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Solid Waste & Hazardous Waste 
Hikmat Al Salim 
March 20123/9/2012 solid & Hazardous waste 1
Waste Classification 
• Municipal waste 
• Construction demolition debris 
• Nonhazardous industrial waste 
• Incineration ash 
• Hazardous waste
Regulations 
Solid waste is regulated under theResource 
Conservation and Recovery Act (RCRA). 
Classification of non-hazardous and hazardous 
waste depends on the chemical constituents of 
the leachate .
A waste is classified as a hazardous if it has a 
hazardous characteristic listed below. 
1. Hazardous Characteristics: 
• Ignitable Hazardous Waste (TRIC) 
– A liquid waste which has a flash point of less than or 
equal to 140 degrees F (60 degrees C) as determined 
by an approved test method. 
– A non-liquid waste which, under standard 
conditions, is capable of causing a fire through 
friction, absorption of moisture or a spontaneous 
chemical change and when ignited, the waste burns 
so vigorously and persistently that it creates a hazard. 
– An ignitable compressed gas or oxidizer. 
March 20123/9/2012 solid & Hazardous waste 4
2. Corrosive Hazardous Waste (TRIC) 
– An aqueous waste with a pH of less than or equal 
to 2 or greater than or equal to 12.5 is considered 
to be a corrosive hazardous waste. 
– A liquid waste that corrodes steel at a minimum 
rate of .25 inch per year as determined by an 
approved test method. 
March 20123/9/2012 solid & Hazardous waste 5
(TRIC) 
3. Reactive Hazardous Waste 
– A solid waste that is normally unstable, reacts 
violently with water, or generates toxic gases 
when exposed to water or other materials. 
4. Toxic Hazardous Waste 
– A waste that contains certain substances 
determined to be harmful at or in excess of the 
maximum concentration. Some of those 
substances include lead, arsenic, and mercury. 
March 20123/9/2012 solid & Hazardous waste 6
Nature of Waste Problem 
 Moisture within and flowing on the waste generates 
leachate 
 Leachate takes the characteristics of the waste 
 Thus leachate is very variable and is site-specific - 
there is no "typical" leachate 
 Flows gravitationally downward into the leachate 
collection system 
 Enters groundwater unless a suitable barrier layer or 
system is provided 
March 20123/9/2012 solid & Hazardous waste 7
Outlines 
• Waste management methods 
• Landfill design and regulations 
• Function and usage of geosynthetics in landfill 
systems 
• Durability of geosynthetics 
• Future trend of landfill management
Source Reduction 
Source reduction involves reduction in the 
quantity or toxicity of materials during the 
manufacturing process via: 
• Decrease the amount of unqualified products by 
improving quality control 
• Decrease the unit weight of the product by 
using high quality material.
Combustion 
• Combustion can reduce the volume of the solid waste 
up to 90% at the same generate power. 
• There are 140 combustion plants the US. 
• Emission must meet the EPA Clean Air Act. 
• Residual ash is hazardous material and should be 
disposed accordingly.
• Destruction of wastes by Combustion 
• The method is suitable for: 
– – Gases 
– – Liquids 
– – Slurries 
– – Sludge wastes 
– – Solids 
– – Containerized 
• Incineration destroys molecular structure, thus 
molecules with more stable structures and stronger 
chemical bonds require longer residence times 
and/or higher temperatures. 
March 20123/9/2012 solid & Hazardous waste 11
• Incinerator operating conditions must be monitored 
continuously. The following are some parameters 
affecting the efficiency of burning: 
 Combustion temperature 
 Residence time 
Degree of mixing 
 Presence of excess air 
• The type of incinerator required depends on the 
chemic and physical state of "waste" : 
March 20123/9/2012 solid & Hazardous waste 12
• Liquid injection 
– Any pumpable waste 
– Converts liquid waste to gas prior to combustion 
Kilns 
– Used on solids, liquids, and gases 
– Many different types (e.g., rotary kilns, cement kilns, lime 
kilns, 
aggregate kilns). 
Calcination or sintering 
• – 1800oC and atmospheric pressure. 
• – Destroys organics; reduces the volume of inorganics 
• Incinerator Performance must be monitored, thus: 
March 20123/9/2012 solid & Hazardous waste 13
• Destruction and Removal Efficiency (DRE) must be 
determined. This done by "monitoring" organization. 
The higher the figure of DRE , the more efficient is 
the incinerator. DRE of 99.99% for all “principal 
organic hazardous constituents” (POHCs) is 
required. 
• – Example: Wastes containing dioxins and furans 
requires 99.9999% DRE 
March 20123/9/2012 solid & Hazardous waste 14
• Incomplete combustion – afterburners must be installed 
for exhaust 
• – Combust the exhaust at higher temperature than the 
combustion of primary waste stream. Example: dioxin 
and furan creation, more toxic than precursors 
• 75 dioxin congeners; 135 furan congeners 
• Incinerators usually produce particulates; thus 
particulate controls are important. Particulates can be 
removed by using bag-houses, and water scrubbers 
• Control of acid formation is also important e.g. HCl from 
combustion of chlorinated organics. Acids corrode 
metals and form "acid precipitates", and acid rain. 
