Method for directly preparing anhydrous calcium dodecyl benzene sulfonate, and product
A technology of calcium dodecylbenzenesulfonate and dodecylbenzenesulfonic acid, which is applied in the field of chemical preparation, can solve the problems of waste of resources, high viscosity of mother liquor, long filtration time, etc., so as to avoid waste of resources and reduce Contamination issues, effect of short filtration times
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Embodiment 1
[0043] Step 1. In a 2 ton reactor, add 360kg of isooctyl alcohol, heat it with steam to 50°C, add 550kg of linear dodecylbenzenesulfonic acid, then add 87.3Kg of calcium carbonate, and keep stirring at 50°C for 8 hours.
[0044] Step 2, adding monoethanolamine to adjust the pH to 4.
[0045] Step 3, heating up to 100°C for dehydration until the moisture content is lower than 0.5%.
[0046] Step 4, cooling down and discharging, adopting vacuum filtration to obtain a clarified product.
[0047] In embodiment 1, finally obtain product 900kg, product yield is 95%.
Embodiment 2
[0049] Step 1. In a 2-ton reactor, add 360kg of n-butanol, heat it with steam to 70°C, add 550kg of linear dodecylbenzenesulfonic acid, then add 64.6Kg of calcium hydroxide, and keep stirring at 70°C for 5h.
[0050] Step 2, adding diethanolamine to adjust the pH to 6.
[0051] Step 3, heating up to 100 degrees and dehydrating until the moisture content is lower than 0.5%.
[0052] Step 4, then cool down and discharge, adopt vacuum filtration to obtain a clarified product.
[0053] In embodiment 2, finally obtain product 900kg, product yield is 95%.
Embodiment 3
[0055] Step 1. In a 2-ton reactor, add 460kg of solvent oil, heat it with steam to 80°C, add 550kg of branched chain dodecylbenzenesulfonic acid, then add 48.9Kg of calcium oxide, and keep stirring at 80°C for 3h.
[0056] Step 2, adding triethanolamine to adjust the pH to 7.
[0057] Step 3, heating up to 100 degrees and dehydrating until the moisture content is lower than 0.5%.
[0058] Step 4, then cool down and discharge, adopt vacuum filtration to obtain a clarified product.
[0059] In embodiment 3, finally obtain product 950Kg, product yield is 92%.
[0060] In Examples 1-3, the yield of the product is high, and the present invention does not use filter aids for multiple filtrations, so the pollution is small and the energy consumption is low.
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