Environmental Engineering (Course Note 2_revised) Joonhong Park Yonsei CEE Department 2015. 03. 09.
Environmental Engineering (Course Note 2_revised)
Joonhong ParkYonsei CEE Department
2015. 03. 09.
Extensive and Intensive Properties
Extensive properties: dependent upon the size of the system or the sample.
Intensive properties: independent of the size of the system or the sample.
Question: which are extensive properties among the followings?
Mass, Energy, Heat Capacity, volume, temperature heat capacity, and pressure.
Measure of Quantity and Concentration
The quantity of a substance: expressed in terms of mass or weight, volume, or number of moles.
Concentration: the quantity of a substrate (i) in a certain quantity of a particular phase (j)
quantity of a substrate (i)C(i,j) =
quantity of a particular phase (j)
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Concentrations and Other Units of Measure
How many molecules in a mole?
Concentration Units-Mass based, mg/L or g/L-Mole based (Molarity), mol/L or M-the concentration of charge associated with ions in water (Normality) eq/L = M X [charge/ion]
Example) 47.8 g of MgCl2 is dissolved in one liter of water. Calculate its mass-based concentration, molarity, and normality.
Ref) Atom mass for Mg = 24.3 g/mole; Atom mass for Cl = 35.5 g/mole
Concentration unitsConcentration units
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p-notation: negative logarithm of the molar concentration of a substrate, pC = -log [C]
e.g. pH = -log [H+]
Equivalent (eq): the quantity of a substrate equivalent to the quantity of the product in a particular reaction.
e.g. For the sulfuric acid reaction:
H2SO4 + 2H2O = 2H3O+ + SO42-
1 mol H2SO4 equivalent to 2 mol H+
Cf) centi-, milli-, micro-, nano-, pico-,…
Other expressions for concentrations
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Mass Fraction and Mole Fraction
Represent the ratio between the amount of the species and the total amount of the solution (fluid plus species)
% (percent): 1 part species per 100 parts solution%o (per mil): 1 part species per 1000 parts solutionppm (part per million): 1 part species per 106 parts solutionppb (part per billion): 1 part species per 109 parts solutionppt (part per trillion): 1 part species per 1012 parts solutioncf) molecular fraction, mass fraction, volumetric fraction
By convention (in general):-In air, fractions are generally expressed on a molar or volume basis (ex. 5ppb benzene = 5 x10-9 mole in a mole of air)-In water, fractions are generally expressed on a mass basis (ex. 5ppb benzene = 5 x10-9 gram in a gram of water)
FractionFraction
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Partial Pressure
Species amounts in air may be expressed in terms of partial pressure.
Idea gas law: PV = nRT (cf. M = n/V = P/RT) here P=pressure, V=volume, R=idea gas constant (82.05 *10-6 mol-1 m3 atm K-1) T=absolute temperature (oK)
pi =Pi/Pair = (ni/Vi)/(nair/Vair)
Example) 5ppb benzene in air at Pair = 5 x 10-9 atm
Ideal gas lawIdeal gas law
Partial pressurePartial pressure
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Unit Conversion
Mass Conc. = molecular weight of species i * molarity of i. Ex) Mass concentration of benzene (C6H6) = 5μg/L Molecular weight of benzene = 12 x 6 + 1 x 6 = 78g/mol Molarity of benzene = 5 (μg/L) / 78 (g/mol) = 0.0128 μmol/L or 0.0128 μM
Mass concentration = solution density * mass fraction cf) Solution of density in dilute solution in water = 1g/ml
The molecular fraction of a species: Yi = Ci / Cair
Cair = P/RT When P = 1atm and T=293 oK, Cair = 41.6 mol/m3
[R=82.05 x10-6 atm * m3/(mol * K)] Ci = 41.6 μmol/m3 corresponds to a mole fraction of 1 ppm.
