WO2020244182A1 - 一种梯度pH沉淀法制备高分散二氧化硅的方法 - Google Patents

一种梯度pH沉淀法制备高分散二氧化硅的方法 Download PDF

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WO2020244182A1
WO2020244182A1 PCT/CN2019/122965 CN2019122965W WO2020244182A1 WO 2020244182 A1 WO2020244182 A1 WO 2020244182A1 CN 2019122965 W CN2019122965 W CN 2019122965W WO 2020244182 A1 WO2020244182 A1 WO 2020244182A1
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gradient
value
sodium silicate
mother liquor
silica
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王永庆
毛善兵
于方琪
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确成硅化学股份有限公司
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    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B33/00Silicon; Compounds thereof
    • C01B33/113Silicon oxides; Hydrates thereof
    • C01B33/12Silica; Hydrates thereof, e.g. lepidoic silicic acid
    • C01B33/18Preparation of finely divided silica neither in sol nor in gel form; After-treatment thereof
    • C01B33/187Preparation of finely divided silica neither in sol nor in gel form; After-treatment thereof by acidic treatment of silicates
    • C01B33/193Preparation of finely divided silica neither in sol nor in gel form; After-treatment thereof by acidic treatment of silicates of aqueous solutions of silicates

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  • the invention relates to a method for preparing highly dispersed silica by a gradient pH precipitation method.
  • Silica is an amorphous white powder, non-toxic, odorless, and non-polluting.
  • the surface is rich in hydroxyl groups, with small particle size and uniform particle size distribution. It has a large specific surface area and high pore volume.
  • As an environmentally friendly functional material it is widely used in daily chemicals. Industries such as supplies, medicine, and liquid carriers, especially the tire industry, have become important reinforcing materials for rubber tires.
  • the traditional precipitation method to prepare silica is mainly obtained by reacting and aging water glass, sulfuric acid or hydrochloric acid as raw materials at a certain pH value.
  • an appropriate amount of dispersing aids, surfactants or modifiers can be added to prevent Excessive aggregation of primary particles, such as CN104828832A, CN102229758A, CN108069430A, CN104891505A, CN102976339A, etc.
  • the actual dispersion effect of silica prepared by this method in rubber is not ideal and still needs to be improved.
  • CN108439414A discloses a method for preparing highly dispersed large pore volume precipitated silica by a pH pendulum method.
  • This method uses liquid sodium silicate and dilute sulfuric acid as raw materials, controls the pH value to swing back and forth from 11 ⁇ 1 to 5 ⁇ 1 for a total of 5 times, and then performs filter press washing, spray drying, and material manufacturing to obtain a dispersion/grade up to 9.5-10 high dispersion and large pore volume precipitated silica.
  • the disadvantage of this method is that a large amount of sulfuric acid is consumed when the pH value swings back and forth.
  • the purpose of the present invention is to provide a method for preparing highly dispersed silica by a gradient pH precipitation method with less acid consumption.
  • a method for preparing high-dispersion silica by gradient pH precipitation method includes the following steps:
  • step (2) the mass percentage concentration of the surfactant in the mother liquor is 0.2-2%.
  • the surface active agent is a non-ionic surface active agent.
  • the non-ionic surfactant is octylphenol polyoxyethylene ether, nonylphenol polyoxyethylene ether and/or laureth polyoxyethylene ether.
  • the density of the sodium silicate solution is 1.1 to 1.25 g/cm 3
  • the modulus of sodium silicate is 2 to 4;
  • the acid solution is sulfuric acid with a concentration of 1 to 3 mol/L;
  • the pH value of the system is adjusted in a gradient from 5 to 11 according to the pH value of 5 ⁇ 7 ⁇ 9 ⁇ 11, and the reaction is 5-15 minutes after each adjustment;
