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Method for circulating preparation of biodiesel

A biodiesel and cycle preparation technology, applied in the direction of biofuel, carboxylate preparation, chemical instruments and methods, etc., can solve the problems of catalyst loss of activity, high production cost, difficult methanol recovery, etc., to increase added value and save raw materials Cost, improve the effect of corrosion equipment

Inactive Publication Date: 2015-05-13
NAT TAIPEI UNIV OF TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

In summary, the prior art all carries out the esterification process with acid catalysts, yet, there are some disadvantages in the preparation of biodiesel by acid catalysts for esterification: (1) use homogeneous acid catalysts (such as sulfuric acid, hydrochloric acid and p- Toluene sulfonic acid, etc.), has problems such as difficult separation of catalyst and product, difficulty in catalyst recovery and treatment, corrosion of equipment, waste water treatment, environmental pollution, etc.; (2) If a solid acid catalyst is used instead of a liquid acid catalyst, although it can improve corrosion, pollution, and Separation and other issues
But the disadvantage is that the life of the catalyst is not long, the production cost is high, and if it is used in oil products with poor quality, the catalyst will easily lose its activity.
(3) Carry out the esterification reaction with methanol as the alcohol of the esterification reaction. It is difficult to remove water during the reaction process, so a large amount of methanol is required to facilitate the reaction and the reaction time is longer
In addition, it is not easy to recover the remaining methanol from the reaction, which will consume a lot of energy and time

Method used

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  • Method for circulating preparation of biodiesel
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  • Method for circulating preparation of biodiesel

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0026] Example 1 In the high temperature and normal pressure esterification process, the influence of glycerol / free fatty acid molar ratio and reaction temperature on the esterification rate

[0027] In this embodiment, free fatty acid is used as a source of material, and the main fatty acid composition of the free fatty acid is 72wt% oleic acid (oleic acid) and 13wt% linoleic acid (linoleate acid), and glycerin is used as the alcohols of the esterification reaction.

[0028] Glycerin and free fatty acid were esterified at a molar ratio of 1:3 to 2:1 under normal pressure, and the reaction temperature was set at 200°C to 250°C, and the stirring and reaction were carried out at a rotation speed of 200rpm for 210 minutes.

[0029] Table 1 compares the effects of different molar ratios of glycerol and free fatty acids on acid value and esterification rate

[0030]

[0031]

[0032]

[0033] The results are shown in Table 1. Using free fatty acid as the material source, t...

Embodiment 2

[0035] The impact of embodiment 2 low pressure environment on the esterification reaction rate

[0036]In Example 2, the mixture of free fatty acid and palm oil is used as raw material, wherein the palm oil is refined palm oil. This embodiment also uses palm sludge oil and crude palm oil from palm oil factories as raw materials. In addition, this embodiment uses vacuum pumping equipment to maintain the interior of the closed reactor at a negative pressure state, which can make the water generated by the esterification reaction easier to be vaporized into water vapor and removed, thereby improving the efficiency of esterification. The reaction speed, on the other hand, can reduce the partial pressure of oxygen in the reactor to reduce the possibility of oil being oxidized in a high temperature environment.

[0037] Table 2 carries out the data of high temperature and low pressure esterification reaction

[0038]

[0039]

[0040] If sample 3 of Table 1 is compared with ...

Embodiment 3

[0041] In the transesterification process of embodiment 3, compare the impact of different operating conditions on the yield of biodiesel

[0042] The oil product in this example is obtained from the glyceride mixture generated by the esterification reaction of sample 4 in Example 1, and the initial acid value is 0.81 milligrams of potassium hydroxide per gram (mg KOH / g). Generally speaking, if the acid value of the oil is less than 2mg KOH / g, the subsequent transesterification reaction can be carried out directly. In this example, the molar ratio of methanol to glyceride mixture is set between 1:1 and 5:1, and 0.52 (w / w%) to 2w / w% potassium hydroxide is added as a transesterification catalyst, the reaction temperature is between 50° C. and 65° C., and the mixing and reaction are carried out at a rotation speed of 400 rpm for 60 minutes.

[0043] Table 3 compares the impact of different operating conditions on the transesterification reaction

[0044]

[0045] The results...

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Abstract

The present invention discloses a method for circulating preparation of biodiesel. The method comprises that: (a) glycerol and a free fatty acid are subjected to an esterification reaction under a high temperature and low pressure environment so as to obtain a glyceride mixture; (b) the glyceride mixture, low carbon alcohol and an alkaline catalyst are mixed and are subjected to a transesterification reaction, and phase separation is performed after completing the reaction so as to obtain a biodiesel solution and a glycerol solution; (c) an acid solution is adopted to neutralize the glycerol solution so as to produce salt precipitate; (d) the glycerol solution obtained in the step (c) is filtered to remove the salt precipitate; and (e) the glycerol solution obtained in the step (d) is heated to remove the low carbon alcohol and the water so as to obtain the purified glycerol product. According to the present invention, the esterification reaction can be performed without additionally addition of the acid catalyst, and the glycerol product can be recovered to carry out circulating preparation of the biodiesel so as to reduce the biodiesel production cost.

Description

technical field [0001] The invention relates to a method for preparing biodiesel in circulation, in particular to a method for preparing biodiesel by using oil with high free fatty acid content as raw material and glycerol as alcohols for esterification reaction. Background technique [0002] The price of raw materials is the main factor affecting the cost of biodiesel (biodiesel). Waste cooking oil and non-edible animal and vegetable oils have become biodiesel raw materials with development prospects due to their low cost. However, these low-cost raw materials usually contain high free fatty acids (FFAs), and cannot be directly subjected to alkali-catalyzed transesterification (transesterification). At present, a two-stage process is commonly used to produce biodiesel from high-content free fatty acids: first, acid esterification, and then alkali-catalyzed transesterification. The acid-catalyzed esterification method uses a homogeneous liquid acid catalyst or a heterogeneo...

Claims

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Application Information

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IPC IPC(8): C11C3/02C11C3/10C11C3/00C10L1/02C07C67/08C07C69/58C07C69/587
CPCC07C67/08C10L1/02C11C3/00C11C3/02C11C3/10C07C69/58C07C69/587Y02E50/10
Inventor 陈奕宏林佳融
Owner NAT TAIPEI UNIV OF TECH
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