case study - water pinch analysis
TRANSCRIPT
1.1. Case Study: Water Pinch Analysis
1.1.1.Introduction
Water Pinch Analysis or also known as WPA is originally derived from
the concept of pinch analysis used in the chemical processes. The simple
term and understanding of water pinch analysis are reduced and reuse the
water. Nevertheless in a scientific term, WPA is a systematic methodology
to reduce water consumption and also minimizing the wastewater
generation through integration of water using activities or processes. This
analysis was first introduced by Wang and Smith. Since then, this method
has been very popular among big factory as they prefer to conserve their
water consumption, thus reducing the operation cost.
Techniques used for setting up the targets for maximum water
recovery capable of handling any type of water using operation includes the
application of mass transfer based and non mass transfer based system.
This includes the source and sink composite curve and water cascade
analysis (WCA). As a graphical tool for setting water recovery targets as
well as for design of water recovery networks, the source and sink
composite curves are used.
1.1.2.Overall Process
As shown in Figure 1, the facility uses water obtained from water
wells and water purchase from the water authority. Rainfall is also
considered as an input to the facility because it crosses the imaginary
dotted line around the facility. Figure 1 is only a rough estimation of the
water input and water output by that company.
Figure 1: Site Wide Facility Water Balance (gallons per day)
The output steams include:
a. Evaporation of water from the facility, for example cooling towers
b. Containment of the water in the facility’s products, for example a
beverage
c. Water that leaks or goes into the ground from the facility’s irrigation
system or piping.
d. Treated effluent from the facility’s on-site wastewater treatment
facility which is discharged to a surface water
e. Sanitary wastewater which are sent to an off-site wastewater
treatment facility operated by the municipality
f. After rainfall event, storm water runoff.
Facility
Well
Water
Purchased
Water
Rainfall
330,00
20,000
Evaporatio
n
Water in
Product
Water to
Ground
136,00 0 34,000
Wastewater
after
treatment to
Surface Water
Wastewater to
Off-site
Treatment
Facility
Storm
water
runoff
130,00
30,000
20,000
Sanitary UtilitiesIrrigation
Production
Purchase + well
water input
Evaporate Evaporator
30000
4000
199955
WastewaterDischarge
Sanitary Wastewaters to Offsite
Treatment Facility
30000
42874
130000
Storm water run-off20000
34000 157081
20000
Rainfall
Water in product
To ground
Water
consumed in
reaction
604545 34000
Figure 2: The plant overall water balance
Flow rate is estimated by process knowledge, engineering calculation and
or judgment, factor or a combination thereof
Flow rate is measured. For example, water meter on purchased water, flow
meter on wastewater, other measurement, e.g., the wastewater collection
tank (volume of 3000 gallons) from building A fills up and is transferred
twice per day.
Figure 2 shows an expanded view of the facility including production,
sanitary, irrigation, and utilities. Other use category where water is used
but does not fit into to one of the categories, example: quality assurance
laboratories.
- In Figure 2, notice that the well water and purchased water are
combined in one line and there is green box signifying for purposes
that the volume of purchased water and well water is measured, in
this case via water meters.
- Rainfall (in inches) is also measured via a rain gauge. By multiplying
the inches of rainfall per year by the surface area of the production
site, the volume of rainwater entering the site is estimated.
- The water outputs (other losses and wastewater discharges) from the
different areas of use are determined via inspection and process
knowledge.
- For example, the output of water used for sanitary purposes,
including water used in toilets, showers, food preparation, dish
washers and human consumption is primarily to the wastewater
collection system. For sanitary usage, there is very little evaporation
or loss to ground, except for leaks from the process waste lines or
from the sewerage system.
- Similarly, the output for water used in irrigation, for example
watering green areas in the facility, is principally to the ground via
percolation into soil or leaks from the irrigation system piping and via
evaporation. For uses in the irrigation area, there is no wastewater
discharge.
There are numerous possibilities and combinations of water inputs and
outputs. Table 1 shown on below provides common inputs and losses and
resulting discharge as wastewater.
