# Fabrication of Polypropylene-g-(Diallylamino Triazine) Bifunctional Nonwovens with Antibacterial and Air Filtration Activities by Reactive Extrusion and Melt-Blown Technology

Authors: Chao Liu; Zijian Dai; Rong Zhou; Qinfei Ke; Chen Huang
Journal: Journal of Chemistry
 (2019)

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## Abstract

Air filtration materials such as protective masks can protect humans from airborne pathogens; however, most of the existing protective filtration materials are aimed to intercept bacteria. Therefore, in this work, modified polypropylene- (PP-) based melt-blown nonwovens with antibacterial property were prepared for reducing the infection rate during the filtering process. Firstly, anN-halamine precursor, 2,4-diamino-6-diallylamino-1,3,5-triazine (NDAM) monomer, was grafted with PP polymers (PP-g-NDAM) by reactive extrusion method, and the grafting effect was confirmed by nitrogen analysis and FTIR spectra. Then, the obtained PP-g-NDAM was mixed with pristine PP resins in different ratios to prepare the filter materials by melt-blown technology. Finally, the new PP-g-NDAM melt-blown filter materials were finishing treated by the chlorination and electrostatic process, which showed a high filtration efficiency with low pressure drop and a potent antibacterial effect against Escherichia coli (E. coli). This work provides an innovative method for manufacturing antibacterial filtration nonwovens, which can improve the quality of conventional filtration products.


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## Body

## 1. Introduction

Human beings unavoidably expose themselves to airborne pathogens in daily lives; it is noted that the pathogens will propagate and spread in conditions of suitable temperature and humidity, which poses a serious risk of respiratory disease to human health. At present, using air filtration media is the most effective way to protect people from the influences of airborne pathogens. However, most of the fiber-based filters only focused on particulate matter (PM) removal, and the majority of pathogens are controlled by the retention on the fiber surface, instead of cleaning them out, resulting in a potential health concern of the secondary infection. Therefore, there is an urgent requirement for fabricating multifunctional filter materials with antibacterial and air filtration properties, which could improve the protective effect.Polypropylene (PP) materials have been intensively used in face masks, air purifiers, protective suit, surgical gown, and hygienic products, where antimicrobial functions are highly desired. Because of the excellent chemical stability, antibacterial modifications of PP materials are relatively difficult to conduct. In the past decades, researchers have used the methods of surface grafting [1–3] or surface coating [4] of antimicrobial agents onto PP polymer materials to achieve antibacterial functions, however, with limited durability and applications. Besides, once the antimicrobial agents are entirely consumed, the antimicrobial property cannot be regenerable anymore [5–7]. To solve the problem mentioned above, N-halamines [8–12] were selected as an ideal antibacterial agent to modify PP polymers, which has advantages of broad-spectrum and long-term sterilization activity, durable, regenerable, stability, safe to human, and environmental friendly [13, 14]. Sun et al. [15–18] have developed N-halamine-modified polymers by grafting method, and it is found the method has been well studied due to the short reaction time, continuous production, and easy industrialization [19, 20]. The modified polymers were then fabricated into nanofibers with the diameter ranging from 100 to 550 nm through an immiscible blending extrusion process and exhibited powerful antibacterial properties. Because of the tedious fabrication process and exceptionally high filtration resistance, the application prospect is limited.Hitherto, PP melt-blown nonwovens are widely used as filter materials because of their high surface area, small pore size distribution, high filtration efficiency, and low pressure drop [21]. Moreover, PP melt-blown technology has the advantages of high output, low cost, and short process [22]. The overall propose of this study was to develop a bifunctional melt-blown fiber filter combining antibacterial and air filtration abilities. Herein, an N-halamine precursor, 2,4-diamino-6-diallylamino-1,3,5-triazine (NDAM), was grafted onto PP using reactive extrusion, and the grafting effect of PP-g-NDAM polymers was characterized by approaches of nitrogen analysis, Fourier transform infrared spectroscopy (FTIR), and thermogravimetric analysis (TG). Then PP-g-NDAM resins were fabricated into nonwovens by melt-blown technology. After chlorination of the as-prepared nonwovens that converted the halamine precursor structures to antibacterial moieties, and corona charging treatment, the new PP-g-NDAM melt-blown filter materials showed a high filtration efficiency with low pressure drop and a potent antibacterial effect against Escherichia coli (E. coli) after short contact times, which has the potential and promising application capabilities in the filtration industry.


## 2. Materials and Methods

### 2.1. Materials

Polypropylene resins (PP, melt flow index: 1500) were purchased from Dawn Co. (Shandong Province, China), 2,4-diamino-6-diallylamino-1,3,5-triazine (NDAM) monomer was obtained from TCI (Portland, OR), and dicumyl initiator (DCP) was obtained from China National Pharmaceutical Group Co. (Beijing, China). Acetone and toluene were used in the purification process, sodium hypochlorite was used for chlorination, and potassium iodide and sodium thiosulfate were used to titrate the active chlorine content. All chemicals used in this research were purchased from China Chemical Reagent Company and employed without further purification.


### 2.2. Synthesis of PP-g-NDAM Polymer

The PP-g-NDAM polymer was produced by grafting the PP with NDAM monomers using reactive extrusion. As shown in Figure1, the PP resins used in this study were predried in an incubator at 60°C for 12 h. 100 g of PP was thoroughly mixed with different amounts of NDAM monomer (i.e., 8, 9, and 10 g) and DCP initiator (i.e., 0.4, 0.5, 0.6, and 0.7 g). All reactants were dry-mixed together for 20 min and then poured fast (<10 s) into a twin-screw extruder (Model MIC 18/GL 30D, Nurnberg, Germany). The feeding and screw speeds were controlled as 20 rpm and 30 rpm, respectively. The temperatures of the screw extruder from feeder to the extrusion were set as 150, 165, 170, 175, 180, 175, and 160°C, respectively. After the reaction is done, the as-prepared polymeric streams were frozen in a cooling water bath and were granulated into particles with a length of less than 10 mm.Figure 1
Schematic diagram of the reactive extrusion process and granulation of NDAM monomers grafted onto PP polymers.In the initial stage of the melt graft polymerization, the peroxide initiator DCP thermally decomposed to initial radicals after entering the twin-screw extruder, which could capture the hydrogen atoms from the tertiary carbon atoms of the PP polymer backbone to form PP macromolecular radicals. Part of the macromolecular radical could initialize the grafting polymerization of NDAM monomer onto the backbones to create desired grafted PP. And the other part undergoesβ-scission to form secondary radicals, which can still react with monomers [23], as shown in Scheme 1. Moreover, when the initial monomer concentration increased, this NDAM monomer that grafted onto PP backbones may react with more monomer molecules, and such a process may contribute to longer chain branches in PP molecules [24].Scheme 1
Grafting reaction of PP with NDAM in the reactive extrusion process.