• . 
Congeners are toxic chemicals that are formed during 
incineration. A member of the same kind, class, or 
group 
March 20123/9/2012 solid & Hazardous waste 15
Municipal Solid Waste Disposal 
INCINIRATION 
March 20123/9/2012 solid & Hazardous waste 16
March 20123/9/2012 solid & Hazardous waste 17
Landfill 
– Landfill implies disposal of waste in the ground. 
– 70% of the waste is disposed in landfill and the 
percentage has been gradually decreasing. 
– The amount of waste actually increased due to 
population growth.
March 20123/9/2012 solid & Hazardous waste 19
March 20123/9/2012 solid & Hazardous waste 20
The Largest Landfill 
• Staten Island, NY 
• 3,000 acres 
• 2.4 billion cubic 
feet of waste 
• 25 times of the 
great pyramid
Nature of Waste Problem 
 Moisture within and flowing on the waste generates 
leachate 
 Leachate takes the characteristics of the waste 
 Thus leachate is very variable and is site-specific - there 
is no "typical" leachate 
 Flows gravitationally downward into the leachate 
collection system 
 Enters groundwater unless a suitable barrier layer or 
system is provided
Hazardous Waste Definition 
• Waste is listed in Appendix VIII of Title 40, Code 
of Federal Regulations, Part 251. 
• Waste is mixed with or derived from hazardous 
waste. 
• Waste is not identified as municipal waste. 
• Waste possesses one of the following 
characteristics: 
– ignitable; corrosive; reactive and toxic.
Minimum Technology Guidance (MTG) 
for a Subtitle D Landfill 
“Solid Waste” 
150 mm 
300 mm 
600 mm 
Filter (or GT) 
Drain (or GN/GC) 
Clay @ 1x10-7 cm/sec 
Soil Subgrade 
GT (opt.) 
GM* 
Composite 
liner
MTG for a Subtitle C Landfill 
300 mm Drain (or GN) 
S-GM* 
“Solid Waste” 
150 mm 
300 mm 
900 mm 
Filter (or GT) 
Drain (or GN/GC) 
Clay @ 1x10-7 cm/sec 
(to highest groundwater level) 
P-GM* 
3.0 m 
Composite 
liner
Landfill Covers 
(Non-hazardous landfill without 
Geosynthetic on the bottom liner system) 
Erosion Layer 
Infiltration Layer 
150 mm 
450 mm
Cover Layers 
• Erosion Layer 
– Earthen material is capable of sustaining native 
plant growth 
• Infiltration Layer 
– Permeability of this layer of soil should be less 
than or equal to the permeability of any bottom 
liner system or natural subsoils present, or 
permeability less than 1x10-5 cm/sec whichever 
is less
Landfill Cover System 
(Subtitle C & D, and Corp of Eng.) 
150 mm 
150 mm 
300 mm Drain (or GN) 
600 to 
900 mm 
Topsoil 
Filter (or GT) 
Clay @ 1x10-7 cm/sec 
”Solid Waste” 
Varies 
(frost depth) 
Cover Soil 
300 mm Gas Vent (or GT) 
GM
Landfill Site 
• Conforms with land use planning of the area 
• Easy access to vehicles during the operation of the 
landfill 
• Adequate quantity of earth cover material that is 
easily handled and compacted 
• Landfill operation will not detrimentally impact 
surrounding environment 
• Large enough to hold community waste for some time
Geosynthetics 
geomembranes (GM) 
geosynthetic clay liners (GCL) 
geonets (GN) 
geotextiles (GT) 
geogrids (GG) 
geopipe (GP) 
geocomposites (GC)
Primary Functions 
Type S R F D B 
GM - - - - Y 
GCL - - - - Y 
GN - - - Y - 
GT Y Y Y Y - 
GG - Y - - - 
GP - - - Y - 
GC Y Y Y Y Y 
S = separation, R = reinforcement, F = filtration 
D = drainage, B = barrier
Liner System 
GT 
GG 
GN 
GCL 
GM 
CCL 
Gravel w/ 
perforated pipe
Final Cover System
Solid Waste
Composite Barriers 
(Intimate Contact Issue) 
Leachate 
CCL 
Clay Liner 
(by itself) 
Leachate 
CCL 
Composite Liner 
(with intimate contact) 
Does the GT compromise the composite 
liner concept? 
Ans: Generally no... 
