Journal Pre-proof Application of Graphene Oxide Aerogel to the Adsorption of Polycyclic Aromatic Hydrocarbons Emitted from the Diesel Vehicular Exhaust Haolin Hsu, Chungyih Kuo, Jihmirn Jehng, Chientai Wei, Chingfeng Wen, Jeanhong Chen, Lungchuan Chen
PII:
S2213-3437(19)30537-8
DOI:
https://doi.org/10.1016/j.jece.2019.103414
Reference:
JECE 103414
To appear in:
Journal of Environmental Chemical Engineering
Received Date:
1 August 2019
Revised Date:
1 September 2019
Accepted Date:
13 September 2019
Please cite this article as: Hsu H, Kuo C, Jehng J, Wei C, Wen C, Chen J, Chen L, Application of Graphene Oxide Aerogel to the Adsorption of Polycyclic Aromatic Hydrocarbons Emitted from the Diesel Vehicular Exhaust, Journal of Environmental Chemical Engineering (2019), doi: https://doi.org/10.1016/j.jece.2019.103414
This is a PDF file of an article that has undergone enhancements after acceptance, such as the addition of a cover page and metadata, and formatting for readability, but it is not yet the definitive version of record. This version will undergo additional copyediting, typesetting and review before it is published in its final form, but we are providing this version to give early visibility of the article. Please note that, during the production process, errors may be discovered which could affect the content, and all legal disclaimers that apply to the journal pertain. © 2019 Published by Elsevier.
Application of Graphene Oxide Aerogel to the Adsorption of Polycyclic Aromatic Hydrocarbons Emitted from the Diesel Vehicular Exhaust
Haolin Hsua, Chungyih Kuob,1,*, Jihmirn Jehngc, Chientai Weib, Chingfeng
oo f
Wenb, Jeanhong Chena, **, Lungchuan Chena
pr
a Green Energy Technology Research Center, Kun Shan University, Tainan, Taiwan,
e-
71070
b Department of Public Health and Health Technology Center, Chung Shan Medical
Pr
University, Taichung, Taiwan, 40201
ur
Taiwan, 40201
na l
c Department of Chemical Engineering, National Chung Hsing University, Taichung,
** Co-Corresponding author: Prof. Jeanhong Chen
Jo
E-mail address:
[email protected] Tel.: +886 920 431177 * Corresponding author: Prof. Chungyih Kuo E-mail address:
[email protected] Tel: +886 4 24730022 ext. 11304 1
Fax: +886 4 22854734
Corresponding authors contributed equally to this work.
Pr
e-
pr
oo f
Graphical Abstract
na l
Highlights
1. The adsorption and sieving efficiency of GOA applied to the PAHs emitted from the
ur
vehicular exhaust by the dynamometer was first investigated. 2. More oxidation time enhanced the crystalline structure between the GOA layered sheets.
Jo
3. The carcinogenic BAP adsorption of the GOA was much better than that of XAD resin. 4. The GOA had better adsorption efficiencies of total PAHs in the engine idling condition. 5. The GOA adsorbent can be reused after three runs of the Soxhlet extraction and drying.
1
Abstract For reducing the carcinogenic BaP and polycyclic aromatic hydrocarbons (PAHs) from the moving and stationary pollution source in the atmosphere, this study demonstrated useful adsorbent of graphene oxide aerogel (GOA). The application of GOA to the
oo f
adsorption of polycyclic aromatic hydrocarbons (PAHs) emitted from diesel vehicular exhaust via the dynamometer was investigated. The surface morphology and microstructure
pr
of GOA were characterized by SEM, TEM, elemental analysis, Raman, and TGA.
e-
According to the result of XRD, the grain size of GOA after 5 hours of oxidation time increased to 28.0 nm with 38 layers estimated. It demonstrated that more oxidation time
Pr
greatly enhanced the crystalline structure and reformation between the GOA sheets. The
na l
GOA sheets possessed the molecular sieving property for the filtration and adsorption of carcinogenic PAH molecules due to the strong hydrogen bonding interaction along the
ur
edges and the Van der Waal's force interactions. Naphthalene, acenaphthene, benzo[a]pyrene (BaP), and dibenz[a,h]anthracene, were chosen to carry out the pre-test
Jo
adsorption experiments. Especially, the BaP compound was known to be carcinogens and mutagens for humans because of their carcinogenicity and genotoxicity. From the result of pre-test adsorption of PAHs, the BAP adsorption capacity of the GOA adsorbent (310 ng BaP / 1g GOA) in 1 hour was much better than that of XAD16 resin (0.060 ng / 1g
2
XAD16), which is the standard adsorbents of PAHs announced by the Environmental Protection Administration of Taiwan. Furthermore, the sample collection of PAHs emitted from the diesel exhaust was performed by using the vehicle dynamometer. At the idling speed, the best adsorption capacity of total PAHs per gram GOA was 12.1 μg g−1, and
oo f
better than that of XAD16 (1.03 μg g−1). Moreover, the adsorption sleeve and adsorbent of GOA material could be recycled and reused repeatedly. The structure of the GOA
pr
adsorbent has maintained after three runs of the Soxhlet extraction and drying. Nevertheless,
e-
the structure of XAD16 resin is decomposed obviously and decreased after the Soxhlet extraction. Owing to the superior adsorption capacity of PAHs and low synthesis cost, the
na l
adsorbent material in the future.
