alexa Influence of Functionalized Multiwall Carbon Nano-Tube on the Structure and Performance of Cellulose Di-Acetate Based Forward Osmotic Membrane for Desalination Process
ISSN: 2155-9589
Journal of Membrane Science & Technology

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Influence of Functionalized Multiwall Carbon Nano-Tube on the Structure and Performance of Cellulose Di-Acetate Based Forward Osmotic Membrane for Desalination Process

Xiulan Zhao1,2, Jianfang Sheng1, Lijing Zhu1, Anjiang Zhang1* and Lixin Xue1,2*

1Polymer and Composite Division, Key Laboratory of Marine Materials and Related Technologies, Zhejiang Key Laboratory of Marine Materials and Protective Technologies, Ningbo Institute of Materials Technology and Engineering, Chinese Academy of Sciences, Ningbo 315201, P.R. China

2Ningbo Lianhua Environmental Science and Technology Co., Ltd, Ningbo 315400, P. R. China

*Corresponding Authors:
Lixin Xue
Ningbo Institute of Materials Technology and Engineering
Chinese Academy if Sciences
E-mail: [email protected]

Anjiang Zhang
Ningbo Institute of Materials Technology and Engineering
Chinese Academy of Sciences, No. 1219, Zhongguan West Road
Zhenhai District, Ningbo, Zhejiang Province, P. R. China 315201
E-mail: [email protected]

Received date: July 31, 2015; Accepted date: February 28, 2015; Published date: August 30, 2015

Citation: Zhao X, Sheng J, Zhu L, Zhang A, Xue L (2015) Influence of Functionalized Multiwall Carbon Nano-Tube on the Structure and Performance of Cellulose Di-Acetate Based Forward Osmotic Membrane for Desalination Process. J Membra Sci Technol 5:135. doi: 10.4172/2155-9589.1000135

Copyright: © 2015 Zhao X, et al. This is an open-access article distributed under the terms of the Creative Commons Attribution License, which permits unrestricted use, distribution, and reproduction in any medium, provided the original author and source are credited.

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To improve the performance of Cellulose di-acetate (CDA) based forward osmotic (FO) membrane in sea water desalination process, functionalized multi-walled carbon nano-tubes (MWCNTs) were blended as additives at varied compositions, from 0 to 5 wt%, into the solutions to prepare FO membranes using a classical phase-inversion method. The structure and property of the formed membranes were characterized by Fourier transfer infrared (FTIR) spectroscopy, Atomic Force Microscopy (AFM), Scanning Electron Microscopy (SEM), Transitional Electron Microscopy (TEM), Water Flux and Reverse Solute Flux Tests. It was found that the content of functionalized MWCNTs was an important factor influencing the morphology, porous structures and properties of the blend membranes. SEM, AFM and TEM images of the blend membranes showed that the surface morphology and the cross-sectional morphology changed with the content of functionalized MWCNTs. It is interesting to see that at the presence of functionalized MWCNTs, the surface contact angle and the reverse solute flux of the FO membranes could be greatly improved without significantly affecting the pure water flux. With the addition of only about 1 wt% MWCNTs, the water flux of CDA based FO membrane was increased from 10.5 to 12.5 L/m2h while its reverse solute flux was reduced from 1.8 to below 0.3 mol/m2h. Desalination tests with 3.5 wt% simulated seawater feed solution had shown that the blend membrane with 1 wt% MWCNTs, was 366% higher in water flux and 53% lower in reverse solute flux than those of pure CDA FO membrane. These results suggest that CDA bases FO membranes modified with functionalized MWCNTs could possess good potential to be further developed for practical applications in the sea water desalination processes.


Porous stainless steel membrane; Hollow fiber; Phase inversion; Sintering


Inorganic membranes possess the advantages of high thermal stability, good chemical resistance and high mechanical strength, and thus have been targeted by a variety of advanced applications at high temperatures or environments involving corrosive chemicals [1,2]. Among them, the porous ceramic membranes have been broadly applied for many years but they generally exhibit some drawbacks such as brittleness and low thermal shock resistance. In contrast, porous metal membranes often made from stainless steel have high mechanical strength, offer good thermal shock resistance and allow for easy integration by welding or brazing in membrane module assembly, and therefore have been extensively used as the porous support to deposit other thin separation films such as Pd, silica and zeolites [3-9].

