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In Situ Photo-Fenton-Like Tandem Reaction for Selective Gluconic
Acid Production from Glucose Photo-Oxidation
Jiu Wang,∥
Lin Chen,∥
Heng Zhao,* Pawan Kumar, Stephen R. Larter, Md Golam Kibria,*
and Jinguang Hu*
Cite This: ACS Catal. 2023, 13, 2637−2646 Read Online
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sı Supporting Information
ABSTRACT: Biomass photorefining to selectively produce value-
added bioproducts is an emerging alternative biomass valorization
approach to alleviate energy crisis and achieve carbon neutrality.
Here, we demonstrate an efficient and selective glucose photo-
oxidation to gluconic acid via a rationally designed dual-functional
carbon nitride photocatalyst that not only allows H2O2 production
via 2e−
oxygen reduction reaction (2e-ORR) but also realizes in
situ photo-Fenton-like reaction. As a result, the essential oxidative
species (•
O2
−
and •
OH) for glucose oxidation into gluconic acid
are generated that achieves >60% glucose conversion and >60% of
gluconic acid selectivity within 4 h. Density functional theory
calculations demonstrate the superior performance of the photo-
catalyst for •
O2
−
and H2O2 generation. Further experimental
results reveal that the moderate concentration of H2O2 produced by 2e-ORR reaction plays a vital role in regulatinge gluconic acid
selectivity. This work demonstrates a good example to realize selective biomass photorefining through tandem reaction of ORR and
in situ photo-Fenton-like process, which could have profound impact on artificial photoenzyme systems involving moderate H2O2
modulation.
KEYWORDS: glucose photo-oxidation, gluconic acid, tandem reaction, 2e-ORR, in situ photo-Fenton-like reaction, photo-enzyme
Biomass valorization into fuels and chemicals provides an
effective approach to resolve energy shortage and
environmental issues.1,2
The abundant monosaccharide
glucose has already been converted into a diverse range of
chemicals with added value including arabinose, gluconic acid,
glucaric acid, fructose, lactic acid, and 5-hydroxymethylfurfu-
ral.3−7
Among these, gluconic acid together with its salts have
already been widely used in the food and pharmaceutical
industry and will reach a remarkable market value of US$ 1.9
billion by 2028.8−10
The current gluconic acid production
mainly rely on enzyme-catalyzed and chemo-catalyzed
processes, in which the first method involves expensive enzyme
and the second method gives rise to environmental
problems.11
Photocatalysis is an emerging green and
sustainable alternative technology platform for chemical
production,12−14
but simultaneously achieving good substrate
conversion and product selectivity over photocatalysis is still
challenging, especially using water as the solvent.15,16
Previous
studies have reported selective gluconic acid production from
glucose photo-oxidation, however, either on alkaline solution
or with the aid of a noble metal or an oxidant.17,18
Therefore,
rational design of the photocatalyst and the reaction pathway is
highly desired for selective biomass photorefining under mild
reaction conditions.
Fenton reaction has been demonstrated as one of the most
efficient methods for water purification in recent years.19,20
Typically, free hydroxyl radicals (•
OH) are generated during
the Fenton oxidation process as the active species to mineralize
the organic pollutants, while the reaction process and liquid
product selectivity are difficult to be controlled.21,22
Besides,
the addition of excessive H2O2, the Fe2+
ions in water, and the
limited pH range restrained the application of Fenton
process.23
It has been reported that high-value gluconic acid
can be obtained through selective glucose oxidation via
traditional Fenton process assisted by ultrasonication method,
during which •
OH plays an important role in the oxidation of
glucose.24
However, excessive •
OH might lead to over-
oxidation process due to the highly oxidative nature.25,26
Alternatively, in situ photo-induced Fenton-like process with
rational control of active species concentration is foreseen to
light up the selective conversion of glucose into gluconic acid.
Received: December 1, 2022
Revised: January 25, 2023
Research Article
pubs.acs.org/acscatalysis
© XXXX American Chemical Society
2637
https://doi.org/10.1021/acscatal.2c05931
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Thus, the key issue is how to design a dual functional
photocatalyst that can both generate H2O2 and decompose it
via in situ photo-Fenton process.
Polymeric carbon nitride (CN) has been considered to be an
ideal and eco-friendly photocatalyst along with surpassing
visible light response and promising band positions.27,28
More
importantly, CN has been demonstrated to have highly
selective H2O2 production via the 2e−
oxygen reduction
reaction (2e-ORR).29,30
However, the bulk CN derived from
ordinary thermal polymerization usually suffers from low
efficiency owing to severe recombination of electron−hole
pairs.31
Band gap engineering is a capable approach to improve
the 2e-ORR process of CN-based photocatalysts to form
H2O2.32−34
Additionally, alkalinization with cyano groups has
been proven to effectively decompose H2O2 into •
OH via
photo-Fenton process.35
Inspired by the aforementioned
literature, designing a dual functional CN photocatalyst that
can realize tandem reaction of ORR and in situ photo-Fenton-
like process would be a feasible strategy for selective glucose
photo-oxidation into gluconic acid. To the best of our
knowledge, such a conceptual design applied for selective
biomass valorization into value-added chemicals is yet to be
investigated.
Herein, for the first time, we demonstrate the feasibility of
selective glucose photo-oxidation into gluconic acid by a dual
functional CN photocatalyst. The procedure is achieved via the
fine construction of red CN photocatalyst with codoping of
potassium/oxygen, which can generate H2O2 by 2e-ORR and
in situ decompose into •
OH via photo-Fenton-like process.
