# Use of Oxalic-Acid-Modified Stellerite for Improving the Filter Capability of PM2.5 of Paper Composed of Bamboo Residues

Authors: Hua Chen; Jian Lou; Fei Yang; Jia-nan Zhou; Yan Zhang; Huabo Yao
Journal: International Journal of Polymer Science
 (2016)

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## Abstract

In this study, pulping conditions for kraft pulping of bamboo residues were investigated, predominantly focusing on cooking temperature and time during pulping. Oxalic acid and cationic starch were used for the modification of natural stellerite, and the use of modified stellerite for preparing filter paper for PM2.5 filtration was investigated. The optimal pulping technology of bamboo residues was established based on the following experimental parameters: liquor ratio of 1 : 5.5, cooking temperature of 160°C, and a holding time of 2 h. Modification by oxalic acid resulted in the promotion of pore formation at the stellerite surfaces and induced the microscopic changes. Nevertheless, paper strength remained practically unchanged after the addition of fillers, indicating that the cationic starch preblend method is a promising technique for papermaking because it enhances the strength properties of paper. With the variation in the addition of modified stellerite from 3 to 15%, while simultaneously maintaining the basis weight constant at 60 gm−2, the filtration efficiency of paper sheets first increased and then decreased later; thus the optimum stellerite content was found to be 9%. Filtration efficiency was suggested to be affected by gas flowing velocity.


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## Body

## 1. Introduction

With the economic development of China as well as the growth of its transportation industry, air pollution is becoming more serious in recent years. Several contaminants and pollutants can be adsorbed on the particles suspended in the atmosphere and enter the body via respiration.Most studies have reported that PM2.5 (particles with an aerodynamic diameter of 2.5 μm or less) [1] with small average particles size, large-scale impact, and high specific surface area can enter the human respiratory system and even penetrate through the lung cells into blood circulation, posing serious hazards to human health [2], including asthma [3] and bronchitis [4]. More importantly studies have increasingly reported that PM2.5 possibly stimulates the mutation of the p53 gene in nasopharyngeal epithelial cells and plays an important role in the carcinogenesis of oral tissues [5]. According to the American Cancer Society, an 8% increase in cancer mortality for every 10 μgm−3 increase in PM2.5 consistency for city population has been observed.On the other hand, China has the richest resources of bamboo in the world, where 33,000 km2 or 3% of the country’s total forest area is occupied by bamboo [6]. With the development of the bamboo industry, a large number of residues are produced, and the utilization of these bamboo residues is not greater than 10%, where its collecting and treatment has noticed by people [7].Both domestic and international studies have indicated that fiber filter material exhibits several advantages, such as mass production, low cost, high surface area, porous nature, and good flexibility [8–12]. The main raw materials used for filter material for high-efficiency PM2.5 capture include natural plant, synthetic fiber, glass, ceramic, and metal fibers. Natural plant fiber, such as bamboo residues, is probably the most promising one among various PM2.5 filter materials, attributed to its wide spread sources, low cost, and excellent reprocessing performance.Zeolite is a type of aqueous silicoaluminate mineral with excellent adsorption characteristics. Porous zeolites have been widely used in catalysis, adsorption, and separation attributed to their open frameworks, high surface areas, and ordered pore structures [13–15]. Nevertheless, few studies have been reported on natural zeolite, despite its low cost and abundant storage [16].In this study, the effect of filter paper made from bamboo residue and oxalic-acid-modified stellerite on PM2.5 filtration was comprehensively investigated. Factors affecting pulping and the use of stellerite were also investigated.


## 2. Experimental

### 2.1. Materials

#### 2.1.1. Raw Materials

Stellerite was purchased from Jinshansida Co., Ltd. (Guilin, China). Oxalic acid, sodium hydroxide (NaOH), and sodium sulfide nonahydrate (Na2S·9H2O) with purities of 96% were supplied by Linfeng Chemical Co., Ltd. (Shanghai, China). Cationic starch with a substitution degree of 0.028 was purchased from Hengfeng Chemical Co., Ltd. (Zhejiang, China). Bamboo(Bambusa rigida species) residue was provided by a bamboo products company (Anji, China). The residue exhibited the following average characteristics: 49.96% cellulose, 22.88% total lignin, and 17.97% hemicelluloses.


#### 2.1.2. Pulping and Beating

First, bamboo residue (abbreviated as BR) was crushed and screened through a mesh with a size of 160. According to ISO 287-1985 standard, its moisture content was determined to be 12.27%. Pulping was conducted by the kraft pulping method with a liquor ratio of 1 : 5.5, active alkali of 30%, and a sulfureted degree of 30%. Samples were referred to as P1, P2, P3, P4, P5, and P6 according to the cooking process as shown in Table1.Table 1
Cooking process.
Sample Extension Cooking temperature (°C) Cooking time (h) BR Bamboo residue — — P1 Pulp 1 150 1.5 P2 Pulp 2 150 2.0 P3 Pulp 3 150 2.5 P4 Pulp 4 160 1.5 P5 Pulp 5 160 2.0 P6 Pulp 6 160 2.5Filtration and washing were conducted after pulping. Finally, the pulp was refined to 30°SR using a TD7 Refiner (TD7-PFI, SUST, Shanxi, China).