### 2.3. Preparation of Melt-Blown Nonwovens

Generally, the fiber webs manufactured by 100 wt.% grafted PP showed a tough hand feeling. Based on this concern and in order to improve the quality of the melt-blown nonwovens, the as-prepared PP-g-NDAM with the highest grafting efficiency was selected to mix with the pristine PP at different weight ratios (i.e., the weight percentage of the PP-g-NDAM was set to 0 wt.%, 40 wt.%, 70 wt.%, and 100 wt.%). Then, the PP-g-NDAM/PP mixtures were extruded into the melt-blown device (see Figure2). During the melt-blown process, the solid PP-g-NDAM/PP resins were firstly supplied into the screw extruder through a hopper, and the resin was gradually melted by the treatment of the heating screw and extruded out through the polymer orifice. Then, the extruded polymer stream was attenuated into microfibers by the high-velocity hot air. In the meantime, the same air streams deliver the fiber to the collector, and the bonding took place at the fiber-to-fiber contact points. Finally, the fibers were cooled at room temperature to form the nonwoven. The technological parameters applied in the melt-blown process were set as follows. The length-to-diameter ratio of screw extruder was 35 : 1, and the screw extruder was heated in six separately regions; correspondingly, the temperature of the six parts of the screw extruder were maintained to 190, 200, 215, 220, 220, and 225°C. It is equal to that the temperature of the extruded polymer melt was 225°C. Air with a pressure of 0.4 MPa and a temperature of 235°C was applied to the melt-blown spinneret. For the structure of the spinneret, the apex angle of the air plates was 60°, and the diameter of the polymer orifice was 0.5 mm. All the microfibrous nonwovens were collected on the rotating roller, and the minimum die-to-collector distance (DCD) was 300 mm.Figure 2
Schematic diagram of the grafted PP melt-blown nonwovens process.Notably, to improve the filtration performance of the melt-blown nonwovens, corona charging treatment was commonly applied to eject electrostatic charges into the polymeric fibers. Electret melt-blown nonwovens have been proved to be a desired material to filtrate fine particulate matter due to the electrostatic force, which can significantly increase the filtration efficiency without increasing the pressure drop. The corona charging apparatus used in this study has been described in detail in the previous paper [25]. Briefly, it consists of a high-voltage power supplier, an array of needles, and a copper holder. The as-prepared nonwovens were placed 10 cm underneath the copper holder to charge for 30 s under a high voltage of 18 kV.


### 2.4. Antibacterial Treatment of Melt-Blown Nonwovens

The anticipated antibacterial properties were carried out by the chlorination reaction, which can change the -NH2 to -NHCl. Refer to the process of chlorination reaction, the PP-g-NDAM melt-blown nonwovens were immersed in dilute chlorine bleach (ca. 2500 mg/L available chlorine) for 1 h at room temperature, and the pH was adjusted to 7 by diluted sulfuric acid. Then, the melt-blown nonwovens were washed thoroughly with excess amounts of distilled water and dried at 40°C for 6 h. As shown in Figure 3, the antibacterial properties of the PP-g-NDAM melt-blown nonwovens were endowed by the active chlorine with highly oxidizing. The active chlorine has the function of destroying or inhibiting the metabolic process of bacteria [26, 27]. It was noted that this antibacterial process accompanied by the reversed conversion of -NHCl into -NH2. However, the antibacterial properties of the PP-g-NDAM melt-blown nonwovens could be rechargeable by the repeated chlorine bleaching process [28, 29].Figure 3
Simplified illustration of chlorination and antibacterial mechanism of the grafted melt-blown nonwoven.


### 2.5. Grafting Effect Measurements

As described in Scheme1, during the grafting process, the NDAM monomer was successfully grafted onto PP backbones. In order to remove the unreacted NDAM monomers, 2 g of the PP-g-NDAM resins was dissolved in 50 mL of hot toluene for 30 min, and then the hot solution was dropped into 200 mL of acetone at room temperature. The precipitated PP-g-NDAM powders were subsequently separated by filtration and washed several times with acetone. Finally, the as-received PP-g-NDAM powders were dried in a vacuum oven at a temperature of 60°C for 12 h.The grafting effect was then determined by FTIR, TGA, and nitrogen elemental analysis. As a control group, the pristine PP resins were also used for such measurements.The FTIR was used to characterize the functional groups of the materials. The samples and the potassium bromide powder were mixed and compressed into pellet to be analyzed by Bruker Tensor 27 Spectrometer in TR mode. The spectral range is from 400 to 4000 cm−1 with 4 cm−1 resolution, and the scanning times were 64 cm−1.TGA (NETZSCH model 209 F1) was applied to test the thermal properties of the materials. The testing was performed by heating samples up to 600°C with a heating rate of 10°C/min under a steady nitrogen flow.Vario EL III (Elementar, Germany) elemental analyzer was also used to characterize the grafting level. The analyzer comprises a combustion section, a thermal conductivity cell detection system, and a data analysis system. The materials used for testing were entirely burned and decomposed at high temperature, where composition elements were converted into their oxidation state. The mixed gas carried by helium gas enters the adsorption and desorption column; after that, the gas components were separated and the content of N in the sample was continuously detected by a thermal conductivity detector (TCD). Since the nitrogen content was obtained, the grafting degree (GD) and grafting efficiency (GE) were calculated from equation (1) and (2):(1)GD=CNCN′×MPPMPP+MDCP+MNDAM×100%,where CN is the nitrogen content (wt.%) of the grafted sample and CN′ is the nitrogen content (wt.%) of the NDAM monomer. MPP, MDCP, and MNDAM are the weight of reactants (g).(2)GE=MNDAM′MNDAM×100%,where MNDAM′ (g) is the weight of the grafted NDAM in the products. MNDAM (g) is the amount of NDAM monomers used in the grafting polymerization.


### 2.6. Melt-Blown Nonwoven Structure and Filtration Efficiency (FE) Measurements

Surface morphology of the melt-blown nonwovens was observed by using JEOL, JSM-IT300A analytical scanning electron microscope (SEM) after a thin AU-Pd layer was sputter-coated on samples. The fiber diameter was measured by the Image-Pro Plus software. The average diameter was calculated by at least 100 measured diameters. Moreover, the pore size of the melt-blown nonwovens was characterized by a capillary flow porometer (CFP-1100AI, Porous Materials Inc., USA) based on the bubble point test.The filtration efficiency (FE) of melt-blown nonwovens was tested by an automatic filter tester (Model 8130, TSI Inc., USA), which can generate sodium chloride (NaCl) aerosol with a mean particle size of 0.26μm at the geometric standard deviation of 1.86. The particle size distribution of the aerosol ranges from 0.1∼2 μm. The aerosol particles passed through the samples with a valid test area of 100 cm2 at the flow rate of 85 L/min. Each sample was tested three times to reduce random error. The air pressure drop for the nonwovens was measured by a flow gauge and two electronic pressure transmitters. Filtration efficiency (FE) was calculated as follows:(3)FE%=1−CdCu×100,where Cd is the aerosol concentration of the downstream side of the respirator filter and Cu is the concentration of the challenge aerosol of the upstream side.


