Process Design and Techno-Economic Feasibility Analysis of an
Integrated Pineapple Processing Waste Biorefinery
Shivali Banerjee, Meghana Munagala, Yogendra Shastri, Ranganathan Vijayaraghavan, Antonio F. Patti,
and Amit Arora*
Cite This: https://doi.org/10.1021/acsengineeringau.1c00028 Read Online
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ABSTRACT: This study assesses the techno-economic feasibility of
an integrated biorefinery based on pineapple processing waste.
Xylooligosaccharides, ethanol, xylitol, bromelain, and silage are
among the key products of the biorefinery. The economic
performance of the processes involved in generating the biorefinery
products was assessed based on calculations performed in ASPEN
Plus. Seven different scenarios were designed with individual and
multiple products and were further evaluated for a plant capacity of
10 tons per hour as the base case. Sensitivity analysis showed that
plant capacity and selling price of value-added products were the
most important factors that influenced plant economics. The plant
capacity twice the base capacity often made the venture
economically feasible as in the case of scenarios 1 (production of
xylitol and silage) and 7 (production of bromelain, xylitol, and
silage) with an NPV of $9.2 million and $8.9 million, respectively. Increasing the selling price of the products by 25% of the base
case made scenarios 1 and 6 (production of bromelain, xylitol, ethanol, and silage) economically viable (NPV > 0). A decrease in the
price for procurement of pineapple waste from $25/ton to $10/ton made scenario 4 (production of bromelain and silage) profitable
with an NPV of $3.3 million and IRR of 42%.
KEYWORDS: pineapple processing waste, biorefinery, bromelain, xylitol, techno-economic model
■
INTRODUCTION
The advancement of the bio-based economy over the
dominant fossil-based economy highlights the requirement to
shift toward sustainability to address the emerging environ-
mental challenges.
1
Biorefineries are characterized as the
leading example of a biobased economy. The biorefinery
concept is very similar to a petrochemical refinery where
different processes are integrated to obtain biofuels, bio-
chemicals, heat, and power as the major value-added products
from biomass.
2
Recent studies have focused upon valorization
pathways for food processing wastes, specifically cereals, oil
crops, fruits, vegetables, fish, meat, dairy, eggs, sugar crops, and
tubers.
3,4
Most of the waste biorefinery concepts are broadly
based upon single conversion processes to produce biobased
chemicals and biofuels.
5
As reported in the literature, the
technology readiness levels (TRL) are higher for the
conversion of biomass into energy.
6
Since some of these
technologies such as anaerobic digestion are implemented on a
commercial scale, the real costs for a similar biorefinery are
easily available. However, the biorefineries focused upon the
production of biochemicals and value-added products present
a lower TRL, and hence, the techno-economic assessment is
difficult and uncertain.
7
Most of the economic analyses of
individual biorefineries are conducted using commercial
process simulators such as ASPEN Plus, SuperPro Designer,
and others.
8,9
The economic viability of such biorefineries is
assessed by integrating the fuel/energy production pathways
along with those of value-added products and biochemicals. A
few recent studies have reported the techno-economic
feasibility assessment of biorefineries exclusively focused on
fruit wastes such as citrus wastes,
10,11
olive wastes,
12
mango
waste,
13
and spent pulp of berries.
14
To the best of authors’
knowledge, there is no published work on techno-economic
feasibility assessment for a pineapple processing waste
biorefinery.
The global production of pineapples was estimated to be
28.3 million tons in 2018.
15
The annual production of
pineapples in India and Australia is reported to be 1.7
million
16
and 0.076 million tons,
17
respectively, in 2018.
Received: October 15, 2021
Revised: January 22, 2022
Accepted: January 24, 2022
Article pubs.acs.org/engineeringau
© XXXX The Authors. Published by
American Chemical Society
A
https://doi.org/10.1021/acsengineeringau.1c00028
ACS Eng. Au XXXX, XXX, XXX-XXX
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