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    Newcastle University (SG) Chemical Engineering

    Assignment Submission & Feedback Sheet

    Student name:Wong Jie WeiShawn GallatinSamuel Lee Mao HuaJean Zhou Li Ting

    Ng Xiao YuanJasmine Tan Lian Fang

    Student No:110526001110525026110525004110526539110524856110522298

    Year:2012 Submittedto:Ms SharonJoyce

    Marked by:

    Module Code:

    CME3113

    Module Title:Sustainable Industries

    Assignment title:Waste Management Strategy for Singapore(Potential Investors)

    Date

    submitted :28 Nov 12

    Date

    returned:

    Blackboard Paper ID:

    I certify that all material in this course which is not our own work has been

    identified.

    Student Signature:

    Student self-evaluation:

    (1) A strong point of our assignment:- Managed to cite actual case studies and related to Singapores context inmonetary terms

    (2) An area which we believe may need improvement:- Analysis in terms of financial sustainability may not be sufficiently critical

    (3) We would particularly like your feedback/help with:List up to two specific areas:

    - Whether the analysis were sufficiently critical and if the report was conciseenough

    Markers comments:

    Overall mark:70100 1

    stClass

    6069 2 - 15059 2 - 24049 3rd0 - 39 Fail

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    CME 3113

    Sustainable Industry

    Potential Investor

    (Cohort 1)

    Team Members:

    Wong Jie Wei (110526001)

    Shawn Gallatin (110525026)

    Samuel Lee Mao Hua (110525004)

    Sim Jiaxuan (110525680)

    Jean Zhou Liting (110526539)

    Ng Xiao Yuan (110524856)

    Jasmine Tan Lian Fang (110522298)

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    Executive Summary

    Five waste management strategies (Incineration, Pyrolysis & Gasification, Improved

    Recycling, Anaerobic Digestion and Composting) were analysed based on the

    investors point of view. Capital and operating costs of the mentioned waste

    management, including its profitability for a period of 10 years were concluded using

    cumulative cash flow diagrams. The results showed that both incineration and

    Thermoselect took 7 years to break even. However, incineration had a higher

    cumulative cash flow of SGD 1069.989M vis--vis Thermoselect which had a

    cumulative cash flow of SGD 692.37M at the end of 10 years. Therefore, incineration

    was chosen as it was the most economically sustainable waste management strategy

    which offered the highest returns on investment in the same period.

    (1884 words inclusive of executive summaryexcluding tabulated texts and appendices)

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    List of Illustrations

    Figure 1 Cash Flow Diagram for Thermoselect ............................................................ 4

    Figure 2 Sensitivity Analysis of Syngas Production (Khoo H.H. et. al., 2006) ............ 4

    Figure 3 Cash Flow Diagram for Anaerobic Digestion ................................................. 5

    Figure 4 Trend of Fertilizer Use in Singapore (TradingEconomics.com, 2012) ........... 6

    Figure 5 Cash Flow Diagram for Composting ............................................................... 7

    Figure 6 Cash Flow Diagram for Improved Recycling ................................................. 9

    Figure 7 Relationship between commodity prices and profit (Fabian B & Mathias S.,

    2012) ............................................................................................................................ 10

    Figure 8 Cash Flow Diagram for Incineration ............................................................. 11

    Figure 9 Factors Affecting Treatment Cost and Subsequently Revenue (Decision

    Makers Guide To Municiple Solid Watse, 1999) ........................................................ 12

    Figure 10 Prices of Ferrous Metals (Letsrecycle: Metal, 2012) .................................. 13

    List of Tables

    Table 1 Comparison between Incineration and Thermoselect (Khoo H.H et. al., 2006)

    ........................................................................................................................................ 3

    Table 2 Estimated Costs of Anaerobic Digestion Facilities to Process Mixed Waste

    (Cant, 2006) ................................................................................................................... 5

    Table 3 Summary of Finances (Steve R.S et al, 2002) .................................................. 6

    Table 4 Summary of finances obtained (SembcorpBusiness at a glance) ................. 8

    Table 5 Summary of Finances of TSIP ........................................................................ 10