### 2.7. Active Chlorine Content Measurement

As shown in Figure3, the anticipated antibacterial properties were carried out by converting the -NH2 to -NHCl. Therefore, the active chlorine content was an indicator for quantifying the antibacterial effect. It was verified that even the polymer materials contained a tiny amount of 0.2 wt.‰ active chlorine. It still shows a strong bactericidal property [30]. The active chlorine content was measured by the method of iodometric/thiosulfate titration. Around 0.15 g of the material was weighed and then mixed with 5 mL of deionized water, 0.2 g of potassium iodide, and 1 mL of 0.5% starch solution. Initially, due to the starchy environment, the solution exhibited a dark blue color when touched with the titrated iodine. The sodium thiosulfate solution was continuously titrated until the dark blue color disappeared. Meanwhile, the volume of sodium thiosulfate solution used in titration was recorded. Each PP-g-NDAM melt-blown nonwoven was titrated three times under the same experimental conditions. The weight ration of the chlorine content (Cl+ ‰) can be determined by the following equation:(4)Cl+‰=35.45×N×V2×W×1000,where Cl+ ‰ is the weight percentage of available active chlorine of the samples, N and V are the normality (equiv./L) and volume (L) of the titrant sodium thiosulfate, respectively, and W is the weight of the grafted PP melt-blown material (g).In order to investigate the regenerability of the bactericidal functional group of -NHCl bond in the grafted melt-blown nonwoven, around 0.15 g of the nonwovens was soaked in sodium thiosulfate solution for 30 min to conduct a simulation study of the loss of -NHCl bond during sterilization. Then, the materials were washed and dried, and the -NHCl bond could be regenerated by soaking the material in dilute chlorine bleach in 1 h. After repeating the reduction and chlorination working cycles by 10 times, the active chlorine content was measured by iodometric/thiosulfate titration.


### 2.8. Antibacterial Property Measurement

The antibacterial properties of the chlorinated grafted melt-blown nonwovens were examined by the sterilization experiment referring toE. coli (K-12, a Gram-negative bacterium). This experiment was under the standard of the AATCC test method 100–1999. Pristine PP melt-blown nonwoven was used for a blank experiment. The melt-blown nonwovens were cut into small pieces (4 × 4 cm), and two swatches of the grafted PP melt-blown nonwovens were placed in a sterilized container. 1 mL of E. coli suspension containing 105∼106 colony-forming units (CFU)/mL was dropped onto the surfaces of the melt-blown nonwovens, and a sterilized 50 mL beaker was placed onto the top of the nonwovens to keep adequate contact of the microbial suspension with the nonwovens. The inoculated controls or the grafted PP melt-blown nonwovens were placed into 100 mL of distilled water after different contact times. The mixture was shaken vigorously for 10 min. An aliquot of the microbial suspension was removed from the mixture and then serially diluted, and 100 μL of each dilution was placed onto a nutrient agar plate and incubated at 37°C for 24 h. The bacterial reduction was calculated according to the following equation:(5)percentage reduction of bacteria%=A−BB×100,where A and B are the number of bacteria counted from control and grafted PP melt-blown nonwovens, respectively. In order to investigate the active chlorine loss during the antibacterial test, after 30 min contact with bacteria, the tested melt-blown nonwovens were washed 3 times with distilled water and dried in vacuum at 40°C for 6 h. The iodometric/thiosulfate titration method was used to measure the active chlorine content after the antibacterial test.


## 2.1. Materials

Polypropylene resins (PP, melt flow index: 1500) were purchased from Dawn Co. (Shandong Province, China), 2,4-diamino-6-diallylamino-1,3,5-triazine (NDAM) monomer was obtained from TCI (Portland, OR), and dicumyl initiator (DCP) was obtained from China National Pharmaceutical Group Co. (Beijing, China). Acetone and toluene were used in the purification process, sodium hypochlorite was used for chlorination, and potassium iodide and sodium thiosulfate were used to titrate the active chlorine content. All chemicals used in this research were purchased from China Chemical Reagent Company and employed without further purification.


## 2.2. Synthesis of PP-g-NDAM Polymer

The PP-g-NDAM polymer was produced by grafting the PP with NDAM monomers using reactive extrusion. As shown in Figure1, the PP resins used in this study were predried in an incubator at 60°C for 12 h. 100 g of PP was thoroughly mixed with different amounts of NDAM monomer (i.e., 8, 9, and 10 g) and DCP initiator (i.e., 0.4, 0.5, 0.6, and 0.7 g). All reactants were dry-mixed together for 20 min and then poured fast (<10 s) into a twin-screw extruder (Model MIC 18/GL 30D, Nurnberg, Germany). The feeding and screw speeds were controlled as 20 rpm and 30 rpm, respectively. The temperatures of the screw extruder from feeder to the extrusion were set as 150, 165, 170, 175, 180, 175, and 160°C, respectively. After the reaction is done, the as-prepared polymeric streams were frozen in a cooling water bath and were granulated into particles with a length of less than 10 mm.Figure 1
Schematic diagram of the reactive extrusion process and granulation of NDAM monomers grafted onto PP polymers.In the initial stage of the melt graft polymerization, the peroxide initiator DCP thermally decomposed to initial radicals after entering the twin-screw extruder, which could capture the hydrogen atoms from the tertiary carbon atoms of the PP polymer backbone to form PP macromolecular radicals. Part of the macromolecular radical could initialize the grafting polymerization of NDAM monomer onto the backbones to create desired grafted PP. And the other part undergoesβ-scission to form secondary radicals, which can still react with monomers [23], as shown in Scheme 1. Moreover, when the initial monomer concentration increased, this NDAM monomer that grafted onto PP backbones may react with more monomer molecules, and such a process may contribute to longer chain branches in PP molecules [24].Scheme 1
Grafting reaction of PP with NDAM in the reactive extrusion process.


## 2.3. Preparation of Melt-Blown Nonwovens

Generally, the fiber webs manufactured by 100 wt.% grafted PP showed a tough hand feeling. Based on this concern and in order to improve the quality of the melt-blown nonwovens, the as-prepared PP-g-NDAM with the highest grafting efficiency was selected to mix with the pristine PP at different weight ratios (i.e., the weight percentage of the PP-g-NDAM was set to 0 wt.%, 40 wt.%, 70 wt.%, and 100 wt.%). Then, the PP-g-NDAM/PP mixtures were extruded into the melt-blown device (see Figure2). During the melt-blown process, the solid PP-g-NDAM/PP resins were firstly supplied into the screw extruder through a hopper, and the resin was gradually melted by the treatment of the heating screw and extruded out through the polymer orifice. Then, the extruded polymer stream was attenuated into microfibers by the high-velocity hot air. In the meantime, the same air streams deliver the fiber to the collector, and the bonding took place at the fiber-to-fiber contact points. Finally, the fibers were cooled at room temperature to form the nonwoven. The technological parameters applied in the melt-blown process were set as follows. The length-to-diameter ratio of screw extruder was 35 : 1, and the screw extruder was heated in six separately regions; correspondingly, the temperature of the six parts of the screw extruder were maintained to 190, 200, 215, 220, 220, and 225°C. It is equal to that the temperature of the extruded polymer melt was 225°C. Air with a pressure of 0.4 MPa and a temperature of 235°C was applied to the melt-blown spinneret. For the structure of the spinneret, the apex angle of the air plates was 60°, and the diameter of the polymer orifice was 0.5 mm. All the microfibrous nonwovens were collected on the rotating roller, and the minimum die-to-collector distance (DCD) was 300 mm.Figure 2
Schematic diagram of the grafted PP melt-blown nonwovens process.Notably, to improve the filtration performance of the melt-blown nonwovens, corona charging treatment was commonly applied to eject electrostatic charges into the polymeric fibers. Electret melt-blown nonwovens have been proved to be a desired material to filtrate fine particulate matter due to the electrostatic force, which can significantly increase the filtration efficiency without increasing the pressure drop. The corona charging apparatus used in this study has been described in detail in the previous paper [25]. Briefly, it consists of a high-voltage power supplier, an array of needles, and a copper holder. The as-prepared nonwovens were placed 10 cm underneath the copper holder to charge for 30 s under a high voltage of 18 kV.


