Subscriber access provided by University of Massachusetts Amherst Libraries
Letter
Few-layered Graphene-like Boron Nitride: A Highly Efficient Adsorbent for Indoor Formaldehyde Removal Jiawei Ye, Xiaofeng Zhu, Bei Cheng, Jiaguo Yu, and Chuanjia Jiang Environ. Sci. Technol. Lett., Just Accepted Manuscript • DOI: 10.1021/acs.estlett.6b00426 • Publication Date (Web): 07 Dec 2016 Downloaded from http://pubs.acs.org on December 7, 2016
Just Accepted “Just Accepted” manuscripts have been peer-reviewed and accepted for publication. They are posted online prior to technical editing, formatting for publication and author proofing. The American Chemical Society provides “Just Accepted” as a free service to the research community to expedite the dissemination of scientific material as soon as possible after acceptance. “Just Accepted” manuscripts appear in full in PDF format accompanied by an HTML abstract. “Just Accepted” manuscripts have been fully peer reviewed, but should not be considered the official version of record. They are accessible to all readers and citable by the Digital Object Identifier (DOI®). “Just Accepted” is an optional service offered to authors. Therefore, the “Just Accepted” Web site may not include all articles that will be published in the journal. After a manuscript is technically edited and formatted, it will be removed from the “Just Accepted” Web site and published as an ASAP article. Note that technical editing may introduce minor changes to the manuscript text and/or graphics which could affect content, and all legal disclaimers and ethical guidelines that apply to the journal pertain. ACS cannot be held responsible for errors or consequences arising from the use of information contained in these “Just Accepted” manuscripts.
Environmental Science & Technology Letters is published by the American Chemical Society. 1155 Sixteenth Street N.W., Washington, DC 20036 Published by American Chemical Society. Copyright © American Chemical Society. However, no copyright claim is made to original U.S. Government works, or works produced by employees of any Commonwealth realm Crown government in the course of their duties.
Page 1 of 20
Environmental Science & Technology Letters
Few-layered Graphene-like Boron Nitride: A Highly Efficient Adsorbent for Indoor Formaldehyde Removal §
§
Jiawei Ye , Xiaofeng Zhu , Bei Cheng, Jiaguo Yu* and Chuanjia Jiang*
State Key Laboratory of Advanced Technology for Materials Synthesis and Processing, Wuhan University of Technology, Luoshi Road 122, Wuhan 430070, P. R. China §
These authors contributed equally to this work.
*Corresponding authors. Tel.: 0086-27-87871029, Fax: 0086-27-87879468, E-mail:
[email protected];
[email protected] 1 ACS Paragon Plus Environment
Environmental Science & Technology Letters
1
ABSTRACT:
2
Highly porous boron nitride (BN) composed of flexible network of hexagonal BN
3
nanosheets was synthesized via thermal treatment of a boric acid and urea mixture.
4
The as-prepared sponge-like BN displayed fast adsorption rates and ultra-high
5
adsorption capacities for gaseous formaldehyde (HCHO), e.g. 19 mg/g in equilibrium
6
with approximately 20 ppm HCHO in air, which is an order of magnitude higher than
7
other tested materials, including commercial hexagonal BN and various metal oxides.
8
The superb HCHO adsorption performance of the porous BN is mainly due to its high
9
specific surface area (627 m2/g), as well as the abundant surface hydroxyl and amine
10
groups. Moreover, chemisorption can occur on the BN layers and contribute to the
11
high HCHO uptake via Cannizzaro-type disproportionation reactions, during which
12
HCHO is transformed into less toxic formic acid and methanol. This porous BN is a
13
promising adsorbent for indoor HCHO removal, and may serve as the support for
14
highly efficient HCHO decomposition catalysts.
2 ACS Paragon Plus Environment
Page 2 of 20
Page 3 of 20
Environmental Science & Technology Letters
15
INTRODUCTION
16
Formaldehyde (HCHO) is a major indoor air pollutant, which is mainly emitted
17
from building and furnishing materials.1,2 Long-term exposure to HCHO may cause
18
serious health problems, including respiratory disease, skin irritation and cancer.1 To
19
reduce indoor HCHO concentration, various techniques have been developed for
20
HCHO removal, such as adsorption (physical adsorption,3-7 chemisorption8,9), plasma
21
oxidation,10-12 photocatalytic degradation13-15 and thermal catalytic oxidation
22
decomposition.16-27 Catalytic oxidation is potentially capable of continuous and
23
complete removal of gaseous HCHO, but the catalysts with high room-temperature
24
HCHO decomposition activity typically contain noble metals28 and are prone to
25
deactivation.29 On the other hand, adsorption offers a feasible strategy for indoor
26
HCHO removal, due to its low cost and easy operation. Various adsorbents such as
27
activated carbon,3,30,31 AlOOH,6 and CeO232 have been studied for removing gaseous
28
HCHO, but their performances are still unsatisfactory even after surface modification
29
or combination as composite materials. Considering the polarity of HCHO molecules,
30
it is hypothesized that materials with hydrophilic surface and a high specific surface
31
area may serve as an effective adsorbent for HCHO.
