Co-reporter:Xiangyang Liu;Waheed Afzal
Industrial & Engineering Chemistry Research October 23, 2013 Volume 52(Issue 42) pp:14975-14978
Publication Date(Web):Publication Date (Web): September 20, 2013
DOI:10.1021/ie402196m
Experimental solubilities are reported for methane, ethane, ethylene, and propane in ionic liquid tetrabutylphosphonium bis(2,4,4-trimethylpentyl) phosphinate [P4444][TMPP] from 313 K to 353 K up to 5 MPa. [P4444][TMPP] shows solubilities for methane, ethane, ethylene, and propane that are appreciably larger than those in other typical ionic liquids. However, unlike a hydrocarbon solvent, [P4444][TMPP] is not flammable at ordinary conditions. Unlike other typical ionic liquids, the solubility for ethane is larger than that for ethylene. Because the viscosity of [P4444][TMPP] is high, we consider a low-viscosity diluent. Therefore, experimental solubilities are also reported for the same solutes in 1-ethyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide, [EMIM][Tf2N] from 299 K to 354 K up to 4 MPa. Comparison between our results and literature data shows good agreement.
Co-reporter:Fuxin Yang, Zhongguo Liu, Waheed Afzal, Zhigang Liu, Alexis T. Bell, and John M. Prausnitz
Energy & Fuels 2015 Volume 29(Issue 3) pp:1743-1750
Publication Date(Web):February 10, 2015
DOI:10.1021/ef502517d
To make biomass more accessible for enzymatic hydrolysis, lime pretreatment of Miscanthus giganteus with oxidants was explored from 100 to 150 °C. Composition data for the recovered solid were obtained to determine the effects of the reaction time, lime dosage, oxidant loading, and temperature on sugar production efficiency. Under selected conditions (0.2 g of lime/g of biomass, 200 psig O2, and 150 °C for 1 h), delignification was 64.7%. The pretreated biomass was then followed by enzymatic hydrolysis. The yield of cellulose in the recovered solid to glucose was 91.7% and hemicellulose to xylose was 67.3%, 7.1 and 18.2 times larger than those obtained from raw biomass, respectively. Pretreatment with oxidants substantially raised delignification of raw M. giganteus, thereby enhancing enzymatic hydrolysis to sugars, while results were not improved when pretreatment included ammonium molybdate.
Co-reporter:Waheed Afzal, Xiangyang Liu, John M. Prausnitz
Fluid Phase Equilibria 2015 Volume 404() pp:124-130
Publication Date(Web):25 October 2015
DOI:10.1016/j.fluid.2015.06.037
Ionic liquids provide a possible absorption process to extract krypton from air. The feed for such a process is an oxygen stream from a liquid-air plant. An effective ionic liquid is [P(14)666][TMPP]; in that solvent, the solubilities of some pertinent common gases are appreciably larger than those in conventional ionic liquids, and the selectivity Kr/O2 is close to 3. A nonvolatile ionic liquid is preferred over a hydrocarbon solvent because of safety and simpler solvent recovery. Because, the viscosity of [P(14)666][TMPP] is very high, 20 wt.% [BHMIM][AC] is added to reduce the viscosity by one order of magnitude without significantly reducing solvent capacity and selectivity. This work provides extensive fundamental data (solubility, density and viscosity) required for process design.
Co-reporter:Fuxin Yang;Waheed Afzal;Kun Cheng;Nian Liu
Biotechnology and Bioprocess Engineering 2015 Volume 20( Issue 2) pp:304-314
Publication Date(Web):2015 April
DOI:10.1007/s12257-014-0658-4
Miscanthus giganteus (M. giganteus) is a promising feedstock for the production of bioethanol or biochemicals. Using only dilute nitric acid, this work describes a two-step process for hydrolyzing hemicellulose and cellulose to fermentable sugars. Primary variables were temperature and reaction time. The solid-to-liquid mass ratio was 1:8. No enzymes were used. In the first step, M. giganteus was contacted with 0.5 wt.% nitric acid at temperatures between 120 and 160°C for 5 to 40 min. The second step used 0.5 or 0.75 wt.% nitric acid at temperatures between 180 and 210°C for less than 6 min. Under selected conditions, almost all hemicellulose and 58% cellulose were transferred to the liquid phase. Small amounts of degradation products were observed. The xylose solution obtained from the nitric-acid hydrolysis was fermented for 96 h and the glucose solution for 48 h to yield 0.41 g ethanol/g xylose and 0.46 g ethanol/g glucose. To characterize residual solids and the liquor from both steps, nuclear-magneticresonance (NMR) spectroscopy was performed for each fraction. The analytical data indicate that the liquid phase from Steps 1 and 2 contain little lignin or lignin derivatives.
