Selection of HCRW Treatment Technologies for Gauteng - PowerPoint PPT Presentation

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Selection of HCRW Treatment Technologies for Gauteng

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Title: Selection of HCRW Treatment Technologies for Gauteng


1
Selection of HCRW Treatment Technologies for
Gauteng
  • David A Baldwin, PhD, Pr.Sci.Nat.
  • Environmental and Chemical Consultants cc
  • and
  • Torben Kristiansen
  • Chief Technical Advisor. Gauteng Department of
    Agriculture, Conservation, Environment and Land
    Affairs
  • Rambøll, Hanneman and Hojland
  • August 2003

2
Introduction
  • Status Quo Study into HCRW in Gauteng 2000
  • Confirmed parlous state of HCRW management in
    Gauteng
  • Treatment facilities included 70 incinerators at
    58 different locations
  • Only 58 were operational but only 25 had a
    permit
  • Many incinerators were poorly operated and
    maintained
  • Only one fitted with emission control equipment,
    which was not operational
  • Capital and operating costs were estimated at
    only R1.00 per kilogram of waste treated

3
Introduction to Technologies -1
  • Thermal treatment/combustion technologies
  • Incineration which includes
  • excess air,
  • controlled air,
  • rotary kiln and
  • fluidised bed
  • Plasma Arc and
  • Pyrolysis

4
Introduction to Technologies -2
  • Sterilisation/Disinfection Technologies,
  • Steam sterilisation, e.g. Autoclaving
  • Chemical sterilisation, e.g. with chlorine,
    glutaraldehyde
  • Gas sterilisation, e.g. with ethylene oxide,
    formaldehyde
  • Dry heat sterilisation, e.g. oil heated screw
    feed technology
  • Electro-thermal deactivation (ETD),
  • Microwave sterilisation,
  • Irradiation sterilisation
  • Cobalt-60 gamma rays
  • Ultra violet
  • Electron beam sterilisation

5
Waste Pathway for Incineration
Infectious waste Sharps
Ash
Landfill
Leachate
Flue gas cleaning residues
Pathological Waste
Incineration
Chemical Waste
Emissions to Air
6
Waste Pathway for Non-Burn Technologies
Leachate Gas Emissions
Non-infectious waste
Infectious waste Sharps
Non-Burn Treatment
Landfill
Incineration Cremation or Burial
Ash or Body Parts
Pathological Waste
Cemetery
Treatment as Hazardous Waste
Waste Treatment Residues to Landfill
Chemical Waste
7
Flow Diagram of Modern Incineration Plant
8
Advantages of Incineration
  • Safe elimination of all infectious organisms in
    the waste at temperatures above 700oC
  • Flexible, as it can accept pathological waste and
    depending on the technology chemical waste.
  • Residues are not recognisable
  • Reduction of the waste by up to 95 by volume or
    83 to 95 by mass typically 5-17 ash is
    obtained.
  • Very well proven technology
  • No pre-shredding required
  • No special requirements for packaging of waste
  • Full disinfection is assumed to have occurred
    provided the high temperatures are maintained and
    the ash quantity is adequate. No monitoring of
    sterilisation efficiency is required.

9
Disadvantages of Incineration
  • Normally higher investment costs required for
    incinerator and flue gas cleaning compared to
    non-burn technologies
  • Point source immediate emissions to the air (as
    opposed to attenuated emission of CH4 and CO2
    from landfill body over a period of decades)
  • High cost of monitoring gas emissions and
    demonstrating compliance to emission standards.
  • Solid and liquid by-products must be handled as
    potentially hazardous waste (may not apply to
    bottom ash if waste is well sorted and FGC
    residues handled separately)
  • Incineration is perceived negatively by many
    sections of the community.
  • PVC and heavy metals in the waste provide a
    significant pollutant load on the gas cleaning
    system and for heavy metals on the quality of
    bottom ash
  • Existing health care risk waste incinerators in
    South Africa cannot accept significant amounts of
    chemical waste because of refractory damage.

10
Flow Diagram a Typical Microwave Plant
11
Advantages Non-Burn Technologies -1
  • Autoclaving, Microwaving ETD and DHS (Cross
    cutting)
  • High sterilisation efficiency under appropriate
    conditions
  • Low temperature of operation 90oC to 160oC
  • Volume reduction depending on type of
    shredding/compaction equipment that has been
    installed
  • Low risk of air pollution
  • Moderate operation costs
  • Easier to locate as generally more acceptable to
    communities and neighbours than incineration
  • Recovery technologies can be used on sterilised
    waste

12
Advantages Non-Burn Technologies -2
  • Autoclaving
  • Proven system that is familiar to health-care
    providers
  • Relatively High Sterilisation Temperature
  • Microwaving
  • Low capacity units are available for small waste
    producers e.g. clinics and GPs
  • Moderate investment costs
  • Low Sterilisation Temperature may lower energy
    costs
  • Electro-thermal Deactivation
  • Low Sterilisation Temperature may lower energy
    costs

13
Disadvantages Non-Burn Technologies -1
  • Autoclaving, Microwaving ETD and DHS (Cross
    cutting)
  • Not suitable for pathological waste and chemical
    waste
  • Good waste segregation required
  • No or limited mass reduction
  • Shredders are subject to breakdowns and blocking
    and repairs are difficult when the waste is
    infectious.
  • It is not possible to visually determine that
    waste has been sterilised
  • Waste is not rendered unrecognisable or unusable,
    if not shredded
  • High monitoring costs to demonstrate compliance
    with sterilisation standards
  • Treated waste must be disposed to landfill
  • Air filtration is needed some odour problems
  • Operation requires highly qualified technicians.
  • HEPA filters must be maintained and replaced
    regularly

14
Disadvantages Non-Burn Technologies -2
  • Autoclaving
  • Significant amounts of volatile organic carbon
    compounds produced
  • Contaminated water must be discharged to sewer
  • Waste and containers must have good steam
    permeability, especially if there is no prior
    shredding
  • No waste reduction
  • Microwaving
  • Unsuitable for very high quantities of infected
    metal (e.g. needles from inoculation campaigns)
  • Low sterilisation temperature increases time
    required for treatment.
  • Electro-thermal Deactivation
  • Relatively high investment and operating costs
  • Low sterilisation temperature increases time
    required for treatment.