#### 2.1.3. Modification of Stellerite

Stellerite was obtained from Jinshansida Co., Ltd. (Guangxi, China). First, stellerite was repeatedly washed using distilled water for removing some impurity ions, and this was followed by dehydration in an oven box at 100°C for 12 h. Second, stellerite (7.5 g) was added into a round flask containing aqueous solution of oxalic acid (150 mL, 1.0 molL−1). Third, the reaction temperature was maintained constant at 85°C for 5 h under stirring. Next, the solid liquid mixture was filtered, and stellerite was washed with distilled water. Further, a AgNO3 test was performed to ensure the absence of remaining Cl− ions in stellerite. After grinding, stellerite was calcined at 105°C for 12 h.


#### 2.1.4. Capping of Cationic Starch Preblend

First, distilled water (400 mL) and cationic starch (20 g) were added together in a 500-mL four-necked-round-bottom flask; and the resulting slurry was stirred to ensure sufficient mixing. Second, modified stellerite (20 g) was added to the slurry, and after stirring for 25 min at 90°C, it was dried at 95°C for 12 h. Finally, the mixture was ground into a powder, and cationic-starch-capped modified stellerite was prepared by the preblend method, with a mass ratio of 1 : 1 for cationic starch and modified stellerite.


#### 2.1.5. Preparation of Hand Sheets and Testing

First, the beaten pulp was diluted to a consistency of 1.2% using distilled water, followed by disintegration using a standard disintegrator at 20,000 revolutions until all fiber bundles were dispersed. Second, cationic-starch-capped modified stellerite was added under stirring at 3000 revolutions for 1 min, where the concentration of the added fillers was maintained constant at 3, 6, 9, 12, and 15% (based on oven-dry pulp mass). Hand sheets with a target basis weight of 60 gm−2 were prepared using the ZBJ1-B Automatic Sheet Former System (SUST, Shanxi, China) according to TAPPI T 205 (TAPPI Test Methods, 2002), with the exception that the pressure utilized for wet sheet pressing was controlled at 200 kPa, followed by drying at 102°C using a Formax 12′′ Drum Dryer (Thwing-Albert Instrument, USA). The hand sheets were conditioned under a controlled environment (temperature of 23±1°C and relative humidity of 50±1%) before analysis.The tensile index and air permeability of hand sheets were determined according to the relevant TAPPI Standards. The tensile index of the paper sheets was determined using a WZL-300B Tensile Strength Tester (Qitongboke, China), and air permeability was tested using an Air Permeance Tester (Messmer Instruments Ltd., Testing Machines Inc., USA). The ash content of the fibers was measured according to ISO 2144:1997 method, and the ash content of the pulp and paper sheets was determined according to TAPPI T 413 om-85 (1985) standards. The retention efficiency of the fillers was calculated by using(1)R=A-B·1-L-CL-B·1-A-C×100%.Here, A, B, and L represent the ash content of the paper sheets, fiber, and pulp, respectively, and C represents the loss on ignition of stellerite.Filtration efficiencies of various hand sheets were investigated using TSI-8130 Automated Filter Tester (TSI Company, USA). The 0.3μm NaCl particle was used as the filtration simulation model (adjusted flow of 32 Lmin−1).


#### 2.1.6. Determination of Pore Distribution

A pore size distribution detector ASAP2010M (Micromeritics, USA) was used for the structural analyses of fiber pores. High-purity N2 was used as the adsorbate, and the adsorption–desorption of high-purity N2 was determined at 77 K in a liquid nitrogen trap by a static volumetric method.


#### 2.1.7. Fourier Transform Infrared Spectroscopy Analysis

Fourier transform infrared (FTIR) spectroscopy analysis of the samples was conducted in the transmission mode by macrotechniques (13 mmΦ pellet; ca. 1.5 mg sample with 350 mg KBr). The spectra were recorded using a Nexus Vector spectrometer (Nexus 670, Thermo Nicolet Company, USA) under the following specifications: Apodization: triangular; detector: DTGS/KBr; regulation: 4 cm−1; and number of scans: 32.


#### 2.1.8. X-Ray Diffraction Analysis

The X-ray powder diffraction (XRD) patterns of the samples were recorded on a Bruker D8 Advance XRD instrument (step size of 0.02° with 17.7 s per step). A Generator with 40 kV and a current of 40 mA were employed as sources for CuKα radiation.The crystallinity index was calculated from the relative intensities of the diffraction peaks [17] as follows:(2)a=I020I020+Iam×100%.Here, I020 represents the intensity (2θ≈22.5°) of the peak belonging to the {020}, which contributes to the strength of the crystalline region, and Iam represents the intensity (2θ≈18°) between the {020} and {110}, which represents the intensity of the amorphous region.


#### 2.1.9. Scanning Electron Microscopy Analysis

Morphologies of the hand sheet surfaces were examined by scanning electron microscopy (SEM, JSM-IT300, JEOL, Japan) operating at an accelerating voltage of 15 kV. Before observation, the samples were coated with gold using a vacuum sputter-coater.All experiments were conducted in triplicate with a relative standard deviation (RSD) of approximately 5%.