Plant Over Balance
Common Inputs Common Losses Wastewater
Water used in production
to clean equipment,
work areas, raw
material and
product containers
If elevated
temperatures are used
for cleaning, some of
the water can be
evaporated
Most of the water that
is used for cleaning
goes to wastewater
collection system.
Water used as an input
to a water treatment
process to make higher
quality water. For
example, purchased
water is used in water
treatment process to
produce a high quality
water via distillation or
reverse osmosis
followed by a
continuous deionizer
for a pharmaceutical
production process
While classified as a
loss, the output water
from the water
treatment process is a
loss.
There are several
wastewater treatment
processes. For filtration
and carbon adsorption,
there are backwash
streams which are
discharged to
wastewater. For
softeners, there are
also backwash,
regeneration streams,
and fast and slow
rinses.
For reverse osmosis
systems, there is a
reject stream that
commonly goes to
wastewater. For
continuous water
demineralizers there
are continuous
blowdown streams. For
distillation units, there
is a blowdown stream
and water blowdown
from the condenser.
for cooling
as one pass non-
contact cooling water
Generally no losses Generally non-contact
cooling water is either
discharged to a surface
water, recharged into
the ground or sent to
an on-site or off-site
wastewater treatment
facility
to cool and lubricate
pump seals
Generally no losses Commonly this water is
discharged to the site's
wastewater system.
Water used for sanitary purposes
Toilets To wastewater
Showers To wastewater
Food Preparation To wastewater
Drinking Water Consumed though a
small amount
Dishwasher To wastewater
Area cleaning To wastewater
Water used in utilities
as an input to a water
treatment process to
produce softened water
and or higher quality
water for boiler feed
water and or cooling
tower makeup
as makeup to the
cooling towers
Water which evaporates
from the cooling tower
and drift losses from ID
fans
Cooling tower blow
down, side stream filter
blow down
as boiler feed water steam/water which is
evaporated,
water/condensate which
is lost from steam traps
Boiler blowdown
as once through cooling
for compressors,
chillers and other
equipment
Generally no losses Discharge to surface
water or wastewater
as water to inject into
gas turbines to reduce
Nox emissions
Water is evaporated Generally no
wastewater discharge
Water used for
Irrigation
to irrigate the lawns,
shrubs, plants, fields
(the green areas)
Discharge to ground Runoff can enter
wastewater collection
Calculations, Published Factors to Prepare a Balance
Sanitary Water Usage 10 -25 gallons per
person per shift
The lower value is used
where there are just
toilets. A higher value
is used where there are
toilets, showers, full
kitchen services, that
is, food preparation
and dish washing.
Irrigation Usage Number of sprinkler
heads x the flow
capacity per head, e.g.
2.5 gpm x the duration
(minutes) of water
application
Inspect the irrigation
system during
operation to determine
if there are leaks from
broken sprinkler heads
and from water
distribution lines.
Wastewater Streams from Water Treatment Operations
Reverse Osmosis Reject
Flow
Reject stream generally
ranges from 25 to 50%
of the feed to the
system
Reject flow can be
higher than the
indicated range. RO
reject streams can be
used as cooling tower
makeup if the water is
softened prior to the
reverse osmosis
system.
Backwash & Rinse
Rates
Backwash, regeneration
and rinse rates can be
obtained from
manufacturer's
literature. The rates
should be verified in the
field.
Cooling Tower Usage Sum of Water lost via
windage + water
evaporated from the
tower + blow down
from the tower
Windage is the water
driven from the tower
due the tower fans. The
windage loss decreases
if the tower is provided
with a mist eliminator.