Co-reporter:Xiangyang Liu, Elia Ruiz, Waheed Afzal, Víctor Ferro, José Palomar, and John M. Prausnitz
Industrial & Engineering Chemistry Research 2014 Volume 53(Issue 1) pp:363-368
Publication Date(Web):2017-2-22
DOI:10.1021/ie402677t
Solubilities are reported for methane, ethane, ethylene, and propane in trimethyloctylphosphonium bis(2,4,4-trimethylpentyl) phosphinate [P8111][TMPP] from 299 to 323 K up to 4 MPa. Consistent with prediction of COSMO-RS, [P8111][TMPP] shows large solubilities for all four hydrocarbons. Contrary to solubility data in conventional ionic liquids, in [P8111][TMPP] the solubility for ethane is higher than that for ethylene. When compared with solubilities in other similar phosphonium-based ionic liquids, the cation has only a small influence on the solubilities of small hydrocarbons. Ionic liquid [P8111][TMPP] may be useful for storage or separation of small hydrocarbons.
Co-reporter:Guangren Yu;Waheed Afzal;Fuxin Yang;Sasisanker Padmanabhan;Zhongguo Liu;Hongxue Xie;Mahmoud Abdel Shafy;Alexis T. Bell
Journal of Chemical Technology and Biotechnology 2014 Volume 89( Issue 5) pp:698-706
Publication Date(Web):
DOI:10.1002/jctb.4172
Abstract
BACKGROUND
Miscanthus×giganteus (M.×giganteus) is a potential source for bioethanol or other useful products. Pretreatment of lignocellulosic biomass is an essential step prior to enzymatic hydrolysis to sugars and fermentation to bioethanol.
RESULTS
In this work, a one-step process uses aqueous ammonia with or without hydrogen peroxide; a proposed two-step process uses aqueous ammonia in the first step and hydrogen peroxide in the second step. In the two-step process, overall 89.5% lignin is removed. The pretreated biomass is followed by using cellulase and β-glucosidase to convert cellulose and hemicellulose from the recovered solid to fermentable sugars. The conversion of cellulose to glucose is 90.2% and to xylose is 73.4%. Characterization data are obtained for the recovered solid using scanning electron microscopy (SEM), attenuated total reflection-infrared spectroscopy (ATR-IR), and X-ray diffraction (XRD) for better understanding of the two-step process.
CONCLUSION
Results from the two-step process using aqueous ammonia and hydrogen peroxide separately are much better than those from the one-step process for removing lignin and for enhancing conversion to sugars by enzymatic hydrolysis. © 2013 Society of Chemical Industry
Co-reporter:Waheed Afzal, Xiangyang Liu, and John M. Prausnitz
Journal of Chemical & Engineering Data 2014 Volume 59(Issue 4) pp:954-960
Publication Date(Web):February 21, 2014
DOI:10.1021/je400655j
Experimental solubilities are reported for carbon dioxide in four ionic liquids: trihexyl tetradecylphosphonium bis(2,4,4-trimethylpentyl) phosphinate [P(14)666][TMPP], tetrabutylphosphonium bis(2,4,4-trimethylpentyl) phosphinate [P4444][TMPP], trimethyloctylphosphonium bis(2,4,4-trimethylpentyl) phosphinate [P8111][TMPP], and trihexyl tetradecylphosphonium dicyanamide [P(14)666][DCA] from 298 K to 334 K up to 4 MPa. Tetraalkyl phosphonium bis(2,4,4-trimethylpentyl) phosphinate ionic liquids show solubilities for carbon dioxide higher than those in other ionic liquids. In these phosphonium-based ionic liquids, the anion appears to have a larger influence on carbon-dioxide solubility than the cation. Water or 1-butyl-3-H-imidazolium acetate ([BHMIM][AC]) are used as diluents to reduce the large viscosity of [P(14)666][TMPP]. Viscosities are reported for mixtures of [P(14)666][TMPP] with varying content of water or [BHMIM][AC] from 298 K to 343 K at atmospheric pressure. Solubilities for carbon dioxide are reported in mixtures of [P(14)666][TMPP] with varying content of water or [BHMIM][AC] from 298 K to 323 K up to 4 MPa. These diluents very much reduce the viscosity. The addition of [BHMIM][AC] does not seriously lower the solubility of carbon dioxide.
