This document discusses odor control in sewerage systems in Lviv, Ukraine. It summarizes Egis' work conducting a pre-diagnosis of odor problems in Lviv's sewerage system. Key outcomes included the need to implement an odor tracking system to identify odor sources and the finding that the sewerage system and wastewater treatment plant are likely major odor sources. The document then outlines Egis' methodological approach to diagnosing specific cases, including field inspections, monitoring, and hydraulic and water quality analyses to identify causes and appropriate treatment solutions.
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€854 M OF MANAGED TURNOVER
78 % ENGINEERING22 % ROAD & AIRPORT
OPERATION
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53% OF SALES ABROAD
4%
AMERICAS
47%
FRANCE
(incl. French Overseas
Departments and Territories)
12%
AFRICA
21%
EUROPE
8%
ASIA
1%
AUSTRALIA
OCEANIA
1%
Ukraine
7%
MIDDLE
EAST
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12,000 EMPLOYEES
12,000 employees
TOTAL WORKFORCE
ON DECEMBER 31, 2014
4,200
ROAD AND AIRPORT OPERATING
COMPANIES STAFF
7,800 ENGINEERING DIVISION STAFF
4,100 FRANCE 3,700 INTERNATIONAL
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EGIS UKRAINA. 20 YEARS OF CREATIVE
WORK
55 employees
30 engineers
40 projects
in Ukraine and
CIS
Key services:
- feasibility study
- mobility study
- corporate development
- technical support to the municipalities
- construction supervision
- project management
822 000 € – 2014 TURNOVER
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KEY FIELDS OF OPERATIONS IN UKRAINE
Urban transport
Roads
Water
Energy
New tramway produced in Lviv for the
LvivElectrotrans modernisation project led by EGIS
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PRE-DIAGNOSIS OF ODOR
PROBLEMS IN THE
SEWERAGE SYSTEM OF
LVIV CITY
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CONTEXT
• Citizen’s complaints for bad smells
• Lviv, tourist capital of Ukraine
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SCOPE OF WORK
• General and preliminary assessment of smell problem
• Define technical solutions or propose further investigations
to understand smell problems
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MAIN OUTCOMES (1)
Odor complaints spread over a large area
No systematic recording and follow-up regarding these
complaints
Implement an Odor tracking system/service
• Find the origin
• Warn LVK of any abnormal situation
• Keep track of the evolution of odor situation
Chapitre
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MAIN OUTCOMES (2)
Sewerage system seems to be the main odors source in
several districts
=> To implement an hydraulic diagnosis and technical
solutions, on a case by case basis
WWTP and sludge deposit area have a large emissivity
and could instigate complaints under specific wind
conditions
=> To implement an olfactometric measurements
campaign to identify main odor sources and prioritize
technical solutions
Chapitre
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FIRST STEP / IMPLEMENTING AN
ODOR TRACKING SYSTEM
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EXEMPLE OF SIAAP - PARIS
(1) Report a complaint on the website :
Odor statement
Date
Hour
Town
Adress
Duration
Less than an hour
A few hours
1 to 2 days
Several days
Kind of smell
Level of annoyance
Level of Intensity
Remarks
I wand to be contacted :
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EXEMPLE OF SIAAP - PARIS
(2) In-field odor inspections
4 inspectors from SIAAP
Daily patrols in-site and in the environment of facilities
Paths and check points determined on a weekly and daily
basis according :
- Citizens complaints
- Maintenance works
- Trials and study about technical solutions or preventive works to
reduce odor emissions
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FOLLOW-UP OVER THE YEAR
Jan. Feb. March April May June July August Sept. Oct. Nov. Déc.
Year 2014
High H2S level at pumping
station 4
Maintenance work on
collector 6
Stopping the deodorization
plant for maintenance
+ propitious weather conditions
: Situation olfactive satisfaisante
: Situation olfactive passable
: Situation olfactive médiocre
: Situation olfactive critique
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SEWERAGE SYTEM
Diagnosis and technical
solutions on a case by case
basis
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METHODOLOGICAL APPROACH
pressure pipe
gravity pipe
junction chamber
vent
1- Where does the odor come from ?
Residential area
Industrial collector
Industrial
collector
in-field odor inspections
H2S continuous monitoring
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METHODOLOGICAL APPROACH
pressure pipe
gravity pipe
junction chamber
vent
Residential area
Industrial collector
Industrial
collector
2- Understanding the causes
Measurements campaign of:
water flow rate + H2S concentrations
+ temperature, BOD5/COD, pH,
over an extended period of time
Retention time
to check
Is the vent high
enough ?