## 2.1. Materials

### 2.1.1. Raw Materials

Stellerite was purchased from Jinshansida Co., Ltd. (Guilin, China). Oxalic acid, sodium hydroxide (NaOH), and sodium sulfide nonahydrate (Na2S·9H2O) with purities of 96% were supplied by Linfeng Chemical Co., Ltd. (Shanghai, China). Cationic starch with a substitution degree of 0.028 was purchased from Hengfeng Chemical Co., Ltd. (Zhejiang, China). Bamboo(Bambusa rigida species) residue was provided by a bamboo products company (Anji, China). The residue exhibited the following average characteristics: 49.96% cellulose, 22.88% total lignin, and 17.97% hemicelluloses.


### 2.1.2. Pulping and Beating

First, bamboo residue (abbreviated as BR) was crushed and screened through a mesh with a size of 160. According to ISO 287-1985 standard, its moisture content was determined to be 12.27%. Pulping was conducted by the kraft pulping method with a liquor ratio of 1 : 5.5, active alkali of 30%, and a sulfureted degree of 30%. Samples were referred to as P1, P2, P3, P4, P5, and P6 according to the cooking process as shown in Table1.Table 1
Cooking process.
Sample Extension Cooking temperature (°C) Cooking time (h) BR Bamboo residue — — P1 Pulp 1 150 1.5 P2 Pulp 2 150 2.0 P3 Pulp 3 150 2.5 P4 Pulp 4 160 1.5 P5 Pulp 5 160 2.0 P6 Pulp 6 160 2.5Filtration and washing were conducted after pulping. Finally, the pulp was refined to 30°SR using a TD7 Refiner (TD7-PFI, SUST, Shanxi, China).


### 2.1.3. Modification of Stellerite

Stellerite was obtained from Jinshansida Co., Ltd. (Guangxi, China). First, stellerite was repeatedly washed using distilled water for removing some impurity ions, and this was followed by dehydration in an oven box at 100°C for 12 h. Second, stellerite (7.5 g) was added into a round flask containing aqueous solution of oxalic acid (150 mL, 1.0 molL−1). Third, the reaction temperature was maintained constant at 85°C for 5 h under stirring. Next, the solid liquid mixture was filtered, and stellerite was washed with distilled water. Further, a AgNO3 test was performed to ensure the absence of remaining Cl− ions in stellerite. After grinding, stellerite was calcined at 105°C for 12 h.


### 2.1.4. Capping of Cationic Starch Preblend

First, distilled water (400 mL) and cationic starch (20 g) were added together in a 500-mL four-necked-round-bottom flask; and the resulting slurry was stirred to ensure sufficient mixing. Second, modified stellerite (20 g) was added to the slurry, and after stirring for 25 min at 90°C, it was dried at 95°C for 12 h. Finally, the mixture was ground into a powder, and cationic-starch-capped modified stellerite was prepared by the preblend method, with a mass ratio of 1 : 1 for cationic starch and modified stellerite.


### 2.1.5. Preparation of Hand Sheets and Testing

First, the beaten pulp was diluted to a consistency of 1.2% using distilled water, followed by disintegration using a standard disintegrator at 20,000 revolutions until all fiber bundles were dispersed. Second, cationic-starch-capped modified stellerite was added under stirring at 3000 revolutions for 1 min, where the concentration of the added fillers was maintained constant at 3, 6, 9, 12, and 15% (based on oven-dry pulp mass). Hand sheets with a target basis weight of 60 gm−2 were prepared using the ZBJ1-B Automatic Sheet Former System (SUST, Shanxi, China) according to TAPPI T 205 (TAPPI Test Methods, 2002), with the exception that the pressure utilized for wet sheet pressing was controlled at 200 kPa, followed by drying at 102°C using a Formax 12′′ Drum Dryer (Thwing-Albert Instrument, USA). The hand sheets were conditioned under a controlled environment (temperature of 23±1°C and relative humidity of 50±1%) before analysis.The tensile index and air permeability of hand sheets were determined according to the relevant TAPPI Standards. The tensile index of the paper sheets was determined using a WZL-300B Tensile Strength Tester (Qitongboke, China), and air permeability was tested using an Air Permeance Tester (Messmer Instruments Ltd., Testing Machines Inc., USA). The ash content of the fibers was measured according to ISO 2144:1997 method, and the ash content of the pulp and paper sheets was determined according to TAPPI T 413 om-85 (1985) standards. The retention efficiency of the fillers was calculated by using(1)R=A-B·1-L-CL-B·1-A-C×100%.Here, A, B, and L represent the ash content of the paper sheets, fiber, and pulp, respectively, and C represents the loss on ignition of stellerite.Filtration efficiencies of various hand sheets were investigated using TSI-8130 Automated Filter Tester (TSI Company, USA). The 0.3μm NaCl particle was used as the filtration simulation model (adjusted flow of 32 Lmin−1).


### 2.1.6. Determination of Pore Distribution

A pore size distribution detector ASAP2010M (Micromeritics, USA) was used for the structural analyses of fiber pores. High-purity N2 was used as the adsorbate, and the adsorption–desorption of high-purity N2 was determined at 77 K in a liquid nitrogen trap by a static volumetric method.