Co-reporter:Xiangyang Liu, Waheed Afzal, Guangren Yu, Maogang He, and John M. Prausnitz
The Journal of Physical Chemistry B 2013 Volume 117(Issue 36) pp:10534-10539
Publication Date(Web):August 15, 2013
DOI:10.1021/jp403460a
Experimental solubilities are reported for methane, ethane, ethylene, propane, and propylene in trihexyl tetradecylphosphonium bis(2,4,4-trimethylpentyl) phosphinate [P(14)666][TMPP] from 313 to 353 K up to 6.7 MPa. A literature review on solubilities of small hydrocarbons in ionic liquids shows that solubilities in [P(14)666][TMPP] are appreciably larger than those in other ionic liquids. Contrary to solubilities in ionic liquids studied earlier, solubilities of paraffins (ethane and propane) in [P(14)666][TMPP] are larger than those of the corresponding olefins (ethylene and propylene). Because, at fixed temperature, the vapor pressure of an olefin is larger than that of the corresponding paraffin, the relative volatility of the olefin exceeds that of the corresponding paraffin, contrary to the relative volatility observed in conventional extractive distillation with polar solvents where the volatility of the paraffin exceeds that of the corresponding olefin.
Co-reporter:Waheed Afzal, Brian Yoo, and John M. Prausnitz
Industrial & Engineering Chemistry Research 2012 Volume 51(Issue 11) pp:4433-4439
Publication Date(Web):January 27, 2012
DOI:10.1021/ie202280y
The inert-gas stripping method is useful for rapidly measuring solubilities of moderately and sparingly soluble gases in liquids. Earlier versions of this method can give only solubilities of volatile-liquid solutes in low-volatile solvents. However, the modifications presented here enable measurement of very low solubilities of gases in liquids. Henry’s constants are reported for carbon dioxide, krypton, oxygen, air, and nitrogen in n-dodecane and n-pentadecane, and for carbon dioxide in ethylene glycol at near-ambient conditions. The new Henry’s constants compare well with those in the literature. Henry’s constants are reported for carbon dioxide, ethane, ethylene, krypton, oxygen, air, and nitrogen at near-ambient conditions in the protic ionic liquid 1-butyl, 3-hydrogen-imidazolium acetate; we select this protic ionic liquid because, relative to other ionic liquids, it has low viscosity and because solubility data in protic ionic liquids are rare.
Co-reporter:Brian Yoo, Waheed Afzal, and John M. Prausnitz
Industrial & Engineering Chemistry Research 2012 Volume 51(Issue 29) pp:9913
Publication Date(Web):June 18, 2012
DOI:10.1021/ie300588s
Solubility parameters are useful for estimating solubilities of solutes in ionic liquids when no solubility data are available. Solubility parameters are reported for nine ionic liquids; they were obtained from solubility data for a variety of solutes. The ionic liquids are 1-butyl,3-methylimidazolium hydrogen sulfate, 1-ethyl,3-methylimidazolium acetate, 1-methyl,3-trimethylsylilimidazolium chloride, 4-methyl,n-butylpyridinium tetrafluoroborate, ethylammonium nitrate, 1-ethyl,3-methylimidazolium bis(trifluoromethylsulfonyl)imide, 1-methyl,3-methylimidazolium bis(trifluoromethylsulfonyl)imide, 1-butyl,3-methylimidazolium bis(trifluoromethylsulfonyl)imide, and 1-ethyl,3-methylimidazolium ethylsulfate.
Co-reporter:Siddharth S. Dey and John M. Prausnitz
Industrial & Engineering Chemistry Research 2011 Volume 50(Issue 1) pp:3-15
Publication Date(Web):July 13, 2010
DOI:10.1021/ie1004916
Because of its generality, thermodynamics is applicable to all substances, including biomacromolecules. To illustrate how thermodynamics can contribute to biotechnology, each of six examples gives a brief summary of pertinent, previously published research. Each example indicates that familiar concepts in chemical engineering thermodynamics can be applied to contribute toward solution of a practical problem. These examples are discussed here to encourage thermodynamically oriented chemical engineers to devote their talents toward helping to advance industrial biotechnology.
