WO2016176953A1 - 一种活性炭纤维烧结滤芯及其制备方法 - Google Patents

一种活性炭纤维烧结滤芯及其制备方法 Download PDF

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WO2016176953A1
WO2016176953A1 PCT/CN2015/090379 CN2015090379W WO2016176953A1 WO 2016176953 A1 WO2016176953 A1 WO 2016176953A1 CN 2015090379 W CN2015090379 W CN 2015090379W WO 2016176953 A1 WO2016176953 A1 WO 2016176953A1
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activated carbon
carbon fiber
filter element
sintered
molecular weight
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PCT/CN2015/090379
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French (fr)
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杨国伟
陈凯
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苏州凯虹高分子科技有限公司
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Priority to DE212015000035.4U priority Critical patent/DE212015000035U1/de
Priority to JP2016546970A priority patent/JP2017519617A/ja
Publication of WO2016176953A1 publication Critical patent/WO2016176953A1/zh

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    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D39/00—Filtering material for liquid or gaseous fluids
    • B01D39/14—Other self-supporting filtering material ; Other filtering material
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/22—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material
    • B01J20/26—Synthetic macromolecular compounds
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/30—Processes for preparing, regenerating, or reactivating

Definitions

  • the invention relates to an activated carbon fiber sintered filter core, belonging to the field of water purification.
  • the filter cores recognized by the majority of customers include: extruded activated carbon powder filter and sintered activated carbon powder filter.
  • the extruded activated carbon powder filter element is extruded from an activated carbon powder and added to a binder heating extruder.
  • the activated carbon powder sintered filter element is a filter element which is mixed, super-high molecular weight polyethylene and activated carbon powder, pressed, semi-melt sintered and formed, compared with the extruded activated carbon filter element, because of the ultra high molecular weight polyethylene During sintering, it is a semi-melt state of surface melting, which does not block the micropores of activated carbon powder, and the opening ratio of activated carbon powder is doubled, so that the product has better adsorption effect, but there is still low strength. , powder removal, small flux, unsatisfactory adsorption effect.
  • Chinese Patent No. 201110237812.4 discloses a preparation method of a filter medium for removing synthetic musk in drinking water, comprising the following steps: a) comprising activated carbon fiber powder, ultra high molecular weight polyethylene powder, nano silica powder, active The raw material of the alumina powder and the porogen is mixed, and the weight ratio of the activated carbon fiber powder, the ultrahigh molecular weight polyethylene powder, the nano silica powder, the activated alumina powder and the pore former is 100-300:200-450: 80 to 200: 80 to 200: 50 to 150; b) The mixture obtained in the step a) is pressed in a mold, sintered, and cooled.
  • the technical problem to be solved by the present invention is to provide an activated carbon fiber sintered filter element.
  • An activated carbon fiber sintered filter core is prepared by mixing ultra-high molecular weight polyethylene and activated carbon fiber, and then being pressed, sintered and cooled.
  • the ultrahigh molecular weight polyethylene 20 to 80 parts
  • the activated carbon fiber 20 to 80 parts
  • the ultrahigh molecular weight polyethylene has a molecular weight of 1.5 to 6 million and a particle diameter of 40 to 300 mesh.
  • the activated carbon fiber is subjected to destaticization and pulverization treatment, and the particle diameter after the treatment is 15-840 ⁇ m.
  • the temperature of the sintering process is 170-300 ° C for 10 - 60 min.
  • the cooling temperature is 20 to 60 °C.
  • a method for preparing an activated carbon fiber sintered filter core comprises the following steps:
  • the activated carbon fiber is subjected to static elimination and pulverization, and the particle size after treatment is 15-840 ⁇ m;
  • step 2) The mixture obtained in the step 2) is pressed, and then semi-melt sintered at 170-300 ° C for 10-60 min; then it is cooled and formed at 20-60 ° C.
  • Products can be made into a variety of shapes.
  • a method for preparing an activated carbon fiber sintered filter core comprises the following steps:
  • the activated carbon fiber is subjected to static elimination and pulverization, and the particle size after treatment is 15 ⁇ m;
  • step 2) The mixture obtained in the step 2) is pressed, and then sintered at 170 ° C for 10 min; then it is cooled and formed at 20 ° C.
  • a method for preparing an activated carbon fiber sintered filter core comprises the following steps:
  • the activated carbon fiber is subjected to static elimination and pulverization, and the particle size after treatment is 840 ⁇ m;
  • step 3 The mixture obtained in the step 2) is pressed, and then sintered at 300 ° C for 60 min; then it is cooled and formed at 60 ° C.
  • a method for preparing an activated carbon fiber sintered filter core comprises the following steps:
  • the activated carbon fiber is subjected to static elimination and pulverization, and the particle size after treatment is 15 ⁇ m;
  • step 3 The mixture obtained in the step 2) is pressed, and then sintered at 300 ° C for 60 min; then it is cooled and formed at 20 ° C.
  • a method for preparing an activated carbon fiber sintered filter core comprises the following steps:
  • the activated carbon fiber is subjected to static elimination and pulverization, and the particle size after treatment is 840 ⁇ m;
  • step 3 The mixture obtained in the step 2) is pressed, and then sintered at 300 ° C for 10 min; then it is cooled and formed at 60 ° C.
  • a method for preparing an activated carbon fiber sintered filter core comprises the following steps:
  • the activated carbon fiber is subjected to static elimination and pulverization, and the particle size after treatment is 540 ⁇ m;
  • step 3 The mixture obtained in the step 2) is pressed, and then sintered at 200 ° C for 40 min; then it is cooled and formed at 40 ° C.