Leachate 
Composite Liner 
(GM + GCL) 
GCL
Composite Barriers 
(Theoretical Leakage) 
GM alone (hole area “a”) 
Composite liner (GM/CCL) 
Leachate 
ks 
= 2 
Q C a gh B 
Q = 0.21 a0.1 h0.9 ks 
0.74 
(for good contact) 
Q = 1.15 a0.1 h0.9 ks 
0.74 
(for poor contact) 
Ref. Bonaparte, Giroud & Gross, GS ‘89)
Average Values of Leakage Quantities 
Life Cycle Stage 
Leakage Rate (lphd) 
1 2 3 
40 
30 
20 
10 
0 
GM 
GM/CCL 
GM/GCL 
Sand 
Leak Detection
Average Values of Leakage Quantities 
(cont’d) 
GM/CCL 
Life Cycle Stage 
Leakage Rate (lphad) 
1 2 3 
20 
15 
10 
5 
0 
GM 
GM/GCL 
Geonet 
Leak Detection
Geomembranes 
Widely Used Geomembranes Limited Used Geomembranes 
High density polyethylene 
(HDPE) 
Chlorosulfonated 
polyethylene (CSPE) 
Linear low density 
polyethylene (LLDPE) 
Ethylene interpolymer alloy 
(EIA) 
Flexible polypropylene 
(f-PP) 
Ethylene propylene 
trimonomer (EPDM) 
Polyvinyl chloride-plasticized 
(PVC-p)
Compositions 
(approximate percentage) 
Type Resin Carbon 
Black 
Plasticizer Anti-oxidant 
Filler 
HDPE 95-97 2-3 0 1-0.5 0 
LLDPE 95-97 2-3 0 1-0.5 0 
PVC-p 50-70 1-2 25-35 1-0.5 5-10 
fPP 95-97 2-3 0 1-0.5 0 
CSPE 40-60 5-40 0 1-0.5 5-15 
EPDM 25-30 20-40 0 1-0.5 20-40
Material Properties 
• Mechanical property 
• Density 
• Melt flow 
• Carbon black 
• Plasticizers 
• Antioxidant
Tensile Behavior 
• Test method varies according to the resin type and 
style of the geomembrane. 
• Each test method consists of unique shape of 
specimen and strain rate. 
• Methods: 
– HDPE, LLDPE and fPP – ASTM D 638 Type IV 
– PVC-p – ASTM D 882 
– All reinforced geomembranes – ASTM D 751
Design Concept 
FS 
Allowable (Test) Property 
Required (Design) Property 
= 
Where: 
• Test methods are from ASTM, ISO, or others 
• Design models from the literatures 
• Factor-of-Safety is site specific
Function of Carbon Black 
• The primary function is as an ultraviolet light 
stabilizer to protect polymer being degraded. 
• Carbon black absorption coefficient increases 
with loading up to ~ 3%. 
• In elastomeric materials, carbon black also 
functions as an reinforcement, and loading can be 
as high as 30-40%.
Addition of Carbon Black 
• The masterbatch technique is utilize to dispersing 
carbon black in plastic. 
• A masterbatch is a resin containing a high 
concentration of carbon black. 
• The masterbatch is blended with polymer resin to 
achieve the desire percentage.
Carbon Black 
• Carbon black content is measured according 
to ASTM D1603. 
• Carbon black dispersion is evaluated 
according to ASTM D 5596.
Plasticizers 
• Plasticizers is used in PVC to lower the glass 
transition temperature (Tg). 
• An addition of 30% plasticizer in PVC can lower 
the Tg from 80oC to –20oC. 
• The plasticized PVC behaves rubbery at normal 
ambient temperature. 
• However, plasticizer can slowly leach out with 
time.
Antioxidants 
• The function of antioxidants is to protect polymers 
from being oxidized during the extrusion process 
and service lifetime. 
• For polyolefines, antioxidants is vital to the longevity 
of the product. 
• Antioxidant will be the focus of the second part of 
this class.
Degradation of 
HDPE Geomembranes 
Chemical Related: 
– Thermal-oxidation 
– Photo-oxidation
Linear PE Structure 
• Linear PE is a graft copolymer 
• Each co-monomer creates one branch 
• Co-monomer can be butene, hexene, or octene
Density of Geomembranes 
• Density decreases as the amount of 
co-monomer increases 
• Density range of PE (ASTM D883) 
–> 0.940 g/ml for HDPE 
– 0.926 - 0.940 g/ml for MDPE 
– 0.910 - 0.925 g/ml for LLDPE 
–<0.909 g/ml for VLDPE or ULDPE
II. Oxidation Degradation 
• Polyolefins, such as HDPE, PP and PB are susceptible 
to oxidation. 
• Oxidation takes place via free radical reactions. 
• Free radicals form at the tertiary carbon atoms (i.e., 
at branches). 
• Oxidation leads to chain scission that results in 
decrease of Mw and subsequently on mechanical 
properties.
