sewage sludge management in egypt_mohamed ghazy
TRANSCRIPT
Institut of Sanitary and Environmental EngineeringTechnische Universität Braunschweig, Germany
Msc. Eng. Mohamed GhazyMsc. Eng. Mohamed Ghazy
E-Mail: [email protected]
Institute of Institute of SanitarySanitary and and EnvironmentalEnvironmental Engineering EngineeringTechnische Universität Braunschweig, GermanyTechnische Universität Braunschweig, Germany
Prof. Dr.-Ing. N. Dichtl Prof. Dr.-Ing. N. Dichtl
Sewage Sludge Management in Egypt:Sewage Sludge Management in Egypt:
Current Status and Perspectives Towards a Current Status and Perspectives Towards a
Sustainable Agricultural UseSustainable Agricultural Use
DAAD International Workshop for Water, Wastewater and the Environment-Urgent Issues for Sustainability (26th October – 3rd November 2009), Braunschweig, Germany.
Institut of Sanitary and Environmental EngineeringTechnische Universität Braunschweig, Germany
PopulationPopulation: Tripled during the last 50 years.
80 million, year 2008, Annual growth rate 1.75 % More than 13 million tourists/year+
IntroductionIntroduction
ClimateClimate: : A desert climate, hot and dry most
of the year.
With the rapidly growing population and
industrial development, the wastewater and
sewage sludge generation has been also
increased.
The Egyptian sanitation sector is facing
many difficulties to manage this wastewater
and sewage sludge, Which require huge
investments currently are above the
presently available national resources.CapitalCapital: Cairo
CairoCairo
Current population 17 million, producing
more than 5 million m3/day of wastewater.
AreaArea: 1 million km2
Only 5% occupied by population along the
Nile Valley and Delta.
Institut of Sanitary and Environmental EngineeringTechnische Universität Braunschweig, Germany
Wastewater Services Coverage in Wastewater Services Coverage in EgyptEgypt
Rural (4700 villages)
57%
Urban (217 cities)
43%
Cover60%
Not cover40%
Urban Areas
About 60 % are covered by wastewater collection
and treatment facilities, and planning to cover
100 % with 2020.
Urban AreasUrban Areas
Cover15%
Not cover85%
Rural Areas
Only 15 % are covered by wastewater collection
and treatment facilities.
The other using Septic tank or disposal the
wastewater direct to water bodies.
Rural AreasRural Areas
It is required more than 100 Billion US$ to cover 100 % of Rural and Urban
areas
Institut of Sanitary and Environmental EngineeringTechnische Universität Braunschweig, Germany
Wastewater Treatment Plants in Wastewater Treatment Plants in EgyptEgypt
Systems of Wastewater Treatment Systems of Wastewater Treatment
Capacities of WWTPsCapacities of WWTPs Total No of WWTPs: 303, Total Treatment Capacity: 12 million m3/day
More than 78 % of WWTPs is relatively small (< 30x103 m3/day) representing 22 % of total treatment capacity.
Scales of WWTPs, and amount of sludge generation in Egypt, year 2008_
Activated Sludge Systems:
Conventional Activated Sludge Conventional Activated Sludge SystemsSystems
Oxidation DitchOxidation Ditch Systems Systems
Mainly conventional and oxidation ditch
systems and representing about 63 % of the
total WWTPs capacity and treating about 7.5
million m3/day.
Representing about 12 % of WWTPs No. and 2.25
% of Treatment capacity (0.3 million m3/day). Preliminary Preliminary TreatmentTreatment
InfluentInfluent
Excess sludgeTo sludge treatment facilities
EffluentEffluent
Oxidation Oxidation PondsPonds
Preliminary Preliminary TreatmentTreatment
InfluentInfluent
Excess sludgeTo sludge treatment facilities
EffluentEffluent
Oxidation Oxidation PondsPonds
Oxidation Pond SystemsOxidation Pond Systems
Oxidation Pond Systems:
Institut of Sanitary and Environmental EngineeringTechnische Universität Braunschweig, Germany
The Applied The Applied Scenarios Scenarios for Sludge Treatment for Sludge Treatment and Disposal and Disposal in in EgyptEgypt
Type of WWTPsType of WWTPs
Oxidation Ponds
Conventional Activated Sludge
Trickling Filter
Agricultural ReuseGravity Thickener
The thickened sludge solids concentration:4-6% DS
Natural Dewatering
The solids concentration after drying beds is 40-60
%.
