mass balance computational procedure
-
Upload
adrian-ruiz -
Category
Environment
-
view
142 -
download
5
Transcript of mass balance computational procedure
Mass Balance Computational
Procedure in Landfill Assessment
1
Jae K. (Jim) Park, Professor
Dept. of Civil and Environmental Engineering
University of Wisconsin-Madison
Mass Balance in Landfills
Estimate the remaining site life for disposal of refuse
Step 1. Develop a general indication of the solid waste specific weight
Step 2. Estimate the volume of soil required to cover each day’s waste from the appropriate solid waste-to-cover ratio (e.g., 4 to 1)
Step 3. Estimate the tonnage of refuse that may still be landfilled, given site volume remaining.
=
2
+ + +Refuseplaced
Mass leavingin leachate
Mass leavingin gas
Waste remaining
Mass transformed to other products
Quantities of Gas Produced
Methanogenic decomposition
CaHbOcNd + 1/4(4a-b-2c+3d) H2O 1/8(4a+b-2c-3d)CH4
+1/8(4a-b+2c+3d)CO2 + dNH3
Estimate an upper bound on the gas production relative to the quantity of substrate utilized.
Because acid-phase anaerobic and aerobic decomposition gives rise to CO2 and not to CH4, there is a higher CO2
content in the gas generated than predicted from eq. above.
a = 60, b = 94.3, c = 32.8, d = 1, noncombustibles = 53.4, and H2O = 44.4 53% CH4 520 L/kg
Theoretical: 300 to 500 L of landfill gas produced from 1 kg of municipal refuse (5 to 8 ft3/lb)
Full-size landfill projected: 50 ~ 400 L/kg (0.8 ~ 6.4 ft3/lb)
Optimum moisture content: 75 ~ 100% of the refuse dry wt.3
Theoretical CH4 & CO2 Production (1)
In 100 lb of solid waste, 56 lb decomposable
C60H94.3O37.8N+18.28H2O → 31.96CH4+28.04CO2+NH3
1433.1 g 329.0 g 511.4 g 1233.5 g 17 g
Specific wt: CH4 – 0.0448 lb/ft3; CO2 – 0.1235 lb/ft3
Solution
CH4 = 511.4/1433.1ⅹ56 lb = 20 lb
CO2 = 1233.5/1443.1ⅹ56 lb = 48.2 lb
Volume
CH4 = 20 lb0.0448 lb/ft3 = 446.4 ft3
CO2 = 48.2 lb0.1235 lb/ft3 = 390.3 ft3
4
Theoretical CH4 & CO2 Production (2)
Fraction of CH4 and CO2
CH4(%) = 446.4(446.4+390.3)ⅹ100=53.3%
CO2(%) = 390.3(446.4+390.3)ⅹ100=46.5%
Gas production based on dry wt. of org. material
(446.4+390.3) ft356 lb=14.9 ft3/lb=0.93 m3/kg
Gas production based on total wt. of org. material
(446.4+390.3) ft3100 lb=8.4 ft3/lb=0.52 m3/kg
5
Empirical Formula of Solid Waste
Element Wt, gAtomic wt.,
g/molMole
Mole ratio (N=1)
C
H
O
N
S
Ash
27.39
3.62
22.97
0.54
0.10
3.48
12.01
1.01
16.00
14.01
32.07
-
2.28
3.584
1.436
0.038
0.003
-
60
94.3
37.8
1.0
0.1
-
C60H94.3O37.8N → C60H94O38N
6
Factors Affecting Gas Production
Refuse composition, age of refuse, moisture content, pH, microbial population present, temperature, and quantity and quality of nutrients
Rate of methane generation
Cumulative gas produced
C = Co (1 - e-kt)
Assume that the factor limiting the rate of methane generation at a landfill is the quantity of material remaining in the landfill.
tk
1 2
0 69/
.C C eo
kt dC
dtkC
7
Estimation of CH4 Production
The Scholl Canyon model may be used to estimate emissions using the following first-order decay equation (IPCC, 1997):
Gi = Mi× k × L0× exp-(k × ti)
where:
Gi = emission rate from the ith section (kg CH4/year);
Mi = mass of refuse in the ith section (ton);
k = CH4 generation rate (1/year);
L0 = CH4 generation potential (kg CH4/ton of refuse);
ti = age of the ith section (years).
IPCC (1997), Revised 1996 IPCC Guidelines for National Greenhouse Gas Inventories,
Vols. 1 and 3, Intergovernmental Panel on Climate Change, Bracknell, U.K. 8
CH4 Generation Potential
L0 = (Mc× Fb× S)/2
where:
Mc = kg of carbon per kg of waste landfilled;
Fb = biodegradable fraction; and
S = stoichiometric factor = 16/12.
