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CN102167386A - Method for preparing barium sulfate nanoparticles - Google Patents

Method for preparing barium sulfate nanoparticles Download PDF

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CN102167386A
CN102167386A CN 201110063603 CN201110063603A CN102167386A CN 102167386 A CN102167386 A CN 102167386A CN 201110063603 CN201110063603 CN 201110063603 CN 201110063603 A CN201110063603 A CN 201110063603A CN 102167386 A CN102167386 A CN 102167386A
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sodium sulfate
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barium
barium sulfide
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CN102167386B (en
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骆广生
杜乐
吕阳成
王玉军
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Tsinghua University
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Abstract

本发明公开了属于化工材料制备技术领域的一种制备硫酸钡纳米颗粒的方法,将硫酸钠溶液通过微孔,从垂直方向分散到流动的硫化钡溶液或循环流动的硫化钡悬浊液中,硫酸钠溶液被错流剪切,混合反应,生成硫酸钡沉淀,反应产物经熟化、固液分离、水洗除杂、干燥、粉碎,制得硫酸钡纳米颗粒。利用本发明的方法制备硫酸钡纳米颗粒,原料成本低,生产能力大,操作过程简便,重复性和稳定性好,使传统的芒硝-黑灰法可以进入纳米级硫酸钡颗粒的生产序列。采用此方法可得到平均粒径在35~48nm的硫酸钡纳米颗粒。The invention discloses a method for preparing barium sulfate nanoparticles, which belongs to the technical field of chemical material preparation. The sodium sulfate solution is dispersed into a flowing barium sulfide solution or a circulating barium sulfide suspension from a vertical direction through micropores. The sodium sulfate solution is sheared by cross-flow, mixed and reacted to form barium sulfate precipitates, and the reaction product is matured, separated from solid and liquid, washed with water to remove impurities, dried and pulverized to obtain barium sulfate nanoparticles. Using the method of the invention to prepare barium sulfate nanoparticles has low raw material cost, large production capacity, simple operation process, good repeatability and stability, so that the traditional mirabilite-black ash method can enter the production sequence of nanoscale barium sulfate particles. The method can be used to obtain barium sulfate nanoparticles with an average particle size of 35-48nm.

Description

一种制备硫酸钡纳米颗粒的方法A method for preparing barium sulfate nanoparticles

技术领域technical field

本发明属于化工材料制备技术领域,特别涉及一种制备硫酸钡纳米颗粒的方法,具体地说,涉及一种利用液相错流剪切的微孔分散法制备硫酸钡纳米颗粒的方法。The invention belongs to the technical field of chemical material preparation, and in particular relates to a method for preparing barium sulfate nanoparticles, in particular to a method for preparing barium sulfate nanoparticles by a micropore dispersion method utilizing liquid phase cross-flow shearing.