32
As an analogue of graphene, hexagonal boron nitride (BN) has recently attracted
33
wide research interests, due to its unique two-dimensional layered structure and
34
physicochemical properties, such as ultra-high specific surface area, outstanding
35
electrical-insulating properties, high thermal conductivity and chemical stability.33
36
These characteristics make BN a promising material in broad applications, especially 3 ACS Paragon Plus Environment
Environmental Science & Technology Letters
37
in hydrogen storage,34,35 electronics,36 and adsorptive removal of organic water
38
pollutants.37 In addition to its large specific surface area, BN has high hydrophilicity,
39
thus porous BN may exhibit good adsorption performance toward gaseous HCHO.
40
Although the adsorption of HCHO molecules on BN has been theoretically studied,38
41
porous BN has rarely been evaluated for the adsorptive removal of indoor HCHO
42
under ambient condition.
43
Herein, highly porous sponge-like BN (p-BN) composed of interconnected
44
network of curled nanosheets was prepared by thermal treatment of a boric acid and
45
urea mixture. The as-prepared material exhibited outstanding performance for the
46
adsorption of gaseous HCHO, as compared with commercial BN (c-BN), activated
47
carbon (AC) and various metal oxides. Furthermore, we reported for the first time that
48
this few-layered porous BN can trigger the Cannizzaro-type reaction, and thus HCHO
49
can be transformed into less toxic species (i.e., formic acid and methanol). This work
50
may shed light on the design of environmentally benign adsorbent for efficient indoor
51
HCHO removal.
52 53
MATERIALS AND METHODS
54
Preparation of p-BN. All chemicals used were reagent-grade without further
55
treatment. Typically, 1.24 g of boric acid (Sinopharm Chemical Reagent Co., Ltd) and
56
14.5 g of urea (Sinopharm) were dissolved in 40 mL of distilled water to form a clear,
57
colorless solution, which was heated at 65 °C under magnetic stirring until water
58
evaporated completely. The dried mixtures were collected into a quartz boat and 4 ACS Paragon Plus Environment
Page 4 of 20
Page 5 of 20
Environmental Science & Technology Letters
59
heated to 900 °C at a rate of 10 °C/min for 5 h under nitrogen (N2) atmosphere,
60
yielding white and fluffy products. Sources of commercial materials for comparison
61
are provided in Table S1 in Supporting Information (SI).
62
Characterization. The phase structures of p-BN and c-BN were analysed by
63
X-ray diffraction (XRD) (Rigaku D/Max-RB, Japan), while the morphology of p-BN
64
was observed by field-emission scanning electron microscopy (FESEM) (JEOL 7500F,
65
Japan), transmission electron microscopy (TEM) and high-resolution TEM (HRTEM)
66
(JEM-2100F). X-ray photoelectron spectra (XPS) measurements were performed on
67
VG ESCALAB210, and Fourier transform infrared (FTIR) spectra were collected
68
using a Shimadzu IRAffinity-1 FTIR spectrometer. The Brunauer-Emmett-Teller
69
(BET) specific surface area (SBET), pore size distribution, pore volume and average
70
pore size of the samples were determined by N2 adsorption measurement
71
(Micromeritics ASAP 2020). In situ diffuse reflectance infrared Fourier transform
72
spectroscopy (DRIFTS) was performed for p-BN exposed to a gas mixture of HCHO
73
and O2 at room temperature (Thermo Fisher Nicolet iS50). More details of the
74
characterization methods are provided in the SI.
75
HCHO adsorption test. HCHO adsorption experiments of the tested materials
76
were performed in the dark and at 25 °C in an organic glass box reactor, with the
77
real-time concentrations of HCHO, carbon dioxide (CO2), carbon monoxide (CO) and
78
water vapor online detected by a Photoacoustic Field Gas Monitor (INNOVA AirTech
79
Instruments, Model 1412).9 For measuring the adsorption isotherms of p-BN and
80
c-BN, initial HCHO concentrations ranged from 20 to 646 ppm. The adsorption 5 ACS Paragon Plus Environment
Environmental Science & Technology Letters
81
kinetics and isotherms were modeled according to Xu et al.39 Detailed procedures are
82
provided in the SI.
83 84
RESULTS AND DISCUSSION
85
Phase Structure and Morphology. The XRD pattern of c-BN (Figure 1a) can be
86
assigned to hexagonal BN (JCPDS 45-0893), while that of p-BN exhibits two
87
broadened peaks corresponding to the (002) and (100) planes of hexagonal BN, which
88
is characteristic of partially disordered BN phases with low crystallinity.37 The shifted
89
(002) peak corresponds to an interplanar spacing of 0.37 nm, which is larger than the
90
standard (002) distance of 0.33 nm in c-BN.35
91
In the FTIR spectra of both p-BN and c-BN (Figure 1b), two intense absorption
92
peaks were observed at 1388 and 800 cm–1, which are attributed to in-plane B-N
93
transverse optical mode of the sp2-bonded BN and the out-of-plane B-N-B bending
94
mode, respectively.40 The FTIR spectrum of p-BN exhibits two additional weak
95
absorption bands at 3410 and 3200 cm–1, which are attributed to the O-H stretching
96
bands from hydroxyl groups and N-H stretching bands from amine groups,
97
respectively.41
98
The FESEM image (Figure 1c) shows that p-BN has a porous sponge-like
99
morphology, which is constructed by interconnected network of twisted nanosheets,
100
while TEM characterization (Figure 1d) also confirmed the porous structure of p-BN.
