Presented by Haleimah Mohamed199903922 Tamadher Ali Mohamed199902261 Reem Khalifa199902241 Fatima...
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Transcript of Presented by Haleimah Mohamed199903922 Tamadher Ali Mohamed199902261 Reem Khalifa199902241 Fatima...
![Page 1: Presented by Haleimah Mohamed199903922 Tamadher Ali Mohamed199902261 Reem Khalifa199902241 Fatima Al-Zarouni199903949 Under the supervision of Dr. Mohamed.](https://reader031.fdocuments.us/reader031/viewer/2022013003/5519ea90550346d67b8b4b3a/html5/thumbnails/1.jpg)
Presented byPresented by
Haleimah MohamedHaleimah Mohamed 199903922199903922
Tamadher Ali MohamedTamadher Ali Mohamed 199902261199902261
Reem KhalifaReem Khalifa 199902241199902241
Fatima Al-ZarouniFatima Al-Zarouni 199903949199903949
Under the supervision ofUnder the supervision ofDr. Mohamed AbdulkarimDr. Mohamed Abdulkarim
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HCl Al2(SO4)3.14.3H2O
SBS
Disinfection pH adjustment
Anti-scalant addition
Media Filter
Coagulation unit
CartridgeFilter
Disinfection(Chlorination)
De-Chlorination unit
Neutralization pH adjustment
Storage Tank
RO
Membr
ane
NaOCl
Hypersperse AS110
HPP
NaOHNaOCl
Pump
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Used to prevent reverse osmosis membrane from fouling by removing large percentage of suspended solid from feed water
SDI measurement commonly used to indicate the effectiveness of media filter
Almost, all RO membrane manufacture recommends SDI to be less than 3
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[Ksp] =2.44 x10-5
[Ksp] =1.05 x10-4
93.176 L/day
[Ca+2] x [SO4-2]= 4.23 x 10-4 mol/L
Ksp= 2.44 x 10-5
The equation of calulating the dose rate
Antiscalant (Hypersperse AS110)
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Plant SDI before cartridge
SDI after cartridge
Al Jubail, Saudi Arabia RO desalination plant
3 2.8
Singapore pilot plant 6.5 6.1
desalination plant at Larnaca, Cyprus
3 2.8
in
outin
SDI
SDISDIremoval
%
%6removal
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%6removal
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Normally, the available free chlorine concentration before RO membrane is 0.5 – 1 ppm.
The maximum allowable chlorine concentration before RO membrane is 0.05 ppm.
Residual free chlorine can be removed by:
adsorption onto activated carbon media filter
chemical reducing agent (SBS)
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Sodium Bisulfite can be formed by dissolving Sodium Metabisulfite (SMBS) in water
In practice, designers used to add 3 mg/L of SMBS of chlorine
Total amount of free chlorine in water = 503 * 106 mg /day
32522 2NaHSOOHOSNa
In theory, 1.34 mg of SMBS will remove 1 mg of free chlorine.
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The amount of SMBS needed to remove free chlorine = 7968.22 mole/day
The dosage rate of SBS needed to remove residual chlorine = 205.58 gal/day
The amount of moles of Sodium Bisulfite needed to remove the free chlorine = 15,936.13 mole/day
SMBS
H2O SBS
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Q6
Stage 1 Stage 2
Q1 Q2 Q4
Q5Q3
RO membrane
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Parameters Value
Overall Recovery% 30%
Recovery for second stage 85%
Salt rejection % 95%
Total product 40MGD
Total dissolved solid for total product 170 ppm
Total dissolved solid for feed 43153ppm
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100%covRe rateflowfeed
rateflowPermeateery
Q2 =47 MGD
Q6
Q1 Q2 Q4
Q5Q3
ionconcentratsaltfeed
ionconcentratsaltpermeaterejectionsalt 1
TDS2 = 2156.79 ppm
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Material balance on first stage:
ppmTDS
QTDSQTDSQTDS
654883
321
Q6
Q1 Q2 Q4
Q5Q3
554422 TDSQTDSQTDSQ
TDS5 =13415 ppm
Material balance on second stage:
664411 TDSQTDSQTDSQ
The overall salt balance for the system
TDS6= 61550.46 ppm
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Added for pH adjustment to minimize the corrosion in the product water pipes
The calculation was based on
The required pH for drinking and potable water is in the range of 6.5 – 9.5
Neutralization of acid
Adjust pH from 7 to 8
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Capacity of each filter = 600L/min
number of filter = 582 filter
349 x 103 L/minFeed flow rate =
feed water flow rate / filter capacity = Number of filter element
Filter cartridge/ vessel = 26Number of vessel = 25 ( 23 in operate + 2 standby)
ΔP = 4 psi per 1 m3/min
The feed flowrate inter each vessel= 15 m3/min
Total ΔP = 15 x 4 = 60 psi = 4 bar
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number of module =
min19mod
GallonQ ule
min92361
GallonQ feed
4861mod
ule
feed
Q
Q module
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number of configuration = 203 configuration
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ions C (mg/l) C (mol/L)
Mg+2 829.35 0.03412
Ca+2 488 0.0122
Na+ 13160.22 0.572
HCO3
_ 115.9 0.0019
SO4-2 3473 0.03617
Cl- 23811 0.6726
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32899.1 im
iosm mTP 27319.1
psiPosm 28.471
For feed
elementAreaelementmembranefluxQ vesselper #,
vesselsper
stageper
Q
QvesselsofNumber
,
1,
6 vesselsofNumberelementofNumber
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properties Stage #1 Stage#2
Permeate flow 47 MGD 40 MGD
Qper,vessel 2755 L/h 2755 L/h
# of vessels 2690 2290
# of element 16140 13740
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One vesselsFeed
Permeate
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7.101.0 fcfc qnq
2
floweconcentratflowfeedq fc
The calculations of pressure drop in RO membrane
vesselsoneperpsiq fc 7.1738.28601.0 7.1
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1. Chemicals• Sodium Hypochlorite • Antiscalent • Hydrochloric acid (HCL) • Sodium bio-sulphate • Coagulant (Aluminum sulphate) • NaOH
2. Process • MMF• Membrane • Desalination plant Intake
3. Products• Brine
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1. Chemicals
2. Process
• Sand filter
Advantage: Sand work as a filter
Disadvantages: Need higher pressure Limits on flow rate Cost
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1) Mix brine with seawater before discharge.
3. Products
2) More than one discharge.These are located a way of each other at a
distance.
RO plant
Feed seawater
To seawater
5) Deep well disposal
3) Mixing brine water with cooling water coming from adjacent power plant.
4) Evaporation ponds
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PID Before HAZOP
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HAZOP analysis on water feed entering multi media filter. (Line no. 2)
Guide Word
Deviation Causes Consequences & Action
NO FLOW Pump failure Ruptured (broken) pipeValve (V2) shut
No productoCheck valveoCheck & Repair pump and pipeoPut flow indicator (FI 2)
LESS FLOW Pipe leakagePump failure
Low production qualityLess feed pressureSlow operationoCheck & Repair pump and pipe
MORE FLOW Damage pump The multi media will be shutdown.The ratio between feed water and coagulant is not the same Need to fix coagulant dosingThe efficiency of media filter will decrease.The suspended solid will not be removedLower the product quality Over flowLower removal capacityoCheck & Repair V2
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PID After Hazop
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