    Table 6 Prices of Ferrous Metal Recyclates in Year 2011 (Letsrecycle: Metal, 2012)

    ...................................................................................................................................... 12

    Table 7 Summary of the Economic Analysis of All Technologies ............................. 14

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    Table of Contents

    1. Introduction .......................................................................................................... 1

    2. Methodology .......................................................................................................... 2

    3. Market Survey ...................................................................................................... 3

    3.1 Thermoselect ....................................................................................................... 3

    3.1.1 Investment Analysis ...................................................................................... 3

    3.1.2 Sensitivity Analysis ....................................................................................... 4

    3.2 Anaerobic Digestion ........................................................................................... 5

    3.2.1 Investment Analysis ...................................................................................... 5

    3.2.2 Sensitivity Analysis ....................................................................................... 6

    3.3 Composting ......................................................................................................... 6

    3.3.1 Investment Analysis ...................................................................................... 6

    3.3.2 Sensitivity Analysis ....................................................................................... 8

    3.4 Improved Recycling ............................................................................................ 8

    3.4.1 Investment Analysis ...................................................................................... 8

    3.4.2 Sensitivity Analysis ..................................................................................... 10

    3.5 Incineration & Landfill ..................................................................................... 10

    3.5.1 Investment Analysis .................................................................................... 10

    3.5.2 Sensitivity Analysis ..................................................................................... 12

    4. Conclusion ........................................................................................................... 14

    5. References ............................................................................................................ 15

    6. Appendices .......................................................................................................... 18

    6.1 Appendix A ....................................................................................................... 18

    6.2 Appendix B ....................................................................................................... 20

    6.3 Appendix C ....................................................................................................... 22

    6.4 Appendix D ....................................................................................................... 24

    6.5 Appendix E ....................................................................................................... 26

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    1. Introduction

    With a population density of approximately 5.3 million ("Statistics," 2012) and

    limited land area, it is imperative that Singapore has an efficient system for the

    collection and disposal of solid waste. Over the years, the output of solid waste in

    Singapore has increased from 4.6 million tons in 2000 to 6.8 million tons in 2011.

    (Tay, 2012) Statistical data showed that 59% of the total waste generated 2011 was

    being recycled. Out of the 41% that was disposed of, 38% goes to the Waste-to-

    Energy (WTE) plants where the waste will be incinerated and the energy recovered.

    The remaining 3% along with the unwanted residue from the incineration would be

    sent to the Semakau Landfill for landfilling. (Tay, 2012)

    At present, the frequency of Singapore building a new incineration plant is one every

    5-7 years. (McCrea et al.)With that, the cost involved in dealing with the wastes in

    Singapore will be constantly increasing as the rate of waste generation increases with

    respect to the growing population. Hence, it is important that a new waste

    management strategy is developed in order to accommodate the growing volume of

    waste. This new strategy should not only be a long term solution to Singapores

    growing waste problems, it should also offer attractive returns; one that is worth

    investing in.

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    2. Methodology

    i. The existing waste management strategies in Singapore were analyzed.ii. Research was done on other forms of waste treatment. Research areas were,

    - Incineration- Pyrolysis & Gasification- Improved Recycling- Anaerobic Digestion- Composting

    iii. Factors such as the capital and operating costs of the plant as well as themarket value of any saleable products were gathered for the respectiveresearch areas.

    iv. With the data, an estimation of the profitability and feasibility of each wastetreatment process was analysed.

    v. The profitability of each waste treatment process was projected for 10 yearsthrough the use of a cumulative cash flow diagram.

    vi. At the same time, wastes generation and recycling patterns were studied todetermine whether it would be worthwhile to be investing in the waste

    management business.

    vii. From the cash flow diagrams, a comparison was done to decide which wastemanagement process would give the best return on investments.

    viii. Finally, a simple risk analysis (sensitivity) of the investment was conducted toinvestigate the effects of various external undesirable factors on the revenue or

    operating conditions/costs.

    In each of the technologies discussed, a brief description of the technology and some

    detailed financial data (if available) are attached in Appendices A-E while the general

    finance related materials are discussed in the report.

