Open access peer-reviewed chapter

Sorption of Pollutants in Wastewater Solids

Written By

Rakesh Govind and Ankurman Shrestha

Submitted: 20 February 2022 Reviewed: 03 March 2022 Published: 28 September 2022

DOI: 10.5772/intechopen.104208

From the Edited Volume

Sorption - From Fundamentals to Applications

Edited by George Z. Kyzas

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Abstract

Sorption in wastewater solids is an important removal mechanism for pollutants in biological treatment systems. It is often an overlooked mechanism, since traditionally, excess solids from biological treatment were land filled. However, with the emergence of using wastewater solids as a potential fertilizer, pollutants sorbed into the solids can re-emerge as soil pollutants, with potential uptake by crops, and even transported into groundwater. This is especially applicable for hydrophobic chemicals, like alkyl fluorinated compounds (PFAS, PFOS), which have recently received widespread attention as pollutants in water bodies across the globe. In this chapter, sorption of pollutants in wastewater solids has been presented from both a thermodynamic analysis, involving equilibrium parameters, as well as a kinetic process involving transport to the cell walls and permeation through the cell membranes. Based on experimental data and models it is shown that biodegradation in wastewater systems is actually mass transfer coefficient for diffusive transport across the microbial cell walls.

Keywords

  • sorption
  • biomass
  • cell
  • permeability
  • transport
  • pollutants

1. Introduction

Transport of pollutants into wastewater solids (biomass) can occur due to a variety of mechanisms, some of which are surface related, while others involve absorption or sorption into the biomass cells. Uptake of pollutants by the surface of the biomass is defined as “adsorption” driven by several possible mechanisms which includes hydrophobic-hydrophobic interaction, electrostatic interaction and hydrogen bonding. The latter two mechanisms are dominant under basic and acidic conditions, respectively, while hydrophobic-hydrophobic interaction occurs mainly under neutral conditions [1].

Sorption or absorption in biomass involves the transport of the pollutants into the cell, rather than adsorbed on the outside surface of the cells. Sorption in wastewater solids is an important mechanism for removal of organic compounds in biological wastewater treatment systems. Experimental results and theoretical developments related to the sorption process have been reported in our previous work [2, 3]. During isotherm measurements, biological activity in wastewater solids, especially in activated sludge, that contains a substantial amount of active biomass, must be controlled to obtain accurate sorption isotherms. Measurements of varying aqueous phase concentrations could include the effect of biodegradation, resulting in apparent sorption capacities greater than actually achieved.

Sorption in Biomass can be analyzed as an equilibrium process, using isotherms, as well as a kinetic process, involving transport to the biomass cell walls and permeation through the cell membranes.

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2. Analysis of equilibrium sorption: surface adsorption vs. partitioning

A dual-process mechanism [4] was postulated for the sorption of lindane and hexachlorocyclohexane on five unidentified bacteria. In this mechanism, sorption was viewed as a combination of rapid surface adsorption and diffusive penetration. A similar mechanism was suggested [5] for the uptake of 2,4-dichlorophenoxyacetic acid by Pseudomonas fluoresces. The result was a combination of the following steps: adsorption onto the cell wall accompanied by passive diffusion into the cytoplasm. Based on the comparable sorption results of organic compounds between live and dead biomass in a Kraft mill generated lagoon, it was suggested that sorption on biomass was mainly a passive diffusion of small molecules into the cell than active or facilitated transport [6].

By comparing the sorption of chloroethanes on different types of microbial biomass, it was speculated [7] that the sorption of organic molecules on microbial biomass was related to the leachable organic carbon which was released from the cell cytoplasm due to the rupture of cells. It was found that the more leachable organic carbon the biomass contained, the higher the uptake capacity of the toxic organic compound it had.

In order to better understand the sorption mechanism on microbial biomass, Bell [8, 9, 10, 11] examined the magnitude of the heats of sorption for diazinon and lindane. The thermodynamic data strongly suggested a physical sorption instead of a chemical sorption. By reviewing the sorption mechanism on biomass in the literature, Bell [9] concluded that firm, general conclusions cannot be reached concerning the mechanism of sorption on biomass. Indeed, the mechanisms may be specific to the particular system of chemicals and biomass. It seems likely that a combination of adsorption and absorption may be responsible for the sorption on biomass and that the relative importance of each mechanism may vary from system to system [12].

Biological activity in wastewater solids, especially in activated sludge which contains a substantial amount of active biomass, must be controlled in order to obtain accurate sorption isotherms. Otherwise, measurements of changing aqueous phase compound concentrations could include the effect of biodegradation, resulting in apparent sorption capacities greater than actually achieved. Despite the difficulties associated with the control of the biological activity in biomass, several attempts have been reported.

In this chapter, sorption in biomass will be modeled as an adsorption partitioning process, in which physical adsorption on the surface and partitioning into the biomass cells occurs simultaneously. Wastewater solids contain high percentage (50–85%) of organic matter, in a relatively loose physical form. It is generally believed that the organic matter is a complex mixture of live and dead microorganisms, which are primarily proteins, fats and carbohydrates, and other organic sediments. While the organic matter is basically solid, it is certainly different from activated carbon. The nature of the organic matter gives the sludge certain characteristics of an organic solvent. Chiou et al. [13, 14, 15] described the sorption of toxic organic compounds on soil organic matter as a partitioning phenomenon. Using the Flory-Huggins theory, they were able to derive an equation relating the partition coefficient of a toxic organic compound between the aqueous phase and the soil organic matter to the molar water solubility of the compound. Essentially, the uptake of toxic organic compounds by sludge through dissolution into cells can be viewed as a partitioning process in which the toxic organic compounds are distributed between two phases: the aqueous solution and the organic matter of the cell.

In the early stage of the sorption process, the cell is basically free of the toxic organic compounds except for the amount adsorbed on the surface. The difference in chemical potential causes the toxic organic compounds to transport from the bulk liquid to the region close to the surface and to be adsorbed onto the surface. In the meantime, the partitioning and subsequent penetration (diffusion) of the toxic organic compounds into cells occurs in parallel with adsorption. When a molecule approaches the site already occupied by another molecule in a process to form a double layer on the sludge surface, unlike in the case of activated carbon adsorption in which the penetration of the adsorbate into the solid wall of carbon normally does not occur, the resulting higher chemical potential on this site is likely to cause the adsorbed molecule to be dissolved in the organic matter of the cell.

To test this hypothesis, isotherm measurements were conducted for the first four compounds in Table 1 using pasteurized sludge to eliminate biodegradation. For the other compounds, listed in Table 1, untreated sludge was used, since these compounds are non-biodegradable within the 6-hour equilibriation time period. The model coefficients obtained for these compounds are also listed in Table 1, along with the average percentage error between the calculated and experimental points. Table 2 lists the contribution of partitioning to the overall sorption amount (qpi/q) along with the partition coefficient, kpi and the octanol–water partition coefficient (KOW).

