Process for the extraction of polyhydroxyalkanoates from biomass
US-2015368393-A1 · Dec 24, 2015 · US
US10214755B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10214755-B2 |
| Application number | US-201615352849-A |
| Country | US |
| Kind code | B2 |
| Filing date | Nov 16, 2016 |
| Priority date | May 6, 2016 |
| Publication date | Feb 26, 2019 |
| Grant date | Feb 26, 2019 |
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A method to prepare functional polyester polyols by using micro-reaction device, wherein mixing ε-caprolactone/δ-valerolactone monomer with mercapto alcohol evenly with appropriate organic solution under moistureless conditions, and continuously transferring the prepared mixing solution into a micro-reaction device supported with an immobilized enzyme for polymerization to synthetize a poly (ε-caprolactone/δ-valerolactone). Compared with the prior art, the present invention achieves a continuous production by using immobilized lipase Novozyme435 as a catalyst.
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What is claimed is: 1. A method for preparing polyester polyol by using a micro-reaction device, wherein the micro-reaction device comprising a feed inlet, a micro mixer and a micro reactor connected in turn via a connecting tube; the method comprising the follow steps (1) dissolving a lactone monomer into a first organic solution; (2) dissolving a mercapto alcohol into a second organic solution; (3) mixing the solution in step (1) with the solution in step (2) into a homogeneous mixture, and pumping the homogeneous mixture into the micro-reaction device for reacting for a sufficient amount of time to produce the polyester polyol compound where the micro-reactor comprises an immobilized enzyme; and (4) recovering and purifying the polyester polyol; wherein the lactone is a δ-valerolactone) or ε-caprolactone; the polyester polyol is a mercapto functional poly (δ-valerolactone) or a mercapto functional poly (ε-caprolactone). 2. The method according to claim 1 , characterized in that, in the step (1), the lactone monomer is ε-caprolactone or δ-valerolactone, the organic solution is toluene, a tetrahydrofuran or a dichloromethane; wherein, the concentration of the lactone monomer in the mixed system acquired in the step (1) is 1-6 mol/L. 3. The method according to claim 1 , characterized in that, in the step (2), the mercapto alcohol is a 2-mercaptoethanol, a 3-mercapto-1-propanol, 4-mercapto-1-butanol or a 6-mercapto-1-hexanol, the organic solution is toluene, tetrahydrofuran or dichloromethane; wherein, the concentration of the mercapto alcohol in the mixed system acquired in step (2) is 0.01-0.6 mol/L. 4. The method according to claim 1 , characterized in that in step (3), the reaction temperature in the micro reactor is 40-140° C., and the duration of stay is 1-180 mins. 5. The method according to claim 1 , characterized in that the immobilized enzyme in step (3) is the immobilized lipase Novozyme435. 6. The method according to claim 1 , characterized in that, in step (3), the method for separation and purification is: adding methanol or hexanol or other solvent, which is soluble for monomer and mercapto-alcohol but non-soluble for the result functional polyester polyol, into the product acquired from the reaction, and precipitating them, then vacuum drying the solid portion obtained by filtering to acquire the product. 7. The method according to claim 1 , characterized in that the molar ratio of the lactone monomer and the mercapto alcohol is 5-100:1. 8. The method according to claim 1 , characterized in that, the mass ratio of the immobilized enzyme and the lactone monomer is 1:3-20.
characterised by the apparatus used · CPC title
Carrier-bound or immobilised enzymes; Carrier-bound or immobilised microbial cells; Preparation thereof · CPC title
Polyesters of hydroxy carboxylic acids · CPC title
Cross-Sectional Technologies · mapped topic
Apparatus specially designed for the use of free, immobilized or carrier-bound enzymes · CPC title
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