The dewatering time is usually 25 days in summer
and 40 days in winter.
Drying Area
Storage period of 1.5 to 6 months according to the
weather and available stacking area before using in
agriculture
Stabilisation Pond
Primary Treatment
UASB
It is noted that, this scenario of sludge treatment does not contain facilities
for stabilization processes. Moreover, the quality of the produced sludge in
most of the WWTPs doesn’t fit the Egyptian or international standards,
especially pathogens limits.
Institut of Sanitary and Environmental EngineeringTechnische Universität Braunschweig, Germany
Recently Applied Recently Applied Scenarios: Scenarios: Anaerobic digestionAnaerobic digestion (Al Gabel Asfer WWTP- Cairo)(Al Gabel Asfer WWTP- Cairo)
GravityGravity thickeningthickening
Phase I: 16 Thickeners with volume of 3,200 m3
Phase II: 3 with volume of 2,500 m3
Thickened sludge: 12,500 m3/day, Conc. 4 % DS
Mechanical dewateringMechanical dewatering
Phase I: 30 belt filter press units with a capacity of 23 m3/hr each
Phase II: 12 units with a capacity of 21 m3/hr each
Solid concentration : 23-30 % ; Polymers dose: 4 kg/ton DS Drying areaDrying area
Stacking area: 54 hectares
Solid concentration : 40-60 % Then it transferred to use in agriculture
Al Gabel Asfer WWTPAl Gabel Asfer WWTPCurrent capacity:1.8 million m3/day, Total area: 630
hectares
First stageFirst stage: Started operation: October 1998
Capacity: 1.2 million m3/day (actual), Cover : 12 million capita
Second stage:Second stage: Started operation: 2004
Capacity:0.5 million m3/day, Cover : 2.5 million capita
Future Stage: Future Stage: Will start operation: 2020
Capacity:1.5 million m3/day (Total capacity 3 million
m3/day).
It will be the largest WWTP in the World
First stage1200*103 m3/day
Second stageSecond stage540540**101033 mm33/day/day
Sludge treatment facility
Future extension 1500 x103 m3day
Sludge Treatment ScenarioSludge Treatment Scenario
Anaerobic digestionAnaerobic digestion
Primary digesters
Phase I: 20 digesters with volume of 11,000 m3
Phase II: 8 with volume of 10,000 m3
Retention time: 20 days Secondary digesters Phase I: 10 digesters with volume of 7,500 m3
Phase II: 2 with volume of 9,000 m3
Retention time: 7 days
Institut of Sanitary and Environmental EngineeringTechnische Universität Braunschweig, Germany
Amount of sludge
3000-4000 m3 /day, conc. 2-3 %
No. 2, Capacity 900 m3
Retention time: 7-9hr
Blower capacity: 800 m3/hr
Mechanical Dewatering SiteAmount of produced sludge:
(400 tons/day, conc. 25-30%)
No of Machines: 12 Belt filter Presses
Belt width: 2 m, Capacity:700-900 m3/day
Destination of Disposal (9 N) site at distance 45 kmSludge Treatment ScenarioSludge Treatment Scenario
Mechanical Dewatering
Agricultural ReuseCompostingPrimary Treatment
WWTPs, Alexandria (9 N Site)
Recently Applied Recently Applied Scenarios: Scenarios: Windrow compostingWindrow composting (9 N site – Alexandria)(9 N site – Alexandria)
WWTPs in AlexandriaWWTPs in Alexandria
West WWTPCapacity: 360x103 m3/day (actual).
Start of operation: 1993 (prim. treatment)
Amount of sludge: 3,100-4,000 m3/day, conc. 3.5-6%
East WWTPCapacity: 600x103 m3/day (actual)
Start of operating: 1990 (prim. treatment)
Amount of sludge: 3000-4000 m3/day, conc. 2-3 %
Others: 6 WWTPs, (Sec. treatment) Total treatment capacity107 x103 m3/day.
