Background, aim, and scopeGlobally, 45 million metric tonnes of palm oil has been produced in 2009. The production of 1 t crude palm oil requires 5 t of fresh fruit bunches (FFB). On average, processing of 1 t FFB in palm oil mills generates 230 kg empty fruit bunches (EFB) and 650 kg palm oil mill effluent (POME) as residues. These residues cause considerable environmental burdens, particularly greenhouse gas emissions. In order to reduce those emissions, four waste management options are compared in the present study using 1,000 kg of FFB as functional unit.MethodsA detailed life cycle model has been used to calculate the environmental impacts of POME and EFB treatment. The options under investigation are: (1) dumping EFB and storing POME and ponds, (2) returning EFB to the plantation and POME as before, (3) using EFB and POME for co-composting and returning the produced compost to the plantation, (4) generating biogas from POME and thereafter as in (3). The CML 2001 method included in the GABI 4.3 software package has been used for the impact calculations. Sensitivity analysis has been carried out in order to estimate the influence of good and poor management practice on the environmental performance.Results and discussionThe main contributor to the GWP is methane from POME and EFB dumping. The GWP of palm oil mill waste treatment can be reduced from 245 kg CO2eq per ton FFB to up to 5 kg CO2eq per ton FFB due to reduced methane emissions and nutrient recycling. Co-composting of POME and EFB leads to considerable nutrient recovery, in addition to GWP reduction. Thus, the composting process reduces not only environmental burdens; it also leads to net environmental benefit regarding most environmental impact categories, e.g., acidification potential, eutrophication potential, ozone layer depletion potential, etc. due to the avoided emissions from inorganic fertilizer production. The recovery of nutrients in EFB can be achieved by solely returning it to the plantation, but only the combined treatment of EFB and POME allows nutrient recovery from POME while methane emissions from pond systems are avoided simultaneously. The fermentation of POME to produce biogas reduces environmental burdens when operating under best practice conditions. However, fugitive biogas emissions of more than 2% reverse that beneficial effect.Conclusion and recommendationA life-cycle-based comparison of conventional and advanced treatment systems for EFB and POME can support decision makers regarding waste treatment options and provide information on technology risks involved. The results of this study may be used as basic calculation data for clean development mechanism for palm oil mills. LCA is shown to be a powerful tool to estimate and compare environmental impacts of different options. Unfortunately, it is rarely used in the palm oil industry in order to improve or optimize palm oil production systems. This study has shown that nutrient recovery from POME and EFB offers considerable environmental and economic benefits to palm oil production systems. However, using EFB for energy production, as it is discussed and realized by some palm oil mills, prohibits environmental beneficial POME utilization. Best waste management practice reduces emissions at palm oil mills and consequently the carbon footprint of palm oil products. Co-composting of EFB and POME, with or without prefermentation of POME in a biogas plant, is a profitable way to use the nutrients from both POME and EFB.
[1]
Subhash Bhatia,et al.
Catalytic cracking of palm oil for the production of biofuels: optimization studies.
,
2007,
Bioresource technology.
[2]
Hans-Jürgen Dr. Klüppel,et al.
The Revision of ISO Standards 14040-3 - ISO 14040: Environmental management Life cycle assessment Principles and framework - ISO 14044: Environmental management Life cycle assessment Requirements and guidelines
,
2005
.
[3]
M. Huijbregts,et al.
Palm oil and the emission of carbon-based greenhouse gases
,
2008
.
[4]
Sune Balle Hansen,et al.
Feasibility Study of Performing an Life Cycle Assessment on Crude Palm Oil Production in Malaysia (9 pp)
,
2007
.
[5]
Subhash Bhatia,et al.
Palm oil: Addressing issues and towards sustainable development
,
2009
.
[6]
Siew Hoong Shuit,et al.
OIL PALM BIOMASS AS A SUSTAINABLE ENERGY SOURCE: A MALAYSIAN CASE STUDY
,
2009
.
[7]
Jeroen B. Guinee,et al.
Handbook on life cycle assessment operational guide to the ISO standards
,
2002
.
[8]
A. Faaij,et al.
Different palm oil production systems for energy purposes and their greenhouse gas implications
,
2008
.
[9]
Abdul Rahman Mohamed,et al.
Utilization of oil palm as a source of renewable energy in Malaysia
,
2008
.
[10]
F. N. Teixeira,et al.
Cogeneration potential in the Columbian palm oil industry: Three case studies
,
2007
.
[11]
Frank Schuchardt,et al.
Effect of new palm oil mill processes on the EFB and POME utilisation
,
2007
.
[12]
Panel Intergubernamental sobre Cambio Climático.
Climate change 2007: Synthesis report
,
2007
.
[13]
Weng ChanKook,et al.
Best-developed practices and sustainable development of the oil palm industry.
,
2005
.
[14]
R. Corley.
How much palm oil do we need
,
2009
.
[15]
Subhash Bhatia,et al.
Catalytic processes towards the production of biofuels in a palm oil and oil palm biomass-based biorefinery.
,
2008,
Bioresource technology.
[16]
Nik Meriam Nik Sulaiman,et al.
Environmental performance of the milling process of Malaysian palm oil using the life cycle assessment approach.
,
2008
.
[17]
Johann Heinrich von Thünen-Institut.
Biogas-Messprogramm II. 61 Biogasanlagen im Vergleich. Publikation
,
2009
.
[18]
M. Z. Abdullah,et al.
Analysis of biomass-residue-based cogeneration system in palm oil mills
,
2003
.
[19]
N. H. Ravindranath,et al.
2006 IPCC Guidelines for National Greenhouse Gas Inventories
,
2006
.
[20]
Kamaruddin Abdullah,et al.
Biodiesel fuels from palm oil via the non-catalytic transesterification in a bubble column reactor at atmospheric pressure : A kinetic study
,
2008
.
[21]
Per Christensen,et al.
Assessing the land use implications of biodiesel use from an LCA perspective
,
2009
.