Density functional theory (DFT) calculations demonstrate the
superior performance of the modified CN for the generation of
•
O2
−
and H2O2. Accordingly, the well-designed potassium/
oxygen codoped red CN exhibited >60% glucose conversion
and >60% gluconic acid selectivity after 4 h upon light
irradiation. The current study offers an alternative approach for
dual functional photocatalyst design to selectively produce
gluconic acid via tandem reaction of photocatalytic ORR and
in situ photo-Fenton-like process, which could also inspire
artificial photoenzyme systems involving moderate H2O2
modulation.
Figure 1. (a) Synthetic process for K, O codoped red CN through one-step thermal copolymerization. (b) FESEM image and (c) HAADF-STEM
image of RCN and relevant elemental mappings. The colors of red, green, yellow, and blue represent the elemental components of C, N, K, and O,
respectively.
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■ RESULTS AND DISCUSSION
Modified red CN by the codoping of K and O is prepared from
urea and potassium persulfate as precursors through one-step
thermal polymerization approach, which is marked as RCN
(Figure 1a). For comparison, pure CN is synthesized by the
same method without the addition of potassium persulfate
(UCN). Field emission scanning electron microscopy
(FESEM) and transmission electron microscopy (TEM)
images of UCN exhibit a nanosheet-like structure (Figure
S1), while the RCN shows a honeycomb-like morphology
(Figure 1b), which is further demonstrated by the HAADF−
STEM image, and relevant elemental mapping indicates that C,
N, K, and O elements are homogeneously distributed within
the structure of RCN (Figure 1c).
The formation of CN is proved by XRD and FTIR
characterizations. The XRD spectra of UCN and RCN are
depicted in Figure 2a. The XRD signals of UCN at 13.0 and
27.5° are associated with the typical (100) plane and (002)
plane of CN.36
Notably, the (100) peak of RCN nearly
disappears, most likely due to the alteration of the in-plane
graphitic structure by K interaction within the CN matrix.37,38
Additionally, the FTIR spectra of UCN and RCN are shown in
Figure S2. A distinguishable signal at 810 cm−1
is owing to s-
triazine rings. The representative features of C−N in the
heterorings are ascribed to the signals from 1150 to 1750 cm−1
,
revealing the obtainment of CN.39,40
The peak of RCN at
around 2150 cm−1
could be ascribed to the formation of
terminal cyano groups.41
The signals from 2900 to 3500 cm−1
are indicative of O−H or N−H.42
RCN shows an obvious
redshift in the light absorption edge and enhanced visible-light
absorption compared to UCN (Figure 2b), which is a hint of
the alteration of electronic band structure by elemental doping,
thus leading to much stronger light-harvesting ability.43
As
shown in the inset of Figure 2b, the band gap of UCN and
RCN is obtained as 2.75 and 2.58 eV according to Kubelka−
Munk function. Steady-state photoluminescence (PL) spectra
qualitatively reveal the enhanced charge separation of RCN
compared to UCN (Figure S3). To further demonstrate the
better charge separation efficiency of RCN, time-resolved
photoluminescence (TRPL) spectra, photocurrent measure-
ments, and electrochemical impedance spectroscopy (EIS) are
carried out. Regarding UCN, the average lifetime of RCN
Figure 2. (a) XRD spectra, (b) UV−vis DRS and high-resolution XPS spectra of (c) C 1s, (d) N 1s, and (e) O 1s of UCN and RCN. (f) Solid-state
13
C NMR spectra of UCN and RCN.
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ACS Catal. 2023, 13, 2637−2646
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decreases from 14.67 to 3.53 ns (Figure S4a and Table S1),
implying the rapid photogenerated electron transfer through
nonradiative pathways from the bulk to interface instead of
recombination, thereby enhancing the separation efficiency of
charge carriers.44,45
As shown in Figure S4b,c, compared with
UCN, RCN shows greater density of photocurrent and smaller
Nyquist plot radius, suggesting better separation efficiency of
charge and reduced resistance to charge migration. According
to Mott−Schottky plots, both UCN and RCN belong to n-type
semiconductors because of the positive slopes (Figure S5a). It
can be measured that UCN and RCN have a flat band position
at −1.09 and −0.68 eV, respectively. The positions of the
conduction bands were estimated at −1.29 and −0.88 eV.46
The sample band structure is provided in Figure S5b. X-ray
photoelectron spectroscopy (XPS) spectra of C 1s show three
peaks at 284.8 eV, 286.1 (286.4) and 288.2 eV, corresponding
to the surface adventitious carbon, sp2
C bonded with the
−NH2 groups, and sp2
C attached to N within the heteroring,
respectively (Figure 2c).47
Additionally, the N 1s is fitted into
four peaks at 398.5, 399.9 (399.4), 401.1, and 404.3 eV, which
are associated with C−N�C, N−(C)3, nitrogen of −NH2, and
charging effects, respectively (Figure 2d).48
Moreover, as
shown in Figure 2e, the O 1s peaks originated from three peaks
at 531.9, 532.6, and 533.4 eV, corresponding to C−O, O−H,
and adsorbed oxygen, respectively.49,50
The RCN shows a
sharper and stronger peak at 531.9 eV, which could be due to
the strong oxidizing property of potassium persulfate to attack
the bi-coordinated N within the CN heterorings during
thermal polymerization, thus leading to the substitution N
sites by O atoms.51
The O doping is further demonstrated by
elemental analysis (Table S2). The ratio of O increases from
3.91% in UCN to 11.64% in RCN, while no noticeable S
content is detected (0.254%). In addition, the signals at 292.8
and 295.6 eV are assigned with K 2p orbitals (Figure S6), while
the former peak could imply the presence of potassium azide
(KN3) and existence of N−K bonds in RCN.52,53
The content
of K in RCN is further determined to be 15.2% by inductively
coupled plasma (ICP) analysis. We adopt solid-state 13
C NMR
spectroscopy to clarify the intrinsic structure of UCN and
RCN (Figure 2f). The peaks of UCN at 156.6 (C2) and 164.6
