Process for producing biodiesel form seeds and fruits of plants

A biodiesel and seed technology, which is applied in the preparation of biological raw materials, biofuels, and liquid hydrocarbon mixtures, etc., can solve the problems of increasing production processes and production costs, decreasing the total extraction yield of biodiesel, and increasing acid value, etc. The effect of overcoming the saponification of oil, low production cost and accelerated reaction speed

Inactive Publication Date: 2008-11-19
陈登龙 +4
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

There are two main disadvantages of this preparation method: one is that the acid value of the vegetable oil squeezed first will increase during storage, so that when using it as a raw material to produce biodiesel with an alkaline method, the raw material oil must be pre-deacidified. The second is that because the chemical composition of vegetable oil is fatty acid triglyceride, its viscosity is relatively large, and there are more oils and fats remaining in the seed pool during pressing, which leads to a decline in the total extraction yield of biodiesel. higher cost

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0021] Embodiment 1, (1) get rapeseed 1000g after sorting, drying, crushing, join in the reactor of band shear stirring equipment (400 revs / min), add fatty acid methyl ester 30g, methyl alcohol 100g, high-speed shear Vigorously stirred for 2 hours, the material formed a flowing and uniform suspension.

[0022] (2) At the same time, 20 g of NaOH was dissolved in methanol to form a 10% NaOH methanol solution by mass percentage.

[0023] (3) Add 10 g of borax to the above (1) suspension, continue stirring at high speed for 1 hour, then slowly add the above (2) NaOH methanol solution, and react at 70° C. for 1.5 hours.

[0024] (4) After the reaction is completed, the temperature of the reaction material is lowered to 40° C., and the separated filtrate is obtained by pressure filtration, and the filter cake is used for other purposes.

[0025] (5) The separated filtrate is left to stand for separation, and by-products such as glycerin in the lower layer are separated to obtain cr...

Embodiment 2

[0028] Embodiment 2, (1) get 1000g of Sapindus seed 1000g after sorting, drying, crushing, join in the reaction kettle of band shear stirring equipment (900 revs / min), add fatty acid methyl ester 40g, methyl alcohol 200g, Stir vigorously under high shear for 4 hours, and the material forms a flowing and uniform suspension.

[0029] (2) At the same time, 2 g of KOH was dissolved in methanol to obtain a KOH methanol solution with a concentration of 8% by mass.

[0030] (3) Add 20 g of sodium carbonate to the above (1) suspension, continue stirring at high speed for 1 h, then slowly add the above (2) KOH methanol solution, and react at 80° C. for 1 h.

[0031] (4) After the reaction is completed, the temperature of the reaction material is lowered to 40° C., and the separated filtrate is obtained by pressure filtration, and the filter cake is used for other purposes.

[0032] (5) The separated filtrate is left to stand for separation, and by-products such as glycerin in the lowe...

Embodiment 3

[0035] Embodiment 3, (1) get after sorting, drying, crushed glabra seed 300g, rapeseed 700g, join in the reactor of band shear stirring equipment (1000 revs / min), add fatty acid methyl ester 35g, 300g of ethanol was stirred vigorously under high shear for 1.2h, and the material formed a suspension with uniform flow.

[0036] (2) At the same time, 30 g of NaOH was dissolved in methanol to obtain a 10% NaOH methanol solution by mass percentage.

[0037] (3) Add 5 g of potassium dihydrogen phosphate to the suspension of (1) above, continue stirring at high speed for 3 h, then slowly add NaOH methanol solution of (2) above, and react at 70° C. for 2 h.

[0038] (4) After the reaction is completed, the temperature of the reaction material is lowered to 40° C., and the separated filtrate is obtained by pressure filtration, and the filter cake is used for other purposes.

[0039] (5) The separated filtrate is left to stand for separation, and by-products such as glycerin in the lowe...

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PUM

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Abstract

The invention relates to a method for making biological diesel oil, in particular to a method for making biological diesel oil by seeds and fruit of plants. The making steps of the invention are as follows: the seeds and fruit of the plants are separated, dried and crushed and put in a reaction kettle provided with a cutting and blending device (the rotary speed is more than 300rev / m) and added with bridle chain alcohols and fatty acid methyl esters, and the mixture undergoes high speed cutting and stirring at the room temperature for 1 to 4 hours to form uniform suspension liquid, and the suspension liquid is added with alkalescent materials and undergoes high speed stirring for 1 to 4 hours; KOH or NaOH is dissolved in methyl alcohols to prepare the KOH or NaOH methanol solution with mass percentage concentration between 8 and 10 percent, which is used as catalyst; the suspension liquid is added with the catalyst and undergoes the back flow reaction for 0.5 to 4 hours; after the reaction, reactants are cooled down to the temperature of 40 DEG C and then undergo pressure filtration to obtain separated filtrate, and filter cakes are used for other purposes; the separated filtrate undergoes the standing separation to remove side products such as glycerin, etc. on the lower layer, and coarse products of biological diesel oil are obtained; the coarse products of biological diesel oil undergo normal pressure distillation to recover excessive bridle chain alcohols and undergo molecular distillation to obtain the qualified biological diesel oil. The method of the invention has the advantages of simple production process, high utilization rate of vegetable fat, low manufacturing cost and good economical efficiency of process, and has a good prospect for large-scale popularization and application.

Description

technical field [0001] The invention relates to a method for producing biodiesel, in particular to a method for producing biodiesel with plant seeds and fruits. Background technique [0002] Biodiesel is obtained from various animal and vegetable oils through esterification or transesterification, and its main component is long-chain fatty acid methyl ester. Biodiesel has high energy density, good lubricating performance, safe storage and transportation, good antiknock performance, full combustion and other excellent performance, renewability, environmental friendliness and good substitution performance, and is the bulk bio-based liquid with the most development potential fuel. The engine exhaust emission index using biodiesel not only meets the current Euro II standard, but even meets the more stringent Euro III emission standard that will be promulgated and implemented in Europe later. [0003] The raw materials for producing biodiesel are mainly animal oil and vegetable...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C10G1/00C10G3/00
CPCY02E50/13C11C3/003Y02E50/10Y02P30/20
Inventor 陈登龙黄三福肖可青吕玮陈顺玉
Owner 陈登龙
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