背景技术Background technique

硫酸钡纳米颗粒具有小尺寸效应和良好的化学稳定性,广泛应用于涂料、塑料、油漆的填充材料和添加剂等领域。目前常用的硫酸钡纳米颗粒制备方法主要有:(1)芒硝-黑灰法-以硫化钠、钡卤水和硫酸钠为原料,首先得到硫化钡溶液或浆料,之后与硫酸钠溶液混合,发生化学反应,之后调节pH值到反应终点,得到硫酸钡浆料,并最终得到产品;(2)络合-沉淀法-以BaCl2和EDTA溶液为原料,将二者混合配制Ba2+-EDTA的络合体系,调节络合体系达到一定的pH值和温度;然后将预先配制好的Na2SO4溶液加入络合体系中反应,反应产物经离心分离、洗涤、干燥,即得纳米硫酸钡产品。这些方法或者引入其它反应组分,使后续分离难度加大;或者制备所得颗粒的粒度偏大、分布较宽、单分散性不佳,如芒硝-黑灰法,该工艺产品现有粒径很难达到纳米级。产生这种情况的原因在于物料微观混合差,传递过程慢,直接沉淀时成核量小、成核不均匀,并直接影响了颗粒的品质。Barium sulfate nanoparticles have small size effect and good chemical stability, and are widely used in coatings, plastics, filling materials and additives for paints and other fields. The preparation methods of barium sulfate nanoparticles commonly used at present mainly contain: (1) Glauber's salt-black ash method-using sodium sulfide, barium brine and sodium sulfate as raw materials, first obtain barium sulfide solution or slurry, mix with sodium sulfate solution afterwards, produce Chemical reaction, and then adjust the pH value to the end of the reaction to obtain barium sulfate slurry, and finally obtain the product; (2) Complexation-precipitation method-BaCl 2 and EDTA solution are used as raw materials, and the two are mixed to prepare Ba 2+ -EDTA The complexation system, adjust the complexation system to reach a certain pH value and temperature; then add the pre-prepared Na 2 SO 4 solution into the complexation system for reaction, and the reaction product is centrifuged, washed, and dried to obtain nano barium sulfate product. These methods either introduce other reaction components, which increases the difficulty of subsequent separation; or the particle size of the prepared particles is too large, the distribution is wide, and the monodispersity is not good, such as the Glauber's salt-black ash method, the existing particle size of the product of this process is very large Difficult to reach the nanoscale. The reason for this situation is that the microscopic mixing of materials is poor, the transfer process is slow, and the nucleation amount is small and uneven during direct precipitation, which directly affects the quality of the particles.

另一方面,利用流体剪切的微孔分散对于均相和非均相混合都有很好的性能,体系传热传质效率高,有助于解决快速反应因传递限制而可控性差的问题,为直接沉淀法在制备硫酸钡纳米颗粒方面取得突破创造了条件。On the other hand, the micropore dispersion using fluid shear has good performance for both homogeneous and heterogeneous mixing, and the system has high heat and mass transfer efficiency, which helps to solve the problem of poor controllability of rapid reactions due to transfer limitations , which created conditions for a breakthrough in the preparation of barium sulfate nanoparticles by the direct precipitation method.

发明内容Contents of the invention

本发明旨在提出一种新的制备硫酸钡纳米颗粒的方法。其原理在于:本发明中所选体系发生的是液相沉淀反应,反应速度快,传递过程为制备过程中的控制步骤;对于此体系,利用流体剪切的微孔分散加快了传递的进行,使体系中有较高的过饱和度,同时保证了混合的均匀性,从而制备得到颗粒小且分布均匀的硫酸钡纳米颗粒。The present invention aims to propose a new method for preparing barium sulfate nanoparticles. Its principle is: what take place in the selected system of the present invention is liquid phase precipitation reaction, and reaction speed is fast, and transfer process is the control step in the preparation process; The system has a higher degree of supersaturation while ensuring the uniformity of mixing, thereby preparing barium sulfate nanoparticles with small particles and uniform distribution.

一种制备硫酸钡纳米颗粒的方法,将硫酸钠溶液从垂直方向通过微孔分散到流动的硫化钡溶液或循环流动的硫化钡悬浊液中,硫酸钠溶液被错流剪切,混合反应,生成硫酸钡沉淀,反应产物经熟化、固液分离、水洗除杂、干燥、粉碎,制得硫酸钡纳米颗粒。A method for preparing barium sulfate nanoparticles, the sodium sulfate solution is dispersed into the flowing barium sulfide solution or the circulating barium sulfide suspension from the vertical direction through the micropores, the sodium sulfate solution is sheared by cross-flow, mixed reaction, A barium sulfate precipitate is generated, and the reaction product is matured, separated from solid and liquid, washed with water to remove impurities, dried and pulverized to obtain barium sulfate nanoparticles.

所述硫化钡溶液或悬浊液的温度为10~70℃,所述硫酸钠溶液的温度为10~70℃.The temperature of the barium sulfide solution or suspension is 10-70°C, and the temperature of the sodium sulfate solution is 10-70°C.