Co-reporter:Sebastian Fendt, Sasisanker Padmanabhan, Harvey W. Blanch, and John M. Prausnitz
Journal of Chemical & Engineering Data 2011 Volume 56(Issue 1) pp:31-34
Publication Date(Web):December 17, 2010
DOI:10.1021/je1007235
For the temperature range (80 to 120) °C, viscosity data are reported for imidazolium-based ionic liquids 1-octyl-3-methylimidazolium chloride [Omim][Cl], 1-hexyl-3-methylimidazolium chloride [Hmim][Cl], 1-butyl-3-methylimidazolium chloride [Bmim][Cl], 1-ethyl-3-methylimidazolium chloride [Emim][Cl], 1-ethyl-3-methylimidazolium acetate [Emim][Ac], 1-butyl-3-methylimidazolium acetate [Bmim][Ac], and 1-butyl-3-methylimidazolium dicyanamide [Bmim] [N(CN)2]. Acetate-based ionic liquids have considerably lower viscosities than the corresponding chloride-based ILs. At 25 °C, viscosity data are reported for binary mixtures of [Bmim][Ac] with diluents water, acetonitrile, dimethylformamide (DMF), and ethylene glycol. Even a small concentration of diluent very much reduces the viscosity of an ionic liquid.
Co-reporter:Qin Xin, Geoffrey G. Poon, John M. Prausnitz
The Journal of Supercritical Fluids 2010 Volume 55(Issue 2) pp:817-824
Publication Date(Web):December 2010
DOI:10.1016/j.supflu.2010.09.043
Following some simplifications to reduce the computational effort, the Percus–Yevick–van der Waals equation of state is used to calculate the isothermal total pressure of a binary liquid system containing one volatile nonelectrolyte liquid and one nonvolatile ionic liquid. Pure-component parameters a and b are found from pure-component enthalpy-of-vaporization and liquid-density data. The single binary parameter a12 is obtained from Henry's constant for the nonelectrolyte in the ionic liquid. For 10 binary systems, calculated total pressures are in good agreement with experiment although in a few systems observed total pressures are slightly higher than those calculated in the region where the ionic liquid is dilute. Brief attention is given to a few binary systems with a miscibility gap.Graphical abstractResearch highlights▶ Used a simple Percus-Yevick-van der Waals equation of state for calculating VLE. ▶ Calculated total pressures are in good agreement with experimental data for binary systems containing one ionic liquid. ▶ One adjustable binary parameter is sufficient for most VLE calculations.
Co-reporter:Nicolas Papaiconomou, Jong-Min Lee, Justin Salminen, Moritz von Stosch and John M. Prausnitz
Industrial & Engineering Chemistry Research 2008 Volume 47(Issue 15) pp:5080
Publication Date(Web):September 12, 2007
DOI:10.1021/ie0706562
Extraction of dilute metal ions from water was performed near room temperature with a variety of ionic liquids. Distribution coefficients are reported for fourteen metal ions extracted with ionic liquids containing cations 1-octyl-4-methylpyridinium[4MOPYR]+, 1-methyl-1-octylpyrrolidinium[MOPYRRO]+, or 1-methyl-1-octylpiperidinium[MOPIP]+ and anions tetrafluoroborate[BF4]+, trifluoromethyl sulfonate[TfO]+, or nonafluorobutyl sulfonate[NfO]+. Ionic liquids containing octylpyridinium cations are good for extracting mercury ions. However, other metal ions were not significantly extracted by any of these ionic liquids. Extractions were also performed with four new task-specific ionic liquids. When these liquids contain a disulfide functional group, they are efficient and selective for mercury and copper, whereas those containing a nitrile functional group are efficient and selective for silver and palladium.
Co-reporter:Jianzhong Wu
PNAS 2008 Volume 105 (Issue 28 ) pp:9512-9515
Publication Date(Web):2008-07-15
DOI:10.1073/pnas.0802162105
Pairwise additivity of the hydrophobic effect is indicated by reliable experimental Henry's constants for a large number of
linear and branched low-molecular-weight alkanes in water. Pairwise additivity suggests that the hydrophobic effect is primarily
a local phenomenon and that the hydrophobic interaction may be represented by a semiempirical force field. By representing
the hydrophobic potential between two methane molecules as a linear function of the overlap volume of the hydration layers,
we find that the contact value of the hydrophobic potential (−0.72 kcal/mol) is smaller than that from quantum mechanics simulations
(−2.8 kcal/mol) but is close to that from classical molecular dynamics (−0.5∼−0.9 kcal/mol).
