Effects of Methylcellulose on the Properties and Morphology of Polysulfone Membranes Prepared by Phase Inversion

Polymer solutions of polysulfone (PSf) and methylcellulose (MC) in 1-methyl-2-pyrrolidone (NMP) were used to prepare ultrafiltration membranes by the phase inversion technique via immersion precipitation. The effect of MC additive on the structure and performances of the membranes was studied. The obtained membranes were characterized by scanning electron microscopy (SEM), differential scanning calorimetry (DSC), infrared spectroscopy (FTIR-ATR), equilibrium water content (EWC), water contact angle, porosity and ultrafiltration experiments of polyethylene glycol solutions. It was found that all the PSf/MC membranes had higher porosity, more hydrophilic surface and more vertically finger like pores than PSf membrane. With an increase in MC content in the casting solution from 0.5% to 1.5%, the hydraulic permeability increases from 17.17 to 118.46 L.m-2.h-1.bar-1, while the rejection decreases from 91.82% to 64.45% with PEG 35000. DSC scan and FTIR analysis confirmed that methylcellulose was trapped in the membranes matrix.


Introduction
Most materials such as polymer, ceramic, metal, carbon and glass can be used to make membranes 1,2 .At present, the commercial membranes are mainly fabricated from polymeric materials.Being membrane materials, the polymers should demonstrate thermal stability over a wide range of temperature and a chemical stability over a range of pH, and possess a strong mechanical strength.The polymers that are suitable for making membranes include cellulose acetate 3,4 , polyamides 5,6 , polysulfones 7,8 , sulfonated polysulfones 9,10 , etc.. Polysulfones are mainly used to form ultrafiltration, microfiltration and gas separation membranes.][13] Polysulfone is one of the most used polymers to prepare membranes due to its excellent characteristics such as high chemical, thermal and mechanical resistance.However, polysulfone membranes exhibit strong adsorption and deposition towards foulants on the membrane surface as well as inside membrane pores due to the hydrophobic nature of polysulfone.This results in a lower water flux and serious membrane fouling.Hence, polysulfone membranes without modification seem less suitable for application in industry 14,15 .In order to improve membrane permeability and anti-fouling behavior, several studies have been devoted to this subject.Among these approaches, polymeric additives 15,16 are considered as an effective and convenient method because of their excellent performance and facility to handle.Polyvinylpyrrolidone [17][18][19] , poly (ethylene glycol) [20][21][22] and the polyaniline (emeraldine base) 14 were used as additives in the preparation of polysulfone membranes to promote their performances.Such additives act as a porogen which favors the formation of pores, also as agent for hydrophilizing the membranes surface.Most of these studies reported that the polymeric additives enhance the membrane surface hydrophilicity, water permeability and improved membrane fouling resistance characteristics.
According to the literature, the synthetic polymeric additives have been used extensively in membrane preparation in order to improve their separation properties, while natural plantbased polymers are rarely reported in this field.Among these polymers, the methylcellulose is classified as an amphiphilic natural plant-based polymer 23 and can be used as an additive to prepare membranes 24 .A new membrane prepared from modified methylcellulose/ cellulose acetate mixture was used to separate the emulsion oil in water 25 .Gcina et al. 26 used a lignin as an additive to probe the mechanical and thermal properties of polysulfone membranes.The result is the formation of thermally stable membranes relative to membranes modified with polyethylene glycol and polyvinyl pyrrolidone.Besides, they concluded that lignin is a good additive due to its interaction with the polymer through hydrogen bonding and make it a reinforcing agent.Therefore, the use of natural additives, cheap and readily available can be a good choice for membranes preparation.In this study, flat sheet membranes were prepared using a cellulose derivative polymer, methylcellulose, as an additive via phase inversion method, in order to create a high performance material that is based on renewable resources.The effect of methylcellulose as an additive on the properties of polysulfone membranes was evaluated using infrared spectroscopy, thermal analysis, electron microscopy, pure water flux and solute rejection studies.