Institut of Sanitary and Environmental EngineeringTechnische Universität Braunschweig, Germany
Mixing with bulking agent
Stabilization stage
Active composting stageActive composting stageComposting time: 2 monthsMixing and aeration: 3 times/day (3 days), Every 15
daysOperating temperature: 55-65 °C
Mentoring and temperature control
Curing stage
Curing stageCuring stageCuring time: 1 monthMoisture content : 10-25%
Composting ProcessComposting Process
Start of operating: 1997
Site area: 1.5 Km2
Ground water depth: 60 m
Distance from nearest residential area: 6 km
(9N) site(9N) site::
Windrow formationWindrow formationNo. of windrows: 60Dimension of each: (250 m, 3.5 m, 1.5 m)Bulking agent: recycle compost, Bulking ratio: 1:1.5Moisture content : (40 to 50%) Dump the raw dry sludge
Cover the raw sludge by old compost
Capacity of Produced CompostCapacity of Produced Compost
YearReciving sludge Produced compost
2005 82000 290002006 109000 390002008 129000 46000
(m3/year) (m3/year)
(9 N) site – (9 N) site – AlexandriaAlexandria
Institut of Sanitary and Environmental EngineeringTechnische Universität Braunschweig, Germany
Gravity thickenersNo of thickeners : 8Diam: 25 m,depth: (4-6.5m)Amount of thickened sludge5000 m3/day, Conc. 5-6 %
Shobera WWTPTreatment Capacity: 600 x 103 m3/day 3.0 million capitaAmount of sludge4700 m3/day,Conc.3%
AL Berka WWTPTreatment Capacity:
600 x 103 m3/day(design)
4.0 million capitaAmount of sludge5700 m3/day,Conc. 2 %
Drying beds Total area: 210 hectaresNo of Beds: 96Dim. 125 x 64 x 2 mDrying time: (25-40 days)Amount of dry sludge450 m3/day (220 tons/day), Conc. 35-50 %
2 force main diam. 350
mm
Distance: 3 km
Al Berka compost project
Recently Applied Recently Applied Scenarios: Scenarios: Windrow compostingWindrow composting (AL Berka pilot project-Cairo)(AL Berka pilot project-Cairo)
Sludge treatment scenario in Al Berka Sludge treatment scenario in Al Berka WWTP WWTP
Gravity Thickener
Al Berka&Shobera WWTPs
Drying beds
Al Berka
Composting
(pilot project)
Agricultural Reuse70 %
30 %
Institut of Sanitary and Environmental EngineeringTechnische Universität Braunschweig, Germany
Composting ProcessComposting Process
Al Berka Pilot Compost Al Berka Pilot Compost ProjectProjectStarted operating: 2007
Investment costs: 3.5 million US$
Raw sludge: 140 m3/day, Site area: 2.6 Ha
Capacity of compost: 25,000 tons/year
Windrow formationWindrow formationNo. of windrows: 26, Dimension of each: (100 m, 3 m, 1.5 m)
Bulking agent: recycle compost and rice straw
Bulking ratio: 4 parts raw sludge (25% DS):1 old compost (60%
DS):1 shredded rice straw (85% DS),
Moisture content : (40 to 50%)
Cover the raw sludge by rice straw
Rice straw shredding
Windrow formation
Mixing with bulking agent
Active composting stageActive composting stageComposting time: 2 months
Mixing and aeration: 3 times (first), Every 15 days
Operating temperature: 55-65 °C
Aeration and temperature control
Stabilization stage Curing stageCuring stageCuring time: 1-2 monthMoisture content : 10-30%
Curing stage
Screening and bagging stage
Municipal Future PlanningMunicipal Future Planning
The project may be expanded to a full-scale project to produce a compost of 250,000 tons/year from the dried sewage sludge accumulated from Al Berka, Shobera and Al Gabel Asfer WWTPs
AL Berka pilot project- AL Berka pilot project- CairoCairo
Institut of Sanitary and Environmental EngineeringTechnische Universität Braunschweig, Germany
Sewage Sludge Production Sewage Sludge Production in in EgyptEgypt
Based on Egyptian BOD and TSS concentrations and taking the effect of Temp. from (10-30 °C) and sludge age (5-20 days)
German standards (ATV A 131E ): The production rate ranged from 0.20 to 0.28 kg/m3 of treated sewage.
Metcalf & Eddy (2003): It ranged from 0.11 to 0.21 kg/m3 of treated sewage.
