Evaluation of absorption efficiency of Zeolite ZSM-5 in the removal of styrene vapors
Yazdani Aval M, MSc1, Mortazavi SB, PhD2*, Asilian Mahabadi H, PhD2
1- MSc in Occupational Health Engineering, Dept. of Occupational Engineering, Faculty of Medical Sciences, Tarbiat Modares University, Tehran, Iran. 2- Assistant Prof., Dept. of Occupational Engineering, Faculty of Medical Sciences, Tarbiat Modares University, Tehran, Iran.
Abstract Received: April 2016, Accepted: October 2016
Background: Volatile organic compounds (VOCs) are one of the most important and prevalent air pollutants. The vapor produced as a result of the vaporization of these compounds, even at very low concentrations, is harmful to the environment and human health. Thus, the aim of this study was to evaluate the removal of styrene vapor from the air flow using Zeolite (ZSM-5) in a continuous flow reactor. Materials and Methods: This cross-sectional study was conducted at a laboratory scale. Styrene concentrations of 200 and 300 ppm were selected for this study and steam saturation method was used to obtain the desired dynamic concentration. The desired concentration of dynamic styrene vapor was prepared in a fireproof cubic continuous flow reactor (canopy). ZSM-5 was synthesized and ground in a flat steel plate with standard mesh number of 20-40 and was used to remove the styrene vapors. In order to evaluate the removal efficiency, two variables of time and initial concentration of pollutant were investigated. In addition, scanning electron microscopy (SEM), X-ray powder diffraction (XRD), the Brunauer–Emmett–Teller (BET) technique, and energy-dispersive X-ray spectroscopy (EDX) were used to investigate the surface and quality of the obtained adsorbent. Results: The results of SEM and XRD indicated the uniform surface and high purity of the synthesized zeolite. Adsorption breakthrough and saturation for 200 ppm of styrene concentration occurred in the first 35 and 510 minutes of the experiment, and for 300 ppm of styrene concentration, occurred 23 and 385 minutes after the beginning of the test, respectively,. Conclusions: ZSM-5 showed a high level of efficiency in the removal of styrene vapors from polluted air; thus, it can be used to remove this pollutant from large industrial environments. |
Keywords: Styrene, Zeolites, Indoor Air, Absorption, Efficiency, Volatile Organic Compounds, Adsorption.
Introduction
Industrial development, in addition to human welfare, has resulted in numerous problems such as environmental pollution especially air pollution which has gradually become one of the major concerns of human communities (1). Volatile organic compounds (VOCs) are one of the most important and prevalent air pollutants. VOCs are carbon compounds which participate in photochemical reactions in the atmosphere (2). The vapor produced as a result of the vaporization of these compounds, even at very low concentrations, are harmful to the environment and human health (3); thus, the controlling of VOCs emissions is one of the most important prerequisites to observing the environmental protection rules in industrial settings. Styrene monomer (C6H5CH=CH2) is a VOC which is largely used in different industries. This substance is an oily VOC (4) which is usually produced as a result of the catalytic reaction of dehydrogenation and hydroperoxidation of ethylbenzene (5, 6). Styrene monomer is primarily used for the production of polystyrene (7). It is also used in different industries for the production of color, plastics, plastic coatings, artificial rubber, synthetic rubber, coatings, pipes, fittings, tanks, lighting tools, and corrosion-resistant products (6). This material may be absorbed by the body through inhalation, ingestion, and contact with the eyes and skin, leading to complications in the body. Among the complications and side effects caused by styrene we may note negative effects on the central nervous system, loss of concentration, fatigue, nausea, irritant contact dermatitis, and negative effects on the reproductive system (8). Results of a study by Vodicka et al. showed that exposure to styrene at concentrations of 10 ppm to 100 ppm and higher could cause irritation in the eyes, throat, and respiratory system (9). In addition, they reported that at a concentration of 376 ppm, it could increase nasal mucus secretion (9). In another study, Cherry and Gautrin reported that 23% and 71% of those, respectively, exposed to concentrations of less than 50 ppm and higher than 100 ppm had decreased level of central and peripheral nervous system activity (10). Based on the classification of the International Agency for Research on Cancer (IARC), styrene is classified in the possibly carcinogenic to humans group (11).
Previous studies have shown that many methods have been used to remove styrene from air in different workplaces (11, 12). However, most presented removal methods have some disadvantages that limit their use (13). Surface absorption method is one of the most commonly used processes for the removal of VOCs (14). In several studies, the efficiency of adsorbents in the removal of VOCs, such as styrene, has been proven (15-18). Among these adsorbents, active carbon and zeolite have been studied more. Although the specific surface area of active carbon is higher, zeolites have more arranged crystalline structures, compared to other adsorbents like active carbon and silica gel, so all the pore diameters in zeolites are similar and uniform. On the other hand, in recent years, zeolite has received more attention due to its unique properties such as crystallization, high surface area, acidity, and ion exchange capacity (19).
