White carbon black high-activity dispersing agent composition and preparation method thereof
A high-activity, dispersant technology, applied in the field of silica high-activity dispersant composition and its preparation, can solve the problem of small dispersing function of silica, and achieve the effect of easy operation and simple process
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Embodiment 1
[0060] Weigh the raw materials by weight:
[0061] Acephenhydrazine 76 kg;
[0062] Lauric acid 60 kg;
[0063] Cetyltrimethylammonium chloride 18 kg;
[0064] Stearyl alcohol 8 kg;
[0065] 16 kg of monoglyceride;
[0066] Diethylene glycol 6 kg;
[0067] C9 petroleum resin 16 kg.
[0068] First put 60 kg of lauric acid, 18 kg of cetyl trimethyl ammonium chloride, 8 kg of stearyl alcohol, 16 kg of monoglyceride, 6 kg of diethylene glycol, and 16 kg of C9 petroleum resin to a pressure of -0.09Mpa In the negative pressure reactor, the reactor heats up. When the temperature rises to 160°C, 76 kg of acetophenazine are added to the reactor through the feeder. After the reaction is over, the high-activity silica dispersant combination can be prepared Discharge the white carbon black high-activity dispersant composition in the reaction kettle into the storage tank of the condensation granulator to form granules or flakes.
Embodiment 2
[0070] Weigh the raw materials by weight:
[0071] 62 kg of benzoyl hydrazide;
[0072] Benzenesulfonyl hydrazide 16 kg;
[0073] 54 kg of oleic acid;
[0074] Palmitic acid 40 kg;
[0075] Cetyl trimethyl ammonium chloride 10 kg;
[0076] Diethylene glycol 6 kg;
[0077] 12 kg of monoglyceride;
[0078] Stearyl alcohol 6 kg;
[0079] C9 petroleum resin 14 kg.
[0080] First put 54 kg of oleic acid, 40 kg of palmitic acid, 10 kg of cetyl trimethyl ammonium chloride, 6 kg of diethylene glycol, 12 kg of monoglyceride, 6 kg of stearyl alcohol, and 14 kg of C9 petroleum resin. In a negative pressure reaction kettle with a pressure of -0.09Mpa, the reaction kettle heats up. When the temperature rises to 180°C, 62 kg of benzoyl hydrazide and 16 kg of benzene sulfonyl hydrazide are added to the reaction kettle through the feeder. After the reaction is completed , The high-active white carbon black dispersant composition can be prepared, and the high-active white carbon black dispersant compositio...
Embodiment 3
[0082] Weigh the raw materials by weight:
[0083] Acephenhydrazine 38 kg;
[0084] Lauric acid 30 kg;
[0085] Monoglyceride 8 kg;
[0086] Cetyltrimethylammonium chloride 9 kg;
[0087] Stearyl alcohol 4 kg;
[0088] C9 petroleum resin 8 kg;
[0089] Diethylene glycol 3 kg.
[0090] First put 30 kg of lauric acid, 8 kg of monoglyceride, 9 kg of cetyl trimethyl ammonium chloride, 4 kg of stearyl alcohol, 8 kg of C9 resin, and 3 kg of diethylene glycol to a pressure of -0.09Mpa In the negative pressure reactor, the reactor heats up. When the temperature rises to 170°C, 38 kg of acetophenazine are added to the reactor through the feeder. After the reaction is completed, the white carbon black high-activity dispersant composition can be prepared , The white carbon black high-activity dispersant composition in the reaction kettle is discharged into the storage tank of the condensation granulator to make granules or flakes.
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