ppm (C3) are indicative of the CN3 moieties and CN2-(NHx),
respectively.54,55
As compared with UCN, the relative intensity
of the C2 peak alters, suggesting the decrease of C2 atoms in
heptazine units. Additionally, the position of C3 peak shifts 1.2
ppm for RCN, revealing that the coordination environment
around C3 atoms has altered. Combined with the shift of
tertiary nitrogen in XPS, it is possible that potassium ions exist
in the form of coordination within the CN matrix, while the
two signals at 122.1 (C1) and 171.7 ppm (C4) correspond to
the cyano group C atom and neighbor C bonded with the
cyano groups.37,50
When the well-designed RCN is utilized for glucose photo-
oxidation into gluconic acid, it certifies exceptional perform-
ance for gluconic acid production. The RCN shows >60%
glucose conversion after 6 h, while UCN presents negligible
glucose conversion (Figure 3a). In the meanwhile, the gluconic
acid yield gradually grows with time and arrives at the
maximum at 5 h, which accounts for ∼40% gluconic acid yield
by converted glucose. As the reaction time increases, gluconic
acid selectivity of RCN declines, but >60% gluconic acid
selectivity of RCN remains after 6 h reaction (Figure 3b). It is
noted that some other byproducts (e.g., glucaric acid, fructose,
arabinose, and formic acid) could be detected during the
photo-oxidation process (Figure S7), which can be regarded as
the inherent reason for the decline in gluconic acid selectivity
by over-oxidation process.56
Extra experiment using increased
glucose concentration (10 g/L) is carried out (Figure S8). The
reaction of glucose photo-oxidation to gluconic acid exhibits
Figure 3. (a) Glucose conversion and gluconic acid yield of UCN and RCN under 6 h reaction. (b) Gluconic acid selectivity of RCN upon 6 h
reaction. (c) Stability experiments of RCN of glucose photo-oxidation into gluconic acid upon 18 h. (d) Experiments of scavenger of RCN after
adding BQ, IPA, EDTA-2Na, and NaN3. (e) DMPO-•
O2
−
and (f) DMPO-•
OH ESR spectra of RCN in methanol dispersion and aqueous solution,
respectively. Reaction conditions: 10 mg photocatalyst, 2 g/L glucose solution with a volume of 10 mL (pH ∼ 7), and 300 W Xenon lamp under
air.
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∼10% glucose conversion and ∼55% gluconic acid selectivity
after 6 h, suggesting that the higher glucose concentration has
a moderately negative influence on gluconic acid production.
The effect of different K amounts has been studied (Figure
S9), and it is found that RCN-0.5 and RCN-1.5 can achieve
glucose photo-oxidation into gluconic acid with ∼33 and
∼45% glucose conversions, respectively. The gluconic acid
selectivity shows decreasing trend with reaction time, and there
are ∼58 and ∼40% gluconic acid selectivities of RCN-0.5 and
RCN-1.5 within 6 h of reaction, respectively, suggesting that a
moderate amount of K doping would be beneficial for the
gluconic acid production. Additionally, the photocatalytic
performance for K-doped CN and O-doped CN are carried
out (Figure S10). It is found that K-doped CN can achieve
∼30% glucose conversion and ∼18% gluconic acid yield upon
6 h illumination, while O-doped CN realizes ∼10% glucose
conversion and the main product becomes arabinose with a
yield of ∼8% under the same reaction conditions. The results
reveal that K doping plays an important role in gluconic acid
production from glucose photo-oxidation. As shown in Figure
3c, RCN exhibits excellent recyclability in terms of glucose
conversion and gluconic acid selectivity during the 18 h cycling
test. More importantly, the yield and selectivity of gluconic
acid of this work stands out with those reported in the
literature, since it is under mild neutral conditions instead of
harsh conditions (e.g., alkaline solution) and without the help
of any noble metals or additional oxidants (Table S3). As a
result of the scavenger experiments, primary reactive species of
photo-oxidation reaction have been further demonstrated,
where 1,4-benzoquinone (BQ), isopropanol (IPA), ethyl-
enediaminetetraacetic acid disodium salt (EDTA-2Na), and
sodium azide (NaN3) have been utilized as captures of •
O2
−
,
•
OH, h+
, and 1
O2, respectively (Figure 3d). Glucose
conversion decreases from 62.87 to 12.51, 31.66, 43.84, and
51.61% for 6 h reaction with the addition of BQ, IPA, EDTA-
2Na, and NaN3, respectively. It implies that •
O2
−
, •
OH, h+
,
and 1
O2 are favorable for the glucose photo-oxidation into
gluconic acid, while •
O2
−
and •
OH are the major active
species, which could play important roles for glucose photo-
oxidation into gluconic acid. 5,5-Dimethyl-1-pyrroline N-oxide
(DMPO) is adopted as a spin trap to conduct electron spin
resonance (ESR) spectra to further prove the major reactive
species in RCN involved in photo-oxidation. Increased
illumination time enhances the typical signal of •
O2
−
,
suggesting more •
O2
−
are generated (Figure 3e). As such,
dark condition cannot produce a signal of •
OH, but light
illumination produces an increasing signal of DMPO-•
OH
(Figure 3f), revealing more •
OH are produced during the
Figure 4. (a) Potential Gibbs free energy landscape for 2e-ORR over K, O-codoped CN system (black line). For comparison, the reactions are also
calculated over pristine (green), K-doped (red), and O-doped (blue) CN systems. The structures for each step are shown below the potential
Gibbs free energy landscape. (b) Charge density difference Δρ(r) for adsorbed O2 over each system is shown. The upper figure shows the top view,
and the down figure shows the side view. Cyan and yellow contours represent regions of electron depletion and accumulation, respectively
(isovalue of ±0.002 electron Å−3
). (c) Bader charge of the atoms in the surface layer is marked on each atom. All colors of the frames for structures
in (a), Δρ(r) in (b), and structures with Bader charges in (c) are consistent with the color in the reaction landscapes. Atom color codes: C (gray),
N (blue), O (red), and K (purple).