Some Basic Units and Conversion Factors
Quantity SI units SI symbol ConversionFactor
USCS units
LengthMassTemperatureAreaVolumePowerVelocityFlow rateDensity
MeterKilogramCelsiusSquare meterCubic meterKilojouleWattMeter/secCubic meter/secKilogram/cubic meter
MKgoCM2M3kJWm/sm3/sKg/m3
3.28082.20461.8 (oC) + 3210.763935.31470.94783.41212.236935.31470.06243
ftLboFft2ft3BtuBtu/hrMi/hrft3/sLb/ft3
Common Prefixes
Quantity Prefix Symbol
10^-150.0000000000010.0000000010.0000010.0010.010.110100100010000001000000000100000000000010^1510^1810^2110^24
femtopiconanomicromillicentidecidekahectokilo
megagigaterapetaexa
zettayotta
fpnμmcddahkMGTPEZY
Precision and Accuracy
PrecisePrecise ImpreciseImprecise
AccurateAccurate
InaccurateInaccurate
Contents:
1. Material Balance Concepts
2. Characteristic times
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Components in Mass/Material Conservation Law
(Mass/Material Balance)
Accumulation rate = Input rate – Output rate + Reaction rate
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Material Balance
Model containers and flow paths Model containers and flow paths in environmental systemin environmental system
closedopen
Converging flow paths Diverging flow paths
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MB1: the amount of a conserved property in a closed container does not change
MB2: the rate of change in the amount of a nonconserved property within a closed container is equal to the net rate of production of that property within the container.
MB3: the rate of change in the amount of a conserved property in an open container is equal to the difference between the rate of flow of that property into the container and the rate of flow out of the container.
MB4: the rate of change in the amount of a nonconserved property in an open container is equal to the rate of flow in, minus the rate of flow out, plus the net rate of production within the container.
Material Balances (MBs)
Different types of MBsDifferent types of MBs
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Batch (Closed) Systems with Conservative Pollutants (MB1)
Accumulation rate = Input rate – Output rate + Reaction rate
Input rate = 0, Out rate = 0 since closed system
Accumulate rate = Reaction rate = 0 since cons. material
(assumption: completely mixed; no sink or no source)
Closed
V: Control Volume (Reactor Volume)C: Cons. Pollutant Conc.
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CompletelyMixedBatch
Reactor(CMBR)
Reactor Volume (V)
Situation: At t = 0, add C pollutant
at Co concentration
Example for MB1
Co
Time (t)
Con
s. P
oll.
Con
c.
0
Reactor Observation
Question:
In the reactor, what would be concentrations at different locations?
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Batch (Closed) Systems with Nonconservative Pollutants (MB2)
Accumulation rate = Input rate – Output rate + Reaction rate
In this case, Input rate = Output rate = 0 (since closed system)
Accumulation rate = Reaction rate for NC Pollutant(assumption: completely mixed; no sink or no source)
Closed
V: Control Volume (Reactor Volume)C: NC Pollutant Conc.
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CompletelyMixedBatch
Reactor(CMBR)
Reactor Volume (V)
Situation: At t = 0, add NC pollutant
at Co concentration
Example for MB2
Co
Time (t)
NC
Pol
l. C
onc.
0
Accumulation rate at t = V * (dC/dt) observed in the reactor at t(function of reactor configuration and other system factors)
Reaction rate = V * (dC/dt) intrinsic reaction rate(function of chemical property and transformation process)
At CMBR, V * (dC/dt)reactor = V * (dC/dt)reaction
Reactor Observation
Question: What if t = infinitely long?
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Open Systems with Conservative Pollutants at SS
(MB3)
Accumulation rate = Input rate – Output rate + Reaction rate
At Steady-State (Water & Pollutant), Accumulation = 0Since the pollutant is a conservative material, intrinsic reaction rate = 0 Input rate = Output rate
CompletelyMixed
ContinuousFlow (V, C)
V: Control Volume (Reactor Volume)C: Cons. Pollutant Conc.
