USING WATER - SEAI - Welcome to the Sustainable Energy
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Transcript USING WATER - SEAI - Welcome to the Sustainable Energy
Basic Cooling Water Treatment
principles
John Cowpar
Area Manager
GE Water and Process
Technologies
USING WATER
POTENTIAL PROBLEMS
CORROSION
DEPOSITION -
Fouling
Biofouling
Scaling
Scale Formation
Results
in loss of heat transfer efficiency
Increased
running costs
Danger of under deposit corrosion
Increased maintenance costs
Danger
of bacteria
Health
implications
Corrosion
Destruction
increased
of plant
maintenance costs
Fouling
loss
of efficiency due to increased pumping
costs
loss of heat transfer efficiency
Increased
fouling
Biological Nutrients
and health implications
Fouling
Loss
of heat transfer efficiency
increase
Under
in running costs
deposit corrosion
increase
in maintenance requirements
Increased
health
biological nutrients
implications
Blockages
increased
in system
operating costs and downtime
Objectives of Water Treatment
MINIMISE
SCALE
MINIMISE CORROSION
MINIMISE FOULING
MINIMISE BIOFOULING
MAXIMUM SAFETY
MAXIMUM EFFICIENCY
NON-POLLUTING
WHAT CAUSES OUR PROBLEMS?
DISSOLVED SOLIDS
e.g.
CALCIUM
MAGNESIUM
SODIUM
CHLORIDE
BICARBONATE
SULPHATE
SILICA
IRON
DISSOLVED GASES
e.g.
OXYGEN
CARBON DIOXIDE
NITROGEN
SULPHUR DIOXIDE
SUSPENDED MATTER
DUST/DIRT
CONTAMINANTS
e.g. OIL
BIOLOGICAL e.g. ALGAE,
FUNGI, BACTERIA
TYPICAL WATER ANALYSIS CHART
Water Analysis
pH
Colour
Turbidity
Solids - Suspended
Chloride as Cl
Alkalinity as CaC03
Ammoniacal Nitrogen as N
Iron (Total) as Fe
Manganese (Total) as Mn
Nitrate as N
Total Hardness as CaC03
Sulphate as S04
Silica - Reactive as Si02
Sulphide as S
Carbon Dioxide - Free
Solids - Total Diss. at 180C
D.O. Concentration (Field Det.)
Coliforms
E. Coli
Faecal Streptococci
Sulphite Red. Clostridia
Result
7.7
3.00
9.00
5
44
144
0.140
311
65
4.0
207
62.3
6.9
0.015
2.50
347
10.7
<10
<10
<1
300
HAZEN
F.T.U.
mg/l
mg/l
mg/l
ug/l
ug/l
ug/l
mg/l
mg/l
mg/l
mg/l
mg.l
mg.l
mg/l
mg/l
/100ml
/100ml
/100ml
/20ml
Hardness
Hardness
is due to calcium and
magnesium salts dissolved in water
All
hardness salts are less soluble in hot
water than in cold water (they show
inverse solubility)
Different hardness salts have different
levels of solubility
Hardness is normally reported as calcium
carbonate
EVAPORATION
WINDAGE
MAKE UP
M=E+W+B
BLEED
Useful Equations
E=R/100 x Temp Drop(degF)/10
W=R x 0.2/100 ( Forced Draught)
W=R x 0.6/100 (Natural Draught)
B=E/(C-1) -W
M=E + B + W
SCALE FORMATION
SCALE CAN BE CONTROLLED BY:
PRE-TREATMENT
CHEMICALS
CONCENTRATION
FACTOR
CORROSION
Iron
ore is found in nature and requires
a large input of energy to convert it into
steel.
Steel corrodes in order to get back to its
natural (lower energy) state
Corrosion is an electrochemical process
CORROSION CAN BE
CONTROLLED BY:
REMOVAL
OF OXYGEN ?
ADDITION
OF CHEMICALS
CONTROL
OF pH
Biofouling
What is Biofouling caused by?
• FUNGI
• ALGAE
• BACTERIA
FOULING/BIOFOULING
Can
be controlled by
Filtration
Control
of Concentration Factor (bleed)
Dispersants
Biocides
Open Cooling
When
evaporation occurs, the heat of
evaporation is used to drive off the
vapour
The loss of this energy results in a
cooling effect in the water
Pure water is evaporated (gases may
also be lost)
Dissolved solids remain in the water
Customer Training WT200C
Page 23
Cooling Water
WATER DROPLET
COOLS BY:
EVAPORATION
RADIATION
CONVECTION
Customer Training WT200C
Page 24
Control of Concentration
The
number of times the solids build in
the system water is termed the
concentration factor (CF).
