显著增强了纱线的机械性能，同时在表面形成聚合表面的防水膜层，增强了灰尘的易去除性。
本发明通过将丙纶纱线的改性浸碳，巧妙地实现了静电除尘与滤网特性的双重提升，将以上特性通过特定组分与制备方式的结合协同实现。
附图说明
图1为本发明实施例1中工业滤袋除尘器的结构示意图，其中1为本体，2为入口，3为除尘袋，4为浸碳除尘网，5为导线接头，6为电晕线，7为储尘仓，8为仓门。
具体实施方式：
实施例1
如图1所示，为本实施例提供的工业滤袋除尘器示意图，包括除尘器的本体1，本体1的一端设置入口2，另一端设置除尘袋3，本体1内部设置浸碳除尘网4，其中浸碳除尘网4两端设置导线接头5，浸碳除尘网4与入口2之间的本体1内部设置有电晕线6。为了便于更换，在本体1上设置有插槽，浸碳除尘网4以可拆卸的方式插入插槽；除尘袋3与本体1以可拆卸方式连接；浸碳除尘网4与入口2之间的本体1底部设置储尘仓7，储尘仓7上设置有仓门8。
本实施例提供的工业滤袋除尘器在除尘过程中，将电晕线6和浸碳除尘网4与电源连接，形成静电除尘场，待除尘气流经入口2进入本体1内部，在静电除尘的作用下尘粒吸附于浸碳除尘网4上得到去除，储尘仓7可以将静电除尘沉积在本体1底部的灰尘收集后通过仓门8排出，在静电除尘场中未除干净的灰尘可以通过后续的除尘袋3进一步去除干净。
本实施例提供的工业滤袋除尘器利用浸碳除尘网作为电极和除尘载体，能够最大限度地发挥除尘效果，不仅通过静电除尘能够吸附尘粒，同时作为除尘网自身也能够发挥除尘作用，进而提高了除尘效果。
实施例2-4
以下实施例2-4中是对实施例1中浸碳除尘网4进行的进一步改进，其中浸碳除尘网(4)由以下重量份计的组分制备而成：环氧树脂6-8份，聚二甲基硅氧烷3-8份，聚氧乙烯脂肪酸酯1-3份，碳粉15-20份，二异氰酸酯4-8份，2,6-二叔丁基对甲酚0.5-1份，酚醛树脂4-7份，苯乙烯2-5份，丙纶纱线20-30份，聚醚二元醇2-5份和溶剂300-350份。
以上环氧树脂为双酚A型环氧树脂；溶剂为甲苯、正丁醇或异丁醇；
制备方法如下：
步骤1，将环氧树脂粉碎至粒径200μm以下，得到环氧树脂粉末；
步骤2，将环氧树脂粉末与丙纶纱线混合，得纱线混合物，再在表面涂刷聚醚二元醇和聚二甲基硅氧烷的混合物，然后热压成型；
步骤3，将碳粉分散于溶剂中，加入聚氧乙烯脂肪酸酯，混合后在氮气保护条件下加入二异氰酸酯，2,6-二叔丁基对甲酚，酚醛树脂和苯乙烯，混合后得到浸碳混合液；
步骤4，将步骤2热压成型后的纱线浸入步骤3得到的浸碳混合液中，35-40℃下反应130-150分钟，然后再在60-70℃条件下反应250-280分钟，降至室温，取出纱线，80-100℃下烘干，得到浸碳纱线；
步骤5，将浸碳纱线进行织网，得到浸碳除尘网。
具体实施过程如下：
项目 实施例2 实施例3 实施例4
环氧树脂 6 7 8
聚二甲基硅氧烷 3 5 8
聚氧乙烯脂肪酸酯 1 2 3
碳粉 15 17 20
二异氰酸酯 4 6 8
2,6-二叔丁基对甲酚 0.5 0.7 1
酚醛树脂 4 6 7
苯乙烯 2 3 5
丙纶纱线 20 25 30
聚醚二元醇 2 4 5
甲苯 300
正丁醇 320
异丁醇 350
