WO1997043213A1 - Particules de silice spongieuse et procede pour leur preparation - Google Patents
Particules de silice spongieuse et procede pour leur preparation Download PDFInfo
- Publication number
- WO1997043213A1 WO1997043213A1 PCT/CN1997/000047 CN9700047W WO9743213A1 WO 1997043213 A1 WO1997043213 A1 WO 1997043213A1 CN 9700047 W CN9700047 W CN 9700047W WO 9743213 A1 WO9743213 A1 WO 9743213A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- silica
- acid
- sponge
- inorganic acid
- sodium silicate
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Ceased
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B33/00—Silicon; Compounds thereof
- C01B33/113—Silicon oxides; Hydrates thereof
- C01B33/12—Silica; Hydrates thereof, e.g. lepidoic silicic acid
Definitions
- the present invention relates to a sponge silica and a preparation method thereof.
- Silica (Si0 2 ) is insoluble in water and acids, has stable chemical properties, high temperature resistance, good electrical insulation properties, and is mostly used for reinforcing fillers.
- the traditional silica production method uses a common precipitation method, in which silicic acid is used Sodium and hydrochloric acid undergo a neutralization reaction at a high temperature, and the spherical silica is obtained by aging, filtration, washing, and drying.
- the silica produced by this method has poor purity, small specific surface area, and large particles, so it cannot be satisfied as, for example, Requirements for reinforcing agents for rubber products.
- Another method for manufacturing silica is the gas phase method, which uses silicon tetrachloride as a raw material, and obtains spherical silica products through thermal cracking combustion decomposition, aggregation, deacidification and other processes.
- Gas phase method Can produce small particles of silica, but strict process requirements, high production costs, and large environmental pollution.
- Another object of the present invention is to provide a method for preparing sponge silica.
- Another object of the present invention is to provide a silicon dioxide with high purity, small particle size, and large specific surface area.
- a sponge-like silica having micropores and irregular shapes.
- a method for preparing sponge-like silica including
- step C> is treated with an inorganic acid, which is added in atomized form to obtain a suspension of silicon dioxide, 0> wash the silica suspension with water,
- Figure 1 shows the sponge-like silica of the present invention (under 1 million times electron microscope).
- Figure 2 shows the spherical silica (under 100,000 times electron microscope) produced by Bayer Company of Germany. Detailed description of the invention
- the present invention prepares a sponge-like silica.
- the silica particles are different from the silica produced by the traditional method. It can be seen from FIG. 1 that under a 1 million times electron microscope, The silica particles of the present invention are sponge-like, and it can be seen from FIG. 2 that the silica particles produced by the conventional method are spherical.
- a sponge-like silica has micropores and is irregular.
- a method for preparing a sponge-like silica includes
- the neutralization reaction is performed at normal temperature and pressure, and the reaction time is about 1.5 to 6 hours.
- the reaction can also be carried out under stirring first, and then left to stand The product to form a silica sol.
- the entire reaction time, including stirring and standing, is about 6-48 hours.
- the ratio of inorganic acid to sodium silicate is about 1.2 ⁇ 2.5: 1 ⁇ 1.5 (volume ratio).
- the generated silica sol is mixed with sodium silicate, and the ratio of the silica sol to sodium silicate is about 1 ⁇ 10: 5-20 (volume ratio), and the mixing is performed at normal temperature and pressure.
- step 8> The mixture obtained in step 8> is treated with an inorganic acid to form a suspension of silica.
- the ratio of the inorganic acid to the mixture is about 15-30: 60-300 (volume ratio).
- the acid treatment is carried out under stirring and atmospheric pressure.
- the processing temperature is about 35 to 100 'C, preferably about 40 to 80'C.
- the inorganic acid is added in the form of atomization, and the acid treatment time is about 40 to 120 minutes.
- the inorganic acid is the same or different.
- the inorganic acid concentration used may be the same or different from the inorganic acid concentration of step A>.
- the wet silica washed with water is dried. Drying can be performed by conventional drying methods, for example, spraying, centrifugation, pressure and other drying methods, preferably spray drying methods.
- the inorganic acid may be hydrochloric acid, sulfuric acid, phosphoric acid, nitric acid, or the like, preferably sulfuric acid.