According to According to theoretical calculationtheoretical calculation
According to the NOPWASD and HCWW dataAccording to the NOPWASD and HCWW data
The total current capacity of treated sewage: 12 million m3/day.The dry sludge production was estimated to 5.8x103 tons/day The sludge production rate: 0.48 kg/m3 of treated sewage (which seems relatively high compared to many
other typical values: USA (0.2-0.3 kg/m3 ); Metcalf & Eddy (0.18 -0.27 kg/m3 ); China was 0.21 kg/m3
Estimation the reliable amount of produced dry sludgeEstimation the reliable amount of produced dry sludge
The dry sludge production rate from the activated sludge systems in Egypt is considered at 0.22 kg/m3
The production rates from the others WWTP types are assumed at 0.05-0.22 kg/m3 according to the literatures
The estimated dry sludge produced from all WWTPs in Egypt, 2008
Activated Sludge 97 0.225 6,703 1,508 2,793Oxidation Ditch 47 0.225 833 187 347Trickling Filter 9 0.22 291 64 119Extended Aeration 17 0.1 170 17 31Oxidation Ponds 35 0.05 266 13 25Aerated Lagoon 4 0.1 197 20 36Primary Treatment 22 0.15 2,021 303 561Others* 72 0.2 1,372 274 508Total 303 11,853 2,387 4,421
Estimated dry sewage sludge
(50 % DS)
Capacity of treated
wastewater 103 m3/day
Type of WWTPsNo of WWTPsSludge
production rate(kg/m3)
Amount (tons/day)
Volume (m3/day)
The estimated amount of produced dry sludge from Egyptian's WWTPs are about 2.4 x103 tons/day.
Institut of Sanitary and Environmental EngineeringTechnische Universität Braunschweig, Germany
Sewage Sludge Agronomic Value Sewage Sludge Agronomic Value
Sewage sludge monetary valueSewage sludge monetary value
Theoretically, the monetary values of the resources contained in sewage sludge can be evaluated according to the current price of these relevant resources in the commercial market.
Egyptian market price
USA Market price
(US$/kg) (US$/kg)Nitrogen (N) 0.76 1.61
Phosphorus (P) 2.23 4.91Potassium (K) 0.43 0.94Organic matter 0.015 0.044
Resourses
The monetary values for the relevant resources in dry sludge
Assume: The average retail price of electricity in USA, 2008 was 10.13 Cent/kWh and in Egypt 3.4 Cent/kWh and the exchange rate used in 2008 was US$ = 5.76 LE (Egyptian pound)
The economic values of the N, P and K resources can be calculated according to the market prices of these elements in the commercial inorganic fertilizers.
The monetary values of the organic matter can be estimated according to the market price of the generated electricity during the anaerobic digestion stabilization.
Nutrients contentNutrients content
The agronomic value of sewage
sludge depends on its nutrients
content, trace elements and organic
matter content
Concentration of nutrient resources in the dried sludge in Egypt’s WWTPs
Field study, 2008 57 3.16 1.13 0.28AFESD, 2007 61 3.13 0.65 0.19IIP, 2002 No data 2.4 0.55 0.3NOPWASD, 2000 61 4.11 1.6 0,55METAP, 1999 45 1.7 0.8 0.3
Average 56 2.90 0.95 0.32
Potassium (K) %
ReferenceTotal organic mater (OM)
%
Total nitrogen (TKN) %
Total Phosphorus
(P) %
The price of dry sewage sludge in the international and Egyptian market
Kg/ton kg/m3 US$/ton US$/m3 US$/ton US$/m3
Nitrogen (N) 2.9 29 15.7 22.0 11.9 46.7 25.2Phosphorus (P) 0.95 9.5 5.1 21.2 11.4 46.6 25.2Potassium (K) 0.32 3.2 1.7 1.4 0.7 3.0 1.6Organic matter 56 560 302.4 8.4 4.5 24.64 13.3
Total 53 28.5 121 65.3
ResourcesAverage
content %
Amount of relevant resources
Monterey valueEgyptian market USA market The theoretical price of
sewage sludge according to its resources price in Egyptian market is 28 US$/m3
or 53 US$/ton.