PollutantPartition coefficient (kp) l/gMaximum adsorption capacity (qao) mg/gEquilibrium adsorption constant (k) l/mg% Error
Methylene chloride0.0120.2500.3012.2
Chloroform0.0350.1490.486.4
1,1-dichloroethylene0.1400.0420.486.4
Carbon tetrachloride0.2100.1001.4021.5
Chlorobenzene0.2430.0102.6018.9
Tetrachloroethylene0.6530.0125.299.7
Phenanthrene6.80.0201.2925.0
Dibutyl phthalate7.000.0145.3014.7

Table 1.

Best-fit parameters of the adsorption-partition (A-P) model for sorption of selected pollutants on activated sludge. % error is the average error between the experimental value of pollutant uptake and calculated value.

PollutantPartition coefficient (kp) l/gOctanol–water partition coefficient (KOW)Total sorption (q) mg/gqp/q
Methylene chloride0.012180.070.172
Chloroform0.035930.0830.420
1,1-dichloroethylene0.1401340.1560.899
Carbon tetrachloride0.2104360.2680.783
Chlorobenzene0.2436900.2500.971
Tetrachloroethylene0.6537590.6630.985
Phenanthrene6.828,1846.8110.998
Dibutyl phthalate7.00158,4897.0120.998

Table 2.

Partition coefficient, octanol–water partition coefficient, Total sorption and ratio of amount partitioned to the Total sorption amount for selected pollutants in activated sludge. Liquid phase concentration of each pollutant is 1 mg/l.

For the last four compounds in Table 2, adsorption is negligible with over 90% sorption occurring due to partitioning. This is also consistent with the KOW values for these compounds, which is an indication of the compound’s hydrophobicity, and thus has a higher tendency to partition with the organic matter of the biomass. This shows that a compound’s equilibrium partitioning into biomass due to sorption is correlated directly with its KOW value, and this correlation (correlation coefficient = 0.97) is given as follows:

Logkp=0.73LogKOW2.64E1

Experimental studies were conducted to better understand the competition effects in multicomponent systems. it was found that compounds which primarily adsorb on the surface have a strong impact of competitive adsorption, with the adsorption extent of one compound varying greatly with the concentration of the second compound. This is due to the fact that the number of surface adsorption sites on biomass are limited and adsorption of one compound will impact the adsorption capacity of the second compound.

However, for compounds which primarily undergo sorption instead of surface adsorption, there is no competitive sorption between the compounds. The adsorption-partitioning (A-P) model was used to fit the sorption of methylene chloride, chloroform and tetrachloroethylene in the presence of 1,1-dichloroethylene. According to Table 2, the percentage of partitioning in the overall uptake for these compounds are 17.2%, 42% and 98.5%, respectively. Hence, the effect of competition would be most significant for methylene chloride and least significant for tetrachloroethylene. The simulation results are shown in Figures 13. For tetrachloroethylene, there is almost no competition effect, as was the case where chlorobenzene was the competing compound. For both methylene chloride and chloroform, the higher the concentration of 1,1-dichloroethylene, the more reduction in total uptake of the key component.

Figure 1.

Effect of concentration of 1,1-dichloroethylene as a competing species for sorption of methylene chloride.

Figure 2.

Effect of the concentration of 1,1-dichloroethylene as a competing species for sorption of chloroform.

Figure 3.

Effect of the concentration of 1,1-dichloroethylene as a competing species for sorption of tetrachloroethylene.

Based on the correlation given by Eq. (1), the degree of domination by either partitioning or surface adsorption depends on the values of KOW. Table 3 compares the KOW values and the competition effect in several binary and multicomponent systems, for uptake of compounds by wastewater solids. It is clearly seen that the KOW value can be qualitatively divided into three ranges: (1) KOW < 500, there is a clear effect of the presence of a competing compound; (2) 500 < KOW < 1000, the competition effect is smaller, and depends on the specific compounds being studied; and (3) KOW > 1000, when competitive surface adsorption can be ignored.

Key pollutantCompeting pollutantsCompeting effectKOWReference
Phenol (P)2-chlorophenol (CP), 2-Nitrophenol (NP)Yes
Yes
29[16]
2-Nitrophenol (NP)2-chlorophenol (CP),
Phenol (P)
Yes
Yes
57[16]
1,1,2-Trichloroethane (TCE-1)1,1,2,2-Tetrachloroethane (TCE-2)Yes117[7]
2-Chlorophenol (CP)Phenol
Nitrophenol (NP)
Yes
Yes
148[16]
1,1,2,2-Tetrachloroethane (TEC-2)TCE-1Yes363[7]
Chlorobenzene (CB)Ethylbenzene (EB)Slight690[16]
Tetrachloroethylene (TCE)CBNo759[2]
Malathion (M)Diazinon (D)Yes776[9]
Diazinon (D)Lindane (L)
Lindane (L), Pentachlorophenol (PCP), Malathion (M)
No
No
1380
1380
[9]
[9]
Ethylbenzene (EB)CBNo1412[9]
Lindane (L)Pentachlorophenol (PCP)No5248[9]
Phenanthrene (PT)Dibutyl Phthalate (DP)No28,000[2]
Pentachlorophenol (PCP)L
L,D,M
No
No
44,668
44,668
[9]
[9]
Dibutyl Phthalate (DP)PTNo1.58 x 105[2]

Table 3.

Relationship between KOW and the competition effect in multicomponent sorption of toxic organic pollutants on wastewater solids.

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3. Analysis of sorption kinetics

The rate of partitioning of compounds into biomass depends on the rate of mass transfer of the compound into the cells, and this can be described as occurring in three steps: (1) mass transfer from the bulk water to the surface of the biomass cells; (2) transport through the cell walls; and (3) bonding with the active inter-cellular enzymes followed by biodegradation of the compound within the cell. In this section, these three steps will be quantified and experimental data on biodegradation rates will be used to analyze the extent of each step’s contribution.

Cell membrane permeability has been shown to play an important role in the biodegradation process, when the membrane permeability is increased [17, 18]. The permeability of bilipid membranes can be estimated from the octanol–water partition coefficient and the molecular weight of the compound [13],

P=0.003KOWMW0.5E2

where Kow is the octanol–water partition coefficient and MW is the molecular weight of the organic compound. The permeability coefficient can also be written as [19],

P=kpDmeanλE3

Where kP is the partition coefficient, Dmean is the average diffusion coefficient of the compound through the cell wall membrane, and λ is the thickness of the cell wall membrane. As discussed in the earlier section, the partition coefficient can be determined from the compound’s KOW value.

The dependance of a compound’s diffusivity through the cell wall, Dmem, on molecular size, represented by molecular volume, is given by the following correlation:

LogDmem=LogDmemV=0mVVE4

where DmemV=0 is the compound’s diffusion coefficient for a theoretical molecule of infinitely small size, through the membrane. This correlation gives a slope of mV = −0.0013 molecules/cm3. From Eq. (3) we get the following result:

PV=0=10mVVPE5

where PV = 0 is the cell wall permeability for a molecule of infinitely small size and this limiting permeability values gives a good correlation with the octanol–water partition coefficient, KOW, as shown in Figure 4.

Figure 4.