- the concentration of the inorganic acid is about 5 ° to 60. Be, preferably 15. ⁇ 55. Be.
- the concentration of sodium silicate is about 5 ° ⁇ 40 ° Be.
- the stirring speed is about 15-500 rpm.
- the sponge silica of the present invention has the following indicators after analysis: silica (dry basis) 92 to 98.5% by weight
- the silica prepared by the method of the invention has excellent activity and adsorption rate, good dispersibility, large specific surface area, many internal pores, and has strong affinity with various rubbers.
- the silanol groups on its surface are The rubber has a cross-linking effect during the vulcanization process, and has a prominent reinforcing effect.
- the silica prepared by the method of the present invention is used as a tire reinforcing agent, filler, abrasion resistance agent, anti-aging agent, and can improve the tire Service life 6-8 times. Widely used in cable and wire sheath, optical fiber, paint, ink, paper, plastic, etc.
- sponge-like silica is used as a rubber reinforcing agent.
- Example 7 7 parts by volume of the aqueous solution was processed under normal pressure and stirring, the temperature was controlled at 70 ° C, the processing time was 2.5 hours, the stirring speed was 350 rpm, the obtained silica suspension was washed with 40 times water, and then Spray drying at 500 -C, the product obtained is similar to Example 1.
- the specific surface area of the product is 300m 2 / g, containing 94% of silica, and its original particle size (without mechanical pulverization) is 99% below 10 microns. 60% below 5 microns, 23% below 1 micron, pH value 7.0, iron content 600ppm, moisture content 5%, DBP absorption value 2.0-3.0cm 3 / g.
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Silicon Compounds (AREA)
Priority Applications (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| EP97921583A EP0959041B1 (en) | 1996-05-14 | 1997-05-14 | Method for preparing spongy silica particles |
| DE69727971T DE69727971T2 (de) | 1996-05-14 | 1997-05-14 | Verfahren zu herstellung schwammartiger kieselsäureteilchen |
| AU27618/97A AU725033B2 (en) | 1996-05-14 | 1997-05-14 | Spongy silica particles and method for preparing the same |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN96104972A CN1048956C (zh) | 1996-05-14 | 1996-05-14 | 二次结晶超细白炭黑的制法 |
| CN96104972.3 | 1996-05-14 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| WO1997043213A1 true WO1997043213A1 (fr) | 1997-11-20 |
Family
ID=5118654
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/CN1997/000047 Ceased WO1997043213A1 (fr) | 1996-05-14 | 1997-05-14 | Particules de silice spongieuse et procede pour leur preparation |
Country Status (5)
| Country | Link |
|---|---|
| EP (1) | EP0959041B1 (enExample) |
| CN (1) | CN1048956C (enExample) |
| AU (1) | AU725033B2 (enExample) |
| DE (1) | DE69727971T2 (enExample) |
| WO (1) | WO1997043213A1 (enExample) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| TWI834757B (zh) * | 2018-11-13 | 2024-03-11 | 日商日鐵化學材料股份有限公司 | 半導體密封材用氧化矽球狀粒子 |
Families Citing this family (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1631777B (zh) * | 2004-11-11 | 2010-09-29 | 孙晓珑 | 纳米二氧化硅粉体及其原位颗粒生成制造方法 |