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photocatalytic reaction. The results of ESR demonstrated the
presence of •
O2
−
and •
OH within the photo-oxidation process.
The presence of •
O2
−
is ascribed to the ORR property of
RCN, and H2O2 is indeed detected during the photocatalytic
reaction (Figure S11). However, the valence band position of
RCN is insufficient to directly oxidize H2O into •
OH
according to the band structure analysis (Figure S5b).57
Thus, the detected •
OH most possibly comes from the in situ
decomposition of H2O2 via photo-Fenton-like process, which
indicates the dual functionality of RCN: generating and
decomposing H2O2.
Then, DFT calculations are carried out to further under-
stand the enhanced 2e-ORR activity of RCN codoped with K
and O atoms. The heptazine-based CNs are considered to be
the model structure as it is determined experimentally. It is
found by geometry optimization that the potassium ion prefers
to intercalate into the space between the CN interlayer via
bridging the layers, which is similar to other reported
works.38,58
Since the sp2
-hybridized nitrogen atom is replaced
by the oxygen atom for O-doping structure as demonstrated
experimentally, the 2e-ORR activity over K, O-codoped CN as
well as over pristine, K-doped and O-doped CN is investigated.
The potential free energy landscapes are shown in the upper
panel of Figure 4a. Along the reaction coordinate, the reference
state in the first stage refers to each CN with H2 and O2 in the
gas phase with 1 bar pressure. Oxygen adsorption step behaves
differently within the four systems. For pristine (green) and K-
doped (red) CN, the oxygen molecule can only be physically
adsorbed over the surface, and both adsorption steps proceed
endothermically. It can be explained by the charge density
difference from Figure 4b (green frame) that the π orbital
electrons deplete toward the surface of pristine CN, which
implies that it induces repulsion between O2 and CN. The
electron redistribution of O2 adsorption on K-doped CN (red
frame) is slightly larger than on pristine CN, and the π orbital
electrons accumulate toward the surface. However, the
interaction between O2 and the surface of K-doped CN is
still weak. It should be noted that O2 chemically adsorbs at the
C site on O-doped and K, O-codoped CN by forming
superoxide radicals (•
O2
−
), which can act as an important
intermediate for glucose photo-oxidation into gluconic acid.
The dramatic electron redistribution between O2 and the
surface of O-doped (blue frame) and K, O-codoped (black
frame) CN in the charge density difference figure denotes the
strong interaction between O2 and the surface. O2 adsorbs
exothermically on K, O-codoped CN but still endothermically
on O-doped CN. By analyzing the Bader charge (Figure 4c), it
is found that the dopant O atom induces the charge increase
for the neighboring C atom from +1.47 e in pristine CN to
+1.66 e in the O-doped system and to +1.64 e in the K, O-
codoped system. The stronger electronegativity for the C atom
explains the lower adsorption energies of O2 on O-doped and
K, O-codoped systems. However, the charge of nitrogen atom
coordinated with the active C atom increases from −1.21 e in
the O-doped CN to −1.06 e in the K, O-codoped CN, which
makes the repulsion of N with the adsorbed O2 weaker in the
codoped system. The following sequential hydrogenation steps
with the formation of OOH and H2O2 can proceed
exothermically compared with the reference state level. The
effect from the coverage of adsorbed O2 is also studied (Figure
S12), and it is found that the adsorption of two oxygen
molecules at the same time is more difficult. To sum up, the K,
Figure 5. (a) Concentration of in situ-generated H2O2 curve of RCN during the 6 h glucose photo-oxidation into gluconic acid process. (b)
Gluconic acid selectivity and glucose conversion of RCN under different H2O2 concentrations in Ar atmosphere for 1 h irradiation. (c) Proposed
mechanism of glucose photo-oxidation into gluconic acid on RCN.
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O-codoped CN, namely, RCN, possesses superior performance
for the generation of •
O2
−
and H2O2, which could play
significant roles during glucose photo-oxidation into gluconic
acid.