101
The HRTEM image (Figure 1d, inset) shows parallel fringes at the edge of the BN
102
nanosheets, suggesting that these nanosheets are composed of a few (e.g. six) stacked 6 ACS Paragon Plus Environment
Page 6 of 20
Page 7 of 20
Environmental Science & Technology Letters
103
BN layers. The average spacing between adjacent fringes was 0.37 nm, consistent
104
with that calculated from the (002) peak in the XRD spectrum.
105
106 107 108 109
Figure 1. XRD patterns (a) and FTIR spectra (b) of the as-synthesized porous BN (p-BN) and the commercial BN (c-BN). FESEM (c), TEM (d) and HRTEM (inset of part d) images of p-BN.
110 111
XPS Surface Chemistry Analysis. The XPS survey spectra (Figure S1a) of
112
p-BN and c-BN indicate the presence of B, N, O and C on both samples, with
113
corresponding binding energies of approximately 191 (B 1s), 398 (N 1s), 532 (O 1s),
114
and 285 eV (C 1s).42 The C 1s peak is due to the adventitious hydrocarbon.
115
High-resolution B 1s spectra of c-BN and p-BN (Figure S1b) show main peaks at
116
190.3–190.9 eV and shoulder peaks at 191.9–192.3 eV. The former peaks correspond
117
to BN3 trigonal units in layered hexagonal BN, while the latter correspond to B-O 7 ACS Paragon Plus Environment
Environmental Science & Technology Letters
118
bonds due to surface hydroxyl or the exposure to air. Notably, the B-O bond peak
119
intensity of p-BN is higher than that of the c-BN due to extra hydroxyl groups
120
originating from the boric acid precursor.37 As compared to c-BN, the positive shift of
121
the B 1s binding energy in p-BN is caused by surface hydroxyl or amine groups
122
bonded to B. The binding energy of N 1s (Figure S1c) from NB3 trigonal units in
123
c-BN and p-BN are located at 397.9 and 398.2 eV, respectively, consistent with
124
reported values.43 A shoulder peak at 399.0 eV in the N 1s spectrum of p-BN can be
125
assigned to amine groups.42 These results, in combination with the FTIR analysis,
126
further indicate the presence of hydroxyl and amine groups in p-BN.
127
Textural Properties. Nitrogen adsorption-desorption isotherms of p-BN and
128
c-BN (Figure S2) are both type IV isotherms with type H3 hysteresis loops,
129
suggesting the presence of slit-shaped mesopores formed between hexagonal BN
130
nanosheets.44 The drastic increases of N2 adsorption at the low relative pressure (P/P0)
131
range for p-BN confirms the presence of micropores,35 as compared to c-BN with
132
minimal N2 adsorption. On the other hand, the hysteresis loops at a P/P0 range
133
between 0.4–1.0 indicate the presence of large mesopores and macropores in c-BN
134
and p-BN.
135
The textural properties of p-BN and the commercial samples are summarized in
136
Table 1. The p-BN sample exhibits significantly larger SBET (627 m2/g) than the other
137
materials. Based on the above results, p-BN is supposed to have high adsorption
138
performance for removal of HCHO from air.
139
8 ACS Paragon Plus Environment
Page 8 of 20
Page 9 of 20
Environmental Science & Technology Letters
140
Table 1. Textural properties and HCHO adsorption capacity of the samples. Sample p-BN c-BN AC f MS g SiO2 γ-Al2O3 α-Fe2O3 Co2O3 TiO2 (P25) CeO2
141 142 143 144
SBET a (m2/g) 627 25 106 389 229 124 109 61 47 14
dp b (nm) 2.7 10.6 5.1 2.5 7.7 6.9 14.6 9.9 9.2 11.0
Vp c (cm3/g) 0.42 0.07 0.14 0.25 0.44 0.21 0.40 0.15 0.11 0.04
qd (mg/g) 19.0 1.93 0.90 1.68 1.61 1.75 1.51 h 1.65 1.08 2.19
q’ e (mg/m2) 0.030 0.077 0.008 0.004 0.007 0.014 0.014 0.027 0.023 0.156
Notes: a BET specific surface area; b average pore diameter; c total pore volume; d HCHO adsorption capacity, measured after 60 min. e HCHO adsorption capacity normalized to SBET; f activated carbon, g molecular sieve (13X). h Estimated from HCHO uptake minus CO2 generation.