Pr
GOA material is possible to be one of the excellent environmental and air pollution
ur
Keyword: Graphene; Graphene oxide aerogel; Polycyclic aromatic hydrocarbons;
Jo
Benzo[a]pyrene; Vehicle dynamometer
3
1. Introduction Graphene derivative materials, such as graphene oxide (GO) [1], reduced graphene oxide [2], carbon aerogel [3] and graphene oxide aerogel (GOA) [4], have attracted worldwide attention in recent years because of their outstanding properties. Graphene exhibits
oo f
excellent physical and chemical properties and can be easily modified [5]. Recent researches have been reported that graphene-related materials present outstanding
pr
performance in many potential applications, including biosensors [6-8], supercapacitors
e-
[9-11], contamination removal, and extraction [12-15]. Graphene and GO are not similar to the Perovskite adsorbent [16], and retain the layer structure. Graphene demonstrates high
Pr
affinity to the polycyclic aromatic hydrocarbons (PAHs), and moreover, the hydrophobic
na l
properties and molecular sizes of the PAHs affect the adsorption of graphene and GO [15]. It is suggested that the high affinities of the PAHs to graphene and GO are achieved mainly
ur
by π–π electrostatic interactions and the sieving properties of the broad groove regions formed by wrinkles on surfaces [17, 18]. Therefore, graphene and graphite oxide materials
Jo
exhibit excellent performance in adsorption with PAHs and their derivatives [19]. PAHs are distinctive classes of steady organic compounds and one of the most hazardous
pollutants with two or more fused benzene rings in linear or cluster arrangements from natural as well as anthropogenic sources. They can pass easily through human cell
4
membranes and into cells [20-21]. They are known to be carcinogens and mutagens for humans because of their carcinogenicity and genotoxicity. In Taiwan, the number of car and motor vehicles has been progressively increasing. Moreover, the exhaust gases emitted by vehicles often contains lots of pollutants, including metal elements, suspended particular
oo f
matter, carbon monoxide [22], volatile organic pollutants [23], and PAHs, etc [24]. PAHs can exist in the gas phase ubiquitously once emitted into the atmosphere. Besides, they can
pr
also be adsorbed onto particle surfaces, such as soot and particulate matters. Therefore, they
e-
spread between gas and particle phases widely [25]. Vehicular emissions of particulate and gas-phase PAHs are of particular interest and importance because of their potentially toxic
Pr
and probable human carcinogenic compounds [26]. Furthermore, the rapid vehicular
na l
growth rate has increased the vehicular emissions, which have become one of the principal anthropogenic sources of PAHs in Taiwan. Nowadays, the removal of PAHs in the
ur
environment atmosphere is a significant worldwide matter. In this study, the main purpose was to examine the adsorption and sieving efficiency of
Jo
PAHs, which were emitted from vehicular exhaust via dynamometer. The reusing ability of GOA adsorbent for the PAHs was also performed. The GO was prepared according to the modified Hummer’s method [1, 4] as the raw material in the study. Different oxidation time (1h, 2h, 3h, 4h, and 5h) was particularly considered as an important controlling factor for
5
the crystalline of GOA nanosheets. Naphthalene (NAP), acenaphthene (ACP), benzo[a]pyrene (BaP), and dibenz[a,h]anthracene (DBA) were chosen to carry out the pre-test adsorption experiments. Sample collection of PAHs for exhaust gas was performed by using the vehicle dynamometer experiments. The polyurethane foam and commercial
oo f
XAD polymer resin are the standard adsorbents of PAHs announced by the Environmental Protection Administration of Taiwan. Owing to the superior adsorption capacity of PAHs
pr
and low synthesis cost, however, the GOA material is possible to be one of the excellent
Pr
e-
environmental and air pollution adsorbent material in the future.
2. Experimental
na l
2.1. Materials and preparations of GOA The powdered flake graphite was purchased from Lancaster Synthesis. ACS reagent
ur
grade concentrated nitric acid, sulfuric acid and hydrochloride acid (Fisher chemical) were
Jo
used in this work. 35% hydrogen peroxide solution was obtained from Tokyo Chemical Industry Co., Ltd. Amberlite® XAD16 was purchased from Sigma-Aldrich Products. From the product information sheet, the surface area is up to 800 m2 g−1. All other chemicals were purchased in analytical grade purity and used without further purification. Milli-Q water was used in all experiments. 6
Basically, the GO was prepared according to the modified Hummer’s method [1, 4] by using powdered graphite as the raw material in our laboratory. It is an oxidation process that can be used to produce graphite oxide and commonly used as a method of generating quantities of graphene oxide via various modifications. Scheme 1 shows the manufacturing
oo f
process of GOA. In particular, various acidification and oxidation time (1h, 2h, 3h, 4h, and 5h) was considered as an important parameter in this process. Then the raw GO gel is
pr
mixed with ethylene glycol and heated at 120 °C for a few hours to prepare a hydrogel.
e-
Then the resulting GO hydrogel was washed several times with a large amount of deionized water to neutral. Afterward, the GO solution was frozen in an air-conditioned environment
Pr
for 24 h and became a freezing hydrogel. After that, the freezing hydrogel was transferred
na l
to the freeze-drying machine set (FD3-12P-80, KINGMECH, Taiwan) at −85 ℃ for 72 h, and the GOA was prepared. With different oxidation time, the black GOA and light brown
ur
one were obtained in this research.
Jo
Position of Scheme 1
2.2. Sample collection of PAHs from the pre-test and vehicle dynamometer experiments Four PAH compounds, NAP, ACP, BaP, and DBA are chosen to carry out the pre-test
7
experiments. These PAHs were placed in the middle of the horizontal tube furnace and then heated to evaporate. The PAH concentration introduced to a detection column filled with a GOA or a XAD16 resin under room temperature at a low volumetric flow rate for 5, 10, 15, 30, and 60 minutes. Finally, samples of the PAH concentrations for the various
oo f
gas-introducing duration were collected and analyzed. GO is evenly distributed in
deionized water, and then the solution is lyophilized after being filled in a glass
pr
sleeve. In such a manner, the carbon aerogel can overcome the assembly difficulties
e-
to the sleeve with a small diameter. It shows that the carbon aerogel has excellent filling properties to containers having various shapes or various sizes.