In order to further explore the effect of in situ generated
H2O2 on the gluconic acid selectivity from glucose photo-
oxidation, the concentrations of H2O2 during the photo-
catalytic reaction were measured (Figure 5a). It can be found
that the H2O2 concentration gradually increases over time and
arrives at a peak of 1535 μM at ∼1 h and gradually decreases
until the end of 6 h photocatalytic reaction, most likely due to
the exhaustion of oxygen in the reactor. Then, we performed
experiments with a series of concentration gradients of H2O2
to figure out the effect of H2O2 concentrations on the
selectivity of gluconic acid from glucose photo-oxidation
process (Figure 5b). The selectivity of gluconic acid first
increases and then decreases with the increasing concentration
of H2O2 while achieving the highest selectivity of ∼80% at a
H2O2 concentration of 1500 μM for 1 h irradiation under Ar
atmosphere. The result indicates that •
OH generated from
H2O2 decomposition via photo-Fenton-like process could
realize selective gluconic acid production, which also reveals
that the moderate concentration of H2O2 produced by 2e-
ORR plays a vital role to regulate gluconic acid selectivity. It is
noted that the control experiment under the same reaction
condition without photocatalyst shows no glucose conversion,
indicting that the photo-Fenton-like process is indeed triggered
by the rationally designed CN rather than the homogeneous
catalysis process. In order to demonstrate the photo-Fenton-
like function of RCN, ESR experiments adding H2O2 under a
N2 atmosphere are performed (Figure S13). It is found that
increased illumination time enhances the signal of the
characteristic peaks of •
OH when adding H2O2, while
negligible •
OH signal is detected without H2O2, indicating
more •
OH could be generated from the H2O2 decomposition
by RCN via photo-Fenton-like process. A detailed mechanism
is then proposed based on experimental and theoretical results
for the glucose photo-oxidation into gluconic acid over RCN
under light irradiation (Figure 5c). On the one hand, in situ-
generated H2O2 and •
OH can be realized via 2e-ORR and
photo-Fenton-like process, respectively. In detail, oxygen can
first combine with the electron to produce •
O2
−
, followed by
the formation of the immediate radical (•
OOH). Then, •
OOH
can react with the proton and the electron to generate H2O2,
followed by the decomposition of H2O2 into •
OH in situ via a
metal-free photo-Fenton-like process. On the other hand,
glucose is first converted into the intermediate state by the
deprotonation process, accompanied by the release of H2O
molecule. After that, the intermediate will combine with the
•
OH derived from H2O2, thus leading to the formation of the
final product, gluconic acid. Herein, this work demonstrates
the great potential of dually functional photocatalyst for
glucose photo-oxidation into gluconic acid over the tandem
reaction of ORR and in situ photo-Fenton-like process.
■ CONCLUSIONS
In conclusion, we have successfully synthesized a dually
functional CN photocatalyst with codoping of potassium/
oxygen. The rationally designed red CN not only achieves
much stronger visible light absorption and highly efficient
charge separation but also realizes tandem reaction of ORR
and in situ photo-Fenton-like process. DFT calculations
further demonstrate the superior performance of the modified
CN for the generation of •
O2
−
and H2O2. Accordingly, the
finely designed CN presents favorable glucose conversion
(>60%) and gluconic acid selectivity (>60%) in the presence
of only water as the solvent (without base or any additional
oxidant). This work sheds new light for the photocatalyst
design to selectively produce gluconic acid from glucose
photo-oxidation under mild conditions through in situ photo-
Fenton-like process.
■ METHODS
Synthesis of UCN and RCN. RCN was prepared as
follows: 10 g of urea and 1 g of potassium persulfate were
grinded completely in a mortar to obtain a homogeneous
mixture. Then, the mixture was put in a 100 mL crucible
covered by a lid and calcined at 550 °C for 2 h with a rate of 5
°C/min in air. Afterward, the solid sample was put in 80 °C
hot water with continuous stirring overnight. After that, the
powder was completely washed and centrifuged several times
to remove the soluble substance and dried at 60 °C for 12 h.
Finally, the final red powders were labeled as RCN. Control
samples with different K amounts were synthesized by the
same method with the addition of 0.5 and 1.5 g of potassium
persulfate, which were named as RCN-0.5 and RCN-1.5,
respectively.
For comparison, UCN was synthesized by one-step
calcination process of urea as the precursor. 10 g of urea was
heated at 550 °C for 2 h under air, and the rate of heating was
5 °C/min. Final obtained powders were labelled as UCN.
Detailed process of K-doped CN and O-doped CN
preparation can be found in the Supporting Information.
Characterizations. A Bruker D8 ADVANCE diffractom-
eter was used to characterize the XRD patterns. FTIR spectra
was obtained via a Nicolet iS 50 spectrometer. A PerkinElmer
(Lambda) spectrometer was utilized to obtain the UV−vis
spectra. The PL and TRPL spectra were obtained on F-4700
and FLS920 instruments with excited wavelength at 350 nm.
XPS was performed by an equipment (Escalab, 250Xi), and
284.8 eV was adopted as the calibrated binding energy. NMR
spectra were acquired via a Bruker AVANCE 600 MHz
spectrometer. JSM 7500 and Talos 200 microscopes were
utilized to obtain the FESEM and HRTEM images. The
electrochemical measurements were obtained by a CHI660D
workstation. Additionally, the sample-loaded FTO glass, Ag/
AgCl, and Pt were considered as the working, reference, and
counter electrodes, which were placed in 0.1 M Na2SO4
aqueous solution. The elemental analysis was conducted on a
Vario EL Cube (Germany) analyzer. The ESR spectra were
obtained by the ESR spectrometer (JES-X320, JEOL) adopting
DMPO as the spin trap. The ESR detection experiments were
conducted in methanol solution for superoxide radicals
(DMPO-•
O2
−
) and in aqueous solution for hydroxyl radicals
(DMPO-•
OH).