Forming Free Radicals
Different Degradation Stages
Various Stages of Oxidation
Reactions during Induction Period 
RH R H  
R O  ROO 2 
ROORHROOH R
Reactions during 
Acceleration Period 
OH  RH  H O R 2 
ROOHROOH 
RORHROH R
Functions of Antioxidants 
• Primary antioxidants react with free radical 
species 
• Secondary antioxidants decompose ROOH to 
prevent formation of free radicals
Types of Antioxidants 
Category Chemical Type Example 
Primary Hindered phenol Irganox 1076 or 1010 
Santowhite crystals 
Hindered amines Various of Tinuvin, 
Chemassorb 944 
Secondary Phosphites Irgafos 168 
Sulfur compound Dilauryl thiodipropionate 
Distearyl thiodipropionate 
Hindered amines Various of Tinuvin, 
Chemassorb 944
Effective Temperature Range 
0 50 100 150 200 250 300 
Phosphites 
Hindered Phenols 
Thiosynergists 
Hindered Amines 
Temperature (oC)
Depletion of Antioxidants 
Two mechanisms: 
a. Chemical reactions – by reacting with free 
radicals and peroxides 
b. Physical loss – by extraction or volatilization
Arrhenius Model 
Rate of reaction = X * Y * Z 
Where: 
X = collision frequency (concentration or pressure) 
Y = energy factor 
Z = probability factor of colliding particles 
(temperature dependent)
Potential Energy 
Eact 
DH 
transition state 
products of 
reaction 
Separate 
Reactants 
Potential Energy 
Progress of Reaction
Distribution of Energy 
dN 
dE 
Energy 
Fraction is 
-E act 
RT 
exp( )
Arrhenius Equation 
E 
RT 
act 
R = 
X e Z r 
 
( )( )( ) 
R A e r 
E 
RT 
act 
= 
 
( )( ) 
(9) 
(10) 
E 
RT r 
act =  (11) 
ln R ln A
Arrhenius Plot 
A 
ln R 
E act 
R 
r 1 
high temperature 
(lab tests) 
low temperature 
(site temperature) 
Inverse Temperature (1/T)
Experimental Design 
• Incubation environment should simulate the field 
(i.e., landfill environment) 
– Limited Oxygen 
– Some degree of liquid extraction 
• Utilize elevated temperatures to accelerate the 
reactions. 
– 55, 65, 75, and 85oC
Incubation Device 
Piezometer 
Insulation 
Perforated steel loading plate 
Sand 
Sand 
Heat tape 
Geomembrane 
Load 
1 10
Tests Performed 
• Oxidative inductive time (OIT) for antioxidant 
content. 
• Melt index for qualitative molecular weight 
measurement. 
• Tensile test for mechanical property
OIT Tests 
• OIT is the time required for the polymer to be 
oxidized under a specific test condition. 
• OIT value indicates the total amount (not the 
type) of the antioxidant remaining in the 
polymer.
OIT Test for Evaluation of 
Antioxidant (AO) 
• OIT Tests: 
– ASTM D3895-Standard OIT (Std-OIT), or 
– ASTM D 5885-High Pressure OIT (HP-OIT) 
• HP-OIT test is used for AOs which are 
sensitive to high temperature testing
Thermal Curve of OIT Test
Test Results 
0 5 10 15 20 25 30 
150 
100 
50 
0 
Std-OIT 
HP-OIT 
Density 
Melt Index 
Yield Stress 
Yield Strain 
Break Stress 
Break Strain 
Incubation Time (month) 
Percent Retained 
Changes in Eight Properties with Incubation Time at 85°C
Analysis of OIT Data 
a. Determine OIT depletion rate at each 
temperature. 
b. Utilize Arrhenius Equation to extrapolate the 
depletion rate to a lower temperature. 
c. Predict the time to consume all antioxidant in 
the polymer.
a) - OIT Depletion Rate 
4.5 
4 
3.5 
3 
2.5 
2 
1.5 
1 
55°C 
65°C 
75°C 
85°C 
0 5 10 15 20 25 
ln OIT (min.) 
Incubation Time (month)
b) –Arrhenius Plot 
-1 
-2 
-3 
-4 
-5 
Standard OIT 
HP-OIT 
0.0027 0.0028 0.0029 0.0030 0.0031 
1/T (°K) 
ln (OIT Depletion Rate) 
y = 17.045 - 6798.2x R^2 = 0.953 
y = 16.856 - 6991.3x R^2 = 0.943
c) Lifetime of Antioxidant 
• Use the OIT depletion equation to find “t” 
ln(OIT) = ln(P) – (S) * (t) 
• The OIT value for unstabilized PE is 
0.5 min. 
• For this particular stabilization package 
t = 200 years
Lifetime of Geomembrane 
• Induction time and degradation period (Stages B & 
C) can be established by using unstabilized polymer 
in the experiment. 
• It was found by Gedde et al. (1994) that the duration 
of Stages B and C is significant shorter than that of 
Stage A. 
• Antioxidants are critical to the long-term 
performance of polyethylene and other polyolefines.
Future of Waste Containment 
• Current waste containment technique is defined 
as “dry dome” method by eliminating leachate 
from being generated after closure. 
• Waste will not degrade since moisture is a critical 
component of the biodegradation process.
Bioreactor Landfill 
“……a sanitary landfill operated for the purpose of 
transforming and stabilizing the readily and 
moderately decomposable organic waste 
constituents within five to ten years following 
closure by purposeful control to enhance 
microbiological processes. The bioreactor landfill 
significantly increases the extent of waste 
decomposition, conversion rates and process 
effectiveness over what would otherwise occur 
within the landfill.”