所述硫化钡溶液或悬浊液的浓度为0.25~2.5mol/L,所述硫酸钠溶液的浓度为5~45wt%。The barium sulfide solution or suspension has a concentration of 0.25-2.5 mol/L, and the sodium sulfate solution has a concentration of 5-45 wt%.

所述微孔当量直径为0.2~1000微米。The equivalent diameter of the micropores is 0.2-1000 microns.

硫化钡溶液或悬浊液的流速为0.2~3m/s,硫酸钠溶液的流速为0.1~5m/s。The flow velocity of the barium sulfide solution or suspension is 0.2-3m/s, and the flow velocity of the sodium sulfate solution is 0.1-5m/s.

具体来说,本发明所述方法包括如下步骤:Specifically, the method of the present invention includes the following steps:

(1)配制硫化钡溶液或硫化钡悬浊液;(1) prepare barium sulfide solution or barium sulfide suspension;

(2)配制硫酸钠溶液;(2) prepare sodium sulfate solution;

(3)在压力作用下,使硫酸钠溶液从垂直方向通过微孔分散到流动的硫化钡溶液或循环流动的硫化钡悬浊液中,硫酸钠溶液被错流剪切,混合反应;(3) Under pressure, sodium sulfate solution is dispersed into flowing barium sulfide solution or circulating barium sulfide suspension from vertical direction through micropores, sodium sulfate solution is sheared by cross flow, mixed reaction;

(4)反应产物经熟化、固液分离、水洗除杂、干燥、粉碎(按工业标准粉碎,即45μm筛余物含量≤0.5%),得到最终的硫酸钡纳米颗粒。(4) The reaction product is ripened, separated from solid and liquid, washed with water to remove impurities, dried, and pulverized (crushed according to industrial standards, that is, 45 μm sieve residue content≤0.5%) to obtain the final barium sulfate nanoparticles.

步骤(3)中,随硫酸钠溶液带入的硫酸钠的摩尔流率和随硫化钡溶液带入的硫化钡的摩尔流率相等。In step (3), the molar flow rate of the sodium sulfate brought in with the sodium sulfate solution is equal to the molar flow rate of the barium sulfide brought in with the barium sulfide solution.

步骤(3)中,硫化钡悬浊液不断循环,直至随硫酸钠溶液带入的硫酸钠的摩尔量与硫化钡悬浊液中初始的硫化钡摩尔量相等。In step (3), the barium sulfide suspension is continuously circulated until the molar weight of the sodium sulfate brought in with the sodium sulfate solution is equal to the initial barium sulfide molar weight in the barium sulfide suspension.

本发明的有益效果为:利用本发明的方法制备硫酸钡纳米颗粒,原料成本低,生产能力大,操作过程简便,重复性和稳定性好,使传统的芒硝-黑灰法可以进入纳米级硫酸钡颗粒的生产序列。采用此方法可得到平均粒径在35~48nm的硫酸钡纳米颗粒。The beneficial effect of the present invention is: utilize the method of the present invention to prepare barium sulfate nano particle, raw material cost is low, production capacity is big, operation process is simple and easy, repeatability and stability are good, make traditional Glauber's salt-black ash method can enter nanoscale sulfuric acid Production sequence of barium pellets. The method can be used to obtain barium sulfate nanoparticles with an average particle size of 35-48nm.

具体实施方式Detailed ways

下面的实施例可以使本专业技术人员更全面的理解本发明,但不以任何方式限制本发明。The following examples can enable those skilled in the art to understand the present invention more comprehensively, but do not limit the present invention in any way.