  • the gradient adjustment of the pH value of the system from 11 to 5 is performed according to the gradient of pH value 11 ⁇ 9 ⁇ 7 ⁇ 5, and the reaction is 5-15 minutes after each adjustment.
  • a surfactant is added to the reaction system to prevent excessive agglomeration of original particles and make the particle size of the aggregate produced uniform; meanwhile, the purpose of adjusting the silica dispersion level is achieved through the gradient adjustment of pH value.
  • the prepared silica The dispersion grade of the product in rubber>9.7.
  • a method for preparing high-dispersion silica by gradient pH precipitation method includes the following steps:
  • step (2) the mass percentage concentration of the surfactant in the mother liquor is 0.2-2%.
  • the surfactant is a nonionic surfactant.
  • the non-ionic surfactant is octylphenol polyoxyethylene ether, nonylphenol polyoxyethylene ether and/or laureth polyoxyethylene ether.
  • the density of the sodium silicate solution is 1.1 to 1.25 g/cm 3 , and the modulus of the sodium silicate is 2 to 4;
  • the acid solution is sulfuric acid with a concentration of 1 to 3 mol/L;
  • the pH value of the system is adjusted in a gradient from 5 to 11 according to the pH value of 5 ⁇ 7 ⁇ 9 ⁇ 11, and the reaction is 5-15 minutes after each adjustment;
  • the gradient adjustment of the pH value of the system from 11 to 5 is performed according to the gradient of pH value 11 ⁇ 9 ⁇ 7 ⁇ 5, and the reaction is 5-15 minutes after each adjustment.
  • the separation method can be filtration, pressure filtration, centrifugation, sedimentation, etc. In the separation process with washing to remove impurities.
  • the drying method can be spray drying and other conventional drying methods.
  • the present invention prepares vulcanized rubber filled with silica according to HG/T 2404-2008, and evaluates the degree of dispersion of silica in the rubber according to method D of GB/T 6030-2006.
  • a method for preparing high-dispersion silica by gradient pH precipitation method includes the following steps:
  • step (3) Add sodium silicate solution to the mother liquor of step (2), adjust the pH value of the system to 7, after reacting for 10 minutes, continue to add sodium silicate solution to adjust the pH value to 9, after reacting for 10 minutes, continue to add Adjust the pH value of sodium silicate solution to 11 and react for 10 minutes;
  • step (3) Add dilute sulfuric acid to the mother liquor treated in step (3), adjust the pH value of the system to 9, after reacting for 10 minutes, continue to add dilute sulfuric acid to adjust the pH to 7, and after reacting for 10 minutes, continue to add dilute sulfuric acid. Adjust the pH to 5 and react for 10 minutes;
  • Step (4) After the reaction, the mother liquor is filtered and washed with a plate and frame filter, and the obtained silica is spray-dried to obtain high-dispersion silica with a degree of dispersion> 9.7.
  • a method for preparing high-dispersion silica by gradient pH precipitation method includes the following steps:
  • step (3) Add sodium silicate solution to the mother liquor of step (2), adjust the pH value of the system to 7, after reacting for 10 minutes, continue to add sodium silicate solution to adjust the pH value to 9, after reacting for 10 minutes, continue to add Adjust the pH value of sodium silicate solution to 11 and react for 10 minutes;
  • step (3) Add dilute sulfuric acid to the mother liquor treated in step (3), adjust the pH value of the system to 9, after reacting for 10 minutes, continue to add dilute sulfuric acid to adjust the pH to 7, and after reacting for 10 minutes, continue to add dilute sulfuric acid. Adjust the pH to 5 and react for 10 minutes;
  • Step (4) After the reaction, the mother liquor is filtered and washed with a plate and frame filter, and the obtained silica is spray-dried to obtain high-dispersion silica with a degree of dispersion> 9.7.