Why Operate a Landfill as a Bioreactor? 
• to increase potential for waste to energy conversion, 
• to store and/or treat leachate, 
• to recover air space, and 
• to ensure sustainability
Status 
• 1993 - less than 20 landfills recirculating leachate 
• 1997 - ~ 130 landfills recirculating leachate 
• My estimate - ~ 5% of landfills
Aerobic Bioreactor 
• Rapid stabilization of waste 
• Enhanced settlement 
• Evaporation of moisture 
• Degradation of organics which are recalcitrant 
under anaerobic conditions 
• Reduction of methane emissions
Research Issues - Aerobic Bioreactor 
• How much air is needed? 
• How can air be delivered? 
• What is the impact on the water balance? 
• How are landfill fires prevented? 
• What are the economic implications?

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Solid Waste & Hazardous Waste

  • 1. Solid Waste & Hazardous Waste Hikmat Al Salim March 20123/9/2012 solid & Hazardous waste 1
  • 2. Waste Classification • Municipal waste • Construction demolition debris • Nonhazardous industrial waste • Incineration ash • Hazardous waste
  • 3. Regulations Solid waste is regulated under theResource Conservation and Recovery Act (RCRA). Classification of non-hazardous and hazardous waste depends on the chemical constituents of the leachate .
  • 4. A waste is classified as a hazardous if it has a hazardous characteristic listed below. 1. Hazardous Characteristics: • Ignitable Hazardous Waste (TRIC) – A liquid waste which has a flash point of less than or equal to 140 degrees F (60 degrees C) as determined by an approved test method. – A non-liquid waste which, under standard conditions, is capable of causing a fire through friction, absorption of moisture or a spontaneous chemical change and when ignited, the waste burns so vigorously and persistently that it creates a hazard. – An ignitable compressed gas or oxidizer. March 20123/9/2012 solid & Hazardous waste 4
  • 5. 2. Corrosive Hazardous Waste (TRIC) – An aqueous waste with a pH of less than or equal to 2 or greater than or equal to 12.5 is considered to be a corrosive hazardous waste. – A liquid waste that corrodes steel at a minimum rate of .25 inch per year as determined by an approved test method. March 20123/9/2012 solid & Hazardous waste 5
  • 6. (TRIC) 3. Reactive Hazardous Waste – A solid waste that is normally unstable, reacts violently with water, or generates toxic gases when exposed to water or other materials. 4. Toxic Hazardous Waste – A waste that contains certain substances determined to be harmful at or in excess of the maximum concentration. Some of those substances include lead, arsenic, and mercury. March 20123/9/2012 solid & Hazardous waste 6
  • 7. Nature of Waste Problem  Moisture within and flowing on the waste generates leachate  Leachate takes the characteristics of the waste  Thus leachate is very variable and is site-specific - there is no "typical" leachate  Flows gravitationally downward into the leachate collection system  Enters groundwater unless a suitable barrier layer or system is provided March 20123/9/2012 solid & Hazardous waste 7
  • 8. Outlines • Waste management methods • Landfill design and regulations • Function and usage of geosynthetics in landfill systems • Durability of geosynthetics • Future trend of landfill management
  • 9. Source Reduction Source reduction involves reduction in the quantity or toxicity of materials during the manufacturing process via: • Decrease the amount of unqualified products by improving quality control • Decrease the unit weight of the product by using high quality material.
  • 10. Combustion • Combustion can reduce the volume of the solid waste up to 90% at the same generate power. • There are 140 combustion plants the US. • Emission must meet the EPA Clean Air Act. • Residual ash is hazardous material and should be disposed accordingly.
