Method of preparing biologic diesel oil from high acid value vegetable oil catalyzed by p-toluenesulfonic acid
A technology of p-toluenesulfonic acid and biodiesel, which is applied in the preparation of liquid hydrocarbon mixtures, biological raw materials, biofuels, etc., can solve the problems of difficult separation, many side reactions, high energy consumption, etc. Outstanding catalytic performance and high equipment requirements
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Embodiment 1
[0022] The influence of embodiment 1 temperature on reaction
[0023] Weigh about 40 g of high acid value vegetable oil samples, and react under the conditions of 5% p-toluenesulfonic acid catalyst, alcohol-oil mass ratio of 1:2, and reaction time of 3 h. Investigate the influence of temperature on the reaction, as shown in Table 2:
[0024] The influence of table 2 temperature on reaction
[0025]
[0026] No reaction at 50°C, slow reaction at 60°C, rapid reaction above 75°C. This is because as the temperature increases, the activity of the reactants increases and the reaction speed increases, which leads to an increase in the esterification rate. However, due to the excess amount of methanol in the reaction system, there is an optimal reaction temperature for the transesterification reaction, and the temperature is low. It will slow down the reaction and reduce the rate of esterification. If the temperature is too high, the volatilization of methanol will be accelerated...
Embodiment 2
[0027] The impact of embodiment 2 catalyst dosage on reaction
[0028] The mass ratio of alcohol to oil was 1:2 and the temperature was 80°C for 3 hours to investigate the effect of different amounts of catalyst p-toluenesulfonic acid (0.5%, 2%, 3%, 5%) on the reaction yield. As in Table 3:
[0029] The influence of table 3 catalyst dosage on reaction
[0030]
[0031] It can be seen from the table above that the influence of the amount of catalyst on the reaction yield and viscosity is not obvious, and the amount of catalyst can be 0.5%-3% of the raw oil.
Embodiment 3
[0032] The influence of embodiment 3 alcohol oil ratio on reaction
[0033] The catalyst addition was 3%, and the reaction was carried out at 75°C for 3 hours to investigate the influence of different alcohol-oil mass ratios (1:0.5, 1:1, 1:2, 1:3) on the reaction yield. As shown in Table 4:
[0034] The impact of table 4 alcohol-oil ratio on reaction
[0035]
[0036] It can be seen from the above table that with the change of methanol concentration, the esterification rate also increases correspondingly. Among them, when the mass ratio of methanol to oil is 1:1, the increase rate of esterification rate is the largest. Considering economic factors comprehensively, adopt Excess methanol not only has little effect on improving the esterification rate, but also leads to an increase in cost. Therefore, in the actual application process, the mass ratio of methanol to acidified oil should be 1:1 to 1:3 as the best.
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