Plot of Log(PV = 0) versus LogKOW. PV = 0 is the cell wall permeability for a molecule of infinitely small size.

According to Fick’s first law of diffusion, the flux (Jb) of a compound from bulk liquid to the outside cell wall surface is given by the following equation:

Jb=kbCbCcmE6

where kb is the mass transfer coefficient from the bulk to the cell surface, Cb and Ccm are concentrations of compound in the bulk liquid and at the cell membrane outside surface, respectively.

Flux (Jcm) through the cell membrane can be written as follows:

Jcm=PCcmCiE7

where P is the compound’s permeability through the cell membrane, Ccm is the compound concentration on the outside surface of the cell membrane and Ci is the intracellular compound concentration. Assuming that the Monod kinetics apply, the rate of substrate biodegradation inside the cell can be given by,

Ji=μmaxCiKi+CiVAE8

where Ji is the mass of substrate consumed per unit time per unit surface area of the cell, mmax, Ki are the maximum growth rate and half saturation constants, respectively, V is the volume of a cell and A is the surface area of the cell. For first order Monod kinetics, Kx ≫ Ci so Eq. (8) can be written as:

Ji=kiCiVAE9

where ki =μmax/Ki is the first order biodegradation rate constant. Eqs. (6), (7), and (9) can be combined to give the following equation for the flux of the compound into the cell:

Ji=Jcm=Jb=J=Cb1kb+1P+AkiVE10

The flux of the compound into the cell can also be written as.

J=ktotalCbCiVAE11

where ktotal is the overall mass transfer coefficient. The active intercellular enzymes will significantly reduce the intracellular concentration so that Ci = 0 Combining Eqs. (10) and (11) we get the following result:

1ktotal=1kbVA+1PVA+1kiE12

The ratio (V/A) can be determined from the biomass concentration, X, in water, density of mixture of ρi, using the following equation, assuming all biomass cells are spherical, with an average diameter of di.

VA=6Xρidi=αE13

Substituting Eq. (13) into Eq. (12) we get the following result (Figure 5).

Figure 5.

Plot of calculated Log(ktotal) vs. Log(α/P) showing that the overall biodegradation rate constant is actually diffusional resistance across the cell membrane for 50 randomly selected toxic organic compounds which were not used in the analysis.

1ktotal=1kbα+1Pα+1kiE14

Values for the overall mass transfer coefficient, ktotal, were taken from an EPA report [20], the mass transfer coefficient from the bulk water to the outside cell surface, kb, was estimated from the diffusivity of the compound in water assuming a boundary layer thickness of 4 micrometers [20], the cell permeability, P, was calculated using Eq. (2) assuming a biomass concentration, X, of 2.5 kg/m3 [21], and a liquid density, ρi, as 1000 kg/m3 and an average cell diameter, di of 1 micrometer [16, 22, 23].

Table 4 shows the calculated values of the bulk phase mass transfer coefficient, kb, the cell wall permeability, P, calculated from Eq. (2), and the biodegradation kinetic constant, ki, determined from Eq. (12), using the values of ktotal from EPA’s report [20]. The calculated values clearly show that the cell wall permeability is the controlling resistance. It also shows that the measured values of the biodegradation kinetic constant, as given in EPA’s Report [20], are mainly resistance of the compound’s diffusion across the cell wall membrane.