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    3. Market Survey

    3.1 Thermoselect

    3.1.1 Investment Analysis

    Presently, the main waste treatment is by incineration. Comparatively, countries such

    as Japan and Germany have ventured into Thermoselect, a plant which features

    cleaner emissions, higher efficiencies and greater investment returns.

    A study by the Institute of Chemical and Engineering Sciences was conducted to

    ascertain the economical viabilities of Thermoselect in Singapore. It was based on a

    plant in Europe which had the same capacity of the Waste to Energy Incinerator in

    Tuas South.

    Table 1 summarizes the cost and operating conditions related to that of the Tuas

    Incinerator and the proposed Thermoselect plant.

    Table 1 Comparison between Incineration and Thermoselect (Khoo H .H et. al., 2006)

    Cost and Operating ConditionsWaste Treatment Technology

    Incinerator Thermoselect

    Capacity (tpd) 3000 3000

    Type of materials processed Mixed MSW Mixed MSW

    Main useful product Electricity(550KWh/ton)

    Syngas (890kg/ton)

    Capital and construction costs in

    millions SGD900 725

    Operating costs in SGD/ton 70 100

    Tipping fee in SGD/ton

    (Source: Cooper J, 2010)80 80

    Disposal cost to landfill in SGD/ton 77 77

    Electricity Input (KWh/ton) 70 302

    Natural gas input (m3/ton)

    (Source: Smart Energy)0.23 34.6

    Residues/Ash Up to 20% Up to 5%

    From Table 1, it was shown that the Thermoselect plant was much cheaper to build as

    compared to the Incinerator. However, the operating cost was slightly higher

    comparatively than the incineration plant.

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    Figure 1 Cash Flow Diagram for Thermoselect

    From Fig. 1, it could be seen that it will take approximately 7 years to break even and

    that the cumulative cash flow at the end of 10 years would be SGD 692.4M.

    3.1.2 Sensitivity Analysis

    Figure 2 Sensitivity Analysis of Syngas Production (Khoo H .H. et. al., 2006)

    From Fig. 2, it can be seen that low production rates of syngas would increase break

    even time required for recovery of capital cost. However, higher production of syngas

    may not reduce the break even time required as the operating costs increases with

    production rates.

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    3.2 Anaerobic Digestion

    3.2.1 Investment Analysis

    Municipal solid waste can be treated using a process known as anaerobic digestion.

    From this process, biogas is produced, which is then combusted and used to drive gas

    engines to produce electricity. The electricity was then sold to the grid. Additional

    income from the tipping fee was also considered when calculating the overall revenue

    of the plant.

    Table 2 Estimated Costs of Anaerobic Digestion Facilities to Process Mixed Waste (Cant, 2006)

    Costs Involved SGD

    Capital Cost 1,5372,000

    Annual Operating Costs

    (including offsite curing

    and residue disposal)

    1,488,400

    Annual Electricity

    revenue1,215,000

    Annual Tipping Fee

    Revenue1,600,000

    Using the estimated costs from Table 2, a cash flow diagram was generated to analyze

    the profitability if this waste treatment process.

    Figure 3 Cash Flow Diagram for Anaerobic Digestion

    From Fig. 3, it was observed that the estimated time taken for the project to break

    even would be slightly more than 12 years. This was due to the high capital and

    operating costs of the facility. This meant that the project would not be profitable due

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    to a low return on investment. Hence, the use of anaerobic digestion as a waste

    treatment process would not be attractive for investors.

    3.2.2 Sensitivity AnalysisGiven the increasing waste generation trend, it is not expected that the production

    rates and revenues would be affected.

    3.3 Composting

    3.3.1 Investment Analysis

    While current practices in Singapore are limited to household scale, the neighbouring

    countries such as Malaysia, Thailand and Philippines already have plants which

    capitalize on the value of the composts.

    Figure 4 Trend of Fertilizer Use in Singapore (TradingEconomics.com, 2012)

    From Fig. 4, it could be noted that the trend of fertilizer use increasing and thus

    presents a potential market to be surveyed for feasibility.

    Table 2 summarizes the finances associated with the investment into

    vermicomposting.