| US20090084035A1 (en) * | 2007-09-28 | 2009-04-02 | General Electric Company | Polygeneration systems |
| CN101830474B (zh) * | 2010-05-17 | 2012-01-11 | 浙江建业化工股份有限公司 | 白炭黑的制备方法 |
| CN102120582B (zh) * | 2011-01-25 | 2014-09-10 | 泉州师范学院 | 搅拌磨法沉淀白炭黑的反应工艺 |
| CN103043610B (zh) * | 2011-10-12 | 2015-06-17 | 北京华宇同方化工科技开发有限公司 | 一种水解法处理四氯化硅的方法和系统 |
| CN104760963A (zh) * | 2015-04-02 | 2015-07-08 | 确成硅化学股份有限公司 | 利用三氧化硫烟气制备二氧化硅的方法 |
| CN106315593A (zh) * | 2016-07-25 | 2017-01-11 | 汪承源 | 一种超微孔纳米SiO2的制法 |
| CN108033453A (zh) * | 2017-12-06 | 2018-05-15 | 安徽凤阳赛吉元无机材料有限公司 | 一种改性沉淀法白炭黑的制备方法 |
| CN111892080B (zh) * | 2020-08-07 | 2022-03-29 | 河南大学 | 一种石墨烯与氧化锡空心球复合纳米材料的制备方法 |
| CN116924421B (zh) * | 2023-07-31 | 2025-09-12 | 福建远翔新材料股份有限公司 | 一种高比表面积中度吸油值的摩擦剂的产生方法 |
| CN117720112B (zh) * | 2023-12-14 | 2024-08-06 | 华沃德源环境技术(济南)有限公司 | 利用制药副产醋酸制备白炭黑联产醋酸钠的方法 |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3857925A (en) * | 1971-07-27 | 1974-12-31 | Canadian Patents Dev | Preparation of reinforcing amorphous silica |
| US3928540A (en) * | 1971-07-26 | 1975-12-23 | Ppg Industries Inc | Process for preparing silica pigment |
| CN1114832A (zh) * | 1993-09-29 | 1996-01-10 | 罗纳·布朗克化学公司 | 沉淀硅石 |
| CN1114833A (zh) * | 1993-09-29 | 1996-01-10 | 罗纳·布朗克化学公司 | 沉淀硅石 |
| CN1128731A (zh) * | 1994-09-26 | 1996-08-14 | 日本制纸株式会社 | 硅酸水合物的制备方法 |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3884776A (en) * | 1973-05-15 | 1975-05-20 | Du Pont | Preparation of hydroquinone |
| JPS5228755A (en) * | 1975-08-29 | 1977-03-03 | Matsushita Electric Ind Co Ltd | Heat exchanger |
| JPS601606A (ja) * | 1983-06-20 | 1985-01-07 | Victor Co Of Japan Ltd | 録音回路 |
| CN1009075B (zh) * | 1985-06-27 | 1990-08-08 | 日东化学工业株式会社 | 高纯度二氧化硅的制备方法 |
-
1996
- 1996-05-14 CN CN96104972A patent/CN1048956C/zh not_active Expired - Lifetime
-
1997
- 1997-05-14 WO PCT/CN1997/000047 patent/WO1997043213A1/zh not_active Ceased
- 1997-05-14 AU AU27618/97A patent/AU725033B2/en not_active Expired
- 1997-05-14 DE DE69727971T patent/DE69727971T2/de not_active Expired - Lifetime
- 1997-05-14 EP EP97921583A patent/EP0959041B1/en not_active Expired - Lifetime
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3928540A (en) * | 1971-07-26 | 1975-12-23 | Ppg Industries Inc | Process for preparing silica pigment |
| US3857925A (en) * | 1971-07-27 | 1974-12-31 | Canadian Patents Dev | Preparation of reinforcing amorphous silica |
| CN1114832A (zh) * | 1993-09-29 | 1996-01-10 | 罗纳·布朗克化学公司 | 沉淀硅石 |
| CN1114833A (zh) * | 1993-09-29 | 1996-01-10 | 罗纳·布朗克化学公司 | 沉淀硅石 |
| CN1128731A (zh) * | 1994-09-26 | 1996-08-14 | 日本制纸株式会社 | 硅酸水合物的制备方法 |
Non-Patent Citations (1)
| Title |
|---|
| See also references of EP0959041A4 * |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| TWI834757B (zh) * | 2018-11-13 | 2024-03-11 | 日商日鐵化學材料股份有限公司 | 半導體密封材用氧化矽球狀粒子 |
Also Published As
| Publication number | Publication date |
|---|---|
| DE69727971D1 (de) | 2004-04-08 |
| CN1165113A (zh) | 1997-11-19 |
| EP0959041A1 (en) | 1999-11-24 |
| AU2761897A (en) | 1997-12-05 |
| AU725033B2 (en) | 2000-10-05 |
| DE69727971T2 (de) | 2005-03-17 |
| EP0959041B1 (en) | 2004-03-03 |
| EP0959041A4 (enExample) | 1999-11-24 |
| CN1048956C (zh) | 2000-02-02 |
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