### 2.1.7. Fourier Transform Infrared Spectroscopy Analysis

Fourier transform infrared (FTIR) spectroscopy analysis of the samples was conducted in the transmission mode by macrotechniques (13 mmΦ pellet; ca. 1.5 mg sample with 350 mg KBr). The spectra were recorded using a Nexus Vector spectrometer (Nexus 670, Thermo Nicolet Company, USA) under the following specifications: Apodization: triangular; detector: DTGS/KBr; regulation: 4 cm−1; and number of scans: 32.


### 2.1.8. X-Ray Diffraction Analysis

The X-ray powder diffraction (XRD) patterns of the samples were recorded on a Bruker D8 Advance XRD instrument (step size of 0.02° with 17.7 s per step). A Generator with 40 kV and a current of 40 mA were employed as sources for CuKα radiation.The crystallinity index was calculated from the relative intensities of the diffraction peaks [17] as follows:(2)a=I020I020+Iam×100%.Here, I020 represents the intensity (2θ≈22.5°) of the peak belonging to the {020}, which contributes to the strength of the crystalline region, and Iam represents the intensity (2θ≈18°) between the {020} and {110}, which represents the intensity of the amorphous region.


### 2.1.9. Scanning Electron Microscopy Analysis

Morphologies of the hand sheet surfaces were examined by scanning electron microscopy (SEM, JSM-IT300, JEOL, Japan) operating at an accelerating voltage of 15 kV. Before observation, the samples were coated with gold using a vacuum sputter-coater.All experiments were conducted in triplicate with a relative standard deviation (RSD) of approximately 5%.


## 2.1.1. Raw Materials

Stellerite was purchased from Jinshansida Co., Ltd. (Guilin, China). Oxalic acid, sodium hydroxide (NaOH), and sodium sulfide nonahydrate (Na2S·9H2O) with purities of 96% were supplied by Linfeng Chemical Co., Ltd. (Shanghai, China). Cationic starch with a substitution degree of 0.028 was purchased from Hengfeng Chemical Co., Ltd. (Zhejiang, China). Bamboo(Bambusa rigida species) residue was provided by a bamboo products company (Anji, China). The residue exhibited the following average characteristics: 49.96% cellulose, 22.88% total lignin, and 17.97% hemicelluloses.


## 2.1.2. Pulping and Beating

First, bamboo residue (abbreviated as BR) was crushed and screened through a mesh with a size of 160. According to ISO 287-1985 standard, its moisture content was determined to be 12.27%. Pulping was conducted by the kraft pulping method with a liquor ratio of 1 : 5.5, active alkali of 30%, and a sulfureted degree of 30%. Samples were referred to as P1, P2, P3, P4, P5, and P6 according to the cooking process as shown in Table1.Table 1
Cooking process.
Sample Extension Cooking temperature (°C) Cooking time (h) BR Bamboo residue — — P1 Pulp 1 150 1.5 P2 Pulp 2 150 2.0 P3 Pulp 3 150 2.5 P4 Pulp 4 160 1.5 P5 Pulp 5 160 2.0 P6 Pulp 6 160 2.5Filtration and washing were conducted after pulping. Finally, the pulp was refined to 30°SR using a TD7 Refiner (TD7-PFI, SUST, Shanxi, China).


## 2.1.3. Modification of Stellerite

Stellerite was obtained from Jinshansida Co., Ltd. (Guangxi, China). First, stellerite was repeatedly washed using distilled water for removing some impurity ions, and this was followed by dehydration in an oven box at 100°C for 12 h. Second, stellerite (7.5 g) was added into a round flask containing aqueous solution of oxalic acid (150 mL, 1.0 molL−1). Third, the reaction temperature was maintained constant at 85°C for 5 h under stirring. Next, the solid liquid mixture was filtered, and stellerite was washed with distilled water. Further, a AgNO3 test was performed to ensure the absence of remaining Cl− ions in stellerite. After grinding, stellerite was calcined at 105°C for 12 h.


## 2.1.4. Capping of Cationic Starch Preblend

First, distilled water (400 mL) and cationic starch (20 g) were added together in a 500-mL four-necked-round-bottom flask; and the resulting slurry was stirred to ensure sufficient mixing. Second, modified stellerite (20 g) was added to the slurry, and after stirring for 25 min at 90°C, it was dried at 95°C for 12 h. Finally, the mixture was ground into a powder, and cationic-starch-capped modified stellerite was prepared by the preblend method, with a mass ratio of 1 : 1 for cationic starch and modified stellerite.