S. NoCompound namektotalh1kbαh1Pαh1kih1
1Diisodecyl Pthalate3.7659765.81823.88271495.8965
2Di-n-Octyl Phthalate2.5381706.90912.57802132.1180
3Dibenzopyrene1,2,7,81.0573981.81821.0727799.1360
4Bromacil1.00871060.36361.0245696.2582
5Indeno (1,2,3-cd)-Pyrene0.65961119.27270.6722364.3080
6Dimethyl Benz(A)ANT 7,120.55221197.81820.5634284.7684
7Dimethylbenz(A)Anthracene (7,12)0.5522981.81820.5628300.4840
8Methyl Cholanthrene 30.53941060.36360.5501285.2126
9PPCB’s (Aroclors)0.48501570.90910.4955231.9249
10Dieldrin0.3411922.90910.3483167.9746
11Benzo(B)Fluoranthene0.32271099.63640.3298153.2084
12Benzo(K)Fluoranthene0.32191099.63640.3289152.7507
13Toluene Diisocyanate (2,4)0.31181217.45450.3187145.4517
14Tetra Chlorodibenzo-p-Dioxin (2,3,7,8)0.27021138.90910.2762124.9391
15Methoxychlor0.2546883.63640.2601120.5382
16DDT0.1823981.81820.186482.3114
17ChloroBenzilate0.17901138.90910.183179.8019
18Dichlorobenzophenone P,P0.16081335.27270.164670.5525
19Benzo(A)Pyrene0.15171767.27270.155365.5411
20Pentachlorobenzene0.14991237.09090.153465.7798
21Dimethyl Trisulfide0.13291629.81820.136157.3433
22Dibenzofurans0.11831178.18180.121151.4321
23DDE, p,p′ -0.11771158.54550.120551.2012
24Aldrin0.1156962.18180.118350.6902
25Pentachloronitrobenzene0.11321197.81820.115949.1063
26Benzo(A)Anthracene0.10971767.27270.112446.9333
27Endrin0.1088922.90910.111347.6631
28Hexachlorobenzene0.09711158.54550.099441.9121
29Tributyl Tin Acetate0.09651138.90910.098841.6854
30Tributyl Phosphate0.09381021.09090.096040.6475
31Warfarin0.09031060.36360.092539.0118
32ChloroBenzylate0.0891903.27270.091238.7346
33Trifluralin0.0878981.81820.089937.9977
34Dodecane0.08601158.54550.088136.9834
35Triisobutylene0.08391374.54550.085935.8866
36Tetrachlorobenzene (1,2,3,4)0.07711453.09090.078932.8341
37Tetrachlorobenzene (1,2,3,5)0.07711453.09090.078932.8330
38Acifluorfen0.0674864.00000.069029.0357
39Heptachlor0.06721119.27270.068828.7305
40ChloroazoBenzene0.06591453.09090.067527.9799
41Triisopropylamine0.06241296.00000.063926.5454
42Diisopropyl Benzene (Para)0.06051413.81820.061925.6515
43Methylene-Bis (2-Chloroaniline) 4,4′0.05901138.90910.060425.1252
44Tributyl Phosphorotrithioate SSS0.0542922.90910.055523.1364
45Diphenylmethane0.05391531.63640.055222.8083
46TetrachloroPhenol (2,3,4,6)0.05231394.18180.053522.1228
47TetrachloroPhenol (2,3,5,6)0.05231394.18180.053522.1223
48Bisphenol(A)0.04741119.27270.048620.1181
49Benzophenone0.04251296.00000.043517.9528
50Tetrachlorobenzene (1,2,4,5)0.04191728.00000.042917.6434
51Trichlorobenzene 1,2,30.03961610.18180.040616.6779
52Trichlorobenzene 1,3,50.03961610.18180.040616.6769
53Diethylthiophosphatebenzo M Ethyl Pether0.03571080.00000.036615.0790
54BIS(1,1,2,2 - Tetrachloropropyl)Ether0.03561040.72730.036415.0343
55Biphenyl0.03391610.18180.034714.2359
56HexaFluoroacetone0.03241394.18180.033113.6190
57ChloroBenzophenone (PARA)0.03221453.09090.033013.5492
58Dimethylbenezidine 3,30.03111217.45450.031913.1076
59Cymene, para0.03081433.45450.031612.9555
60Diethylbenzene P0.03081590.54550.031612.9429
61Methyl Napthalene (1-)0.03011531.63640.030812.6524
62Methyl Napthalene (2-)0.03011531.63640.030812.6527
63Chloronapthalene, 2-0.02981728.00000.030512.5058
64Silvex0.02861138.90910.029312.0378
65Chlorophazine0.02571276.36360.026310.7930
66Nitrobiphenyl, 4-0.02561374.54550.026210.7449
67Pinene (alpha-)0.02541433.45450.026010.6626
68Acenapthene0.02501512.00000.025610.4963
69Phenylphenol P0.02301335.27270.02359.6402
70Diazinon0.0229962.18180.02359.6582
71Ethylhexylacrylate 2-0.02201197.81820.02259.2396
72Ethyl Toluene, 40.02201531.63640.02259.2213
73Tetralin0.02181590.54550.02239.1447
74Dichlorobenzonitrile,2,6-0.02161492.36360.02219.0648
75Hexachlorobutadiene0.02141217.45450.02198.9730
76Dipropylbutral0.02121433.45450.02178.8953
77Anthraquinone0.02121492.36360.02178.8772
78Phenylcyclohexanone 40.02051315.63640.02108.6025
79Pentachloropheol0.02041197.81820.02098.5610
80Diisobutylene0.02011433.45450.02068.4367
81Dichlorophenol (2,4)0.01981728.00000.02038.3269
82Aminobiphenyl, 4-0.01901492.36360.01957.9636
83Octane0.01881394.18180.01937.8944
84Propyl (−n) Benzene0.01881531.63640.01937.8850
85Dimethyl Phthalate0.01861237.09090.01908.0786
86TrimethylPentane 2,2,40.01841472.72730.01887.6955
87Diethyl (N,N) Aniline0.01831158.54550.01877.6749
88Endosulfan0.0181903.27270.01857.6105
89Chlorotoluene-40.01791708.36360.01837.4858
90Bromotoluene 40.01791669.09090.01837.4864
91Dimethyl Amino Azobenzene, 4-0.01761296.00000.01817.3979
92Dazomet0.0176141.81820.01807.3761
93DichloroBenzidine, 3,3′-0.01751315.63640.01797.3261
94Cumene0.01731394.18180.01777.2422
95Acetylaminofluorene, 2-0.01701178.18180.01757.1539
96Alpha Methyl Styrene0.01682238.54550.01727.0159
97Methylstyrene (−4)0.01681728.00000.01727.0224
98Hexachloroethane0.01671335.27270.01716.9875
99Trichloro-1,2,2,- Trifluoroethane, 1,1,2-0.01671590.54550.01716.9805
100Acenapthlyene0.01621472.72730.01666.7824
101Dimethyl Disulfide0.01601983.27270.01646.6994
102Carbendazim0.01561276.36360.01606.5580
103Methylene Diphenylamine (MDA)0.01561256.72730.01606.5331
104Methylene Diphenyl Diisocyanate0.01461217.45450.01506.1368
105Toxaphene0.0145844.36360.01496.1114
106Toluene0.01441688.72730.01486.0352
107Chlorambucil0.01421178.18180.01465.9616
108Dichlorophenol (2,6)0.01381728.00000.01415.7780
108Dichlorophenol0.01381394.18180.01415.7826
110Dichlorophenol 2,50.01381394.18180.01415.7841
111Dichloroethane (1,1) ethylidenedichloride0.01382061.81820.01415.9160
112Nitrobenzene0.01381688.72730.01415.9137
113DichloroBenzene (1,4) (−p)0.01381551.27270.01415.7758
114Bromobenzene0.01371826.18180.01405.7183
115Xylene(−m)0.01331531.63640.01365.5749
116Anthracene0.01321512.00000.01355.5204
117Terpinenol, Alpha0.01311453.09090.01345.4917
118Heptane ISO0.01291394.18180.01325.3957
119Heptane (−n)0.01291492.36360.01325.3896
120Dimethoxy-(3,3′)-Benzidine0.01281080.00000.01315.3488
121Xylene(−p)0.01271649.45450.01315.3348
122EthylBenzene0.01261527.70910.01295.2726
123Nonanol, n0.01201354.90910.01235.0072
124Naphthol, alpha0.01201492.36360.01225.0034
125Nitro m Xylene, 20.01191570.90910.01214.9607
126Parathion0.01171138.90910.01204.9201
127DiphenylHydrazine (1,2)0.01151453.09090.01184.8052
128DiChloroAniline 2,30.01141413.81820.01174.7824
129DichloroAniline(2,3)0.01141413.81820.01174.7832
130Methyl Cyclohexane0.01081669.09090.01114.5316
131Xylene0.01081826.18180.01114.5150
132Xylene(−o)0.01081963.63640.01114.5154
133Diethylene Glycol Diethyl Ether0.01061335.27270.01084.4195
134Captan0.0105962.18180.01074.3904
135Isodecanol0.01041453.09090.01074.3643
136Benzotrichloride0.01041531.63640.01074.3649
137Tetrafluoromethane0.01021826.18180.01044.2524
1382,4,5 Trichlorophenoxyacetic acid0.00981315.63640.01014.1248
139Dinitro-o-Cresol (4,6)0.00981354.90910.01004.1089
140Methyl Isocyanate0.00982847.27270.01004.0764
141Naphthol, beta-0.00971492.36360.01004.0679
142Dichlorophenoxyacetic Acid (2,4)0.00931276.36360.00953.9000
143Chlordane0.0092864.00000.00943.8742
144Carbon Tetrachloride0.00901728.00000.00923.7650
145Dichloropropylene 1,2,-(Cis)0.00892160.00000.00913.7104
146Hexane(−n)0.00881531.63640.00903.6858
147Xylidine Dimethylaniline0.00881649.45450.00903.6854
148Pentachloroethane0.00871433.45450.00903.6556
149Guthion0.0087942.54550.00893.6368
150Trifluoroethane (1,1,1)0.00862552.72730.00883.6057