## 2.4. Antibacterial Treatment of Melt-Blown Nonwovens

The anticipated antibacterial properties were carried out by the chlorination reaction, which can change the -NH2 to -NHCl. Refer to the process of chlorination reaction, the PP-g-NDAM melt-blown nonwovens were immersed in dilute chlorine bleach (ca. 2500 mg/L available chlorine) for 1 h at room temperature, and the pH was adjusted to 7 by diluted sulfuric acid. Then, the melt-blown nonwovens were washed thoroughly with excess amounts of distilled water and dried at 40°C for 6 h. As shown in Figure 3, the antibacterial properties of the PP-g-NDAM melt-blown nonwovens were endowed by the active chlorine with highly oxidizing. The active chlorine has the function of destroying or inhibiting the metabolic process of bacteria [26, 27]. It was noted that this antibacterial process accompanied by the reversed conversion of -NHCl into -NH2. However, the antibacterial properties of the PP-g-NDAM melt-blown nonwovens could be rechargeable by the repeated chlorine bleaching process [28, 29].Figure 3
Simplified illustration of chlorination and antibacterial mechanism of the grafted melt-blown nonwoven.


## 2.5. Grafting Effect Measurements

As described in Scheme1, during the grafting process, the NDAM monomer was successfully grafted onto PP backbones. In order to remove the unreacted NDAM monomers, 2 g of the PP-g-NDAM resins was dissolved in 50 mL of hot toluene for 30 min, and then the hot solution was dropped into 200 mL of acetone at room temperature. The precipitated PP-g-NDAM powders were subsequently separated by filtration and washed several times with acetone. Finally, the as-received PP-g-NDAM powders were dried in a vacuum oven at a temperature of 60°C for 12 h.The grafting effect was then determined by FTIR, TGA, and nitrogen elemental analysis. As a control group, the pristine PP resins were also used for such measurements.The FTIR was used to characterize the functional groups of the materials. The samples and the potassium bromide powder were mixed and compressed into pellet to be analyzed by Bruker Tensor 27 Spectrometer in TR mode. The spectral range is from 400 to 4000 cm−1 with 4 cm−1 resolution, and the scanning times were 64 cm−1.TGA (NETZSCH model 209 F1) was applied to test the thermal properties of the materials. The testing was performed by heating samples up to 600°C with a heating rate of 10°C/min under a steady nitrogen flow.Vario EL III (Elementar, Germany) elemental analyzer was also used to characterize the grafting level. The analyzer comprises a combustion section, a thermal conductivity cell detection system, and a data analysis system. The materials used for testing were entirely burned and decomposed at high temperature, where composition elements were converted into their oxidation state. The mixed gas carried by helium gas enters the adsorption and desorption column; after that, the gas components were separated and the content of N in the sample was continuously detected by a thermal conductivity detector (TCD). Since the nitrogen content was obtained, the grafting degree (GD) and grafting efficiency (GE) were calculated from equation (1) and (2):(1)GD=CNCN′×MPPMPP+MDCP+MNDAM×100%,where CN is the nitrogen content (wt.%) of the grafted sample and CN′ is the nitrogen content (wt.%) of the NDAM monomer. MPP, MDCP, and MNDAM are the weight of reactants (g).(2)GE=MNDAM′MNDAM×100%,where MNDAM′ (g) is the weight of the grafted NDAM in the products. MNDAM (g) is the amount of NDAM monomers used in the grafting polymerization.


## 2.6. Melt-Blown Nonwoven Structure and Filtration Efficiency (FE) Measurements

Surface morphology of the melt-blown nonwovens was observed by using JEOL, JSM-IT300A analytical scanning electron microscope (SEM) after a thin AU-Pd layer was sputter-coated on samples. The fiber diameter was measured by the Image-Pro Plus software. The average diameter was calculated by at least 100 measured diameters. Moreover, the pore size of the melt-blown nonwovens was characterized by a capillary flow porometer (CFP-1100AI, Porous Materials Inc., USA) based on the bubble point test.The filtration efficiency (FE) of melt-blown nonwovens was tested by an automatic filter tester (Model 8130, TSI Inc., USA), which can generate sodium chloride (NaCl) aerosol with a mean particle size of 0.26μm at the geometric standard deviation of 1.86. The particle size distribution of the aerosol ranges from 0.1∼2 μm. The aerosol particles passed through the samples with a valid test area of 100 cm2 at the flow rate of 85 L/min. Each sample was tested three times to reduce random error. The air pressure drop for the nonwovens was measured by a flow gauge and two electronic pressure transmitters. Filtration efficiency (FE) was calculated as follows:(3)FE%=1−CdCu×100,where Cd is the aerosol concentration of the downstream side of the respirator filter and Cu is the concentration of the challenge aerosol of the upstream side.


## 2.7. Active Chlorine Content Measurement

As shown in Figure3, the anticipated antibacterial properties were carried out by converting the -NH2 to -NHCl. Therefore, the active chlorine content was an indicator for quantifying the antibacterial effect. It was verified that even the polymer materials contained a tiny amount of 0.2 wt.‰ active chlorine. It still shows a strong bactericidal property [30]. The active chlorine content was measured by the method of iodometric/thiosulfate titration. Around 0.15 g of the material was weighed and then mixed with 5 mL of deionized water, 0.2 g of potassium iodide, and 1 mL of 0.5% starch solution. Initially, due to the starchy environment, the solution exhibited a dark blue color when touched with the titrated iodine. The sodium thiosulfate solution was continuously titrated until the dark blue color disappeared. Meanwhile, the volume of sodium thiosulfate solution used in titration was recorded. Each PP-g-NDAM melt-blown nonwoven was titrated three times under the same experimental conditions. The weight ration of the chlorine content (Cl+ ‰) can be determined by the following equation:(4)Cl+‰=35.45×N×V2×W×1000,where Cl+ ‰ is the weight percentage of available active chlorine of the samples, N and V are the normality (equiv./L) and volume (L) of the titrant sodium thiosulfate, respectively, and W is the weight of the grafted PP melt-blown material (g).In order to investigate the regenerability of the bactericidal functional group of -NHCl bond in the grafted melt-blown nonwoven, around 0.15 g of the nonwovens was soaked in sodium thiosulfate solution for 30 min to conduct a simulation study of the loss of -NHCl bond during sterilization. Then, the materials were washed and dried, and the -NHCl bond could be regenerated by soaking the material in dilute chlorine bleach in 1 h. After repeating the reduction and chlorination working cycles by 10 times, the active chlorine content was measured by iodometric/thiosulfate titration.