Materials
Polysulfone (PSf, Udel P-3500, M w : 35000 Da) used as membrane material was supplied by Solvay Advanced Polymer (Belgium).Methylcellulose (MC, Mn~63000 Da, vis.1500 cps) from Aldrich was used as an additive.The molecular formulas of theses polymers are represented in

Membrane preparation
Flat sheet polysulfone-based membranes were prepared by phase inversion method via immersion precipitation in water coagulation bath as reported in literature [27][28][29] .Several polysulfone solutions were prepared by dissolving a measured amount of polymer (16 wt %) in NMP at room temperature.Then different quantities of methylcellulose were added in viscous polysulfone solutions, as shown in table 1.The polymeric mixture was stirred using a magnetic stirrer until having a homogeneous solution (~24h), and then it was left without stirring for 30 minutes to remove air bubbles.Thereafter, the solution was spread uniformly on a glass plate into ca.300µm film with the help of a casting knife.The resulting film was then immersed directly into coagulation bath containing water maintained at fixed temperature (25°C).The casted films changed their color from transparent to white immediately after immersion and separates out of the glass plate after a few seconds.The prepared membranes were stored in distilled water until use.The degradation property of methylcellulose polymer was determined using thermogravimetric analyzer (TGA Instrument Q500).The sample of pure methylcellulose was used without preparation and it was heated from 30 °C to 575 °C at a heating rate of 10 °C.min -1 under nitrogen atmosphere.

Differential scanning calorimetry (DSC)
The thermal behavior of the methylcellulose and of the prepared membranes was investigated by differential scanning calorimetry (Jade DSC instrument, Perkin Elmer), to measure the glass transition temperatures (Tg).For each measurement 5-8 mg of samples were weighed and scanned, from 25 to 250 °C, under dry nitrogen.

Chemical analysis
The powdered sample of methylcellulose and the membranes surface were analyzed by a Fourier transform infrared spectroscopic method with attenuated total reflectance (Perkin Elmer-Spectrum Two spectrophotometer) between 450 and 4000 cm -1 at a resolution of 2 cm -1 with 32 scans.Before analysis, the membranes were dried in an oven at 50 °C to remove water traces.

Membrane morphology
The cross section morphologies of the membranes were observed by an electron microscope (SEM) (Philips ESEMXL  30).Before SEM analysis, the membrane samples were cut into appropriate size, frozen in liquid nitrogen and fractured.

Contact angle (CA)
In order to evaluate the hydrophilic / hydrophobic character of membranes, water contact angles were measured using a measuring instrument (GBX DIGIDROP "Digitizer of droplets").A drop of water (1μl) was deposited on the membrane surface using a syringe.When the droplet is formed on the surface, an image of the drop was taken using a video camera.To minimize experimental error, the contact angle was measured at three different locations for each sample and the average was then reported.

Membrane characterization by the determination of equilibrium water content (EWC) and porosity
Equilibrium water content is a parameter related to porosity and can predict the degree of hydrophilicity or hydrophobicity of a membrane 30 .

Equilibrium Water content (EWC)
The membrane samples were cut in the dimension of 3×3 cm and put in distilled water for 24 hours, then weighed after removing excess of water on the surface.After that, the membrane samples were dried in an oven at a temperature of 50 °C until a constant mass was obtained (~24h).The equilibrium water content is calculated as follows: Where W w and W d are the mass of the wet membrane sample and the mass of the dried state (g) respectively.
To minimize the error, three pieces of each membrane were cut.

Membrane porosity
The membrane porosity was obtained by Eq.2. 31 Where W w and W d are the mass of the wet membrane sample and the mass of the dried state (g) respectively.A, L and ρ are the sample area (cm 2 ), the sample thickness (cm) at wet state and pure water density (g/cm 3 ) respectively.

Hydrodynamic characterization
Filtration experiments were performed using a dead end filtration stirred cell (Model 8050, 50ml, Amicon) connected to a nitrogen pressure.Each fresh membrane was compacted before use.The compaction was carried out with deionized water for 30 minutes at 1 bar.The pure water flux was measured in a range of pressure of 0.6 to 4 bars.For each membrane, several discs were tested and the average pure water flux was reported.

