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A method for directly extracting fatty acid methyl esters from microalgae wet biomass

A fatty acid methyl ester and biomass technology, applied in the direction of fatty acid esterification, fat production, fatty acid production, etc., can solve the problem of high product cost, achieve scientific design, reasonable process, and improve simplicity

Inactive Publication Date: 2018-09-11
山东省海洋资源与环境研究院
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] The purpose of the present invention is to solve the problem of high product cost in the prior art, and provide a method for extracting fatty acid methyl esters through acid-base combined transesterification

Method used

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  • A method for directly extracting fatty acid methyl esters from microalgae wet biomass
  • A method for directly extracting fatty acid methyl esters from microalgae wet biomass
  • A method for directly extracting fatty acid methyl esters from microalgae wet biomass

Examples

Experimental program
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Effect test

Embodiment 1

[0029] Centrifuge at 4000rpm for 10min to collect the cell density to 10 7 100 mL of Phaeodactylum tricornutum algae liquid per mL. After removing the supernatant, about 0.1 g of microalgae wet biomass is obtained. The water content is determined to be 88%. Add 0.5 mL n-hexane and 1 mL mass fraction to the centrifuge tube It is a 2% methanol solution of sodium hydroxide, transferred to a sealed test tube, heated to 80°C, kept at a constant temperature for 20 minutes, cooled for 5 minutes to room temperature after the reaction, and then added 1 mL of 10% acetyl chloride methanol solution and heated to 80 Keep the temperature at a constant temperature for 20 minutes. After the reaction, cool for 5 minutes to room temperature. Add 0.5 mL of n-hexane and 1 mL of potassium carbonate solution with a mass fraction of 6%, shake and stand. After stratification occurs, all the upper liquid is transferred to the rotary evaporator. Heat to 68℃, distill the n-hexane out, and the remaining li...

Embodiment 2

[0031] Centrifuge at 4500rpm for 10min to collect the cell density to 10 7 100 mL of Isochrysis sphaeroides per mL. After removing the supernatant, about 0.1 g of microalgae wet biomass is obtained. The water content is determined to be 90%. Add 0.5 mL of n-hexane and 1 mL of mass fraction to the centrifuge tube. Transfer 2% methanol solution of sodium hydroxide to a sealed test tube, heat to 80℃, keep constant temperature for 20min, after the reaction, cool for 5min to room temperature, then add 1mL 10% acetyl chloride methanol solution and heat to 80℃ , Constant temperature for 20 minutes, cooling for 5 minutes to room temperature after the completion of the reaction, adding 0.5 mL of n-hexane and 1 mL of potassium carbonate solution with a mass fraction of 6%, shaking and standing, after stratification, all the upper liquid is transferred to the rotary evaporator, heating When the temperature reaches 68°C, the n-hexane is distilled out, and the remaining liquid is fatty acid ...

Embodiment 3

[0033] In this example, glyceryl heptadecanoate is used as the test sample. Most of the fatty acids in microalgae are in the form of triacylglycerides, and glyceryl heptadecanoate is one of them. Therefore, by measuring glyceryl heptadecanoate The conversion rate of ester into methyl heptadecanoate can further prove the accuracy of the present invention. Take 0.5 mL of glyceryl heptadecanoate in toluene solution (containing 0.1 mg of glyceryl heptadecanoate, equivalent to about 0.1 mg of methyl heptadecanoate) in a test tube, and add 0.5 mL of n-hexane and 1 mL of mass 2% sodium hydroxide methanol solution, after sealing, heat to 80℃, keep the temperature for 20min, after the reaction, cool for 5min to room temperature, then add 1mL 10% acetyl chloride methanol solution, heat to 80℃, keep the temperature for 20min After the reaction, cool for 5 minutes to room temperature, add 0.5 mL of methyl nonadecanate n-hexane solution (containing 0.1 mg of methyl nonadecanate) and 1 mL of...

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Abstract

The invention relates to a method for extracting fatty acid methyl esters from microalgae wet biomass through acid-base combined transesterification, and belongs to the field of biochemical industry. The method obtains the crude extract of fatty acid methyl ester from the microalgae wet biomass with water content below 90% through a reasonable ratio of alkaline catalyst and acidic catalyst and joint catalysis, and then extracts fatty acid methyl ester by distillation. Specific operation steps: 1) collecting microalgal wet biomass; 2) base catalysis; 3) acid catalysis; 4) neutralization reaction; 5) distillation. The advantages of the invention: scientific design, reasonable process, no sticking to the wall during the transfer of microalgae, no loss of samples, no need to pre-break the wall, no need for special mechanical equipment, under normal pressure and lower reaction temperature and in the same reaction kettle. The whole process can be completed, and the yield of fatty acid methyl ester is above 95%.

Description

Technical field [0001] The invention relates to the technical field of biochemical engineering, in particular to a method for directly extracting fatty acid methyl esters from microalgae wet biomass. Background technique [0002] Microalgae is rich in oils and fatty acids. It is not only an important source of n-3 highly unsaturated fatty acids (DHA, EPA, etc.), but also biodiesel can be extracted (mainly fatty acid methyl or ethyl esters) to supplement The increasingly tense petrochemical energy. However, microalgae biomass is usually accompanied by a large amount of water. The open culture density is generally less than 1 g / L, and the closed high-density culture can only reach 30g / L, resulting in extremely high harvest and dehydration costs, which account for its production cost ( Including cultivation and harvesting) 20% to 30%. There are many types of microalgae, and the cell wall composition is complex, mainly containing cellulose, hemicellulose, lignin and other component...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C11C3/04C11C3/00C11B1/04
CPCC10L1/02C11B1/00
Inventor 乔洪金王际英张利民黄炳山王世信李宝山
Owner 山东省海洋资源与环境研究院