Photocatalytic Measurement. The photocatalytic tests
were carried out in a 20 mL glass vial. Typically, 10 mg of the
photocatalyst was distributed uniformly in 10 mL of glucose
solution (2 g/L). The tightly sealed reactor was placed in dark
condition with constant stirring for 1 h. Afterward, a 300 W
Xenon lamp was used to initiate the photocatalytic reaction.
High-performance liquid chromatography (1200 Agilent) was
utilized to analyze glucose and other reaction products with an
Aminex HPX-87H column and a refractive index detector. The
flow rate of 0.5 mL/min was used for the mobile phase of 5
mM sulfuric acid. A three-time repeat of each experiment was
ACS Catalysis pubs.acs.org/acscatalysis Research Article
https://doi.org/10.1021/acscatal.2c05931
ACS Catal. 2023, 13, 2637−2646
2643
also conducted in order to determine the error bar. The
glucose conversion, gluconic acid selectivity, and gluconic acid
yield are obtained as follows
glucose conversion
glucose glucose
glucose
100 %
O T
O
=
[ ] [ ]
[ ]
×
gluconic acid selectivity
gluconic acid
glucose glucose
100 %
T
O T
=
[ ]
[ ] [ ]
×
gluconic acid yield
gluconic acid
glucose
100 %
T
O
=
[ ]
[ ]
×
where [glucose]O
and [glucose]T
correspond to the molar
concentrations of original glucose solution and at time T
during the reaction. [gluconic acid]T
represents the molar
concentration of gluconic acid at time T during the reaction.
The concentration of H2O2 during the glucose photo-
oxidation into gluconic acid was determined by iodometry.
After a certain time of reaction, the sample solution was
collected, centrifuged, and filtered. After that, 0.1 mol L−1
solution of potassium hydrogen phthalate (C8H5KO4) and 0.4
mol L−1
solution of potassium iodide (KI) were ready for use.
Then, these three solutions were mixed in a ratio of 1:1:1 and
left to stand for 2 h, where H2O2 could react with iodide
anions (I−
) under acidic condition to produce I3
−
(H2O2 + 3I−
+2H+
→ I3
−
+2H2O). The amount of I3
−
was then measured
by a UV−visible spectrometer (Lambda, PerkinElmer) based
on the characteristic absorption at 350 nm.
Computational Details. DFT calculations are carried out
with the Vienna Ab-initio Simulation Package (VASP).59−61
The Kohn−Sham orbitals are expanded with plane waves using
a 450 eV energy cutoff, and the interaction between the
valence electrons and the cores is described with the plane
augmented wave approach.62,63
The number of valence
electrons considered in the calculations are 7 (K), 6 (O), 5
(N), 4 (C), and 1 (H). The exchange−correlation effects are
described within the generalized gradient approximation
according to Perdew, Burke, and Ernzerhof.64
The D3
approach proposed by Grimme and co-workers is added to
describe the vdW interactions.65,66
Structures are optimized
with the conjugate gradient method, and geometries are
considered to be converged when the electronic energy
difference between subsequent steps is lower than 1 × 10−5
eV and the largest force is lower than 0.03 eV/Å. The pressure
for H2 and O2 is set as 1 bar. The charge density difference plot
is performed via VESTA.67
The Bader charge was calculated by
using the algorithm developed by G. Henkelman’s group.68,69
■ ASSOCIATED CONTENT
*
sı Supporting Information
The Supporting Information is available free of charge at
https://pubs.acs.org/doi/10.1021/acscatal.2c05931.
Preparation process; FESEM image; TEM image; FTIR
spectra; steady-state PL spectra; TRPL spectra; photo-
current measurements and EIS Nyquist plots; Mott−
Schottky plots; XPS spectra; HPLC measurements;
glucose conversion and gluconic acid selectivity of
higher glucose concentration and different K amounts;
glucose conversion and gluconic acid yield of K-doped
CN and O-doped CN; photograph of the H2O2 test
paper; potential Gibbs free energy landscape; ESR
spectra; fluorescence lifetimes; ICP and elemental
analysis; and comparison of gluconic acid yield with
those in the literature (PDF)
■ AUTHOR INFORMATION
Corresponding Authors
Heng Zhao − Department of Chemical and Petroleum
Engineering, University of Calgary, Calgary, Alberta T2N
1N4, Canada; Email: heng.zhao1@ucalgary.ca
Md Golam Kibria − Department of Chemical and Petroleum
Engineering, University of Calgary, Calgary, Alberta T2N
1N4, Canada; orcid.org/0000-0003-3105-5576;
Email: md.kibria@ucalgary.ca
Jinguang Hu − Department of Chemical and Petroleum
Engineering, University of Calgary, Calgary, Alberta T2N
1N4, Canada; orcid.org/0000-0001-8033-7102;
Email: jinguang.hu@ucalgary.ca
Authors
Jiu Wang − Department of Chemical and Petroleum
Engineering, University of Calgary, Calgary, Alberta T2N
1N4, Canada
Lin Chen − Department of Physics and Competence Centre for
Catalysis, Chalmers University of Technology, SE-412 96
Göteborg, Sweden; orcid.org/0000-0002-7905-9587
Pawan Kumar − Department of Chemical and Petroleum
Engineering, University of Calgary, Calgary, Alberta T2N
1N4, Canada; orcid.org/0000-0003-2804-9298
Stephen R. Larter − Department of Geosciences, University of
Calgary, Calgary Alberta T2N 1N4, Canada
Complete contact information is available at:
https://pubs.acs.org/10.1021/acscatal.2c05931
Author Contributions
∥
J.W. and L.C. contributed equally in this work.