## 2.1.5. Preparation of Hand Sheets and Testing

First, the beaten pulp was diluted to a consistency of 1.2% using distilled water, followed by disintegration using a standard disintegrator at 20,000 revolutions until all fiber bundles were dispersed. Second, cationic-starch-capped modified stellerite was added under stirring at 3000 revolutions for 1 min, where the concentration of the added fillers was maintained constant at 3, 6, 9, 12, and 15% (based on oven-dry pulp mass). Hand sheets with a target basis weight of 60 gm−2 were prepared using the ZBJ1-B Automatic Sheet Former System (SUST, Shanxi, China) according to TAPPI T 205 (TAPPI Test Methods, 2002), with the exception that the pressure utilized for wet sheet pressing was controlled at 200 kPa, followed by drying at 102°C using a Formax 12′′ Drum Dryer (Thwing-Albert Instrument, USA). The hand sheets were conditioned under a controlled environment (temperature of 23±1°C and relative humidity of 50±1%) before analysis.The tensile index and air permeability of hand sheets were determined according to the relevant TAPPI Standards. The tensile index of the paper sheets was determined using a WZL-300B Tensile Strength Tester (Qitongboke, China), and air permeability was tested using an Air Permeance Tester (Messmer Instruments Ltd., Testing Machines Inc., USA). The ash content of the fibers was measured according to ISO 2144:1997 method, and the ash content of the pulp and paper sheets was determined according to TAPPI T 413 om-85 (1985) standards. The retention efficiency of the fillers was calculated by using(1)R=A-B·1-L-CL-B·1-A-C×100%.Here, A, B, and L represent the ash content of the paper sheets, fiber, and pulp, respectively, and C represents the loss on ignition of stellerite.Filtration efficiencies of various hand sheets were investigated using TSI-8130 Automated Filter Tester (TSI Company, USA). The 0.3μm NaCl particle was used as the filtration simulation model (adjusted flow of 32 Lmin−1).


## 2.1.6. Determination of Pore Distribution

A pore size distribution detector ASAP2010M (Micromeritics, USA) was used for the structural analyses of fiber pores. High-purity N2 was used as the adsorbate, and the adsorption–desorption of high-purity N2 was determined at 77 K in a liquid nitrogen trap by a static volumetric method.


## 2.1.7. Fourier Transform Infrared Spectroscopy Analysis

Fourier transform infrared (FTIR) spectroscopy analysis of the samples was conducted in the transmission mode by macrotechniques (13 mmΦ pellet; ca. 1.5 mg sample with 350 mg KBr). The spectra were recorded using a Nexus Vector spectrometer (Nexus 670, Thermo Nicolet Company, USA) under the following specifications: Apodization: triangular; detector: DTGS/KBr; regulation: 4 cm−1; and number of scans: 32.


## 2.1.8. X-Ray Diffraction Analysis

The X-ray powder diffraction (XRD) patterns of the samples were recorded on a Bruker D8 Advance XRD instrument (step size of 0.02° with 17.7 s per step). A Generator with 40 kV and a current of 40 mA were employed as sources for CuKα radiation.The crystallinity index was calculated from the relative intensities of the diffraction peaks [17] as follows:(2)a=I020I020+Iam×100%.Here, I020 represents the intensity (2θ≈22.5°) of the peak belonging to the {020}, which contributes to the strength of the crystalline region, and Iam represents the intensity (2θ≈18°) between the {020} and {110}, which represents the intensity of the amorphous region.


## 2.1.9. Scanning Electron Microscopy Analysis

Morphologies of the hand sheet surfaces were examined by scanning electron microscopy (SEM, JSM-IT300, JEOL, Japan) operating at an accelerating voltage of 15 kV. Before observation, the samples were coated with gold using a vacuum sputter-coater.All experiments were conducted in triplicate with a relative standard deviation (RSD) of approximately 5%.


## 3. Results and Discussion

### 3.1. Pore Structure Analysis of Fibers and Stellerite

Table2 lists the results obtained from the pore structural analysis of fibers and stellerite. The results indicated that, with increasing cooking degree, surface area and pore volume became greater than the initial volume. Moreover, pore size significantly decreased, indicative of the generation of abundant micropores and mesopores. At this stage, the pulping yield increased because of the reduction in the discharge rate during filtration after cooking. However, cooking for a long time resulted in overcooking, leading to a decrease of surface area and the destruction of the fiber porous structure. Moreover, pulping yield also decreased during overcooking, attributed to the massive reduction of fines in washing process. Thus, the optimal pulping conditions were as follows: cooking temperature of 160°C and a holding time of 2 h (sample P5).Table 2
Pore structure analysis of fibers and stellerite.
Sample Specific surface area(SBET, m2g−1) Pore volume(Vt-plot, cm3g−1) Pore size(DBET, nm) Yield(%) P1 0.0064 ± 0.0001 0.000126 ± 0.000003 2941.4 ± 76.48 35.46 ± 0.85 P2 0.0316 ± 0.0001 0.000169 ± 0.000007 714.2 ± 14.99 38.19 ± 0.99 P3 0.0687 ± 0.0002 0.000269 ± 0.000010 405.1 ± 10.94 39.72 ± 1.23 P4 0.0753 ± 0.0005 0.000322 ± 0.000009 218.5 ± 5.244 40.98 ± 0.98 P5 0.0932 ± 0.0007 0.000358 ± 0.000012 89.4 ± 1.699 42.91 ± 1.03 P6 0.0417 ± 0.0008 0.000125 ± 0.000004 120.2 ± 3.366 36.77 ± 1.02 Natural stellerite 2.2179 ± 0.0581 0.000487 ± 0.000012 8.0 ± 0.152 — Modified stellerite 108.8327 ± 2.1921 0.051550 ± 0.001288 1.9 ± 0.034 91.41 ± 2.01With respect to the oxalic-acid-modified stellerite, specific surface area (SBET) for natural stellerite was 2.2179 m2 g−1; in contrast, for the sample treated with 1.0 mol L−1 oxalic acid, SBET was 108.8327 m2 g−1 (increase by 49 times). In particular, pore size (DBET) was also significantly less than that observed for natural stellerite, indicating that a microporous structure was formed. Moreover, the modification yield was 91.41%, attributed to the removal of impurities and loss during washing.


