Intermittent reaction device for producing biodiesel by catalyzing illegal cooking oil through liquid enzyme

The utility model discloses an intermittent reaction device for producing biodiesel by catalyzing illegal cooking oil through liquid enzyme, and solves the technical problems of high reaction temperature, long reaction time and high acid value of a product in the existing biodiesel production of the...

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Bibliographische Detailangaben
Hauptverfasser:	YE BIN, YE ZHENGQIANG, XU XING, SHI SHUXUN
Format:	Patent
Sprache:	chi ; eng
Schlagworte:	ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE ORUNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL ANIMAL AND VEGETABLE OILS, FATS, FATTY SUBSTANCES AND WAXES APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY BEER BIOCHEMISTRY CANDLES CHEMISTRY DETERGENTS ENZYMOLOGY ESSENTIAL OILS FATS, OILS OR FATTY ACIDS BY CHEMICAL MODIFICATION OF FATS,OILS, OR FATTY ACIDS OBTAINED THEREFROM FATTY ACIDS FROM FATS, OILS OR WAXES FATTY ACIDS THEREFROM FIRELIGHTERS FUELS FUELS NOT OTHERWISE PROVIDED FOR LIQUEFIED PETROLEUM GAS LUBRICANTS METALLURGY MICROBIOLOGY MUTATION OR GENETIC ENGINEERING NATURAL GAS PEAT PERFUMES PETROLEUM, GAS OR COKE INDUSTRIES PRODUCING (PRESSING, EXTRACTION), REFINING AND PRESERVINGFATS, FATTY SUBSTANCES (e.g. LANOLIN), FATTY OILS AND WAXES,INCLUDING EXTRACTION FROM WASTE MATERIALS SPIRITS SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BYSUBCLASSES C10G, C10K TECHNICAL GASES CONTAINING CARBON MONOXIDE VINEGAR WINE
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Beschreibung
Zusammenfassung:	The utility model discloses an intermittent reaction device for producing biodiesel by catalyzing illegal cooking oil through liquid enzyme, and solves the technical problems of high reaction temperature, long reaction time and high acid value of a product in the existing biodiesel production of the illegal cooking oil. The device comprises a liquefying enzyme main tank, a first auxiliary tank, a second auxiliary tank and a vacuum dryer, wherein the liquefying enzyme main tank is used for hydrolyzing gutter oil to generate fatty acid methyl ester; the first auxiliary tank and the second auxiliary tank are respectively led out from the liquefying enzyme main tank, are connected into the liquefying enzyme main tank and are used for liquid enzyme circulation; the vacuum dryer is led out from the liquefying enzyme main tank; the immobilized enzyme reaction device is connected out of the vacuum dryer and is used for secondary reaction of the primary product; the liquefied enzyme main tank is respectively connected