CN105038329B - A kind of mashing process for dispersing of titanium dioxide - Google Patents

A kind of mashing process for dispersing of titanium dioxide Download PDF

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CN105038329B
CN105038329B CN201510426705.4A CN201510426705A CN105038329B CN 105038329 B CN105038329 B CN 105038329B CN 201510426705 A CN201510426705 A CN 201510426705A CN 105038329 B CN105038329 B CN 105038329B
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titanium dioxide
mashing
dispersing
slurry
dispersant
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CN105038329A (en
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肖勇丽
景建林
廖荣华
袁秀香
郭菊仙
刘佳
周俊
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Chongqing Titanium Industry Co Ltd of Pangang Group
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Titanium Industry Co Ltd of Pangang Group
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Abstract

The invention belongs to chemical field, it is related to a kind of mashing process for dispersing of titanium dioxide, the mashing process for dispersing for the high-concentration titanium dioxide slurry being specifically related to before titanium dioxide first product wet-milling.It is an object of the invention to provide the mashing process for dispersing can solve the problems such as existing beating process slurry concentration is low, slurry dispersion stabilization is poor, viscosity is big, environmental pollution is big, improve yield and quality, reduction unit cost and energy consumption.Present invention mashing process for dispersing comprises the following steps:(1) processing mashing dispersant:Dispersant is added water and is beaten in the beating equipment with agitating device, and mashing dispersant addition is the 0.1~0.5% of content of titanium dioxide;(2) slurry concentration is controlled:Titanium dioxide first product is added into beating equipment, it is 600~1200g/L to add water and control slurry concentration;(3) dispersed paste:Slurry obtained by step (2) is scattered 30~60 minutes, produce and be beaten scattered titania slurry.