    Table 3 Summary of Finances (Steve R.S et al, 2002)

    Direct costs of operating the processing system

    Expenses incurred at Waste Research Centre

    (WRC)Cost per Block

    Land Rental $200

    Waste application and handling equipment $200

    Screening/harvesting equipment $980

    Utilities $200

    Workshop rental $600

    Labour $810

    Depreciation of beds $1200

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    ($4190)

    Potential Income (per Block)

    WRC Income Worst case Best case

    Compost sales (estimated 20 m3/yr) $600 $2400

    Earthworm sales (estimated 50 kg/yr) $500 $1000($1100) ($3400)

    Direct Processing Cost (per Block)

    Details Worst case Best case

    Direct processing costs $4190 $4190

    Total income $1100 $3400

    Net costs $3190 $790

    Tonnes processed/year 52 52

    Gate fee required to break even $62 $16

    Estimated Overhead Cost (per Block)

    Details Cost per Block

    Staff costs $960Marketing/administration $300

    Premises/facilities $300

    Tonnes processed/year 52

    Gate fee required to break even $30

    Figure 5 Cash Flow Diagram for Composting

    Fig. 5 was constructed from Table 3 to illustrate the cumulative cash flow. The plant

    was constructed under slightly in a year and that with an operating cost of $3340 per

    annum (due to the fixed capacity of the plant). From the CFD, it would take

    approximately 2.2 years to break even and at the end of 10 years, the cumulative cash

    flow would be SGD 32,340.

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    3.3.2 Sensitivity Analysis

    The costs of fertilizers in Singapore are relatively constant and are usually affected by

    demands and transportation costs. This would then affect production cost and

    subsequently the selling price of the product. As waste generation is on the rise

    coupled with the increase in composting trends, it is not expected that the plant feed

    rate would reduce and hence production efficiencies would not be affected.

    However, as the market for the composts is small in Singapore, majority of the

    products would have to be shipped to the neighbouring countries and by doing so

    would then increase the gate fee & reduce the profit margin. With all the addition of

    all the discussed components, the final selling price would be insufficiently

    competitive even though the cost price and general benefits of composting are cheaper

    and better than the inorganic fertilizers used alone.

    3.4 Improved Recycling

    3.4.1 Investment Analysis

    Case studies of recycling firms were studied for its economic feasibility. However a

    financial report for a recycling-only firm could not be obtained. This was because

    most companies in Singapore incorporate collection and waste treatment. As such,

    companies such as Sembwaste were used as the basis. Table 3 summarizes the

    finances of Sembwaste in Year 2011.

    Table 4 Summary of finances obtained (SembcorpBusiness at a glance)

    Year 2011 Sembwaste

    Total waste recycled

    (tonnes/year)150,000

    Revenue

    (SGD in million)370.3

    Profit(SGD in million)

    42

    Capital Cost

    (SGD in million)328.3

    Break even

    (years)8.7

    Based on Table 4, a 10-year cash flow diagram (Fig. 6) was computed to illustrate the

    cumulative cash flow. The following assumptions were made in the computation;

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    Increment of 1% in recycling rate. (According to NEAs waste report ofaverage increment of 1% throughout 10 years.) (ZerowastesgSingapore

    Waste Statistics, 2011)

    Not all waste collected are recycled.

    Figure 6 Cash Flow Diagram for Improved Recycling

    The waste statistics from National Environment Agency showed that the recycling

    rate in year 2011 was 59% with the total waste recycled at 4,038,800 tonnes. From the

    financial report of Sembwaste, it was noted that they only had a share of 2.2%

    (150,000 tonnes) of the 59% of waste recycled in Singapore. This low percentage

    proved that the potential for revenue is high; furthermore it is expected that the

    recycling rates are to be increased.

    From Fig. 6, it could be seen that it took 8.7 years to break even with a cumulative

    cash flow of SGD 65.2M at the end of 10 years.

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    3.4.2 Sensitivity Analysis

    Figure 7 Relationship between commodity prices and profit (Fabian B & Mathias S.,

    2012)

    From Fig. 7, it could be seen that the increase in amount of waste recycled could

    affect the income. Similarly, the commodity price also affects the income as seen

    from the gradients of the lines in Fig. 7 (commodity price being the gradient of the

    lines). Hence, with the increasing trend in the commodity prices coupled with the

    increase in waste generation, it is not expected that business would be affected by a

    reduction in waste processing rate.