Most inorganic membranes in applications are usually designed into a planar or tubular configuration. Comparatively, the hollow fiber geometry is more favorable for practical use because it can provide a much higher surface-area-to-volume ratio. In the past decade, a combined phase inversion/sintering technique has been developed to fabricate various ceramic hollow fiber membranes [10-13]. Compared to other methods to produce inorganic hollow fibers, the phase inversion induced hollow fiber membranes also exhibit very significant advantages over the planar or tubular ones such as low permeation resistance due to the resultant asymmetric microstructures and low fabrication costs. Furthermore, the phase inversion/sintering technique is very versatile and can be modified to synthesize porous stainless steel (PSS) hollow fiber membranes [14-17].

So far the limited several studies on the preparation of PSS hollow fiber membranes by the phase inversion/sintering technique are mainly focused on the microstructure formation of the PSS hollow fibers during the phase inversion process. For example, Luiten-Olieman and co-workers reported the variation trend of the PSS hollow fiber microstructures with the spinning conditions and the composition of the spinning suspension [14-16]. We also reported the synthesis of the PSS hollow fiber membranes in spiral configurations by adding special additives in the spinning solution [18]. But the hollow fibers have low gas permeability due to the low surface porosity despite their apparent porosities are larger than 40%, indicating the majority of pore volume was closed inside the fiber wall. Actually, the membrane properties like microstructure, surface porosity, pore size distribution and mechanical strength that should be critically considered in practical applications are significantly affected by the sintering conditions in the preparation of inorganic membranes [19]. For example, sintering of the PSS hollow fibres under air, CO2, He and H2 atmospheres would lead to different microstructures [20]. However, the general evolution of microstructure and performance of the resultant PSS hollow fibers with the variation of sintering conditions has not been much clarified.

The objective of this work was to elucidate the effects of sintering parameters including atmosphere, temperature and dwelling time on the microstructure and properties of the PSS hollow fibers spun by the phase inversion-sintering technique, and to identify the optimal sintering conditions at which high performance PSS hollow fiber membranes can be achieved.


Spinning of the PSS hollow fiber precursors

The PSS hollow fiber precursors were spun from a dope mixture via the phase inversion process described in more details elsewhere [10,11]. For preparation of the spinning dope, stainless steel powder (AISI 316L, Fe/Cr18/Ni10/Mo3, mean particle size=3 μm, purchased from Good Fellow Cambridge Limited) and organic additives were added into N-methylpyrrolidone (NMP, AR Grade, >99.8%, Kermel Chem Inc, Tianjin, China) solution followed by stirring for 30 min. Polysulfone (PSf, Udel35000, Solvay USA) was then added in three steps, each separated by 2 h. The mixture was stirred for 36 h untill all the polymer was completely dissolved to form a uniform suspension. The contents of PSf, NMP, 316L steel powder and organic additives in the spinning solution were 6.2, 26.8, 65.4, and 1.6 wt%, respectively. Prior to spinning, the suspension was degassed by applying vacuum for 1 h and left overnight under dry air. The spinning solution was extruded by a syringe pump through a tube-in-orifice spinneret (inner and outer diameter of 1.5/3.0 mm, respectively) into a tap water bath for coagulation. Deionized water as the internal coagulant was pumped through the bore of the spinneret at a flow rate of 8 mL min-1. The PSS hollow fiber precursors were kept in a water bath for 24 h for the thorough removal of NMP solvent.

