edf r&d wp2 : energetic aspects of urban waste treatments claire lecointe, charlotte barbut 3 rd...
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EDF R&D
WP2 : Energetic aspectsof urban waste treatmentsClaire Lecointe, Charlotte Barbut
3rd AWAST WorkshopJune 20-21st, 2002, Trondheim
ECO-EFFICIENCY AND INDUSTRIAL PROCESSES
PLAN
Introduction Inventory of energy data in waste
management Incineration model Biogas energy recovery model
Conclusion
ECO-EFFICIENCY AND INDUSTRIAL PROCESSES
Introduction
D3 : Comparable energetic data for the different channels and for the contractor countries
D4 : Energetic models
EDF R&D
Inventory of energy data
ECO-EFFICIENCY AND INDUSTRIAL PROCESSES
Negative points :few data about energy consumption
Transport : only available data are from the French Agency for the Environment and the Energy Control (ADEME)
Composting : only available data are from LQARS. They are low according to some general values (16,3 kWh/t compared to 20 to 100 kWh/t)
Sorting : no data
ECO-EFFICIENCY AND INDUSTRIAL PROCESSES
Positive points :inventory of energy production
Incineration :energy production and self-consumption reports easily available
data like temperature, pressure… only available for some models of French installations with our own software
Methanisation and landfill : energy production and self-consumption reports easily available
But information differs a lot from country to country and is not complete for all countries
EDF R&D
Incineration model
ECO-EFFICIENCY AND INDUSTRIAL PROCESSES
Incineration flows with the model entrieswater (H2O 1)
temperaturepressureenthalpyentropyflow
FURNACE
BOILER
Turbine andAlternator Group
airair excessdensity
wastecompositionflow
smokes 1temperaturepressurecomponents enthalpycomponents heat capacitycomponents density
smokes 2temperaturepressurecomponents enthalpycomponents heat capacity
steam 1 (H2O 2)temperaturepressureenthalpyentropy
steam 2 (H2O 3)temperaturepressureenthalpyentropy
electricity
ECO-EFFICIENCY AND INDUSTRIAL PROCESSES
Strasbourg incineration plant results
electricity yield = 5,1%
thermal yield = 25,0%
exergetic power (MW) yield
combustible mixture 29.2
smokes 1 19.9
smokes 2 7.5
water (H2O 1) 1.2
steam 1 (H2O 2) 10.1
steam 2 (H2O 3) 8.5
electricity production 1.48
furn
ace
bo
iler
TAG
92.5%
71.8%
68.2%exCM = LHVwaste / [1 + air (1+) VA]
exS = h - Tambiant cp ln(TS/Tambiant)
exH2O = h - Tambiant s
F = MS*exS1 / [(MW+MA)*exCM]
B = MH2O(exH2O2- exH2O1) / [MS(exS2- exS1)]
T = We / [MH2O(exH2O3- exH2O2)]
e = We / [(MW+MA)*exCM]
th = MH2O(exH2O3- exH2O1) / [(MW+MA)exCM]
ECO-EFFICIENCY AND INDUSTRIAL PROCESSES
Strasbourg incineration plant results
electricity yield = 5,1%
thermal yield = 25,0%
exergetic power (MW) yield
combustible mixture 29.2
smokes 1 19.9
smokes 2 7.5
water (H2O 1) 1.2
steam 1 (H2O 2) 10.1
steam 2 (H2O 3) 8.5
electricity production 1.48
furn
ace
bo
iler
TAG
92.5%
71.8%
68.2%
EDF R&D
Biogas energy recovery model
ECO-EFFICIENCY AND INDUSTRIAL PROCESSES
biogas production
>20% CH4
>100 m3/h
>40% CH4
>400 m3/h
heat production
electricity production
burner, furnace or boiler
biogas engine
boiler + steam turbine
<1 MWe
(~700 m3/h)
>1 MWe
(700 to 800 m3/h
with LHV = 5 kWh/Nm3)
if
if
then then
with then then
The different ways of biogas energy recovery
ECO-EFFICIENCY AND INDUSTRIAL PROCESSES
Energy recovery with biogas engine
exergy = thermal + physical exergy electricity production linked to mechanical energy provided
by the piston mechanical energy provided during compression,
expansion and combustion for a diesel engine study of thermal exergy similar to the incineration case
water (H2O1)
smokes 3smokes 2
electricity
smokes 1combustionspace
piston(expansion) +
alternator heatexchanger
hot water or steam(H2O2)
piston(compression)
air air
biogas
ECO-EFFICIENCY AND INDUSTRIAL PROCESSES
Conclusion
Delay for both deliverables Incineration model : OK Biogas energy recovery model : at the
moment the only available data for biogas engine are theoretical
Problem with biogas production model for methanisation and landfill
Participation in Orleans Case Study Greenhouse gases study
ECO-EFFICIENCY AND INDUSTRIAL PROCESSES
Financial statementsmost of the cost is personal cost
Personal hours on project
Contract Statement
2001 500 930
2002 850 ~ 1700
2003 1000 ?