    3.5 Incineration & Landfill

    3.5.1 Investment Analysis

    The total waste generated in Singapore was 6.8 million tonnes in 2011 with a

    projected increment of approximately 5.37% per year due to population growth and

    increasing effluence. (Solid Waste management, 2012)

    Table 5 summarizes the approximated finances for the processing of 2.3 million

    tonnes of waste per annum.

    Table 5 Summary of Finances of TSIP

    Spending Avenue Rate Generation/Production Cost per Annum

    - Capital Cost S$890M NA NA

    - Waste Generated to

    TSIP

    NA 2.3Mil ton/yr NA

    - Operation Cost S$70/ton NA -S$161M

    - Landfill fee S$77/ton 0.066Mil ton/Yr -$5.13M

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    Revenues

    - Electricity sold S$0.27/kWh 64MW S$151.4M

    - Ferrous Metal sold S$270 0.39Mil tonne/yr S$105.3M

    - Tipping Fee S$80/tonne 2.3Mil tonne/yr S$184M

    Net Profit less Capital S$440.7M

    Figure 8 Cash Flow Diagram for Incineration

    From Fig. 8, it will take approximately 6.8 years to break even with a cumulative cash

    flow of S$ 1070M at the end of 10 years.

    From the Table 5, it was observed that the tipping fee contributed to the biggest

    portion of the revenue. The tipping fee was calculated based on weight of the waste

    and would hence increase as the waste generation increases.

    Recovered ferrous metal could be sold to local steel mills. The resale of ferrous metal

    only contributes to 24% of the whole revenue generated. The total recovered metalswas 0.39 million tonnes in year 2011. (Solid Waste management, 2012) The average

    price for ferrous metal of S$270/tonne was derived from Table 6.

    Recently a potential market in the bottom ash produced from incineration was found

    for use in concrete. As the bottom ash is very porous, concrete made from bottom ash

    is lighter than those made from natural gravel which helps in lowering the

    transportation cost. For this reason, more construction businesses have switched to

    bottom ash for use in concrete. This reduced the cost of land filling the bottom ash by

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    15-20% which was estimated to be $22/tonne from the current $25/tonne. (Heiner

    Zwahr)

    Table 6 Prices of Ferrous Metal Recyclates in Year 2011 (Letsrecycle: M etal, 2012)

    3.5.2 Sensitivity Analysis

    The energy recovered from the incineration of wastes is also reliant on the calorific

    value of the waste. Figure 9 shows how the calorific value and working capacity

    would affect production cost and subsequently revenue.

    Figure 9 Factors Affecting Treatment Cost and Subsequently Revenue(Decision Makers Guide To Municiple Solid Watse, 1999)

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    From Fig. 10, it was observed that revenue would not be affected significantly despite

    the decline in the prices of ferrous metals due to the increase in waste generation per

    year.

    Figure 10 Prices of Ferrous Metals (Letsrecycle: M etal, 2012)

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    4. Conclusion

    Amongst the explored technologies available for proposal in the survey, a Table 7 was

    constructed to aid in decision making process for the final selection of the technology

    for investment.

    Table 7 Summary of the Economic Analysis of All Technologies

    Technology Indicators Performance

    Thermoselect

    Breakeven period 7 years

    Cumulative Cash @ 10 year SGD 692.37M

    Risk (Sensitivity) High

    Anaerobic Digestion

    Breakeven period 12 - 13 years

    Cumulative Cash @ 10 year SGD -3.433M

    Risk (Sensitivity) Low

    Composting

    Breakeven period 2 years

    Cumulative Cash @ 10 year SGD 25,135

    Risk (Sensitivity) Medium

    Improved Recycling

    Breakeven period 9 years

    Cumulative Cash @ 10 year SGD 65.178M

    Risk (Sensitivity) Low

    Incineration

    Breakeven period 7 years

    Cumulative Cash @ 10 year SGD 1069.989M

    Risk (Sensitivity) Low

    It is clear from Table 7 that Thermoselect, Composting and Incineration were

    promising technologies which would be profitable with a reasonable period to

    breakeven. Both Thermoselect and Incineration broke even at the 7th year mark and

    were low in investment risk. However, at the 10thyear of investment, it could be seen

    that Incineration had the highest cumulative cash flow which meant higher return on

    investment. Furthermore, the Thermoselect technology was assessed to be high in risk

    compared to Incineration, with only low risk.