Sintering of the membranes

Thermal treatment of the hollow fiber membranes was performed in a tubular furnace (GSL-1700X, Hefei Kejin Materials Tech. Co., China). Prior to sintering, the hollow fiber precursor was cut into short pieces of around 20 cm in length and dried in air for 48 h. The hollow fiber precursors were firstly heated with the heating rate of 5°C min-1 to 600°C and calcined in static air at this temperature for 60 min to remove the polymer binder and the organic additives. Subsequent sintering was performed in static air or H2-N2 streams with different hydrogen concentrations, while the temperature was further elevated at a heating rate of 3°C min−1 to 1000~1200°C, dwelling for 30, 60, 120 or 240 min, respectively. The sintering process ended by cooling down to room temperature at 3°C min−1 under the same atmosphere. For each sintering condition, five hollow fiber samples were prepared for characterization and performance test. The average values over the samples were taken to evaluate the sintering effects on the hollow fiber properties.


Scanning electron microscope (SEM, JEOL JSM 5600 LV) was used to examine the morphology and the microstructures of the hollow fiber membranes sintered under different conditions. SEM images were taken on both the cross-section and surface of the fibers. X-ray diffraction (XRD) patterns of the PSS hollow fibers were recorded with a Bruker D8 Advance diffractometer using Cu Kα radiation (λ= 0.15404 nm). The hollow fibers were ground into fine powders prior to the XRD measurement. Continuous scan mode was used to collect 2θ data from10° to 80° with a 0.02° sampling pitch and a scan rate of 2° min−1. The X-ray tube voltage and current were set at 40 kV and 30 mA, respectively.

The pore size distribution of hollow fibers was measured using a mercury porosimeter (Micromeritics, Auto Pore IV 9500) employing mercury pressures between 1.50 and 33000 psi. Prior to measurement, the samples were heat-treated at 200°C for 2 h to remove adsorbed vapor. The weight of each sample for the measurements was around 1.2 g. The evacuation and the equilibrating time were 5 min and 10 s, respectively. In addition, the porosity of the hollow fibers was also calculated from the bulk density estimated by the weight and the corresponding dimensions of the samples.

The mechanical strength of the hollow fibers was measured with a three-point bending instrument (Instron Model 5544) with a crosshead speed of 0.5 mm min-1 [21]. Hollow fiber samples were fixed on the sample holder with a distance of 4 cm. The bending strength, image , was calculated from the following equation:

image (1)

Where F is the measured force at which fracture takes place; L, D and d are the length (4 cm), the outer diameter and the inner diameter of the hollow fibers, respectively. The values of outer diameter (D) and inner diameter (d) were obtained from the SEM micrographs.

The permeation properties of the PSS hollow fiber membranes were evaluated by the nitrogen and pure water permeation measured in a dead-end mode under constant flux operation. The modules were custom-made by gluing a single fiber into glass tubing with an organic sealant [22]. Three different flux settings were used for each sample. The permeate flow was recorded as a function of the trans-membrane pressure. The pressure drop over the fiber is assumed to be negligible. The gas or water permeance through the hollow fiber was calculated by,

image (2)

Where Np is the molar flow rate of the permeate gas or water, Am the effective membrane area calculated by

image (2)

and Δp is the pressure difference across the membrane.


Results and Discussion

In order to obtain pure stainless steel membranes, the organics in the PSS hollow fiber precursors should be removed completely while the stainless steel phase is retained well. The burnout of organics is highly dependent on the composition of organics and the microstructure of precursor, thus much related to the gaseous atmosphere surrounding the precursor. A major concern of the sintering atmosphere is the presence of oxygen as it is required to burn out the organics, but on the other hand it should be used as less as possible to avoid the possible oxidation of iron phase. Thus, in this work, air was used at lower temperature of 600°C to burn out the organics in the hollow fiber precursor, after which inert or reducing gases were introduced to protect the stainless steel hollow fiber during the subsequent high temperature treatment to achieve the desired density and mechanical strength. Figure 1 shows the morphology of the hollow fiber precursor and the fiber sintered at 600°C for 1 h. It can be seen that short fingerlike structures have been formed near both the outer and inner walls of the fiber, while a sponge-like structure occurs at the center of the fiber precursor (Figure 1a). This is the special feature of the hollow fiber membranes prepared by phase inversion method using water as both the external and the internal coagulants as the rapid precipitation occurred at both the inner and outer walls close to coagulants resulting in short finger pores but the slow precipitation at the center of the fiber giving the sponge-like structure [10,11]. The stainless steel particles are well dispersed and embedded inside polymeric matrix, as displayed in Figure 1a. After sintering at 600°C for 1 h, the cross-sectional structure of the fiber precursor has been well preserved, as shown in Figure 1(b). The surface SEM image shows the absence of organic binders as they were removed completely during the sintering process (Figure 1b). The stainless steel particles keep their original spherical shape with particle size of around 1-3 microns, indicating sintering has not occurred yet at this temperature.


