diesel fuel via the catalytic depolymerization - Imvemvane Logistics

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3. SYSTEM FUNCTIONALITY 3.1 Plant Summary 12 SLUDGE PLANT KDV PLANT ASH PLANT GENSET PLANT OPTIONAL DESULPHURATION PLANT 12
3. SYSTEM FUNCTIONALITY 3.2 Inputs and feedstock WASTE TREATMENT 13 INPUTS MSW (municipal solid waste) All Plastics Animal waste Mineral oils Sewage Sludge Agricultural waste Biomass cut material FEEDSTOCK Particle size: Max 25mm diameter Humidity: Max 20% weight Inorganics: Max 5% weight Calorific value Optimal mix (biomass content) Ash content OUTPUT • Diesel quality 65 “Cetan” (20% more efficient compared to the diesel of a regular gas station) • Lower freezing point aprox. -60 Cº • Distilled Water • 1-3% ash (fertilizer) binds hazardous materials PRODUCTION: 1,2 t biological mass = aprox 500L diesel depending on the water saturation. • NO chimney necesarry • NO heat pollution • NO Methane / CO2 • NO Dioxine
Page 1 and 2: DIESEL FUEL VIA THE CATALYTIC DEPOL
Page 3 and 4: 1. INTRODUCTION Inventor Dr.-Ing. C
Page 5 and 6: 1. INTRODUCTION 1.1 Problems Global
Page 7 and 8: 1. INTRODUCTION 1.2 Solution + prod
Page 9 and 10: 2. MAIN CHARACTERISTICS 2.1 Technol
Page 11: 2. MAIN CHARACTERISTICS 2.1 Technol
Page 15 and 16: 3. SYSTEM FUNCTIONALITY 3.4 Product
Page 17 and 18: 4. SCENARIOS 4.1 Industrial install
Page 19 and 20: 4. SCENARIOS 4.2 Example instalatio
Page 21 and 22: 5. ECONOMICAL FIGURES 5.2 Break Eve
Page 23 and 24: APPENDICE A: CO2 CALCULATION The KD

diesel fuel via the catalytic depolymerization - Imvemvane Logistics

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