rutile titanium dioxide mbr9668-coating

The leaching of the electrolytic zinc acid leaching slag: 1500 ml of ammonia-ammonium sulphate solution is used as the ammonia immersion liquid, wherein the ammonia concentration is 6. Omol / ammonium sulfate molar concentration is 0. 9mol / L, added per cubic meter of ammonia immersion liquid 0. 075kg of sodium dodecylbenzenesulfonate, 0. 45kg of sodium fluorosilicate, 0.75kg of dicyandiamide. 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 %), added to the above ammonia-ammonium sulfate immersion liquid for three-stage leaching, each leaching time is 2 hours, after solid-liquid separation, 1450ml final immersion liquid (taken away in the remaining liquid slag), zinc leaching The rate of 90. 02%; the final solution containing zinc 65. 6g / L; containing S0 4 2 - 69. 64g / L ;

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Despite these advancements, the pigment lithopone industry faced competition from alternative pigments like titanium dioxide, which offered similar properties at a lower cost. This competition forced many factories to adapt or risk closure This competition forced many factories to adapt or risk closure This competition forced many factories to adapt or risk closure This competition forced many factories to adapt or risk closurepigment lithopone factories. Some chose to specialize in niche markets where lithopone's unique characteristics were highly valued, while others focused on improving their production processes to reduce costs.

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