Adsorption equilibrium modeling for water on activated carbons

Adsorption equilibrium modeling for water on activated carbons

Carbon 43 (2005) 2258–2263 www.elsevier.com/locate/carbon Adsorption equilibrium modeling for water on activated carbons Nan Qi, M. Douglas LeVan * ...

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Carbon 43 (2005) 2258–2263 www.elsevier.com/locate/carbon

Adsorption equilibrium modeling for water on activated carbons Nan Qi, M. Douglas LeVan

*

Department of Chemical Engineering, Vanderbilt University, VU Station B #351604, 2301 Vanderbilt Place, Nashville, TN 37235, USA Received 12 May 2004; accepted 30 March 2005 Available online 17 May 2005

Abstract A new equation for describing adsorption equilibria of water on activated carbon is developed based on a mechanism proposed by Dubinin. It is HenryÕs law consistent, mathematically simple, and explicit in pressure. The model describes the full range of the adsorption isotherm with high accuracy using only a small number of parameters. Adsorption equilibrium data for water on several activated carbons quite different in surface area, surface chemical properties, and pore structure are used to test the model. A twovariable series expansion is used to extend a single adsorption isotherm to an adsorption isotherm family at multiple temperatures. The model description of pure water adsorption isotherms at different temperatures on BPL activated carbon is in good agreement with experimental data.  2005 Elsevier Ltd. All rights reserved. Keywords: Activated carbon; Adsorption; Modeling; Adsorption properties; Surface oxygen complexes; Water

1. Introduction Water vapor adsorption equilibria have been measured on different kinds of porous adsorbents [1–6] and on carbons with different degrees of surface oxidation [7,8]. Unlike organic adsorption on a microporous carbonaceous adsorbent, for which the isotherm shows type I behavior according to the classification of Brunauer et al. [9], water adsorption isotherms show type IV behavior on carbons with a highly oxidized surface, or type V behavior (S-shaped) on carbons with a strongly hydrophobic surface. Generally, water adsorption exhibits hysteresis on porous media. Different theories try to explain and model water vapor adsorption equilibrium. DubininÕs [10] water adsorption mechanism is a commonly accepted one. Dispersion interactions between water molecules and the carbon surface are negligibly weak while hydrogen *

Corresponding author. Tel.: +1 6153222441; fax: +1 6153437951. E-mail address: [email protected] (M.D. LeVan). URL: www.vuse.vanderbilt.edu/~cheinfo/levan.htm (M.D. LeVan).

0008-6223/$ - see front matter  2005 Elsevier Ltd. All rights reserved. doi:10.1016/j.carbon.2005.03.040

bonds play a more significant role. Oxygen complexes on the adsorbent surface act as the primary sites for water molecules to be adsorbed by hydrogen bonding. The adsorbed water molecules supply secondary sites for more water vapor molecules to be adsorbed via hydrogen bonds. As more and more water molecules are adsorbed, clusters are formed. Heat released during water adsorption is close to the heat of condensation, which is approximately 45 kJ/mol. Water adsorption hysteresis occurs predominantly because of the porous structure of the adsorbent and can be explained as the coalescence of water clusters on the adsorption branch and evaporation of capillary condensed water on the desorption branch [11]. The hysteresis loop vanishes, giving a closed single S-shape isotherm, for water adsorbed on nonporous carbon black [10]. Based on DubininÕs water adsorption mechanism, four water adsorption isotherm models have been developed from kinetic theory in a way similar to the classical development of the Langmuir isotherm. They are the DS-1 [10], DS-2 [12], DS-3 [13], and DS-4 [14] equations.