Pure water flux (PWF)
The pure water flux was calculated using Eq. ( 3) Where J (L.m -2 .h - ) is the pure water flux, V (L) is the volume of filtrate, A (m 2 ) is the membrane area and Δt (h) is the filtration time.
Hydraulic permeability (P h ) was obtained from the slope of the plot of J and ΔP and was calculated using Eq.4 32

Solute rejection (SR)
The rejection rate of the membranes was determined by filtration of PEG solutions of different molecular weights at a pressure of 1 bar.The solute rejection was calculated using Eq. ( 5) Where C p and C f are the concentrations of permeate and feed solutions respectively, which were determined by Dragendorff reagent method using spectrophotometry analysis. 33

DSC and FTIR Characterization of membranes
During the immersion/ precipitation of casting solution, on the one hand, the water soluble methylcellulose is extracted by the coagulant (water) in order to make porous polysulfone membrane with absence of MC.On the other hand, the coagulated chains of polysulfone surround the MC chains and bloc them in the matrix due to the instantaneous demixing of polymers solution.Consequently, the extraction of all the amount of MC from the polymer film cannot easily occur due to the short time of the coagulation.
In this aim, the thermal behavior and chemical surface analysis are studied in order to prove the presence of MC on the membrane matrix.

Differential Scanning Calorimetry (DSC)
Prior to differential thermal analysis (DSC), the thermal degradation by TGA studies of such a sample is needed.A TGA analysis was performed for MC to determine its temprature degradation.
The TGA thermogram of MC (figure 2) shows one decomposition stage and a minor weight loss of 4% at around 100 °C due to moisture and water retention from the polysaccharide structure.The decomposition process observed for this sample starts at 300 °C and shows only one max differential thermo-gravimetric (DTG) peak at 358.70 °C, indicates a good thermal stability of the methylcellulose used.These results are similar to those reported in the literature by Guimes et al. 34   From the DSC thermogram of methylcellulose (Figure 3), it can be seen that the water flow endotherm occurs in the range of 80 °C and 100 °C.This endotherm is present on the thermograms of cellulosic materials due to the interaction of the water and the non-substituted hydroxyl groups of the cellulose derivatives 36 .The presence of an endotherm at 147 °C in DSC can be attributed to a glass transition, as reported in literature 37   The thermal behaviors of different membranes were studied from DSC plots.Figure 4 presents the DSC results of the prepared membranes.From the above spectra, only a single glass transition temperature is observed in the range of 180-200 °C for all the membranes.The thermograme of control membrane (PSf) shows a glass transition temperature at 189.39 °C.The thermogrames of PSf/MC membranes show glass transition temperatures at 182.19 °C, 185.17 °C and 184.38 °C respectively by increasing the amount of methylcellulose in the polymer mixture from 0.5% to 1.5%.Comparing to the controle membrane, the Tg of PSf/MC membranes is slightly lower, this may be due to the presence of flexible side groups (Alkyl) of MC that increase the distance between chains in the mixture and reduces the inter-chain interactions that cause a decrease in Tg 28 .Generally, a lower glass transition temperature indicates more free volume in polymer which tends to release its molecular structure 26 .The slight changes of Tgs in DSC curves reflect the small amounts of MC in membranes.Consequently, the thermal properties of these membranes are near to those of control membrane.

