Preparation of subsphaeroidal barium sulfate by sulfuric acid process and use in copper foil substrate
A barium sulfate, near-spherical technology, applied in chemical instruments and methods, calcium/strontium/barium sulfate, calcium/strontium/barium compounds, etc., can solve the problems of barium sulfate particle shape irregularity, wide particle size distribution, etc. , to achieve the effect of improving Tg value and flame retardant performance, improving whiteness and high thermal conductivity
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[0022] Example 1
[0023] (a) Crush and mix barite and anthracite, put them into a calcining converter for calcination, the temperature is controlled at 1200°C, and the calcination time is 2 hours to produce crude barium sulfide containing about 60% of barium sulfide;
[0024] (b) Put the above crude barium sulfide into the leaching tank and soak it with 80°C hot water to prepare a solution containing 114g / L barium sulfide, and adjust the temperature to 67°C. The barium sulfide solution and excess sulfuric acid (industrial sulfuric acid, 98%) was added into the continuous reactor at the same time to react to produce barium sulfate slurry and hydrogen sulfide. The addition rate of barium sulfide solution was 4000L / h. The amount of sulfuric acid added was 2.7g / L according to the remaining sulfuric acid concentration in the barium sulfate slurry after the reaction was completed. Calculation
[0025] (c) Pass hot air into the barium sulfate slurry to discharge hydrogen sulfide, and th...
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[0028] Example 2
[0029] (a) Crush and mix barite and anthracite, put them into a calcining converter for calcination, the temperature is controlled at 1200°C, and the calcination time is 2 hours to produce crude barium sulfide containing about 60% of barium sulfide;
[0030] (b) Put the above-mentioned crude barium sulfide into the leaching tank and soak it with hot water at 80°C to prepare a solution containing 110g / L barium sulfide, and adjust the temperature to 65°C. The barium sulfide solution and excess sulfuric acid (industrial sulfuric acid, 98%) was added into the continuous reactor at the same time to react to produce barium sulfate slurry and hydrogen sulfide. The addition rate of barium sulfide solution was 3000L / h, and the amount of sulfuric acid added was 12.5g / L according to the concentration of remaining sulfuric acid in the barium sulfate slurry after the reaction was completed. Calculation
[0031] (c) Pass hot air into the barium sulfate slurry to discharge hyd...
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[0034] Example 3
[0035] The remaining steps are the same as in Example 2, except that in step (d), after dehydration and washing, the filter cake is dissolved in water to make a barium sulfate slurry, and the coupling agent KH-560 is added to the barium sulfate slurry.
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