Co-reporter:G.T. Fukuda, P.F. Peterson, D.R. Olander, J.M. Prausnitz
Fluid Phase Equilibria 2007 Volume 255(Issue 1) pp:1-10
Publication Date(Web):1 July 2007
DOI:10.1016/j.fluid.2007.01.041
Molten mixtures of LiF, NaF, and BeF2 may be useful as a liquid first wall in a fusion-energy reactor. For design, it is necessary to know the thermodynamic properties of these mixtures, in particular, the total pressure as a function of temperature and composition. For successful application inside fusion chambers, the total pressure normally should be small, on the order of 0.1 Pa or less. This work presents a simple molecular-thermodynamic model based on the “chemical” theory of solutions with corrections for physical interactions. Parameters in this model are obtained from experimental binary and ternary data reported previously. The simple model, with only a few adjustable parameters, provides a good description of the thermodynamic properties for this system. For the temperature range 600–650 °° C at BeF2 mole fractions between 0.3 and 0.4, the total pressure is in the region 0.01–0.1 Pa.
Co-reporter:F. Fornasiero;C. Langel;J.M. Prausnitz;C.J. Radke;C. Weinmüller;C. Weinmüller;C. Langel;F. Fornasiero;C.J. Radke;J.M. Prausnitz
Journal of Biomedical Materials Research Part A 2006 Volume 77A(Issue 2) pp:230-241
Publication Date(Web):3 JAN 2006
DOI:10.1002/jbm.a.30598
A gravimetric-sorption technique was used to obtain kinetic and equilibrium adsorption/desorption data for water vapor in four different soft-contact-lens (SCL) polymers at 35°C. The SCL materials are a conventional hydrogel (polymacon) with a low water content at saturation (<50 wt %); two conventional hydrogels (hilafilcon A and alphafilcon A) with a high water content at saturation (>50 wt %); and a siloxane hydrogel (balafilcon A). Absorption and desorption equilibrium isotherms (water activity versus water weight fraction) overlap at high water contents, whereas significant hysteresis is observed at low water contents. The hysteresis loop is likely due to trapping of water in the polymer during the desorption process because of a rubber-to-glass transition of the SCL-film surfaces. Sorption data were interpreted using Flory–Rehner theory. The positive Zimm and Lundberg cluster function suggests that water tends to cluster in these SCL materials, except at very low water content. For polymacon and hilafilcon A, Fickian diffusion is observed for all activities for both water sorption and desorption. However, for alphafilcon A and balafilcon A, non-Fickian features appear at intermediate/low activities, in particular during water desorption, suggesting coupling of the diffusion process with polymer-matrix relaxation. The diffusion coefficient increases significantly with water concentration for polymacon and hilafilcon A (from ∼0.3 × 10−8 to 4.0 × 10−8 cm2/s) because of augmented mixture free volume induced by water sorption, whereas a more complex composition dependence is observed for alphafilcon A and balafilcon A probably as consequence of a combined effect of polymer relaxation, plasticization, and water clustering. © 2005 Wiley Periodicals, Inc. J Biomed Mater Res, 2006
Co-reporter:Bo Hyun Lee, Yuan Qin, John M. Prausnitz
Fluid Phase Equilibria 2006 Volume 240(Issue 1) pp:67-72
Publication Date(Web):10 February 2006
DOI:10.1016/j.fluid.2005.12.002
Common classical expressions for the molar excess Gibbs energy of mixing gE do not contain a contribution from composition fluctuations that are significant in the vicinity of the plait point for a ternary system. We propose a correction to gE based on reasonable phenomenological assumptions. This correction requires three ternary constants, but two are obtained from stability relations provided that we know the composition of the plait point. While the method proposed here is not predictive, it provides a consistent thermodynamic procedure for calculating the liquid–liquid phase diagram of a ternary system with a plait point. The proposed method is illustrated for three ternaries. When calculations are based on the classical expressions for gE alone, calculated results are in serious disagreement with experiment near critical conditions. Inclusion of the proposed correction for gE provides dramatic improvement.
Co-reporter:Francesco Fornasiero, Florian Krull, Clayton J. Radke, John M. Prausnitz
Fluid Phase Equilibria 2005 Volumes 228–229() pp:269-273
Publication Date(Web):February 2005
DOI:10.1016/j.fluid.2004.08.020
Using an evaporation-cell method, molecular diffusion data were obtained for water through a thin membrane of HEMA (2-hydroxyethyl methacrylate) that is a soft contact lens material. Water evaporates from the bottom surface of the membrane that supports a small water reservoir on the top surface. The so-induced chemical potential gradient causes a water flux across the membrane. Measured steady-state water fluxes are interpreted with an extended Maxwell–Stefan model for mixtures whose molecules differ appreciably in size. Flory–Rehner theory accounts for thermodynamic non-ideality of the hydrogel membrane/water mixture. Measured diffusivities are a strong increasing function of water concentration in the membrane.