## 2.8. Antibacterial Property Measurement

The antibacterial properties of the chlorinated grafted melt-blown nonwovens were examined by the sterilization experiment referring toE. coli (K-12, a Gram-negative bacterium). This experiment was under the standard of the AATCC test method 100–1999. Pristine PP melt-blown nonwoven was used for a blank experiment. The melt-blown nonwovens were cut into small pieces (4 × 4 cm), and two swatches of the grafted PP melt-blown nonwovens were placed in a sterilized container. 1 mL of E. coli suspension containing 105∼106 colony-forming units (CFU)/mL was dropped onto the surfaces of the melt-blown nonwovens, and a sterilized 50 mL beaker was placed onto the top of the nonwovens to keep adequate contact of the microbial suspension with the nonwovens. The inoculated controls or the grafted PP melt-blown nonwovens were placed into 100 mL of distilled water after different contact times. The mixture was shaken vigorously for 10 min. An aliquot of the microbial suspension was removed from the mixture and then serially diluted, and 100 μL of each dilution was placed onto a nutrient agar plate and incubated at 37°C for 24 h. The bacterial reduction was calculated according to the following equation:(5)percentage reduction of bacteria%=A−BB×100,where A and B are the number of bacteria counted from control and grafted PP melt-blown nonwovens, respectively. In order to investigate the active chlorine loss during the antibacterial test, after 30 min contact with bacteria, the tested melt-blown nonwovens were washed 3 times with distilled water and dried in vacuum at 40°C for 6 h. The iodometric/thiosulfate titration method was used to measure the active chlorine content after the antibacterial test.


## 3. Results and Discussion

### 3.1. The Effect of Mixing Weight Ratio on Grafting

The effects of the monomer and the initiator content on the grafting effect of NDAM were studied. As mentioned above (equation (1) and (2)), the grafting level of NDAM onto PP was confirmed by the GD and GE results. As shown in Table 1, when the DCP content was set to 0.4 g, the GD results increased from 2.51 wt.% to 3.34 wt.% with the increase of NDAM from 8 g to 10 g. Notably, a similar trend is found for other weight variations of DCP (i.e., 0.5, 0.6, and 0.7 g). That is because when the content of DCP was constant, the amount of initial free radicals generated by thermal decomposition was relatively fixed, and increasing the NDAM content could enhance the reaction between NDAM monomer and PP macromolecular radicals, resulting in the increasing GD and GE values of NDAM. However, the concentration of macromolecules generated per unit time was limited when the monomer content reached a specific value, which made GD to increase slowly and GE to decrease. In other words, using too much NDAM could lead to more waste of monomer reactants.Table 1
Composition, grafting degree, and grafting efficiency of modified samples.
Sample code
PP (g)
NDAM (g)
DCP (g)
GD (wt.%)
GE (%)
A1
100
8
0.4
2.51
34.03
A2
100
8
0.5
3.07
41.69
A3
100
8
0.6
3.16
42.92
A4
100
8
0.7
2.91
39.85
B1
100
9
0.4
2.98
37.24
B2
100
9
0.5
3.54
46.05
B3
100
9
0.6
4.61
56.13
B4
100
9
0.7
4.45
53.95
C1
100
10
0.4
3.34
36.78
C2
100
10
0.5
4.01
44.39
C3
100
10
0.6
4.85
53.71
C4
100
10
0.7
4.72
52.23From another point of view, when the content of NDAM was 8 g, the GD increased to a peak value when the weight of DCP was 0.6 g. However, GD decreased with further increase of DCP. A similar tendency could be found for the other weight of NDAM (i.e., 9 and 10 g). Moreover, the index of GE has the same tendency as GD when keeping NDAM constant. The results may be due to the simultaneous occurrence of graft polymerization and degradation reaction in the process of reactive extrusion, and the initial free radical concentration produced by thermal decomposition increased with the increase of the DCP content, which enhanced the chance of collision between NDAM monomer and PP macromolecular free radicals. However, the excessive content of the DCP initiator could induce more polymer degradation, resulting in the reduction of tertiary C-H bonds and the decrease of GD and GE. It is obvious to see that the maximum GD was 4.85 wt.% when the content of NDAM was 10 g and DCP was 0.6 g, while the maximum GE was 56.13% when the content of NDAM was 9 g and DCP was 0.6 g.The successful graft polymerization for adding NDAM monomer onto PP was confirmed with FTIR spectroscopic analysis. The FTIR spectra of pristine PP and the grafted PP are shown in Figure4. Compared with the spectrum of the pristine PP, all the grafted materials showed two additional characteristic peaks around 1615 and 1558 cm−1 which were attributed to the bending deformations of amino-azine and the stretching vibration of planar triazine ring, respectively [31]. Given that the unreacted monomer and homopolymers have been removed by the treatment in hot toluene and acetone, the spectra can confirm that the NDAM monomer was successfully grafted onto the PP polymer chains. In addition, the intensity of characteristic peaks increased with an increase in the GD of NDAM monomer.Figure 4
FTIR spectra of pristine PP and grafted PP samples prepared with different compositions, A3: [NDAM] = 8 g and [DCP] = 0.6 g, B3: [NDAM] = 9 g and [DCP] = 0.6 g, and C3: [NDAM] = 10 g and [DCP] = 0.6 g.Figure5 shows the thermogravimetric analysis of the pristine PP and the grafted PP (samples A3, B3, and C3) with different NDAM contents. The TG curves of the grafted PP samples shifted slightly to a higher temperature, and the temperature of pristine PP with 10% thermal weight loss was 415°C, whereas the temperature raised to 426°C for those grafted PP polymers, and the residual mass of the grafted PP was also higher than pristine PP. The TGA results indicated that the thermal stability of the grafted PP polymers had been improved after the grafting process. This phenomenon may be contributed to the triazine ring structure in the NDAM monomer, which could improve the thermal stability of PP.Figure 5
TG and DTG (inset) profiles for pristine PP and grafted PP samples prepared with different compositions.


