Biodiesel production method

A biodiesel and production method technology, applied in biofuel, petroleum industry, liquid carbon-containing fuel, etc., can solve the problems of high reaction temperature, high price, high alcohol-oil ratio, etc., and achieve mild reaction conditions, no waste water discharge, High conversion effect

Inactive Publication Date: 2013-08-14
RESEARCH INSTITUTE OF TSINGHUA UNIVERSITY IN SHENZHEN
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Among them, patent CN101045878, a method for producing biodiesel using solid acid and solid base two-step catalytic method uses solid superacid as catalyst, but the reaction temperature is high and the catalyst price is also relatively expensive; patent CN101884931, a solid superacid The preparation method of catalyst and the solid acid SO prepared in application 4 2- / ZrO 2 -CeO 2 As a catalyst for the preparation of biodiesel from jatropha oil, but this catalyst is not only cumbersome to prepare but also requires a longer time and higher temperature for transesterification; patent CN101474571, a hydrotalcite-like catalyst is prepared in a solid base catalyst for the preparation of biodiesel The compound was used as a catalyst for the production of biodiesel with satisfactory yields, but required a longer reaction time and higher reaction temperature
In summary, although the use of solid acid-base catalysts instead of traditional acid-base catalysts for the preparation of biodiesel has the advantage of no waste water discharge, but because the reaction is a heterogeneous reaction, it is different from homogeneous catalytic reactions (such as using sodium hydroxide as a catalyst, etc.) ) in comparison, there are problems such as longer reaction time, higher reaction temperature, higher alcohol-oil ratio, cumbersome preparation of catalyst, and high price. It is difficult to realize industrial production in a short period of time.

Method used

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  • Biodiesel production method

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0025] In a 2000ml three-necked flask, add 800g of corn oil and 132.27g of methanol to mix according to the molar ratio of alcohol to oil at 6:1, then add 53.33g of methanol-sodium hydroxide solution with a concentration of 15%, and stir at 60°C After reacting for 40 minutes, the reaction was completed, and then poured into a separatory funnel to stand for stratification. The upper layer was crude biodiesel, and the lower layer was crude glycerol, a by-product. After separating the crude glycerin, the excess methanol was evaporated to obtain crude biodiesel. Then add 38.4g of solid neutralizing agent—acid clay to the crude biodiesel, stir and react for 30 minutes, and separate the solid neutralizing agent—acid clay to obtain the product biodiesel. Yield 96.7%.

Embodiment 2

[0027] In a 2000ml three-neck flask, add 1200g of rapeseed oil and 198.4g of methanol according to the molar ratio of alcohol to oil at 6:1, mix them, add 80g of methanol-sodium hydroxide solution with a concentration of 15%, and stir at 60°C After reacting for 40 minutes, the reaction was completed, and then poured into a separatory funnel to stand for stratification. The upper layer was crude biodiesel, and the lower layer was crude glycerol, a by-product. After the crude glycerin was separated, excess methanol was evaporated to obtain crude biodiesel. Then add 45.7g of solid neutralizer—a mixture of modified zeolite molecular sieve and acid clay at a ratio of 1:3 (mass ratio) to the crude biodiesel, stir and react for 30 minutes, and then separate the modified zeolite molecular sieve and acid clay to obtain the product biodiesel. Yield 95.3%.

Embodiment 3

[0029] In a 1000ml three-neck flask, add 610g of cottonseed oil and 100.87g of methanol according to the molar ratio of alcohol to oil at 6:1 and mix them. Add 40.67g of methanol-potassium hydroxide solution with a concentration of 15%, and stir at 60°C After reacting for 45 minutes, the reaction was completed, and then poured into a separatory funnel to stand for stratification. The upper layer was crude biodiesel, and the lower layer was the by-product crude glycerin. After the crude glycerin was separated, excess methanol was distilled off. Then add 23.1g of solid neutralizer—a mixture of modified zeolite molecular sieve and strong acid resin at a ratio of 1:1 (mass ratio) to crude biodiesel, and stir for 30 minutes to separate the modified zeolite molecular sieve and strong acid resin. The product biodiesel is obtained. Yield 94.6%.

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Abstract

The invention relates to a biofuel production method, and especially relates to a biodiesel production method with mild reaction conditions, a high conversion rate, high yield, and no waste water discharge. The biodiesel production method comprises the following steps: S1, mixing raw materials of grease and medium and short-chain alcohol, completing a transesterification reaction under the actionof a homogeneous base catalyst; S2, separating the reaction solution completing the transesterification reaction to obtain crude biodiesel; S3, adding a solid neutralizer into the crude biodiesel, reacting for 10-60 minutes; S4, separating the solid neutralizer to obtain the biodiesel.

Description

technical field [0001] The invention relates to a biofuel production method, in particular to a biodiesel production method with mild reaction conditions, high conversion rate, high yield and no waste water discharge. Background technique [0002] With the depletion of fossil fuels and the deterioration of the ecological environment, countries around the world regard the development of biomass energy as their future energy strategy in order to get rid of the heavy dependence on fossil energy. As a renewable and environmentally friendly new energy source, biodiesel is favored by researchers from all over the world. Biodiesel is a long-chain fatty acid monoalkyl obtained by transesterifying animal fats, woody oil crops, herbaceous oil crops, seaweeds, and industrial and catering industry waste oils with low-carbon alcohols such as methanol and ethanol. ester. It has appeared four different production methods: direct mixing method, microemulsion method, thermal cracking metho...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C11C3/10C11C3/04C10L1/02
CPCY02E50/13Y02E50/10
Inventor 杨海燕李敏陈福明
Owner RESEARCH INSTITUTE OF TSINGHUA UNIVERSITY IN SHENZHEN
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