Membrane surface chemistry
The functional groups present in the control membrane, in the methylcellulose and in the PSf/MC membranes were obtained by attenuated total reflection Fourier transform infrared spectroscopy (FTIR-ATR), and the recorded spectra are shown in Figures 5, 6   The FTIR spectrum of the control membrane (Figure 5) displayed the characteristics absorption peaks of all the bonds, in which the absorption band at 2969.40 cm -1 is attributed to C-H stretching vibrations.The presence of a strong peak and concentration of additives play important roles in the modification of the membrane properties.To evaluate the morphology of the membranes, the cross-sections of different prepared ultrafiltration membranes were characterized by SEM images and presented in figures 8 and 9.It can be seen that the membranes exhibit an asymmetric structure with a dense skin in the top layer and open pores (macrovoids and finger like pores) at the sublayer (Figure 8)  at 1242.83 cm -1 is assigned to the ether C-O-C stretch of the polysulfone moiety.The aromatic carbon carbon (C=C) streching vibration occurs at 1585.98 cm -1 , 1504.03 cm -1 and 1488.35cm -1 .The peaks at 1323.99 cm -1 ,1294.79cm -1 and 1169.77cm -1 correspond to a symmetric stretch of the sulfone group (SO 2 ), and these results are consistent with previous works. 14,38he FTIR-ATR spectroscopy was used to examine the functional groups of methylcellulose.The FTIR-ATR spectrum of MC (Figure 6) shows that pure methylcellulose had an absorption band at 3468.28 cm -1 related to stretching vibration of hydroxyl group ν(O-H).The bands at 2933.81cm - 1 , 2837.83 cm -1 are attributed to asymmetric and symmetric stretching vibration of C-H respectively.The pics at 1375.67 and 1458.9 cm -1 are assigned to the vibration of deformation in the plane of δ(C-H).The absorption band at 1063.59 cm -1 is ascribed to C-O-C stretching mode from glucosidic units.The peak at 944.95 cm -1 is related to OCH 3 groups.These results were consistent with those reported in the literature. 39,40 l peaks infrared absorption characteristics of PSf are present in FTIR spectra of PSf/MC membranes (Figure 7a,7c).In addition to the PSf absorption peaks, new peaks were observed in the region of 3200-3500 cm -1 characteristic to the hydroxyl groups (O-H) due probably to the presence of MC in the membranes matrix (Figure 7b).

Membrane morphology
The structure of the membrane is affected by the composition of the casting solution, where the nature  The cross-sectional morphology of the control membrane display both finger like pores and macrovoids near the bottom.This structure is formed by an instantaneous demixing produced between the surface of polymer casting solution and water coagulation bath 30,41 which results a formation of polymer reach phase and poor phase.
In fact, the instantaneous demixion of membrane is due to (1) the incompatibility of the system PSf/ water results the precipitation of PSf and (2) the high mutual affinity between the solvent (NMP) and the non-solvent (water) results the high diffusion between solvent and nonsolvent at the interface of casting solution.Consequently, the polymer-reach phase produces the thin film and the formation of nuclei of a polymer-poor phase form the porous structure 42 .The formation of finger like pores in sub-layer is the result of a longer exchange between solvent and non-solvent in polymer poor phase follows the increase of solution viscosity which cause a delayed precipitation of the polymer and then, a decrease in the diffusion rate of water into the polymer film 43,44 .
Compared with the control membrane, the finger like pores and macrovoids of PSf/MC membranes become more porous with increasing concentrations of MC.A similar observation was found by Gcina et al. 26 for the PSf membrane using ligning as an additive and NMP as a solvent.Generaly, water soluble polymers have been considered as pore-formers during membrane formation 45 .It is assumed that most of water soluble polymers can be leached out of the casting film and the sites where the polymer exists become micropores in the prepared membrane 14 .The evolutions found in crosssection confirm that the water soluble methylcellulose form pores when used, as additive, in membranes.In fact, the MC has good solubility in NMP, a portion of MC located near the surface of the casting film could diffuse out along with NMP into the coagulation bath, resulting in the increase of membrane porosity.
At higher magnification, a spongy morphology appeared between the open pores with the PSf/MC membranes as shown in Figures 9b.For a clear observation of this morphology, membrane at 3% of MC was prepared and analysed by SEM (Figures 9c and d).
For the controle membrane, the fast formation of the rigid PSf matrix prevents the growth of the polymer-lean droplets (spongy structure) in between the macrovoids 46,47 .It is well known that the structure of the membrane is affected by the kinetic diffusion of solvent and non solvent.In our system PSf/ NMP/water, the high affinity between water and NMP induce the instantaneous demixion and form asymetric membrane.In the contrary case, the low affinity between solvent/non solvent induce the delayed demixion and the spongious structure become favorable.The open pores structure in controle membrane are formed by nucleation and growth of the polymer lean phase due to the formation of skin layer.The early formation of skin layer delay the diffusion of water through the top layer which cause the delayed demixion of sublayer.This new phenomenon is not produced from the lower affinity of solvent/ non solvent but produced by the low concentration of non solvent in polymer poor phase.In this region, the solvent concentrations become so high locally, these conditions become favorable for delay of demixing 48 .In this case, a nucleus is formed serving as a tiny coagulation bath.The polymer solution surrounding the nucleus.As long as the conditions of delayed demixing remain the same, as long as the solvent concentration in the nucleus remains high enough, the growth of the nucleus continues 48 .
However, the spongious structure in between open pores was observed in controle membrane at hight concentration of PSf 49 .Gillen et al. explain that the polymer precipitation also occurs rapidly at the inner walls of the finger like voids and forms a thin skin and the region between open pores remain fluid.The slow diffusion of non-solvent into the inter-void regions of the membrane causes nucleation of the polymer rich phase and eventually polymer precipitation, hence a spongy morphology arises from precipitated nuclei.
With the PSf/ MC/ NMP/water system, the integrated hydrophilic polymer MC in skin layer make the diffusion of water through the top layer relatively higher compared with the controle membrane.The conditions for delay of demixing cannot take place in some points: growth of a nucleus is effectively blocked by the creation of new nuclei.Such structure is observed by SEM microscopy for the PSf/ AN69/NMP systems 47 , when the non water soluble polymer (AN69) was used as an additive.The longer time is observed before the matrix vitrification which allows the nucleated polymer-lean droplets to grow further in the delayed phaseseparation zones, leading to larger cells in the spongy part between the open pores.