Description

A kind of mashing process for dispersing of titanium dioxide
Technical field
The invention belongs to chemical field, it is related to a kind of mashing process for dispersing of titanium dioxide, is specifically related to titanium dioxide Mashing process for dispersing before first product wet-milling, even more the mashing process for dispersing for high-concentration titanium dioxide slurry.
Background technology
Titanium dioxide is commonly called as titanium dioxide, is a kind of important Chinese white, white with traditional white lead, zinc white, lithopone etc. Color pigment is compared, and it is a variety of excellent that titanium dioxide has that refractive index is high, reducing power is strong, covering power is big, good dispersion, whiteness are good, nontoxic etc. Different in nature energy, is referred to as the king of Chinese white, is widely used in the industries such as coating, plastics, ink, papermaking, chemical fibre, ceramics.
But, the crude product that either sulfuric acid process or chloridising are produced, although purity is very high cannot function as white face Material is used, it is necessary to carry out surface modification by post processing.The post processing of titanium dioxide includes:Mashing is scattered, wet-milling, at inorganic surfaces The processes such as reason, washing, dry, organic surface treatment, vapour powder and packaging.Due to titanium dioxide Ti-O bond lengths from small and Long, this uneven so that titania molecule polarity is very strong, easy to reunite, dispersion stabilization is poor in pulping process, slurry viscosity Height, poor fluidity, it is impossible to be smoothly pumped into wet-milling process, can also influence the quality of wet-milling and inorganic surface treatment, and slurry is dense Degree is higher, and the dispersion stabilization of slurry is poorer, and viscosity is higher, and mobility is poorer, and the influence to subsequent handling is bigger.Therefore, titanium The selection of white powder manufacturer is beaten under low concentration, i.e., content of titanium dioxide is less than 600g/L, and is added when mashing is scattered It is beaten dispersant.But there is following defect in above-mentioned processing mode:
1) mashing can influence yield, unit cost increase, and the efficiency of influence wet-milling under low concentration, increase wet-milling and set Standby loss and energy consumption.
2) addition mashing dispersant and acid or alkali regulation slurry pH value, at present conventional mashing point in pulping process are needed Powder be alcamines and phosphoric acid salt, or alcamines and phosphoric acid salt compound, but this two class mashing dispersant contain respectively Nitrogen and phosphorus, are unfavorable for environmental protection.
The present invention is intended to provide a kind of mashing process for dispersing of high-concentration titanium dioxide slurry, will can be beaten using this method mashing Slurry concentration brings up to 600~1200g/L, and obtained Titanium dioxide slurry has good dispersion stabilization, and slurry viscosity is low, and The mashing dispersant is not nitrogenous and phosphorus, environmentally safe, it is not required that addition acid or alkali regulation slurry pH value.
The content of the invention
It is an object of the invention to provide a kind of mashing of the high-concentration titanium dioxide slurry before titanium dioxide first product wet-milling Process for dispersing, is asked with solving that existing beating process slurry concentration is low, slurry dispersion stabilization is poor, viscosity is big, environmental pollution is big etc. Topic, improves yield and quality, reduction unit cost and energy consumption.
To reach above-mentioned purpose, the invention provides a kind of mashing process for dispersing of new titania slurry, especially Applied to the high-concentration titanium dioxide slurry before titanium dioxide first product wet-milling, it the described method comprises the following steps:
(1) processing mashing dispersant:Dispersant is added water and be beaten in the beating equipment with agitating device, is beaten dispersant Addition is the 0.1~0.5% of content of titanium dioxide;
(2) slurry concentration is controlled:Into beating equipment add titanium dioxide first product, add water control slurry concentration be 600~ 1200g/L;
(3) dispersed paste:Slurry obtained by step (2) is scattered 30~60 minutes, produce and be beaten scattered titanium dioxide Slurry.
Wherein, step (1) beating equipment with agitating device is mashing tank.
Wherein, step (1) and step (2) described water are deionized water or distilled water.
Wherein, the compound that dispersant is polycarboxylate and silicate is beaten described in step (1), it is preferred that described poly- Carboxylate is polycarboxylic acids sodium, and the silicate is sodium metasilicate.
Wherein, the compound proportion of polycarboxylate and silicate is by weight:Polycarboxylate:Silicate=9:1~1:9.
Preferred scope:Polycarboxylate:Silicate=9:1~1:1.
Most preferably it is worth:Polycarboxylate:Silicate=4:1.
Further, the titanium dioxide first product added in step (2) can be sulfuric acid process production or chloridising Technique productions.
The beneficial effect of present invention mashing process for dispersing includes:
(1) dispersant is not nitrogenous and phosphorus for mashing, is conducive to environmental protection;
(2) acid or alkali regulation slurry pH value need not be added, good dispersion effect can be equally reached, simplify technique, Reduce cost;
(3) beating consistency can be brought up to 600~1200g/L, wet-grinding efficiency and yield is improved, the damage of wet milling device is reduced Consumption and energy consumption.
Embodiment
The embodiment of form, remakes further specifically to the above of the invention by the following examples It is bright, illustrate but do not limit the present invention.
Present invention mashing process for dispersing realizes that the key being beaten to high-concentration titanium dioxide is to use polycarboxylate and silicon The compound of hydrochlorate is used as mashing dispersant.It is below the experiment of screening mashing dispersant:By changing dispersant, disperseing The Parameter Conditions such as agent ratio, dispersant dosage, slurry concentration carry out mashing experiment, and fixed mashing jitter time is 45 minutes, is surveyed Determine slurry viscosity.
(1) deionized water or distilled water are added into the mashing tank with agitating device, starts stirring, is added into mashing tank Dispersant is beaten, addition is in terms of content of titanium dioxide;
(2) toward addition titanium dioxide first product in mashing tank, then a certain amount of deionized water or distilled water are added, controls slurry Concentration;
(3) it is slurry obtained by step (2) is scattered 45 minutes, produce and be beaten scattered high-concentration titanium dioxide slurry.
Parameter designing and it the results are shown in Table 1.
Table 1 is beaten parameter designing and viscosity measurements
Example Dispersant Dispersive agent ratio Dispersant dosage/% Slurry concentration/(g/L) Viscosity/cP
1 Polycarboxylic acids sodium Nothing 0.1 600 250
2 Polycarboxylic acids sodium Nothing 0.3 900 315
3 Polycarboxylic acids sodium Nothing 0.5 1200 382
4 Sodium metasilicate Nothing 0.1 600 405
5 Sodium metasilicate Nothing 0.3 900 410
6 Sodium metasilicate Nothing 0.5 1200 420
7 Calgon Nothing 0.1 600 320
8 Calgon Nothing 0.3 900 351
9 Calgon Nothing 0.5 1200 403
10 Polycarboxylic acids sodium and sodium metasilicate 9:1 0.3 900 135
11 Polycarboxylic acids sodium and sodium metasilicate 4:1 0.3 900 115
12 Polycarboxylic acids sodium and sodium metasilicate 1:1 0.3 900 150
13 Polycarboxylic acids sodium and sodium metasilicate 9:1 0.5 1200 158
14 Polycarboxylic acids sodium and sodium metasilicate 4:1 0.5 1200 122
15 Polycarboxylic acids sodium and sodium metasilicate 1:1 0.5 1200 180
16 Polycarboxylic acids sodium and sodium metasilicate 9:1 0.1 600 118
17 Polycarboxylic acids sodium and sodium metasilicate 4:1 0.1 600 105
18 Polycarboxylic acids sodium and sodium metasilicate 1:1 0.1 600 127
As it can be seen from table 1 the mashing effect that polycarboxylic acids sodium, sodium metasilicate or calgon make mashing dispersant is used alone Fruit is not as polycarboxylic acids sodium and the beating resultses of sodium metasilicate compounding use.Mashing point is used as using polycarboxylic acids sodium and with sodium metasilicate compounding Powder, beating resultses are good, can carry out high concentration mashing, and not nitrogenous and phosphorus is conducive to environmental protection, and need not additionally add acid or alkali Adjust slurry pH value.