Figure 1: The danger signal can induce immature dendritic cell to mature dendritic cell.

In order obtain the sintered PSS hollow fiber membranes with 1050°C at heating rate of 5°C min-1 and dwelling for 2 hours, under different atmospheres with flowing air, nitrogen and hydrogencontaining streams. Figure 2 compares the morphology of the resultant PSS hollow fibers. The general porous structure can be observed in all the sintered samples from the cross sectional areas, but the sandwiched structure is more perfectly preserved when using hydrogen-containing atmosphere although the quantity and the size of the pores have greatly decreased after the sintering process. The significant effect of the sintering atmosphere can be seen more clearly from the inner surface morphologies. For the fiber sintered in air, the inner surface looks quite dense with a few pores in the size of 1-2 microns randomly distributed. The formation of such dense surface structure may be due to the iron oxidation on the surface layer. Compared to metal iron, the formed iron oxides of Fe2O3 or Fe3O4 would increase the weight by 40%, thus causing the volume swelling and making the surface denser. The formation of iron oxides can be confirmed by the XRD pattern that will be discussed later. For the sample sintered in nitrogen atmosphere, the surface also looks dense but the number of open pores is more than that of the fiber sample sintered in air. The possible reason for this phenomenon is still related to the volume and weight increase caused by the formation of iron nitride formed during the high temperature sintering stage or other impurities like iron oxides or carbonized compounds [23], which also can be evidenced by the XRD results below. However, when H2-containing atmosphere was applied, the resultant hollow fibers have shown a completely different surface morphology. The stainless steel particles retained their original spherical shape, and connected with each other to form a large quantity of micro pores. Sintering does not occur as deeply as in the air and nitrogen atmospheres, because hydrogen as the most effective reducing atmosphere allows for enhanced oxide removal, which necessitates longer sintering times. Furthermore, the small hydrogen atoms may diffuse into the metal lattice, leading to a puffy structure on the particle surfaces and inhibiting the elimination of final porosity, as shown in the Figure 2 [24]. Nevertheless, the dependence of the porosity with the H2 partial pressure in the sintering atmosphere cannot be easily perceived just from the SEM image alone. Other characterization techniques are required to better evaluate the effects of the hydrogen concentration in sintering atmosphere on the properties of the PSS hollow fiber membranes.


Figure 2: SEM images of the cross sectional and inner surface of the PSS hollow fiber membranes sintered at 1050°C for 2 h in different sintering atmosphere.

Figure 3 shows the XRD patterns of the PSS hollow fiber membranes sintered at 1050°C under different atmospheres, where the XRD pattern of the original stainless steel powders is also presented for comparison. As can be seen, the dominate phase in the original powder is martensite phase (α-Fe) identified at 44.50° and 64.76°, but a minor amount of austenite phase (γ-Fe) is also present identified by the characteristic peaks of 43.54°, 50.70° and 75.8°. After the stainless steel powder is formed into hollow fibers via sintering, the predominant phase will transform from martensite to austenite. Furthermore, the intensity of the characteristic peaks of all the hollow fibers has been reduced significantly. This can be attributed to the re-crystallization effect, i.e., the large grains were broken up into smaller ones during the high-temperature sintering process [25]. Some additional peaks are also identified in the XRD patterns of the hollow fibers, indicating that some impurity phases have been generated after sintering. Types of the impurity phases are highly dependent on the sintering atmosphere. For example, carbon compounds such as Mo12Fe22C10 (PDF card code 78-0272) and Mo2C (PDF card code 77-0720) were detected in the N2-sintered hollow fibers, whereas the main impurity would be Fe2O3 in the hollow fibers sintered in the air atmosphere. Under the H2- containing reducing atmosphere, the impurities would no longer be observed in the XRD pattern. In the presence of hydrogen, any iron oxides like Fe2O3 could be reduced to metal phase, and the formation of iron compounds would be inhibited.


