Process for producing biodiesel from high acid number grease

A high-acid value oil and biodiesel technology, which is applied in the production of fatty acids, biological raw materials, biofuels, etc., can solve the problems of high environmental protection treatment costs, large sewage discharge, and large investment in equipment, and achieve low manufacturing costs and fast response The effect of speeding up and shortening the reaction time

Inactive Publication Date: 2008-11-19
陈登龙 +4
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

When the acid value of the used oil > 0.5, the industry usually uses the "two-step" production process of first carrying out the oil acid catalyzed esterification reaction and then carrying out the alkali catalyzed transesterification reaction (that is, first carry out the oil acid catalyzed esterification, and then carry out the oil acid catalyzed esterification by The esterification reaction removes the acid value, and then carries out the intermediate step of washing to reduce the acid value to below 0.5, and then uses sodium methoxide as a catalyst to carry out the transesterification reaction) to avoid oil saponification. This method has complicated procedures, large equipment investment, and sewage discharge Large quantity, high cost of environmental protection treatment

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0020] (1) 40g of NaOH is dissolved in methanol to form a 10% NaOH methanol solution in mass percent concentration.

[0021] (2) Add 1000g of waste vegetable oil with an acid value of 4 to a reactor with a high-speed stirring device (above 500 rpm / min), add 30g of fatty acid methyl ester, 300g of methanol, stir vigorously at high speed for 2 hours, and the material flows uniformly of emulsion.

[0022] (3) Add 20 g of borax to the emulsion of (2) above, continue high-speed stirring for 1.5 h, then slowly add the NaOH methanol solution of (1) above, and react at 70° C. for 1.5 h.

[0023] (5) After the reaction is completed, the temperature of the reaction material is lowered to 40° C., and the mixture is left to stand for separation, and by-products such as glycerin in the lower layer are separated to obtain crude biodiesel.

[0024] (6) The biodiesel crude product is subjected to atmospheric distillation to recover excess short-chain alcohols

[0025] (7) After molecular di...

Embodiment 2

[0027] (1) Dissolving 30 g of KOH in methanol to prepare a KOH methanol solution with a mass percent concentration of 8%.

[0028] (2) Add 1000g of waste oil with an acid value of 5 into a reaction kettle with a high-speed stirring device (above 400 rpm / min), add 10g of fatty acid methyl ester, 400g of ethanol, stir vigorously at a high speed for 1h, and the material flows uniformly of emulsion.

[0029] (3) Add 30 g of sodium carbonate to the emulsion of (2) above, continue high-speed stirring for 1 h, then slowly add the KOH methanol solution of (1) above, and react at 70° C. for 0.5 h.

[0030] (5) After the reaction is completed, the temperature of the reaction material is lowered to 40° C., and the mixture is left to stand for separation, and by-products such as glycerin in the lower layer are separated to obtain crude biodiesel.

[0031] (6) The biodiesel crude product is subjected to atmospheric distillation to recover excess short-chain alcohols

[0032] (7) After mo...

Embodiment 3

[0034] (1) Dissolving 12 g of KOH in methanol to form a KOH methanol solution with a concentration of 10% by mass.

[0035] (2) 1000g of jatropha fruit oil with an acid value of 3 is added to a reactor with a high-speed stirring device (more than 400 revolutions per minute), and 10g of fatty acid methyl esters and 200g of methyl alcohol are added, and the mixture is vigorously stirred for 1h at a high speed, and the material Forms a flowing, uniform emulsion.

[0036] (3) Add 10 g of potassium dihydrogen phosphate to the emulsion of (2) above, continue stirring at high speed for 1 hour, then slowly add the KOH methanol solution of (1) above, and react at 70° C. for 0.5 hour.

[0037] (5) After the reaction is completed, the temperature of the reaction material is lowered to 40° C., and the mixture is left to stand for separation, and by-products such as glycerin in the lower layer are separated to obtain crude biodiesel.

[0038] (6) The biodiesel crude product is subjected t...

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PUM

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Abstract

The invention relates to a method for making biological diesel oil, in particular to a method for making biological diesel oil by grease with high acid value, belonging to the renewable energy resource technical field. The production formula of the method in weight portion is as follows: 100 portions of grease, 20 portions of bridle chain alcohol, 1 to 10 portions of fatty acid methyl ester, 0.5 to 4 portions of catalyst and 0.1 to 5 portions of alkalescent buffer substances. The concrete steps are as follows: the grease is put in a reaction kettle provided with a high speed blending device, added with the bridle chain alcohol and the fatty acid methyl ester, and undergoes high speed stirring at the room temperature for 1 to 4 hours so as to form emulsion, and the emulsion is added with the alkalescent substances and undergoes high speed stirring for 1 t0 4 hours; KOH or NaOH is dissolved in methyl alcohols to prepare the KOH or NaOH methanol solution with mass percentage concentration between 8 and 10 percent, which is used as catalyst; the emulsion is added with the catalyst and undergoes back flow reaction for 0.5 to 4 hours; after the reaction, reactants are cooled down to the temperature of 40 DEG C and then undergo standing separation to remove side products such as glycerin, etc. on the lower layer, and coarse products of the biological diesel oil are obtained; the coarse products of the biological diesel oil undergo normal pressure distillation to recover excessive bridle chain alcohols and undergo molecular distillation to obtain the qualified biological diesel oil. The method of the invention has the advantages of simple production process, mild condition, easy post treatment, low manufacturing cost, good economical efficiency of process and easy realization of industrialization, and has a good prospect for large-scale popularization and application.

Description

technical field [0001] The invention relates to a method for producing biodiesel, in particular to a method for producing biodiesel from oil with high acid value, and belongs to the technical field of renewable energy. Background technique [0002] Liquid fuel is one of the cornerstones of maintaining the normal operation of modern society and is the most important power fuel. With the development of the world economy, global fossil resources are becoming increasingly depleted, and the supply situation of liquid fuel is becoming increasingly severe. Energy shortage has become one of the important factors restricting the economic development of all countries in the world. my country imported 120 million tons of crude oil in 2004, accounting for 44% of the total processed crude oil. Excessively high import dependence has threatened the national energy strategy security. In terms of energy consumption structure, my country is a big diesel consumer. In 2003, it consumed 83.07 m...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C10G3/00C11C3/00
CPCY02E50/13Y02E50/10Y02P30/20
Inventor 陈登龙黄三福肖可青吕玮陈顺玉
Owner 陈登龙
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