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Using a life cycle assessment methodology for the analysis of two - - PowerPoint PPT Presentation

Using a life cycle assessment methodology for the analysis of two treatment systems of food-processing industry wastewaters L. Maya-Altamira* , A.Baun*, M.Hauschild** and J.E.Schmidt* *Institute of Environment & Resources, DTU **Department


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Using a life cycle assessment methodology for the analysis of two treatment systems of food-processing industry wastewaters

  • L. Maya-Altamira*, A.Baun*, M.Hauschild** and

J.E.Schmidt*

*Institute of Environment & Resources, DTU **Department of Manufacturing Engineering and Management, DTU

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The problem

Alternative: introduce a pre-treatment unit to cope with high loads. Criteria needed: Evaluate technologies by environmental & technical considerations. The effect of wastewater composition assessed. FPI wastewaters conventionally treated in municipal Activated Sludge (AS) Systems in Denmark. FPI ww introduce high organic loads: higher consumptions (oxygen, electricity, ancillaries) & higher emissions (sludge).

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The need

To have a flexible tool to quantify the inputs &

  • utputs that are relevant for the life cycle

assessment of wastewater treatment systems for food-processing industry streams.

Aggregated in a set of indicators that assess technical & environmental performance Represented by two mature technologies: Activated Sludge & Anaerobic Tank Reactor Effect of switching ww stream

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The assessment

Focus on:

  • a. System’s use stage.
  • b. Effect of individual streams.

Functional unit: 1 volumetric Person Equivalent (P.E.) = 0.2 m3/d.

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System boundaries

BACKGROUND SYSTEM: Generic models: Databases & literature data. Trace materials, predict process’ requirements & emissions. FOREGROUND SYSTEM: Process’ specific models: Efficiencies & consumptions dependent on ww composition & volume. Predict process’ requirements, emissions, & efficiencies.

Effluents Effluents Waste Pet food wastewaters Input Vector Fish meals wastewaters Input Vector Ancillaries & electricity Input Vector

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System boundaries

Inputs/outputs of foreground system were modeled & aggregated 1 day after a steady-state operation was achieved.

Ancillaries & electricity Wastewater streams

Ancillary Products Production Energy Production Pasteurisation Agricultural spread Dewatering Renewable Energy Production Fertiliser Production Renewable District Heating Production Mesophilic Anaerobic Influent Discharge S econdary S ettler Nitrification Denitrification Denitrification Nitrification

Waste Effluent

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Scenarios

FOREGROUND SYSTEM: Activated sludge plant

Fish meals summer

FOREGROUND SYSTEM: Activated sludge plant

Fish meals winter

FOREGROUND SYSTEM: Activated sludge plant

Pet food non-pre

FOREGROUND SYSTEM: Activated sludge plant

Pet food pretreated

FOREGROUND SYSTEM: Anaerobic digestion + AS plant

Fish meals summer

FOREGROUND SYSTEM: Anaerobic digestion + AS plant

Fish meals winter

FOREGROUND SYSTEM: Anaerobic digestion + AS plant

Pet food non-pre

FOREGROUND SYSTEM: Anaerobic digestion + AS plant

Pet food pretreated

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Influent input to system

Influent content (kg d-1 PE-1)

0.00 0.25 0.50 0.75 1.00 Pet non pre Pet pre Fish winter Fish summer

Influent content (COD/TAN ratio)

5 10 15 Pet non pre Pet pre Fish winter Fish summer

COD TAN

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LCIA – Normalized Ressource Consumption (EDIP 97)

0,0E+00 2,0E+02 4,0E+02 6,0E+02 8,0E+02 1,0E+03 1,2E+03

mPEWDK04

Pet Non pre Pet Pre Fish Winter Fish Summer Pet Non pre Pet Pre Fish Winter Fish Summer Activated sludge Anaerobic + AS

SCENARIOS

Resources consumption

Zinc Nickel Natural gas Manganese Lignite Iron Hard coal Crude oil Copper Aluminum 2 4 6 8 10 12

mPEWDK04

Pet Non pre Pet Pre Fish Winter Fish Summer Anaerobic + AS

SCENARIOS

Resources consumption

Zinc Nickel Natural gas Manganese Lignite Iron Hard coal Crude oil Copper Aluminum