L0: 4.4 to 194 kg CH4/ton of waste (Pelt et al., 1998)
EPA: L0 = 165 kg CH4/ton of waste
9
Organic portion of municipal wastes
Readily decomposable: food wastes (t1/2 = 0.5~1.5 yrs)
Moderately decomposable: paper (t1/2 = 5 ~ 25 yrs), wood grass, brush, greens, leaves, oils, and paint
Non-decomposable: plastics, leather, rubber, and rags
Landfill methane generation
Lag phase
Active methane generation phase
Life of methane gas generation for economic recovery: 5 to 20 years
Gas Production Rate
10
Decomposition Time in Landfill
11
Waste product Decomposition time
Banana skin 3~4 wksPaper bag 1 monthCardboard 2 monthsWool sock 1 yrOrange peel Up to 2 yrsCigarette butts Up to 12 yrsPlastic bags* Up to 20 yrsPolyfilm wrapping (clingwrap)* 25 yrsLeather shoe Up to 45 yrsTin cans 50 yrsPlastic bottle* 450 yrsPlastic 6-pack holder* 500 yrsDisposable nappies 550 yrsPolystyrene cups > 500 yrsAluminum cans > 1 million yrs or forever?Glass 1~2 million yrs
* Even though these products break down in the times indicated they are still petrochemical products and will always remain in the environment.
Example - Solution
Example: Calculate CO2, CH4, and water consumed in the formation of landfill gas per kg of MSW. MSW empirical formula: C68H111O50N
C68H111O50N + 16H2O 33CO2 + 35CH4 + NH3
(1741) (288) (1452) (560) (17)
Water consumed = 288/1741 = 0.165 kg H2O/kg MSW
= 0.165 kg H2O/0.435 m3 gas/kg MSW
= 0.38 kg H2O/m3 gas
CO2 and CH4: 95 to 99% of landfill gas
12
Typical Landfill Gas Composition
Typical conc.
Component Source (% by vol.) Concern
Methane Biodegradation 50~70 Explosive
Carbon dioxide Biodegradation 30~50 Acidic in GW
Hydrogen Biodegradation < 5 Explosive
Mercaptans (CHS) Biodegradation 0.1~1 Odor
Hydrogen sulfide Biodegradation < 2 Odor
Toluene Contaminant 0.1~1 Hazardous
Benzene Contaminant 0.1~1 Hazardous
Disulfates Contaminant 0.1~2 Hazardous
Others Biodegradation Traces Hazardous
or contamination
13
Leachate Production Rates
Water quantity
Water present in the waste (small)
Water produced during decomposition (negligible)
Water added to the landfill - percolation through the landfill surface, horizontal flow through the sides, and upward flow through the bottom (major)
Hydrologic water balance Formation of surface water runoff, evaporation directly
to the atmosphere, transpiration to the atmosphere through vegetation surfaces, or infiltration into the cover soils and refuse at the surface of the landfill Infiltrates may be held in surficial soil and percolate through the refuse (leachate).
14
Leachate Quality
Cellulose is a major carbohydrate in domestic refuse.
15
CelluloseGlucose &
cellobiose
CO2, H2, ethanol, &
acetic, propionic,
butyric, valeric and
caproic acids
CH4 & CO2
pH increase
to 7~8
Cellulose:hemicellulose:lignin = 70:15:15
Major Compositions of Papers Landfilled
Cellulose: A long chain of glucose molecules, linked to one another primarily with glycosidic bonds. Only a small number of enzymes are required to degrade this material.
Hemicelluloses: Branched polymers of xylose, arabinose, galactose, mannose, and glucose. Hemicelluloses enhance the stability of the cell wall. They also cross-link with lignin, creating a complex web of bonds which provide structural strength, but also challenge microbial degradation.
Lignin: A complex polymer of phenylpropane units, which are cross-linked to each other with a variety of different chemical bonds. This complexity has thus far proven as resistant to detailed biochemical characterization as it is to microbial degradation. Lignin degradation is primarily an aerobic process, and in an anaerobic environment lignin can persist for very long periods.
16
Biological Decomposition in Landfill
17
Aerobic decomposition
High CO2, temp. , pH , high COD, BOD, and
specific conductance, high concentrations of most
inorganic constituents
Anaerobic acid phase
Highest COD, BOD, and specific conductance
Methanogenic phase
pH ~7, COD, BOD, and specific conductance
LandGEM
EPA Landfill Methane Outreach Program, Program Development Handbook: http://www.epa.gov/lmop/publications-tools/handbook.html
LandGEM program: http://www.epa.gov/ttn/catc/dir1/landgem-v302.xls
Useful reference: http://www.stormh2o.com/MSW/Editorial/LandGEM_the_EPAs_Landfill_Gas_Emissions_Model_15957.aspx
18