151Benzene0.00841924.36360.00863.5278
152Dichloropropane 1,20.00841708.36360.00863.5210
153Chrysene0.00841217.45450.00863.5101
154Methyl 1-Pentene 20.00831767.27270.00853.4883
155Propyl Ether Iso0.00831826.18180.00853.4528
156Styrene Oxide0.00821747.63640.00843.4277
157Ehtyl(2)Hexanol0.00821433.45450.00843.4257
158Octanol 30.00821433.45450.00843.4257
159Octanol 20.00821433.45450.00843.4257
160Octanol 40.00821433.45450.00843.4257
161Octanol 10.00821433.45450.00843.4237
162MethyleneDianiline 4,40.00811472.72730.00833.3975
163Benzofuran 2,30.00811767.27270.00833.3710
164ChloroNitrobenzene, p0.00791845.81820.00813.3086
165Chloronitrobenzene (−o)0.00791845.81820.00813.3082
166Chloroacetophnone, 2-0.00781708.36360.00803.2837
167Freon 11, Fluorotrichloromethane0.00771963.63640.00793.2307
168Dichloropropylene 1,2,- (Trans)0.00772160.00000.00793.2068
169ChloroBenzotriFluoride, P0.00761688.72730.00783.1867
170ButylIsoButyrate0.00741728.00000.00763.1139
171Trichlorofluoromethane0.00741904.72730.00763.1019
172Cyclohexane0.00741786.90910.00763.0974
173Dimethyl Benzylamine N,N0.00741708.36360.00763.0938
174Allyl Ether, diallyl ether0.00731669.09090.00753.0718
175Chlorophenol-40.00711904.72730.00732.9702
176Nitrotoluene, o0.00691708.36360.00712.9057
177Nitrotoluene, p0.00691688.72730.00712.9055
178Nitrotoluene, m0.00691610.18180.00712.9068
179ChloroButadiene, 10.00691963.63640.00712.9022
180ChloroBenzyl Alcohol - (m)0.00681865.45450.00702.8579
181Triethylene Glycol Dimethyl Ether0.00681315.63640.00702.8445
182Freon 12, Dichlorodifluoromethane0.00661669.09090.00682.7746
183Ethylphenol,3-0.00661845.81820.00682.7671
184Tetraethyl Lead0.00661256.72730.00672.7591
185Methyl Benzyl Alcohol 40.00651688.72730.00672.7345
186Carbaryl Sevin0.00641394.18180.00652.6771
187Triethylamine0.00641551.27270.00652.6720
188Phosphine0.00633573.81820.00652.6302
189Proporur (Baygon)0.00621315.63640.00632.5915
190Cumeme Hydroperoxide0.00611492.36360.00632.5584
191Paraldehyde0.00611570.90910.00622.5471
192Bromoform0.00612022.54550.00622.5417
193Benzyl Chloride0.00611531.63640.00632.5349
194Dibromo-4-HydroxyBenzonitrile,3,50.0060981.81820.00622.5341
195Dichloroethane (1,2)0.00591944.00000.00602.5085
196Naphthylamine, beta -0.00581649.45450.00592.4275
197Acetylmethylphthalate 40.00571099.63640.00582.3825
198Naphthylamine, alpha -0.00571649.45450.00582.3676
199Diisopropylamine0.00561531.63640.00572.3488
200Dichloroethylene (1,2) Cis0.00562218.90910.00572.3285
201Diethylene Glycol Monobutyl Ether0.00561374.54550.00572.3317
202Butyl Carbitol0.00561374.54550.00572.3310
203TolueneSulfonyl Chloride0.00551276.36360.00562.3096
204Thiourea, 1-(o-Chlorophenyl)-0.00541413.81820.00552.2656
205Carbon Disulfide0.00541963.63640.00552.2452
206Freon 12 Dichlorodifluoromethane0.00542061.81820.00552.2469
207Benzal Chloride0.00531865.45450.00552.2321
208Chlorophenol-20.00531865.45450.00542.2282
209Trichloroethylene0.00531786.90910.00542.2093
210TriPropylene Glycol0.00521413.81820.00532.1848
211Toluidine (−0)0.00521786.90910.00532.1607
212Toluidine m0.00521806.54550.00532.1613
213Dipropylamine0.00512022.54550.00532.1505
214Butyl Acrylate0.00511512.00000.00522.1430
215Toluic Acid (para-)0.00511531.63640.00522.1441
216Pentadiene 1,20.00502022.54550.00512.0718
217Dinitro Toluene 2,60.00491433.45450.00502.0460
218Benzonitrile0.00492002.90910.00502.0319
219Methyl Parathion0.00481158.54550.00492.0302
220Quinoline0.00481629.81820.00492.0086
221Cyclopentadiene0.00482140.36360.00491.9997
222DinitroToluene (2,4)0.00471394.18180.00481.9766
223Cyclohexylamine0.00472042.18180.00481.9466
224Bromoxynil0.00461021.09090.00471.9477
225Chloropropylene-20.00462709.81820.00471.9276
226Dichloropropene (1,3)0.00461963.63640.00471.9226
227Acrylonitrile0.00452631.27270.00461.9706
228Benzoyl Chloride0.00452140.36360.00461.8869
229Trichloroethane 1,1,1, Methyl Chloroform0.00441728.00000.00451.8555
230Trichloroethane 1,1,20.00441728.00000.00451.8590
231Ethyl Morpholine, Ethyl Diethylene Oxime0.00441728.00000.00451.8341
232Methyl Chloride0.00431276.36360.00451.8212
233Nitrophenol,4-0.00431885.09090.00441.8103
234Methyl-Tertiary-Butyl Ether0.00432061.81820.00441.7926
235Ethylene Glycol MonoPhenyl Ether0.00421649.45450.00431.7791
236Bromodichloromethane0.00422081.45450.00431.7656
237Butadiene - (1,3)0.00422120.72730.00431.7449
238Butene0.00412002.90910.00421.7362
239Benzoic Acid0.00411570.90910.00421.7335
240Butane0.00412199.27270.00421.7281
241Furan0.00412395.63640.00421.7190
242Tetrachloroethene0.00411610.18180.00421.7043
243Tetrachloroethane (1,1,2,2)0.00411551.27270.00421.7049
244Dichloromonofluoromethane0.00402258.18180.00411.6878
245Benzidine0.00392945.45450.00401.6619
246Isobutylene0.00392002.90910.00401.6351
247Butyl Acetate (−n)0.00391590.54550.00401.6334
248Nitrophenol,2-0.00391669.09090.00401.6288
249Diethylene Glycol Dimethyl Ether0.00391354.90910.00391.6204
250Hexanol-10.00381472.72730.00391.6080
251Dinitrophenol 2,40.00371786.90910.00381.5741
252Amyl Acetate (−n)0.0036235.63640.00371.5311
253Dimethyl Sulfide0.00362866.90910.00371.5114
254Isophorone0.00361335.27270.00371.5106
255Methyl Iodide0.00362042.18180.00361.4961
256Benzyl Alcohol0.00351767.27270.00361.4764
257Adiponitrile0.00351747.63640.00361.4764
258DichloroBenzene (1,2) (−o)0.00351551.27270.00361.4545
259Tetraethyldithiopyrophosphate0.00351080.00000.00351.4628
260Trichloropropane (1,1,2)0.00341826.18180.00351.4545
261Vinyl Acetylene0.00342768.72730.00351.4435
262Ethyl Vinyl Ether0.00341924.36360.00351.4363
263Diethyl Ether0.00341688.72730.00351.4284
264Ethyl Ether0.00341826.18180.00351.4281
265Anisidine, o-0.00331747.63640.00341.3925
266Ethlene Dibromide0.00332336.72730.00341.3862
267Chloramben0.00331669.09090.00331.3778
268Hexanoic Acid0.00331649.45450.00331.3734
269Acetophenone0.00321708.36360.00331.3597
270Bis(2-Chloroethyl)Ether0.00321472.72730.00331.3628
271Furfural0.00322042.18180.00331.3564
272Cyclohexanol0.00321629.81820.00331.3543
273Ethylene Glycol Monobutyl Ether0.00321610.18180.00321.3295
274Butyl Cellosolve0.00321590.54550.00321.3305
275Dinitrobenzene M0.00311492.36360.00311.2970
276Ethyl Acrylate0.00301688.72730.00311.2703
277Chloral0.00301904.72730.00311.2573
278Ethylene Glycol Monobutyl Ether Acetate0.00301335.27270.00301.2618
279Dichloroethene 1,2 trans0.00302336.72730.00301.2462
280Benzaldehyde0.00301786.90910.00301.2472
281TolueneDiamine (2,6)0.00291806.54550.00301.2216
282TolueneDiamine (3,4)0.00291806.54550.00301.2214
283Toluene Diamine (2,4)0.00291786.90910.00301.2225
284Epoxybutane 1,20.00292022.54550.00291.2047
285tetrahydrofuran0.00292061.81820.00291.2050
286Propylene0.00282670.54550.00291.1914
287Propene0.00282336.72730.00291.1923
288Chloroethane (Ethyl Chloride)0.00282258.18180.00291.1920
289Trichloropropane (1,2,2)0.00281826.18180.00291.1964
290Propane0.00282592.00000.00291.1847
291Chlorophenol-30.00281845.81820.00281.1693
292Toluidine p0.00271845.81820.00281.1537
293Methyl Isobutyl Ketone0.00271531.63640.00281.1408
294Trinitrotoluene (2,4,6)0.00271256.72730.00272.0189
295Propyl Acetate Iso0.00271708.36360.00271.1239
296Propyl (−n) Acetate0.00271728.00000.00271.1234
297Methyl Morpholine0.00271767.27270.00271.1224
298Chloro 2 Butene, 1 Trans0.00261904.72730.00271.1134
299Hexen-2-ONE 50.00261728.00000.00271.1083