Cin=CQin =Q
Cout =C, Qout = Q
Terminology:•CSTR: Completely Stirred Tank Reactor•CMCFR: Completely Mixed Continuous Flow Reactor
Question: By the way, what is steady state??
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Steady-State Conservative Systems at SS
Steady State: Accumulation rate = 0Conservative Pollutant: No transformation rate
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Example: Steady-State Conservative Systems
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Steady-State Conservative Systems
Step 1: Make simplified the situations (Sketch)Step 1: Make simplified the situations (Sketch)
Qs
Cs
Qw
Cw
Assumptions: conserved properties converging flow paths steady state
Qm
Cm
What materials?What Processes? (Transformation? Transport?)
Cw: contaminant concentration in wastewaterQw: volumetric flow rate of wastewaterCs: contaminant concentration in upstream riverQs: volumetric flow rate in upstream riverCm: contaminant concentration in downstream riverQm: volumetric flow rate in downstream river
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Steady-State Conservative Systems
Qs
Cs
Qw
Cw
Water Balance: Water Density *Qm = Water Density * (QS + QW)
Contaminant Balance: CmQm = QSCS +QWCW
Qm = Qs + Qw = 10.0 m3/s + 5.0 m3/s = 15.0 m3/s
Cm = (CsQs +CwQw)/Qm = (20.0*10.0 + 40.0*5.0) (mg/L * m3/s) / (15.0 m3/s) = 26.7 mg/L
Accumulation Rate = Input Rate – Out Rate + Reaction RateSteady-State means Accumulation Rate = 0Conservative Materials means Reaction Rate = 0Therefore, Input Rate = Out Rate
Qm
Cm
Step 2: Set the material balancesStep 2: Set the material balances
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Steady-State Systems with Nonconservative Pollutants (MB4)
Accumulation rate = Input rate – Output rate + Reaction rate
At Steady-State (Water & Pollutant), Accumulation = 0 Reaction rate = - V * (dC/dt) 0 = Input rate - Output rate + Reaction rate 0 = Cin * Q - C * Q - V * (dC/dt) => C*Q = Cin*Q - V*(dC/dt) => C = Cin – V/Q * (dC/dt) here V/Q = hydraulic retention time
CompletelyMixed
ContinuousFlow (V, C)
V: Control Volume (Reactor Volume)C: NC Pollutant Conc.
CinQin =Q
Cout =C, Qout = Qin =Q
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Characteristic times
Def: magnitude estimates of the time required for a process to approach completion.
When t >> τ (fast process); When t << τ (slow process)
When t ~ τ (intermediate cases)
Characteristic time (Characteristic time (ττ))
Def: a magnitude estimate of the average time that a molecule of a specific matter(or material) will remain in the system before being removed by flow out of the system.
Characteristic residence time (Characteristic residence time (ττrr))
S (stock): the amount of the materials in a system
Fin (flow in) Fout (flow out) Assume FAssume Finin = = FFoutout= F= F
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Example: Characteristic residence time
Given) In Nanji Wastewater Treatment Plant (Seoul, Korea), wastewater flows into its treatment reactor at a steady flow rate (Q) of 1,000 m3/day, and flows out of the treatment reactor at the sample steady flow rate. The volume of treatment reactor (V) was 50 m3.
Mission) Calculate the characteristic residence time of a water molecule
Step 1: Identify S
☞ NOTE: What assumptions may be needed?
Step 2: Identify F
☞ NOTE: Any assumptions to be made?
Step 3: Calculate residence time by S/F in hours
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Reading Assignment and HW#2
Reading Assignment: EES (Environmental Engineering Science, Nazaroff & Alvarez-Cohen) pp. 1-25
H.W.#2
In EES, solve some problems in Chapter 1 (p.26-29)
-1.1, 1.2, 1.3, 1.8, 1.9, 1.12, 1.14
-Due( 제출마감일시 ): March 23 (6pm) at C218