145 146
HCHO Adsorption Activity. After the adsorption started, HCHO concentration
147
quickly decreased in the presence of p-BN (Figure S3a), while CO2 concentration did
148
not change significantly (Figure S3b), indicating that HCHO was removed by
149
adsorption rather than catalytic decomposition. The HCHO adsorption kinetics of
150
p-BN
151
pseudo-first-order model (Figure S4), with a calculated pseudo-second-order rate
152
constant of 0.023 g/mg/min (Table S2). In contrast, HCHO concentration only slightly
153
decreased in the presence of c-BN and other commercial materials (Figure S3a).
154
Correspondingly, the amount of HCHO adsorption on p-BN rapidly increased within
155
10 min and reached 19.0 mg/g after 1 h, which was much higher than the other
156
materials (< 2.3 mg/g) (Figure 2 and Table 1). Moreover, after 60 min of adsorption,
157
p-BN was in equilibrium with a much lower HCHO concentration (~20 ppm) than the
were
better
fitted
with
the
pseudo-second-order
9 ACS Paragon Plus Environment
model
than
the
Environmental Science & Technology Letters
158
other materials (≥120 ppm). Given the same equilibrium HCHO concentration,
159
HCHO adsorption by p-BN is expected to be even higher than by the other materials.
160
For example, with an equilibrium HCHO concentration of 133 ppm (i.e., 0.169 mg/L),
161
the adsorption capacity of p-BN was 26.8 mg/g (Figure S5). The adsorption isotherm
162
of c-BN (Figure S6) can be described by the Freundlich model (R2 = 0.91) but not the
163
Langmuir model (R2 < 0.01), while that of p-BN cannot be well described by either of
164
these models (Figure S7). These results were due to the fact that partial oxidation of
165
adsorbed HCHO occurred (shown in later sections), which were not considered in the
166
classical adsorption models. The HCHO adsorption of the commercial materials were
167
also fast (Figure 2), despite the low adsorption capacities; due to the low time
168
resolution of the measured data compared to the adsorption rates, the adsorption
169
kinetics could not be accurately modeled.
170
It should be noted that α-Fe2O3 was able to decompose HCHO at room
171
temperature,45 with HCHO concentration decreased from 149 ppm to 119 ppm and
172
CO2 concentration increased by approximately 20 ppm within 60 min (Figure S3).
173
This suggests that approximately two thirds of the HCHO removed by α-Fe2O3 was
174
decomposed into CO2 and H2O, and approximately one third remained adsorbed on
175
α-Fe2O3, either as HCHO or as transformed species. Thus, while HCHO removal by
176
α-Fe2O3 was 4.5 mg/g after 60 min of reaction, the HCHO adsorption capacity of
177
α-Fe2O3 was estimated to be approximately 1.5 mg/g.
10 ACS Paragon Plus Environment
Page 10 of 20
Page 11 of 20
Environmental Science & Technology Letters
178 179
Figure 2. HCHO uptake over time on p-BN and commercial materials.
180 181
The as-prepared p-BN had much higher HCHO adsorption capacity than c-BN,
182
mainly due to its larger SBET, while both the BN samples were more effective in
183
adsorbing HCHO than most of the other tested materials (except CeO2) when SBET is
184
taken into account (Table 1). Therefore, in additional to the large SBET, surface
185
properties of boron nitride also have great contributions to the high HCHO adsorption.
186
Hydrogen bonding between HCHO and hydroxyl or amine groups plays an important
187
role in the adsorption of HCHO,6,30 and this can explain why boron nitride has higher
188
HCHO adsorption capacity than activated carbon, which is less hydrophilic than BN.
189
However, boron nitride is also more effective in adsorbing HCHO than materials with
190
high surface hydroxyl content, e.g. γ-Al2O3, SiO2 and molecular sieve (13X). Hence, 11 ACS Paragon Plus Environment
Environmental Science & Technology Letters
191
another reason for the high adsorption capacity of boron nitride is that HCHO
192
molecules and BN layers are both planar configuration, resulting in lower adsorption
193
resistance. Furthermore, HCHO molecules have π-conjugation between C and O
194
atoms, while BN also exhibits a large 2D delocalized π-conjugated structure. Thus,
195
π−π conjugation interaction can occur between BN and HCHO, and this strong
196
interaction can significantly enhance the adsorption of HCHO. As a result of the
197
above-mentioned advantages, p-BN exhibited outstanding performance for HCHO
198
adsorption.
199
The HCHO adsorption performance stability of p-BN was measured by testing
200
used p-BN after heating under an infrared lamp (Figure S8). The adsorption capacity
201
decreased with recycling times, probably due to partial blocking of micropores.