300Diethylene Glycol Monoethyl Ether0.00261570.90910.00271.1035
301Diethylene Glycol Monoethyl Ether0.00251983.27270.00261.0507
302Nitropropane 20.00251413.81820.00251.0446
303HexaMethylene 1,6 Diisocyanate0.00251276.36360.00251.0482
304Diethylene Glycol Monoethyl Ether Acetate0.00242454.54550.00251.0167
305Diethyl Amine0.00242297.45450.00251.0155
306Methylene Chloride, Dichloromethane0.00242002.90910.00240.9926
307Dioxane (1,4)0.00231158.54550.00240.9923
308Ametryn0.00231688.72730.00230.9700
309Nitroaniline P0.0023216.00000.00230.9720
310Phosgene (decomposes)0.00233161.45450.00230.9536
311Hydrogen Sulfide0.00232906.18180.00230.9527
312Methyl Mercaptan0.00221590.54550.00220.9365
313Dibromoethane-1,20.00221845.81820.00220.9275
314Ethylene Glycol Dimethyl Ether0.00221983.27270.00220.9208
315Butyraldehyde ISO0.00222395.63640.00220.9204
316Dimethylethylamine0.00222238.54550.00220.9202
317Butyraldehyde0.00222395.63640.00221.1617
318Acrolein0.00221826.18180.00220.9194
319Ethylene Glycol MonoPropyl Ether0.00212376.00000.00220.9018
320Bromomethane0.00212002.90910.00220.8841
321Crotonaldehyde0.00521786.90910.00532.1607
322Vinyl Bromide0.00212317.09090.00210.8773
323Chloropropane-20.00201983.27270.00210.8609
324Dimethyl Carbamoyl Chloride0.00201963.63640.00210.8621
325Quinone0.00202101.09090.00200.8445
326Ethane0.00193279.27270.00200.8140
327Bromochloromethane0.00191963.63640.00190.8134
328Allyl Chloride0.00192120.72730.00190.7973
329Chloropropene-30.00192729.45450.00190.7952
330Chloropropane-10.00192022.54550.00190.7908
331Catechol0.00181806.54550.00190.7854
332Hexachloroxyclohexane (Gamma Isomer)0.00181433.45450.00190.7904
333Lindane Hexachlorocyclohexane0.00181217.45450.00190.7945
334Dichlorvos0.00181433.45450.00190.7938
335Vinyl Acetate0.00181806.54550.00190.7799
336EthylAcetate0.00181904.72730.00190.7758
337Methyl Isopropyl Ketone0.00181806.54550.00180.7624
338Diethylene Glycol Monomethyl Ether0.00181688.72730.00180.7647
339Propyl Amine Iso0.00182061.81820.00180.7534
340ButylAmine0.00171885.09090.00180.7466
341Dichloro-2-Butene, 1,20.00172022.54550.00180.7464
342Dichloro-2-Butene, (1,4)0.00171590.54550.00180.7465
343Dichloro-2-Butene, 1,40.00171826.18180.00180.7502
344Thiourea0.00172709.81820.00180.7349
345Phenylene Diamine (−o)0.00171944.00000.00170.7272
346Phenylene Diamine (−p)0.00171944.00000.00170.7272
347Phenylene Diamine (−m)0.00171944.00000.00170.7251
348Phthalimide0.00171629.81820.00170.7302
349Phthalic Acid0.00171335.27270.00170.7152
350Terephthalic Acid0.00171394.18180.00170.7192
351Caprolactam0.00171767.27270.00170.7144
352Cyclohexanone0.00161688.72730.00170.7094
353Cyanogen0.00162690.18180.00170.7009
354Acrylamide0.00162081.45450.00170.6970
355Resorcinol0.00161708.36360.00170.6960
356Butyric Acid0.00151983.27270.00160.6611
357Formaldehyde0.00153888.00000.00150.6257
358Dibromomethane0.00151649.45450.00150.6528
359Propionaldehyde0.00152238.54550.00150.6351
360Ethoxyethanol-20.00151885.09090.00150.6364
361Dichloroethyl Ether0.00151865.45450.00150.6432
362Methacrylic Acid0.00142061.81820.00150.6241
363Pyridine0.00141492.36360.00150.6139
364Nitroglycerin0.00141531.63640.00150.6355
365Methyl Ether Dimethyl Ether0.00142925.81820.00140.6034
366Chloroethylene0.00143024.00000.00140.6030
367Diethylhydrazine N,N0.00142022.54550.00140.6022
368Ethylene Glycol Monoethyl Ether Acetate0.00141492.36360.00140.6138
369Propylenimine 1,22 Methyl Aziridine0.00142847.27270.00140.5962
370Methyl Aziridine 20.00142847.27270.00140.5946
371Dimethyl Hydrazine (1,1)0.00142140.36360.00140.5858
372Hydroquinone0.00141767.27270.00140.5909
373Aminophenol (−o)0.00131688.72730.00140.5867
374Aminophenol (−p)0.0013471.27270.00140.5874
375Chloroprene0.00131963.63640.00140.5756
376Tamaron (Methamidiphos)0.00131531.63640.00130.5692
377Propanol0.00122238.54550.00130.5397
378Propiolactone b0.00122238.54550.00130.5356
379Tetranitromethane0.00121374.54550.00130.5583
380Methanol0.00123220.36360.00120.8385
381Methyl Ethyl Ketone, 2 Butanone0.00121924.36360.00120.5352
382Urethane0.00122081.45450.00120.5202
383Acetaldehyde0.00122768.72730.00120.5096
384Piperazine0.00122042.18180.00120.5174
385Chloropropionitrile,3-0.00122454.54550.00120.5161
386Chloroallyl Alcohol 20.00112415.27270.00110.4933
387DimethylSulfoxide0.00112179.63640.00110.4872
388Neopentyl Glycol0.00111806.54550.00110.4925
389Butanedinitrile0.00112317.09090.00110.4828
390Dimethyl Sulfate0.00111885.09090.00110.4803
391Acrylic Acid0.00112081.45450.00110.4682
392Propanoic Acid0.00102199.27270.00110.4606
393Aminopyridine, 4-0.00102120.72730.00110.4630
394Propyn-1-Ol 2(Proparlgyl)0.00102611.63640.00100.4468
395Ethylene Glycol MonoMethyl Ether0.00102199.27270.00100.4463
396Ethylene Glycol Monoethyl Ether Cellosol0.00101924.36360.00100.4505
397Propylene Oxide0.00101963.63640.00100.4366
398Trichloropropane (1,2,3)0.00101552.27270.00100.4409
399Trichloropropane 1,1,10.00101551.27270.00100.4342
400Dibromo-3-Chloropropane,1,20.00101374.54550.00100.4542
401Nitroso-N-Methylurea N0.00102002.90910.00100.4248
402Ethylene Glycol MonoMethyl Ether Acetate0.00101570.90910.00100.4406
403Ethylamine0.00093298.90910.00100.4190
404Aziridine ethylene imine0.00093102.54550.00100.4144
405Acetaldol0.00092120.72730.00100.4232
406Allyl Alcohol0.00092238.54550.00100.4118
407Dipropylene Glycol0.00091512.00000.00100.4185
408Tetraethylene Pentamine0.00091276.36360.00090.4169
409Xylenol(3,4)0.00091629.81820.00090.4092
410Methyl Formate0.00092493.81820.00090.3950
411Nitromethane0.00092749.09090.00090.3849
412Vinyl Chloride0.00092415.27270.00090.3870
413Dimethyl Amine0.00083279.27270.00090.3783
414DimethylAcetamide0.00082415.27270.00090.3789
415DimethylSulfoxide0.00082592.00000.00090.3753
416Epichlorohydrin0.00081924.36360.00090.3753
417Glutaric Acid0.00081570.90910.00080.3752
418HexamethylPhosphoramide0.00081354.90910.00080.3877
419Propylene Chlorohydrin0.00082061.81820.00080.3726
420Dimethyl Formamide0.00082022.54550.00080.3564
421Butylene Glycol - (1,3)0.00082002.90910.00080.3604
422Methyl Acetate0.00071963.63640.00080.3504
423Diazomethane0.00073436.36360.00070.3248
424Adenine0.00071708.36360.00070.3469
425Chloromethyl Methyl Ether0.00072631.27270.00070.3201
426Chloroacetaldehyde0.00072258.18180.00070.3168
427Butanol(S)0.00072199.27270.00070.2783
428Butanol-10.00071826.18180.00070.2778
429Butanol Iso0.00071826.18180.00070.2781
430DimethylSulfone0.00061944.00000.00070.3156
431Ethlene Diamine0.00062768.72730.00070.2986
432Dichloro Propanol 2,230.00061924.36360.00070.3229
433Carbonyl Sulfide0.00062552.72730.00070.2936
434Diethyl Sulfate0.00061590.54550.00060.3067
435Methomyl0.00061413.81820.00060.3234
436Acetyl Chloride0.00062258.18180.00060.3021
437Acetonitrile0.00063259.63640.00060.2786
438Bis(Chloromethyl)Ether0.00061845.81820.00060.2984
439Glycidol0.00062395.63640.00060.2774
440Succinic Acid0.00061669.09090.00060.3003
441Sodium Formate0.00063200.72730.00060.2680
442Nitrosomorpholine0.00061963.63640.00060.2879
443Maleic Acid0.00052258.18180.00060.2779
444Fumaric Acid0.00051688.72730.00060.2895
445Ethyl Carbamate0.00052474.18180.00060.2834
446Urea0.00052690.18180.00050.2649
447Nitrosodimetylamine N0.00052434.90910.00050.2724
448Methyl Hydrazine0.00052729.45450.00050.2567
449Propylene Glycol0.00052002.90910.00050.2648
450Dichloro 2-Propanol 1,30.00051924.36360.00050.2671

