Environmental Engineering : Treatment of raw water

By Aditya Kumar|Updated : September 8th, 2021

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Treatment of Water

 

 

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Theory of Sedimentation

·     Stokes Law

(a)

 byjusexamprep for d < 0.1 mm.

 Where,

 byjusexamprep The velocity of the settlement of particle in m/s.

 byjusexamprep The diameter of the particle in the meter.

 byjusexamprep SP gravity of the particle

 byjusexamprep 

 byjusexamprep Kinematic viscosity of water in m2/sec.

(b)

byjusexamprep 

 byjusexamprep 

 byjusexamprep 

(c)

byjusexamprep 

 Where,

 T = Temperature of water in oC

 byjusexamprep is in mm/sec.

 d is in mm.

(d) byjusexamprep 

(e) byjusexamprep 

Sedimentation Tank : Surface Over flow Rate

(a) byjusexamprep 

 byjusexamprep 12000 to 18000 lit/m2 day for plain sedimentation.

 byjusexamprep 24000 to 30,000 lit/m2/day for sedimentation with coagulation.

 

byjusexamprep

 

(b) Velocity of flow, byjusexamprep 

(c) Time of horizontal flow, or Detention time

 byjusexamprep 

(d) Time of falling through height ‘H’

          byjusexamprep

(e) Detention time,

             byjusexamprep 

    For plain sedimentation tank → 4 to 8 hours

    For sedimentation with coagulation → 2 to 4 hours

 

(f) byjusexamprep Efficiency

 byjusexamprep 

 where,

 byjusexamprep of lighter particles (with settling velocity (Vs )less than Vo ) which shall be removed in an ideal settling basin.

(g) % of particle removed

 byjusexamprep 

 where corresponds to byjusexamprep 

 

byjusexamprep

 

(h) Detention time ‘t’

 byjusexamprep for a rectangular tank.

 byjusexamprep for circular tank

 where,

 d = Dia. of the tank

 H = Vertical depth of wall or side water depth

(i) byjusexamprep

(j) Scour velocity, byjusexamprep 

 Where,

 byjusexamprep 0.04 for uniform granular sand and 0.06 or more for non-uniform (interlocking) sticky material.

 byjusexamprep Darcy Weisbach friction factor.

 = 0.025 to0.03 for settling tanks.

 

Chemicals used for Coagulation

·     Alum byjusexamprep 

 byjusexamprep 

 666 gm of Alum reacts with 48 gm of to byjusexamprep give 146 gm of byjusexamprep 

 byjusexamprep 1 gm of Alum reacts with 0.73 gm of byjusexamprepalk. or 0.45 gm of byjusexamprepalk.

 to give 0.234 gm of Al(OH)3 ppt.

 byjusexamprep 

·   Copperas byjusexamprep 

 byjusexamprep 

·    Chlorinated Copperas : byjusexamprep 

 byjusexamprep

·    Sodium Aluminate

 byjusexamprep 

 Mixing Basin

 byjusexamprep 

 Where,

G’ = Temporal mean Velocity gradient (per second).

P = Power dissipated in watts i.e., N-m/s.

V = Volume of raw water to which P is applied in m3.

byjusexamprep Dynamic viscosity (N-s/m2).

Flocculation

·    Velocity gradient,

      byjusexamprep 

·     byjusexamprep 

·   Detention time is 10 to 30 minutes.

·    byjusexamprep 

·    Number of particle collision byjusexamprep 

·       byjusexamprep 

·      byjusexamprep 

 Filtration

 

A. Slow Sand Filter

· Depth of filter is 2.5 to 3.5 m.

·  Plan area of the filter is 100 to 200 m2.

·  byjusexamprep 

·    byjusexamprep 

·    Design period = 10 years.

·    Depth of sand is 90 to 110 cm.

·    Frequency of cleaning is 1 to 3 months

·    Rate of filtration = 2400 to 4800 lit/m2/day or 100 to 200 lit/m2/hr.

·    Efficiency of bacteria removal = 98 to 99%.

·    It can not be used if turbidity > 50 ppm.

·    It is designed for maximum daily demand.

·    byjusexamprep 

B. Rapid Sand Filter

·     byjusexamprep 

where,

N = Number of unit required

Q = Plant capacity in million lit/day (MLD)

·   byjusexamprep 

·    Sand layer depth is 60 to 90 cm.

