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Modeling Study of Crude Oil Enhanced Removal in a Two-Liquid Phase Partitioning Bioreactor

  • Zainab Z. Ismail EMAIL logo and Ibtihaj A. Abdulrazzak
Published/Copyright: May 27, 2015

Abstract

A combined process of solvent extraction and two-phase biodegradation was carried out to remove crude oil from water by mixed cultures, where silicone oil was selected as the organic solvent due to its biocompatibility and non-biodegradability. The crude oil removal and cell growth was experimentally studied. A simple model that combined steady mass transfer equations and dynamic growth kinetics of suspended cells was suggested to follow the entire process. Under the conditions studied, complete removal of crude oil from water was achieved at initial crude oil concentration of 5,000 mg/L. Results revealed that the proposed model satisfactorily described the process as long as crude oil level in the cell medium did not exceed the toxicity limit of suspended cells.

Acknowledgment

The Ministry of Environment, Iraq, is greatly acknowledged for the financial and technical support.

Nomenclature

a

effective contact area (m2)

DAB

diffusivity of solute A in solvent B (m2/s)

J

volumetric mass transfer flux of crude oil (g/m2 h)

ka a

Individual volumetric mass transfer coefficient for aqueous cell medium, based on the concentration difference (h−1)

Ka a

Overall volumetric mass transfer coefficient for organic phase based on the concentration difference (h−1)

koa

Volumetric mass transfer coefficient for aqueous cell medium, based on the concentration difference (h−1)

Ki

Substrate inhibition constant (g/m3)

KS

Substrate affinity constant (g/m3)

MSM

mineral salt media

M

molecular weight (g/mol)

N

number of data points

P

Partition coefficient of crude oil between organic phase and aqueous phase

S0

initial crude oil level in the system (g/m3)

Scm

crude oil level in cell medium at any time (g/m3)

Sicm

crude oil level at the cell medium–organic interface (g/m3)

Siorg

Organic-side crude oil level adjacent to the cell medium–organic interface (g/m3)

Sorg

crude oil level in organic phase at any time (g/m3)

Stotal

total crude oil level in the system at any time (g/m3)

SD

standard deviation

t

time (h)

t90

time required when Stotal = 0.1 S0 (h)

T

absolute temperature (K)

TPPB

two-phase partitioning bioreactor

VA

molar volume of solute A at its normal boiling point (cm3/mol)

VC

critical volume of solute A (m3)

X

cell concentration (g/m3)

Y

cell yield on crude oil substrate (g cell/g crude oil)

Greek letters

µB

viscosity of solvent B (cp)

µ

specific cell growth rate (h−1)

µmax

maximum specific cell growth rate (h−1)

ΦB

association parameter of solvent B (-)

Subscripts

exp

experimental value

model

modeled (predicted) value

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Published Online: 2015-5-27
Published in Print: 2015-9-1

©2015 by De Gruyter

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