Equilibrium water content, porosity and hydrophilicity
All the prepared membranes were characterized in terms of equilibrium water content (EWC), porosity and surface hydrophilicity.The results are presented in table 2. The EWC is considered as a parameter that indirectly indicates the degree of hydrophilicity of a membrane and it is closely related to the porosity.The pores on the surface as well as cavities in the sublayer are responsible for accommodating water in the membranes 30,32 .It may be found from the table that a small increase in EWC is observed with increasing the rate of MC in membranes, and the values are around 74-75%.This indicates the increment of the number of pores in the membrane or the pore size of the existing pores.
A significant increase in porosity is found when MC content increases in polymer solutions.The PSf/MC membranes showed a high porosity in the range of 68% to 81% compared to the control membrane that present a porosity of 57%.This may be the results of hydrophilic character of MC which lead to form the spongy structure between the open pores.
Water contact angle is a parameter used to evaluate the surface hydrophilicity and also one of the most important parameter which could affect the flux of the membranes.As presented in table 2, the contact angle of the PSf /MC membranes is lower than that of the control membrane and decreases by 2° when increasing the concentration of MC by 0.5%.The variation in the contact angle is small; it reflects a small change in the hydrophilic nature of the membrane surface which can be explained by the low rate of MC trapped in the membrane and/or the lack of hydrophilic group (hydroxyl) in the methylcellulose.
During the immersion precipitation process, the MC can diffuse on the membrane surface due to its good solubility in water, leading to the improvement of wettability on the membrane surface due to its hydrophilic groups (OH).Therefore, contact angle is closely related with surface energy 32 .

