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Waste and Biomass Valorization

, Volume 10, Issue 7, pp 1845–1855 | Cite as

Combined Effects of Ionic Liquid and Tungsten–Halogen Radiation on Heterogeneous Hydrolysis Kinetics of Waste Papaya Epidermis for Production of Total Reducing Sugar

  • Swapnendu Chatterjee
  • Sourav Barman
  • Rajat ChakrabortyEmail author
Original Paper
  • 123 Downloads

Abstract

This article reports on optimization and kinetic modeling of Amberlyst-36 heterogeneous catalytic hydrolysis of papaya (Carica Papaya) epidermis (PE) in conjunction with ionic liquid (1-butyl-3-methylimidazolium chloride, [BMIM]Cl) for total reducing sugar (TRS) production. The intensification effects in presence of tungsten–halogen radiator (THR) on sequential pretreatment and hydrolysis have been optimized. In pretreatment and hydrolysis, the optimized factors were 70 and 80 °C reactor temperature, 20 and 10 min batch time, water to PE ratio (w/w) of 5 and 20 respectively. An optimum 2.5 (w/w) NH4OH loading in pretreatment while 7.5 wt% catalyst concentration and 20 (w/w) [BMIM]Cl loading in hydrolysis using the tungsten–halogen radiated reactor (THRR) yielded maximum 89.02 mol% TRS which was significantly greater than that obtained (37.41 mol%) through the conventionally heated reactor (CHR). Eley–Rideal mechanism best fitted the hydrolysis kinetics while pseudo-homogeneous model could best represent pretreatment kinetics. Remarkably, the larger activation energy (69.02 kJ/mol) in CHR in comparison with THRR evidently established the greater energy-efficiency of the THRR system. The evaluated kinetic parameters can be useful for reactor design and scale-up studies. The developed energy-efficient, green hydrolysis for optimum TRS synthesis from papaya epidermis also provides sustainable valorization of similar lignocellulosic biomass waste.

Graphical Abstract

Keywords

Papaya epidermis Tungsten-halogen radiation Total reducing sugar synthesis Factorial optimization Heterogeneous kinetic models Lignocellulosic biomass 

Abbreviations

\({C_{Fp0}}\)

Initial glucose concentration (mol/L) during pretreatment

\({C_{F0}}\)

Initial glucose concentration (mol/L) during AILCH

\({C_{Fp}}\)

Concentration of glucose (mol/L) during pretreatment

\({C_F}\)

Concentration of glucose (mol/L) during AILCH

\({C_{PE}}\)

Concentration of raw papaya epidermis (mol/L)

\({C_P}\)

Concentration of pretreated papaya (mol/L)

\({C_\omega }\)

Concentration of water (mol/L) during pretreatment

\({C_\omega }\)

Concentration of water (mol/L) during AILCH

\({E_{Po}}\)

Pre-exponential factor

\({E_P}\)

Activation energy (kJ/mol)

\({F_p}\)

TRS in pretreatment

F

TRS in AILCH

i

Number of replications

\({k_{p1}}\)

Reaction rate constants for formation of TRS in pretreatment (L/mol min)

\({k_1}\)

Reaction rate constants for formation of TRS in AILCH (L/mol min)

\({k_{p2}}\)

Decomposition of TRS in pretreatment (min− 1)

\({k_2}\)

Decomposition of TRS in AILCH (min− 1)

\({K_\omega }\)

Adsorption equilibrium constant of water (L/mol)

\({k_S}\)

Surface reaction rate constant (L/mol min)

\({K_F}\)

Desorption equilibrium constant of glucose (L/mol)

\({k^{\prime}}\)

Apparent reaction rate constant for Eley–Rideal kinetic model (L/mol min)

N

Number of experiments performed in specified parametric combinations

N

Noise

PE

Raw papaya epidermis

PPE

Pretreated papaya epidermis

\(R\)

Gas constant (kJ/mol K)

\({r_{ER}}\)

Surface reaction rate for ER kinetic model (mol/L min)

\({r_{Fp}}\)

Rate of formation of TRS in pretreatment (mol/L min)

\({r_F}\)

Rate of formation of TRS in AILCH (mol/L min)

S

Signal

S/N

Signal to noise ratio

\({T_1}\)

Temperatures at otherwise optimal conditions derived through TOD

\({T_2}\)

Temperatures at otherwise optimal conditions derived through TOD

UP

Undesired product

\(\omega\)

Water

Greek Letters

ΘcH

Catalyst concentration in subsequent AILCH process

ΘNp

NH4OH loading in pretreatment process

ΘTH

THRR temperature in subsequent AILCH process (°C)

ΘtH

Batch time in subsequent AILCH process (min)

ΘTN

Reactor temperature in pretreatment process (°C)

ΘtN

Batch time in pretreatment process (min)

ΘwN

Water to PE weight ratio in pretreatment process

ΘwH

Water to PPE weight ratio in subsequent AILCH process

Ωg

TRS yield

Notes

Acknowledgements

The reactor used in this work was financed by University Grants Commission, New Delhi, India through Major Research Project [F. No. 43–161/2014 (SR)].

Supplementary material

12649_2018_220_MOESM1_ESM.doc (335 kb)
Supplementary material 1 (DOC 335 KB)

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Copyright information

© Springer Science+Business Media B.V., part of Springer Nature 2018

Authors and Affiliations

  • Swapnendu Chatterjee
    • 1
  • Sourav Barman
    • 1
  • Rajat Chakraborty
    • 1
    Email author
  1. 1.Department of Chemical EngineeringJadavpur UniversityKolkataIndia

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