N. Qi, M.D. LeVan / Carbon 43 (2005) 2258–2263

n ¼ n0 cpr =ð1  cpr Þ

ðDS  1Þ

ð1Þ

n ¼ cpr ðn0 þ nÞð1  jnÞ ðDS  2Þ

ð2Þ

n ¼ pr ðcjn3  cjn0 n2 þ cnÞ ðDS  3Þ n h  io 2 n ¼ pr cn0 þ cn 1  exp j2 ðn  nc Þ

ð3Þ ðDS  4Þ ð4Þ

where n, pr, c, n0, j and nc are, respectively, the loading (mol/kg), relative pressure (p/psat), kinetic constant, concentration of primary sites, constant for decrease in number of adsorption sites, and parameter initiating the decline in adsorptive power [14]. The DS-1 equation normally gives only a fair description at low relative pressures (e.g., pr < 0.5 for BPL carbon at 25 C [13]) and fails at higher relative pressures. Different empirical factors have been introduced to account for the decrease of available adsorption sites as (1  jn) for DS-2, (1  jn2) for DS-3 and [1  exp(j2(n  nc)2)] for the DS-4 equation. The data correlations are improved such that DS-3 is more accurate than DS-2, and DS-4 is the most accurate among the series of the four equations. Sircar developed a general model for type I, IV, and V isotherms on porous carbons [15,16]. The amount adsorbed is determined through the pore filling mechanism in micropores and through both physical adsorption and capillary condensation in macropores. A full range pore size distribution is used to account for pore structure heterogeneity. Water adsorption on sugar charcoal are fit nicely by SircarÕs model [16]. Although the model is explicit, it involves complicated procedures to evaluate a gamma function and seven parameters. Talu and Meunier [17] developed a thermodynamic model for type V behavior by treating cluster formation as a series of chemical reactions for self-associating molecules. Water adsorption on activated carbons was described with a good fit at ambient temperature with 3 parameters and at multiple temperatures with 5 parameters. All parameters are physically significant. Do and Do [18] proposed a model to describe both type IV and type V isotherms for water on different carbons. Water molecules form clusters around functional groups. In their model, a cluster of 5 molecules can penetrate into a micropore as adsorbed water. Capillary condensation was evaluated using the Kelvin equation in mesopores as water vapor approaches the saturation pressure. The model gives very good descriptions for some water adsorption isotherms. Mahle [19] derived an equation for a type V isotherm by describing capillary condensation with the Kelvin equation and integrating over a pore size distribution. The model successfully describes water adsorption equilibria on activated carbon for both adsorption and desorption branches. It can be written explicitly in terms of either pressure or loading.

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Stoeckli [20] expressed water adsortion equilibria by combining a type I and a type V isotherm, both described by the Dubinin–Astakhov (D–A) equation. The method has had success in correlating some data. However, a thermodynamic concern with this approach is that the D–A equation does not follow HenryÕs law at low loadings. Cooperative multi-molecular sorption theory was used by Rutherford [21] to describe water adsorption isotherms. The model works well below 80% relative pressure. It is not valid above 80% relative pressure where capillary condensation and hysteresis occur. Describing water adsorption equilibrium with high accuracy is important, especially in modeling multi-component adsorption equilibrium, in which accurate pure component adsorption isotherms are required. A simple and explicit adsorption isotherm model is highly desirable in order to increase computation speed in fixedbed simulation and other applications where extensive iterations and calculations are performed. In this paper, we develop an equation to describe water adsorption equilibrium on activated carbon. It obeys HenryÕs law at low loadings and describes the full range of the adsorption isotherm with high accuracy using a small number of parameters. The model is mathematically simple and explicit in pressure. Adsorption equilibrium data for water on BPL, PVDC, UO3-1, NC100, polymeric type E, and ACF activated carbons are used to test the model. We also extend a single adsorption isotherm at one temperature to an adsorption isotherm family at multiple temperatures with very few parameters by using a two-variable Taylor series expansion. An example is given for developing water adsorption isotherms over a wide range of temperatures on BPL activated carbon.

2. Theory 2.1. Adsorption equilibrium of water on activated carbons Similar to the DS equation series [10,12–14], water adsorption on the microscale is depicted as a set of chemical reactions following the mechanism of Dubinin [10], i.e. k1

SþR ! SþA k2

AþR ! AþA k3

ð5Þ ð6Þ

ð7Þ A ! R where S symbolizes a primary adsorption site given by a surface oxygen complex; R symbolizes a water vapor molecule; A symbolizes an adsorbed water molecule and the secondary site it supplies; and k1, k2 and k3 are rate constants. Note that according to this mechanism,

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when a water molecule is adsorbed, a site is not removed, but another (secondary) site is supplied. Adsorption equilibrium on the macroscale is taken to be analogous to reaction equilibrium, where the total water adsorption rate on both primary and secondary sites is equal to the water desorption rate from the secondary sites. Thus, we have k 1 n0 pG1 þ k 2 npG2 ¼ k 3 n