Pr
Sample collection of PAHs for exhaust gas was carried out by using the vehicle dynamometer experiments as shown in Fig. 1. The test vehicle was positioned on the
na l
chassis dynamometer, and then its engine idled and warmed up for constant duration
ur
by a stand-by mode. After which, an exhaust vent of the vehicle was directly connected to a quartz tube. In order to simulate the real driving emission of the
Jo
vehicle, a dilution chamber and a condensation machine were not considered, and an adsorbing sleeve was connected to the quartz tube. A low-volume air sampler pump was used to ensure the adsorbing sleeve fully collecting a constant volume of the exhaust gas for various driving rates and various driving durations. The total exhaust
8
gas volume was 75, 225 and 375L, respectively. The collection was performed at idle speed, a low speed, or a high speed to estimate the adsorption efficiency, the recycling efficiency, and the reuse efficiency of the adsorbent materials.
oo f
Position of Fig. 1
pr
2.3. Analysis of PAHs from pre-experiment and vehicle dynamometer experiments
e-
Total PAHs in the samples of the pre-test and vehicle dynamometer experiments were Soxhlet-extracted using a 300 and 600 mL high-purity mixture of organic solvents
Pr
(n-hexane and dichloromethane in a 1:1 volumetric ratio) for 24 h, respectively. The
na l
extracted PAHs were dried using a rotating evaporator and then purified using a silica gel cleanup set. The samples that remained in the silica gel columns were diluted with 60 ml of
ur
n-hexane. The runoff solution was filtered through a 0.45 μm PTFE membrane and dried using a rotating evaporator. 30 PAHs were quantified by gas chromatography/mass
Jo
spectrometry (Varian CP 3900/Saturn 2100 T) with a capillary column (30 m × 0.25 mm × 0.10 μm). Compounds monitored in this work included naphthalene (NAP), acenaphthylene (ACPy), acenaphthene (ACP), fluorene (FLU), phenanthrene (PHE), anthracene (ANTHR), fluoranthene
(FLT),
pyrene
(PYR),
benzo(c)phenanthrene
(BcPH),
9
benzo(b)napth(2,1-d)thiophene (BNT), cyclopenta(cd)pyrene (CPP), benz(a)anthracene (BaA), chrysene (CHR), benzo(b)fluoranthene (BbF), benzo(k)fluoranthene (BkF), benzo(e)pyrene (BeP), Benzo[a]pyrene (BaP), pyridine (PYL), Indeno[1,2,3-cd]pyrene (IND), dibenz(ah)anthrancene (DBA), BghiP, anthanthrene (ANTHA), Dibenzo[a,l]pyrene
(2Me-NAP),
1-methylfluorene
(1Me-FLU),
oo f
(DBalP), Coronene (COR), 1-methylnaphthalene (1Me-NAP), 2-methylnaphthalene 2-methylphenanthrene
(2Me-PHE),
pr
3-methylphenanthrene (3Me-PHE), and 3,6-dimethylphenanthrene (3,6Me-PHE). A
e-
standard solution consisting of known amounts of thirty PAHs dissolved in dichloromethane was prepared to spike with a known volume of naphthalene-d8,
Pr
phenanthrene-d10, and perylene-d12 as the internal standard. An internal standard was also
na l
added to the collected samples of each analytical batch. Known volumes of PAHs standard were spiked into GOAs to determine the efficiency of the extraction and analysis. The
ur
extraction efficiency yielded agreements between 75 ‒ 125 %, except for the lower molecular weight species of NAP, ACP, ACPy, and Me-NAP. The extraction method was
Jo
assessed for linearity, recovery, reproducibility, the limit of detection (LOD) and limit of quantification (LOQ) before sample analysis. LOD value was estimated from sequential injections of diluted standard solutions by using a signal-to-noise ratio of 3. The measured concentrations from most samples were higher than the limit of LOQ.
10
2.4. Characterization Surface morphology and structure of GOA were investigated with a field-emission scanning electron microscope (FESEM, JSM-6700F, JEOL) equipped with an energy-dispersive X-ray spectroscopy (EDX) detector (Oxford Instruments). Besides,
oo f
high-resolution transmission electron microscopy (HRTEM, JEOL JEM-2010, operated at 200 kV) was also employed to monitor the morphology and layers of the GOA. Elemental
pr
analysis (EA) results were obtained with a Heraeus CHN-O-S-Rapid Analyzer F002 to
e-
determine the contents of carbon, hydrogen, and oxygen in the GOA. Raman spectra were recorded using a Tokyo Instruments spectrometer with He–Ne 632.8 nm laser source. The
Pr
thermal stability of GOA was performed by using a thermogravimetric analysis (TGA) system (PerkinElmer Pyris 1 series). Typically, 10 mg of sample was heated from 100 to
na l
800 ℃ at a heating rate of 10 ℃ min−1 in N2 atmosphere. The Brunauer-Emmett-Teller
ur
(BET) specific surface area of the GOA before and after combustion was determined by N2 adsorption/desorption at −196 °C using a Micromeritics ASAP 2020, America. The X-ray
Jo
diffraction (XRD) data was investigated by using the instrument (MAC Science, MO3XHF) with a CuKα radiation source (λ= 1.54056 Å), and recorded from 2º to 80º at a scanning rate of 2º min−1.