Table 4.

Values of mass transfer coefficients for overall transport of toxic organic compounds (1/ktotal), obtained from Ref. [19], bulk diffusion from bulk water to outside cell surface (α/kb), across the cell membrane (α/P) and biodegradation rate constant (1/ki).

To check this surprising finding, 50 organic compounds, listed in Table 5, were randomly selected from EPA’s report [20]. These compounds were not used to correlate the overall degradation rate with the cell wall permeability. Figure 4 shows the plot of the reported Log(ktotal) values for these 50 compounds [20] versus the mass transfer resistance for pollutant transport across the cell wall, (α/P). This resulted in an excellent correlation, indicating that cell wall permeability is the rate controlling step for biodegradation, as well as the rate controlling step for sorption, which precedes biodegradation.

S. NoCompound name
11,3-Dichloro 2-Propanol
2Glyphosate
3Methyl Amine
4Formamide
5Phthalic Anhydride
6Chloroacetic Acid
7Ethylene Thiourea
8Acetyl-2-thiourea, 1-
9Diethanolamine
10Iso-Propanol
11Monomethyl Formamide
12Ethanolamine (mono-)
13Acetamide
14N,N-Dimethylaniline
15Ethylene Glycol
16Formic Acid
17Chlorohydrin
18Morpholine
19Hydroxyacetic Acid
20Glyoxal
21Oxalic Acid
22Hydrazine
23Glycerin (Glycerol)
24Dibromochloromethane
25Pentaerythritol
26Nabam
27Triethanolamine
281,3-Propane Sultone
29Styrene
302,4,6-Trichlorophenol
31Bis(2-Ethylhexyl) Phthalate
32p-Chloroaniline
332-Chloroaniline
343-Chloroaniline
35Ethylene Oxide
36Aldicarb
37Vinylidene Chloride
38Diisopropyl Ketone
39Ethanol
40Dichloroethene (1,1) vinylidene chloride
41Maleic Anhydride
42Napthalene
43DibutylPhthalate
44Acetal
45Toluic Aldehyde
46Acetic Acid
47Phosphine
48Proporur (Baygon)
49Cumeme Hydroperoxide
50Paraldehyde

Table 5.