Figure 3: XRD patterns of the original stainless steel powder and the PSS hollow fiber membranes sintered at 1050°C under different atmospheres (impurity phases: * Mo12Fe22C10; ◊ Mo2C; ♥ Fe2O3).

Figure 4 describes the pore size distribution of the hollow fibers sintered at 1050°C under different sintering atmospheres. Despite the atmosphere difference, all the fiber samples exhibit a bimodal pore size distribution (Figure 4a) with the pores ranging from 0.01 to 3 μm. This is a typical feature of the asymmetric membranes fabricated by the phase inversion method [26,27]. Figure 4b shows the cumulative pore volume distribution, from which it is clear that the majority of porosity is contributed from the pores of 1-3 microns. The pore volume alternation is highly related to the sintering atmosphere. At the same sintering temperature, the sintering atmosphere with larger H2 partial pressure confers the sample with a larger volume; on the other hand, the sample sintered in oxidant (air) environment possesses the smallest volume. This result is consistent with the observation from the SEM images, and also agrees with the literature report [24]. It suggests that, to be applied as the substrate for supported thin membrane synthesis for fluid separation, the PSS hollow fibers should be sintered in the atmosphere with H2 since a more porous structure is preferred to minimize the transport resistance through the substrate. Furthermore, although the fibers sintered in the 50% H2-N2 atmosphere possess the largest pore volume, the 25% H2-N2 atmosphere is more preferably recommended since the resultant fibers have the most micro pores smaller than 0.2 μm while those sintered in the 50% H2-N2 atmosphere mainly possess the macro pores between 1~3 μm in diameter. In order to further recognize the role of hydrogen in sintering, the effect of hydrogen concentration in the sintering atmosphere on the porosity, mechanical strength and permeances of both nitrogen and pure water have been investigated and presented below.


Figure 4: Pore size distribution (a) and cumulative volume (b) of the PSS hollow fiber membranes sintered under different atmospheres.

Figure 5 plots the porosity and mechanical strength of the prepared PSS hollow fibers against the H2 concentration in the sintering atmosphere. As displayed, the general trend of porosity change with the H2 concentration is increasing, which is opposite to the change of mechanical strength. This is a reasonable observation as a higher porosity generally signals a lower mechanical strength. However, as consistently observed, the change of the porosity and mechanical strength with further H2 concentration increment is very marginal after the H2 concentration reached up to 25%. In this case, a higher H2 concentration than 25% in the sintering atmosphere is not very necessary as it will increase the operational cost related to the safety issues during the sintering operation.


Figure 5: Effect of hydrogen content in the H2-N2 sintering atmosphere on the porosity and mechanical strength of the PSS hollow fibers sintered at 1050°C for 2 h.

Figure 6 displays the N2 and water permeance of the sintered membranes versus the H2 content in the sintering atmosphere, where the sintering temperature and the dwelling time were fixed at 1050°C and 2 h, respectively. As expected, both the nitrogen and water permeance increases with increasing the hydrogen concentration in the sintering atmosphere, since the presence of hydrogen induces more porosity especially on the hollow fiber surfaces. For example, when sintered in nitrogen atmosphere, the hollow fiber exhibited a nitrogen permeance of 1.77×10-4 mol m-2 s-1 Pa-1, which is of the same order of magnitude as reported in the literature [16]. As the hydrogen content in the sintering stream was increased to 10% and 25%, the nitrogen permeance would increase by 42.8% and 72.6% to 2.52×10-4 and 3.05×10-4 mol m-2 s-1 Pa-1, respectively. These values for the permeance mean that the fibers are suitable as porous support structures for gas separation membranes. Likewise, the water permeance increased significantly from 41.6 L m-2 h-1 bar-1 for fiber sintered in the nitrogen atmosphere to 115.2 (2.79 times) and 135.4 (3.25 times) L m-2 h-1 bar-1 for the fibers sintered in the 10% H2-N2 and 25% H2-N2 sintering atmospheres, respectively. Again, the permeation results also indicate that the higher hydrogen concentration than 25% in the sintering atmosphere would yield a limited increase in both the nitrogen and water permeance, thus is not necessary for sake of safety and operational cost.