Windage Rate Commonly 0.1 to 0.3 %
of the Recirculation
Rate
The Tower recirculation
rate can be obtained
from the manufacturers
literature and or head
versus flow curve for
the pump
Tower Evaporation Rate C x _T x Cp / (Hv) C is the tower
recirculation rate in the
units of lbs of water per
minute , T is the
temperature difference
across the cooling
tower in degrees
Fahrenheit, Cp is the
specific heat = 1
BTU/lb and Hv is the
heat of vaporization =
1,000 Btu/lb of water
evaporated
Cooling Tower Blow
down Rate
(Windage Rate x
( Cycles of
Cycles of Concentration
= conductivity or
Concentration -1) -
Tower Evaporation
Rate) / (1- Cycles of
Concentration)
chloride level in the
cooling tower
blowdown/ conductivity
or chloride level in the
cooling tower makeup
water
Boiler Usage
Boiler make up Boiler Steam Rate -
Condensate Return +
Boiler Blow Down
Boiler Blow down Range of 4 to 8 % of
boiler makeup
Table 1: Description of Common Inputs, Losses and Wastewater
Discharges
- Where the inputs and output flows are not measured, estimates of
water flow can be obtained by calculation, process knowledge and
engineering judgment.
- At many facilities, the utilities area is the largest user of water.
Reasons:
Facility in a warm climate which requires controlled humidity and
temperatures in the production and packaging areas uses a
significant amount of water in the cooling towers to remove heat
from the sites chillers
Water is blown down from the cooling tower at a higher rate than is
required to control corrosion, scaling and bio-fouling.
Facilities that generate steam for production and heating or cooling
purposes which have low rates of condensate return can use
considerable amount of water.
1.1.3.Water Consumption and Generation
The plant needs to reduce its water consumption because it was
facing uncertainty in the sustainability of its water supply for new drug
products. They rely most on the water authority for water supply.
Therefore, it is very difficult for them to get a constant water supply.
Besides, the groundwater was polluted with saltwater intrusion and also
other property contamination. Reducing consumption of water in the
factory brings a lot of impact on reliability on the water authority as well as
saving cost of production. Since pharmaceutical companies need a large
amount of water, reducing is another way to reduce cost in their plant.
Reducing wastewater generation will definitely benefits to the
environment. Water pollution has been increasing drastically throughout
the years and it have been said that the freshwater sources have been
depleting towards the years. Wastewater can be recycled, but water
treatment operations have to be used in order to recycle them. Therefore,
reducing wastewater can help the treatment plant to lessen their burden as
well as preventing pollution to the environment. As for the plant, the
wastewater generated from the utilities is less polluted and can be treated
or safe to be used for other purposes such as sanitary and also irrigation.
From here, it will not only reduce the wastewater generation but also
reduces the water consumption in the plant. This enables the company to
use the water more efficiently.
1.1.4.Water Pinch Analysis
1.1.4.1. Introduction
Water Pinch Analysis or known as WPA is a concept of systematic
technique for reducing water consumption and wastewater generation
through many processes or activities that uses water. This concept
originates from the heat pinch analysis. The WPA was first used by Wang
and Smith. From there onwards, it has been widely used as a tool for water
conservation in industrial process plants. Now, they have even applied it for
urban or domestic building.
Techniques for setting targets for maximum recovery of water
capabilities of any type of water using operation includes mass transfer and
non mass transfer based systems. These include the course and sink
composite curves and water cascade analysis (WCA). The source and sink
composite curves is a graphical tool for setting water recovery and also the
design of water recovery networks.
We have identified one of the software which is called the Water
Design. Water Design is a software tool which is sufficient for developing
many aspects of water pinch analysis and synthesis. This software could
cover chapter 1 to 7 of the Industrial Water Reuse and Wastewater
Minimization by Mann, J.G. and Y.A. Liu, Mcgraw-Hill, 1999. It originates
from the Virginia Polytechnic Institute and State University, Blacksburg,
Virginia, United States.
1.1.4.2. Advantages
Advantages
Free software
Easy to install and user friendly
Capable of solving most of the water pinch analysis problems
Compact size of software size
Won many awards from the institution level up to international level.