11
3. Results and discussion The typical FESEM and HRTEM images of GOA are presented in Fig. 2a-b and c-d, respectively. The surface morphology of GOA can be confirmed by the broad wrinkled sheet without clear crack and gap structure, and obtained at low (Fig. 2a and Fig. 2c) and
oo f
high (Fig. 2b and Fig. 2d) magnification images. The TEM images revealed that GOA film was more smooth and transparent with fewer wrinkles (red arrows) as shown in Fig. 2c and
pr
Fig. 2d. Besides, it appears that the GOA sheet consists of about 8-10 graphene layers from
e-
the edges of GOA sheets [16, 27]. Because of the broad wrinkled sheet without clear crack and gap structure, and the hydrogen bond between GOA layers, the measured surface area
Pr
of GOA via Hummer's method is usually small [28]. As shown in Fig. S5a, N2
na l
adsorption-desorption isotherms of the GOA before and after short ambient combustion were measured to evaluate the specific surface area. The BET specific surface area of raw
ur
GOA was 5 m2 g‒ 1 and with H4 loop with the narrow slit-like pore [29]. Fig. S5b shows the pore-size (diameter) distributions with a major pore-size ~ 1nm. However, the specific
Jo
surface area of GOA after combustion raised to 200 m2 g‒ 1 and obtained a type IV isotherm with H3 and H2 hysteresis loops, indicating mesoporous pore mainly. It demonstrates that the gaseous nitrogen molecules adsorbed and desorbed easily because strong affinity and weak hydrogen bonding interaction between graphene layers. Furthermore, we suggest that
12
GOA sheets possess the molecular sieving property for applying to the filtration and adsorption of carcinogenic PAH molecules due to the low specific surface area. The surface morphology of the announced commercial XAD16 resin adsorbent with a high surface area about 800 m2 g‒ 1 is presented in Fig. 2e-f. From EDX results, the XAD16 were mainly
oo f
composed of carbon and oxygen elements.
e-
pr
Position of Fig. 2
Elemental analysis results of the graphite powder, GOA and XAD16 are listed in Table 1
Pr
to indicate the contents before and after modified Hummer's method. The relative atomic
na l
molar ratios of C/O were approximately 168.2:1, 7.7:1 and 9.0:1 for the raw graphite powder, GOA, and GOA after ambient combustion, respectively. The C/O ratio of graphite
ur
powder after oxidation was decreased to 7.7:1. Moreover, the C/O ratio of GOA after combustion was further increased from 7.7:1 to 9.0:1, owing to the removal of surface
Jo
functional groups (e.g., carboxylic groups, epoxy groups, hydroxyl groups, and carbonyl groups). Therefore, these results indicate that the content of oxygen atoms after the oxidation process increased. The relative C/O ratio of polymeric resin XAD16 is 17.8:1. It is significantly different compared to GOA.
13
Position of Table 1
Raman spectra of the raw graphite powder, GOA, and XAD16 with a laser wavelength at
oo f
632.8 nm are shown in Fig. 3(a). The characteristic disorder and graphitic peaks of graphite and GOA were D band (1350 cm− 1) and G band (1580 cm− 1), respectively. In addition, the
pr
peaks named G' band which is the overtone of the D band was also observed at 2700 cm− 1
e-
[30]. According to the observation of the Raman shifts of 1000, 1604, 2904, and 3054 cm−1, the composition of XAD16 resin were determined mainly polystyrene [31]. The relative
Pr
intensity ratio of G band to D band, IG/ID, demonstrates the quality of graphitization or
na l
defective disorders on carbon materials. In this study, the IG/ID ratio of the raw GOA (0.881) is lower than that of graphite powder (3.379), indicating that the functional groups formed
ur
onto the surface and edge of graphene sheets via the modified Hummer's method. Fig. 3b shows the TGA weight loss curves of the graphite powder and GOA. From the TGA result,
Jo
the graphite powder is stable with higher temperature treatments from 100 to 800 °C, and about 5.8% weight loss. The GOA begins to lose weight from 100 to 300 °C because of the decomposition of functional groups and hydrogen bound between GOA layers. The GOA material is lower thermal stable than graphite powder, and its estimated weight loss is ~
14
49.2% at 800 °C. It reveals that the GOA is more thermal stable than other carbon material we synthesized before [32], showing the better crystalline structure in GOA layers.
oo f
Position of Fig. 3
Fig. 4a shows the powder XRD patterns of the graphite powder and GOA. For the
pr
graphite powder, the basal spacing (d002) reflection obtained at a 2θ value of 26.5º
e-
corresponding to an interlayer distance of 3.40 Å. The basal spacing (d004) reflection also obtained at a 2θ value of 54.6º corresponding to an interlayer distance of 1.68 Å. After the
Pr
oxidation via the Hummer’s method, a larger basal spacing (d001) reflection of GOA
na l
observed at 2θ = 9.8º corresponding to an interlayer distance of 9.03 Å. The characteristic basal spacing reflections of d002 and d004 almost not observed. The Scherrer equation is a
ur
widely used tool to determine the nano-scale crystallite size of polycrystalline samples [33]. The crystallite size (D) of the GOA was estimated by the Scherrer equation:
Jo
D = 0.91 × λ / ( B × cosθ ),
where 0.91 is the shape factor constant; λ is the wavelength of the Cu K radiation source (0.15418 nm); B is the half-width of the strongest diffraction peak, and θ is its diffraction angle (in radian unit) of the strongest diffraction peak. Furthermore, the full width at half
15
maximum (FWHM) of XRD profiles is used to characterize different material properties and surface integrity features. Fig. 4b-c shows the effect of oxidation time on the diffraction angle and the basal d spacing. It shows a steady increase in diffraction angle and a decrease in basal d spacing
oo f
with increasing oxidation time. Peak width due to crystallite size varies inversely with crystallite size. By calculation with the XRD result, FWHM and the Scherrer equation, the
pr
grain sizes of graphite powder and GOA were estimated in 39.4 nm and 14.0 nm,
e-
respectively. In addition, it shows that the crystalline graphite powder and GOA possessed approximate 116 and 20 layers, respectively. Moreover, the grain size of GOA after 5 hours
Pr
of oxidation time increased to 28.0 nm with 38 layers estimated. We suggest that more
ur
GOA layers.
na l
oxidation time extremely enhanced the crystalline structure and reformation between the
Jo
Position of Fig. 4
Four PAH compounds (NAP, ACP, BaP, and DBA) with high toxic equivalency
factors (TEFs) were chosen to carry out the pre-test experiments [34]. The possible adsorption mechanism and diagram is drawn as scheme 2. Due to the hydrogen bonding
16
interaction along the edge, the surface morphology of GOA became the broad wrinkled sheets. In Scheme 2, large molecular size of the PAHs filtered on the surface of GOA, and besides, the PAHs adsorbed onto the surface of GOA by the Van der Waal's force interaction. Molecular sieving effect and the Van der Waal's force interaction were mainly
oo f
physical adsorption mechanism between PAHs and GOA. Fig. 5 shows the PAH concentrations of NAP, ACP, BaP, and DBA adsorbed by XAD16
pr
and GOA material adsorbents in 5, 10, 15, 30, and 60 minutes. Additionally, these four
e-
PAHs concentrations analyzed in detail are shown in Table 2. For these PAH compounds, the GOA material adsorbent had higher adsorption concentrations than the XAD resin one.
