Transcript arabwaterweek.com
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Wastewater treatment by Biofilm technology Compact Waste Water Treatment Unit Pilot Project-Tunisia.
Dr.-Eng. Noama Shareef GEA Heat Exchangers / GEA 2H Water Technologies GmbH
Summary
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Principles of municipal waste water treatment
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Biofilm technology for wastewater treatment
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Concept of a hybrid-plant for high Treatment Efficiency (compact- System) for full treatment
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Overview of the WWTP in Bent Saiden / Tunisia
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Process steps of the WWTP in Bent Saiden
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Conclusions / results
2 Mai 20
GEA Heat Exchangers / GEA 2H Water Technologies GmbH
Biofilm technology for Wastewater Treatment Purification is performed by a Biofilm:
Biofilm Systems: Bacteria is attached on support media 3 Mai 20
GEA Heat Exchangers / GEA 2H Water Technologies GmbH
Overview of the WWTP in Bent Saiden / Tunisia
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Research project: Hybrid biofilm plant.
The pilot unit is supported by German Ministry of Development and Research.
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200 PE, Inflow 30-40m3/d, BOD 20kg/d GEA Heat Exchangers / GEA 2H Water Technologies GmbH
Process steps of the WWTP in Bent Saiden Primary Sedimentation-Tank De-nitrification Inflow C-Stage Sedimentation Tank Secondary Sedimentation Tank Outlet Nitrification (N1-N3) Sludge Tank GEA Heat Exchangers / GEA 2H Water Technologies GmbH
Concept –system of hybrid-plant The conventional upstream denitrification process
Primary treatment (screen, settling) Denitrification (anoxic conditions) Sludge recycle C/N Elimination (aerobic conditions) Internal recycle Final settling
The compact-system process
Primary treatment (screen, settling) Denitrification (anoxic Moving bed) Internal recycle Intermediate settling C/N Elimination (aerobic fixed bed) Final settling with 6 Best practice: MOFIX
GEA Heat Exchangers / GEA 2H Water Technologies GmbH
Concept - system of hybrid-plant
denitrification BOD removal settling Nitrifikation settling recycle Concept - system of hybrid-plant
GEA Heat Exchangers / GEA 2H Water Technologies GmbH
Demonstration of Deni- stage in WWTP-Tunis Inflow
Separation Screening sheet
outet to
intermedia sedimentation tank Mixer 836m²/m³ BCN 09
C-Stage DeNi
Recerculation line Air supply + Layout of Denitrification and C-removal stages Spicall Mixer • • For de-nitrification reactor a specific density above 1 kg/l should be applied.
A special shaped mixing device must be tested and applied because agitator of moving bed system with propeller shaped mixers often leads to the damage of carriers.
GEA Heat Exchangers / GEA 2H Water Technologies GmbH
Moving bed for De-nitrification -Stage
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GEA Heat Exchangers / GEA 2H Water Technologies GmbH
Fixed Bed Reactor with BIOdek ® for Nitrification
10 Mai 20
GEA Heat Exchangers / GEA 2H Water Technologies GmbH
Nitrification in 3 phases
11 Text über "Einfügen Kopf- u. Fußzeile" einfügen
GEA Heat Exchangers / GEA 2H Water Technologies GmbH
Aeration device for Nitrification Stage GEA Heat Exchangers / GEA 2H Water Technologies GmbH
Conclusions / results
Removal rates (%) during 80 day start-up period (without process optimization)
Mo/Fix-Hybrid ® - Data & results pilot plant GEA Heat Exchangers / GEA 2H Water Technologies GmbH
Conclusions / results
Treatment of N in the WWTP Treatment of BOD in the WWTP
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GEA Heat Exchangers / GEA 2H Water Technologies GmbH
Conclusions / results -
Compact System
Comparison between activated sludge and compact-system design Denitrification Carbon removal Interm. Settling Nitrification Final settling
Total volume Activated sludge Tank (m³) MOFIX Tank (m³)
714 75 127
MOFIX Media (m³)
37,5 80 714 263
1691
143 444 57
846
30 333 11
492 MOFIX Media (Type)
BCN 14 KVP 623 FS41.84
KVP 618 FS41.50
15 Best practice: MOFIX
GEA Heat Exchangers / GEA 2H Water Technologies GmbH
Conclusions / results Compact System
• Compact-System (Mofix) is a wastewater treatment process designed for highest standards, reliable and easy to operate.
• The effluent concentrations of MOFIX treated municipal wastewater comply with highest German and European standards for BOD, COD, NH4-N and NO3-N • The treated wastewater by compact system MOfix (BOD5≤10 mg/l, COD ≤100 mg/l, TSS: ≤25 mg/l, NH4-: ≤2 mgN/l, NO3≤10 mgN/l) can be reused for irrigation after disinfection or discharged to the Water bodies • The generated excess sludge can be exposed for drying in sludge drying beds which can be built in the proximity of the unit. And reuse it for Agriculture. 16 Mai 20
GEA Heat Exchangers / GEA 2H Water Technologies GmbH
Thank you very much for your attention
17 Mai 20
GEA Heat Exchangers / GEA 2H Water Technologies GmbH
Demonstration of Deni- stage in WWTP-Tunis Structure of a moving bed
• (1) mixing device
(slow motion)
• (2) moving bed carrier
(max 50% filling)
• (3) baffle • (4) screen
(30 m/h)
• (5) diffusors 18 Best practice: MOFIX
GEA Heat Exchangers / GEA 2H Water Technologies GmbH
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Overview in 3-D of the WWTP
Final clarification Nitrification in 3 phases (fixed bed) Recirculation Screening Agitator Denitrification reactor Sludge thickener BOD removal fixed bed Intermediate clarifier
GEA Heat Exchangers / GEA 2H Water Technologies GmbH
Aims of waste water treatment Biological waste water treatment
It is a type of waste water treatment in which microorganisms such as bacteria are used to remove pollutants from waste water through biological stag,
Wastewater treatment means:
removal of pollutants like solids, organic matters i.e. BOD-load and inorganic matter (nitrogen, phosphorous, Heavy metals etc.).
• BOD removal • Nitrification • De-nitrification 20
GEA Heat Exchangers / GEA 2H Water Technologies GmbH