Effects of MC on membrane permeability and solute rejection
Pure water flux (PWF) and solution rejection are considered to be significant factors for any membranes.PWF and solute rejection have a direct relationship with the number of pores and the pore size on the membrane surface.The effect of MC rate on PWF and solute rejection is shown in the Figures 10 and 11.It can be seen from Figure 10 that PWF increases with increasing in transmembrane pressure linearly.This result verifies Darcy's law, which means that in this case, the transport through a membrane is described by Darcy's law.The free volume elements (pores) are relatively large and fixed, do not fluctuate in position or volume on the timescale of permeant motion, and are connected to one another 2 .From the same figure, it can be observed that the membrane which contains 1.5% MC, exhibits the highest water flux of 45.31 L.m -2 .h - and 427.40 L.m -2 .h - at 0.6 bar and 4 bars respectively.The variation of the water flux could be explained by the porosity of the membranes.It is observed from table 2 that a significant increase in porosity is found when the amount of MC increased in a polymer solution.From the same figure, it can be observed that the membrane permeability was improved by increasing the amount of MC in polymers solutions.The control membrane shows a low permeability of 4.71 L.m -2 .h-1.bar -1 , and then it was increses to 17.17, 28.29 and 118.46 L.m -2 .h - .bar - respectively by increasing the MC content from 0.5 to 1.5%.These can be the results of the double effect of MC manifested by the improvement of membrane surface hydrophilicity (table 1) and the alteration of the membrane structure.The increase of MC content leads to a larger pores compared to the control membrane, so that the water molecules penetrate easily through the membrane.
Another term used to define the performance of membranes is the removal percentage of unwanted solute.Ultrafiltration membranes are porous membrane, wich indicate that the basic mechanism of rejection will be the sieving mechanism.Molecules with a greater size than the pores will be rejected.From the solute rejection results (Figure 11), the rejection of PEG 35000, PEG 10000 and PEG 6000 by the membranes are in the ranges of 64.45 -91.82%, 31.57-82.30% and 21.43 -70.77% respectively.For all the membranes, the rejections decrease with increasing MC content in a polymer solution in the following order PEG 35000 rejection >PEG 10000 rejection > PEG 6000 rejection.This is due to the difference of molecular weights.Consequently, the pore size of the PSf/MC membranes increases with the amount of MC, which is in complete agreement with the values of the permeability where hydraulic permeability increases from 17.17 to 118.46 L.m -2 .h - .bar - by increasing the rate of MC from 0.5% to 1.5% (Table 2).The molecular weight cut-off (MWCO) is defined as the lowest molecular weight of a solute that has a rejection of 90% 50 .According to this, the MWCO of the PSf/MC membranes is higher than 35000 Da for PSf-1.5, is about 35000 Da for PSf-1, and is 35000 Da for PSf-0.5.

Conclusion
In order to study the effect of methylcellulose as an additive on membrane structure and performances, polysulfone based membranes were prepared via phase inversion method and different amounts of methylcellulose were added to the polymer solution.The morphology of the modified membranes shows an asymmetric structure with a dense skin at the surface and both finger like pores and macrovoids penetrating the membrane cross section.At higher magnification, a spongy morphology was observed between finger like pores with the excepetion for the control membrane.On the one hand, the evolutions found in cross-section confirm that the water soluble methylcellulose could leach out in the coagulation bath during phase separation and act as pore forming agent, on the other hand, FTIR-ATR and DSC results demonstrate that a amount of MC remains trapped in the matrix of the prepared membranes.The increase in membrane porosity by increasing the amount of MC in polymer solutions enhance pure water flux and consequently decrease the PEG rejection, and the contact angle of different membranes show an improvement in the surface hydrophilicity.
The results obtained in this work suggest that the natural plant-based polymers may be promising additives in membrane formation and demonstrate a good performance; thus, it can be considered as an additive in practical applications.
It could be interesting to study the effect of different types of soluble cellulose derivatives in term of morphology, pore size and performance against the effluent treatment, and make a comparative study with those prepared with synthetic additives.

Figure 1 .
N-methyl-2-pyrrolidone (NMP, 99%) from Fluka was used as solvent directly without any further purification.Polyethylene glycols of different molecular weights (6000, 10000 and 35000 Da) from Fluka were used to measure the rejection and molecular weight cut-off of the membranes.Bismuth (III) nitrate pentahydrate (BiN 3 O 9 .5H 2 O), potassium iodide (KI) and hydrochloric acid (HCl) were analytical reagents provided by Sigma-Aldrich factory used to prepare Dragendorff reagent.
. Zuo et al. found a glass transition temperature of a commercial MC (M450) of about 108.7 °C.

Figure 5 :
Figure 5: The FTIR-ATR spectra of the control membrane.

Figure 11 :
Figure 11: Effect of MC dosage on solute rejection of the membranes.

Table 1 :
The compositions of the PSf/MC/NMP casting solutions.