Pr
Especially, the XAD resin adsorbent has poor adsorption affinity for the linear five fused
na l
benzene rings compound (DBA). The NAP compound was a low molecule weight PAH and easier to vaporize than the DBA compound, which was a high molecule weight PAH of
ur
five fused benzene rings. In addition, the DBA concentrations were not detected for any time by using the XAD resin adsorbent. It reveals that the XAD resin material does not
Jo
have the ability to adsorp the high molecular weight PAH compound. Furthermore, BaP is considered to be highly carcinogenic to humans and adsorbed by the XAD resin announced by the Environmental Protection Administration of Taiwan. However, the BAP adsorption capacity in 1 hour of the GOA adsorbent (310ng BaP / 1g GOA) was a thousand times
17
better than that of XAD resin one (0.060 ng BaP / 1g XAD16). It demonstrates that the GOA adsorbent material has excellent adsorption efficiency for BaP than the XAD resin according to the pre-test result. From the result of FESEM and pre-test, GOA layered sheets possess the molecular sieve property to filtrate and adsorb PAHs compounds efficiently.
oo f
Furthermore, we suggested that the GOA adsorbent material seems to be an excellent material to use as the PAHs adsorbent for the following vehicle dynamometer
na l
Pr
Position of Fig. 5, scheme 2, and Table 2
e-
dynamometer simulation experiments.
pr
experiments. The further work of adsorption efficiency was carried out by real vehicle
Fig. 6 shows the total PAHs concentrations adsorbed by per gram XAD16 (Fig. 6a) and
ur
GOA (Fig. 6b) adsorbent at 0 (idling speed), 30 and 60 km h− 1 speed. The adsorption quantity of total PAHs by the adsorbents of XAD16 and GOA all increased with the engine
Jo
running time. Compared to three sampling speeds, the highest adsorption quantity of total PAHs is obtained at idling speed. It demonstrates that the higher engine temperature makes the combustion reaction of the diesel oil more complete, and generate more carbon dioxide and water. Besides, the PAHs compound emissions will be significantly improved and
18
reduced due to the higher speed engine temperature. At the idling speed, the best adsorption efficiencies of total PAHs per gram GOA is 12.1 μg g− 1, and better than that of XAD16 (1.03 μg g− 1). In comparison with previous literature, the adsorption of PAH compound of fluoranthene was investigated and possessed adsorption capacity of 2.212 mmol g− 1 ( ~
oo f
1.09 μg g− 1) [18]. Nevertheless, the sum of total PAHs by using the solid phase extraction [35-36] was lower than the result of vehicle dynamometer simulation experiments. It shows
pr
that the GOA material adsorbent has excellent adsorption capacity. At 60 km h− 1 speed, the
e-
total PAHs weight adsorbed by the XAD16 and GOA material is shown in Fig. 6c. Because the amount of XAD16 used as the sampling adsorbent is more than that of GOA, the total
Pr
PAHs concentration adsorbed by XAD16 is higher than GOA one. The total PAHs
na l
adsorbed efficiency based on per gram adsorbent is further shown in Fig. 6d. After evaluation and calculation, the adsorbed total PAHs concentration based on per gram GOA
ur
is much higher than that of XAD16. The GOA material has great potential to substitute the expensive commercial XAD resin adsorbent to lower the manufacturing cost in the future.
Jo
As is known to all, the adsorbent's reusability is decisive and crucial to the practical
application, due to the manufacturing expense and mechanical property. The tests of the reusability of XAD16 and GOA were conducted repeatedly at the same condition, and the adsorption plug tubes were also recycled and reused again. Because of the limitation of
19
frequency and time for operating vehicle dynamometer, the efficiency of the reusability at 60 km h− 1 speed was mainly achieved. Fig. 6e shows the reusability of XAD16 and GOA adsorbent material. First of all, the manufacturing cost of the GOA adsorbent via this process is much lower than the XAD16 resin. The real vehicle dynamometer temperature of
oo f
test adsorbent is lower than 150℃. According to the TGA result at 150℃ in Fig. 3, the structure of GOA material decomposed about 3 weight percent. The structure of GOA
pr
adsorbent has maintained after three runs of the Soxhlet extraction and drying. Nevertheless,
e-
the structure of XAD16 resin is decomposed apparently and decreased after the Soxhlet extraction. The total PAHs concentration analyzed in the first run was the lowest during
Pr
these three reused runs because there were a regular vehicle inspection and mechanical
na l
adjustment of the exhaust black smoke detection. However, it obviously demonstrates that the adsorption sleeve and adsorbent of GOA material can be recycled and reused repeatedly.
ur
There is not much difference in the concentration of total PAHs adsorbed by the second and third adsorption runs. Nevertheless, the adsorption efficiency of XAD16 resin material in
Jo
recycling reuse significantly reduces.