  • 11. • Destruction of wastes by Combustion • The method is suitable for: – – Gases – – Liquids – – Slurries – – Sludge wastes – – Solids – – Containerized • Incineration destroys molecular structure, thus molecules with more stable structures and stronger chemical bonds require longer residence times and/or higher temperatures. March 20123/9/2012 solid & Hazardous waste 11
  • 12. • Incinerator operating conditions must be monitored continuously. The following are some parameters affecting the efficiency of burning:  Combustion temperature  Residence time Degree of mixing  Presence of excess air • The type of incinerator required depends on the chemic and physical state of "waste" : March 20123/9/2012 solid & Hazardous waste 12
  • 13. • Liquid injection – Any pumpable waste – Converts liquid waste to gas prior to combustion Kilns – Used on solids, liquids, and gases – Many different types (e.g., rotary kilns, cement kilns, lime kilns, aggregate kilns). Calcination or sintering • – 1800oC and atmospheric pressure. • – Destroys organics; reduces the volume of inorganics • Incinerator Performance must be monitored, thus: March 20123/9/2012 solid & Hazardous waste 13
  • 14. • Destruction and Removal Efficiency (DRE) must be determined. This done by "monitoring" organization. The higher the figure of DRE , the more efficient is the incinerator. DRE of 99.99% for all “principal organic hazardous constituents” (POHCs) is required. • – Example: Wastes containing dioxins and furans requires 99.9999% DRE March 20123/9/2012 solid & Hazardous waste 14
  • 15. • Incomplete combustion – afterburners must be installed for exhaust • – Combust the exhaust at higher temperature than the combustion of primary waste stream. Example: dioxin and furan creation, more toxic than precursors • 75 dioxin congeners; 135 furan congeners • Incinerators usually produce particulates; thus particulate controls are important. Particulates can be removed by using bag-houses, and water scrubbers • Control of acid formation is also important e.g. HCl from combustion of chlorinated organics. Acids corrode metals and form "acid precipitates", and acid rain. • . Congeners are toxic chemicals that are formed during incineration. A member of the same kind, class, or group March 20123/9/2012 solid & Hazardous waste 15
  • 16. Municipal Solid Waste Disposal INCINIRATION March 20123/9/2012 solid & Hazardous waste 16
  • 17. March 20123/9/2012 solid & Hazardous waste 17
  • 18. Landfill – Landfill implies disposal of waste in the ground. – 70% of the waste is disposed in landfill and the percentage has been gradually decreasing. – The amount of waste actually increased due to population growth.
  • 19. March 20123/9/2012 solid & Hazardous waste 19
  • 20. March 20123/9/2012 solid & Hazardous waste 20
  • 21. The Largest Landfill • Staten Island, NY • 3,000 acres • 2.4 billion cubic feet of waste • 25 times of the great pyramid
  • 22. Nature of Waste Problem  Moisture within and flowing on the waste generates leachate  Leachate takes the characteristics of the waste  Thus leachate is very variable and is site-specific - there is no "typical" leachate  Flows gravitationally downward into the leachate collection system  Enters groundwater unless a suitable barrier layer or system is provided
  • 23. Hazardous Waste Definition • Waste is listed in Appendix VIII of Title 40, Code of Federal Regulations, Part 251. • Waste is mixed with or derived from hazardous waste. • Waste is not identified as municipal waste. • Waste possesses one of the following characteristics: – ignitable; corrosive; reactive and toxic.
  • 24. Minimum Technology Guidance (MTG) for a Subtitle D Landfill “Solid Waste” 150 mm 300 mm 600 mm Filter (or GT) Drain (or GN/GC) Clay @ 1x10-7 cm/sec Soil Subgrade GT (opt.) GM* Composite liner
  • 25. MTG for a Subtitle C Landfill 300 mm Drain (or GN) S-GM* “Solid Waste” 150 mm 300 mm 900 mm Filter (or GT) Drain (or GN/GC) Clay @ 1x10-7 cm/sec (to highest groundwater level) P-GM* 3.0 m Composite liner
  • 26. Landfill Covers (Non-hazardous landfill without Geosynthetic on the bottom liner system) Erosion Layer Infiltration Layer 150 mm 450 mm
  • 27. Cover Layers • Erosion Layer – Earthen material is capable of sustaining native plant growth • Infiltration Layer – Permeability of this layer of soil should be less than or equal to the permeability of any bottom liner system or natural subsoils present, or permeability less than 1x10-5 cm/sec whichever is less
  • 28. Landfill Cover System (Subtitle C & D, and Corp of Eng.) 150 mm 150 mm 300 mm Drain (or GN) 600 to 900 mm Topsoil Filter (or GT) Clay @ 1x10-7 cm/sec ”Solid Waste” Varies (frost depth) Cover Soil 300 mm Gas Vent (or GT) GM
  • 29. Landfill Site • Conforms with land use planning of the area • Easy access to vehicles during the operation of the landfill • Adequate quantity of earth cover material that is easily handled and compacted • Landfill operation will not detrimentally impact surrounding environment • Large enough to hold community waste for some time
