Method for preparing biodiesel by zirconia solid base catalyst

A solid base catalyst, biodiesel technology, applied in catalyst activation/preparation, physical/chemical process catalyst, metal/metal oxide/metal hydroxide catalyst, etc., can solve the problem of high conversion rate, difficult catalyst separation, and environmental pollution and other problems, to achieve the effect of convenient recovery and excellent physical and chemical stability

Inactive Publication Date: 2009-12-02
ZHEJIANG UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The traditional process for preparing biodiesel uses homogeneous catalysts, such as sodium hydroxide, sodium methoxide, sodium carbonate, potassium hydroxide and potassium carbonate, etc., and the dosage accounts for about 1% of the oil weight. The reaction temperature is not high, generally methanol Boiling point temperature, fast reaction speed, high conversion rate (above 95%)
However, the separation of the catalyst in the homogeneous method is difficult, and a large amount of industrial wastewater will be generated in the post-treatment process, causing environmental pollution.
Using enzymes as catalysts can be recycled, and the reactants and products in the catalyst have a large mass transfer rate, but during the reaction, if the process and parameters are improperly grasped, it is easy to cause enzyme "poisoning" and affect the catalytic effect
In addition, the application of enzyme-catalyzed transesterification is limited due to high enzyme price, long reaction time and low reaction yield.
The supercritical non-catalytic transesterification reaction is carried out, the reaction time is short, the conversion rate is high, and the post-treatment is simple, but the molar ratio of alcohol to oil is high, and the reaction temperature and pressure exceed the critical temperature and critical pressure of methanol, which requires high equipment requirements.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0014] In a 100ml autoclave, add 18.60g of refined sunflower oil, 17.52g of methanol, and add about 5% of the oil weight of La 2 o 3 / ZrO 2The catalyst is 0.92g, the reaction temperature is controlled at 190-200°C, the magnetic stirring speed is 600rpm, and the reaction time is 5h. After the reaction was completed, the catalyst was filtered with suction while it was hot, and the catalyst was recovered by distillation, and then the filtrate was allowed to stand overnight to separate layers. The upper product is biodiesel, and the lower product is glycerin. The product after further vacuum distillation and purification of crude biodiesel meets 0 # diesel standard. Both biodiesel and glycerin are neutral, which saves the industrial waste water produced by neutralization and washing, and reduces environmental pollution. Detected by liquid chromatography, the content of the obtained fatty acid methyl ester was 95.6%.

Embodiment 2

[0016] In a 100ml three-necked flask, add 18.04g of sunflower oil and 11.73g of methanol according to the ratio of alcohol to oil molar ratio of 10:1, add about 3% of La 2 o 3 / ZrO 2 The catalyst is 0.54g, the reaction temperature is controlled at 130-140°C, the magnetic stirring speed is 600rpm, and the reaction time is 5h. After the reaction was completed, the catalyst was filtered with suction while it was hot, and the catalyst was recovered by distillation, and then the filtrate was allowed to stand overnight to separate layers. The upper product is biodiesel, and the lower product is glycerin. Detected by liquid chromatography, the content of the obtained fatty acid methyl ester was 96.4%.

Embodiment 3

[0018] In a 100ml three-necked flask, add 18.26g of sunflower oil and 17.34g of methanol according to the ratio of alcohol to oil molar ratio of 30:1, and add about 5% of Sm 2 o 3 / ZrO 2 The catalyst is 093g, the reaction temperature is controlled at 190-200°C, the magnetic stirring speed is 600rpm, and the reaction time is 5h. After the reaction was completed, the catalyst was filtered with suction while it was hot, and the catalyst was recovered by distillation, and then the filtrate was allowed to stand overnight to separate layers. The upper product is biodiesel, and the lower product is glycerin. Detected by liquid chromatography, the content of the obtained fatty acid methyl ester was 94.0%.

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PUM

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Abstract

The invention discloses a method for preparing biodiesel by a zirconia solid base catalyst. The biodiesel is obtained by taking vegetable oil as a raw material to react with methanol or ethanol, adding the catalyst into the obtained product, and performing the transesterification. The solid base catalyst is rare earth metal oxide which takes zirconia as a carrier to support rare earth oxide, or takes zirconia supported rare earth metal oxide as the carrier and supports potassium fluoride. The preparation of the biodiesel by adopting the zirconia solid base catalyst as a catalyst for alcohol-grease exchange has high catalytic activity, has the conversion rate which is more than 94 percent, and has convenient post-treatment; the catalyst can be repeatedly used for multiple times after the recovery; and a product, namely the biodiesel and a byproduct glycerol are neutral, do not need to wash, and cannot produce industrial wastewater.

Description

technical field [0001] The invention relates to a method for preparing biodiesel, in particular to a zirconia solid alkali catalyst used for preparing biodiesel. Background technique [0002] Using oil crops such as soybeans and rapeseeds, fruits of oil trees such as oil palm and pistachio chinensis, engineering microalgae and other oil-bearing aquatic plants, animal fats, waste cooking oil, etc. as raw materials, the organic Fatty acid methyl ester or ethyl ester fuel is biodiesel, and the by-product is glycerin. The traditional process for preparing biodiesel uses homogeneous catalysts, such as sodium hydroxide, sodium methoxide, sodium carbonate, potassium hydroxide and potassium carbonate, etc., and the dosage accounts for about 1% of the oil weight. The reaction temperature is not high, generally methanol Boiling point temperature, fast reaction speed, high conversion rate (above 95%). However, the separation of the catalyst in the homogeneous method is difficult, and...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C10L1/02B01J23/10B01J27/135B01J37/02
CPCY02E50/13Y02E50/10
Inventor 楼辉孙辉丁宇琦段谨钊韩军兴李望郑小明
Owner ZHEJIANG UNIV
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