Compatibility with Window Vista, and XP
1.1.4.3. Important Parameters
The important parameters that have to been included into the software are
Limiting flowrate (ton/hr)
Limiting inlet concentration (ppm)
Limiting outlet concentration(ppm)
1.1.4.4. Approach used and why, source to be reuse and assumptions
As for the approach for the plant, firstly, the main water source usage was
analyzed into sections. From here, few sections have been analyzed to
have large amount of water consumption. The water consumption is as
follows:
Section Water Consumption (gallons per
day)
Production 66,045
Sanitary 30,000
Irrigation 34,000
Utilities 199,955
total 330000
Table 2 : Water consumption according to sections
After knowing the water consumption in each section, we analyzed the
limiting water concentration consumption in each section. Then,
assumption has been for setting the minimum water targets for the plant
water usage. Assumptions have been made as follows:
Section Limiting Inlet
Concentration(ppm)
Limiting Outlet
Concentration(ppm)
Production 0.00 150.00
Sanitary 5.00 100.00
Irrigation 5.00 50.00
Utilities 0.00 10.00
Table 3 : Limiting concentration for each sections
As shown above, assumptions have been made on the limiting inlet
concentration as well as the limiting outlet concentration. These
assumptions have been made from references from journals as well as
books. In pharmaceutical companies, production section must use water
with 0 ppm concentration due to consumption purposes. Most of the water
in the production section is used for cleaning the equipment and also some
are used in the process. While for sanitary, a little concentration was
allowed as the water is only used for flushing the toilet and washing the
toilet. Similarly, a little concentration was also allowed for irrigation as it is
only used for flowering and gardening purposes. Utilities must use 0 ppm
water concentration as well, due to prevention of corrosion and also
contamination of the equipments. Utilities refer more to cooling towers and
boilers in this section.
The source of stream wanted to be reused is the water from the
utilities because the wastewater does not contain too many impurities
inside it and therefore, can be used for irrigation and also sanitary
purposes.
1.1.4.5. Process flow diagram of the water analysisFigure : Process flow diagram of the water analysis
The blue line denotes freshwater, green line denotes recycle water
and finally the red line denotes wastewater. Operation 1 represents
production, operation 2 represents sanitary, operation 3 represents
irrigation and finally operation 4 represents utilities. The diagram also
denotes the impurities concentration at each operation. The limiting inlet
and outlet concentration is also shown to let the users know the amount of
water that can be recycled. As shown, operation 4 which is the utilities can
recycled back their water source to the operation 2, sanitary and operation
3, irrigation at 10ppm. This is because the water concentration recycled
back into the operation 2 and 3 is within the range acceptable for the
operation (Table 2 ). Total flow rate recycled is also shown in the diagram
with 2.35ton/hr for operation 2 and 2.70 ton/hr for operation 3.
1.1.4.6. Results of the approach and how to use pinch analysis
Our approach is quite similar with the water pinch analysis results.
From the assumption made on the limiting concentration of the water, we
can estimate the water source that we can recycle. As estimated, the water
source from the utilities can be recycled due to the low contamination of
the water. By inserting the data into the water pinch analysis, it shows that
which operation we can recycle the water from. Indirectly, this can reduce
the water consumption for the respectively operation later on. From this
case, water consumption for sanitary and also irrigation can be reduced
because the water consumption can be recycled from the water used in the
utilities.
1.1.4.7. Graphs and diagrams to support our results
There are two diagrams that can be used to support our results. As
we can see from Figure 1, water concentration at operation 4 is within the
range of operation 2 and 3. Therefore the water pinch can be applied into
this section. The water pinch can be done at 10 ppm as highlighted in the
diagram.
Figure 1: Concentration-Interval Diagram
While the second diagram will be the concentration-composite curve,
where it shows how the wastewater and also the freshwater intersect in the
graph in terms of concentration. Red line represents wastewater while blue
line represent freshwater. The graph shows that intersection of the red line
and blue line is at 10 ppm which represents the freshwater can be pinch for
usage in the operation. Each slope represents the water concentration in
the operation. The minimum flow rate is 31.20 ton/hr while the average
outlet concentration is 77.15 ppm.
Figure: Concentration-Composite Curve Graph
1.1.5.Conclusion
Before water pinch analysis, total water consumption is 330000 gpd.
After water pinch analysis, the total water consumption is 266000.
Therefore, there have been reductions of 64000gpd in the water usage or
19.4% in percentage terms.