Zeolite (ZSM-5) is a type of zeolite which has high thermal resistance, high surface area, and low porosity; as a result, it is largely used for reduction and photo catalytic oxidation of organic compounds (20). To the best of our knowledge, no study has been performed on the use of this adsorbent for the removal of styrene from air stream. Therefore, the aim of this study was to investigate the removal of styrene from polluted air by ZSM-5 in a dynamic system.
Materials and Methods
This cross-sectional study was conducted at a laboratory scale. The desired concentration of dynamic styrene vapor was prepared using steam saturation method in a fireproof cubic continuous flow reactor (canopy).
Preparation of Zeolite ZSM-5: The synthetic compounds with a composition ratio of 2O:60SiO2:0.5Al2O3:936H2O TPA (12-O-tetradecanoylphorbol-13-acetate) was prepared by adding aluminum sulfate and silica to ammonium hydroxide solution 20% w/w in boiling water. After 10 minutes of stirring under reflux condition, a clear homogeneous solution was obtained. Then, the solution temperature was lowered to 25 °C. This transparent solution was poured into flasks that were placed in an oil bath containing reflux. Crystallization occurred at ambient pressure and at a temperature of 80 ºC for 72 hours. The obtained zeolite nanoparticles were separated from the solution via centrifugation at 5000 rpm. They were poured into distilled water and separated again using ultrasonic bath in order to obtain the concentrated colloidal suspension. To classify the sizes of ZSM-5 standard sieves with a mesh of 20 and 40 (ASTM, PA, USA) were, respectively, used to separate particle sizes of 0.85 and 0.425 mm. ZSM-5 with 20-40 mesh included particles that passed through the 20-mesh sieve, but remain on the 40-mesh sieve. Scanning electron microscopy (SEM), X-ray powder diffraction (XRD), Brunauer–Emmett–Teller (BET) technique, and energy-dispersive X-ray spectroscopy (EDX) were used to assess the surface and quality of the obtained adsorbent.
Reactor Design: The reactor system was a cube-shaped chamber with a length of 26 cm, a width of 10 cm, and a height of 15 cm (height of the reactor: 6 cm) and its base was like a canopy. Polluted air entered the cube-shaped chamber from the top and exited from the bottom (the canopy part). At a height of 5 cm from the chamber’s floor there was a stainless steel plate (standard mesh number of 40), on which 38.6 grams of heated ZSM-5 with a uniform distribution and a thickness of 2 mm was placed. Figure 1 shows a three-dimensional image of the reactor.
Figure 1: The three-dimensional image of the designed reactor
Concentration system: In order to supply the entrance air a 51 w pump with 147.11 mmHg pressure (Hitachi Ltd., Tokyo, Japan,) was used. For the removal of probable pollutants and controlling of humidity, the entrance air was passed through a vessel containing an activated charcoal bed and silica gel, and then, was entered into the concentration system.
Due to the likelihood of increasing of pump temperature during the experiment and the subsequent warming of the outlet air, the exhaust air tubes of the pump were placed into a plastic container filled with water so that it would reach the laboratory ambient temperature. The exhaust tube (which was placed inside the plastic container filled with water) was made of aluminum so that the air passing the tube could easily transfer its heat to the surrounding environment. The high heat capacity of water and high surface area of the plastic graduated cylinder helped to prevent significant change in the temperature of the glass thermometer placed in the water during the experiment. In addition, the high length (2 m) of the pump’s exhaust tube helped the air reach the laboratory ambient temperature. In this study, different concentration systems were evaluated, and ultimately, the steam saturation concentration system was used. For this purpose, a 500 ml gas washer bottle (Shot Co., Germany) was used. In order to ensure the accuracy of the operation, 3 alcohol thermometers were used; one was attached to the outer wall of the liquid container exactly next to a thermocouple sensor, another was placed in the chamber, and the third one was placed outside the isothermal box. Accordingly, the temperature outside the chamber and the accuracy of the displayed numbers were continuously monitored using a digital thermocouple.
Method of analysis: To evaluate the performance of the adsorbent, styrene, at the two concentrations of 200 and 300 PPM, was injected into the designed reactor. Using an automatic meter reading device (Model 5000, PhoCheck, UK) that works via Photo Ionization Detection (PID) method, the concentration of styrene in the air exiting the chamber was measured at intervals of 10 minutes. In order to ensure the accuracy of the collected data, each of the measurements was repeated at least 3 times. In order to ensure the accuracy of the measured data, the concentration of some random samples were also measured using gas chromatography (GC) (Model PU 4410, Philips, Amsterdam, Netherlands) which was equipped with a flame ionization detector (FID). Using a 5 ml gas syringe, 3 ml of the pollutant was quickly injected through the injector each time. Columns were used in the devices of the type Pack (length of 1.5 m and diameter of 4 mm). In order to conduct the decomposition, the standard 89 proposed by the Occupational Safety and Health Administration (OSHA) was followed which suggested a thermal plan of 200 ºC for the injector, 250 ºC for the detector, and 100 ºC for the column. Nitrogen (33 ml/minute) was used as the carrier gas. It was found that the PhoCheck and GC results were very close to each other and had a correlation (R2 = 0.977). Finally, in order to ensure the repeatability of the results, each experiment was repeated at least 3 times. Excel software (version 2013, Microsoft, Redmond, WA, USA) was used to draw the charts.
