Method for esterifying high-acid value grease by utilizing vaporized methanol
A technology of esterification with high acidity and high acid value, applied in the direction of fatty acid esterification, etc., can solve the problems of long time consumption, slow heating process, heater blockage, etc., and achieve the effects of less energy consumption, improved reaction speed, and easy control
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Embodiment 1
[0017] Soybean acidified oil with an acid value of 138mgKOH / g is purified and sundries settled, then dehydrated until the water content is less than 0.5%, and then put 5m soybean acidified oil into the reactor with a circulation pipeline at the bottom 3 . Soybean acidified oil is heated to 140 DEG C, then in reactor, add the acid catalyst of soybean acidified oil quality 1.5‰ (acid catalyst is the sulfuric acid solution of sulfuric acid mass fraction 98%, it is diluted to sulfuric acid mass fraction with methanol earlier before adding. 35%), use vaporized methanol at 120°C to contact and mix with the circulating acidified soybean oil in the circulation pipeline, and then enter the reactor for esterification after passing through a section of pipeline. The amount of vaporized methanol per hour is the added soybean 10% of acidified oil mass. The pressure in the reactor is controlled at 0.05MPa. After reacting for 1.5 hours, measure the acid value of the material. When AV≤50mgKO...
Embodiment 2
[0019] After the palm oil with an acid value of 160mgKOH / g is purified and the debris is settled, it is dehydrated until the water content is less than 0.5%, and then 5m of palm oil is injected into the reactor with a circulation pipeline at the bottom. 3 . Palm oil is heated to 130 DEG C, then in reactor, add the acid catalyst of palm oil quality 2.0‰ (acid catalyst is the sulfuric acid solution of sulfuric acid mass fraction 70%, it is diluted to sulfuric acid mass fraction with methanol earlier before adding and is 45% ), use vaporized methanol at 110°C to contact and mix with the circulating palm oil in the circulation pipeline, and then enter the reaction kettle to start the esterification reaction after passing through a section of pipeline. 12%. The pressure in the reactor is controlled at 0.04MPa. After 1.5 hours of reaction, measure the acid value of the material. When AV≤50mgKOH / g, add an acid catalyst with a palm oil quality of 0.5‰ to carry out the second step of ...
Embodiment 3
[0021] After the waste oil with an acid value of 120mgKOH / g is purified and the debris is settled, it is dehydrated until the water content is less than 0.5%, and then poured into the reaction kettle with a circulation pipeline at the bottom for 5m 3 . Waste oil is heated to 145 ℃, then in reactor, add the acid catalyst of waste oil quality 2‰ (acid catalyst is the sulfuric acid solution of sulfuric acid mass fraction 98%, it is diluted to sulfuric acid mass fraction with methanol earlier before adding and is 45% ), using vaporized methanol at 130°C in the circulation pipeline to contact and mix the recycled waste oil in reverse, and then enter the reactor for esterification after passing through a section of pipeline. 8%. The pressure in the reactor is controlled at 0.06MPa. After reacting for 1.5 hours, measure the acid value of the material. When AV≤50mgKOH / g, add an acid catalyst with a waste oil quality of 1.5‰ to carry out the second step of catalytic esterification rea...
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