202
However, the performance became stable after the fourth run, and HCHO uptake
203
remained at 8.5 mg/g, which is still high compared to other materials and previously
204
reported value.4
205
Adsorption Mechanisms Study by in situ DRIFTS. When p-BN was exposed
206
to the HCHO/O2 mixture at ambient temperature, the DRIFTS spectra exhibited
207
multiple bands (Figure S9), which could be assigned to formic acid (HCOOH),
208
methanol (CH3OH) and HCHO (Table S3). Specifically, the bands at 2986, 2863,
209
2750, 1610, 1566 and 1371 cm–1 are attributed to adsorbed formate,17,22,25,27,46-50 those
210
at 2912, 2804 and 1467 cm–1 to methoxy group,48 and those at 1771, 1700 and 1413
211
cm–1 to molecularly adsorbed HCHO.47,51 Moreover, the broad bands at 3200–3600
212
cm–1 are attributed to the stretching vibration of hydroxyl groups.27 These results 12 ACS Paragon Plus Environment
Page 12 of 20
Page 13 of 20
Environmental Science & Technology Letters
213
indicate that HCOOH and CH3OH are the products of HCHO adsorption on p-BN,
214
likely via a Cannizzaro-type disproportionation reaction pathway. Notably, an
215
intensive negative peak was observed at 1640 cm–1, corresponding to adsorbed
216
water,17,21,23
217
disproportionation reaction of HCHO.
which
suggests
that adsorbed
water
was
consumed
in
the
218
Thus, a possible mechanism for the Cannizzaro-type disproportionation reaction
219
of HCHO on p-BN surface is proposed (Figure S10). Briefly, HCHO molecules are
220
adsorbed on the surface of p-BN. Then the N atoms of BN layer, which act as Lewis
221
base, trigger the nucleophilic addition reaction, and a H atom of HCHO transfers to
222
another HCHO molecule (step I). As a result, some adsorbed HCHO molecules
223
transform into formamide while others form methoxy salts (step II). Finally, the
224
formamide and methoxy salts react with surface adsorbed water molecules and
225
transform into less toxic HCOOH and CH3OH (step III). Thus, while water vapor can
226
compete with HCHO for adsorption,31 water molecules are necessary in the
227
chemisorption of HCHO onto p-BN surface. The complex role of air moisture in the
228
overall HCHO uptake performance needs further investigation.
229
Outlook. The porous BN exhibited superb HCHO adsorption performance at
230
room temperature, which was mainly due to its high specific surface area, as well as
231
the abundant surface hydroxyl and amine groups. This material can be used as a
232
support for synthesizing highly efficient HCHO decomposition catalysts, e.g.
233
supported Pt catalysts. Moreover, chemisorption occurred on the BN layers and
234
contributed to the high HCHO uptake via Cannizzaro-type disproportionation 13 ACS Paragon Plus Environment
Environmental Science & Technology Letters
Page 14 of 20
235
reactions. Thus, the adsorption isotherms could not be well described by the classical
236
adsorption models; alternatively, models are needed for describing such reaction
237
systems, which should consider both partitioning between phases and chemical
238
reactions occurring at the heterogeneous surfaces.
239
This study highlighted the complex role of water vapor in affecting the HCHO
240
uptake performance by the porous BN, which needs to be more systematically
241
investigated. In addition, another important influencing factor is temperature, since
242
exothermic and endothermic adsorptions are affected by temperature in different
243
ways.39
244
temperature-dependent adsorption isotherms,39,52 but a prerequisite for such
245
approaches is the definition of standard reference state for the adsorbed species in
246
order to calculated the chemical activity of these species at different interfaces.
247
Alternatively, the adsorption energy of the materials can be calculated by density
248
functional theory (DFT) computation,38 but it is necessary to quantitatively
249
characterize the atomic structure of the materials, including the presence and quantity
250
of vacancies and other types of defects, as well as the precise contents of hydroxyl,
251
amino and other functional groups involved in the adsorption of HCHO.
The
adsorption
thermodynamics
can
be
investigated
from
252 253
Acknowledgments
254
This work was supported by the NSFC (51320105001, 51372190, 21573170,
255
51272199 and 21433007), 973 program (2013CB632402), the Natural Science
256
Foundation of Hubei Province (2015CFA001), the Fundamental Research Funds for 14 ACS Paragon Plus Environment
Page 15 of 20
Environmental Science & Technology Letters
257
the Central Universities (WUT: 2015-III-034) and Innovative Research Funds of
258
SKLWUT (2015-ZD-1).
259 260
Supporting
Information
Available:
Additional
information
related
to
the
261
characterization and HCHO adsorption test procedures, sources of commercial
262
materials (Table S1), kinetics parameters (Table S2), In situ DRIFTS band assignment
263
(Table S3), XPS (Figure S1), N2 adsorption-desorption (Figure S2), concentration
264
change of HCHO and CO2 over time (Figure S3), HCHO adsorption kinetics
265
modeling (Figure S4), HCHO adsorption isotherms (Figure S5), data fitting of HCHO
266
adsorption isotherms (Figure S6 and S7), HCHO uptake in recycle tests (Figure S8),
267
in situ DRIFTS (Figure S9) and proposed disproportionation reaction mechanism
268
(Figure S10). This material is available free of charge via the Internet at
269
http://pubs.acs.org.