Position of Fig. 6
20
From the result of analysis FESEM, XRD, TGA and vehicle dynamometer experiment data, it appears that the GOA sheets possess the molecular sieve property to the filtration and adsorption of carcinogenic PAH molecules. In addition, it shows that the crystalline graphite powder and GOA possessed approximate 116 and 20 layers, respectively.
oo f
Moreover, the grain size of GOA after 5 hours of oxidation time increased to 28.0 nm with 38 layers estimated. We suggested that more oxidation time extremely enhanced the
pr
crystalline structure and reformation between the GOA layers. From the result of pre-test
e-
adsorption of PAHs, the BAP adsorption capacity of the GOA adsorbent in 1 hour was a thousand times better than that of XAD resin. The highest adsorption quantity of total
Pr
PAHs is obtained at idling speed via the vehicle dynamometer experiments. At the idling
na l
speed, the best adsorption efficiencies of total PAHs per gram GOA is 12.1 μg g − 1, and better than that of XAD16. The structure of GOA adsorbent has maintained after three runs
ur
of the Soxhlet extraction and drying. Nevertheless, the structure of XAD16 resin is decomposed obviously and decreased after the Soxhlet extraction. In apparent, the GOA
Jo
material has great potential and opportunity to substitute the expensive commercial XAD resin adsorbent to lower the manufacturing cost in the future.
21
4. Conclusions In this study, the GOA layers particularly become more crystalline structure enhanced by more oxidation time. We demonstrate that the GOA sheets possess the molecular sieve property to the filtration and adsorption of carcinogenic PAH molecules. Especially, the
oo f
XAD resin adsorbent has poor adsorption affinity for the linear five fused benzene rings compound (DBA). Besides, that GOA material has outstanding adsorption efficiency for
pr
human carcinogenic BaP. Additionally, GOA presents excellent adsorption quantity of total
e-
PAHs than that of XAD one. Furthermore, the structure of GOA material decomposed about 3 weight percent at 150℃. The structure of GOA adsorbent still maintains after three
Pr
runs of the Soxhlet extraction and drying. Nevertheless, the structure of XAD16 resin is
na l
decomposed apparently and decreased after the Soxhlet extraction. The adsorption sleeve and adsorbent of GOA material can be recycled and reused repeatedly. Because of the
ur
superior adsorption capacity of PAHs and low synthesis cost, the GOA material is possible
Jo
to be the perfect useful environmental and air pollution adsorbent material in the future.
Acknowledgments Financial support of the National Science Council of Taiwan (104-2622-E-040-001-CC2 and 105-2622-E-040-001-CC2) and the Featured Areas Research Center Program within
22
the Higher Education Sprout Project by the Ministry of Education of Taiwan (107-N-270-EDU-T-142) is gratefully acknowledged. The support of vehicle dynamometer experiments from the Taichung City Government Diesel Vehicle Smoke Exhaust
oo f
Inspection Station is also acknowledged and appreciated.
References
pr
[1] D.C. Marcano, D.V. Kosynkin, J.M. Berlin, A. Sinitskii, Z. Sun, A. Slesarev, L.B.
e-
Alemany, W. Lu, J.M. Tour, Improved synthesis of graphene oxide, ACS Nano 4 (2010) 4806–4814.
Pr
[2] H. He, C. Gao, General Approach to individually dispersed, highly soluble, and
na l
conductive graphene nanosheets functionalized by nitrene chemistry, Chem. Mater. 22 (2010) 5054–5064.
ur
[3] W. Wan, R. Zhang, W. Li, H. L, Y. Lin, L. Li, Y. Zhou, Graphene–carbon nanotube aerogel as an ultra-light, compressible and recyclable highly efficient absorbent for oil
Jo
and dyes, Environ. Sci.: Nano 3 (2016) 107–113.
[4] T.H. Tu, P.T.N. Cam, L.V.T. Huy, M.T. Phong, H.M. Nam, N.H. Hieu, Synthesis and application of graphene oxide aerogel as an adsorbent for removal of dyes from water, Mater. Lett. 238 (2019) 134–137.
23
[5] A.K. Geim, Graphene: status and prospects, Science 324 (2009) 1530–1534. [6] G. Bharath, R. Madhu, S.M. Chen, V. Veeramani, A. Balamurugan, D. Mangalaraj, C. Viswanathan, N. Ponpandian, Enzymatic electrochemical glucose biosensors by mesoporous 1D hydroxyapatite-on-2D reduced graphene oxide, J. Mater. Chem. B 3
oo f
(2015) 1360–1370. [7] Y. Guo, Y. Han, S. Shuang, C. Dong, Rational synthesis of graphene–metal
pr
coordination polymer composite nanosheet as enhanced materials for electrochemical
e-
biosensing, J. Mater. Chem. 22 (2012) 13166–13173.
[8] M. Li, Y. Wang, Q. Liu, Q. Li, Y. Cheng, Y. Zheng, T. Xi, S. Wei, In situ synthesis and of
nano
hydroxyapatite
Pr
biocompatibility
on
pristine
na l
and chitosan functionalized graphene oxide, J. Mater. Chem. B 1 (2013) 475–484. [9] F. Li, L. Xie, G. Sun, F. Su, Q. Kong, Q. Li, Y. Chao, X. Guo, C. Chen, Boosting the
ur
specific surface area of hierarchical porous carbon aerogel by multiple roles of the catalyst towards high-performance supercapacitors, ChemElectroChem 4 (2017)
Jo
3119–3125.
[10] H.C. Chen, C.C. Wang, S.Y. Lu, γ-Fe2O3/graphene nanocomposites as a stable high performance anode material for neutral aqueous supercapacitors, J. Mater. Chem. A 2 (2014) 16955–16962.
24
[11] V. Kuzmenko, N. Wang, M. Haque, O. Naboka, M. Flygare, K. Svensson, P. Gatenholm, J. Liu, P. Enoksson, Cellulose-derived carbon nano fibers/graphene composite electrodes for powerful compact supercapacitors, RSC Adv. 7 (2017) 45968–45977.
oo f
[12] S.M. Alatalo, F.D. Pileidis, E. Mäkilä, M. Sevilla, E. Repo, J.J. Salonen, M. Sillanpää, M.M. Titirici, Versatile cellulose-based carbon aerogel for the removal of both cationic
pr
and anionic metal contaminants from water, ACS Appl. Mater. Interfaces 7 (2015)
e-
25875–25883.
