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Journal of Renewable and Sustainable Energy / Volume 1 / Issue 6 / REGULAR ARTICLES

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J. Renewable Sustainable Energy 1, 063102 (2009); doi:10.1063/1.3259170 (15 pages)

Energy recovery from sugarcane biomass residues: Challenges and opportunities of bio-oil production in the light of second generation biofuels

W. Alonso-Pippo1, Carlos A. Luengo1, F. Fonseca Felfli1, Pietro Garzone2, and Giacinto Cornacchia2

1Grupos Combustíveis Alternativos, DFA/IFGW/UNICAMP, Campinas, São Paulo 13083-970, Brazil
2ENEA's Trisaia Research Centre, CAP 75026, Rotondella, Matera, Italy

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(Received 23 March 2009; accepted 14 October 2009; published online 6 November 2009)

The lack of an alternative energy carrier to electricity with storage capability for use in off-season has to date been an unsolvable question for the sugar agroindustry. The improvement in cogeneration capacity via implementation of condensing extraction steam turbines or biomass integrated gasifier/gas turbine combined cycle and the barriers for their implementation were analyzed. The introduction of a fast pyrolysis (3 tons/h) module (FPM3) as a solution for off-season energy demand in the sugarcane agroindustry was also analyzed. The production cost of 1 ton of bio-oil for FPM3 condition was calculated at 87 USD/ton of bio-oil (0.104 USD/l of bio-oil). The economic feasibility of the FPM3 was estimated, comparing the added values for two alternatives: first alternative regarding the sugar and bioethanol simultaneous production (first generation biofuel production) and second alternative regarding the sugar and bio-oil simultaneous production (second generation biofuel production). Although the highest added value figure for a ton of sugarcane (49.30 USD) was gotten by the second alternative, the bioethanol production for cars fuel continues to be most attractive business option because of large fuel ethanol market demand.

© 2009 American Institute of Physics

Article Outline

  1. INTRODUCTION
  2. BARRIER TO PLANT COGENERATION IMPROVEMENT IMPLEMENTATION (CONDENSING EXTRACTION STEAM TURBINE AND BIOMASS INTEGRATED GASIFIER/GAS TURBINE COMBINED CYCLE)
  3. FAST PYROLYSIS AT SUGAR MILL
    1. Advantages and disadvantages
    2. Energy requirement for bagasse and SCAR FPM3 at medium size sugar mills
  4. FAST PYROLYSIS AT SUGAR MILL: THE OPPORTUNITIES
    1. Technical and economical assessment
      1. Feedstock value estimation
      2. FPM3 and bio-oil production cost
      3. Methodology of added value/added production cost analysis
        1. Added production cost and added value analysis: First generation biofuel (bioethanol) versus second generation biofuel (bio-oil)
  5. CONCLUSIONS

RELATED DATABASES

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KEYWORDS and PACS

Keywords

agriculture, biofuel, cogeneration, pyrolysis, steam turbines

PACS

  • 88.20.F-

    Renewable alternative fuels from biomass energy

  • 89.20.Kk

    Engineering

  • 88.20.T-

    Markets for renewable alternative fuels

ARTICLE DATA

Permalink
http://link.aip.org/link/doi/10.1063/1.3259170

PUBLICATION DATA

ISSN:

1941-7012 (print)  
1941-7012 (online)

Publisher:

$abstract.society.value is a Member of CrossRef American Institute of Physics

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Figures (6) Tables (9)

Figures (click on thumbnails to view enlargements)

FIG.1
Traditional cogeneration scheme BPST; sugar production only (52% steam/ton of milled cane).

FIG.1 Download High Resolution Image (.zip file) | Export Figure to PowerPoint

FIG.2
Improved variant of sugar mill cogeneration scheme; simultaneous sugar-ethanol production.

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FIG.3
Sugar mill cogeneration scheme; CEST; and simultaneous sugar-ethanol production.

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FIG.4
Sugar mill cogeneration scheme; CEST; and cogeneration system (sugar production only).

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FIG.5
Sugar mill cogeneration scheme; CEST; and bio-oil production starting from SCAR.

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FIG.6
Pilot plant (20 kg/h) for biomass residues thermoconversion into liquid and gaseous biofuels.

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Tables

Table I. Sugarcane energy content (average figures for currently commercial sugarcane varieties).

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Table II. FPM3 main features.

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Table III. Maximum acceptable price of sugarcane solid residues used as fuel. Data used: ηresidue and ηbunker C are 0.6 and 0.8, respectively; pricebunker = 193.7 USD/ton (crude oil price 180 USD/ton); HHVbunker C = 43 MJ/kg; LHVbunker C = 40.38 MJ/kg; additional cost = 0; sugarcane residues moisture content: 50% of weight; bunker C moisture content: 11% [USD (2008)].

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Table IV. Estimated capital cost of FPM3 equipments.

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Table V. FPM3 capital cost of investment.

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Table VI. FPM3 operation cost and bio-oil production cost. Basis for estimation: (1) 1 metric ton of bio-oil; (2) two workers; (3) FPM3 (one module); (4) three work shifts; (5) milling season: 160 days/year; (6) depreciation period: 10 years; (7) FPM3 capital cost: $940 000.00; (8) bio-oil production: 48 tons/day (70% process efficiency); (9) annual bio-oil production: 7680 tons/year; (10) previous expenses R&D: $25 000.00.

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Table VII. Alternatives production schemes of a sugar factory.

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Table VIII. Added value/added cost analysis. First alternative: 100 tons of cane. The average yields the following: sugar—0.11 tons/1 ton of cane; ethanol—85 l/1 ton of cane.

View Table
Table IX. Added value/added cost analysis; second alternative (100 tons of cane).

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