Calcium hydroxyapatite based calcium sulfonate grease compositios and method of manufacture
A technology of calcium sulfonate and composition, which is applied in the field of calcium carbonate-based calcium sulfonate oil composition and its preparation, can solve the problems of not providing and simultaneously improving calcium sulfonate compound oil technology, interfering with the transformation process, and inferior oil compounds
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Embodiment 1
[0033] Example 1: The calcium sulfonate compound grease according to the present invention is prepared as follows: 36.00 parts by weight of 400TBN overbased calcium sulfonate (with amorphous calcium carbonate dispersed therein) is added to an open mixing container, and then 33.38 parts are added The solvent-neutral group I paraffinic base oil and 1.00 parts of PAO. The viscosity of the paraffinic base oil is about 600SUS at 100°F, and the viscosity of the PAO is 4cSt at 100°C. Start stirring without heating with a planetary stirring paddle. Then 3.60 parts of main C12 alkyl benzene sulfonic acid was added as accelerating acid. After 20 minutes, 7.58 parts of finely divided calcium carbonate was added as the basic calcium source, the average particle size of the calcium carbonate was less than 5 microns, and it was mixed for 10 minutes. Then 1.80 parts of hexanediol and 4.5 parts of water were added as conversion agents. The mixture is heated until the temperature reaches 190°...
Embodiment 2
[0034] Example 2: Another batch of grease was made using the same equipment, raw materials, quantity and manufacturing process as the grease of Example 1, except that after conversion and after adding complex acids (12-hydroxystearic acid, acetic acid, and phosphoric acid) ) Add calcium carbonate immediately before. The composition of this grease is the same as the grease of Example 1 above. The initial penetration of the final grease is 285 and the penetration of 60 working strokes is 288. The dropping point is 555°F. The proportion of high-alkali oil-soluble calcium sulfonate in this batch of fats and oils is 36.0%. It can be seen that the grease of this example is 35 points softer than the grease of Example 1 and has a significantly lower drop point. Since the only difference between the two fats and oils is the addition time of calcium carbonate relative to the conversion, the softer consistency (lower thickener yield) and low dropping point must be due to this differenc...
Embodiment 3
[0036] Example 3: Another batch of grease was made using the same equipment, raw materials, quantity and manufacturing process as the grease of Example 1, except for the following changes: (1) Add acetic acid immediately before adding hexanediol and water, and this batch The materials are reacted at ambient temperature; (2) 12-hydroxystearic acid is added at 170°F before conversion while heating the reactants to 190°F; and (3) no calcium carbonate is added. The proportion of high-alkali oil-soluble calcium sulfonate in this batch was 36.0%. This batch of reactants did not turn into a grease structure even after heating for several hours and was therefore discarded.
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