Claims (7)

1. the mashing process for dispersing of titanium dioxide, the described method comprises the following steps:
(1) processing mashing dispersant:Dispersant is added water and is beaten in the beating equipment with agitating device, and mashing dispersant is added Measure as the 0.1~0.5% of content of titanium dioxide;
(2) slurry concentration is controlled:Into beating equipment add titanium dioxide first product, add water control slurry concentration be 600~ 1200g/L;
(3) dispersed paste:Slurry obtained by step (2) is scattered 30~60 minutes, produce and be beaten scattered titania slurry;
Wherein described step (1) the mashing dispersant is the compound of polycarboxylate and silicate, and compound proportion is by weight For:Polycarboxylate:Silicate=9:1~1:9.
2. the mashing process for dispersing of titanium dioxide according to claim 1, it is characterised in that:The polycarboxylate and silicic acid The compound proportion of salt is by weight:Polycarboxylate:Silicate=9:1~1:1.
3. the mashing process for dispersing of titanium dioxide according to claim 2, it is characterised in that:The polycarboxylate and silicic acid The compound proportion of salt is by weight:Polycarboxylate:Silicate=4:1.
4. the mashing process for dispersing of the titania slurry according to claim any one of 1-3, it is characterised in that:It is described poly- Carboxylate is polycarboxylic acids sodium, and the silicate is sodium metasilicate.
5. the mashing process for dispersing of titanium dioxide according to claim 1, it is characterised in that:Added in the step (2) Titanium dioxide first product using sulfuric acid process produce or chlorination process production.
6. the mashing process for dispersing of titanium dioxide according to claim 1, it is characterised in that:Step (1) the band stirring The beating equipment of device is mashing tank.
7. the mashing process for dispersing of titanium dioxide according to claim 1, it is characterised in that:Step (1) and step (2) institute Water is stated for deionized water or distilled water.
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CN105921212B (en) * 2016-06-23 2019-02-15 攀钢集团攀枝花钢铁研究院有限公司 The method for reducing titania slurry viscosity
CN107400382B (en) * 2017-08-23 2019-03-22 攀钢集团重庆钛业有限公司 A kind of mashing dispersing method of titanium dioxide primary product
CN110988037A (en) * 2019-11-20 2020-04-10 攀钢集团重庆钛业有限公司 Method for detecting dispersion state of titanium dioxide
CN113088106A (en) * 2021-04-06 2021-07-09 攀钢集团重庆钒钛科技有限公司 Depolymerization dispersant and depolymerization dispersion method for titanium dioxide primary product

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US3847640A (en) * 1973-03-26 1974-11-12 A L Ind Inc Titanium pigment slurries for preparation of latex-base coating compositions
JPS5895614A (en) * 1981-12-03 1983-06-07 Onahama Sakai Kagaku Kk Preparation of titanium dioxide slurry
US5603411A (en) * 1994-12-07 1997-02-18 Engelhard Corporation Method for separating mixture of finely divided minerals
CN101280128B (en) * 2008-06-02 2011-08-17 深圳职业技术学院 Anatase titanium dioxide type titanium white pulp and preparation thereof
CN102391689B (en) * 2011-08-11 2013-05-22 四川龙蟒钛业股份有限公司 Preparation method of high dispersing rutile product
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Address after: 617063 Panzhihua Vanadium-Titanium Industrial Park, Sichuan Province

Patentee after: PANGANG GROUP TITANIUM INDUSTRY Co.,Ltd.

Address before: 617063 No. 1491, East Section of Jinshajiang Avenue, Panzhihua City, Sichuan Province

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Patentee after: CHONGQING TITANIUM INDUSTRY CO., LTD OF PANGANG Group

Address before: 617063 vanadium and Titanium Industrial Park, Panzhihua City, Sichuan Province

Patentee before: PANGANG GROUP TITANIUM INDUSTRY Co.,Ltd.