### 3.2. Functional Group Analysis of Different Samples

Figure1 shows the FTIR spectra of samples BR, P1, P2, P3, P4, P5, and P6. The peak observed at 3447 cm−1 is attributed to the hydroxylgroups (OH) in the fibers; it is a band characteristic of cellulose [18]. The peak observed at 2960 cm−1 is attributed to the C–H absorption. The strong band observed at 1642 cm−1 is attributed to the vibration of absorbed water molecules in the noncrystalline region of cellulose. The band observed at 1511 cm−1 is attributed to the vibration of the aromatic ring of lignin, and the peak observed at 1735 cm−1 is ascribed to the C=O stretching vibration of acetyl and carboxyl of hemicellulose [19]. The comparison of the different spectra indicated that, with increasing cooking degree, the cellulose characteristics of spectra were more apparent, attributed to the fact that, in comparison, cellulose, lignin, and hemicellulose degrade more rapidly in the cooking process.Figure 1
FTIR spectroscopy of different pulp samples: (a) BR, (b) P1, (c) P2, (d) P3, (e) P4, (f) P5, and (g) P6.


### 3.3. XRD Patterns of Fibers

Figure2(a) shows the XRD patterns of bamboo residues, exhibiting low crystallinity (crystallinity index = 51.8%), as evidenced by their faint pattern. The crystallinity of pulp clearly increased after cooking, with the main peaks observed at 2θ of 22.5° and 18°, attributed to {020}, and the amorphous region of cellulose. Moreover, the crystallinity of P1, P2, P3, P4, P5, and P6 increased to 54.4, 55.6, 56.8, 57.2, 59.9, and 57.8%, respectively. This result is attributed to the following two reasons: the removal of disordered material in the amorphous region and the formation of new crystalline region, ascribed to the realignment of the cellulose chain caused by the penetration of water molecules into the amorphous region [19].Figure 2
XRD curves of different samples: (a) BR, (b) P1, (c) P2, (d) P3, (e) P4, (f) P5, and (g) P6.


### 3.4. SEM Images of Different Samples

Figure3 shows the SEM images of different samples, clearly displaying their surface morphology. The bamboo residues consist of piece structure, with several pits randomly distributed on the residue surface (Figure 3(a)). The bamboo fibers with complete shape and clear contours were obtained for the appropriate cooking process (P5, Figure 3(b)). Natural stellerite exhibits a clear layer structure (Figure 3(c)). Treatment with oxalic acid led to the formation of cracks on its surface, resulting in the promotion of pore formation at the stellerite surfaces and induced microscopic changes; this result is consistent with those shown in Table 2 (Figure 3(d)). Figure 3(e) shows the hand sheet without fillers, and Figure 3(f) demonstrates the distribution of granular-modified stellerite between fibers.Figure 3
SEM images of different samples: (a) BR, (b) P5, (c) natural stellerite, (d) modified stellerite, (e) hand sheet composed of P5 without stellerite, and (f) hand sheet composed of P5 with modified stellerite (9%).
(a) (b) (c) (d) (e) (f)


### 3.5. Ash Content and Filler Retention

Figure4 shows the ash content and filler retention of different paper sheets. With increasing stellerite content, ash content increases, and approximately 7.2% of ash was obtained with the addition of 15% stellerite. In contrast, filler retention significantly decreases.Figure 4
Ash content and filler retention of different paper sheets.


### 3.6. Tensile Indices and Air Permeability of Paper Sheets

Figure5 shows the effects of stellerite content on the tensile indices and air permeability of the paper sheets. Compared to the control (without stellerite), the tensile index of the paper sheet with the addition of 3% stellerite indicated a 3.7% increase; however, the ash content increased from 0.14 to 1.98%. Thus, under experimental conditions employed in this study, appropriate addition of cationic-starch-preblend-modified stellerite exerted a certain positive effect on the tensile index of the paper sheet, possibly attributed to the improvement of evenness. Moreover, with increasing filler content, air permeability also increased. With the addition of 15% stellerite, the air permeability of the paper sheet increased from 3.44 to 6.62 μm Pa−1 s−1, indicating that the porosity of the paper increased because of the addition of filler.Figure 5
Tensile indices and air permeability of paper sheets.


