Presentation on theme: "CE 510 Hazardous Waste Engineering Department of Civil Engineering Southern Illinois University Carbondale Instructors: Jemil Yesuf Dr. L.R. Chevalier."— Presentation transcript:
CE 510 Hazardous Waste Engineering Department of Civil Engineering Southern Illinois University Carbondale Instructors: Jemil Yesuf Dr. L.R. Chevalier Lecture Series 6: Volatilization
Course Goals Review the history and impact of environmental laws in the United States Understand the terminology, nomenclature, and significance of properties of hazardous wastes and hazardous materials Develop strategies to find information of nomenclature, transport and behavior, and toxicity for hazardous compounds Elucidate procedures for describing, assessing, and sampling hazardous wastes at industrial facilities and contaminated sites Predict the behavior of hazardous chemicals in surface impoundments, soils, groundwater and treatment systems Assess the toxicity and risk associated with exposure to hazardous chemicals Apply scientific principles and process designs of hazardous wastes management, remediation and treatment
Volatilization Evaporation of solid or liquid into the gaseous phase Air emissions from hazardous management facilities regulated under Clean Air Act. May be considered Hazardous Air Pollutants (HAP)
Diagram of an air stripping tower. Water is piped into the top, and pours over the packing. A Counter current of air is blown into the bottom of the tower, and blows by the water, removing the contamination. contaminated water in clean water out packing support air blower clean air in packing material vent Engineered Systems: Air Stripping
Source Packing media: new and after four years
water table C.F. unsaturated saturated impermeable boundary LNAPL residual NAPL Engineered Systems: Soil Vapor Extraction air vent or injection well vacuum vapor treatment vent to atmosphere surface soil cap
A typical vapor phase GAC system. The grey cylinder on the right is an air/water separator. This unit is necessary to keep water from fouling the GAC vessels. Water removed from the soil gas is stored in the black tank on the right. The two white cylinders contain the GAC, which adsorbs organic contaminants from the soil gas. The grey unit on the left contains the blower that pulls the soil gas from the wells and through the vessels.GAC Source
Approach First we need to review the definition of vapor pressure and Henrys Law Volatilization from Deep Soil Contamination Volatilization from Surface Soils Volatilization from Open Containers
Vapor Pressure mm Hg 760 mm Hg 20 C T VP The temperature that causes the vapor pressure to reach 760 mm Hg is the boiling point of the compound. See Appendix J p. 705 Table 6.1 p. 309 Higher driving force
Class Problem Determine the vapor pressure for anthracene and carbon tetrachloride. Which is more volatile?
Henrys Law For a closed system Equilibrium between gaseous and aqueous phase Dilute contaminant P= partial pressure (atm) H = Henrys Law const. (atm-m 3 /mole) X = concentration (mole/m 3 ) H<10 -7 atm-m 3 /mole less volatile than water, conc. will increase. H>10 -3 atm-m 3 /mole volatilization is rapid
Henrys Law Henrys Law constant may also be considered a partition coefficient between air and water, analogous to the octanol-water partition coefficient Here, S is water solubility High water solubilities and low vapor pressure tend to decrease the potential for volatilization of dilute species
Henrys Law Correction for temperature See values Table 6.2 p Dimensionless quantity that may be used in design -the ratio of the mass of compound in the vapor phase to the mass of compound in the aqueous phase.
Class Problem Estimate Henrys Law constant for benzene at 30 C.
Solution From Table 6.2, A = 5.53 and B = compare to H = at 25 C
Class Problem Experimental determination and application of Henrys constant Air is comprised by 21% oxygen on a molar basis. If we bubble a large amount of air through a liter of water until it is saturated with the air, the amount of oxygen in the water at this condition of equilibrium is dictated by Henrys law. If the amount of oxygen is measured using a DO probe and is 9.3 mg/L, a)Calculate Henrys law constant b)Determine how much oxygen will be dissolved in water at 20 ºC if pure oxygen (P O2 = 1 atm) is bubbled through the water until it is saturated. Density of air at 20 ºC = 1.2 g/L Density of water at 20 ºC = 998 g/L
Solution a) Mass ratio of oxygen in the water: = 9.3 mg/L X g/mg X 1L/998 g = 9.3x10 -6 g-O 2 /g-water Mass ratio of oxygen in the air: Remember that 1 mole of any gas occupies L of volume at 1 atm. pressure and 20ºC (Ideal Gas Law) and density of air is 1.2 g/L, Number of moles of oxygen in 1 L of air is: = 0.21 X (1/24.05) moles = moles Mass ratio of oxygen in the air ( 1 liter basis) is then calculated as: = ( moles X 32 g/mole)/(1.2 g) = g-O 2 /g-air
Solution Henrys constant in non-dimensional form (H) is then: = (0.233 g-O 2 /g-air)/ 9.3x10 -6 g-O 2 /g-water Converting g-air and g-water into volume basis, multiplying the above expression by, (1.2x10 3 g/m 3 )/(0.998x10 6 g/m 3 ) H = (mol O 2 /m 3 -air)/(mol O 2 /m 3 -water) And from H = H/RT, H = HRT = x 8.21x10-5 x 293 = atm-m 3 /mol
Solution b) From Henrys law equation: P O 2 = H.X, And for pure oxygen, P O 2 = 1 atm; thus X = P O 2 /H = 1 atm/(0.725 atm-m3/mol) = 1.38 mol/m3 = 44.1 g/m3 = 44.1 mg/L......end of example
Estimation of Flux from an Open Container This term represents the driving force Q is the evaporation rate (mass/time) VP is the vapor pressure (atm) P is the partial pressure of the compound above the liquid If open, P = 0
Estimation of Flux from an Open Container where Q = mass flux (evaporation rate) M = molecular weight K = mass transfer coefficient per area
Estimation of Flux from an Open Container The mass transfer coefficient K can be estimated using water as a reference K w = cm/s Molecular weight of water = 18 g/m
Class Problem A container of benzene has been left open. Estimate the rate of volatilization across the surface of the container. The dimensions of the container are 1.25m x 0.75m x 0.3 m deep. The temperature is 20 C.