ð8Þ

where n is the water loading; p is the water pressure in the vapor phase; and n0 is the concentration of primary sites. G1 and G2 are factors to express the macroscopic decreases in primary adsorption sites and secondary adsorption sites, respectively, as the loading increases and water fills the pore structure of the carbon. Rearranging Eq. (8) gives n p¼ ð9Þ ðk 1 =k 3 Þn0 G1 þ ðk 2 =k 3 ÞnG2 or p¼

n b0 G1 þ b1 nG2

ð10Þ

with b0 ¼ k 1 n0 =k 3

ð11Þ

b1 ¼ k 2 =k 3

ð12Þ

Two empirical and flexible functional relations proposed here to describe how G1 and G2 change with water loading are G 1 ¼ 1  b1 n  b 2 n 2  b 3 n 3    

ð13Þ

G 2 ¼ 1  c 1 n  c 2 n2    

ð14Þ

where b and c are constants related to oxygen complexation and the pore size distribution, respectively. Substituting Eqs. (13) and (14) into Eq. (10) gives p¼

n b0 þ ðb0 b1 þ b1 Þn þ ðb0 b2  b1 c1 Þn2 þ ðb0 b3  b1 c2 Þn3 þ 

ð15Þ

or, with further simplification, n p¼ n0 þ n1 n þ n2 n2 þ n3 n3 þ   

ð16Þ

where n0 ¼ b0

ð17Þ

n1 ¼ b0 b1 þ b1

ð18Þ

ni ¼ b0 bi  b1 ci1

ði P 2Þ

ð19Þ

Eq. (16) is the equation used here to describe water adsorption isotherms on activated carbon. Values of n are only functions of system characteristic values (e.g., b0, b1, b, and c) and are constants for a specific adsorbate–adsorbent pair.

If molecules are independently exploring a surface without interacting with one another, then the system will be in the HenryÕs law region, irrespective of whether the surface is homogeneous or heterogeneous. The fraction of the time each molecule is associated with the surface will be proportional to the adsorbed-phase concentration, and the fraction of the time the molecule is not associate with the surface is proportional to the fluid-phase concentration. Eq. (16) obeys HenryÕs law at low loadings. n0 is the HenryÕs law constant and signifies the adsorption affinity of water molecules for the primary sites. The model reduces to mathematical formulas equivalent to the DS-1 and DS-2 models as the polynomial denominator is truncated after n1n and n2n2 terms, respectively. 2.2. Multi-temperature extension A general method based on a series expansion is used here to develop a family of isotherms at different temperatures from a known isotherm at one temperature by examining an important property—the isosteric heat of adsorption, qst, as given by the Clausius–Clapeyron type equation  o ln p qst ¼ Rg T 2 ð20Þ oT  n

where T, p, and Rg are the temperature, pressure, and gas constant. If qst is constant, the result of integrating Eq. (20) is well known (e.g., [22]). However, as observed in experiments over a wide temperature and loading range, qst is not a constant, but a function of temperature and loading. Before investigating this relationship, we recall the two-variable Taylor series expansion about a reference point (x0, y0) f ðx; yÞ ¼ f ðx0 ; y 0 Þ þ fx0 ðx  x0 Þ þ fy0 ðy  y 0 Þ 1h 0 2 f ðx  x0 Þ þ 2fxy0 ðx  x0 Þðy  y 0 Þ þ 2! xx i 2 þfyy0 ðy  y 0 Þ þ   

ð21Þ

where fx0 and fy0 are first-order partial derivatives, and fxx0 , fxy0 and fyy0 are second-order partial derivatives, all evaluated at the reference point (x0, y0). Rearranging Eq. (21) gives 1 f ðx; yÞ ¼ f ðx0 ; y 0 Þ  fx0 x0  fy0 y 0 þ fxx0 x20 2 1 0 2 0 0 þ fxy x0 y 0 þ fyy y 0 þ ðfx  fxx0 x0  fxy0 y 0 Þx 2 1 1 0 0 þ ðfy  fyy y 0  fxy0 x0 Þy þ fxx0 x2 þ fyy0 y 2 2 2 þ fxy0 xy þ   

