environment Flashcards
impacts of suspended solids in raw water?
- growth of disease causing micro-organisms
- aesthetically displeasing
- provides adsorption surface, interfere with chlorination
- incrustation of pipes
apparatus used for measuring suspended solids and acceptance limits?
muffle furnace
500 mg/l, 2000 mg/l
turbidity measuring methods and reference chemical
turbidity rod method -pt niddle, Si02 Jackson turbidity method -lighting candle, (0-25) JTU Baylis turbidmeater -color matching , absorption principle 0-2 NTU Nephlometer (0-1) NTU - scattering principle, formazene is used - FTU or NTU is unit, 1 NTU- 10 NTU
color measurement and limits
TinTometer
color matching technique, chloroplatinate ion
5 TCU - 25 TCU
measurement of alklinity
titration with 0.02N H2SO4
1 ml for 1mg of alklinity as CaCO3
ph 10 to 8.3 : Oh, 1/2 CO3 , phenopthelene indicator
ph 8.3 to 4.5: HCO3, 1/2 CO3, methyl orange
Limits 200 mg/l, 600 mg/l
Ph levels for drinking water
07 -8.5
6.5-9.2
corrosion and incrustation
number of rapid sand filter bed by Morell and Wallace equation
flow rate and depth and size of medium
N= 1.22 sqrt(Q) + 1(stndby)
Q - discharge in MLD
back-washing 45cm/min [6-16 X flow]
depth = (60-90 cm) & size=(0.35-0.55 mm)
R.O.F = 3-6 m/hr = 30 times slow sand
settling velocity of non laminar particle
if d > 0.1 Vs = [4/3 g.d.(G-1) /Cd ]^0.5 Cd= 0.4 for Re > 10^4 Cd= 24/ Re for Re<0.5mm Cd = 24 /Re + 3/sqrt(Re) +0.34 for transition
example applied??
effective height of stack
dH = [1.5 + 2.68PD *(Ts -Ta)/Ts] DVs /u
P ~ 1
T in kelvin
Factors to be considered in the design and operation of a sanitary landfill site
-Access to the site
-Cell design and construction
collection of gas and lechate
water table
-Cover material
1 Cum soil for 4~6 Cum of refuse
clayey soils are preferred
-Equipment’s required
earth movers
-Fire prevention
separations and water availability
-Land area
minimum 1 year dump, preffrable 5~10 years
-Land filling method
-Litter control
-Unloading Area
should be kept small, generally under 30 m.
-Drainage arrangements
drainage ditches shall be installed
1~2% surface slope must be there
INDORE meathod of refuse disposal
- manual turning of piled up mass for its decomposition under aerobic conditions.
- layers of vegetable wastes and night soil are alternatively piled in depths of about 7.5 to 10 cm each, to a total depth of about 1.5 m in a trench; or above the ground to form a mound called a windrow.
- The mixture is kept aerobic by turning regularly for 2 to 3 months.
- This compost mass is then left for another about 1 to 1½ months without any turning; after which, the compost becomes ready for use.
- The entire process thus takes about 4 months.
Design of manifold lateral under drainage of rapid sand filter
Area of perforation = 0.2% x Area of filter Area of each lateral = 2 x Area of perf. Area of manifold. =2 x Area of lateral Find Dia of manifold assume spacing of laterals as 15 cm No of laterals = L / 0.15 Length of laterals = 0.5*[L -D] assume dia of perforation = 6 mm find No of perforation in all laterals N = Area of all perf /Ap1 find Area and dia of each lateral Check Lateral.Length/Dia.lateral <60
back-washing check:
velocity in laterals and manifolds < 2.4 m/s
four mechanisms of coagulation
1. ionic layer compression (van der waal's force vs zeta potential) 2. adsorption and charge neutralization (aqua metallic ions or hydro-oxides) 3. sweep coagulation 4. inter-particle bridging
blade floculator design points
P = F.V
P=μ.V.G^2
Cd = 1.8 for flat blades
V = 75% of blade center Velocity
oxidation pond design characterstics
detention time = 2~6 week OLR = 150 kg/ha/day depth = 1~ 1.8m only area of unit = 0.5~1 acre pathogen removal= 99% BOD removal = 95%
design of inlet pipe
v=0.9m/s, [Q =VA]
D.outlet = 1.5 D.in
environmental impact assessment
prepared and submitted along DPR
compulsory by GOI in all projects
Methodology
1. Impact identification
checklist, matrices, networks, activity and connected impact
2.Prediction of E.Impact
greatest degree of scientific application, real impacts of proposed development by performing calculations
3. Evaluation of impact
conversion of impacts in a comparable units and normalization.
conversion in monetary values to make it comparable with other cost and benefit of project
KMnO4 points
- water contaminated with lesser amount of bacteria is treated
- helps in oxidizing taste producing organic matter
- used as an algicide and for removing color and iron
- normal dose for disinfection 1-2 mg/L ,contact period 4-6 hrs
- 48 hrs dont use water
- kills 98% bacteria and 100% cholera virus
- dark brown precipitate
COD for glucose solution
180 g glucose + 196 g of O2
plume behavior coming out of stack
Looping= super adiabatic + strong wind
Neutral = upward vertical= near adiabatic + no wind
Coning = near adiabatic + winds
fanning =(horizontal)= negative adiabatic + wind
Lofting = inversion + super adiabatic + wind
Fumigating = super adiabatic + inversion + wind
Trapping = inversion+adia+ inversion + wind
various processing tehniques used in solid waste management
mechanical volume reduction (1100kg/cu.m)
thermal volume reduction
manual components separationx,
Land fill area method & Depression method & Trench method
Area method
- when area is unsuitable for excavation of trenches
- earthen levee is built first
- thickness of compacted waste 2-3 m
- 150 to 300 mm layer of cover material is placed over the completed fill
- completed lift including cover is called cell
trench method
- adequate depth of cover material is available & water table well below
- dragline or more scrappers are used
Depression method
- location where artificial or natural depression exist
canyons, ravines, dry borrow pits quarries
points on sanitary composting
- aerobic “INDORE PROCESS”
(2~3 months) mixing of refuse is ensured
left for 1.5 month - layers of vegetable waste and night soil are piled up alternatively 7.5cm and 10cm to a total 1.5 m
- anaerobic “BANGLORE PROCESS” (4~6 months)
- covered over by 15 cm earth and left
- decomposition start in 3-4 days and temp ~75 C
- end product is humus/manure/compost
- optimum C/N ratio = 30 to 50
Fire demand formulas
National board of Fire underwriters
Q = 4367 sqrt(P)[1 -.01*sqrt(P)]
P= population in thousands
Q= discharge in Ltr/minute
Kuchling’s formula
Q = 3182 *sqrt(P)
Freeman formula
Q= 1136 *[P/10 +10]
Buston’s formula
Q= 5663 * sqrt(P)
Control of Gas movement in landfill sites
By vents and barriers - gravels and clay
By gas recovery - gas recovery wells
Control of leachate Movement in land fill sites- geotextiles and clay