·    byjusexamprep of sand is 0.35 to 0.55 mm.

·    Depth of tank = 2.5 m to 3.5 m.

·    Area = 10 to 80 m2 each unit.

·   Rate of filtration 3000 to 6000 lit/m2/hour (slow sand filter × 30)

·    Cross-sectional area of Manford = 2 × cross-sectional area of lateral.

·   Cross-sectional area of each lateral = 2 to 4 times cross-sectional area of perforations in it.

·  Total cross-sectional area of perforation = 0.2% of the total area of 1 filter bed

·     byjusexamprep 

·    4.5% of filtered water is used as a backwash.

·     30 min. used for backwash.

 

Hydraulics of Sand Gravity Filters

 byjusexamprep 

 Where,

byjusexamprep Frictional head loss through the filter in the meter.

byjusexamprep Approach velocity or filtration velocity in m/s.

byjusexamprep Depth of filter in meter

byjusexamprep Shape factor (for non-spherical particle)

byjusexamprep The diameter of sand particles in the meter.

byjusexamprep Accelerations due to gravity in m/s2.

byjusexamprep Porosity

byjusexamprep Newton’s dray coefficient.

byjusexamprep Mass friction of sand particle of dia d.

Rose Equation, byjusexamprep 

 

Hydraulic head loss and expansion of the filter during backwash of RSF

·   byjusexamprep 

 Where,

byjusexamprep= Head loss through the filter bed required to initiate expansion in the meter.

byjusexamprep Unit weight of meter in kN/m3.

byjusexamprep Depth of filter bed in the meter.

byjusexamprep Submerged unit weight of sand in bed of depth ‘D’

·     byjusexamprep 

·     byjusexamprep

Where,

byjusexamprep Depth of expanded/fluidized bed in the meter.

byjusexamprep The porosity of the expanded fluidized bed.

·    byjusexamprep 

·    byjusexamprep 

Where,

f = mass fraction of sand of various sizes in the sand (as per sieve analysis0

·  byjusexamprep 

·   byjusexamprep 

where,

byjusexamprep The porosity of the expanded bed

byjusexamprep Backwash velocity in m/s

byjusexamprep Setting velocity in m/s.

 

Disinfection or Sterilization

(i) Treatment with Ozone

 byjusexamprep 

(ii) Disinfecting Action of Chlorine

 byjusexamprep

 

 byjusexamprep 

 

(iii) Doses of Chlorine

byjusexamprep

(iv) Forms in which chlorine is applied

 (a) Free chlorine

 (b) Hypochlorites & Bleaching Powder

 (c) Chloramines

 (d) Chlorine dioxide

byjusexamprep 

Type of Chlorination

 (i) Plain chlorination

 (ii) Pre-chlorination

 (iii) Post-chlorination

 (iv) Double chlorination

 (v) Break point chlorination

 (vi) Super chlorination

 (vii) Dechlorination

 

byjusexamprep

 

Test of Chlorine Residual

1. Orthotoulidine test: color – matching method

2. Arsenide ortho-toulodine test – when mineral present in the water sample, Also a color matching method.

3. DPD and chlorotic test (Di-ethyl phenylene diamine): color making method.

4. Starch iodide Test

byjusexamprep

Water Softening

Methods of Removing Temporary hardness

 (i) Boiling

 byjusexamprep 

 (ii) Addition of lime

 byjusexamprep 

Method of Removing Permanent Hardness

 (i) Lime-Soda Process

 (a) byjusexamprep

 (b) (i) byjusexamprep

      (ii) byjusexamprep 

 (c) byjusexamprep 

 (d) byjusexamprep 

 (e) byjusexamprep 

 (f) byjusexamprep 

 (g) byjusexamprep byjusexamprepwhere,

byjusexamprep calcium hardness removed in mg/lit (expressed as byjusexamprep 

byjusexamprep Magnesium hardness removed in mg/lit (expressed as vbyjusexamprep

byjusexamprep Lime added in mg/lit (expressed as byjusexamprep

Zeolite or Base Exchange or Cation-Exchange Process for Removing Hardness

 byjusexamprep

Demineralization Process for Removing Hardness

 byjusexamprep 

Drinking water specification: IS: 10500, 1992 (Reaffirmed 1993)

Tolerance Limit

 

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