### 3.2. Structure and Filtration Property of the Grafted Melt-Blown Nonwovens

The sample B3 with the highest grafting efficiency was selected for granulation, and then the obtained PP-g-NDAM and pristine PP resins were thoroughly mixed in different weight ratios to fabricate melt-blown nonwovens with a basic weight of 40 ± 3 g/m2. Figure 6 shows the morphologies of the melt-blown nonwovens characterized by SEM. A randomly arranged three-dimensional microporous structure could be observed on the received melt-blown nonwovens. Moreover, the large diameter distribution is caused by the unstable attenuating effect of air (airflow is turbulence). Figure 6(a) shows a smooth surface on pristine fibers. However, as shown in Figures 6(b)–6(d), when increasing the concentration of PP-g-NDAM, some spots appeared on the fiber surface.Figure 6
SEM images of melt-blown nonwovens containing (a) 0 wt.%, (b) 40 wt.%, (c) 70 wt.%, and (d) 100 wt.% PP-g-NDAM. (e) Fiber average diameter and (f) pore size distribution curves.
(a)
(b)
(c)
(d)
(e)
(f)Figure6(e) shows the effect of PP-g-NDAM concentration on the diameter of the melt-blown fibers. The fiber diameter was increased from 3.16 ± 0.65 μm to 4.69 ± 1.39 μm with the increase of the concentration of PP-g-NDAM. In addition, the concentration of PP-g-NDAM also played a significant role in the pore size distribution of the as-received melt-blown nonwovens. As shown in Figure 6(f), the unimodal pore size distribution was shown in each case, and the peaks shifted in sequence upon an increase in the concentration of PP-g-NDAM. Moreover, the distribution peaks broadened with the increase in the concentration of PP-g-NDAM, which could be attributed to the branching reaction of PP chains with the introduction of NDAM. Typically, PP macromolecules with long-chain branching lead to an increase in melt viscosity. The high melt viscosity would hinder fiber stretching in the hot-speed drawing process, resulting in an increase of fiber diameter, pore size as well as the number of spots.In order to assess the capability in air filtration, the filtration efficiency against NaCl aerosols of the grafted melt-blown nonwovens was investigated. Figure7(a) shows the filtration efficiency and the pressure drop of the grafted melt-blown nonwovens with different concentrations of PP-g-NDAM. It indicates that the process of corona charging is beneficial to improve the filtration performance. After corona charging, the filtration efficiency of 40 wt.% PP-g-NDAM melt-blown nonwoven dramatically increased from 37.64% to 85.88% with no striking change in pressure drop. The electrostatic attraction is responsible for the boost in filtration performance, as the NaCl aerosols are mostly charged and adsorbed on the fibers when they approached the nonwovens [32, 33]. Figure 7(a) also shows the same trends in uncharged nonwovens because the filtration efficiency and pressure drop of the grafted nonwovens gradually decreased with the increase in the concentration of PP-g-NDAM, which is ascribed to the construction of larger fiber diameters and pore sizes.Figure 7
(a) Filtration efficiency and pressure drop and (b) quality factor value of melt-blown nonwovens with different concentrations of PP-g-NDAM.
(a)
(b)Quality factor (QF) is usually used to characterize the filtration performance of filter materials [34–37], and it could be calculated by the following equation:(6)QF=−ln1−ηΔp,where η is the filtration efficiency and Δp is the pressure drop. As shown in Figure 7(b), the QF values of all samples before corona charging are less than 0.0120 Pa−1 because the filtration efficiency of each sample was relatively low. After charging, the filtration efficiency of each sample significantly increases, whereas the pressure drop remains unchanged; as a result, a high QF value of the target sample is obtained after corona charging treatment. The QF of pristine PP melt-blown nonwoven reaches to 0.0504 ± 0.0015 Pa−1, and the QF of the modified melt-blown nonwovens decreases gradually with the increase of the PP-g-NDAM concentration, and the QF of 100 wt.% PP-g-NDAM melt-blown nonwoven reaches to the minimum value, i.e., 0.0348 ± 0.0011 Pa−1. Besides, Figure 7 further indicates that the corona charging could effectively improve the filtration efficiency of the melt-blown nonwovens without increasing the pressure drop.


### 3.3. Active Chlorine Content

The content of active chlorine was used to assess the antibacterial ability of the melt-blown nonwovens, and a higher content of the active chlorine indicates a better antibacterial ability of the nonwovens [38]. Figure 8(a) shows the active chlorine content of melt-blown nonwovens containing 0, 40, 70, and 100 wt.% PP-g-NDAM after chlorination. It could be seen that no active chlorine was formed on the pristine PP melt-blown nonwovens, even after the chlorination treatment. That is because there is no chemical modification site on PP surface to bind active chlorine, which results in easy wash-off of the unreacted chlorine after chlorination. However, the other melt-blown nonwovens containing PP-g-NDAM exhibited sufficient active chlorine contents. The active chlorine content of the melt-blown nonwovens with the PP-g-NDAM concentration of 40, 70, and 100 wt.% was 0.309 ± 0.012‰, 0.409 ± 0.024‰, and 0.463 ± 0.031‰, respectively. It could be found that the content of active chlorine increased with the increase of the PP-g-NDAM concentration. This is because the nonwovens containing a higher PP-g-NDAM concentration could provide more -NH2 groups, which is essential for chlorination to form -NHCl (see Scheme 1 and Figure 3). However, the increasing rate of active chlorine slows down with the increase of the PP-g-NDAM concentration, and due to the N-halamine transformation on the fiber surface, the specific surface area of fibers will be decreased with the average diameter of melt-blown fibers getting larger. It could be also verified from Figure 6(e) that the fiber diameter was increased with the increase of the PP-g-NDAM concentration. Furthermore, in the antibacterial test, after 30 min the active chlorine content reduced significantly for PP-g-NDAM melt-blown nonwovens (Figure 8(a)). Due to the consumption of active chlorine in the antibacterial process, the active chlorine content is finally decreased to 0.103 ± 0.007‰, 0.172 ± 0.026‰, and 0.223 ± 0.030‰ for 40 wt.%, 70 wt.%, and 100 wt.% PP-g-NDAM melt-blown nonwovens, respectively.Figure 8
Active chlorine content of chlorinated melt-blown nonwovens with different concentrations of PP-g-NDAM (a) before and after antibacterial treatment and (b) after repeating the reduction and chlorination treatment for 10 times.
(a)
(b)As shown in Figure8(b), after repeating the reduction and chlorination treatment for 10 times, the active chlorine content of 40 wt.%, 70 wt.%, and 100 wt.% PP-g-NDAM melt-blown nonwovens decreases slightly by 3.35%, 3.13%, and 3.08%, respectively, indicating the good regeneration ability of the PP-g-NDAM melt-blown nonwovens. However, with the increase of regeneration times, the active chlorine content in the melt-blown nonwovens will gradually decrease according to the performance after 10 times of cycling (Figure 8(b)). This may be ascribed to the loss of the grafted antibacterial agent (NDAM) during chlorine bleaching treatment, which results in an insufficient regeneration of active chlorine.


### 3.4. Antibacterial Property of the Grafted Melt-Blown Nonwovens

The antibacterial results of melt-blown nonwovens containing different PP-g-NDAM concentrations are listed in Table2. The proliferated colonies of E. coli were observed on the pristine PP melt-blown nonwoven, while the grafted melt-blown nonwovens showed excellent antibacterial properties against E. coli. For the nonwovens containing 40 wt.% PP-g-NDAM, 95.35% and 99.99% of the bacteria were sterilized within 15 and 30 min, respectively. For the nonwovens containing 70 wt.% PP-g-NDAM, 99.99% of the bacteria were killed just within 15 min. However, the sterilization speed is no longer faster for the 100 wt.% PP-g-NDAM nonwovens, indicating that 70 wt.% PP-g-NDAM is sufficient for sterilizing the E. coli. Moreover, long-term stability of antibacterial properties was also investigated. After 10 days, the antibacterial properties of the samples show no significant change as all grafted melt-blown nonwovens could sterilize 99.99% of E. coli after a contact time of 30 min.Table 2
Antibacterial properties of grafted melt-blown samples againstE. coli after different contact times.
Concentration of PP-g-NDAM (wt.%)
Percentage reduction ofE. coli at different contact times (%)
15 min
30 min
60 min
40
95.35
99.99
99.999
70
99.99
99.999
99.999
100
99.99
99.999
99.999