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METHODOLOGICAL APPROACH
pressure pipe
gravity pipe
junction chamber
vent
Residential area
Industrial collector
Industrial
collector
2- Understanding the causes
Hydraulics characteristics :
Water flow rate
Water velocity
Diameter changes
Slopes changes
Turbulence, confluence of major tributary systems
Manhole locations
Measurements campaign of:
H2S concentrations in headspace
Water quality = Sulfates (SO4--), pH, dissolved and total
sulfides, sewage temperature, BOD5/COD, suspended solid,
Pressure in the headspace
Structural conditions of the collector
Failures inspections
Maintenance man hole sealing
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HEADSPACE CONSTRICTION
Chapitre
Downstream sewer cannot accept
all of the upstream air causing out
venting off the sewer
Lowvelocity water pushes back on
fast moving air causing a pressure
zone to form upstream
Hydraulic jumps can also
constrict airspace causing
more backpressure
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CLASSICAL LIQUID PHASE TREATMENT (1)
Iron salts addition
H2S curative application
Chapitre
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CLASSICAL LIQUID PHASE TREATMENT (2)
Calcium Nitrate
H2S preventive application
Chapitre
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OTHER INVESTIGATIONS / SOLUTIONS
Chapitre
Odor tracking system
Control the proper design and hydraulics characteristics
Control the maintenance
Control of wastewater entry - Industrial and non-domestic
waste water surveys, hauled waste station to implement
Inhibition of H2S (nitrate, oxygen injection…)
Collection of air (gaz trap on rain gullies, ventilating
facilities) and treatment
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www.egis-group.com
H élène PIET A rnaud D E R U GY
A i r / O d o r E x p e r t R e g i o n a l M a n a g e r f o r
U k r a i n e a n d C I S
H e l e n e . p i e t @ e g i s . f r A r n a u d . D E R U G Y @ e g i s . f r
,
Т e l . + 3 8 0 4 4 2 4 6 6 4 4 8
CONTACT
Goodafternoon everybody.
My name is Helen Piet from Egis Group
I’m gonna talk today about odor control in sewerage system. We will see methods approachs and feedback experiences that we have in Lviv and other cities
If there is confusing during the talks please to feel free to interrupt me to ask a question
Let me first show you some key figures about Egis Group
Egis Group is a French company. The group is specialized in engineering in the field of transportation, water and environment.
Egis is also involved in the business of setting up projects and operations for roads and airports
Rajouter des éléments sur Egis Ukrain
Egis Group has about 12 000 employees. A large majority is engineering staff
The reason of my presence here today is because very recently we have performed a study about odor problems in Lviv City
Many citizen’s complaint for bad smells.
And you have to realize that Lviv is a very touristic city in Ukrain.
So it is important to do something
because Lviv is a very touristic city in Ukrain, it is important for Lviv to keep a good environmental image.
Between april to july 2014 : more than 50 complaints /month
Between July to september 2012 : more than 300 complaints/month. In this period Lviv was one of the venues for the UEFA Euro 2012.
The scope of work can be summarize as follow.
First we have to..
Once this is done/after that, we must define technical solutions or propose further…
The main outcomes are the following.
Odor complaints are spread over a large area, as you can see in this map.
This map is from a website implemented by a citizen of Lviv, by its personnal initiative. It represents odor complaints over one specific day. People go on the website and they can declare (They answer a few questions) if there is an odor or not and if it’s really stink or not. An from all these answers, automatic map is generated/ This map represent these answers
Between april to july 2014 : more than 50 complaints /month
Between July to september 2012 : more than 300 complaints/month. In this period Lviv was one of the venues for the UEFA Euro 2012.
This study and especially my observations tends to show that the sewerage system seems to be the main odors source.
Why ? Because in some streets, odor are restricted/localized to the small area along the street and the collector. Located around.
5 levels scale
On a scale to 1 to 5 you have to define
Phone numer : not complusory. It’ optionnal.
From these data, a report is made on a daily basis and then a weekly basis. In ordre to undesrtand the problem ad then to solve the problem.
Thses inspectors are people that every day do watch, patrols
Determiiiined
Finir les animations
Finir les animations
Let me show you what we can fo to undesrtand the causes.
How we do that ?
Finir les animations
Expliquer que LVK a déjà implementer cette solution
Iron salts solution Reacts with dissolved sulfides in water by the following summary reaction:
2FeCl3 + 3H2S ‡ S_ + 2FeS_ + 6HCl
Applying a dosage beyond that dose required for initial H2S removal, Ferric Chloride then reacts to form Ferric Hydroxide which is a coagulant/ flocculant. The result is enhanced settling of both the generated sulfide removal solids and other wastewater
Iron Salts (Ferric and Ferrous)
Iron Salt Applications
Iron salts are a proven technology for long-duration hydrogen sulfide control in collection system gravity and forcemains, solids processing units, solids transfer lines and anaerobic digesters. They have been used for over 30 years in hydrogen sulfide control applications and are a well understood technology.
Depending on the wastewater plant unit process configuration, iron salts may also provide improvements in clarification, phosphate removal, struvite control, solids dewatering and anaerobic digester performance. Iron salt performance is not impacted by oxygen uptake rates but they do remove dissolved oxygen from the water.
Iron Salt Properties and Dosing
Iron salts are supplied as liquid solutions containing 5-13% ferrous or ferric iron as either a chloride or sulfate salt. They are supplied in containers of 55 or 300 gallons, or in bulk shipments of 4,000 - 20,000 gallons.
