Preparation method of biodiesel

A technology of biodiesel and waste oil, which is applied in the fields of biofuel, petroleum industry, fatty acid production, etc., can solve the problems of unsuitable diesel production enterprises for wide application, incomplete reaction, and unqualified products, so as to improve urban air quality and shorten the Short esterification reaction cycle and short construction cycle

Active Publication Date: 2014-08-06
TANGSHAN JINLIHAI BIODIESEL
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0006] In the actual production process, the above two processes often lead to incomplete reaction and unqualified products due to poor handling. Therefore, most production enterprises usually set up a stirring process to promote the reaction and vacuum distillation for product separation. However, these two processes are both high-energy-consuming processes, which not only consume high energy, but also require a large investment, so they are not suitable for widespread use by small-scale diesel production enterprises.

Method used

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  • Preparation method of biodiesel

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preparation example Construction

[0032] The preparation method of the biodiesel disclosed in the present invention mainly uses waste oil as raw material, the main components of which are triglycerides and higher fatty acids, and two different products can be prepared according to actual production needs:

[0033] 1. Product a with biodiesel as the main component. The methanol and dimethyl carbonate contained in this product are used as oxygen enhancer components, which greatly improve the thermal efficiency of fatty acid methyl esters, reduce exhaust emissions, and improve urban air quality;

[0034] 2. Product b, containing 100% fatty acid methyl ester, can blend diesel and fuel oil in any proportion, and can flexibly adjust products according to market demand.

Embodiment 1

[0036] 10 tons of swill oil (50% triglyceride, 50% fatty acid) is unloaded to the raw material pool 4 for pretreatment, and the steam produced by the steam boiler 3 is passed into the raw material pool, and the temperature is raised to 90°C for heat preservation. 500KG concentrated sulfuric acid comes from Sulfuric acid storage tank 1 is evenly sprayed onto the surface of the raw material oil in the raw material pool through the sulfuric acid distributor 2, and left to stand for 10 hours. The tank 7 and the co-solvent storage tank 8 are simultaneously metered and discharged, and the flow rates are 5000L / h, 1250L / h, and 750L / h respectively. The three raw materials are mixed in the buffer 6 and then enter the continuous tubular reactor 9 for continuous reaction. The total volume of the tubular reactor is 10000L, and there are 200 microporous baffles 10 inside it. The whole reaction process is about 2.5 hours. , put acid water every 0.5h, repeat 4 times to get crude methyl ester,...

Embodiment 2

[0038] Acidified oil (30% triglyceride, 70% fatty acid) is 10 tons, unloaded to the raw material pool 4 for pretreatment, the steam produced by the steam boiler 3 is passed into the raw material pool, the temperature is raised to 80°C for heat preservation, and 250KG concentrated sulfuric acid comes from Sulfuric acid storage tank 1 is evenly sprayed onto the surface of the raw material oil via distributor 2, and left to stand for 7 hours. The upper layer of pretreated oil is extracted to the pretreated oil temporary storage pool 5, and then from the pretreated oil temporary storage pool 5, the methanol storage tank 7, and the co-solvent The storage tank 8 measures and discharges the material at the same time, and the flow rates are 5000L / h, 1500L / h, and 600L / h respectively. After being mixed in the mixing buffer 6, the three raw materials enter the continuous tubular reactor 9 for continuous reaction. The continuous tubular reactor The total volume is 15,000L, and there are 30...

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Abstract

A preparation method of biodiesel is carried out according to the following steps: pretreatment of waste oils and fats is carried out; esterification reaction is carried out; three raw materials, namely oil, methanol and a cosolvent, are pretreated and measured by a metering pump and are fed into a buffer; the three raw materials are pumped into a continuous tubular reactor; the materials react during the flow process and the process lasts for 1-3h; separation is performed; decolouring is carried out without heating, specifically sending crude methyl esters into a decolouring tank to undergo filtering and decolouring with white clay so as to obtain a product a; and decolouring and degassing are carried out with heating, specifically sending crude methyl esters into the decolouring tank to react with white clay, heating the decolouring tank by the use of steam at the temperature of 70-80 DEG C and keeping the temperature for 1-3h so as to obtain a product b. The preparation method has the following advantages: heating and stirring are not required during the esterification reaction process so as to highly efficiently save energy; the whole process is carried out in the environment of low temperature and normal pressure, thus leading to low energy consumption and high utilization rate and being energy saving and environmentally friendly; and equipment is simple, cost is low, construction cycle is short, and dilatancy is strong.

Description

technical field [0001] The invention relates to the field of new energy, in particular to a method for preparing biodiesel from waste oil, and belongs to the field of biodiesel preparation. Background technique [0002] Biodiesel is a mixed fatty acid methyl ester obtained by esterification of waste oil (mainly composed of triglycerides and higher fatty acids) with methanol. [0003] At present, the preparation process of biodiesel is divided into acid method, alkali method, acid-base method, enzymatic method, supercritical method, etc. according to the different catalytic esterification methods in the reaction process. These methods all include the following two processes: [0004] First, during the esterification reaction, oleyl alcohol has a two-phase immiscibility phenomenon, and it is in a state of upper and lower stratification after standing. Measures need to be taken to expand the contact area between the two, accelerate the reaction rate, and improve the reaction co...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C11C3/00C11C3/04C10L1/02
CPCY02E50/13Y02E50/10
Inventor 王洪李鸿鹏冯立艳冯立光闻广明
Owner TANGSHAN JINLIHAI BIODIESEL
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