实施例1:Example 1:

在70℃下,配制1000mL摩尔浓度为2.5mol/L的硫化钡悬浊液,和800g质量分数为45%的硫酸钠溶液。在压差的作用下,硫酸钠溶液以0.5m/s的流速穿过当量直径为200微米的微孔与作错流循环流动、流速为1m/s的硫化钡悬浊液混合,反应生成硫酸钡沉淀,循环反应至化学配比。产物经熟化、固液分离、水洗除杂、干燥、粉碎,得到最终的硫酸钡颗粒,其平均粒径为48nm。At 70°C, prepare 1000 mL of a barium sulfide suspension with a molar concentration of 2.5 mol/L and 800 g of a 45% sodium sulfate solution. Under the action of pressure difference, the sodium sulfate solution passes through micropores with an equivalent diameter of 200 microns at a flow rate of 0.5m/s and mixes with the barium sulfide suspension flowing in a cross-flow cycle with a flow rate of 1m/s to generate sulfuric acid. Barium is precipitated, and the reaction is cycled to the stoichiometric ratio. The product is matured, separated from solid and liquid, washed with water to remove impurities, dried and pulverized to obtain final barium sulfate particles with an average particle diameter of 48nm.

实施例2:Example 2:

在50℃下,配制1000mL摩尔浓度为1.5mol/L的硫化钡溶液,和720g质量分数为30%的硫酸钠溶液。在压差的作用下,硫酸钠溶液以5m/s的流速穿过当量直径为200微米的微孔与作错流流动、流速为3m/s的硫化钡溶液混合,反应生成硫酸钡沉淀。产物经熟化、固液分离、水洗除杂、干燥、粉碎,得到最终的硫酸钡颗粒,其平均粒径为43nm。At 50°C, prepare 1000 mL of barium sulfide solution with a molar concentration of 1.5 mol/L and 720 g of a 30% sodium sulfate solution. Under the action of pressure difference, the sodium sulfate solution passes through the micropores with an equivalent diameter of 200 microns at a flow rate of 5 m/s and mixes with the barium sulfide solution that flows in a cross flow with a flow rate of 3 m/s, and reacts to form barium sulfate precipitates. The product is matured, separated from solid and liquid, washed with water to remove impurities, dried and pulverized to obtain final barium sulfate particles with an average particle diameter of 43nm.

实施例3:Example 3:

在20℃下,配制1000mL摩尔浓度为0.5mol/L的硫化钡悬浊液,和720g质量分数为10%的硫酸钠溶液。在压差的作用下,硫酸钠溶液以0.1m/s的流速穿过当量直径为600微米的微孔与作错流循环流动、流速为0.3m/s的硫化钡悬浊液混合,反应生成硫酸钡沉淀,循环反应至化学配比。产物经熟化、固液分离、水洗除杂、干燥、粉碎,得到最终的硫酸钡颗粒,其平均粒径为40nm。At 20°C, prepare 1000 mL of a barium sulfide suspension with a molar concentration of 0.5 mol/L and 720 g of a 10% sodium sulfate solution. Under the action of pressure difference, the sodium sulfate solution passes through micropores with an equivalent diameter of 600 microns at a flow rate of 0.1 m/s and mixes with barium sulfide suspension with a flow rate of 0.3 m/s for cross-flow circulation, and the reaction forms Barium sulfate is precipitated, and the reaction is cycled to the stoichiometric ratio. The product is matured, separated from solid and liquid, washed with water to remove impurities, dried and pulverized to obtain final barium sulfate particles with an average particle diameter of 40nm.

实施例4:Example 4:

在10℃下,配制1000mL摩尔浓度为0.25mol/L的硫化钡溶液,和720g质量分数为5%的硫酸钠溶液。在压差的作用下,硫酸钠溶液以0.2m/s的流速穿过当量直径为0.2微米的微孔与作错流流动、流速为0.2m/s的硫化钡溶液混合,反应生成硫酸钡沉淀。产物经熟化、固液分离、水洗除杂、干燥、粉碎,得到最终的硫酸钡颗粒,其平均粒径为35nm。At 10°C, prepare 1000 mL of a barium sulfide solution with a molar concentration of 0.25 mol/L and 720 g of a 5% sodium sulfate solution. Under the action of pressure difference, the sodium sulfate solution passes through micropores with an equivalent diameter of 0.2 microns at a flow rate of 0.2 m/s and mixes with the barium sulfide solution that flows in a cross-flow with a flow rate of 0.2 m/s, and reacts to form barium sulfate precipitates . The product is matured, separated from solid and liquid, washed with water to remove impurities, dried and pulverized to obtain final barium sulfate particles with an average particle diameter of 35nm.