    Therefore, Incineration was chosen for the ideal waste management technology for

    Singaporebusiness as usualfrom an investors point of view for an economically

    sustainable investment.

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    5. References

    Benefits-of-Recycling:Recycling Prices. What is the Cost of Recycling?Available at: http://www.benefits-of-recycling.com/recyclingprices/

    (Accessed: 30/09/12)

    Business Week: Veolia environment-adr (VE:Singapore).Available at:http://investing.businessweek.com/research/stocks/financials/financials.asp?tic

    ker=VE:SP

    (Accessed: 1/11/12)

    Cant, M. (2006, April). Municipal solidwaste (MSW) options: Integratingorganics management and residual treatment/disposal.

    Cooper, J (2010) Singapores Tuas Incinerator Officially Opened. Availableat: http://www.letsrecycle.com/news/special-reports/singapores-tuas-

    incinerator-officially-opened.

    (Accessed 10/11/12)

    Eco-Business:Recycling in Singapore: 10 years onChute, we got it wrong.Available at:http://www.eco-business.com/news/recycling-singapore-10-years-chute-we-got-it-wrong/

    (Accessed: 1/11/12)

    Fabian B. & Mathias S. (2012)Economic Feasibility of e-Waste Treatment inTanzania, pg25, Swiss Federal Institute for Material Science and Technology

    (EMPA),Switzerland.

    Heiner Zwahr: Ash Recycling: Just A Dream? Available athttp://gcsusa.com/pdf%20files/Ash%20Recycling%20%20Just%20a%20Drea

    m.pdf

    (Accessed 14/11/12)

    Khoo H.H, R. Tan B.H, Salim S. & Wu Y.M (2006)Life cycle evaluation andeconomic considerations of the pyrolysis-gasification of municipal solid waste

    in Singapore, pg 46, Institute of Chemical and Engineering Sciences,

    Singapore.

    Letsrecycle: Metal. Available at:http://www.etsrecycle.com/prices/metals

    (Accessed 14/11/12)

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    Mewr: Solid Management . Available at:http://app.mewr.gov.sg/web/Contents/contents.aspx?ContId=680

    (Accessed 12/11/12)

    NEA:Envision. Available at:http://www.nea.gov.sg/cms/sei/Envision_11Jan_Issue1.pdf

    (Accessed: 10/10/12)

    NEA: Waste Minimisation & Recycling. Available athttp://app2.nea.gov.sg/topics_wasteminimisation.aspx

    (Accessed: 9/10/12)

    Sembcorp:Business at A Glance. Available at:http://www.sembcorp.com/en/investor-relations-businesses-glance.aspx

    (Accessed: 21/11/12)

    Sembcorp: Solid Waste Management. Available at:http://www.sembcorp.com/en/global-presence.aspx?type=waste

    (Accessed: 21/11/12)

    Singapore Power: Tariff Rates. Available athttp://www.singaporepower.com.sg/irj/portal?NavigationTarget=navurl://41c8

    e6a3faf48bb168af2c222faa8ee4&windowId=WID1353506908214

    (Accessed: 22/11/12)

    Smart Energy: Current Price. Available at:http://www.smartenergy.sg/SMART_Energy/Welcome.html

    (Accessed on: 15 Nov 2012)

    Steve R.S & Jim F (2001) Vermicomposting Financial Evaluation and MarketProtential, pg 68-71, Urban Mines Pte Ltd

    Trading EconomicsFertilizer Use in Singapore. Available at:http://www.tradingeconomics.com/singapore/fertilizer-consumption-metric-

    tons-wb-data.html

    (Accessed: 10/11/12)

    Worlds Bank: Decision Makers Guide To Municiple Solid Watse Availableat:

    http://web.mit.edu/urbanupgrading/urbanenvironment/resources/references/pdf

    s/DecisionMakers.pdf (Accessed 14/11/12)

    World-Wire:Recession Proof Cleantech Investing: The Recycling Industry.Available at: http://world-wire.com/news/0804010002.html (Accessed:

    9/10/12)

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    6. Appendices

    6.1 Appendix A

    Incineration

    Introduction

    Incineration is a thermal disposal technique that combusts waste with excess of

    oxygen. There are currently 3 incineration plants in Singapore. The Tuas South Waste

    to Energy Incineration plant would be discussed in this report.