### 3.7. Filter Performance of Paper Sheets

Tables3 and 4 summarize the filter performance of different paper sheets and the impact of gas flowing velocities. The filter performance was suggested to be affected not only by the dosage of fillers, but also by the gas flowing velocities during testing. The best performance was obtained with the addition of 9% modified stellerite, predominantly attributed to the fact that extremely high air permeability of paper sheets results in the decline of adsorption quantity. This result indicates the existence of an important difference between fibers and fillers in the adsorption of PM2.5. It has been reported that micron wood fibers have low collection efficiency toward particles with the diameter from 0.4 to 0.6 μm, while they have significantly higher collection efficiency for particles with other sizes. Among these particles with the diameter of 0.01 μm, the collection efficiency of micron wood fibers can reach up to 90% [20].Table 3
Effect of the variation of stellerite content on filter performance∗.
Dosage of stellerite (%) 0 3 6 9 12 15  Filtration efficiency (%) 5 9.3 ± 2.1 72.5 ± 1.9 74.1 ± 2.3 78.4 ± 2.5 76.5 ± 2.9 75.8 ± 3.1 ∗Gas flowing velocity = 0.2 ms−1.Table 4
Effect of different gas flowing velocities on filter performance∗.
Gas flowing velocities (ms−1) 0.2 0.4 0.6 0.8  Filtration efficiency (%) 78.4 ± 2.8 69.7 ± 1.7 62.6 ± 2.5 58.2 ± 2.0 ∗Dosage of stellerite = 9%.In fact, the filtering process of PM2.5 particles by plant fibers and fillers is very complex and specific to location; therefore, filter performance is affected not only by the z-direction position, but also by time. This observation is referred to as layered filtration and nonstationary filtration (see Figure 6), which will be further explored in our future study.Figure 6
Filtration sketch of paper sheets.


## 3.1. Pore Structure Analysis of Fibers and Stellerite

Table2 lists the results obtained from the pore structural analysis of fibers and stellerite. The results indicated that, with increasing cooking degree, surface area and pore volume became greater than the initial volume. Moreover, pore size significantly decreased, indicative of the generation of abundant micropores and mesopores. At this stage, the pulping yield increased because of the reduction in the discharge rate during filtration after cooking. However, cooking for a long time resulted in overcooking, leading to a decrease of surface area and the destruction of the fiber porous structure. Moreover, pulping yield also decreased during overcooking, attributed to the massive reduction of fines in washing process. Thus, the optimal pulping conditions were as follows: cooking temperature of 160°C and a holding time of 2 h (sample P5).Table 2
Pore structure analysis of fibers and stellerite.
Sample Specific surface area(SBET, m2g−1) Pore volume(Vt-plot, cm3g−1) Pore size(DBET, nm) Yield(%) P1 0.0064 ± 0.0001 0.000126 ± 0.000003 2941.4 ± 76.48 35.46 ± 0.85 P2 0.0316 ± 0.0001 0.000169 ± 0.000007 714.2 ± 14.99 38.19 ± 0.99 P3 0.0687 ± 0.0002 0.000269 ± 0.000010 405.1 ± 10.94 39.72 ± 1.23 P4 0.0753 ± 0.0005 0.000322 ± 0.000009 218.5 ± 5.244 40.98 ± 0.98 P5 0.0932 ± 0.0007 0.000358 ± 0.000012 89.4 ± 1.699 42.91 ± 1.03 P6 0.0417 ± 0.0008 0.000125 ± 0.000004 120.2 ± 3.366 36.77 ± 1.02 Natural stellerite 2.2179 ± 0.0581 0.000487 ± 0.000012 8.0 ± 0.152 — Modified stellerite 108.8327 ± 2.1921 0.051550 ± 0.001288 1.9 ± 0.034 91.41 ± 2.01With respect to the oxalic-acid-modified stellerite, specific surface area (SBET) for natural stellerite was 2.2179 m2 g−1; in contrast, for the sample treated with 1.0 mol L−1 oxalic acid, SBET was 108.8327 m2 g−1 (increase by 49 times). In particular, pore size (DBET) was also significantly less than that observed for natural stellerite, indicating that a microporous structure was formed. Moreover, the modification yield was 91.41%, attributed to the removal of impurities and loss during washing.


## 3.2. Functional Group Analysis of Different Samples

Figure1 shows the FTIR spectra of samples BR, P1, P2, P3, P4, P5, and P6. The peak observed at 3447 cm−1 is attributed to the hydroxylgroups (OH) in the fibers; it is a band characteristic of cellulose [18]. The peak observed at 2960 cm−1 is attributed to the C–H absorption. The strong band observed at 1642 cm−1 is attributed to the vibration of absorbed water molecules in the noncrystalline region of cellulose. The band observed at 1511 cm−1 is attributed to the vibration of the aromatic ring of lignin, and the peak observed at 1735 cm−1 is ascribed to the C=O stretching vibration of acetyl and carboxyl of hemicellulose [19]. The comparison of the different spectra indicated that, with increasing cooking degree, the cellulose characteristics of spectra were more apparent, attributed to the fact that, in comparison, cellulose, lignin, and hemicellulose degrade more rapidly in the cooking process.Figure 1
FTIR spectroscopy of different pulp samples: (a) BR, (b) P1, (c) P2, (d) P3, (e) P4, (f) P5, and (g) P6.


## 3.3. XRD Patterns of Fibers

Figure2(a) shows the XRD patterns of bamboo residues, exhibiting low crystallinity (crystallinity index = 51.8%), as evidenced by their faint pattern. The crystallinity of pulp clearly increased after cooking, with the main peaks observed at 2θ of 22.5° and 18°, attributed to {020}, and the amorphous region of cellulose. Moreover, the crystallinity of P1, P2, P3, P4, P5, and P6 increased to 54.4, 55.6, 56.8, 57.2, 59.9, and 57.8%, respectively. This result is attributed to the following two reasons: the removal of disordered material in the amorphous region and the formation of new crystalline region, ascribed to the realignment of the cellulose chain caused by the penetration of water molecules into the amorphous region [19].Figure 2
XRD curves of different samples: (a) BR, (b) P1, (c) P2, (d) P3, (e) P4, (f) P5, and (g) P6.