实施例5:Example 5:

在40℃下,配制1000mL摩尔浓度为1.0mol/L的硫化钡溶液,和720g质量分数为20%的硫酸钠溶液。在压差的作用下,硫酸钠溶液以0.5m/s的流速穿过当量直径为200微米的微孔与作错流流动、流速为1m/s的硫化钡溶液混合,反应生成硫酸钡沉淀。产物经熟化、固液分离、水洗除杂、干燥、粉碎,得到最终的硫酸钡颗粒,其平均粒径为37nm。At 40°C, prepare 1000 mL of barium sulfide solution with a molar concentration of 1.0 mol/L and 720 g of a 20% sodium sulfate solution. Under the action of pressure difference, the sodium sulfate solution passes through micropores with an equivalent diameter of 200 microns at a flow rate of 0.5m/s and mixes with the barium sulfide solution with a flow rate of 1m/s as a cross-flow flow, and reacts to form barium sulfate precipitates. The product is matured, separated from solid and liquid, washed with water to remove impurities, dried and pulverized to obtain final barium sulfate particles with an average particle diameter of 37nm.

以上所述,仅为本发明较佳的具体实施方式,但本发明的保护范围并不局限于此,任何熟悉本技术领域的技术人员在本发明揭露的技术范围内,可轻易想到的变化或替换,都应涵盖在本发明的保护范围之内。因此,本发明的保护范围应该以权利要求的保护范围为准。The above is only a preferred embodiment of the present invention, but the scope of protection of the present invention is not limited thereto. Any person skilled in the art within the technical scope disclosed in the present invention can easily think of changes or Replacement should be covered within the protection scope of the present invention. Therefore, the protection scope of the present invention should be determined by the protection scope of the claims.

Claims (9)