    The plant has six refuse cells with a capacity of 3000 tonnes per day. Steam is

    generated from each boiler with a capacity of 105 tonnes/hr at a pressure of 35barg

    and temperature of 370C. The diesel requirement for cold start-up of the plant is

    5000L/boiler. Cold start-ups are only performed if the plant requires to be shut down

    for maintenance otherwise the refuse are capable of sustaining the combustion itself.

    The plant is rated at 80MW using a 10.5kV generator. 20% of the electricity produced

    is used by the plant while the remaining 80% is sold. Incineration can achieve up to

    90% and 75% reduction in volume and weight respectively. Digital control systems in

    the central control room are used to monitor and control the processes to ensure

    optimum efficiency and reliability.

    Capital Cost refers to the amount of capital required to build the plant which in this

    case is approximately S$890M. The construction of the incineration plant took four

    years.

    Operating cost includes the maintenance cost and the labour cost. An estimated

    operating cost would be S$70/tonne of waste received. Landfilling contributes to a

    fraction of the operating cost as the company is responsible for the disposal of waste

    that cannot be incinerated. A cost of S$77-S$80 (Cooper J, 2010) would be incurred

    by the company for every tonne of waste that is sent for landfill.

    Energy can be recovered from hot water, low grade steam or super-heated steam.

    Price of electricity is $0.27 per kWh in Singapore. Electricity generated by the plant is

    dependent on the amount of waste generated.

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    Process

    The most important process to obtain electricity in the incineration plant is the heat

    generated by the combusting the refuse. The heat from combustion is used to generate

    steam in boilers. Electricity is generated by two steam turbines that are driven by the

    steam. Used steam from the two turbines is condensed by air condenser fans. This

    condensate would then be recycled back into the boiler.

    Figure A1 Process Flow of TSIP

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    6.2 Appendix B

    Thermoselect

    Introduction

    Figure A2 Process Flow of Thermoselect (Yamada S. et. al., 2004)

    Figure A2 shows the typical flow of Thermoselect process. Wastes are compressed

    dried and pyrolyze by indirect heating in a degassing channel. The products are then

    charged into high temperature reactor, where it is melted under controlled amount of

    oxygen and pyrolyzed carbon to form gas. The gas is treated with gas reforming /

    refining / quenching processes before being recovered as clean synthesized fuel gas or

    syngas.

    Process Features

    The features are as follows:

    - Low emissions of dioxins and no generation of fly ash- Increase in use of recyclates

    The waste input is being processed into synthetic gas metals recovered, i.e.

    granulated slag, metal hydroxides and mixed salts. Most substances are

    used effectively as resources and results in minimum waste disposal.

    - Gas ProductsThe key components of syngas are H2and CO, which can be used as fuel

    and also as chemical feedstock. Syngas is applicable to a wide range of

    power generation technologies such as the gas turbine combined cycle.

    Syngas can be sold

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    - Process EconomyThe process uses the energy contained in waste to perform melting and

    remove the need for treatment processes for dioxins and fly ash with heavy

    metal impurity. Due to the efficiency, total cost is lower than conventional

    methods employed such as incineration first followed by ash melting. As

    the process also minimizes the need for landfill, tipping fees are generally

    reduced.

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    6.3 Appendix C

    Improved Recycling

    Introduction

    In the late 1990s, Singapore introduced measures such as recycling in order to cope

    with the increasing waste generation and depleting land space for landfilling.

    Recycling is the process of re-using solid waste materials and re-manufacturing it so

    that it could be used again. This conserves landfill space and prevents wasting of

    useful materials.

    The wastes are collected and distributed to the sorting centers for processing. The

    process will vary with different waste materials. Waste statistics from NEA showed

    that current recycling method can recycle 13 types of wastes as shown in Table A1.

