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Esterification and ester interchange reaction method of biodiesel

A technology of transesterification reaction and biodiesel, which is applied in the fields of biofuel, fatty acid esterification, petroleum industry, etc., can solve the problems of complicated product purification, high reaction pressure and temperature, affecting the yield and quality of biodiesel, etc.

Inactive Publication Date: 2016-12-07
上海中器环保科技有限公司 +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, chemical synthesis of biodiesel has the following disadvantages: the reaction temperature is high and the process is complicated; excessive methanol is used in the reaction process, and the subsequent process must have a corresponding alcohol recovery device, the treatment process is complicated, and the energy consumption is high; Free fatty acids will seriously affect the yield and quality of biodiesel; the purification of products is complicated, and the esterification products are difficult to recover; the by-products generated by the reaction are difficult to remove, and the use of acid and alkali catalysts produces a large amount of waste water, and the discharge of waste acids and lyes is easy to harm the environment cause secondary pollution
However, there are still some problems to be solved urgently in the preparation of biodiesel by biological enzyme method: lipase is effective for the esterification or transesterification of long-chain fatty alcohols, but the conversion rate of short-chain fatty alcohols (such as methanol or ethanol, etc.) is low, Generally only 40% to 60%; methanol and ethanol have certain toxicity to enzymes, which are easy to inactivate enzymes; by-product glycerol and water are difficult to recover, not only for product formation, but also glycerol is toxic to enzymes; short-chain fats The presence of alcohol and glycerol affects the reactivity and stability of the enzyme, greatly shortening the service life of the immobilized enzyme
The inventive method has a certain limitation on the acid value range of the raw material oil, and is not suitable for the raw material oil with an acid value less than 50mgKOH / g, and the reaction pressure and temperature are relatively high, and the reaction time is relatively long

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0025] The details are as follows: (1) Methanol is heated and pressurized to 84°C, 0.2MPa through a methanol vaporizer, and injected into the reaction tower by diffusion from the bottom of the reaction tower; (2) Grease raw materials are preheated to 80°C from the top of the reaction tower Spray into the reaction tower at a flow rate of 30L / min to keep the temperature in the reaction tower at 84℃ and pressure at 0.2MPa; (3) 3 sieve trays are installed in parallel and equidistant to the direction of the grease falling. The pore size is 10mm, and the opening rate of the sieve tray is 5%; (4) The pressure of each sieve tray is monitored by a pressure gauge, and the thickness of the grease accumulation on the sieve tray is adjusted to 10mm; (5) Excess methanol enters the methanol recovery tower from the top outlet of the reaction tower, and then enters the methanol vaporizer for heating and pressurization, and then enters the reaction tower for recycling; (6) After the reaction is c...

Embodiment 2

[0027] The details are as follows: (1) Methanol is heated and pressurized to 112.5°C, 0.5MPa through a methanol vaporizer, and injected into the reaction tower by diffusion from the bottom of the reaction tower; (2) Grease raw materials are preheated to 100°C from the top of the reaction tower Spray into the reaction tower at a flow rate of 65L / min, keep the temperature in the reaction tower at 112.5°C and the pressure at 0.5MPa; (3) 6 sieve trays are installed in parallel and equidistant perpendicular to the direction in which the grease falls. The pore size is 30mm, and the opening rate of the sieve tray is 7.5%; (4) The pressure of each sieve tray is monitored by a pressure gauge, and the thickness of grease accumulation on the sieve tray is adjusted to 50mm; (5) Excessive Methanol enters the methanol recovery tower from the top outlet of the reaction tower, and then enters the methanol vaporizer for heating and pressurization, and then enters the reaction tower for recycling...

Embodiment 3

[0029] The details are as follows: (1) Methanol is heated and pressurized to 138°C, 1.0MPa through a methanol vaporizer, and injected into the reaction tower by diffusion from the bottom of the reaction tower; (2) Grease raw materials are preheated to 120°C from the top of the reaction tower Spray into the reaction tower at a flow rate of 100L / min, keep the temperature in the reaction tower 138℃, and pressure 1.0MPa; (3) 9 sieve trays are installed in parallel and equidistant perpendicular to the direction in which the grease falls. The opening rate of the sieve tray is 10%; (4) The pressure of each sieve tray is monitored by a pressure gauge, and the thickness of the grease accumulation on the sieve tray is adjusted to 90mm; (5) The excess methanol The top outlet of the reaction tower enters the methanol recovery tower, and then enters the methanol vaporizer for heating and pressurization, and then enters the reaction tower for recycling; (6) After the reaction is completed, th...

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Abstract

The invention discloses an esterification and ester interchange reaction method of biodiesel. The method is characterized in that methanol is heated and pressurized by a methanol gasifier, the gasification temperature of 84-220 DEG C and the pressure of 0.2-5.5 MPa make methanol be in a near subcritical state, and the obtained methanol gas is injected to a reaction tower in the above state from the bottom of the reaction tower through adopting a porous pipeline; raw material oil is preheated to 80-120 DEG C through a heater, and the preheated oil is sprinkled to the reaction tower at a certain flow velocity from the top end of the reaction tower; and the temperature of 84-220 DEG C and the pressure of 0.2-5.5 MPa in the reaction tower are kept and controlled, and allow methanol to be in a subcritical state and make the raw material oil be miscible with methanol, so a two-phase chemical reaction under routine reaction conditions becomes a single-phase chemical reaction in order to solve the interphase mass transfer problem. The method has the advantages of fast reaction speed, high esterification and ester interchange efficiency, and no addition of catalysts in the reaction process.

Description

Technical field [0001] The invention belongs to the technical field of biodiesel production, and specifically relates to a method for esterification and transesterification of biodiesel. Background technique [0002] Biodiesel refers to fatty acid monoalkyl esters obtained by transesterification of animal and vegetable oils and alcohols (methanol or ethanol), the most typical being fatty acid methyl esters. Compared with traditional petrochemical energy, its sulfur and aromatics content is low, the flash point is high, the cetane number is high, and it has good lubricity. It can be partially added to petrochemical diesel, so biodiesel is a real green diesel. [0003] At present, the methods for industrialized production of biodiesel include chemical synthesis and bioenzyme synthesis. The chemical synthesis of biodiesel uses oil and methanol or ethanol and other low-carbon alcohols, and uses acidic or alkaline catalysts for esterification or transesterification. , Generate the corr...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C11C3/04C11C3/10C10L1/02
CPCY02E50/10
Inventor 杨建斌张学旺徐世杰
Owner 上海中器环保科技有限公司
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