270 271
References
272 273 274 275 276 277 278 279 280 281 282 283 284 285
1. Salthammer, T.; Mentese, S.; Marutzky, R., Formaldehyde in the indoor environment. Chem. Rev. 2010, 110, 2536-2572. 2. Liang, W. H.; Yang, S.; Yang, X. D., Long-term formaldehyde emissions from medium-density fiberboard in a full-scale experimental room: Emission characteristics and the effects of temperature and humidity. Environ. Sci. Technol. 2015, 49, 10349-10356. 3. Wen, Q. B.; Li, C. T.; Cai, Z. H.; Zhang, W.; Gao, H. L.; Chen, L. J.; Zeng, G. M.; Shu, X.; Zhao, Y. P., Study on activated carbon derived from sewage sludge for adsorption of gaseous formaldehyde. Bioresour. Technol. 2011, 102, 942-947. 4. Xu, Z. H.; Yu, J. G.; Xiao, W., Microemulsion-assisted preparation of a mesoporous ferrihydrite/SiO2 composite for the efficient removal of formaldehyde from air. Chem. Eur. J. 2013, 19, 9592-9598. 5. Lin, F.; Zhu, G. Q.; Shen, Y. N.; Zhang, Z. Y.; Dong, B., Study on the modified montmorillonite for adsorbing formaldehyde. Appl. Surf. Sci. 2015, 356, 150-156. 15 ACS Paragon Plus Environment
Environmental Science & Technology Letters
286 287 288 289 290 291 292 293 294 295 296 297 298 299 300 301 302 303 304 305 306 307 308 309 310 311 312 313 314 315 316 317 318 319 320 321 322 323 324 325 326 327 328 329
6. Xu, Z. H.; Yu, J. G.; Low, J. X.; Jaroniec, M., Microemulsion-assisted synthesis of mesoporous aluminum oxyhydroxide nanoflakes for efficient removal of gaseous formaldehyde. ACS Appl. Mater. Interfaces 2014, 6, 2111-2117. 7. Chen, F.; Liu, S. W.; Yu, J. G., Efficient removal of gaseous formaldehyde in air using hierarchical titanate nanospheres with in situ amine functionalization. Phys. Chem. Chem. Phys. 2016, 18, 18161-18168. 8. Pei, J. J.; Zhang, J. S. S., On the performance and mechanisms of formaldehyde removal by chemi-sorbents. Chem. Eng. J. 2011, 167, 59-66. 9. Yu, J. G.; Li, X. Y.; Xu, Z. H.; Xiao, W., NaOH-modified ceramic honeycomb with enhanced formaldehyde adsorption and removal performance. Environ. Sci. Technol. 2013, 47, 9928-9933. 10. Chang, M. B.; Lee, C. C., Destruction of formaldehyde with dielectric barrier discharge plasmas. Environ. Sci. Technol. 1995, 29, 181–186. 11. Fan, X.; Zhu, T. L.; Sun, Y. F.; Yan, X., The roles of various plasma species in the plasma and plasma-catalytic removal of low-concentration formaldehyde in air. J. Hazard. Mater. 2011, 196, 380-385. 12. Zhu, X. B.; Gao, X.; Qin, R.; Zeng, Y. X.; Qu, R. Y.; Zheng, C. H.; Tu, X., Plasma-catalytic removal of formaldehyde over Cu-Ce catalysts in a dielectric barrier discharge reactor. Appl. Catal. B 2015, 170, 293-300. 13. Han, Z. N.; Chang, V. W.; Wang, X. P.; Lim, T. T.; Hildemann, L., Experimental study on visible-light induced photocatalytic oxidation of gaseous formaldehyde by polyester fiber supported photocatalysts. Chem. Eng. J. 2013, 218, 9-18. 14. Wu, C. L., Facile one-step synthesis of N-doped ZnO micropolyhedrons for efficient photocatalytic degradation of formaldehyde under visible-light irradiation. Appl. Surf. Sci. 2014, 319, 237-243. 15. Zhu, X. B.; Chang, D. L.; Li, X. S.; Sun, Z. G.; Deng, X. Q.; Zhu, A. M., Inherent rate constants and humidity impact factors of anatase TiO2 film in photocatalytic removal of formaldehyde from air. Chem. Eng. J. 2015, 279, 897-903. 16. Zhang, C. B.; He, H.; Tanaka, K., Perfect catalytic oxidation of formaldehyde over a Pt/TiO2 catalyst at room temperature. Catal. Commun. 2005, 6, 211-214. 17. Zhang, C. B.; He, H.; Tanaka, K., Catalytic performance and mechanism of a Pt/TiO2 catalyst for the oxidation of formaldehyde at room temperature. Appl. Catal. B 2006, 65, 37-43. 18. Huang, H. B.; Leung, D. Y. C., Complete oxidation of formaldehyde at room temperature using TiO2 supported metallic Pd nanoparticles. ACS Catal. 