1.一种制备硫酸钡纳米颗粒的方法,其特征在于:将硫酸钠溶液从垂直方向通过微孔分散到流动的硫化钡溶液或循环流动的硫化钡悬浊液中,硫酸钠溶液被错流剪切,混合反应,生成硫酸钡沉淀,反应产物经后处理,制得硫酸钡纳米颗粒。1. A method for preparing barium sulfate nanoparticles is characterized in that: sodium sulfate solution is dispersed into flowing barium sulfide solution or the barium sulfide suspension of circulating flow through micropore from vertical direction, and sodium sulfate solution is cross-flowed Shearing and mixing reactions generate barium sulfate precipitation, and the reaction product is post-processed to prepare barium sulfate nanoparticles. 2.根据权利要求1所述的方法,其特征在于:所述后处理包括如下步骤:熟化、固液分离、水洗除杂、干燥、粉碎。2. The method according to claim 1, characterized in that: the post-treatment comprises the following steps: ripening, solid-liquid separation, washing to remove impurities, drying, and crushing. 3.根据权利要求1所述的方法,其特征在于:所述硫化钡溶液或悬浊液的温度为10~70℃,所述硫酸钠溶液的温度为10~70℃。3. The method according to claim 1, characterized in that: the temperature of the barium sulfide solution or suspension is 10-70°C, and the temperature of the sodium sulfate solution is 10-70°C. 4.根据权利要求1所述的方法,其特征在于:所述硫化钡溶液或悬浊液的浓度为0.25~2.5mol/L,所述硫酸钠溶液的浓度为5~45wt%。4. The method according to claim 1, characterized in that: the concentration of the barium sulfide solution or suspension is 0.25 to 2.5 mol/L, and the concentration of the sodium sulfate solution is 5 to 45 wt%. 5.根据权利要求1所述的方法,其特征在于:所述微孔当量直径为0.2~1000微米。5. The method according to claim 1, characterized in that: the equivalent diameter of the micropores is 0.2-1000 microns. 6.根据权利要求1所述的方法,其特征在于:硫化钡溶液或悬浊液的流速为0.2~3m/s,硫酸钠溶液的流速为0.1~5m/s。6. The method according to claim 1, characterized in that: the flow velocity of the barium sulfide solution or suspension is 0.2 to 3 m/s, and the flow velocity of the sodium sulfate solution is 0.1 to 5 m/s. 7.根据权利要求1所述的方法,其特征在于包括如下步骤:7. The method according to claim 1, characterized in that comprising the steps of: (1)配制硫化钡溶液或硫化钡悬浊液;(1) prepare barium sulfide solution or barium sulfide suspension; (2)配制硫酸钠溶液;(2) prepare sodium sulfate solution; (3)在压力作用下,使硫酸钠溶液从垂直方向通过微孔分散到流动的硫化钡溶液或循环流动的硫化钡悬浊液中,硫酸钠溶液被错流剪切,混合反应;(3) Under pressure, sodium sulfate solution is dispersed into flowing barium sulfide solution or circulating barium sulfide suspension from vertical direction through micropores, sodium sulfate solution is sheared by cross flow, mixed reaction; (4)反应产物经熟化、固液分离、水洗除杂、干燥、粉碎,得到硫酸钡纳米颗粒。(4) The reaction product is matured, separated from solid and liquid, washed with water to remove impurities, dried and pulverized to obtain barium sulfate nanoparticles. 8.根据权利要求7所述的方法,其特征在于:步骤(3)中,随硫酸钠溶液带入的硫酸钠的摩尔流率和随硫化钡溶液带入的硫化钡的摩尔流率相等。8. The method according to claim 7, characterized in that: in step (3), the molar flow rate of the sodium sulfate brought in with the sodium sulfate solution is equal to the molar flow rate of the barium sulfide brought in with the barium sulfide solution. 9.根据权利要求7所述的方法,其特征在于:步骤(3)中,硫化钡悬浊液不断循环,直至随硫酸钠溶液带入的硫酸钠的摩尔量与硫化钡悬浊液中初始的硫化钡摩尔量相等。9. method according to claim 7, it is characterized in that: in step (3), barium sulfide suspension is constantly circulated, until the molar weight of the sodium sulfate that brings into with sodium sulfate solution is the same as the initial value in barium sulfide suspension. The molar amount of barium sulfide is equal.
CN 201110063603 2011-03-16 2011-03-16 Method for preparing barium sulfate nanoparticles Expired - Fee Related CN102167386B (en)

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Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103130260A (en) * 2013-03-19 2013-06-05 冉金友 Production method of barium sulfate
CN104512923A (en) * 2013-09-30 2015-04-15 上海梅山钢铁股份有限公司 Preparation method of nano-barium sulfate
CN106241850A (en) * 2016-07-12 2016-12-21 重庆工商大学 The preparation method and applications of insoluble sulfur hydrochlorate photocatalyst
CN106745152A (en) * 2015-11-25 2017-05-31 宜宾丝丽雅股份有限公司 Method for preparing nano barium sulfate and co-producing sodium chloride
CN111285389A (en) * 2018-12-06 2020-06-16 南风化工集团股份有限公司 Production method of superfine precipitated barium sulfate
CN111362293A (en) * 2020-04-03 2020-07-03 河北化工医药职业技术学院 Preparation method of spindle-shaped barium sulfate and spindle-shaped barium sulfate
CN111533153A (en) * 2020-04-20 2020-08-14 中国日用化学研究院有限公司 Preparation method of nano barium sulfate powder
CN116375075A (en) * 2023-04-20 2023-07-04 广西联壮科技股份有限公司 Continuous modification preparation method of barium sulfate powder
CN116588964A (en) * 2023-04-17 2023-08-15 贵州红星发展股份有限公司 Barium sulfate and preparation method thereof