Co-reporter:Francesco Fornasiero, Florian Krull, John M. Prausnitz, Clayton J. Radke
Biomaterials 2005 Volume 26(Issue 28) pp:5704-5716
Publication Date(Web):October 2005
DOI:10.1016/j.biomaterials.2005.02.028
Water transport through soft contact lenses (SCL) is important for acceptable performance on the human eye. Chemical-potential gradient-driven diffusion rates of water through SCL materials are measured with an evaporation-cell technique. Water is evaporated from the bottom surface of a lens membrane by impinging air at controlled flow rate and humidity. The resulting weight loss of a water reservoir covering the top surface of the contact-lens material is recorded as a function of time.New results are reported for a conventional hydrogel material (SofLens™ One Day, hilafilcon A, water content at saturation w10=70w10=70 weight %) and a silicone hydrogel material (PureVision™, balafilcon A, w10=36%w10=36%), with and without surface oxygen plasma treatment. Also, previously reported data for a conventional 2-hydroxyethyl methacrylate (HEMA)-SCL (w10=38%)(w10=38%) hydrogel are reexamined and compared with those for SofLens™ One Day and PureVision™ hydrogels. Measured steady-state water fluxes are largest for SofLens™ One Day, followed by PureVision™ and HEMA. In some cases, the measured steady-state water fluxes increase with rising relative air humidity. This increase, due to an apparent mass-transfer resistance at the surface (trapping skinning), is associated with formation of a glassy skin at the air/membrane interface when the relative humidity is below 55–75%.Steady-state water fluxes are interpreted through an extended Maxwell–Stefan diffusion model for a mixture of species starkly different in size. Thermodynamic nonideality is considered through Flory–Rehner polymer-solution theory. Shrinking/swelling is self-consistently modeled by conservation of the total polymer mass. Fitted Maxwell–Stefan diffusivities increase significantly with water concentration in the contact lens.
Co-reporter:Alberto Arce, Francesco Fornasiero, Oscar Rodríguez, Clayton J. Radke and John M. Prausnitz
Physical Chemistry Chemical Physics 2004 vol. 6(Issue 1) pp:103-108
Publication Date(Web):27 Nov 2003
DOI:10.1039/B307996A
Using a gravimetric technique, experimental data at 35°C are reported for isothermal sorption equilibria and sorption kinetics of water vapor in poly(N,N-dimethyl methacrylamide)
(PDMAA), poly(2-dimethyl aminoethyl methacrylate)
(PDMAEMA), poly(acrylic acid)
(PAA), and in a typical membrane of a commercial soft-contact lens made of poly(2-hydroxyethyl methacrylate)
(PHEMA). The highest sorption of water vapor is in PDMAA. The Flory–Huggins model and the Zimm–Lundberg clustering theory are used to interpret the equilibrium data. Over the entire range of water activity, the four materials show clustering functions larger than −1 indicating that water molecules cluster together in the polymers. The least hydrophilic polymer, PDMAEMA, and the most hydrophilic one, PDMAA, show respectively, the highest and the lowest tendency of water molecules to form clusters. Water diffusion into the polymer matrix is faster in PDMAEMA (diffusion coefficient, D=10–20×10−8 cm2 s−1) and in PDMAA (D=4.9–8.7×10−8 cm2 s−1) than in PHEMA-lens material (D=0.55–3.4×10−8 cm2 s−1) and PAA (D=0.98–3.5×10−8 cm2 s−1). The measured diffusion coefficients increase with water activity in the PHEMA-lens, decrease with activity in PDMAEMA, and show a more complex concentration dependence in PDMAA and PAA. By writing the diffusion coefficient as a product of an intrinsic mobility, Đ, and a non-ideality thermodynamic factor, Γ, the concentration dependence of D is explained by the interplay of two factors: rising plasticization with water activity, which causes an increase in Đ, and the effect of composition on Γ, decreasing with water activity.
Co-reporter:Christopher A. Teske, Harvey W. Blanch, John M. Prausnitz
Fluid Phase Equilibria 2004 Volume 219(Issue 2) pp:139-148
Publication Date(Web):28 May 2004
DOI:10.1016/j.fluid.2004.01.025
A chromatographic method is used to measure ovalbumin-lysozyme and BSA-lysozyme interactions in aqueous salt solutions as a function of solution conditions (pH, ionic strength, salt type). In this method, one protein is immobilized on the support surface, and the other, dissolved in a buffer/electrolyte solution, flows over that surface. The retention time provides a measure of immobile/mobile protein–protein interactions. Trends in ovalbumin-lysozyme interactions suggest that they are primarily electrostatic. The identity of the electrolyte has a strong influence on the magnitude of the interaction. Assuming a potential of mean force that contains a hard sphere, electrostatic, and square-well potential, experimental results are used to fit the square-well depth. For BSA-lysozyme interactions, the square-well depth depends on which protein is immobilized on the solid phase.