2011, 1, 348-354. 19. Huang, H. B.; Leung, D. Y. C., Complete elimination of indoor formaldehyde over supported Pt catalysts with extremely low Pt content at ambient temperature. J. Catal. 2011, 280, 60-67. 20. Zhang, C. B.; Liu, F. D.; Zhai, Y. P.; Ariga, H.; Yi, N.; Liu, Y. C.; Asakura, K.; Flytzani-Stephanopoulos, M.; He, H., Alkali-metal-promoted Pt/TiO2 opens a more efficient pathway to formaldehyde oxidation at ambient temperatures. Angew. Chem. Int. Edit. 2012, 51, 9628-9632. 21. Xu, Q. L.; Lei, W. Y.; Li, X. Y.; Qi, X. Y.; Yu, J. G.; Liu, G.; Wang, J. L.; Zhang, P. 16 ACS Paragon Plus Environment
Page 16 of 20
Page 17 of 20
Environmental Science & Technology Letters
330 331 332 333 334 335 336 337 338 339 340 341 342 343 344 345 346 347 348 349 350 351 352 353 354 355 356 357 358 359 360 361 362 363 364 365 366 367 368 369 370 371 372 373
Y., Efficient removal of formaldehyde by nanosized gold on well-defined CeO2 nanorods at room temperature. Environ. Sci. Technol. 2014, 48, 9702-9708. 22. Wang, J. L.; Zhang, P. Y.; Li, J. G.; Jiang, C. J.; Yunus, R.; Kim, J., Room-temperature oxidation of formaldehyde by layered manganese oxide: Effect of water. Environ. Sci. Technol. 2015, 49, 12372-12379. 23. Qi, L. F.; Ho, W. K.; Wang, J. L.; Zhang, P. Y.; Yu, J. G., Enhanced catalytic activity of hierarchically macro-/mesoporous Pt/TiO2 toward room-temperature decomposition of formaldehyde. Catal. Sci. Technol. 2015, 5, 2366-2377. 24. Wang, J. L.; Yunus, R.; Li, J. G.; Li, P. L.; Zhang, P. Y.; Kim, J., In situ synthesis of manganese oxides on polyester fiber for formaldehyde decomposition at room temperature. Appl. Surf. Sci. 2015, 357, 787-794. 25. Yan, Z. X.; Xu, Z. H.; Yu, J. G.; Jaroniec, M., Highly active mesoporous ferrihydrite supported Pt catalyst for formaldehyde removal at room temperature. Environ. Sci. Technol. 2015, 49, 6637-6644. 26. Xu, Z. H.; Yu, J. G.; Jaroniec, M., Efficient catalytic removal of formaldehyde at room temperature using AlOOH nanoflakes with deposited Pt. Appl. Catal. B 2015, 163, 306-312. 27. Ma, Y.; Zhang, G. K., Sepiolite nanofiber-supported platinum nanoparticle catalysts toward the catalytic oxidation of formaldehyde at ambient temperature: Efficient and stable performance and mechanism. Chem. Eng. J. 2016, 288, 70-78. 28. Nie, L. H.; Yu, J. G.; Jaroniec, M.; Tao, F. F., Room-temperature catalytic oxidation of formaldehyde on catalysts. Catal. Sci. Technol. 2016, 6, 3649-3669. 29. Zhu, X. F.; Cheng, B.; Yu, J. G.; Ho, W. K., Halogen poisoning effect of Pt-TiO2 for formaldehyde catalytic oxidation performance at room temperature. Appl. Surf. Sci. 2016, 364, 808-814. 30. Ma, C. J.; Li, X. H.; Zhu, T. L., Removal of low-concentration formaldehyde in air by adsorption on activated carbon modified by hexamethylene diamine. Carbon 2011, 49, 2873-2875. 31. Lee, K. J.; Miyawaki, J.; Shiratori, N.; Yoon, S. H.; Jang, J., Toward an effective adsorbent for polar pollutants: Formaldehyde adsorption by activated carbon. J. Hazard. Mater. 2013, 260, 82-88. 32. Zhou, J.; Mullins, D. R., Adsorption and reaction of formaldehyde on thin-film cerium oxide. Surf. Sci. 2006, 600, 1540-1546. 33. Golberg, D.; Bando, Y.; Huang, Y.; Terao, T.; Mitome, M.; Tang, C. C.; Zhi, C. Y., Boron nitride nanotubes and nanosheets. ACS Nano 2010, 4, 2979-2993. 34. Weng, Q. H.; Wang, X. B.; Zhi, C. Y.; Bando, Y.; Golberg, D., Boron nitride porous microbelts for hydrogen storage. ACS Nano 2013, 7, 1558-1565. 35. Weng, Q. H.; Wang, X. B.; Bando, Y.; Golberg, D., One-step template-free synthesis of highly porous boron nitride microsponges for hydrogen storage. Adv. Energy Mater. 2014, 4, 8. 36. Britnell, L.; Gorbachev, R. V.; Jalil, R.; Belle, B. D.; Schedin, F.; Katsnelson, M. I.; Eaves, L.; Morozov, S. V.; Mayorov, A. S.; Peres, N. M. R.; Neto, A. H. C.; Leist, J.; Geim, A. K.; Ponomarenko, L. A.; Novoselov, K. S., Electron Tunneling through Ultrathin Boron Nitride Crystalline Barriers. Nano Lett. 2012, 12, 1707-1710. 17 ACS Paragon Plus Environment