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Analytical Chemistry (AREA)
  • Organic Chemistry (AREA)
  • Water Treatment By Sorption (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)
  • Filtering Materials (AREA)

Abstract

一种活性炭纤维烧结滤芯及其制备方法。该滤芯由超高分子量聚乙烯和活性炭纤维混合后，经压制、烧结、冷却成型制得。该滤芯具有强度高、通量大、吸附效果好、去余氯和杂质效果好的优点。

Description

一种活性炭纤维烧结滤芯及其制备方法 技术领域
本发明涉及一种活性炭纤维烧结滤芯，属于净水领域。
背景技术
随着人们对饮用水安全的重视，市场上出现了各种各样饮用水处理用滤芯，被广大客户所认同的滤芯主要有：挤出活性炭粉末滤芯和烧结活性炭粉末滤芯。挤出活性炭粉末滤芯是由活性炭粉末加入粘结剂加温用挤出机挤出而成，大部份的活性炭粉末的颗粒和相互之间的微孔会被粘结剂包裹及堵塞，从而使产品吸附效果稍差；活性炭粉末烧结滤芯是由超高分子量聚乙烯和活性炭粉末混合后，经压制、半融熔烧结、成型的滤芯，与挤出活性炭滤芯相比，因超高分子量聚乙烯在烧结成型时是表面融熔的半融熔状态，不会较多的堵塞活性炭粉末的微孔，活性炭粉末的开孔率成倍的增加，使产品具有较好吸附效果，但仍存在有强度低、脱粉、通量小、吸附效果不理想的问题。
例如：中国专利201110237812.4公开了一种用于去除饮用水中人工合成麝香的过滤介质的制备方法，包括如下步骤：a)将包含活性炭纤维粉、超高分子量聚乙烯粉、纳米氧化硅粉、活性氧化铝粉和发孔剂的原料混合，所述活性炭纤维粉、超高分子量聚乙烯粉、纳米氧化硅粉、活性氧化铝粉和发孔剂的重量比为：100～300∶200～450∶80～200∶80～200∶50～150；b)将步骤a)所得的混合物在模具中压制，烧结，冷却。
发明内容
本发明要解决的技术问题是提供一种活性炭纤维烧结滤芯。
本发明是通过以下技术方案来实现：
一种活性炭纤维烧结滤芯，由超高分子量聚乙烯和活性炭纤维混合后，经压制、烧结、冷却成型制得。
进一步，超高分子量聚乙烯：20～80份，活性碳纤维：20-80份。
进一步，所述超高分子量聚乙烯的分子量：150万-600万，粒径：40-300目。
进一步，所述活性炭纤维经去静电和粉碎处理，处理后粒径为15-840μm。
进一步，烧结过程的温度170-300℃，时间10-60min。
进一步，冷却温度为20-60℃。
一种活性炭纤维烧结滤芯的制备方法，包括以下步骤：
1)将活性炭纤维经去静电和粉碎，处理后粒径为15-840μm；
2)将分子量为150万-600万粒径40-300目的聚乙烯粉末和步骤1)得到的物料按照重量份数20～80份和20～80份混合均匀；
3)将步骤2)得到的混合物料压制，然后再170-300℃下半融熔烧结10-60min；然后在20-60℃下冷却成型即可。
与现有技术相比，本发明取得的有益效果是：
(1)不掉粉，初始出极少量的黑水(原活性炭粉末滤芯开始使用时会有大量的黑水流出)；
(2)通量大，出水量高(同为10吋的滤芯，活性炭粉末滤芯在的0.2MPa压力下，通量为6.6L/min，总出水量为：8－10吨；活性碳纤维滤芯在同样条件下，通量为：8L/min，出水量为10-12吨)；
(3)吸附效果好：去余氯和杂质效果好(同为10吋的滤芯，活性炭粉末滤芯余氯去除率50％，活性碳纤维制品余氯去除率65—70％)；
(4)质轻
(5)产品强度高(活性炭粉末滤芯：高度1.2m处自由落下，有破碎；活性碳纤维滤芯：高度5m处自由落下，无破碎)。
(6)产品可以做成各种各样的形状。
具体实施方式
下面结合具体实施方式对本发明作进一步描述：
实施例1
一种活性炭纤维烧结滤芯的制备方法，包括以下步骤：
2)将活性炭纤维经去静电和粉碎，处理后粒径为15μm；
3)将40目分子量为150万的聚乙烯和步骤1)和得到的物料按照重量份数20份和20份混合均匀；
4)将步骤2)得到的混合物料压制，然后再170℃下烧结10min；然后在20℃下冷却成型即可。
实施例2
一种活性炭纤维烧结滤芯的制备方法，包括以下步骤：
1)将活性炭纤维经去静电和粉碎，处理后粒径为840μm；
2)将300目分子量为600万的聚乙烯和步骤1)得到的物料按照重量份数60份和80份混合均匀；
3)将步骤2)得到的混合物料压制，然后再300℃下烧结60min；然后在60℃下冷却成型即可。
实施例3
一种活性炭纤维烧结滤芯的制备方法，包括以下步骤：
1)将活性炭纤维经去静电和粉碎，处理后粒径为15μm；
2)将40目分子量为600万的聚乙烯和步骤1)得到的物料按照重量份数80份和20份混合均匀；
3)将步骤2)得到的混合物料压制，然后再300℃下烧结60min；然后在20℃下冷却成型即可。
实施例4
一种活性炭纤维烧结滤芯的制备方法，包括以下步骤：
1)将活性炭纤维经去静电和粉碎，处理后粒径为840μm；
2)将300目分子量为150万的聚乙烯和步骤1)得到的物料按照重量份数20份和80份混合均匀；
3)将步骤2)得到的混合物料压制，然后再300℃下烧结10min；然后在60℃下冷却成型即可。
实施例5
一种活性炭纤维烧结滤芯的制备方法，包括以下步骤：
1)将活性炭纤维经去静电和粉碎，处理后粒径为540μm；
2)将200目分子量为300万的聚乙烯和步骤1)得到的物料按照重量份数50份和40份混合均匀；
3)将步骤2)得到的混合物料压制，然后再200℃下烧结40min；然后在40℃下冷却成型即可。
上述实施例只为说明本发明的技术构思及特点，其目的在于让熟悉此项技术的人士能够了解本发明的内容并据以实施，并不能以此限制本发明的保护范围。凡根据本发明精神实质所作的等效变化或修饰，都应涵盖在本发明的保护范围之内。

