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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

Active Publication Date: 2014-11-19
中泽国际有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

When the reaction temperature exceeds 65°C, the methanol is evaporated before the esterification reaction, which increases the pressure in the kettle. At the same time, due to the continuous phase change of liquid phase methanol during the heating process and the reaction process, it absorbs a large amount of heat, resulting in a slow heating process. , the reaction temperature is difficult to control, the reaction time of the reaction section is 6 hours, which takes a long time, and more water is produced during the esterification reaction, which prevents the reaction from proceeding forward
When an external heater is used to heat the grease, since the grease needs to pass through the heater during the whole reaction process, it is easy to cause blockage of the heater

Method used

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Examples

Experimental program
Comparison scheme
Effect test

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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PUM

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Abstract

The invention discloses a method for esterifying high-acid value grease by utilizing vaporized methanol. The method comprises the steps: adding the high-acid value grease into a reaction kettle having the bottom with a circulation pipeline, and heating to a preset reaction temperature; then allowing the grease to be continuously circulated in the circulation pipeline, carrying out reverse contact and mixing with the continuously-introduced vaporized methanol in the circulation pipeline, and then sending into the reaction kettle until an acid value of the materials in the reaction kettle is less than or equal to 1 mg KOH / g; and adding an acid catalyst into the reaction kettle to catalyze an esterification reaction. The vaporized methanol and the grease are in inverse contact in the circulation pipeline, so that the two materials can be fully mixed and the esterification reaction is brought forward to the circulation pipeline for rapid performing, the reaction time is shortened, the grease is only required to be heated for one time before the reaction, the temperature in the reaction kettle is not required to be controlled in the reaction process, and an external heater is more not required to be used for continuously heating the reaction materials; and the method has the advantages of easy manipulation, fast speed, less energy consumption and the like.

Description

technical field [0001] The invention belongs to the technical field of biodiesel production, and in particular relates to a method for esterifying high-acid-value oil with vaporized methanol. Background technique [0002] Biodiesel is a renewable clean energy. The existing biodiesel acid-catalyzed esterification process mainly involves adding grease, catalyst and liquid phase methanol into a reactor, heating to a certain temperature and then maintaining a constant temperature for esterification. When the reaction temperature exceeds 65°C, the methanol is evaporated before the esterification reaction, which increases the pressure in the kettle. At the same time, due to the continuous phase change of liquid phase methanol during the heating process and the reaction process, it absorbs a large amount of heat, resulting in a slow heating process. , the reaction temperature is difficult to control, the reaction time of the reaction section is 6 hours, which takes a long time, and...

Claims

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Application Information

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IPC IPC(8): C11C3/04
Inventor 王晓宁张少明陈献锟
Owner 中泽国际有限公司
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