Environmental Science & Technology Letters
374 375 376 377 378 379 380 381 382 383 384 385 386 387 388 389 390 391 392 393 394 395 396 397 398 399 400 401 402 403 404 405 406 407 408 409 410 411 412 413 414 415 416 417
37. Lei, W. W.; Portehault, D.; Liu, D.; Qin, S.; Chen, Y., Porous boron nitride nanosheets for effective water cleaning. Nat. Commun. 2013, 4, 1777. 38. Wang, R. X.; Zhu, R. X.; Zhang, D. J., Adsorption of formaldehyde molecule on the pristine and silicon-doped boron nitride nanotubes. Chem. Phys. Lett. 2008, 467, 131-135. 39. Xu, J.; Wang, L.; Zhu, Y. F., Decontamination of bisphenol A from aqueous solution by graphene adsorption. Langmuir 2012, 28, 8418-8425. 40. Nag, A.; Raidongia, K.; Hembram, K.; Datta, R.; Waghmare, U. V.; Rao, C. N. R., Graphene analogues of BN: Novel synthesis and properties. ACS Nano 2010, 4, 1539-1544. 41. Gu, Y. L.; Zheng, M. T.; Liu, Y. L.; Xu, Z. L., Low-temperature synthesis and growth of hexagonal boron-nitride in a lithium bromide melt. J. Am. Ceram. Soc. 2007, 90, 1589-1591. 42. Moulder, J. F.; Stickle, W. F.; Sobol, P. E.; Bomben, K. D., Handbook of X-ray Photoelectron Spectroscopy. Perkin-Elmer Corporation: Eden Prairie, MN, 1992. 43. Song, L.; Ci, L. J.; Lu, H.; Sorokin, P. B.; Jin, C. H.; Ni, J.; Kvashnin, A. G.; Kvashnin, D. G.; Lou, J.; Yakobson, B. I.; Ajayan, P. M., Large scale growth and characterization of atomic hexagonal boron nitride layers. Nano Lett. 2010, 10, 3209-3215. 44. Sing, K. S. W.; Everett, D. H.; Haul, R. A. W.; Moscou, L.; Pierotti, R. A.; Rouquerol, J.; Siemieniewska, T., Reporting physisorption data for gas/solid systems with special reference to the determination of surface area and porosity. Pure Appl. Chem. 1985, 57, 603-619. 45. Sekine, Y., Oxidative decomposition of formaldehyde by metal oxides at room temperature. Atmos. Environ. 2002, 36, 5543-5547. 46. Collins, S. E.; Baltanas, M. A.; Bonivardi, A. L., An infrared study of the intermediates of methanol synthesis from carbon dioxide over Pd/beta-Ga2O3. J. Catal. 2004, 226, 410-421. 47. Chen, D.; Qu, Z. P.; Sun, Y. H.; Gao, K.; Wang, Y., Identification of reaction intermediates and mechanism responsible for highly active HCHO oxidation on Ag/MCM-41 catalysts. Appl. Catal. B 2013, 142, 838-848. 48. Kattel, S.; Yan, B. H.; Yang, Y. X.; Chen, J. G. G.; Liu, P., Optimizing binding energies of key intermediates for CO2 hydrogenation to methanol over oxide-supported copper. J. Am. Chem. Soc. 2016, 138, 12440-12450. 49. Qi, L. F.; Cheng, B.; Yu, J. G.; Ho, W. K., High-surface area mesoporous Pt/TiO2 hollow chains for efficient formaldehyde decomposition at ambient temperature. J. Hazard. Mater. 2016, 301, 522-530. 50. Quiroz, J.; Giraudon, J. M.; Gervasini, A.; Dujardin, C.; Lancelot, C.; Trentesaux, M.; Lamonier, J. F., Total oxidation of formaldehyde over MnOx-CeO2 catalysts: The effect of acid treatment. ACS Catal. 2015, 5, 2260-2269. 51. Sun, S.; Ding, J. J.; Bao, J.; Gao, C.; Qi, Z. M.; Li, C. X., Photocatalytic oxidation of gaseous formaldehyde on TiO2: An in situ DRIFTS study. Catal. Lett. 2010, 137, 239-246. 52. Khan, A. A.; Singh, R. P., Adsorption thermodynamics of carbofuran on Sn(IV) 18 ACS Paragon Plus Environment
Page 18 of 20
Page 19 of 20
Environmental Science & Technology Letters
418 419
arsenosilicate in H+, Na+ and Ca2+ forms. Colloids Surf. 1987, 24, 33-42.
19 ACS Paragon Plus Environment
Environmental Science & Technology Letters
420 421
For Table of Contents Use Only
422
20 ACS Paragon Plus Environment
Page 20 of 20