CF is controlled by bleed
to
increase CF - decrease bleed
to decrease CF - increase bleed
Customer Training WT200C
Page 25
Bleed Control
Effect
Too
of too much or too little bleed:
much bleed :-
low
concentration factor
waste of water
waste of treatment
Too
little bleed:-
high
concentration factor
danger of scale and fouling
increased nutrient in system
danger of biofouling
Customer Training WT200C
Page 26
x
Water
Use
x
While increasing concentration factor
reduces water use, it also increases
nutrients in the system water,
encouraging growth of bacteria and
slimes. Therefore, we normally run
most cooling systems between 2 and 5
x
x
1
2
3
4
x
x
5
6
Concentration Factor
Customer Training WT200C
Page 27
Non-biological Fouling
Treated
by addition of dispersants
dispersants
(antifoulants) coat the particles
and so keep them apart
The
dispersed particles are then
removed from the system water
either
filter
Customer Training WT200C
with the bleed or via a side stream
Page 28
Non-biological Foulants
Silt
Rust
Process
all
contamination
removed by dispersant/bleed
Oil
Grease
a
different chemical is required but the
principle is the same
Customer Training WT200C
Page 29
MICROBIOLOGY
Customer Training WT200C
Page 30
Microbiology
in
Industrial Cooling Systems
•
•
•
•
•
Problematic Microorganisms
The Biofouling Process
Water Treatment Biocides
Biocide Programming
Monitoring and Control
Customer Training WT200C
Page 31
FUNGI
• Although yeast and some aquatic fungi are
normally unicellular, most fungi are
filamentous organisms
• Fungi form solid structures which can reach a
considerable size
• Some wood destroying fungi exist,
associated with deterioration of tower timber
• Fungi require presence of organic energy
source
• Exist at between 5 to 38 C and pH 2 to 9 with
an optimum of 5 to 6
Customer Training WT200C
Page 32
ALGAE
• Classified as plants as they grow by
photosynthesis
• Range in size from unicellular microscopic
organisms to plants that can be up tp 50m in
length
Single cells
Customer Training WT200C
Multi cellular
Page 33
ALGAE
• Algae cannot survive in the absence of air,
water or sunlight
• Basic difference is that algae utilise CO2 and
water using sunlight as the energy source to
assimilate food
• Large quantities of polysaccharides (slime) can
be produced during algal metabolism
• Plug screens, restrict flow and accelerate
corrosion
• Provide excellent food source
• Exist between 5 to 65 C and pH 4 to 9
Customer Training WT200C
Page 34
BACTERIA
•
•
•
•
•
•
Universally distributed in nature
Great variety of micro organisms
Multiply by cell division
Slime formation
Pseudomonas (utilise hydrocarbon contaminants)
Sulphur bacteria - anaerobic sulphate reducing
bacteria
• Nitrogen cycle bacteria
Customer Training WT200C
Page 35
FACTORS CONTRIBUTING TO
MICROBIAL GROWTH
•
•
•
•
•
•
•
Rate of incoming contamination
Amount of nutrient present
pH
Temperature
Sunlight
Availability of oxygen/carbon dioxide
Water velocities
Customer Training WT200C
Page 36
THE BIOFOULING PROCESS
• Bacteria prefer to colonise surfaces
– enables production of biofilm which acts to protect
and entrap food sources
• Planktonic bacteria
– free swimming in bulk water
• Sessile bacteria
– attached to surfaces
Customer Training WT200C
Page 37
EFFECTS OF BIOFOULING
• Fouling of: tower, distribution pipework, heat
exchangers
• Reduction in heat transfer efficiency
• Lost production
• Under deposit corrosion
• Inactivation/interference with inhibitors
Customer Training WT200C
Page 38
WATER TREATMENT BIOCIDES
• Oxidising Biocides
– Have the ability to oxidise organic matter eg. protein
groups
• Non-Oxidising Biocides
Prevent normal cell metabolism in any of the following
ways :
– Alter permeability of cell wall
– Destroy protein groups
– Precipitate protein
– Block metabolic enzyme reactions
Customer Training WT200C
Page 39
OXIDISING BIOCIDES
•
•
•
•
•
Sodium Hypochlorite
Hypobromous Acid
Chlorine dioxide
Ozone
Hydrogen Peroxide
Customer Training WT200C
Page 40
Oxidising Biocides
• Rapid kill
• Cost effective
• Tolerant of contamination
e.g. Bromine, Chlorine Dioxide
• Minimal environmental impact
e.g. Bromine, Ozone, Peroxide, Chlorine Dioxide
• Ineffective against SRB’s
• Low residual toxicity
• Counts approaching potable water standards
possible
Customer Training WT200C
Page 41
Non Oxidising Biocides
•
Screen water
•
Select alternating biocide to prevent resistant strains from
developing
•
Effective against SRB’s
•
Can protect system long after dosing.
•
Contain biodispersant
•
Higher dosage for kill possible
•
Environmentally some have rapid breakdown e.g.
DBNPA
Customer Training WT200C
Page 42
BIODISPERSANTS
• Improves penetration of biocide within
bacterial slime
• Disperse released bacteria and biofilm into
bulk water for removal by blowdown
• Reduces ability for bacteria to attach to
system surface
• Improves performance of both non oxidising
and particularly oxidising biocides
Customer Training WT200C
Page 43
Physical Methods
Ultra Violet and Ultra Filtration
• Only Effective At Point Of Use
• Cannot Kill Sessile Organisms
• Offer No Protection To Isolated Parts Of
System (Static Areas)
• Environmentally Acceptable.
Customer Training WT200C
Page 44
Control of Concentration
The
number of times the solids build in
the system water is termed the
concentration factor (CF).
CF is controlled by bleed
to
increase CF - decrease bleed
to decrease CF - increase bleed
Customer Training WT200C
Page 45
Customer Training WT200C
Page 46
Customer Training WT200C
Page 47