Claims (7)

  1. 一种活性炭纤维烧结滤芯，其特征在于，由超高分子量聚乙烯和活性碳纤维混合后，经压制、烧结、冷却成型制得。
  2. 根据权利要求1所述的一种活性炭纤维烧结滤芯，其特征在于，超高分子量聚乙烯：20～80份，活性碳纤维：20-80份。
  3. 根据权利要求2所述的一种活性炭纤维烧结滤芯，其特征在于，所述超高分子量聚乙烯的分子量：150万-600万，粒径：40-300目。
  4. 根据权利要求2所述的一种活性炭纤维烧结滤芯，其特征在于，所述活性炭纤维经去静电和粉碎处理，处理后粒径为15-840μm。
  5. 根据权利要求1-4任一项所述的一种活性炭纤维烧结滤芯，其特征在于，烧结过程的温度170-300℃，时间10-60min。
  6. 根据权利要求1-4任一项所述的一种活性炭纤维烧结滤芯，其特征在于，冷却温度为20-60℃。
  7. 一种活性炭纤维烧结滤芯的制备方法，其特征在于，包括以下步骤：
    1)将活性炭纤维经去静电和粉碎，处理后粒径为15-840μm；
    2)将分子量为150万-600万粒径40-300目的聚乙烯粉末和步骤1)得到的物料按照重量份数20～80份和20～80份混合均匀；
    3)将步骤2)得到的混合物料压制，然后再170-300℃下烧结10-60min；然后在20-60℃下冷却成型即可。
PCT/CN2015/090379 2015-05-05 2015-09-23 一种活性炭纤维烧结滤芯及其制备方法 WO2016176953A1 (zh)

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CN104826397A (zh) * 2015-05-05 2015-08-12 苏州凯虹高分子科技有限公司 一种活性炭纤维烧结滤芯及其制备方法
CN105964053A (zh) * 2016-06-24 2016-09-28 马鞍山市顺达环保设备有限公司 一种锅炉除尘器用净化滤料及其制备方法
CN106215509A (zh) * 2016-08-30 2016-12-14 广州澜泉家用电器有限公司 一种炭纤维复合材料及其应用
CN106904790B (zh) * 2017-03-06 2020-08-25 武汉理工大学 一种雨水资源化的处理装置及方法
CN107262042A (zh) * 2017-06-20 2017-10-20 安徽梦谷纤维材料科技有限公司 一种应用于水质净化的改性玄武岩纤维
CN109260825A (zh) * 2018-10-11 2019-01-25 苏州凯虹高分子科技有限公司 一种混合烧结滤芯及其制备方法
CN109157913A (zh) * 2018-10-19 2019-01-08 中山市洁鼎过滤制品有限公司 一种生产活性炭滤芯的方法以及应用其生产的活性炭芯棒

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