Optimization of Reaction Conditions of Two-Step Batch Operation for Biodiesel Fuel Production Using KOH Catalyst
スポンサーリンク
概要
- 論文の詳細を見る
For the biodiesel-fuel production by methanolysis, the reaction mixture is composed of a methyl-ester phase and a glycerol phase. One of the reactants, triglyceride, is mainly contained in the ester phase. The other reactant, methanol, is easily dissolved in the glycerol phase. Therefore, the methanol in the system is not effectively used for the reaction due to interface mass transfer resistance. An excess amount of methanol is required to increase the conversion in single-step operation. Since the glycerol phase is removed during the operation, a two-step batch operation can effectively intensify the process. In the present study, the optimal operating conditions to increase the conversion are obtained for the methanolysis of rapeseed oil using a KOH catalyst. The distribution ratio of methanol addition in the first step was about 0.8, which is confirmed by a simple reaction model.
- 社団法人 化学工学会の論文
- 2010-03-01
著者
-
MATAKI YUKO
Department of Surgical Oncology, Digestive Surgery, Graduate School of Medicine, Kagoshima Universit
-
KAI Takami
Department of Applied Chemistry and Chemical Engineering, Kagoshima University
-
NAKAZATO Tsutomu
Department of Biological and Chemical Engineering, Gunma University
-
Takanashi Hirokazu
Department Of Applied Chemistry Oita University
-
Kai Takami
Department Of Applied Chemistry And Chemical Engineering Kagoshima University
-
Nakazato Tsutomu
Department Of Applied Chemistry And Chemical Engineering Kagoshima University
-
Mataki Yuko
Department Of Applied Chemistry And Chemical Engineering Kagoshima University
-
Takanashi Hirokazu
Department Of Bioengineering Kagoshima University
関連論文
- A case of leptomeningeal carcinomatosis from esophageal basaloid carcinoma diagnosed by quantitative reverse transcription-polymerase chain reaction for carcinoembryonic antigen
- Application of Fast X-ray CT Scanner to Visualization of Bubbles in Fluidized Bed
- Dynamic Evaluation of Membrane-Electrode Assembly in Operation of a Direct Methanol Fuel Cell by Simultaneous Measurements of Crossovers of Methanol and CO_2
- Efficacy of anatomic resection vs nonanatomic resection for small nodular hepatocellular carcinoma based on gross classification
- Hydrolysis Rates of Olive Oil by Lipase in a Monodispersed O/W Emulsion System Using Membrane Emulsification
- PREPARATION OF GPC PACKED POLYMER BEADS BY A SPG MEMBRANE EMULSIFIER
- Hydrolysis of Olive Oil with Lipase in a "VibroMixer"
- Hydrolysis Kinetyics of Olive Oil with Lipase in a Transfer Cell
- PERMEABILITY CONTROL OF ACTIVE AGENT FROM POLYMERIC MICROCAPSULES BY COATING OF GELATIN/GUM ARABIC MEMBRANE
- Preparation of Highly Active Methanol Steam Reforming Catalysts from Glassy Cu-Zr Alloys with Small Amount of Noble Metals
- Hydrogenation of Benzene over Catalyst Prepared from Amorphous Pt-Zr Alloy
- Removal of Selenium (VI) from Simulated Wet Flue Gas Desulfurization Wastewater Using Photocatalytic Reduction
- Semi-dry Process for Production of Very Fine Calcium Carbonate Powder by a Powder-Particle Spouted Bed
- Total Solid Entrainment Rate in a Circulating Powder-Particle Fluidized Bed
- Entrainment Rates and Elutriation Rate Constants of Bed Particles and Group C Fine Powder in a Fluidized Bed and in a Circulating Fluidized Bed
- Optimization of Reaction Conditions of Two-Step Batch Operation for Biodiesel Fuel Production Using KOH Catalyst
- MEASUREMENT AND PREDICTION OF THE SURFACE TENSION OF NITROGEN + OXYGEN AND NITROGEN + OXYGEN + ARGON SYSTEM
- Asymptomatic Somatostatinoma of the Pancreatic Head : Report of a Case
- Analysis of Acclimation Behavior against Nitrification Inhibitors in Activated Sludge Processes
- PREPARATION AND DEMULSIFICATION OF W/O EMULSION CONTAINING AQUEOUS ALKALINE SOLUTION
- REACTIVE EXTRACTION OF CEPHALOSPORIN C
- Penetration of fine cohesive powders through a powder-particle fluidized bed
- Methanol Diffusion through a Porous Plate in Anode Backing of a Passive Direct Methanol Fuel Cell under Closed Circuit Conditions
- Elimination of Defluidization Caused by Reactions Involving a Volume Reduction in a Fluidized Catalyst Bed and Improvement of Fluidization by Two-Stage Feeding
- Relationship between Apparent Bed Viscosity and Fluidization Quality in a Fluidized Bed with Fine Particles
- Approach to Zero Emission Processes in Food Industry : - Case Study for Soy-Sauce Production Process -
- A phase II study of oral S-1 with concurrent radiotherapy followed by chemotherapy with S-1 alone for locally advanced pancreatic cancer
- Continuous Production of N–F-Codoped Titanium Oxide Photocatalyst Powders via Drip Pyrolysis in a Fluidized Bed under Reduction Conditions
- Production of Chloro-5-hydroxy-2-nitrobenzoic Acid through Chlorination of 3-Methyl-4-nitrophenol, a Typical Hydrolysate of Fenitrothion
- Effect of internal baffles on conversion of hydrogen chloride oxidation and pressure fluctuations in a fluidized catalyst bed.
- Detection of Fenitrothion and its Degradation Product 3-Methyl-4-nitrophenol in Water Environment
- Analytical Method for Simultaneous Determination of Pesticides and Pesticide Transformation Products in Water Environment Using GC-MS and LC-MS/MS
- Moisture Absorption Characteristics of Porous Calcium Oxide Powders Produced by Calcination of Pulverized Limestone with Inorganic Salts Using a Powder-Particle Fluidized Bed
- Continuous production of hydroxyapatite powder by drip pyrolysis in a fluidized bed
- Effect of the Addition of Chelators on the Acute Toxicity of Some Heavy Metals to Freshwater Organisms
- Effects of Increase in Gas Volume on the Fluidization Properties in Fluidized Bed Reactors
- Methanation of carbon monoxide by a fluidized catalyst bed.