  • 30. Geosynthetics geomembranes (GM) geosynthetic clay liners (GCL) geonets (GN) geotextiles (GT) geogrids (GG) geopipe (GP) geocomposites (GC)
  • 31. Primary Functions Type S R F D B GM - - - - Y GCL - - - - Y GN - - - Y - GT Y Y Y Y - GG - Y - - - GP - - - Y - GC Y Y Y Y Y S = separation, R = reinforcement, F = filtration D = drainage, B = barrier
  • 32. Liner System GT GG GN GCL GM CCL Gravel w/ perforated pipe
  • 35. Composite Barriers (Intimate Contact Issue) Leachate CCL Clay Liner (by itself) Leachate CCL Composite Liner (with intimate contact) Does the GT compromise the composite liner concept? Ans: Generally no... Leachate Composite Liner (GM + GCL) GCL
  • 36. Composite Barriers (Theoretical Leakage) GM alone (hole area “a”) Composite liner (GM/CCL) Leachate ks = 2 Q C a gh B Q = 0.21 a0.1 h0.9 ks 0.74 (for good contact) Q = 1.15 a0.1 h0.9 ks 0.74 (for poor contact) Ref. Bonaparte, Giroud & Gross, GS ‘89)
  • 37. Average Values of Leakage Quantities Life Cycle Stage Leakage Rate (lphd) 1 2 3 40 30 20 10 0 GM GM/CCL GM/GCL Sand Leak Detection
  • 38. Average Values of Leakage Quantities (cont’d) GM/CCL Life Cycle Stage Leakage Rate (lphad) 1 2 3 20 15 10 5 0 GM GM/GCL Geonet Leak Detection
  • 39. Geomembranes Widely Used Geomembranes Limited Used Geomembranes High density polyethylene (HDPE) Chlorosulfonated polyethylene (CSPE) Linear low density polyethylene (LLDPE) Ethylene interpolymer alloy (EIA) Flexible polypropylene (f-PP) Ethylene propylene trimonomer (EPDM) Polyvinyl chloride-plasticized (PVC-p)
  • 40. Compositions (approximate percentage) Type Resin Carbon Black Plasticizer Anti-oxidant Filler HDPE 95-97 2-3 0 1-0.5 0 LLDPE 95-97 2-3 0 1-0.5 0 PVC-p 50-70 1-2 25-35 1-0.5 5-10 fPP 95-97 2-3 0 1-0.5 0 CSPE 40-60 5-40 0 1-0.5 5-15 EPDM 25-30 20-40 0 1-0.5 20-40
  • 41. Material Properties • Mechanical property • Density • Melt flow • Carbon black • Plasticizers • Antioxidant
  • 42. Tensile Behavior • Test method varies according to the resin type and style of the geomembrane. • Each test method consists of unique shape of specimen and strain rate. • Methods: – HDPE, LLDPE and fPP – ASTM D 638 Type IV – PVC-p – ASTM D 882 – All reinforced geomembranes – ASTM D 751
  • 43. Design Concept FS Allowable (Test) Property Required (Design) Property = Where: • Test methods are from ASTM, ISO, or others • Design models from the literatures • Factor-of-Safety is site specific
  • 44. Function of Carbon Black • The primary function is as an ultraviolet light stabilizer to protect polymer being degraded. • Carbon black absorption coefficient increases with loading up to ~ 3%. • In elastomeric materials, carbon black also functions as an reinforcement, and loading can be as high as 30-40%.
  • 45. Addition of Carbon Black • The masterbatch technique is utilize to dispersing carbon black in plastic. • A masterbatch is a resin containing a high concentration of carbon black. • The masterbatch is blended with polymer resin to achieve the desire percentage.
  • 46. Carbon Black • Carbon black content is measured according to ASTM D1603. • Carbon black dispersion is evaluated according to ASTM D 5596.
  • 47. Plasticizers • Plasticizers is used in PVC to lower the glass transition temperature (Tg). • An addition of 30% plasticizer in PVC can lower the Tg from 80oC to –20oC. • The plasticized PVC behaves rubbery at normal ambient temperature. • However, plasticizer can slowly leach out with time.
  • 48. Antioxidants • The function of antioxidants is to protect polymers from being oxidized during the extrusion process and service lifetime. • For polyolefines, antioxidants is vital to the longevity of the product. • Antioxidant will be the focus of the second part of this class.
  • 49. Degradation of HDPE Geomembranes Chemical Related: – Thermal-oxidation – Photo-oxidation
  • 50. Linear PE Structure • Linear PE is a graft copolymer • Each co-monomer creates one branch • Co-monomer can be butene, hexene, or octene
  • 51. Density of Geomembranes • Density decreases as the amount of co-monomer increases • Density range of PE (ASTM D883) –> 0.940 g/ml for HDPE – 0.926 - 0.940 g/ml for MDPE – 0.910 - 0.925 g/ml for LLDPE –<0.909 g/ml for VLDPE or ULDPE
  • 52. II. Oxidation Degradation • Polyolefins, such as HDPE, PP and PB are susceptible to oxidation. • Oxidation takes place via free radical reactions. • Free radicals form at the tertiary carbon atoms (i.e., at branches). • Oxidation leads to chain scission that results in decrease of Mw and subsequently on mechanical properties.
  • 55. Various Stages of Oxidation
  • 56. Reactions during Induction Period RH R H  R O  ROO 2 ROORHROOH R
  • 57. Reactions during Acceleration Period OH  RH  H O R 2 ROOHROOH RORHROH R
  • 58. Functions of Antioxidants • Primary antioxidants react with free radical species • Secondary antioxidants decompose ROOH to prevent formation of free radicals
  • 59.
