8- Company Profile_IES BIOGAS
-
Upload
stefan-curarari -
Category
Documents
-
view
6 -
download
1
description
Transcript of 8- Company Profile_IES BIOGAS
The biological process
PROTEINS CARBOHYDRATES FATS
AMINO ACIDS/ SUGARS/ FAT ACIDS
VOLATILE ACIDS
ACETATE / HYDROGEN
METHANE + CO2
HYDROLITIC BACTERIA
METANOGEN BACTERIA
ACETOGENIC BACTERIA
FERMENTER BACTERIA
HYDROLYSIS
FERMENTATION (ACIDOGENESIS)
FERMANTATION (ACETOGENENIS)
METHANOGENESIS (38-42 C°)
ANAEROBIC DIGESTION
The biological process
THE ANAEROBIC DIGESTION AND THE CATTLE DIGESTION
Substrates’ grinding and suspension
1° Hydrolytic phase Destruction of the easy to degrade substances
Methanation phase Transformation into Biogas (CH4 + CO2)
2° Hydrolytic phase Destruction of the no-easy to degrade substances
LOADING/ FEEDING SYSTEM
CROP & RETICULUM
OMASO ABOMASO - STOMACH
INTESTINE
DIGESTATE
Biogas: main substrates
LIVESTOCK AND AGRICULTURE
FOOD & BEVERAGE INDUSTRIES
MUNICIPALITIES
SUBSTRATES MARKETS
Organic matrices (substrates)
BIOMASS
CATTLE MANURE – 25% T.S.
BEEF CATTLE SLURRY – 8% T.S.
DIARY CATTLE SLURRY – 10% T.S.
PIG SLURRY – 5% T.S.
CORN SILAGE – 32% T.S.
CORN GRAINS – 87% T.S.
SORGHUM SILAGE – 30% T.S.
BARLEY SILAGE – 35% T.S.
Nm3 biogas /Ton as it
80-100
25-33
28-36
18-24
180-230
500-600
140- 170
150-180
Digester: features
COVERING (DOUBLE MEMBRANE)
HEATING SYSTEM
SUBMERSIBLE MIXER
DIGESTATE
BIOGAS STORAGE
INSULATION
SUBMERSIBLE MIXER
Digestate – alternative disposal ways
DIGESTATE
SEPARATOR UNIT
LIQUID FRACTION SOLID FRACTION
< 5% DRY CONTENT 27- 30% DRY CONTENT
• Fertilization/ irrigation • Aerobic treatment and unloading • Disposal into depuration plants
• Organic fertilizer
Cogenerator - CHP
• Thermal combustion engine • Synchronous alternator • Heat recovery, compound from a heat exchanger that recover the heat produced by the whole system, both from the 1st intercooler stage, the cooling water circuit, the 200°C exhausted cooling and the lubricating oil circuit.
• Electric station which allows to use the produced energy for its own consumption and/or connect to the national grid
The Biomethane is a gas derived from biogas that has undergone a process of upgrading (refining and purification), bringing the concentration of methane CH4 to exceed 98 %.
Biomethane: the next step
The advantages of bio-methane: programmable renewable energy reducing the dependence on gas
importations development of the local economy environmental sustainability closed circuit contribute to reducing the gas
emissions (greenhouse effect) maximum flexibility
Field of application: biofuel for motor vehicles put into the national gas pipeline transported and stored for
subsequent energy production even in places far away from the production site
Plant Project
1) ENTRANCE 2) PARKING 3) OFFICES 4) METHANE CABIN 5) WEIGHS 6) SQUARE 7) WAREHOUSE 8) STORE PLANTS PROTECTION 9) SERVICES ROOM
10) CANOPY 11) DRIER 12) GRAIN SILOS 13) GARAGE 14) WAREHOUSE GRAIN 15) DEPOSIT 16) SHELTER TOOLS 17) ELECTRIC ROOM 18) POST FERMENTER
19) FERMENTER 1 20) FERMENTER 2 21) BIOGAS SEAL COVERED TANK 22) NO-BIOGAS SEAL COVERED TANK 23) PUMP ROOM 24) COGENERATOR 25) OIL DEPOSIT 26) BIOGAS TREATMENT
27) BIOGAS EMERGENCY FLARE 28) PRE-STORAGE TANK 29) LOADING SYSTEM 30) SEPARATOR 31) COVERED WAREHOUSE FOR THE SOLID SEPARATE 32) SILOS SILAGE 33) RAIN WATER COLLECTING BASIN 34) PAVED SQUARE
System Data
ENERGY YIELD Annual production of electricity: 8.500.000 kWh Annual production of biogas: 4.100.000 mc Average concent. (CH4) in biogas: 52-54 % GROUP OF CO-GENERATION Manufacturer: AB Energy Model: Ecomax 10 Bio ENGINE Manufacturer: GE Jenbacher Model: J 320 GS–C25
INSTALLED ELECTRIC POWER 999 kWh TWO-STAGE PROCESS MESOPHILIC Fermenters: n.2 Ø 24 h=6m Post-fermenter: n.1 Ø 26 h=6m Biogas sealed storage tank: n.1 Ø 32 h=6m Storage tank: n.1 Ø 32 h=6m Biomass Loading: n.2 hopper 60 mc DAILY FEED TABLE Cattle slurry: 60 mc Cattle manure: 14 ton Corn silage: 30 ton Rye silage: 20 ton
TEP equivalent – avoided C02 emission
THERMAL ENERGY • 1082 Kw x 8000hours = 8,656,000 kWh/year • 8,656,000 X 8,803 x 10-5 = 762 TEP (The Rate of conversion of the heat energy in primary energy is equal to 8,803 x 10-5 TEP).
ELECTRIC ENERGY • 999 Kwh x 8400 h = 8,400,000 KWH/year • 8,400,000 X 0.187X10-3 = 1571 TEP (The conversion index of the electric energy in primary energy is equal to 0,187 x 10-3 TEP). Considering that an inhabitant consumes an average of 5300 kWh/year of electric energy, we can estimate that the plant can satisfy the energy consumption of almost 3000 inhabitants.
CO2 EMISSIONS In total, we have a production of approx. 17,056,000 kWh/year of electric and thermal energy. The generated energy is equivalent to a saving of approx. 6437 Ton of CO2 / year (considering 1 kWh386,5 g. of CO2 as indicated by the International Energy Agency.