Iron salts bind with hydrogen sulfide according to the following equations:
Ferrous Salts:
H2S + FeCl2 → FeS + 2HCl Ferric Salts:
3 H2S + 2 FeCl3 → S + 2 FeS + 6 HCl
Theoretical dose ratios of ferrous iron to H2S are 1.75 lbs Fe2+:lb H2S with practical dose rates anywhere from 2 to 6 depending on the application. Theoretical dose ratios of ferric iron to H2S are 1.2 lbs Fe3+:lb H2S with practical dose rates anywhere from 1.5 to 4 depending on the application.
Iron Salt Pricing and Sources
Iron salt pricing is highly regional and dependent on the local sources and demand for the product. Iron salts for sulfide control are mostly obtained from spent pickle liquor from the steel industry. More recently, newer sources have been manufactured from scrap materials and acid in order to meet regional demand.
Iron Salt Drawbacks
Some drawbacks of iron salt use are as follows:
Removes dissolved oxygen from the water
Precipitate settles out in low-velocity sewers (< 2 fps)
Iron films form on pipe walls and instrument sensors
Ineffective for (non-sulfide) organic odors
Hard to achieve low sulfide limits (pH dependent)
Does not destroy sulfide (H2S may volatilize if the pH is lowered)
Product purity may impact biosolids re-use (heavy metal contamination)
Messy to handle
CERCLA rating may restrict dosing sites (persistent environmental hazard)
High dosages may cause solids carry-over from clarifiers
Solids production (> 3 lbs/lb - Sulfide) increases processing and disposal costs
Nitrate Applications for Hydrogen Sulfide Control
Nitrates are a proven technology for medium to long-duration hydrogen sulfide control in collection system gravity and force mains. They have been used for over 15 years in hydrogen sulfide odor control applications and are a well understood technology. Nitrates can be used in certain applications where hydrogen sulfide odor is already present (curative) or to prevent the formation of hydrogen sulfide (preventative) odor.
Curative Applications
Nitrates react mainly in the water column providing electrons for oxidation. In the curative application mode, a minimum retention time of 2-3 hours is required in order to be effective. In the preventative mode, nitrates condition the biofilm for anoxic process, preventing sulfate from being reduced to hydrogen sulfide in anaerobic sewer conditions.
Preventative Applications
A minimum retention time of 3 hours is necessary in order to be effective. When applied properly, control to low hydrogen sulfide levels is possible. Bioxide may provide some in-line BOD reduction in the collection system. Most calcium and sodium nitrate formulations are considered a non-hazardous material and can be stored in simple feed systems.
Nitrate Properties and Dosing
Nitrate is available as either in either granular or liquid form, and either as a calcium or sodium salt. The granular product comes in 100-lb bags, 2000-lb supersacks, or bulk hopper cars. The liquid product is the more commonly used form, and is available in bulk shipments of 2,000 - 4,000 gallons. Typical calcium nitrate formulations contain 4.3 lbs NO3 per gallon of solution. Typical sodium nitrate formulations contain 3 lbs NO3 per gallon.
Nitrates prevent or remove hydrogen sulfide according to the following equations:
Curative (Biomediated Oxidation):
5 H2S + 8 NO3 → 5 SO42- + 4 N2 + 4 H2O + 2 H+Prevention:
8/5 NO32 + [2 O2] (approximate representation)Theoretical dose ratios in the preventative mode of nitrate to H2S are 2.6 lbs NO3:lb H2S. Practical preventative dose rates for calcium nitrate vary anywhere from 2 to 8 gallons per pound H2S depending on the application. Theoretical dose ratios in the curative mode of nitrate to H2S are 0.7 lbs NO3:lb H2S. Practical curative dose rates for calcium nitrate vary anywhere from 1 to 2 gallons per pound H2S depending on the application.
Nitrate Pricing and Sources
The most common form of nitrate on the market for hydrogen sulfide control is liquid calcium nitrate solution. Typical pricing for calcium nitrate solutions is $2.00 to $2.50 per gallon. In the preventative mode, the cost per pound of sulfide treated is anywhere from $4.00 to $20.00. In the curative mode, the cost per pound of sulfide treated is anywhere from $2.00 to $5.00. Nitrates for sulfide control are mostly obtained from fertilizer manufacturers.
Nitrate Drawbacks
Some drawbacks of nitrate use are as follows:
Inefficient for gravity lines
Increases nitrogen levels in the wastewater
Resultant N2 gas (or residual NO3) may present problems downstream at the wastewater plant
Costs for prevention mode may be excessive in long retention time lines
Biomediated oxidation mode may require several hours, making nitrates less effective in certain applications (e.g. manifolded force mains)
Costs may be high in applications with high oxygen uptake rates (higher temperature, etc...)
Costs for prevention mode impacted by high BOD levels
Note: The use of nitrates for the removal of odors present at the point of addition (biomediated oxidation mode) may be covered under US Patent.