  • 60. Types of Antioxidants Category Chemical Type Example Primary Hindered phenol Irganox 1076 or 1010 Santowhite crystals Hindered amines Various of Tinuvin, Chemassorb 944 Secondary Phosphites Irgafos 168 Sulfur compound Dilauryl thiodipropionate Distearyl thiodipropionate Hindered amines Various of Tinuvin, Chemassorb 944
  • 61. Effective Temperature Range 0 50 100 150 200 250 300 Phosphites Hindered Phenols Thiosynergists Hindered Amines Temperature (oC)
  • 62. Depletion of Antioxidants Two mechanisms: a. Chemical reactions – by reacting with free radicals and peroxides b. Physical loss – by extraction or volatilization
  • 63. Arrhenius Model Rate of reaction = X * Y * Z Where: X = collision frequency (concentration or pressure) Y = energy factor Z = probability factor of colliding particles (temperature dependent)
  • 64. Potential Energy Eact DH transition state products of reaction Separate Reactants Potential Energy Progress of Reaction
  • 65. Distribution of Energy dN dE Energy Fraction is -E act RT exp( )
  • 66. Arrhenius Equation E RT act R = X e Z r  ( )( )( ) R A e r E RT act =  ( )( ) (9) (10) E RT r act =  (11) ln R ln A
  • 67. Arrhenius Plot A ln R E act R r 1 high temperature (lab tests) low temperature (site temperature) Inverse Temperature (1/T)
  • 68. Experimental Design • Incubation environment should simulate the field (i.e., landfill environment) – Limited Oxygen – Some degree of liquid extraction • Utilize elevated temperatures to accelerate the reactions. – 55, 65, 75, and 85oC
  • 69. Incubation Device Piezometer Insulation Perforated steel loading plate Sand Sand Heat tape Geomembrane Load 1 10
  • 70. Tests Performed • Oxidative inductive time (OIT) for antioxidant content. • Melt index for qualitative molecular weight measurement. • Tensile test for mechanical property
  • 71. OIT Tests • OIT is the time required for the polymer to be oxidized under a specific test condition. • OIT value indicates the total amount (not the type) of the antioxidant remaining in the polymer.
  • 72. OIT Test for Evaluation of Antioxidant (AO) • OIT Tests: – ASTM D3895-Standard OIT (Std-OIT), or – ASTM D 5885-High Pressure OIT (HP-OIT) • HP-OIT test is used for AOs which are sensitive to high temperature testing
  • 73.
  • 74. Thermal Curve of OIT Test
  • 75. Test Results 0 5 10 15 20 25 30 150 100 50 0 Std-OIT HP-OIT Density Melt Index Yield Stress Yield Strain Break Stress Break Strain Incubation Time (month) Percent Retained Changes in Eight Properties with Incubation Time at 85°C
  • 76. Analysis of OIT Data a. Determine OIT depletion rate at each temperature. b. Utilize Arrhenius Equation to extrapolate the depletion rate to a lower temperature. c. Predict the time to consume all antioxidant in the polymer.
  • 77. a) - OIT Depletion Rate 4.5 4 3.5 3 2.5 2 1.5 1 55°C 65°C 75°C 85°C 0 5 10 15 20 25 ln OIT (min.) Incubation Time (month)
  • 78. b) –Arrhenius Plot -1 -2 -3 -4 -5 Standard OIT HP-OIT 0.0027 0.0028 0.0029 0.0030 0.0031 1/T (°K) ln (OIT Depletion Rate) y = 17.045 - 6798.2x R^2 = 0.953 y = 16.856 - 6991.3x R^2 = 0.943
  • 79. c) Lifetime of Antioxidant • Use the OIT depletion equation to find “t” ln(OIT) = ln(P) – (S) * (t) • The OIT value for unstabilized PE is 0.5 min. • For this particular stabilization package t = 200 years
  • 80. Lifetime of Geomembrane • Induction time and degradation period (Stages B & C) can be established by using unstabilized polymer in the experiment. • It was found by Gedde et al. (1994) that the duration of Stages B and C is significant shorter than that of Stage A. • Antioxidants are critical to the long-term performance of polyethylene and other polyolefines.
  • 81. Future of Waste Containment • Current waste containment technique is defined as “dry dome” method by eliminating leachate from being generated after closure. • Waste will not degrade since moisture is a critical component of the biodegradation process.
  • 82. Bioreactor Landfill “……a sanitary landfill operated for the purpose of transforming and stabilizing the readily and moderately decomposable organic waste constituents within five to ten years following closure by purposeful control to enhance microbiological processes. The bioreactor landfill significantly increases the extent of waste decomposition, conversion rates and process effectiveness over what would otherwise occur within the landfill.”
  • 83. Why Operate a Landfill as a Bioreactor? • to increase potential for waste to energy conversion, • to store and/or treat leachate, • to recover air space, and • to ensure sustainability
  • 84. Status • 1993 - less than 20 landfills recirculating leachate • 1997 - ~ 130 landfills recirculating leachate • My estimate - ~ 5% of landfills
  • 85. Aerobic Bioreactor • Rapid stabilization of waste • Enhanced settlement • Evaporation of moisture • Degradation of organics which are recalcitrant under anaerobic conditions • Reduction of methane emissions
  • 86. Research Issues - Aerobic Bioreactor • How much air is needed? • How can air be delivered? • What is the impact on the water balance? • How are landfill fires prevented? • What are the economic implications?