Preparation method of biological diesel oil

A biodiesel and oil technology, which is applied in the preparation of liquid hydrocarbon mixtures, biological raw materials, biofuels, etc., can solve the problems of complex process, waste lye discharge, high cost, etc., and achieves simple and safe process route, mild reaction conditions, and high cost. The effect of reducing waste residue discharge

Inactive Publication Date: 2009-07-15
张海军
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  • Summary
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  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0009] At present, the production of biodiesel by transesterification mainly adopts chemical methods. The traditional chemical method transesterification uses homogeneous catalysts, such as NaOH, KOH, sodium methylate, etc., and the dosage is about 1%. The reaction temperature is generally the boiling point of methanol. The speed is fast and the conversion rate is high, but at the same time there are obvious disadvantages: the process is complicated, the alcohol must be excessive, and the subsequent process must have a corresponding alcohol recovery device; high energy consumption, dark color, because unsaturated fatty acids in fat are easy to deteriorate at high temperatures , the esterification product is difficult to recycle, and the cost is high; the product must be neutralized and washed to bring a large amount of industrial wastewater, causing environmental pollution; the generation process has waste lye discharge, which is not conducive to environmental protection requirements
However, most of the conventional super strong solid bases are complicated to prepare, expensive in cost, poor in strength, and easily destroyed by CO in the atmosphere. 2 、H 2 Contaminated by impurities such as O, and the specific surface area is small

Method used

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Examples

Experimental program
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Effect test

Embodiment 1

[0038] Preparation of solid catalyst A:

[0039] Mix titanium tetrachloride and aluminum trichloride with a molar ratio of 1:2 to make a 30% solution, 1kg of catalyst A requires 435g titanium tetrachloride and 584g aluminum trichloride, use 28% ammonia water as a precipitant, and control the pH The value is 7~8, the precipitate is filtered, washed, ground, passed through a 100-mesh sieve, impregnated with 0.5mol / L sulfuric acid for 2 hours, filtered with suction, dried at 110°C, activated at 430°C for 3h, cooled, and placed in a desiccator After medium drying, the composite titanium sulfate super strong solid acid SO 4 2- / TiO 2 —Al 2 o 3 . The solid catalyst A is loaded in the fixed-bed reactor A, and the amount of the solid catalyst A is 2% of the mass of the cottonseed oil, which is supplemented with the reaction.

[0040] Preparation of solid catalyst B: 1020g Al 2 o 3 1kg of solid catalyst B can be produced.

[0041] With 20% KNO 3 solution, the Al 2 o 3 Powde...

Embodiment 2

[0054] Preparation of solid catalyst A:

[0055] Make a 30% solution of chromium tetrachloride and aluminum trichloride according to the molar ratio of chromium and aluminum at 1:2, use 28% ammonia water as a precipitant, control the pH value to 7-8, and filter and wash the precipitate , grind, pass through a 100-mesh sieve, impregnate with 0.5mol / L sulfuric acid for 2 hours, filter with suction, dry at 110°C, activate at 480°C for 3 hours, cool, and dry in a desiccator to obtain a composite titanium sulfate super solid acid SO 4 2- / ZrO 2 —Al 2 o 3

[0056] The rapeseed oil enters the raw material storage tank after removing mechanical impurities, and enters the raw material storage tank after being heated to 80°C with a vacuum degree of -0.095Mpa and a dehydrator at a temperature of 130°C. effect on catalyst activity.

[0057] Ethanol and co-solvent tetrahydrofuran were prepared according to the volume ratio of 1:1.25, and put into No. 2 raw material tank for standby.

...

Embodiment 3

[0065] The preparation method is the same as that of Example 1, the raw material is agricultural seed oil, the activation condition of solid catalyst A is 450° C. for 3 hours, and other process conditions are the same.

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Abstract

The present invention relates to biodiesel oil preparing process, and provides one biodiesel oil preparing process with solid acid and solid alkali as catalyst to lower the activating energy and raise the reaction speed. The biodiesel oil preparing process includes the following steps: reacting dried grease with high free fatty acid content, methanol or ethanol, and cosolvent in the molar ratio of 1 to 6-1 to 6.05 in the first fixed bed reactor with solid catalyst A at 60-65 deg.c for about 3 hr; separating the oil phase from others; reacting the oil phase in the second fixed bed reactor with solid catalyst B with methanol or ethanol and cosolvent at 60-65 deg.c for about 3 hr; distilling out methanol or ethanol and cosolvent; separating the biodiesel oil from glycerin phase; and distilling the biodiesel oil phase to obtain biodiesel oil product. The catalyst of the present invention has high catalytic activity and can lower the activating energy and raise the reaction speed.

Description

technical field [0001] The invention relates to a method for preparing biodiesel from oil high in free fatty acid by using solid acid and solid base as catalysts for heterogeneous catalytic reaction. Background technique [0002] Diesel is an important fuel oil and the main power fuel for many large machinery (such as trucks, ships, diesel locomotives and generators, etc.). It has the advantages of high power and low price, so it has been widely used. According to estimates, the current annual demand for diesel in my country has exceeded 80 million tons. [0003] Mineral diesel is mainly obtained through petroleum refining process. At present, domestic oil production capacity is far lower than the domestic demand for oil products, which requires a large amount of imports. Due to changes in the international situation, the stability of oil imports is also threatened by some potential factors. If the situation of oil imports changes greatly, it will seriously affect the sust...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C10G3/00
CPCY02E50/13Y02E50/10Y02P30/20
Inventor 张海军
Owner 张海军
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