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1377831A (en) * 2001-04-03 2002-11-06 黄榕 Process for preparing super fine deposited barium sulphate
CN1398789A (en) * 2002-08-13 2003-02-26 华北工学院 Prepn of nano barium sulfate
CN101423239A (en) * 2008-11-21 2009-05-06 北京化工大学 Method for preparing nano barium sulfate with controllable particle size distribution
CN101580262A (en) * 2009-04-08 2009-11-18 王嘉兴 Method for preparing nano barium sulfate series products by using barium slag
CN101798090A (en) * 2010-04-07 2010-08-11 清华大学 Method for preparing nanometer silicon dioxide
CN101811685A (en) * 2010-04-07 2010-08-25 清华大学 Method for preparing beta-calcium phosphate or hydroxyapatite nanoparticles
CN101823752A (en) * 2009-04-13 2010-09-08 王嘉兴 Method for preparing nano barium sulfate and co-producing hydrochloric acid by using barium chloride

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1377831A (en) * 2001-04-03 2002-11-06 黄榕 Process for preparing super fine deposited barium sulphate
CN1398789A (en) * 2002-08-13 2003-02-26 华北工学院 Prepn of nano barium sulfate
CN101423239A (en) * 2008-11-21 2009-05-06 北京化工大学 Method for preparing nano barium sulfate with controllable particle size distribution
CN101580262A (en) * 2009-04-08 2009-11-18 王嘉兴 Method for preparing nano barium sulfate series products by using barium slag
CN101823752A (en) * 2009-04-13 2010-09-08 王嘉兴 Method for preparing nano barium sulfate and co-producing hydrochloric acid by using barium chloride
CN101798090A (en) * 2010-04-07 2010-08-11 清华大学 Method for preparing nanometer silicon dioxide
CN101811685A (en) * 2010-04-07 2010-08-25 清华大学 Method for preparing beta-calcium phosphate or hydroxyapatite nanoparticles

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103130260A (en) * 2013-03-19 2013-06-05 冉金友 Production method of barium sulfate
CN103130260B (en) * 2013-03-19 2014-11-19 冉金友 A kind of production method of barium sulfate
CN104512923A (en) * 2013-09-30 2015-04-15 上海梅山钢铁股份有限公司 Preparation method of nano-barium sulfate
CN106745152A (en) * 2015-11-25 2017-05-31 宜宾丝丽雅股份有限公司 Method for preparing nano barium sulfate and co-producing sodium chloride
CN106241850A (en) * 2016-07-12 2016-12-21 重庆工商大学 The preparation method and applications of insoluble sulfur hydrochlorate photocatalyst
CN106241850B (en) * 2016-07-12 2018-01-02 重庆工商大学 The preparation method and applications of insoluble sulfur hydrochlorate photochemical catalyst
CN111285389A (en) * 2018-12-06 2020-06-16 南风化工集团股份有限公司 Production method of superfine precipitated barium sulfate
CN111362293A (en) * 2020-04-03 2020-07-03 河北化工医药职业技术学院 Preparation method of spindle-shaped barium sulfate and spindle-shaped barium sulfate
CN111533153A (en) * 2020-04-20 2020-08-14 中国日用化学研究院有限公司 Preparation method of nano barium sulfate powder
CN116588964A (en) * 2023-04-17 2023-08-15 贵州红星发展股份有限公司 Barium sulfate and preparation method thereof
CN116375075A (en) * 2023-04-20 2023-07-04 广西联壮科技股份有限公司 Continuous modification preparation method of barium sulfate powder

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