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Silicon Compounds (AREA)

Abstract

本发明公开了一种梯度pH沉淀法制备高分散二氧化硅的方法,该方法包括以下步骤:(1)配制硅酸钠溶液和酸溶液;(2)向硅酸钠溶液中加入表面活性剂和酸溶液,至体系的pH值为5,得到母液;(3)向母液中加入硅酸钠溶液,将体系的pH值由5梯度调节至11,然后向母液中加入酸溶液,将体系的pH值由11梯度调节至5;(4)母液经分离、干燥,得到高分散二氧化硅。与现有技术相比,依本发明方法所制备的二氧化硅产品在橡胶中的分散等级>9.7,且酸消耗较少。

Description

一种梯度pH沉淀法制备高分散二氧化硅的方法 技术领域
本发明涉及一种梯度pH沉淀法制备高分散二氧化硅的方法。
背景技术
二氧化硅为无定形白色粉末,无毒、无味、无污染,表面富含羟基,粒径小且粒度分布均匀,具有大比表面积和高孔容,作为一种环保功能材料,被广泛用在日化用品与医药以及液体载体等行业,尤其是轮胎行业,已经成为了橡胶轮胎重要的补强材料。传统沉淀法制备二氧化硅主要是以水玻璃、硫酸或盐酸为原料在一定pH值下反应、陈化得到,在该过程中可加入适量的分散助剂、表面活性剂或改性剂以防止原始粒子的过度聚集,如CN104828832A、CN102229758A、CN108069430A、CN104891505A、CN102976339A等,但该方法所制备的二氧化硅在橡胶中的实际分散效果并不太理想,仍有待于提高。
CN108439414A公开了一种pH值摆法制备高分散大孔容沉淀二氧化硅的方法。该方法以液体硅酸钠和稀硫酸为原料,控制pH值从11±1至5±1之间来回摆动共5次,然后进行压滤洗涤、喷雾干燥、造料,得到分散度/级达9.5-10的高分散大孔容沉淀二氧化硅。该方法的不足是pH值来回摆动需要消耗大量的硫酸。
发明内容
根据上述现有技术的不足,本发明的目的在于提供一种酸消耗更少的梯度pH沉淀法制备高分散二氧化硅的方法。
为实现上述目的,本发明采用的技术方案如下:
一种梯度pH沉淀法制备高分散二氧化硅的方法,包括以下步骤:
(1)配制硅酸钠溶液和酸溶液;
(2)向硅酸钠溶液中加入表面活性剂和酸溶液,至体系的pH值为5,得 到母液;
(3)向母液中加入硅酸钠溶液,将体系的pH值由5梯度调节至11,然后向母液中加入酸溶液,将体系的pH值由11梯度调节至5;
(4)母液经分离、干燥,得到高分散二氧化硅。
作为优选技术方案之一,步骤(2)中,所述的表面活性剂在母液中的质量百分比浓度为0.2~2%。
作为更进一步的优选技术方案之一,所述的表面活性剂为非离子型表面活性剂。
作为更进一步的优选技术方案之一,所述的非离子型表面活性剂为辛基酚聚氧乙烯醚、壬基酚聚氧乙烯醚和/或月桂醇聚氧乙烯醚。
作为优选技术方案之一,所述的硅酸钠溶液的密度为1.1~1.25g/cm 3,硅酸钠的模数为2~4;
所述的酸溶液为浓度为1~3mol/L的硫酸;
所述的体系的pH值由5梯度调节至11是按pH值为5→7→9→11的梯度进行调节,每次调节后反应5~15min;
所述的体系的pH值由11梯度调节至5是按pH值为11→9→7→5的梯度进行调节,每次调节后反应5~15min。
本发明在反应体系中加入表面活性剂,防止原始粒子过度聚集,使生产的聚集体粒径均匀;同时通过pH值的梯度调节来达到调控二氧化硅分散等级的目的,所制备的二氧化硅产品在橡胶中的分散等级>9.7。
具体实施方式
下面通过具体实施例对本发明的具体技术方案作进一步地详细说明。
一种梯度pH沉淀法制备高分散二氧化硅的方法,包括以下步骤:
(1)配制硅酸钠溶液和酸溶液;
(2)向硅酸钠溶液中加入表面活性剂和酸溶液,至体系的pH值为5,得到母液;