[13] N. T. Hoai, N. N. Sang, T. D. Hoang, Thermal reduction of graphene-oxide-coated
Pr
cotton for oil and organic solvent removal, Mater. Sci. Eng. B 216 (2017) 10–15.
na l
[14] F. Wang, J.J.H. Haftka, T.L. Sinnige, J.L.M. Hermens, W. Chen, Adsorption of polar, nonpolar, and substituted aromatics to colloidal graphene oxide nanoparticles, Environ.
ur
Pollut. 186 (2014) 226–233.
[15] S. Dong, G. Huang, M. Su, T. Huang, Environmentally friendly method: Development
Jo
and application to carbon aerogel as sorbent for solid-phase extraction, ACS Appl. Mater. Interfaces 7 (2015) 22256–22263.
[16] Y. Wang, Y. Wang, L. Yu, J. Wang, B. Du, X. Zhang, Enhanced catalytic activity of templated-double perovskite with 3D network structure for salicylic acid degradation
25
under microwave irradiation: Insight into the catalytic mechanism, Chem. Eng. J. 368 (2019) 115–128. [17] J. Wang, Z. Chen, B. Chen, Adsorption of polycyclic aromatic hydrocarbons by graphene and graphene oxide nanosheets, Environ. Sci. Technol. 48 (2014) 4817–4825.
oo f
[18] C. Zhang, L. Wu, D. Cai, C. Zhang, N. Wang, J. Zhang, Z. Wu, Adsorption of Polycyclic Aromatic Hydrocarbons (Fluoranthene and Anthracenemethanol) by
pr
Functional Graphene Oxide and Removal by pH and Temperature–Sensitive
e-
Coagulation, ACS Appl. Mater. Interfaces 5 (2013) 4783–4790.
[19] L. Ji, W. Chen, Z. Xu, S. Zheng, D. Zhu, Graphene nanosheets and graphite oxide as
Pr
promising adsorbents for removal of organic contaminants from aqueous solution, J.
na l
Environ. Qual. 42 (2013) 191–198.
[20] C.A. Pope, R.T. Burnett, M.J. Thun, E.E. Calle, D. Krewski, K. Ito, G.D. Thurston,
ur
Lung cancer, cardiopulmonary mortality, and long-term exposure to fine particulate air pollution, JAMA 287 (2002) 1132–1141.
Jo
[21] J.D. Pleil, A.F. Vette, B.A. Johnson, S.M. Rappaport, Air levels of carcinogenic polycyclic aromatic hydrocarbons after the World Trade Center disaster, PNAS 101 (2004) 11685–11688. [22] X. Zhang, H. Li, Y. Yang, T. Zhang, X. Wen, N. Liu, D. Wang, Facile synthesis of
26
new efficient Cu/MnO2 catalysts from used battery for CO oxidation, J. Environ. Chem. Eng. 5 (2017) 5179–5186. [23] X. Zhang, X. Lv, X. Shi, Y. Yang, Y. Yang, Enhanced hydrophobic UiO-66 (University of Oslo 66) metal-organic framework with high capacity and selectivity for
oo f
toluene capture from high humid air, J. Colloid. Interf. Sci. 15 (2019) 152–160. [24] S.H. Chang, M.Y. Hsieh, H.J. Yang, M.C. Chen, C.Y. Kuo, Effects of diesel vehicle
pr
emissions of polycyclic aromatic hydrocarbons on the surrounding environment and
e-
residents, J. Environ. Sci. Health C 27 (2009) 141–154.
[25] E. Demircioglu, A. Sofuoglu, M. Odabasi, Particle-phase dry deposition and air-soil
na l
Mater. 186 (2011) 328–335.
Pr
gas exchange of polycyclic aromatic hydrocarbons (PAHs) in Izmir, Turkey, J Hazard
[26] C.Y. Kuo, H.C. Chen, F.C. Cheng, L.R. Huang, P.S. Chien, J.Y. Wang, Polycyclic
ur
aromatic hydrocarbons in household dust near diesel transport routes, Environ, Geochem Health 34 (2012) 77–87.
Jo
[27] M.A. Worsley, J.H. Satcher, T.F. Baumann, Synthesis and characterization of monolithic carbon aerogel nanocomposites containing double-walled carbon nanotubes, Langmuir 24 (2008) 9763–9766. [28] A. Garcia-Gallastegui, D. Iruretagoyena, V. Gouvea, M. Mokhtar, A.M. Asiri, S.N.
27
Basahel, S.A. Al-Thabaiti, A.O. Alyoubi, D. Chadwick, M.S.P. Shaffer, Graphene oxide as support for layered double hydroxides: enhancing the CO2 adsorption capacity, Chem. Mater. 24 (2012) 4531–4539. [29] IUPAC Recommendations, Pure Appl. Chem. 57 (1985) 603–619.
oo f
[30] H.L. Hsu, J.M. Jehng, Y. Sung, L.C. Wang, S.R. Yang, The synthesis, characterization of oxidized multi-walled carbon nanotubes, and application to surface acoustic wave
pr
quartz crystal gas sensor, Mater. Chem. Phys. 109 (2008) 148–155.
e-
[31] A. Palm, Raman spectrum of polystyrene, J. Phys. Chem. 55 (1951) 1320-1324. [32] H.L. Hsu, J.M. Jehng, Synthesis and characterization of carbon nanotubes on clay
Pr
minerals and its application to a hydrogen peroxide biosensor, Mater. Sci. Eng. C 29
na l
(2009) 55–61.
[33] A.D. Dysart, X.L. Phuah, L.K. Shrestha, K. Ariga, V.G. Pol, Room and elevated
ur
temperature lithium-ion storage in structurally submicron carbon spheres with mechanistic, Carbon 134 (2018) 334–344.
