dye pigment titanium dioxide factory

As a trusted supplier of Lithopone B301, we understand the importance of consistent quality and reliable supply. Our manufacturing facilities are equipped with state-of-the-art technology to ensure that our product meets the highest standards of purity and performance Our manufacturing facilities are equipped with state-of-the-art technology to ensure that our product meets the highest standards of purity and performance Our manufacturing facilities are equipped with state-of-the-art technology to ensure that our product meets the highest standards of purity and performance Our manufacturing facilities are equipped with state-of-the-art technology to ensure that our product meets the highest standards of purity and performancelithopone b301 quotes supplier. We also have a dedicated team of professionals who are committed to providing exceptional service and support to our customers.

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In conclusion, while both lithopone and titanium dioxide have their advantages and disadvantages, TiO2 appears to be the better choice for most applications. Its superior whiteness, UV protection properties, and chemical stability make it a popular choice in the paint, plastics, and paper industries. However, for applications where cost and safety are primary concerns, lithopone may still be a viable option. Ultimately, the choice between these two pigments will depend on the specific requirements of the application and the desired balance of performance and cost.

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At present, the domestic wet zinc smelting mainly adopts the roasting-leaching-electrowinning production process, and the zinc content in the acid leaching residue is generally 8-15%, some up to 20%, and the sulfur mass fraction is 6-12%, of which sulfuric acid The root mass fraction is 15-30%, mainly in the form of 0^0 4 (in this ammoniatic environment, the leaching rate of sulfate leaching in multiple stages can reach 70%). The zinc in the acid leaching residue is mainly in the form of ZnFe 2 0 4 . In order to recover these zinc, the treatment methods are currently available in the fire method and the wet method. The fire method is the rotary kiln evaporation method (Wilz method) and the fumigating furnace evaporation method. . The wet method has hot acid leaching or high temperature pressure leaching. The fire treatment process is long, the equipment maintenance is large, the investment is high, the working environment is poor, and a large amount of coal or metallurgical coking coal is consumed, which has low efficiency and large environmental pollution. Therefore, it is usually leached by hot acid or high-pressure leaching. These methods still have the disadvantages of: 1 consumption of a large amount of acid, low leaching rate, due to the large amount of calcium sulfate, calcium sulphate and other ultrafine particles to isolate the zinc oxide particles, resulting in Electrolytic zinc enterprises are difficult to leach in acid environment, and the second weak acid leaching is not meaningful because the recovery rate is too low. 2 If leached with strong acid, although ZnFe 2 0 4 is destroyed, the leaching rate is improved, but the iron leaching rate is also high (up to 60%). The pressure of iron removal is large, and more reagents are consumed. 3 High temperature and high pressure equipment is corroded. Serious, complicated equipment investment; 4 high operating costs, poor economic returns. 5 The last slag discharged is acid leaching residue, which brings new pollution to the environment. It has to be cured and landfilled, which not only pollutes the environment, but also wastes resources.

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