ð22Þ

or f ðx; yÞ ¼ d0 þ d1 x þ d2 y þ d3 x2 þ d4 y 2 þ d5 xy þ   

ð23Þ

N. Qi, M.D. LeVan / Carbon 43 (2005) 2258–2263

where d0 signifies the six leading terms on the right side of Eq. (22) and the remaining values of d correspond one to one in order with the remaining terms of Eq. (22). Values of d depend on the reference point selected and are independent of x and y. Thus, the isosteric heat of adsorption as a function of temperature and loading can be expressed as   1 1 1 1 st q n; ¼ d 0 þ d1 n þ d2 þ d3 n2 þ d4 2 þ d5 n þ    T T T T ð24Þ For a Taylor series truncated at first-order, substituting Eq. (24) with only the first three terms on the right side into Eq. (20), and integrating at constant n gives ln p ¼

d0 þ d1 n d2 þ þ g ð nÞ Rg T 2Rg T 2

ð25Þ

where g(n) is a temperature independent function of n. With a reference adsorption isotherm at a particular temperature Tref, given by pref = pref(n, Tref), the adsorption isotherm at any other temperature T can be obtained from      d0 þ d1 n 1 1 d2 1 1  þ p ¼ pref ðn;T ref Þexp  Rg T T ref 2Rg T 2 T 2ref ð26Þ

where the d parameters are constants independent of temperature and loading. Note that Eq. (26) incorporates the well known form for a constant qst given only by the term involving d0. The terms involving d1 and d2 extend this to allow for some dependence of qst on loading and temperature. Additional terms can be easily added.

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determined by performing a nonlinear least-squares regression on experimental data with the objective function, e, defined as M  2 X e¼ prexp;i  prcal;i ð27Þ i¼1

where M is the total number of data points, and prexp;i and prcal;i are relative pressures measured experimentally and calculated by the model, respectively. The average percentage deviation, , was calculated as an index for model fitting quality using  M  r p  prcal;i  1 X  exp;i   100 ¼ ð28Þ  M i¼1  prexp;i Water adsorption isotherms and model descriptions are shown in Fig. 1 for BPL, PVDC, and UO3-1 activated carbons and in Fig. 2 for NC100, polymeric type E, and ACF activated carbons. The equilibrium data points for polymeric type E system are representations of original experiment results, which contain many more points [5]. The model depicts HenryÕs law behavior at low loadings accurately and describes the full range of the isotherms very well. The model gives successful portrayals for water adsorption on various activated carbons with quite different pore and surface structures using a small number of parameters. The model parameters and the average percentage deviations are given in Tables 1 and 2. Higher values of n0, the HenryÕs law constants, for the BPL and PVDC systems compared to the UO3-1 system reveal that the surfaces of BPL and PVDC are more oxidized on a per weight basis, which gives a higher affinity for the water molecules.

30

3. Results and discussion

BPL (25°C) 25

3.1. Water adsorption on various activated carbons

20 n (mol/kg)

Six sets of adsorption equilibrium data for water on various activated carbons with large differences in surface area, pore size distribution, and surface chemical composition were chosen to test the proposed model. These water/carbon equilibrium data were measured on BPL at 25 C by Rudisill et al. [1], PVDC at 20 C by Bradley and Rand [2], UO3-1 at 20 C by Kraehenbuehl et al. [3], NC100 at 25 C by Cossarutto et al. [4], polymeric type E at 25 C by Terzyk et al. [5], and ACF at 100 C by Kaneko et al. [6]. Shapes of the isotherms differ greatly in adsorption characteristics such as the slope in the HenryÕs law region, the pressure and sharpness of the rise for filling of the micropores, and the saturation loading. The proposed model given by Eq. (16) was used to analyze all experimental data. The n parameters were

PVDC (20°C) UO3-1 (20°C) Model

15

10

5

0 0.0

0.2

0.4

0.6

0.8

1.0

pr Fig. 1. Water vapor isotherms for activated carbons: BPL, PVDC and UO3-1.

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30

25

n (mol/kg)

20

NC100 (25°C) Polymeric Type E (25°C) ACF (100°C) Model

15

10

5

0 0.0

0.2

0.4

0.6

0.8

1.0

pr Fig. 2. Water vapor isotherms for activated carbons: NC100, polymeric type E and ACF.