Co-reporter:Jun Cai, John M. Prausnitz
Fluid Phase Equilibria 2004 Volume 219(Issue 2) pp:205-217
Publication Date(Web):28 May 2004
DOI:10.1016/j.fluid.2004.01.033
To describe thermodynamic properties of fluid mixtures near to and far from the vapor–liquid critical point, we need a method where a classical equation-of-state is augmented with a correction based on renormalization group (RG) theory. The advantage of the method described here is that, subject to well-defined assumptions, it can be applied not only to binary mixtures but to mixtures containing any number of components. While our method is based on White’s recursion procedure, our extension to mixtures is based on the isomorphism assumption and on an approximation suggested by Kiselev. To illustrate, calculations are presented for the critical loci of some alkane mixtures containing one discrete component and one pseudo-component whose composition is characterized by a continuous distribution of molecular weight. While critical loci calculated with the RG correction are similar to those calculated by the classical equation-of-state alone, inclusion of the RG correction provides better agreement with experiment.
Co-reporter:A. Striolo, F. W. Tavares, D. Bratko, H. W. Blanch and J. M. Prausnitz
Physical Chemistry Chemical Physics 2003 vol. 5(Issue 21) pp:4851-4857
Publication Date(Web):29 Sep 2003
DOI:10.1039/B309975J
Molecular thermodynamics is used to calculate phase diagrams for aqueous charged dipolar colloids or globular proteins. Because normal pressures are not important for condensed systems, here a phase diagram is a plot of temperature versus colloid concentration. Properties of the fluid phase are obtained from the random-phase approximation, whereas those for the solid phase correspond to a perfect crystal. Crystal structures considered are face-centered and body-centered cubic. For each phase, the Helmholtz energy is determined by the sum of a hard-sphere reference term and a perturbation term that uses a potential of mean force for pairs of charged, dipolar colloids that also interact through dispersion forces. In view of different screening effects on charge–charge repulsion and dipolar attraction, the net electrostatic term features an extremum at intermediate ionic strengths leading to a non-monotonic dependence of the phase behavior on salt concentration. Illustrative phase diagrams are shown as a function of colloid charge, dipole moment, and ionic strength of the aqueous medium. Calculated results show that the phase diagram is sensitive to the structure assumed for the solid phase.
Co-reporter:Nicola Elvassore, John M. Prausnitz
Fluid Phase Equilibria 2002 Volumes 194–197() pp:567-577
Publication Date(Web):30 March 2002
DOI:10.1016/S0378-3812(01)00782-8
van der Waals perturbation theory is used to calculate fluid–solid phase diagrams for a system of perturbed-hard-sphere chains. In both fluid and solid phases, the free energy is the sum of a hard-sphere-chain term as the reference system, and a van der Waals term as the perturbation. The reference system for both phases follows from the Percus–Yevick integral theory coupled with Chiew’s results for hard chains. An analytic model for the solid-phase reference term of a hard-chain system agrees well with computer-simulation data for the solid hard-chain compressibility. Simulation data for fluid–solid coexistence curves for hard spheres, and for 4-mer hard chains, are used to fit the reference Helmholtz free energy of the solid phase. The pressure and solid and fluid densities at the hard-chain melting point, predicted by our model, fairly reproduce the available simulation data at different chain lengths.The attractive perturbation term follows from an inverse-power potential with variable exponent n for both fluid and solid phases. The theory here presented reproduces the simulated phase diagrams of chain-like molecules and gives the correct trend for experimental melting points of normal alkanes.