## 3.1. The Effect of Mixing Weight Ratio on Grafting

The effects of the monomer and the initiator content on the grafting effect of NDAM were studied. As mentioned above (equation (1) and (2)), the grafting level of NDAM onto PP was confirmed by the GD and GE results. As shown in Table 1, when the DCP content was set to 0.4 g, the GD results increased from 2.51 wt.% to 3.34 wt.% with the increase of NDAM from 8 g to 10 g. Notably, a similar trend is found for other weight variations of DCP (i.e., 0.5, 0.6, and 0.7 g). That is because when the content of DCP was constant, the amount of initial free radicals generated by thermal decomposition was relatively fixed, and increasing the NDAM content could enhance the reaction between NDAM monomer and PP macromolecular radicals, resulting in the increasing GD and GE values of NDAM. However, the concentration of macromolecules generated per unit time was limited when the monomer content reached a specific value, which made GD to increase slowly and GE to decrease. In other words, using too much NDAM could lead to more waste of monomer reactants.Table 1
Composition, grafting degree, and grafting efficiency of modified samples.
Sample code
PP (g)
NDAM (g)
DCP (g)
GD (wt.%)
GE (%)
A1
100
8
0.4
2.51
34.03
A2
100
8
0.5
3.07
41.69
A3
100
8
0.6
3.16
42.92
A4
100
8
0.7
2.91
39.85
B1
100
9
0.4
2.98
37.24
B2
100
9
0.5
3.54
46.05
B3
100
9
0.6
4.61
56.13
B4
100
9
0.7
4.45
53.95
C1
100
10
0.4
3.34
36.78
C2
100
10
0.5
4.01
44.39
C3
100
10
0.6
4.85
53.71
C4
100
10
0.7
4.72
52.23From another point of view, when the content of NDAM was 8 g, the GD increased to a peak value when the weight of DCP was 0.6 g. However, GD decreased with further increase of DCP. A similar tendency could be found for the other weight of NDAM (i.e., 9 and 10 g). Moreover, the index of GE has the same tendency as GD when keeping NDAM constant. The results may be due to the simultaneous occurrence of graft polymerization and degradation reaction in the process of reactive extrusion, and the initial free radical concentration produced by thermal decomposition increased with the increase of the DCP content, which enhanced the chance of collision between NDAM monomer and PP macromolecular free radicals. However, the excessive content of the DCP initiator could induce more polymer degradation, resulting in the reduction of tertiary C-H bonds and the decrease of GD and GE. It is obvious to see that the maximum GD was 4.85 wt.% when the content of NDAM was 10 g and DCP was 0.6 g, while the maximum GE was 56.13% when the content of NDAM was 9 g and DCP was 0.6 g.The successful graft polymerization for adding NDAM monomer onto PP was confirmed with FTIR spectroscopic analysis. The FTIR spectra of pristine PP and the grafted PP are shown in Figure4. Compared with the spectrum of the pristine PP, all the grafted materials showed two additional characteristic peaks around 1615 and 1558 cm−1 which were attributed to the bending deformations of amino-azine and the stretching vibration of planar triazine ring, respectively [31]. Given that the unreacted monomer and homopolymers have been removed by the treatment in hot toluene and acetone, the spectra can confirm that the NDAM monomer was successfully grafted onto the PP polymer chains. In addition, the intensity of characteristic peaks increased with an increase in the GD of NDAM monomer.Figure 4
FTIR spectra of pristine PP and grafted PP samples prepared with different compositions, A3: [NDAM] = 8 g and [DCP] = 0.6 g, B3: [NDAM] = 9 g and [DCP] = 0.6 g, and C3: [NDAM] = 10 g and [DCP] = 0.6 g.Figure5 shows the thermogravimetric analysis of the pristine PP and the grafted PP (samples A3, B3, and C3) with different NDAM contents. The TG curves of the grafted PP samples shifted slightly to a higher temperature, and the temperature of pristine PP with 10% thermal weight loss was 415°C, whereas the temperature raised to 426°C for those grafted PP polymers, and the residual mass of the grafted PP was also higher than pristine PP. The TGA results indicated that the thermal stability of the grafted PP polymers had been improved after the grafting process. This phenomenon may be contributed to the triazine ring structure in the NDAM monomer, which could improve the thermal stability of PP.Figure 5
TG and DTG (inset) profiles for pristine PP and grafted PP samples prepared with different compositions.


## 3.2. Structure and Filtration Property of the Grafted Melt-Blown Nonwovens

The sample B3 with the highest grafting efficiency was selected for granulation, and then the obtained PP-g-NDAM and pristine PP resins were thoroughly mixed in different weight ratios to fabricate melt-blown nonwovens with a basic weight of 40 ± 3 g/m2. Figure 6 shows the morphologies of the melt-blown nonwovens characterized by SEM. A randomly arranged three-dimensional microporous structure could be observed on the received melt-blown nonwovens. Moreover, the large diameter distribution is caused by the unstable attenuating effect of air (airflow is turbulence). Figure 6(a) shows a smooth surface on pristine fibers. However, as shown in Figures 6(b)–6(d), when increasing the concentration of PP-g-NDAM, some spots appeared on the fiber surface.Figure 6
SEM images of melt-blown nonwovens containing (a) 0 wt.%, (b) 40 wt.%, (c) 70 wt.%, and (d) 100 wt.% PP-g-NDAM. (e) Fiber average diameter and (f) pore size distribution curves.
(a)
(b)
(c)
(d)
(e)
(f)Figure6(e) shows the effect of PP-g-NDAM concentration on the diameter of the melt-blown fibers. The fiber diameter was increased from 3.16 ± 0.65 μm to 4.69 ± 1.39 μm with the increase of the concentration of PP-g-NDAM. In addition, the concentration of PP-g-NDAM also played a significant role in the pore size distribution of the as-received melt-blown nonwovens. As shown in Figure 6(f), the unimodal pore size distribution was shown in each case, and the peaks shifted in sequence upon an increase in the concentration of PP-g-NDAM. Moreover, the distribution peaks broadened with the increase in the concentration of PP-g-NDAM, which could be attributed to the branching reaction of PP chains with the introduction of NDAM. Typically, PP macromolecules with long-chain branching lead to an increase in melt viscosity. The high melt viscosity would hinder fiber stretching in the hot-speed drawing process, resulting in an increase of fiber diameter, pore size as well as the number of spots.In order to assess the capability in air filtration, the filtration efficiency against NaCl aerosols of the grafted melt-blown nonwovens was investigated. Figure7(a) shows the filtration efficiency and the pressure drop of the grafted melt-blown nonwovens with different concentrations of PP-g-NDAM. It indicates that the process of corona charging is beneficial to improve the filtration performance. After corona charging, the filtration efficiency of 40 wt.% PP-g-NDAM melt-blown nonwoven dramatically increased from 37.64% to 85.88% with no striking change in pressure drop. The electrostatic attraction is responsible for the boost in filtration performance, as the NaCl aerosols are mostly charged and adsorbed on the fibers when they approached the nonwovens [32, 33]. Figure 7(a) also shows the same trends in uncharged nonwovens because the filtration efficiency and pressure drop of the grafted nonwovens gradually decreased with the increase in the concentration of PP-g-NDAM, which is ascribed to the construction of larger fiber diameters and pore sizes.Figure 7
(a) Filtration efficiency and pressure drop and (b) quality factor value of melt-blown nonwovens with different concentrations of PP-g-NDAM.
(a)
(b)Quality factor (QF) is usually used to characterize the filtration performance of filter materials [34–37], and it could be calculated by the following equation:(6)QF=−ln1−ηΔp,where η is the filtration efficiency and Δp is the pressure drop. As shown in Figure 7(b), the QF values of all samples before corona charging are less than 0.0120 Pa−1 because the filtration efficiency of each sample was relatively low. After charging, the filtration efficiency of each sample significantly increases, whereas the pressure drop remains unchanged; as a result, a high QF value of the target sample is obtained after corona charging treatment. The QF of pristine PP melt-blown nonwoven reaches to 0.0504 ± 0.0015 Pa−1, and the QF of the modified melt-blown nonwovens decreases gradually with the increase of the PP-g-NDAM concentration, and the QF of 100 wt.% PP-g-NDAM melt-blown nonwoven reaches to the minimum value, i.e., 0.0348 ± 0.0011 Pa−1. Besides, Figure 7 further indicates that the corona charging could effectively improve the filtration efficiency of the melt-blown nonwovens without increasing the pressure drop.


