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Upgrading of a traditional sugar cane mill to a modern mill and assessing the potential of energy saving during steady state and transient conditions—part II: models for a modified cogeneration unit

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Abstract

It is known that there is a significant amount of thermal energy used for the sugar cane industry for the purpose of power production and for use in the sugar or ethanol processing in cane sugar industries. Likewise, it is understood that there are substantial amounts of waste heat that is not being recovered, in particular for traditional sugar mills. Regardless of this, energy conservation is given less consideration as compared to operational convenience due to the fact that sugar mills are self-sufficient in energy (heat and power). The identification of such potential heat loss areas (especially during transient conditions) suggests the sugar mills play a vital role in energy saving. In this study, a modified setup of the base case plant considered in part I of this paper is assessed for its energy potential and possible major heat losses during steady state and transient conditions where 2-h stoppage of the mill presses are considered to occur. For the modified setup, there are two major scenarios considered having two sub-scenarios each. The result of the assessment showed that the steady state assumption scenario of the modified plant (where bagasse drying is not considered) indicated a 20 % reduction in the losses considered which resulted in a 57 % power generation increase as compared to the steady state model of the base case plant. It is also possible to save excess bagasse by drying the bagasse for later use during unexpected stoppage. The carbon dioxide emission (amounting 29 t/day in case 2a of this study) that occurs during the use of fuel oil during such stoppages will thus be avoided. The simple economic analysis showed that it is only in case 2a where fuel oil cost is included in the operation cost that resulted in a negative NPV. Since the rest of the scenarios use bagasse as a fuel which is free, the NPV for all was positive. For the electricity price of 0.04 US $/kWh and discount rate of 15 %, the minimum payback period attained is about 3 years (case 1b) where the bagasse moisture content is 30 % whereas the maximum payback period is 6 years (case 1a) where there is no bagasse drying considered.

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Notes

  1. According to ZURN’s design document [21], these losses are Lash = 3.5, Lrad = 0.41 and LMM = 1.5 %

Abbreviations

EEPCo:

Ethiopian Electric Power Corporation

FSF:

Finchaa Sugar Factory

FW:

Feed water

NPV:

Net present value

PBP:

Payback period

TCD:

Tonnes of cane per day

C:

Carbon content [%]

CP :

Specific heat capacity [kJ/kg-°C]

E:

Emission (accumulated per day) [tonnes]

\( \overset{\cdot }{\mathrm{E}} \) :

Emission [tonnes/day]

F:

Moisture content [wt%]

h:

Enthalpy [kJ/kg]

H:

Hydrogen content [%]

HHV:

Higher heating value [kJ/kg]

i:

Interest rate [%]

Inv:

Investment [USD]

L:

Loss [%]

LHV:

Lower heating value [kJ/kg]

m:

Mass kg or tonnes

\( \overset{\cdot }{\mathrm{m}} \) :

Mass flow [kg/s] or [tonnes/day]

O:

Oxygen content [%]

P:

Pressure [bar]

PLoss:

Loss [kW], [MW] or [GJ/day]

R:

Revenue [USD/year]

Q:

Heat demand (accumulated per day) [GJ/day]

\( \overset{\cdot }{\mathrm{Q}} \) :

Heat flow [kW] or [GJ/day]

S:

Sulphur [%]

T:

Temperature [°C]

W:

Work output (accumulated per day) [GJ/day]

\( \overset{\cdot }{\mathrm{W}} \) :

Power output [kW]

x:

Steam quality

Ĉ:

Cost [USD]

Ƞ:

Efficiency [%]

α:

Electricity sales price [USD/kWh]

ρ:

Density [kg/L]

r:

Heat of vaporization of water [kJ/kg]

μ:

Mass ratio [kg/kg]

A:

Air

Acc:

Accumulated

Act:

Actual

B:

Boiler

BC:

Base case

D:

Dry

Eqp:

Equipment

El:

Electrical

Eng:

Engineering

Ex:

Excess

F:

Fuel

Fg:

Flue gas

G:

Generator

Is:

Isentropic

Ins:

Installed

Lat:

Latent

MA:

Moisture in air

Me:

Mechanical

MM:

Manufacturer’s margin

n:

Normal conditions (0 °C and 1.013 bar)

New:

New moisture content

OP&M:

Operation and maintenance

PT:

Power turbine

pur:

Purchase

Rad:

Radiation

sm:

Shredder and mill

st:

Steam

tr:

Transmission

tot:

Total

w:

Water

Sen:

Sensible

References

  1. Olivério LJ, Ferreira MF (2010) Cogeneration—a new source of income for sugar and ethanol mills or bioelectricity a new business. Proc Int Soc Sugar Cane Technol 7

  2. Hugot E (1986) Handbook of sugar cane engineering, 3rd edn. Elsevier, New York

    Google Scholar 

  3. Deshmukh R, Jacobson A, Chamberlin C, Kammen C (2013) Thermal gasification or direct combustion? Comparison of advanced cogeneration systems in the sugarcane industry. Biomass Bioenergy 55:163–164

    Article  Google Scholar 

  4. Brazilian Sugarcane Industry Association (UNICA) (2013) http://sugarcane.org/resource-library/books/Folder%20and%20Brochure.pdf. Accessed Feb 2014

  5. ISO (International Sugar Organization) (2009) Cogeneration-opportunities in the world sugar industry. http://www.isosugar.org. Accessed Jan 2014