Figure 2: XRD pattern of synthesized Zeolite Socony Mobil-5
Results
Structural properties of Zeolite ZSM-5: Figure 2 shows the XRD patterns. The results showed a very good relationship between the crystal structure of the synthetized samples and the crystal structure of ZSM-5 catalyst described in the references. According to figure 2, the main peak of ZSM-5 crystal is 2θ = 28˚, with an intensity of about 700 counts. This shows that calcination temperature can be increased, but, because of surface area, this temperature is at its optimum.
Table 1: The results of the Scherrer equation
ʎ (Å) |
θ (radians) |
FWHM* (radians) |
Crystal size (nm) |
1.78901 |
0.4682 |
6.87×10-3 |
23.37 |
* Peak Width-Full Width at Half Maximum
The Scherrer equation was used to calculate the ZSM-5 particle size. The results obtained from the mentioned equation are presented in table 1.
The specific surface area, total pore volume, and mean pore diameter of ZSM-5 was measured using the BET technique. Table 2 shows the results of the BET method.
Table 2: Results of the Brunauer–Emmett–Teller analysis
Sample |
Specific surface area (m2/g) |
Mean pore diameter (nm) |
Total pore volume (cm3/g) |
ZSM5 |
529.24 |
2.3026 |
0.3047 |
ZSM-5: Zeolite Socony Mobil-5
Figure 3: Scanning Electron Microscopy images of Zeolite ZSM-5 at different magnifications
Based on the results of BET analysis, the surface area of ZSM-5 was 529.24 m2/g which suggested a significant increase in specific surface area of ZSM-5 as compared with the industrial samples (21).
The morphology of the samples was evaluated using SEM at a high magnification. The images obtained from SEM analysis are shown in figure 3. As shown in figure 3, ZSM-5 particles have a uniform size distribution and specific geometric shape close to a cube or rectangular cube.
The results of EDX analysis of synthesized ZSM-5 are shown in figure 4. The presence of O, Si, and Al in EDX elemental analysis can be observed which is indicative of the composition of the zeolite (zeolite is a type of aluminum silicate).
Figure 4: Structure of the synthesized Zeolite ZSM-5 analyzed via energy-dispersive X-ray spectroscopy
Regarding the peak obtained by the device, it should be mentioned that this method usually determines components heavier than the carbon which exists in the surface layer of the adsorbents. In this method, the device calculates the amount of each element at every desired sample surface through the integration of the graph surface of each element. The graph shows that silica and aluminum are among the important elements which exist in the structure of the studied zeolite. The results of this analysis showed that the ZSM-5 used in this study contained silica (27.91%) and aluminum (1.56%). The presence of SiO2/Al2O3 is one of the factors affecting the zeolite absorption rate. The proportion of SiO2/Al2O3 in the studied ZSM-5 was calculated as 19.88. This is compared with other commercial samples of ZSM-5 with different SiO2/Al2O3 ratios in table 3. As can be seen in table 3, with the decreasing of SiO2/Al2O3 ratio, the specific area of zeolite was increased.
Table 3: Comparison of the Zeolite ZSM-5 synthesis used in the present study and other commercial samples of Zeolite ZSM-5
Zeolite type |
Company |
SiO2/Al2O3 |
Surface area (m2/g) |
ZSM-5 |
Zeolyst(CBV 2314) |
23 |
425 |
ZSM-5 |
Zeolyst(CBV 28014) |
28 |
400 |
ZSM-5 |
Present study |
19/88 |
529/24 |
ZSM-5: Zeolite ZSM-5
The effect of time on the adsorption rate: Figure 5 shows the rate of styrene vapor absorption in an inlet concentration of 300 ppm by the ZSM-5 particles with 20-40 mesh at different times. In this experiment, after placing the ZSM-5 inside the reactor, the inlet air flow with a constant concentration was passed over the zeolite and the rate of vapor absorption over time was evaluated for all the samples. As shown in figure 5, at the beginning of the experiment, the absorption rate was about 100%, and after a period of 23 minutes, it reached the break point (5% of the inlet volume). Subsequently, the adsorption rate sharply reduced to the extent that, 395 minutes after the start of the experiment, the adsorbent was saturated; thus, the concentration of the input and output gases became the same and the absorption rate was reduced to 0.