Co-reporter:F. Fornasiero;M. M. Olaya;B. Esprester;V. Nguyen;J. M. Prausnitz
Journal of Applied Polymer Science 2002 Volume 85(Issue 10) pp:2041-2052
Publication Date(Web):12 JUN 2002
DOI:10.1002/app.10804
Experimental results at 25°C are reported for infinite-dilution distribution coefficients for 19 nonvolatile solutes between aqueous solution and three kinds of polymer films, and for their diffusion coefficients in the polymer matrix. The experiments were performed by coupling UV spectroscopy and gravimetric measurements with mass balances. The solutes are aromatic nonvolatile compounds that are of interest in environmental technology and may serve as model compounds for drug-delivery systems. The polymers are ethylene-vinyl acetate copolymers with 33 (EVAc33) and 45 (EVAc45) weight percentage vinyl acetate, and poly(vinyl acetate) (PVAc) widely used in drug-delivery devices. For PVAc, a long time is required to reach equilibrium. Because the required time is too long for reasonable experimental studies, equilibrium distribution coefficients were calculated from finite-time data by using a diffusion model. The contribution of surface adsorption is shown to be negligible. Infinite-dilution distribution coefficients Ks, defined as the volume fraction of solute in the polymer divided by that in water, tend to increase with vinyl acetate content; they range from near unity to several hundred. Diffusion coefficients, determined from time-dependent sorption data, are significantly larger in EVAc copolymers (10−10 to 10−8 cm2/s) than in PVAc (10−12 cm2/s). These data may be useful for design of membrane processes, for controlled delivery of drugs, and for application in packaging and storage of food, chemicals, and pharmaceuticals. © 2002 Wiley Periodicals, Inc. J Appl Polym Sci 85: 2041–2052, 2002
Co-reporter:Alberto Striolo, Dusan Bratko, John M. Prausnitz, Nicola Elvassore, Alberto Bertucco
Fluid Phase Equilibria 2001 Volumes 183–184() pp:341-350
Publication Date(Web):1 July 2001
DOI:10.1016/S0378-3812(01)00446-0
Drug-loaded polymers and polymeric microparticles provide an attractive form for controlled drug-delivery systems. Design of new systems requires knowledge of polymer–drug interactions. The effect of polymer architecture and chemistry upon active-ingredient loading is investigated by Monte Carlo simulation. The ensemble-growth method is used to sample conformations of a model polymer comprising polar and nonpolar segments. The polymer is a block copolymer, linear or branched. In our calculations, the polar portion of the polymer contains 21 segments. The polymers are dissolved in either of two types of solvent models. In the first, nonpolar solvent, the polar segments tend to collapse, but the bulky nonpolar groups, easily soluble in the medium, create some cavities in the polymer. These cavities are suitable hosts for the slightly polar active ingredient. In the second solvent, polar, the nonpolar segments contribute to attract the active ingredient within the polymer segments, therefore lowering the burst-release rate. The relative uptake of the active ingredient, proportional to the probability of finding an active ingredient within the radius of gyration of the polymer, is computed as a function of the number of nonpolar segments in the polymer. Simulation results are reported for active ingredients of two different sizes. For given size of the polar portion, short nonpolar tails increase the active-ingredient relative uptake in both solvents considered. Linear block copolymers look promising for obtaining higher entrapment efficiency for the active ingredient and for controlled release.
Co-reporter:Y.U Moon, C.O Anderson, H.W Blanch, J.M Prausnitz
Fluid Phase Equilibria 2000 Volume 168(Issue 2) pp:229-239
Publication Date(Web):29 February 2000
DOI:10.1016/S0378-3812(99)00337-4
Experimental data at 25°C are reported for osmotic pressures of aqueous solutions containing lysozyme and any one of the following salts: ammonium sulfate, ammonium oxalate, and ammonium phosphate at ionic strength 1 or 3 M. Data were obtained using a Wescor colloid membrane osmometer at lysozyme concentrations from about 4 to 20 g/l at pH 4, 7, or 8. Osmotic second virial coefficients for lysozyme were calculated from the osmotic-pressure data. All coefficients were negative, increasing in magnitude with ionic strength. Results are insensitive to the nature of the anion, but rise slightly in magnitude as the size of the anion increases.
Co-reporter:Jun Cai, Ying Hu, John M. Prausnitz
Chemical Engineering Science (15 April 2010) Volume 65(Issue 8) pp:2443-2453
Publication Date(Web):15 April 2010
DOI:10.1016/j.ces.2009.11.024
Stability theory for multicomponent fluid mixtures is used to calculate the spinodal and the critical locus for a multicomponent mixture. Upon using well-defined simplifying assumptions, the criteria developed here are suitable for mixtures whose properties are described by a molecular-thermodynamic model where the Helmholtz energy depends on composition-average model parameters. Such mixtures are typically encountered in systems that contain homologues. Our method is especially useful when the homologue-mixture contains a large number of components. Different from our previous work (Fluid Phase Equilibria, 206, 41–59, 2003), the criteria developed here do not require that the model parameters depend on moments of a characteristic property (e.g. molecular weight) used to characterize the distribution of components. The spinodal lines and the critical points obtained by our method are identical to those obtained from the less-computer-efficient Gibbs traditional method. To illustrate, the Soave–Redlich–Kwong equation of state is used to calculate critical properties of mixtures containing carbon dioxide, hydrogen sulphide, and alkanes.