(3)向母液中加入硅酸钠溶液,将体系的pH值由5梯度调节至11,然后 向母液中加入酸溶液,将体系的pH值由11梯度调节至5;
(4)母液经分离、干燥,得到高分散二氧化硅。
在另一优选的技术方案中,步骤(2)中,所述的表面活性剂在母液中的质量百分比浓度为0.2~2%。
在另一优选的技术方案中,所述的表面活性剂为非离子型表面活性剂。
在另一优选的技术方案中,所述的非离子型表面活性剂为辛基酚聚氧乙烯醚、壬基酚聚氧乙烯醚和/或月桂醇聚氧乙烯醚。
在另一优选的技术方案中,所述的硅酸钠溶液的密度为1.1~1.25g/cm 3,硅酸钠的模数为2~4;
所述的酸溶液为浓度为1~3mol/L的硫酸;
所述的体系的pH值由5梯度调节至11是按pH值为5→7→9→11的梯度进行调节,每次调节后反应5~15min;
所述的体系的pH值由11梯度调节至5是按pH值为11→9→7→5的梯度进行调节,每次调节后反应5~15min。
分离方式可采取过滤、压滤、离心、沉降等。在分离的过程中配合洗涤,以除去杂质。
干燥方式可采取喷雾干燥等常规的干燥方式。
本发明依HG/T 2404-2008制备填充有二氧化硅的硫化橡胶,并依GB/T 6030-2006的方法D评估二氧化硅在橡胶中的分散度等级。
实施例1
一种梯度pH沉淀法制备高分散二氧化硅的方法,包括以下步骤:
(1)将模数为2.5的硅酸钠用水溶解,配制成密度为1.15g/cm 3的硅酸钠溶液,将浓硫酸用水稀释配制成浓度为1mol/L的稀硫酸;
(2)将硅酸钠溶液加热至70℃后,在搅拌下,先向硅酸钠溶液中加入辛基酚聚氧乙烯醚,混匀后,再加入稀硫酸,至体系的pH值为5,反应10min,得到母液,辛基酚聚氧乙烯醚的质量百分比浓度为0.5%;
(3)向步骤(2)的母液中加入硅酸钠溶液,将体系的pH值调节至7,反 应10min后,继续加入硅酸钠溶液将pH值调节至9,反应10min后,再继续加入硅酸钠溶液将pH值调节至11,反应10min;
(4)向经步骤(3)处理的母液中加入稀硫酸,将体系的pH值调节至9,反应10min后,继续加稀硫酸将pH调节至7,反应10min后,再继续加稀硫酸将pH调节至5,反应10min;
(5)步骤(4)反应完毕后的母液用板框过滤机过滤洗涤,得到的二氧化硅喷雾干燥,得到高分散二氧化硅,分散度等级>9.7。
实施例2
一种梯度pH沉淀法制备高分散二氧化硅的方法,包括以下步骤:
(1)将模数为3.5的硅酸钠用水溶解,配制成密度为1.25g/cm 3的硅酸钠溶液,将浓硫酸用水稀释配制成浓度为3mol/L的稀硫酸;
(2)将硅酸钠溶液加热至90℃后,在搅拌下,先向硅酸钠溶液中加入辛基酚聚氧乙烯醚,混匀后,再加入稀硫酸,至体系的pH值为5,反应10min,得到母液,辛基酚聚氧乙烯醚的质量百分比浓度为1%;
(3)向步骤(2)的母液中加入硅酸钠溶液,将体系的pH值调节至7,反应10min后,继续加入硅酸钠溶液将pH值调节至9,反应10min后,再继续加入硅酸钠溶液将pH值调节至11,反应10min;
(4)向经步骤(3)处理的母液中加入稀硫酸,将体系的pH值调节至9,反应10min后,继续加稀硫酸将pH调节至7,反应10min后,再继续加稀硫酸将pH调节至5,反应10min;
(5)步骤(4)反应完毕后的母液用板框过滤机过滤洗涤,得到的二氧化硅喷雾干燥,得到高分散二氧化硅,分散度等级>9.7。
最后应说明的是:以上所述仅为本发明的优选实施例而已,并不用于限制本发明,尽管参照前述实施例对本发明进行了详细的说明,对于本领域的技术人员来说,其依然可以对前述各实施例所记载的技术方案进行修改,或者对其中部分技术特征进行等同替换。凡在本发明的精神和原则之内,所作的任何修改、等同替换、改进等,均应包含在本发明的保护范围之内。

