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May 26, 2026Fermentation0 citationsOpen Access

Orange-Peel Waste Enzymatic Saccharification: Scaling-Up Under Diverse pH-Control Strategies

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RCRamón J. Ceballos-ZúñigaUniversidad Complutense de MadridMLMiguel LaderoUniversidad Complutense de Madrid

Key Points

  • The aim is to optimize the enzymatic saccharification of orange-peel waste by examining different pH control methods to enhance sugar yields.
  • Studied enzymatic hydrolysis of orange-peel waste using batch and fed-batch processing.
  • Utilized 50 mM citrate buffer and 9 g/L NaCl solution with CaCO3 for pH control.
  • Evaluated particle size effects and stirring conditions to achieve high yields.
  • Achieved glucose yields of up to 136 g/L and fermentable sugars of 74 g/L with NaCl and CaCO3 condition.
  • Shortened processing time to 50 hours compared to longer times with citrate buffer.
  • Fractal kinetic models effectively represented compositional changes across varying conditions.

Abstract

Waste from the fruit juice industry presents high sugar and phenolic contents, high humidity and biological activities and cumbersome disposal or low-added valorization. Orange-peel waste (OPW) represents 35–55% w/w of processed fruit, with oranges being the main citric crop. OPW saccharification leads to sugar-rich hydrolysates that can be further processed via fermentative and catalytic routes. In this work, OPW enzymatic hydrolysis was studied via batch and fed-batch processing using either a 50 mM citrate buffer or a 9 g/L NaCl solution with pH control by adding CaCO3 to ensure high enzyme activity across the enzymatic process. Preliminary runs showed that particle size of 3.4 mm diameter and a 300 r.p.m. stirring speed, a six-blade Rushton turbine and wall baffles were adequate to reach high sugar yields in batch. Further scale-up in batch at medium solid loading (12.5% w/w) and fed-batch operation at high-solid loading (20% w/w) led to high yields and glucose and fermentable sugars (up to 74 and 136 g/L, respectively, when using the saline solution and CaCO3 as pH-controlling agent, in only 50 h; notably shorter and higher than when using the citrate buffer). Fractal kinetic models have been shown to accurately represent the compositional change across all batch and fed-batch conditions, highlighting NaCl reaction medium and alkali-driven pH control as the most appropriate approach to achieve high yields at low process times, a promising result for further developments at demonstration and industrial scales using automatic pH control.

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Cite This Study

Ceballos-Zúñiga et al. (2026) studied this question.

synapsesocial.com/papers/6a153bdfb5d9c58d83e8d4a7https://doi.org/10.3390/fermentation12060254
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