    [NEA: Waste Statistics]:

    Table A1 Types of Waste Recycled

    Waste Type

    1 Construction Debris

    2 Used Slag

    3 Ferrous Metal

    4 Non-ferrous Metals

    5 Scrap Tyres

    6 Wood/Timber

    7 Paper/Cardboard

    8 Horticultural Waste

    9 Glass

    10 Textile/Leather

    11 Plastics

    12 Food waste

    13 Others (stones, ceramics & rubber)

    Events such as Annual Recycling Weekwere held to encourage and educate citizens

    understand the 3R (Reduce, Reuse and Recycle) scheme and thereby raise awareness

    on the importance of waste minimization and recycling. There were also schemes like

    SPA (Singapore Packaging Agreement) which allowed companies to collaborate with

    the government to reduce packaging waste over a 5-year period.

    Presently, the only investors in Singapore are statutory boards such as the Singapore

    Environment Council and National Environment Agency. While more schemes are

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    being introduced to encourage recycling, there are currently no incentive or

    obligations for the citizens to recycle.

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    6.4 Appendix D

    Anaerobic Digestion

    Introduction

    Anaerobic Digestion is a process that converts biomass into beneficial products using

    microorganism in the absence of air. Nearly all biomass can be converted using

    Anaerobic Digestion; some examples are food waste, manure and crop residues.

    However woody biomass cannot be processed using this method, as the

    microorganism is not capable of breaking down lignin in wood.

    The process starts with placing biomass in a sealed tank and allows the

    microorganism to digest the matters. Some of the major products of the process areBiogas and Digestates.

    Biogas can be used as a fuel substitute and can be combust to produce both heat and

    electricity. Typically the mixture is comprised of 60% methane and 40% carbon

    dioxide and some contaminant gases, but the exact composition depends on the type

    of feedstock used.

    Digestates are extremely rich in nutrient and thus it can be used as commercial

    fertilisers. Some of the benefit of using digestates as fertiliser is that it provides

    moisture retention and prevents soil erosion.

    Since there are no anaerobic digestion case studies in Singapore, thus in this report the

    reference would be based on a Germany waste treatment plant. In this report, the case

    study on anaerobic digestion was based on a plant in Germany. Biogas produced from

    the anaerobic digestion plant as well as landfill gases from a nearby landfill is being

    converted to energy.

    The biogas and landfill gases are combusted and the hot flue gas is used to drive gas

    engines which will in turn convert the mechanical energy to electrical energy. The

    electrical output of the plant is an estimated 1400kW. (Mergias, Malamis & Loizidou,

    2007)

    From the information gathered from the case study, the plant is designed to generate

    kWh/year based on the combustion of the gases. During operation, the

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    plant consumes kWh/year, giving it a net electricity production of

    kWh/year. (Mergias, Malamis & Loizidou, 2007)

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    6.5 Appendix E

    Composting

    Introduction

    Composting is the natural breakdown (aerobic) of organic material or waste (paper,

    cardboard, food & horticulture) into useful composts which are then used as fertilizers.

    While there are many types of composting, they are often combined so that it

    increases the type of wastes which can be composted. As Anaerobic Digestion is

    similar in concept as with Anaerobic Composting and that it has been discussed in the

    previous section, it will not be discussed further in this section.

    Of interest, Vermicomposting have increasingly been employed as the method for

    composting due to its ability to entirely eliminate the need for landfill.

    Vermicomposting is the use of worms (black soldier fly larvae or red wrigglers) to

    feed on the waste to produce composts which are used as either fertilizers or animal

    feed.

    The process begins with the conditioning and mechanical sorting and sizing of the

    waste so that the composting period can be shortened. The feedstock (waste) would

    then be fed through a continuous mechanical bed (in blocks, which aerates and

    moisturizes it at specific intervals to ensure a conducive environment for the worms to

    work & reproduce. This process takes approximately 1.5 to 2 months before the

    compost is ready for use. Figure A1 summarizes the process using integrated cow

    farm & vermicomposting plant (Thomas H., 2008)

    Figure A1 Summary of Process Flow