Jo
[34] I.C.T. Nisbet, P.K. LaGoy, Toxic equivalency factors (TEFs) for polycyclic aromatic hydrocarbons (PAHs), Regul. Toxicol. Pharmacol. 16 (1992) 290–300.
[35] R. Shi, L. Yan, T. Xu, D. Liu, Y. Zhu, J. Zhou, Graphene oxide bound silica for solid-phase extraction of 14 polycyclic aromatic hydrocarbons in mainstream cigarette
28
smoke, J. Chromatogr. A 1375 (2015) 1–7. [36] Y. Zhang, H. Zhou, Z.H. Zhang, X.L. Wu, W.G. Chen, Y. Zhu, C.F. Fang, Y.G. Zhao, Three-dimensional ionic liquid functionalized magnetic graphene oxide nanocomposite for the magnetic dispersive solid phase extraction of 16 polycyclic aromatic
Jo
ur
na l
Pr
e-
pr
oo f
hydrocarbons in vegetable oils, J. Chromatogr. A 1489 (2017) 29–38.
29
Captions: Fig. 1. Schematic illustration for vehicle dynamometer sampling tests.
Fig. 2. (a-b) FESEM and (c-d) TEM images of GOA; and (e-f) FESEM images of XAD16
oo f
resin.
e-
weight loss curves of the graphite powder and GOA.
pr
Fig.3. (a) Raman spectra of the graphite powder, GOA, and XAD16 resin; and (b) TGA
Pr
Fig. 4. (a) Powder XRD patterns of the graphite powder and GOA; (b) XRD diffraction
na l
patterns of GOAs after the oxidation time of 1h, 2h, 3h, 4h and 5h; and (c) the plot of the
ur
effect of oxidation time on the diffraction angle and basal d spacing.
Fig. 5. PAH concentrations of NAP, ACP, BaP and DBA adsorbed by (a) XAD16 and (b)
Jo
GOA adsorbent in 5, 10, 15, 30, and 60 minutes.
Fig. 6. Total PAHs concentration adsorbed by (a) XAD16 and (b) GOA adsorbent at 0 (idling state), 30 and 60 km h− 1 speed; (c) Total PAHs weight amount adsorbed by XAD16
30
and GOA at 60 km h− 1 speed and (d) after calculation based on per gram XAD16 and GOA; and (e) The reusability of XAD16 and GOA adsorbent material.
oo f
Table 1 EA results of raw graphite powder, GOAs, and XAD16
Table 2 The PAH concentrations of NAP, ACP, BaP, and DBA adsorbed by XAD16 and
e-
pr
GOA adsorbent in 5, 10, 15, 30, and 60 minutes
Pr
Scheme 1 The manufacturing process of GOA
Jo
ur
na l
Scheme 2 Physical adsorption mechanisms between PAHs and GOA
31
oo f
ur
na l
Pr
e-
pr
Scheme 1.
Jo
Scheme 2.
32
na l
ur
Jo
oo f
pr
e-
Pr
Fig. 1.
33
na l
ur
Jo Fig. 2.
34
oo f
pr
e-
Pr
(a) D
G'
GOA G
IG / ID = 3.379
G'
D
pr
Graphite Powder
oo f
IG / ID = 0.881
XAD16
1000
1500
2000
2500
3000
Pr
500
e-
Relative Intensity (a.u.)
G
Jo
ur
na l
Raman Shift (cm-1)
35
oo f pr ePr
Fig. 3.
(a)
na l ur
Jo
Relative Intensity (a.u.)
Graphite (002) 2 theta = 26.5o d = 0.340 nm
Graphite (004) 2 theta = 54.6o
Graphite Powder
10
2 theta = 9.8o, d = 0.903 nm 20
30
GOA 40
50
60
Diffraction Angel (2 theta) 36
2 theta = 9.8o, d = 0.903 nm
1 hour
2 theta = 10.2o, d = 0.867 nm
2 hours
oo f
Relative Intensity (a.u.)
(b)
2 theta = 10.3o, d = 0.860 nm
10
20
4 hours
5 hours
e-
2 theta = 10.7o, d = 0.827 nm
pr
2 theta = 10.5o, d = 0.843 nm
3 hours
30
40
Pr
Diffraction Angel (2 theta)
Jo
ur
na l
Fig. 4.
37
(c) 12 Diffraction Angel d spacing 11
10
10
oo f
d spacing (10
-10
m)
11
9
9
8
pr
8
7
0
1
2
3
e-
Diffraction Angel (2 theta/deg.)
12
4
5
7 6
Jo
ur
na l
Fig. 4. (continue)
Pr
Oxidation Time (hour)
38
(a) 700
NAP
600
AcP BaP
ppm
500 400
oo f
300 200
0 0
20
40
pr
100
60
80
60
80
(b) NAP
600
AcP
ppm
500 400
BaP
DBA
ur
300
na l
700
Pr
e-
Time (min)
Jo
200 100 0
0
20
40
Time (min) Fig. 5.
39
(a) total PAHs ( μg / g )
15
60 km / h 30 km / h
12
0 km / h
oo f
9 6
0 0
10
pr
3
20
30
Pr
e-
Time (min)
(b)
na l
60 km / h 30 km / h
12
0 km / h
9
Jo
ur
total PAHs ( μg / g )
15
6 3 0
0
10
20
30
Time (min) Fig. 6.
40
(c) 70
GOA
oo f
50 40 30 20
pr
total PAHs ( μg )
60
XAD16
e-
10 0 5
15
25
Jo
ur
na l
Pr
Samplng time (min)
41
(d) 12
GOA XAD16
10 8 6 4
oo f
total PAHs ( μg / g )
14
2 0 15
25
pr
5
Samplng time (min)
Jo
ur
na l
Pr
e-
Fig. 6. (continue)
42
(e) 15
XAD16
12 9 6
oo f
total PAHs (μg / g)
GOA
3
1
2
3
pr
0
Reused number
Jo
ur
na l
Pr
e-
Fig. 6. (continue)
43