  6. WADE, World Alliance for Decentralized Energy (2004) Bagasse cogeneration global review and potential. https://cdm.unfccc.int/filestorage/2/K/J/2KJXDVUHFZ0MYG3WOBT91NA7QE6LP5/4057Annex6BagasseCogeneration-GlobalReviewandPotential.pdf?t=M098bm9qdTNxfDBDkAsZVdlUBjCPmWdKPybd. Accessed Jan 2014

  7. Pellegrini FL, Oliveira SO Jr (2011) Combined production of sugar, ethanol and electricity: thermoeconomic and environmental analysis and optimization. Energy 36:3704–3715

    Article  Google Scholar 

  8. Premalatha M, Priya SS, Sivaramakrishnan V (2008) Efficient cogeneration scheme for sugar industry. J Sci Ind Res 67:239–242

    Google Scholar 

  9. Johansson TB, Kelly H, Reddy A, Williams R (eds) (1993) Renewable energy—sources for fuels and electricity Island Press, chapter on “Advanced gasification-based biomass power generation, references 45 and 46”

  10. Sedl Jay Mahesh sugar mill—case study. Available at: http://issuu.com/firetreedesign/docs/sgm_brevini_mill_drives_-case_study_sedl_jay_mahe. Accessed Mar 2014

  11. ABB (2010) ACS 1000 variable speed drives increase energy efficiency at sugar plant-case study. http://www05.abb.com/global/scot/scot216.nsf/veritydisplay/46ae6cf38fa1228bc12577e40056e21d/$file/CS_Sugar%20RevB_lowres.pdf. Accessed Feb 2014

  12. Ensinas VA, Lozano MA, Serra LM (2007) Analysis of process steam demand reduction and electricity generation in sugar and ethanol production from sugarcane. Energy Convers Manag 48:2978–2987

    Article  Google Scholar 

  13. Finchaa Sugar Factory (FSF) (2012) Interview and documents gathered during field study

  14. Yarnal SG, Vinod S, Puranik SV (2010) Energy management study in sugar industries by various bagasse drying methods. Strateg Plan Energy Environ 29(3):56–78. doi:10.1080/10485231009595087

    Article  Google Scholar 

  15. Birru (2007) Investigation of the potential of cane sugar industries. Msc thesis, Royal Institute of Technology-KTH, Sweden

    Google Scholar 

  16. Modesto MJ, Zemp JR, Nebra AS (2009) Ethanol production from sugar cane: assessing the possibilities of improving energy efficiency through exergetic cost analysis. Heat Trans Eng 30(4):272–281. doi:10.1080/0145763080238038

    Article  Google Scholar 

  17. Alemu A (2009) Energy assessment, energy utilization & generation efficiency—a case study in Finchaa sugar factory. Msc thesis, Royal Institute of Technology-KTH, Sweden

    Google Scholar 

  18. Mujeebu AM, Abdullah ZM, Ashok S (2011) Husk-fueled steam turbine cogeneration for a rice mill with power export—a case study. Energy Sources Part A Recover Utilization Environ Eff 33(8):724–734. doi:10.1080/15567030903226298

    Article  Google Scholar 

  19. ECN (2012) Database for biomass and waste. https://www.ecn.nl/phyllis2/. Accessed Jan 2015

  20. Energy efficiency guide for industry in Asia (2006) http://www.energyefficiencyasia.org/energyequipment/assessment_boiler_indirectmethod.html. Accessed Aug 2014

  21. ZURN (2006) Boiler design document-USA

  22. Alibaba (2014) Cost of motor+gearbox (2014) Available at: http://www.alibaba.com/trade/search?fsb=y&IndexArea=product_en&CatId=&SearchText=motor+mounted+gearbox+sugar. Accessed May 2014

  23. ABB Sverig team (2014) Svensk Försäljning Motorer, Drivsystem & Kraftkonvertering / Domestic sales motors, drives and power conversion

  24. SENTECH Incorporated Commercial and Industrial CHP Technology Cost and Performance Data Analysis for EIA (2010) http://www.meede.org/wp-content/uploads/Commercial-and-Industrial-CHP-Technology-Cost-and-Performance-Data-Analysis-for-EIA_June-2010.pdf. Accessed Jan 2015

  25. Alibaba (2014) Cost of bagasse dryers (2014). http://www.alibaba.com/product-detail/High-Quality-China-bagasse-rotary-dryer_1309967662.html?s=p. Accessed May 2014

  26. Finance formulas (2014) http://financeformulas.net/Net_Present_Value.html. Accessed Sept 2014

  27. EEPCo-Ethiopian Electric Power Corporation (2012) http://www.eepco.gov.et/. Accessed Jan 2014

  28. Finance formulas (2014) http://www.financeformulas.net/Payback_Period.html. Accessed Sept 2014

  29. Cardozo E, Erlich C, Alejo L, Fransson TH (2014) Combustion of agricultural residues: an experimental study for small-scale applications. Fuel 115:778–787

    Article  Google Scholar 

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Acknowledgments

Many thanks for the financial support of the Swedish International Development Cooperation Agency (SIDA) that fully funds this project. Thanks to all from Finchaa Sugar Factory, Ethiopian Sugar Corporation, and Ethiopian Electric Power Corporation personnel who helped in gathering relevant data during field study.

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Correspondence to Eyerusalem Birru.

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Birru, E., Erlich, C., Beyene, G.B. et al. Upgrading of a traditional sugar cane mill to a modern mill and assessing the potential of energy saving during steady state and transient conditions—part II: models for a modified cogeneration unit. Biomass Conv. Bioref. 6, 233–245 (2016). https://doi.org/10.1007/s13399-015-0180-8

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