METHOD FOR MAKING BIO-OIL AND CARBIDE USING BIO-MASS

PURPOSE: A bio-oil and carbide manufacturing method using biomass are provided use crude glycerin as a heating material for rapidly producing bio-oil from the biomass. CONSTITUTION: A bio-oil and carbide manufacturing method using biomass comprises the following: mixing 50-80 parts of biomass by wei...

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Bibliographische Detailangaben
1. Verfasser:	GU, JA SUNG
Format:	Patent
Sprache:	eng ; kor
Schlagworte:	ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE ORUNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL CHEMISTRY CRACKING HYDROCARBON OILS DESTRUCTIVE DISTILLATION OF CARBONAGEOUS MATERIALS FORPRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS FERTILISERS FIRELIGHTERS FUELS FUELS NOT OTHERWISE PROVIDED FOR LIQUEFIED PETROLEUM GAS LUBRICANTS MANUFACTURE THEREOF METALLURGY MINERAL WAXES NATURAL GAS ORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C, e.g. FERTILISERS FROM WASTE OR REFUSE PEAT PETROLEUM, GAS OR COKE INDUSTRIES PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVEHYDROGENATION, OLIGOMERISATION, POLYMERISATION RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, ORGASES REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS REFORMING OF NAPHTHA SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BYSUBCLASSES C10G, C10K TECHNICAL GASES CONTAINING CARBON MONOXIDE
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Beschreibung
Zusammenfassung:	PURPOSE: A bio-oil and carbide manufacturing method using biomass are provided use crude glycerin as a heating material for rapidly producing bio-oil from the biomass. CONSTITUTION: A bio-oil and carbide manufacturing method using biomass comprises the following: mixing 50-80 parts of biomass by weight and 20-50 parts of crude glycerin by weight in a reactor(10); heating the inserted materials for evaporating steam; maintaining the anoxic or low oxygen condition side the reactor, and directly heating the crude glycerin for heat-decomposing the biomass; transferring gas generated inside the reactor to a first cooler(30), and transferring carbide which is not heat-decomposed to a carbide storage tank(20); cooling the gas in the first cooler, and decompress-evaporating the condensed components using a vacuum evaporator(35); transferring gas generated by the decompress-evaporating process to a second cooler(40); and cooling and condensing the gas to obtain bio-oil.