Notes
The authors declare no competing financial interest.
■ ACKNOWLEDGMENTS
This work was supported by the Canada First Research
Excellence Fund (CFREF).
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In Situ Photo-Fenton-Like Tandem Reaction for Selective Gluconic Acid Production from Glucose Photo-Oxidation

  • 1. In Situ Photo-Fenton-Like Tandem Reaction for Selective Gluconic Acid Production from Glucose Photo-Oxidation Jiu Wang,∥ Lin Chen,∥ Heng Zhao,* Pawan Kumar, Stephen R. Larter, Md Golam Kibria,* and Jinguang Hu* Cite This: ACS Catal. 2023, 13, 2637−2646 Read Online ACCESS Metrics & More Article Recommendations * sı Supporting Information ABSTRACT: Biomass photorefining to selectively produce value- added bioproducts is an emerging alternative biomass valorization approach to alleviate energy crisis and achieve carbon neutrality. Here, we demonstrate an efficient and selective glucose photo- oxidation to gluconic acid via a rationally designed dual-functional carbon nitride photocatalyst that not only allows H2O2 production via 2e− oxygen reduction reaction (2e-ORR) but also realizes in situ photo-Fenton-like reaction. As a result, the essential oxidative species (• O2 − and • OH) for glucose oxidation into gluconic acid are generated that achieves >60% glucose conversion and >60% of gluconic acid selectivity within 4 h. Density functional theory calculations demonstrate the superior performance of the photo- catalyst for • O2 − and H2O2 generation. Further experimental results reveal that the moderate concentration of H2O2 produced by 2e-ORR reaction plays a vital role in regulatinge gluconic acid selectivity. This work demonstrates a good example to realize selective biomass photorefining through tandem reaction of ORR and in situ photo-Fenton-like process, which could have profound impact on artificial photoenzyme systems involving moderate H2O2 modulation. KEYWORDS: glucose photo-oxidation, gluconic acid, tandem reaction, 2e-ORR, in situ photo-Fenton-like reaction, photo-enzyme Biomass valorization into fuels and chemicals provides an effective approach to resolve energy shortage and environmental issues.1,2 The abundant monosaccharide glucose has already been converted into a diverse range of chemicals with added value including arabinose, gluconic acid, glucaric acid, fructose, lactic acid, and 5-hydroxymethylfurfu- ral.3−7 Among these, gluconic acid together with its salts have already been widely used in the food and pharmaceutical industry and will reach a remarkable market value of US$ 1.9 billion by 2028.8−10 The current gluconic acid production mainly rely on enzyme-catalyzed and chemo-catalyzed processes, in which the first method involves expensive enzyme and the second method gives rise to environmental problems.11 Photocatalysis is an emerging green and sustainable alternative technology platform for chemical production,12−14 but simultaneously achieving good substrate conversion and product selectivity over photocatalysis is still challenging, especially using water as the solvent.15,16 Previous studies have reported selective gluconic acid production from glucose photo-oxidation, however, either on alkaline solution or with the aid of a noble metal or an oxidant.17,18 Therefore, rational design of the photocatalyst and the reaction pathway is highly desired for selective biomass photorefining under mild reaction conditions. Fenton reaction has been demonstrated as one of the most efficient methods for water purification in recent years.19,20 Typically, free hydroxyl radicals (• OH) are generated during the Fenton oxidation process as the active species to mineralize the organic pollutants, while the reaction process and liquid product selectivity are difficult to be controlled.21,22 Besides, the addition of excessive H2O2, the Fe2+ ions in water, and the limited pH range restrained the application of Fenton process.23 It has been reported that high-value gluconic acid can be obtained through selective glucose oxidation via traditional Fenton process assisted by ultrasonication method, during which • OH plays an important role in the oxidation of glucose.24 However, excessive • OH might lead to over- oxidation process due to the highly oxidative nature.25,26 Alternatively, in situ photo-induced Fenton-like process with rational control of active species concentration is foreseen to light up the selective conversion of glucose into gluconic acid. Received: December 1, 2022 Revised: January 25, 2023 Research Article pubs.acs.org/acscatalysis © XXXX American Chemical Society 2637 https://doi.org/10.1021/acscatal.2c05931 ACS Catal. 2023, 13, 2637−2646 Downloaded via UNIV OF CALGARY on February 9, 2023 at 04:45:49 (UTC). See https://pubs.acs.org/sharingguidelines for options on how to legitimately share published articles.