Table 1 Model parameters for water vapor adsorption on activated carbons: BPL, PVDC and UO3-1

n0 n1 n2 n3 n4 

BPL (25 C)

PVDC (20 C)

UO3-1 (20 C)

BPL (75 C)

1.780 0.1370 0.04559 1.866 · 103

4.308 0.2079 0.08219 2.640 · 103

0.1343 0.7161 0.01541 8.848 · 104 2.474 · 105 0.91

0.03227 0.03856 5.157 · 104 5.056 · 105

1.1

6.7

The water adsorption isotherm on BPL at 75 C was chosen as the reference isotherm. The proposed equilibrium model, Eq. (16), was fitted to this reference isotherm as shown by the solid curve in Fig. 3. The model gives excellent description of the experimental data. Model parameters and the average percentage deviation for the reference isotherm description are listed in Table 1. With the reference isotherm at 75 C known in pressure explicit form pref(n, Tref), the multi-temperature model of Eq. (26) with the Taylor series truncated after the first-order terms was applied to the water adsorption equilibrium data measured at 25 C, 50 C, 100 C, and 125 C. The result is shown by the dashed curves in Fig. 3. It can be seen that the proposed multi-temperature model describes the experimental data satisfactorily over this wide range of temperatures and loadings. The proposed multi-temperature model with the Taylor series truncated at higher orders, e.g., the secondorder (using five parameters), was used to analyze the same data in order to study model efficiency. No substantial improvement in model description accuracy was observed by the addition of more parameters. The model with the Taylor series truncated at the first-order using only three parameters (d0 = 3.618 · 104, d1 = 9.876 · 101 and d2 = 3.335 · 106) gives good precision in data correlation ( = 12).

24 0.64

22 20 18

Table 2 Model parameters for water vapor adsorption on activated carbons: NC100, polymeric type E and ACF Polymeric type E (25 C)

ACF (100 C)

1.363 0.1786 0.02647 8.025 · 104

1.361 1.257 0.1814 0.01865 6.231 · 104 7.5

0.02364 0.01518 9.415 · 104 5.388 · 105

11

1.9

n (mol/kg)

n0 n1 n2 n3 n4 

NC100 (25 C)

16 14

25°C 50°C 75°C 100°C 125°C Model,Tref Model,T

12 10 8 6 4

3.2. Multi-temperature water adsorption on BPL carbon Water adsorption equilibrium data on BPL activated carbon at 25 C, 50 C, 75 C, 100 C, and 125 C, measured by Rudisill et al. [1], were used to demonstrate the performance of the proposed multi-temperature model. The d parameters were determined by nonlinear regression [23]. The average percentage deviation, , was calculated using Eq. (28).

2 0 0.0

0.2

0.4

0.6

0.8

1.0

1.2

1.4

1.6

pr Fig. 3. Water vapor isotherms on BPL activated carbon. For clarity, pr, relative pressures (p/psat), for each isotherm are shifted by 0.1 consecutively from the 25 C isotherm. The solid curve is the model description of the Tref = 75 C reference isotherm. Dashed curves are model descriptions at other temperatures.

N. Qi, M.D. LeVan / Carbon 43 (2005) 2258–2263

4. Conclusions A new equation has been developed to describe water adsorption equilibria on activated carbon. The model is consistent with HenryÕs law at low loading, is mathematically simple, and is explicit in pressure. It depicts the full range of isotherms with high accuracy using a small number of parameters. The model was used to analyze water adsorption equilibrium data on BPL, PVDC, UO3-1, NC100, polymeric type E, and ACF activated carbons, which have large differences in surface area, surface chemical properties, and pore structure. A new versatile model has been proposed to generate adsorption isotherms at other temperatures from a reference isotherm known at a specific temperature. The model description of the multi-temperature water adsorption equilibria on BPL activated carbon is in good agreement with experimental data using very few parameters. Acknowledgement We are grateful to the National Aeronautics and Space Administration for the support of this research under award NCC2-1127.

[6]

[7]

[8]

[9]

[10] [11] [12] [13] [14]

[15] [16] [17]

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