15
Cost Comparison of Selected HCRW Treatment
Technologies - 1
  • Assumptions
  • Salary costs include all normal contributions
  • The cost for the establishment of a building in
    the estimated costs.
  • A standard fixed amount for consultancy fees and
    other expenditure required to obtain an EIA
    authorisation, etc
  • The cost of equipment was based on
    International/South African price levels for
    delivery in Gauteng.
  • Incinerators include gas-cleaning equipment, i.e.
    lime treatment plus a ceramic filter.
  • The cost of civil works and installation were
    based on Gauteng prices

16
Cost Comparison of Selected HCRW Treatment
Technologies - 2
  • Economic life of civil works and treatment
    technologies 12 years
  • Economic life of storage and transportation
    equipment 10 years
  • The following costs not included
  • Infrastructure at the generators site,
  • Establishment of public utilities used, e.g.
    landfills
  • Cost of administration, invoicing, marketing etc.
  • Cost of training of operators
  • Cost of PPE/OSH programmes.
  • Value Added Tax.
  • Depreciation costs are estimated as 10 years for
    equipment and 15 years for other capital and a
    real interest rate of 12 p.a.

17
Cost Comparison of Selected HCRW Treatment
Technologies - 3
  • The operational hours for the plants were based
    on operation for 26 days per month and 12 months
    per year. However, the maximum operational hours
    were varied as follows
  • Incinerators lt 200kg/hr 12 hrs per day - manual
    de-ashing
  • Incinerators ? 200kg/hr 20 hours per day -
    automatic de-ashing
  • Non-burn Technologies 24 hours per day
  • The costs for disposal of residues, such as the
    ash and gas cleaning waste from incinerators, and
    sterilised the waste from non-burn technologies,
    were estimated using current disposal costs.
    Residues from non-burn are assumed deposited at
    normal landfill sites, whereas residues from
    incinerators are assumed deposited at a Hazardous
    Waste Landfill site.
  • For non-burn technologies an estimate of the
    costs of disposal of pathological waste and
    chemical waste that could not be treated by the
    technology was included

18
Costs for HCRW Treatment Technologies
Technology Capacity, kg/hr Investment Cost, R m Running Cost, R m R/kg
Microwaving 100 5.83 2.33 3.27
  5.83 7.40 3.10 1.95
  2.33 10.61 5.09 1.08
Autoclaving 3.27 4.84 1.82 3.03
  250 6.34 2.55 1.34
  7.40 9.90 5.14 1.71
Incineration 3.10 3.96 1.66 5.55
  1.95 5.16 2.49 2.00
  1000 7.42 4.53 0.97
Running Costs Interest Depreciation on Capital Operating (monitoring excluded) Running Costs Interest Depreciation on Capital Operating (monitoring excluded) Running Costs Interest Depreciation on Capital Operating (monitoring excluded) Running Costs Interest Depreciation on Capital Operating (monitoring excluded) Running Costs Interest Depreciation on Capital Operating (monitoring excluded)
19
Cost of HCRW Technologies
  • Treatment cost decreases dramatically as plant
    capacity increases
  • For incineration, there is a discontinuity that
    occurs below 200kg/hr due to the assumptions made
  • The costs are based on operating the facility at
    its maximum capacity.
  • According to the available data, microwaving is
    relatively expensive but the costs become
    comparable at higher loads.
  • The investment costs for incineration appear to
    be relatively low compared to the other two
    technologies.

20
Testing and Monitoring Incineration Plants - 1
  • Requirements
  • Performance Testing to conform to ROD
  • Standard Testing at least over first year of
    operation
  • Minimum Programme once prove conformance
  • Analysis Required
  • Continuous Monitoring of PM, carbon monoxide,
    oxygen, water vapour, hydrochloric acid and
    sulphur dioxide
  • Dioxins Performance x 1 Standard 2/yr
    Minimum 1/yr
  • Metals Performance x 1 Standard 2/yr Minimum
    1/yr
  • Loss on Ignition for Ash Performance x 1
    Standard and Minimum 12/yr

21
Testing and Monitoring Incineration Plants - 2
Performance Analysis Standard Analysis Minimum Analysis
Performance Analysis Standard Analysis Minimum Analysis
Capital Cost R868,000 R868,000 R868,000
Depreciation R1,041,000 R1,041,000 R1,041,000
Running Cost R90,000 R370,000 R283,00
22
Testing and Monitoring Incineration Plants - 3
Waste Throughput, kg/hr Standard Programme Standard Programme Minimum Programme Minimum Programme
Waste Throughput, kg/hr Treatment Cost R/kg Monitoring Cost as Treatment Cost R/kg Monitoring Cost as
100 7.09 22 6.49 14
250 2.37 16 2.22 9.0
500 1.43 8.2 1.36 6.2
1000 1.00 7.0 0.96 4.0
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