Institut of Sanitary and Environmental EngineeringTechnische Universität Braunschweig, Germany
Options of beneficial uses of sewage sludge Options of beneficial uses of sewage sludge
1. Agriculture Reuse 1. Agriculture Reuse Soil ConditionerOrganic Fertilizer
Cement Industrial Construction Materials3. Construction materials3. Construction materials
4. Phosphorus recovery4. Phosphorus recovery
Phosphors
2. Energy recovery2. Energy recovery Electricity GenerationHeat Generation
Institut of Sanitary and Environmental EngineeringTechnische Universität Braunschweig, Germany
Potential uses of sewage sludge inPotential uses of sewage sludge in
Egypt Egypt
Egypt is an arid country, the dessert represents more than 95% of the total area.
Only 5 % of Egypt area occupied by overpopulation in the limited strip of the Nile valley and Delta.
Nile valley
Delta
950
500380
0
100
200
300
400
500
600
700
800
900
1000
1960 1996 2017
Year
m2 /
Ca
pit
a
Change of the cultivated land per capita in Egypt
The sharp decline of the per capita cultivated land will also reduce the per capita crop production.
An important issue for Egyptian agricultural policy is to redistribute the population over a larger area
Institut of Sanitary and Environmental EngineeringTechnische Universität Braunschweig, Germany
Expansion of reclamation desert Expansion of reclamation desert land land Over the last 30 years, More than 3.3 million acres have
been reclaimed and that will be increased in the future.
About 170,000 acres are reclaiming yearly (the
South Valley Development Project about 1 million acres
until 2020)
South South valley development development projectproject
Soil conditions of the reclaimed Soil conditions of the reclaimed landland Often saline, mild to moderately alkaline (pH 7.7 -
8.2).
Micronutrient elements shortage are common,
particularly manganese, iron and zinc, which are
required for plant growth and are present in sludge.
Calcareous soils limit crop uptake of heavy metals
and potential toxicity.
Extensive sunshine exposure, high temperature,
and dry conditions, Which provide unfavorable
conditions for survival of microbial pathogens
Beneficial use of sewage sludge in Beneficial use of sewage sludge in EgyptEgypt (Potential demand of sewage sludge in agriculture)(Potential demand of sewage sludge in agriculture)
Institut of Sanitary and Environmental EngineeringTechnische Universität Braunschweig, Germany
Beneficial use of sewage sludge in Beneficial use of sewage sludge in EgyptEgypt (Sewage sludge market )(Sewage sludge market )
Sewage sludge market price Sewage sludge market price
The current sale price of dry sludge in Egyptian market ranges from 1.5-11
US$/m3. This price of the other organic fertilizer are about 17 US$/m3.
The target price of treated dry sewage sludge is estimated by 12 US$/m3.
This price has still a proper competition margin up to 5 US$/m3 less than other
organic fertilizers and less than the estimated theoretical price of sewage sludge by
16 US$/m3 .
Potential market demand Potential market demand
The recommended application rate of dry sewage sludge in Egypt: 8 - 20 m3
DS/acre/year for arable crops.
The current dry sludge production represent only less than 5 % of the actual
demand of the target market (the reclaimed desert land only).
The target market: New reclaimed desert land, which can be considered more
preferably for sludge application, hence the supply of sludge more practical,
safe and any input of organic matter will improve the soil properties.
Institut of Sanitary and Environmental EngineeringTechnische Universität Braunschweig, Germany
ConclusionConclusion
The use of sewage sludge in agriculture in Egypt may offer the most sustainable and
beneficial use of sewage sludge under Egyptian conditions. Also, it may offer the
most economical route for sludge disposal because the Egyptian farmers are
prepared to pay for any source of organic fertilizers.
The treated sewage sludge has a good potential demand in the Egyptian market. The
target price of municipalities is estimated at 12 US$/m3 of dry sludge (it will provide a
yearly income about 19 million US$, which represents more than 30 % of the
operation and maintenance costs of all Egyptian WWTPs).
The sewage sludge production is continuously increasing in Egypt. Therefore, the
main currently pressing needs are to find/develop more efficient and more
sustainable technologies to allow a safe and suitable reuse of sewage sludge in
agriculture. Recently, the application of the anaerobic digestion technology for sludge
stabilization and power generation in Al Gabelb Asfer WWTP and the windrow
composting processes in (9N) site and Al Berka WWTP have achieved good results.
There is a growing interest in using such technologies on large scale in the future.
Institut of Sanitary and Environmental EngineeringTechnische Universität Braunschweig, Germany
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