对以上实施例2-4制备得到的浸碳除尘网进行性能测试，并与单纯的实施例中的丙纶纱线织网后形成的同样规格的滤网进行对比，结果表明，滤网的经向与纬向的拉伸断裂强度均提高了1000N/5cm以上，热收缩率(100℃，放置60min)提高了5％以上，同时水滴角从85°提高到了126°以上。
本发明提供的浸碳除尘网，通过将丙纶纱线进行改性，使得其更加容易与后期浸碳混合液中的组分共聚来提高碳粉与纱线的结合力。
以上实施例提供的浸碳除尘网，具有良好的综合性能，不仅增强了滤网的机械性能，同时经涂覆后的滤网表面水滴角达到了126°以上，同时显著提升了滤网的拉伸断裂强度。滤网上的灰尘能够较为容易的被清除，延长了滤网使用寿命，同时，在丙纶纱线混合改性后，在后期浸碳过程中，浸碳混合液中的二异氰酸酯，2,6-二叔丁基对甲酚，酚醛树脂和苯乙烯在共聚改性的过程中，通过低温(30-40℃)改性嫁接与高温(60-70℃)共聚反应，能够与改性丙纶纱线共聚结合，从而牢固地将碳附着在纱线表面，形成复合共聚体，显著增强了纱线的机械性能，同时在表面形成聚合表面的防水膜层，增强了灰尘的易去除性。

Claims (9)

1.一种工业滤袋除尘器，其特征在于，包括除尘器的本体(1)，本体(1)的一端设置入口(2)，另一端设置除尘袋(3)，本体(1)内部设置浸碳除尘网(4)，其中浸碳除尘网(4)两端设置导线接头(5)，浸碳除尘网(4)与入口(2)之间的本体(1)内部设置有电晕线(6)。
2.根据权利要求1所述的工业滤袋除尘器，其特征在于，本体(1)上设置有插槽，浸碳除尘网(4)以可拆卸的方式插入插槽。
3.根据权利要求1所述的工业滤袋除尘器，其特征在于，除尘袋(3)与本体(1)以可拆卸方式连接。
4.根据权利要求1所述的工业滤袋除尘器，其特征在于，浸碳除尘网(4)与入口(2)之间的本体(1)底部设置储尘仓(7)，储尘仓(7)上设置有仓门(8)。
5.根据权利要求1所述的工业滤袋除尘器，其特征在于，浸碳除尘网(4)由以下重量份计的组分制备而成：环氧树脂6-8份，聚二甲基硅氧烷3-8份，聚氧乙烯脂肪酸酯1-3份，碳粉15-20份，二异氰酸酯4-8份，2,6-二叔丁基对甲酚0.5-1份，酚醛树脂4-7份，苯乙烯2-5份，丙纶纱线20-30份，聚醚二元醇2-5份和溶剂300-350份。
6.根据权利要求5所述的工业滤袋除尘器，其特征在于，环氧树脂为双酚A型环氧树脂。
7.根据权利要求5所述的工业滤袋除尘器，其特征在于，溶剂为甲苯、正丁醇或异丁醇。
8.根据权利要求5所述的工业滤袋除尘器，其特征在于，浸碳除尘网(4)的制备方法如下：
步骤1，将环氧树脂粉碎至粒径200μm以下，得到环氧树脂粉末；
步骤2，将环氧树脂粉末与丙纶纱线混合，得纱线混合物，再在表面涂刷聚醚二元醇和聚二甲基硅氧烷的混合物，然后热压成型；
步骤3，将碳粉分散于溶剂中，加入聚氧乙烯脂肪酸酯，混合后在氮气保护条件下加入二异氰酸酯，2,6-二叔丁基对甲酚，酚醛树脂和苯乙烯，混合后得到浸碳混合液；
步骤4，将步骤2热压成型后的纱线浸入步骤3得到的浸碳混合液中，35-40℃下反应130-150分钟，然后再在60-70℃条件下反应250-280分钟，降至室温，取出纱线，烘干，得到浸碳纱线；
步骤5，将浸碳纱线进行织网，得到浸碳除尘网。
9.根据权利要求8所述的工业滤袋除尘器，其特征在于，步骤4中烘干的温度为80-100℃。
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