Approach Governing Equation
Solution 1.Need to solve for K. 2.Molecular weight of benzene is 6(12)+6 = 78 g/mol
Solution 3. Area = 1.25 m x 0.75 m = 0.94 m 2 4. Vapor pressure = 76 mm Hg = 0.1 atm Compare to Ex. 6.1 p. 313
Saturation in an Enclosed Area Spills in waste transfer areas drum storage areas Need to assess the saturated vapor concentration in order to assess toxicity or explosivity of the vapor Factors to consider: ventilation rate volume of enclosed space contaminant flow rate out of enclosed space contaminant volatilization rate
Saturation in an Enclosed Area where Q m = volatilization rate of the compound [M/T] (g/s) Q v = ventilation rate of the enclosed area [M/T] (m 3 /s) k = factor for incomplete mixing ( ) M = molecular weight (g/mol)
Class A container of benzene has been left open in a warehouse. The dimensions of the container are 1.25 m x 0.75 m x 0.3 m deep. The temperature is 20 C and pressure is 0.1 atm. The facility is 220 m 3 in volume. Ventilation is 12 changes of air per hour. Using k=0.2, determine the steady state benzene concentration in the warehouse.
Solution 1.From previous problem Q m = 1.55 g/s 2.Calculate the ventilation rate Q v = (12 changes of air/hr)(220 m 3 /change)(1 hr/3600 sec) = 0.73 m 3 /s
Solution Continued 3. Determine the steady-state benzene concentration
Volatilization from Soils Soil particles air water Sorption/desorption diffusion
Volatilization from Soils Soil particles air water sorption diffusion
Volatilization from Soils Soil particles air water sorption diffusion DOW researchers determined an empirical relationship for a first-order decay rate for contaminant loss from a surface spill, k v where VP = vapor pressure (mm Hg) K oc = soil adsorption coeff. (mL/g) S = solubility (mg/L)
Example A carrier has spilled lindane on soil. Estimate the time required for 70% volatilization.
Solution From reference tables in the appendix S = 7.3 mg/L Koc = 1995 mL/g VP = 9.4 x mm Hg
Volatilization in Deep Soils More complex Models are mostly specific to matrix Hamaker Equation one of the better generalized models and assumes that the contaminant zone is semi-infinite i.e. the contaminant zone extend into the aquifer and the source is large
Volatilization in deep soils Q t = volatilization of compound per unit surface area (g/cm 2 ) C o = initial concentration (g/cm 3 ) D = diffusion coefficient of vapor through coils (cm 2 /s) t = time (sec) Very few data are available for diffusion coefficients. This equation allows a prediction of D based on the known value of 0.01 cm 2 /s for ethylene dibromide and cm 2 /s for ethanol.
Problem Estimate the flux of benzene from a deeply contaminated soil over 1 day with a concentration of 500 ppm and a bulk density of 1.50 g/cm 3.
Data and Governing Equations MW Benzene 78 g/mol MW Ethanol 46 g/mol MW Ethylene dibromide 188 g/mol D for ethanol cm 2 /s D for ethylene dibromide 0.01 cm 2 /s
Solution D average = cm 2 /s 1. Determine D using both equations and take the average
Solution 2. Convert 500 ppm benzene to g/cm 3
Solution 3. Determine Q
Summary of Important Points and Concepts The two most important parameters for assessing volatilization are vapor pressure and Henrys Law constant Vapor pressure of hazardous waste range from essentially nonvolatile to those that rapidly evaporate Henrys Law constant is a useful predictor of volatilization from water Henrys Law constant is analogous to the octanol-water partition
Summary of Important Points and Concepts Vapor pressure and the mass transfer coefficient K are needed to determine the flux across an open container For enclosed areas, an equation based on mass balance can be used to determine the concentration of contaminant in the air Equations for determining the volatilization for soils are more complex because of variability in characteristics (e.g. sorption, water content, diffusion)
Summary of Important Points and Concepts Researchers at Dow developed an empirical equation for estimating the first order decay rate for surface soils Hamakers equation works reasonable well for a range of problems involving the volatilization of contaminants in deep aquifers