## 3.4. SEM Images of Different Samples

Figure3 shows the SEM images of different samples, clearly displaying their surface morphology. The bamboo residues consist of piece structure, with several pits randomly distributed on the residue surface (Figure 3(a)). The bamboo fibers with complete shape and clear contours were obtained for the appropriate cooking process (P5, Figure 3(b)). Natural stellerite exhibits a clear layer structure (Figure 3(c)). Treatment with oxalic acid led to the formation of cracks on its surface, resulting in the promotion of pore formation at the stellerite surfaces and induced microscopic changes; this result is consistent with those shown in Table 2 (Figure 3(d)). Figure 3(e) shows the hand sheet without fillers, and Figure 3(f) demonstrates the distribution of granular-modified stellerite between fibers.Figure 3
SEM images of different samples: (a) BR, (b) P5, (c) natural stellerite, (d) modified stellerite, (e) hand sheet composed of P5 without stellerite, and (f) hand sheet composed of P5 with modified stellerite (9%).
(a) (b) (c) (d) (e) (f)


## 3.5. Ash Content and Filler Retention

Figure4 shows the ash content and filler retention of different paper sheets. With increasing stellerite content, ash content increases, and approximately 7.2% of ash was obtained with the addition of 15% stellerite. In contrast, filler retention significantly decreases.Figure 4
Ash content and filler retention of different paper sheets.


## 3.6. Tensile Indices and Air Permeability of Paper Sheets

Figure5 shows the effects of stellerite content on the tensile indices and air permeability of the paper sheets. Compared to the control (without stellerite), the tensile index of the paper sheet with the addition of 3% stellerite indicated a 3.7% increase; however, the ash content increased from 0.14 to 1.98%. Thus, under experimental conditions employed in this study, appropriate addition of cationic-starch-preblend-modified stellerite exerted a certain positive effect on the tensile index of the paper sheet, possibly attributed to the improvement of evenness. Moreover, with increasing filler content, air permeability also increased. With the addition of 15% stellerite, the air permeability of the paper sheet increased from 3.44 to 6.62 μm Pa−1 s−1, indicating that the porosity of the paper increased because of the addition of filler.Figure 5
Tensile indices and air permeability of paper sheets.


## 3.7. Filter Performance of Paper Sheets

Tables3 and 4 summarize the filter performance of different paper sheets and the impact of gas flowing velocities. The filter performance was suggested to be affected not only by the dosage of fillers, but also by the gas flowing velocities during testing. The best performance was obtained with the addition of 9% modified stellerite, predominantly attributed to the fact that extremely high air permeability of paper sheets results in the decline of adsorption quantity. This result indicates the existence of an important difference between fibers and fillers in the adsorption of PM2.5. It has been reported that micron wood fibers have low collection efficiency toward particles with the diameter from 0.4 to 0.6 μm, while they have significantly higher collection efficiency for particles with other sizes. Among these particles with the diameter of 0.01 μm, the collection efficiency of micron wood fibers can reach up to 90% [20].Table 3
Effect of the variation of stellerite content on filter performance∗.
Dosage of stellerite (%) 0 3 6 9 12 15  Filtration efficiency (%) 5 9.3 ± 2.1 72.5 ± 1.9 74.1 ± 2.3 78.4 ± 2.5 76.5 ± 2.9 75.8 ± 3.1 ∗Gas flowing velocity = 0.2 ms−1.Table 4
Effect of different gas flowing velocities on filter performance∗.
Gas flowing velocities (ms−1) 0.2 0.4 0.6 0.8  Filtration efficiency (%) 78.4 ± 2.8 69.7 ± 1.7 62.6 ± 2.5 58.2 ± 2.0 ∗Dosage of stellerite = 9%.In fact, the filtering process of PM2.5 particles by plant fibers and fillers is very complex and specific to location; therefore, filter performance is affected not only by the z-direction position, but also by time. This observation is referred to as layered filtration and nonstationary filtration (see Figure 6), which will be further explored in our future study.Figure 6
Filtration sketch of paper sheets.


## 4. Conclusions

In this study, the following optimum cooking condition of the bamboo residues by kraft pulping was established: a liquor ratio of 1 : 5.5, a cooking temperature of 160°C, and a holding time of 2 h. Modification with oxalic acid resulted in the promotion of pore formation at the stellerite surfaces, which induced microscopic changes while simultaneously maintaining the porous structure of stellerite. The cationic starch preblend method is a promising technique for papermaking as it results in the enhanced strength of paper. The filter performance of paper sheets was significantly increased by the addition of oxalic-acid-modified stellerite. With the addition of 9% oxalic-acid-modified stellerite, the paper sheet exhibited the best filter performance (78.4%) at a gas flowing velocity of 0.2 ms−1.



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*Source: 2198506-2016-12-27.xml*