Figure 6: Plots of nitrogen and pure water permeances of the PSS hollow fibers sintered at 1050°C for 2 h against the hydrogen content in the H2-N2 sintering atmosphere.

For the H2-containing atmosphere (25% H2), other sintering parameters such as the sintering temperature and dwelling time have also been investigated with the results presented in Figures 7-9. Figure 7 illustrates the porosity and mechanical strength of the PSS hollow fibers sintered at different temperatures with a fixed dwelling time of 2 h. In general, there is a trade-off between the porosity or pemeance and the mechanical strength. That is, a larger porosity often mirrors the better performance in fluid permeance but suffers a lower mechanical strength due to the insufficient bonding at lower temperature. An important indication from this figure is that the sintering temperature should not be higher than 1100°C otherwise the porosity would decrease remarkably from 50.3% to 14.1%, although the mechanical strength has also improved significantly. This implies that the permeation properties of the PSS hollow fibers would be deteriorated noticeably as the sintering temperature increases. As shown in Figure 8, the water permeance decreased significantly from 155.0 L m-2 h-1 bar-1 to 38.3 L m-2 h-1 bar-1, and then to 2.2 L m-2 h-1 bar-1 as the sintering temperature was increased from 1050°C to 1100°C and 1150°C, respectively. Further increment of the sintering temperature to 1200°C will transfer the hollow fiber into a dense structure, for which no gas permeation could not be detected any more.


Figure 7: Effect of sintering temperature on the porosity and mechanical strength of the PSS hollow fiber membranes sintered under the 25% H2- containing atmosphere.


Figure 8: Nitrogen and pure water permeance of the PSS hollow fiber membranes sintered at different temperatures under the 25% H2-containing atmosphere.


Figure 9: Effect of sintering time on the porosity, mechanical strength of the PSS hollow fiber membranes sintered under the 25% H2-containing atmosphere.

Figure 9 shows the porosity and mechanical strength of the PSS hollow fibers sintered at 1050°C under the 25% H2-containing atmosphere as a function of sintering time. It can be seen that the porosity decreased from 65.1% to 61.7%, while the mechanical strength increased noticeably from 107.9 MPa to 210.9 MPa as the sintering time was extended from 30 min to 90 min, but further extension of the sintering time would hardly change the mechanical strength and the porosity any more. This implies that the fusion and bonding of the stainless particles mainly occurred within the initial 90 min duration. In order to guarantee the complete sintering, two hours of sintering time is sufficient for economical purpose.


Porous stainless steel (PSS) hollow fibers with asymmetric structure have been developed through the immersion-induced phase inversion and sintering technique. The sintering atmosphere has significant influence on the microstructure and properties of the resultant hollow fiber membranes. Experimental results indicate that H2-containing atmosphere for sintering can lead to the formation of highly permeable porous membranes with desirable mechanical strength, but the H2 concentration in the sintering atmosphere higher than 25% in nitrogen is not necessary as it yields a limited improvement on the membrane performances. For a sufficient sintering, the sintering temperature should be higher than 1050°C so as to yield a desirable mechanical strength, but not higher than 1100°C, otherwise the porosity will be decreased noticeably due to densification. For cost effective and less time consuming, sintering time can be controlled within two hours. The resultant PSS hollow fibers possess the advantages of high porosity, high fluid permeance, robustness to be handled with stress, thereby in addition to be directly applied for microfiltration, they are also suitable to be used as porous supports for next step thin membrane synthesis for gas separations or desalinations.


The authors gratefully acknowledge the research funding provided by the National Natural Science Foundation of China (NSFC 21176187), the Research Fund for the Doctoral Program of Higher Education of China (RFDP 20131201110007) and the Program for Changjiang Scholars and Innovative Research Team in University (PCSIRT) of Ministry of Education of China (IRT 13084).


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