Statistical optimisation of saccharification process using Amorphophallus paeoniifolius tubers into fermentable sugars for bioethanol production in stirred tank batch reactor (STBR)

被引:0
|
作者
S. P. Rakshitha
K. V. Keerthana
P. Anjuna
S. G. Sangam
K. Sandesh
Vinayaka B. Shet
J. N. Neetha
P. Ujwal
N. M. Mubarak
机构
[1] N.M.A.M. Institute of Technology (Visvesvaraya Technological University,Department of Biotechnology Engineering
[2] Belagavi),Department of Chemical and Energy Engineering, Faculty of Engineering and Science
[3] Curtin University,undefined
来源
关键词
Central composite design (CCD); Stirred tank batch reactor (STBR); Bioethanol;
D O I
暂无
中图分类号
学科分类号
摘要
Current technologies to produce biofuels from various renewable feedstocks have considerably captured vast scientific attention since they can be used as an alternative fuel. Bioethanol being one of the most interesting biofuels and due to its positive impact on the environment has been categorised significantly in terms of scientific and technological investments. The aim of this study was to investigate tubers of Amorphophallus paeoniifolius biomass as a feedstock for bioethanol production. The composition analysis of A. paeoniifolius tubers revealed high carbohydrate content (78.30 ± 0.33%). The feedstock was subjected to physicochemical pre-treatment by treating with dilute acid followed by pressure cooking. The pre-treatment factors were optimised by CCD using RSM approach. The optimum condition was found to be 1.32% (v/v) of HCl, 5.83% (w/v) of elephant foot yam biomass and 66.84 min of pressure-cooking time yielding 45.87 g/L of total sugar. The second-order polynomial equation was generated for the saccharification of biomass and validated with R2 0.89. The fermentation of pre-treated biomass in the presence of Saccharomyces cerevisiae MTCC170 yielded 22.12 ± 0.62 g/L of bioethanol at 120 h utilising 92% of initial total sugar. The resultant ethanol yield and productivity was estimated to be 0.51 g/g and 0.30 g/(L/h), respectively. The Gompertz model equation was applied to experimental data using nonlinear regression with least square method and the kinetic fermentation parameters such as maximum ethanol concentration (Pm), production rate (rpm), and lag phase (h) were estimated to be Pm = 21.90 g/L, rpm = 0.57 g/(L/h) and tL = 8.22 h.
引用
收藏
页码:9315 / 9323
页数:8
相关论文
共 14 条
  • [1] Statistical optimisation of saccharification process using Amorphophallus paeoniifolius tubers into fermentable sugars for bioethanol production in stirred tank batch reactor (STBR)
    Rakshitha, S. P.
    Keerthana, K. V.
    Anjuna, P.
    Sangam, S. G.
    Sandesh, K.
    Shet, Vinayaka B.
    Neetha, J. N.
    Ujwal, P.
    Mubarak, N. M.
    BIOMASS CONVERSION AND BIOREFINERY, 2023, 13 (10) : 9315 - 9323
  • [2] Evaluation of power density on the bioethanol production using mesoscale oscillatory baffled reactor and stirred tank reactor
    Yussof, H. W.
    Bahri, S. S.
    Mazlan, N. A.
    3RD INTERNATIONAL CONFERENCE ON CHEMICAL ENGINEERING SCIENCES AND APPLICATIONS 2017 (3RD ICCHESA 2017), 2018, 334
  • [3] Bioleaching of uranium in batch stirred tank reactor: Process optimization using Box-Behnken design
    Eisapour, M.
    Keshtkar, A.
    Moosavian, M. A.
    Rashidi, A.
    ANNALS OF NUCLEAR ENERGY, 2013, 54 : 245 - 250
  • [4] Simultaneous pretreatment and saccharification process for fermentable sugars production from Casuarina equisetifolia biomass using transgenic Trichoderma atroviride
    Rathankumar, Abiram Karanam
    Ravindran, Somdutt
    Saikia, Kongkona
    Arvind, Varshni
    Batista-Garcia, Ramon Alberto
    Folch-Mallol, Jorge Luis
    Kumar, Vaidyanathan Vinoth
    JOURNAL OF THE AIR & WASTE MANAGEMENT ASSOCIATION, 2020, 70 (12) : 1244 - 1251
  • [5] STUDIES ON THE PROCESS FOR UTILIZING OKARA .1. ENZYMATIC SACCHARIFICATION OF OKARA USING CONTINUOUSLY STIRRED-TANK REACTOR
    KITAMURA, Y
    TAGAWA, A
    HAYASHI, H
    JOURNAL OF THE JAPANESE SOCIETY FOR FOOD SCIENCE AND TECHNOLOGY-NIPPON SHOKUHIN KAGAKU KOGAKU KAISHI, 1994, 41 (11): : 821 - 825
  • [6] Batch xylitol production from wheat straw hemicellulosic hydrolysate using Candida guilliermondii in a stirred tank reactor
    Canilha, L
    Silva, JBAE
    Felipe, MGA
    Carvalho, W
    BIOTECHNOLOGY LETTERS, 2003, 25 (21) : 1811 - 1814
  • [7] Batch xylitol production from wheat straw hemicellulosic hydrolysate using Candida guilliermondii in a stirred tank reactor
    Larissa Canilha
    João B. Almeida e Silva
    Maria G.A. Felipe
    Walter Carvalho
    Biotechnology Letters, 2003, 25 : 1811 - 1814
  • [8] Comparison of a batch, fed-batch and continuously operated stirred-tank reactor for the enzymatic synthesis of (R)-mandelonitrile by using a process model
    Willeman, WF
    Straathof, AJJ
    Heijnen, JJ
    BIOPROCESS AND BIOSYSTEMS ENGINEERING, 2002, 24 (05) : 281 - 287
  • [9] Comparison of a batch, fed-batch and continuously operated stirred-tank reactor for the enzymatic synthesis of (R)-mandelonitrile by using a process model
    W. F. Willeman
    A. J. J. Straathof
    J. J. Heijnen
    Bioprocess and Biosystems Engineering, 2002, 24 : 281 - 287
  • [10] Optimisation of a Sequencing Batch Reactor for Production of Polyhydroxybutyrate Using Process Characterisation Method and Neural Network Modelling
    Ganjian, Amin
    Zhang, Jie
    Oliveira, Rui
    24TH EUROPEAN SYMPOSIUM ON COMPUTER AIDED PROCESS ENGINEERING, PTS A AND B, 2014, 33 : 733 - 738