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LCIA – Normalized Environmental Impacts (EDIP 97)

10 20 30 40 50 60 70

mPEWDK94

Pet Non pre Pet Pre Fish Winter Fish Summer Pet Non pre Pet Pre Fish Winter Fish Summer Activated sludge Anaerobic + AS

SCENARIOS

Environmental Impacts

Photochemical oxidant (low NOx) Ozone depletion Nutrient enrichment Global warming (100 years) EDIP Human toxicity water EDIP Human toxicity soil EDIP Human toxicity air EDIP ecotox water chronic EDIP ecotox water acute EDIP ecotox soil cronic Acidification 0,0 0,3 0,5 0,8 1,0 1,3 1,5 1,8 2,0 mPEWDK94 Pet Non pre Pet Pre Fish Winter Fish Summer Anaerobic + AS

SCENARIOS

Environmental Impacts

Photochemical oxidant (low NOx) Ozone depletion Nutrient enrichment Global warming (100 years) EDIP Human toxicity water EDIP Human toxicity soil EDIP Human toxicity air EDIP ecotox water chronic EDIP ecotox water acute EDIP ecotox soil cronic Acidification

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LCI indicators

Energy indicators

AS Pet Non pre AS Pet Pre AS Fish Winter AS Fish Summer

  • 5

5 10 15

AS+AD Pet Non pre AS+AD Pet Pre AS+AD Fish Winter AS+AD Fish Summer

Electricity consumption pausterisation (kWh d-1 PE-1) Methane produced (kg d-1 PE-1) Ancillary oxygen consumed (kg d- 1 PE-1) Energy balance_foreground: Consumption - Production (kWh d-1 PE-1)

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LCI indicators

Removal efficiencies

0% 20% 40% 60% 80% 100% AS Pet non pre AS Pet pre AS Fish winter AS Fish summer AS+AD Pet non pre AS+AD Pet pre AS+AD Fish winter AS+AD Fish summer TAN Removal Efficiency COD Removal Efficiency TSS Removal Efficiency

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Conclusions

  • Energy related LCI indicators exerted the greatest influence on the systems

assessed.

  • AS plants caused the greatest LC Ressource Consumptions & Environmental

Impacts.

  • Anaerobic digestion as an alternative for pre-treatment unit.
  • Pasteurisation of sludge prior disposal (fertiliser) is critical in the assessment.
  • The removal of N from the wastewater is overcome by the nutrient enrichment

caused by the power production processes at the activated sludge scenarios.

  • Differences in ww compositions affected the LCA of ww treatment systems,

particularly for AS & AD systems.

  • This flexible tool can help on the LCA of wastewater treatment systems of FPI

ww.

  • Important to integrate technical indicators in the LCA of such ww treatment

systems.

  • Important to aggregate inventory data with sufficient level of detail for scenario

analysis of FPI ww in a LCA context.

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Thanks to the National Minister of Science & Technology of Mexico for its funding to this project and to Arovit Pet Food & Fiske Fiskerness Industries for providing the wastewater samples.

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Thanks for your attention ! Any question?

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Modeling References

Henze et al. (1987) Activated sludge model No.1, IWAQ Scientific and Technical Report No.1, London, UK. Batstone et al. (2002) Anaerobic digestion model No.1, IWA Scientific and Technical Report No.13, London, UK. Copp J.B. (2002) The COST Simulation Benchmark: Description and simulator manual, COST Actions 624 & 682 Report, COST European Cooperation in the development of Science and Technology. Copp et al.(2003) Towards an ASM1-ADM1 state variable interface for plant-wide wastewater treatment modeling. 76th Annual WEF Conference and Exposition, Oct.11-15, Los Angeles USA. Vanrolleghem et al.(1996) Integration of wastewater treatment plant design and operation-a systematic approach using cost functions, Water Science and Technology 34(3-4), 159-171. Hauschild M. & Wenzel H.(1998) Environmental Assessment of Products, Volume 2, Scientific Background, Chapman & Hall.