## 3.3. Active Chlorine Content

The content of active chlorine was used to assess the antibacterial ability of the melt-blown nonwovens, and a higher content of the active chlorine indicates a better antibacterial ability of the nonwovens [38]. Figure 8(a) shows the active chlorine content of melt-blown nonwovens containing 0, 40, 70, and 100 wt.% PP-g-NDAM after chlorination. It could be seen that no active chlorine was formed on the pristine PP melt-blown nonwovens, even after the chlorination treatment. That is because there is no chemical modification site on PP surface to bind active chlorine, which results in easy wash-off of the unreacted chlorine after chlorination. However, the other melt-blown nonwovens containing PP-g-NDAM exhibited sufficient active chlorine contents. The active chlorine content of the melt-blown nonwovens with the PP-g-NDAM concentration of 40, 70, and 100 wt.% was 0.309 ± 0.012‰, 0.409 ± 0.024‰, and 0.463 ± 0.031‰, respectively. It could be found that the content of active chlorine increased with the increase of the PP-g-NDAM concentration. This is because the nonwovens containing a higher PP-g-NDAM concentration could provide more -NH2 groups, which is essential for chlorination to form -NHCl (see Scheme 1 and Figure 3). However, the increasing rate of active chlorine slows down with the increase of the PP-g-NDAM concentration, and due to the N-halamine transformation on the fiber surface, the specific surface area of fibers will be decreased with the average diameter of melt-blown fibers getting larger. It could be also verified from Figure 6(e) that the fiber diameter was increased with the increase of the PP-g-NDAM concentration. Furthermore, in the antibacterial test, after 30 min the active chlorine content reduced significantly for PP-g-NDAM melt-blown nonwovens (Figure 8(a)). Due to the consumption of active chlorine in the antibacterial process, the active chlorine content is finally decreased to 0.103 ± 0.007‰, 0.172 ± 0.026‰, and 0.223 ± 0.030‰ for 40 wt.%, 70 wt.%, and 100 wt.% PP-g-NDAM melt-blown nonwovens, respectively.Figure 8
Active chlorine content of chlorinated melt-blown nonwovens with different concentrations of PP-g-NDAM (a) before and after antibacterial treatment and (b) after repeating the reduction and chlorination treatment for 10 times.
(a)
(b)As shown in Figure8(b), after repeating the reduction and chlorination treatment for 10 times, the active chlorine content of 40 wt.%, 70 wt.%, and 100 wt.% PP-g-NDAM melt-blown nonwovens decreases slightly by 3.35%, 3.13%, and 3.08%, respectively, indicating the good regeneration ability of the PP-g-NDAM melt-blown nonwovens. However, with the increase of regeneration times, the active chlorine content in the melt-blown nonwovens will gradually decrease according to the performance after 10 times of cycling (Figure 8(b)). This may be ascribed to the loss of the grafted antibacterial agent (NDAM) during chlorine bleaching treatment, which results in an insufficient regeneration of active chlorine.


## 3.4. Antibacterial Property of the Grafted Melt-Blown Nonwovens

The antibacterial results of melt-blown nonwovens containing different PP-g-NDAM concentrations are listed in Table2. The proliferated colonies of E. coli were observed on the pristine PP melt-blown nonwoven, while the grafted melt-blown nonwovens showed excellent antibacterial properties against E. coli. For the nonwovens containing 40 wt.% PP-g-NDAM, 95.35% and 99.99% of the bacteria were sterilized within 15 and 30 min, respectively. For the nonwovens containing 70 wt.% PP-g-NDAM, 99.99% of the bacteria were killed just within 15 min. However, the sterilization speed is no longer faster for the 100 wt.% PP-g-NDAM nonwovens, indicating that 70 wt.% PP-g-NDAM is sufficient for sterilizing the E. coli. Moreover, long-term stability of antibacterial properties was also investigated. After 10 days, the antibacterial properties of the samples show no significant change as all grafted melt-blown nonwovens could sterilize 99.99% of E. coli after a contact time of 30 min.Table 2
Antibacterial properties of grafted melt-blown samples againstE. coli after different contact times.
Concentration of PP-g-NDAM (wt.%)
Percentage reduction ofE. coli at different contact times (%)
15 min
30 min
60 min
40
95.35
99.99
99.999
70
99.99
99.999
99.999
100
99.99
99.999
99.999


## 4. Conclusions

NDAM monomer was successfully grafted onto the PP backbone by using radical polymerization during reactive extrusion, which was confirmed by nitrogen analysis and FTIR spectra. Increasing NDAM monomer content could increase the degree of substitution; however, excessive NDAM may result in a decrease in GE. Besides, the GD and GE reached to the maximum value when the weight of DCP was 0.6 g. However, further increase of DCP initiators could result in a decline on GD and GE value. The sample B3 with the highest GE of 4.85 wt.% was selected to prepare melt-blown nonwovens with pristine PP resins in different ratios, and the filtration efficiency of the charged melt-blown nonwovens containing 40, 70, and 100 wt.% PP-g-NDAM can reach 85.88 ± 1.77%, 81.16 ± 2.04%, and 73.33 ± 2.29% with low resistance, respectively. The chlorinated melt-blown samples containing 70 and 100 wt.% PP-g-NDAM exhibited potent antibacterial properties againstE. coli bacterium after 15 min contact time. Thus, the grafted melt-blown nonwovens may become a good candidate for personal protective filtration materials with antibacterial properties. Further investigation can be done in the improvement of filtration performance by reducing fiber diameters and increasing specific surface areas of the bifunctional nonwoven filters. At the same time, the mechanism studies on the regeneration of active chlorine content and antibacterial properties after chlorine bleaching should be investigated.



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*Source: 3435095-2019-12-04.xml*