List of 50 toxic organic compounds selected from the EPA report [19], which were used to test the finding that the biodegradation kinetics, as reported in Ref [19] is actually a measurement of diffusional resistance across the cell membrane.

The kinetics of sorption is the rate of mass transfer to the cell wall followed by permeation of the compound across the cell membrane. Between these two transport steps, permeation across the cell wall is the rate controlling step. This can be written as follows

1ksorptionα1PE15

Table 4 shows that permeation of the compound through the cell membrane is the rate controlling step. The kinetic biodegradation rate constants, as presented in the EPA report [20], also given in Table 4, are actually sorption rate constants, since the cell wall permeability is the dominant rate controlling step.

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4. Conclusions

In this chapter, sorption in wastewater solids has been presented both from a thermodynamic viewpoint, with surface adsorption and sorption into the cells represented by an equilibrium isotherm. Experimental data on the equilibrium concentrations of several compounds was analyzed using a multicomponent model. The experimental data shows that for compounds with low KOW vales (KOW < 500), competitive surface adsorption occurred, indicating that the multiple compounds were competing for the limited number of surface adsorption sites on the biomass. For compounds with KOW vales in the 500–1000 range, surface adsorption dominated and there was less competition between the compounds for adsorption. When the KOW value exceeded 1000, there was insignificant competition between the compounds for surface adsorption and sorption into the cell was dominant. The reason for diminishing competition between the compounds in a multi-component system was due to increasing partitioning of the compounds within the cell, with increases in KOW above 500. Partitioning of compounds into the cell dominates when the KOW value exceeds 1000.

Sorption of compounds into biomass has also been presented from a kinetic point of view by detailing the compound’s transport across the cell membrane. The rate of a compounds transfer from bulk water into the biomass cells was sub-divided into three steps: (1) transport from the bulk water to the outside of the cell walls; (2) permeation through the cell membrane walls; and (3) bonding with active intercellular enzymes followed by biodegradation. Each step in the sorption process was further modeled and values of the mass transfer coefficients for each step were calculated using EPA’s data on the overall biodegradation rate for over 500 compounds. This analysis showed that the rate controlling step in sorption was permeation of the compound through the cell walls, and the rate of mass transfer to the cell wall and biodegradation within the cell were not major contributors.

Analysis of sorption kinetics clearly shows that experimental biodegradation rates in the literature, as summarized in EPA report [20] are actual rates of permeation through the cell wall and the use of Monod kinetics, which has been presented as an enzymatic process of biodegradation, is actually a passive diffusive process through the walls of the microbial cells.

References

  1. 1. Al-Ghouti MA, Al Absi RS. Mechanistic understanding of the adsorption and thermodynamic aspects of cationic methylene blue dye onto cellulosic olive stones from wastewater. Scientific Reports. 2020;10:15928
  2. 2. Dobbs RA, Wang L, Govind R. Sorption of toxic organic compounds on wastewater solids: Correlation with fundamental properties. Environmental Science and Technology. 1989;23(9):1092
  3. 3. Wang L, Govind R, Dobbs RA. Sorption of toxic organic compounds on wastewater solids: Mechanism and modeling. Environmental Science and Technology. 1993;27:152
  4. 4. Sugiura K, Sato S, Goto M. The adsorption-diffusion mechanism of BHC-residues. Chemosphere. 1975;4:189
  5. 5. Wedemeyer G. Uptake of 2,4-Dichlorophenoxyacetic acid by Pseudomonas fluorescens. Applied and Environmental Microbiology. 1966;14:486
  6. 6. Amy GL, Bryant CW, Alleman BC, Barkley WA. Biosorption of organic halide in a Kraft mill generated lagoon. Journal—Water Pollution Control Federation. 1988;60(8):1445
  7. 7. Tsezos M, Seto W. The adsorption of chlroethanes by microbial biomass. Water Research. 1986;20(7):851
  8. 8. Bell JP. Biosorption of hazardous organic pollutants. [PhD thesis]. Canada: McMaster University; 1987
  9. 9. Bell JP, Tsezos M. Removal of hazardous organic pollutants by adsorption on microbial biomass. Water Science and Technology. 1987;19:409
  10. 10. Bell JP, Tsezos M. Removal of hazardous organic pollutants by biomass adsorption. Journal—Water Pollution Control Federation. 1987;59(4):91
  11. 11. Bell JP, Tsezos M. The selectivity of biosorption of hazardous organics by microbial biomass. Water Research. 1988;22(10):1245
  12. 12. Torres E. Biosorption: A review of the latest advances. PRO. 2020;8:1584
  13. 13. Chiou CT. Partition coefficients of organic compounds in lipid-water system and correlations with fish bioconcentration factors. Environmental Science and Technology. 1985;19(1):57
  14. 14. Chiou CT, Peters LJ. Freed VH. A physical concept of soil-water equilibria for nonionic organic compounds. Science. 1979;206(16):831
  15. 15. Chiou CT, Porter PE, Schmedding DW. Partition equilibria of nonionic compounds between soil organic matter and water. Environmental Science and Technology. 1983;17(4):227
  16. 16. Ouzounov N et al. Orientation correlates with cell diameter in Escherichia coli. Biophysical Journal. 2016;111:1035-1043
  17. 17. Wang L et al. Biosorption and degradation of decabromodiphenyl ether by Brevibacillus brevis and the influence of decabromodiphenyl ether on cellular metabolic responses. Environmental Science and Pollution Research. 2016;23:5166-5178
  18. 18. Liao L et al. Biosorption and biodegradation of pyrene by Brevibacillus brevis and cellular responses to pyrene treatment. Ecotoxicology and Environmental Safety. 2015;115:166-173
  19. 19. Bressler DC, Gray MR. Transport and reaction processes in bioremediation of organic contaminants. 1. Review of bacterial degradation and transport and reaction processes in bioremediation of organic contaminants. International Journal of Chemical Reactor Engineering. 2003;1:1–16
  20. 20. Air emission models for waste and wastewater. EPA-453/R-94-080A. 1994. pp. C5–C30
  21. 21. Wioland HC, Woodhouse FG, Dunkel J, Kessler JO, Goldstein RE. Confinement stabilizes a bacterial suspension into a spiral vortex. Physical Review Letters. 2013;110:1-5
  22. 22. Govind R, Gao C, Lai L, Tabak HH. Continuous automated and simultaneous measurement of oxygen uptake and carbon dioxide evolution in biological systems. Water Environment Research. 1996;69:73-80
  23. 23. Selvakumar A, Hsieh HN. Competitive adsorption of organic compounds by microbial biomass. Journal of Environmental Science and Health. 1988;A23(8):729

Written By

Rakesh Govind and Ankurman Shrestha

Submitted: 20 February 2022 Reviewed: 03 March 2022 Published: 28 September 2022