Claims (5)

  1. 一种梯度pH沉淀法制备高分散二氧化硅的方法,包括以下步骤:
    (1)配制硅酸钠溶液和酸溶液;
    (2)向硅酸钠溶液中加入表面活性剂和酸溶液,至体系的pH值为5,得到母液;
    (3)向母液中加入硅酸钠溶液,将体系的pH值由5梯度调节至11,然后向母液中加入酸溶液,将体系的pH值由11梯度调节至5;
    (4)母液经分离、干燥,得到高分散二氧化硅。
  2. 根据权利要求1所述的方法,其特征在于:步骤(2)中,所述的表面活性剂在母液中的质量百分比浓度为0.2~2%。
  3. 根据权利要求2所述的方法,其特征在于:所述的表面活性剂为非离子型表面活性剂。
  4. 根据权利要求3所述的方法,其特征在于:所述的非离子型表面活性剂为辛基酚聚氧乙烯醚、壬基酚聚氧乙烯醚和/或月桂醇聚氧乙烯醚。
  5. 根据权利要求1至4任一所述的方法,其特征在于:
    所述的硅酸钠溶液的密度为1.1~1.25g/cm 3,硅酸钠的模数为2~4;
    所述的酸溶液为浓度为1~3mol/L的硫酸;
    所述的体系的pH值由5梯度调节至11是按pH值为5→7→9→11的梯度进行调节,每次调节后反应5~15min;
    所述的体系的pH值由11梯度调节至5是按pH值为11→9→7→5的梯度进行调节,每次调节后反应5~15min。
PCT/CN2019/122965 2019-06-05 2019-12-04 一种梯度pH沉淀法制备高分散二氧化硅的方法 WO2020244182A1 (zh)

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Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104058415A (zh) * 2014-04-29 2014-09-24 清华大学 高分散纳米二氧化硅的制备方法
CN108383130A (zh) * 2018-05-04 2018-08-10 福建远翔新材料股份有限公司 一种沉淀水合二氧化硅的合成方法
CN108439414A (zh) * 2018-02-11 2018-08-24 确成硅化学股份有限公司 一种pH值摆动法制备高分散大孔容沉淀二氧化硅的方法
CN110127709A (zh) * 2019-06-05 2019-08-16 确成硅化学股份有限公司 一种梯度pH沉淀法制备高分散二氧化硅的方法

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105000567B (zh) * 2015-07-30 2017-03-29 西南石油大学 一种高分散纳米二氧化硅的制备方法

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104058415A (zh) * 2014-04-29 2014-09-24 清华大学 高分散纳米二氧化硅的制备方法
CN108439414A (zh) * 2018-02-11 2018-08-24 确成硅化学股份有限公司 一种pH值摆动法制备高分散大孔容沉淀二氧化硅的方法
CN108383130A (zh) * 2018-05-04 2018-08-10 福建远翔新材料股份有限公司 一种沉淀水合二氧化硅的合成方法
CN110127709A (zh) * 2019-06-05 2019-08-16 确成硅化学股份有限公司 一种梯度pH沉淀法制备高分散二氧化硅的方法

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114286800A (zh) * 2021-12-01 2022-04-05 无锡恒诚硅业有限公司 一种疏水白炭黑橡胶补强剂及其制备方法与应用
WO2023097549A1 (zh) * 2021-12-01 2023-06-08 无锡恒诚硅业有限公司 一种疏水白炭黑橡胶补强剂及其制备方法与应用

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