  • 2. Thus, the key issue is how to design a dual functional photocatalyst that can both generate H2O2 and decompose it via in situ photo-Fenton process. Polymeric carbon nitride (CN) has been considered to be an ideal and eco-friendly photocatalyst along with surpassing visible light response and promising band positions.27,28 More importantly, CN has been demonstrated to have highly selective H2O2 production via the 2e− oxygen reduction reaction (2e-ORR).29,30 However, the bulk CN derived from ordinary thermal polymerization usually suffers from low efficiency owing to severe recombination of electron−hole pairs.31 Band gap engineering is a capable approach to improve the 2e-ORR process of CN-based photocatalysts to form H2O2.32−34 Additionally, alkalinization with cyano groups has been proven to effectively decompose H2O2 into • OH via photo-Fenton process.35 Inspired by the aforementioned literature, designing a dual functional CN photocatalyst that can realize tandem reaction of ORR and in situ photo-Fenton- like process would be a feasible strategy for selective glucose photo-oxidation into gluconic acid. To the best of our knowledge, such a conceptual design applied for selective biomass valorization into value-added chemicals is yet to be investigated. Herein, for the first time, we demonstrate the feasibility of selective glucose photo-oxidation into gluconic acid by a dual functional CN photocatalyst. The procedure is achieved via the fine construction of red CN photocatalyst with codoping of potassium/oxygen, which can generate H2O2 by 2e-ORR and in situ decompose into • OH via photo-Fenton-like process. Density functional theory (DFT) calculations demonstrate the superior performance of the modified CN for the generation of • O2 − and H2O2. Accordingly, the well-designed potassium/ oxygen codoped red CN exhibited >60% glucose conversion and >60% gluconic acid selectivity after 4 h upon light irradiation. The current study offers an alternative approach for dual functional photocatalyst design to selectively produce gluconic acid via tandem reaction of photocatalytic ORR and in situ photo-Fenton-like process, which could also inspire artificial photoenzyme systems involving moderate H2O2 modulation. Figure 1. (a) Synthetic process for K, O codoped red CN through one-step thermal copolymerization. (b) FESEM image and (c) HAADF-STEM image of RCN and relevant elemental mappings. The colors of red, green, yellow, and blue represent the elemental components of C, N, K, and O, respectively. ACS Catalysis pubs.acs.org/acscatalysis Research Article https://doi.org/10.1021/acscatal.2c05931 ACS Catal. 2023, 13, 2637−2646 2638
  • 3. ■ RESULTS AND DISCUSSION Modified red CN by the codoping of K and O is prepared from urea and potassium persulfate as precursors through one-step thermal polymerization approach, which is marked as RCN (Figure 1a). For comparison, pure CN is synthesized by the same method without the addition of potassium persulfate (UCN). Field emission scanning electron microscopy (FESEM) and transmission electron microscopy (TEM) images of UCN exhibit a nanosheet-like structure (Figure S1), while the RCN shows a honeycomb-like morphology (Figure 1b), which is further demonstrated by the HAADF− STEM image, and relevant elemental mapping indicates that C, N, K, and O elements are homogeneously distributed within the structure of RCN (Figure 1c). The formation of CN is proved by XRD and FTIR characterizations. The XRD spectra of UCN and RCN are depicted in Figure 2a. The XRD signals of UCN at 13.0 and 27.5° are associated with the typical (100) plane and (002) plane of CN.36 Notably, the (100) peak of RCN nearly disappears, most likely due to the alteration of the in-plane graphitic structure by K interaction within the CN matrix.37,38 Additionally, the FTIR spectra of UCN and RCN are shown in Figure S2. A distinguishable signal at 810 cm−1 is owing to s- triazine rings. The representative features of C−N in the heterorings are ascribed to the signals from 1150 to 1750 cm−1 , revealing the obtainment of CN.39,40 The peak of RCN at around 2150 cm−1 could be ascribed to the formation of terminal cyano groups.41 The signals from 2900 to 3500 cm−1 are indicative of O−H or N−H.42 RCN shows an obvious redshift in the light absorption edge and enhanced visible-light absorption compared to UCN (Figure 2b), which is a hint of the alteration of electronic band structure by elemental doping, thus leading to much stronger light-harvesting ability.43 As shown in the inset of Figure 2b, the band gap of UCN and RCN is obtained as 2.75 and 2.58 eV according to Kubelka− Munk function. Steady-state photoluminescence (PL) spectra qualitatively reveal the enhanced charge separation of RCN compared to UCN (Figure S3). To further demonstrate the better charge separation efficiency of RCN, time-resolved photoluminescence (TRPL) spectra, photocurrent measure- ments, and electrochemical impedance spectroscopy (EIS) are carried out. Regarding UCN, the average lifetime of RCN Figure 2. (a) XRD spectra, (b) UV−vis DRS and high-resolution XPS spectra of (c) C 1s, (d) N 1s, and (e) O 1s of UCN and RCN. (f) Solid-state 13 C NMR spectra of UCN and RCN. ACS Catalysis pubs.acs.org/acscatalysis Research Article https://doi.org/10.1021/acscatal.2c05931 ACS Catal. 2023, 13, 2637−2646 2639
  • 4. decreases from 14.67 to 3.53 ns (Figure S4a and Table S1), implying the rapid photogenerated electron transfer through nonradiative pathways from the bulk to interface instead of recombination, thereby enhancing the separation efficiency of charge carriers.44,45 As shown in Figure S4b,c, compared with UCN, RCN shows greater density of photocurrent and smaller Nyquist plot radius, suggesting better separation efficiency of charge and reduced resistance to charge migration. According to Mott−Schottky plots, both UCN and RCN belong to n-type semiconductors because of the positive slopes (Figure S5a). It can be measured that UCN and RCN have a flat band position at −1.09 and −0.68 eV, respectively. The positions of the conduction bands were estimated at −1.29 and −0.88 eV.46 The sample band structure is provided in Figure S5b. X-ray photoelectron spectroscopy (XPS) spectra of C 1s show three peaks at 284.8 eV, 286.1 (286.4) and 288.2 eV, corresponding to the surface adventitious carbon, sp2 C bonded with the −NH2 groups, and sp2 C attached to N within the heteroring, respectively (Figure 2c).47 Additionally, the N 1s is fitted into four peaks at 398.5, 399.9 (399.4), 401.1, and 404.3 eV, which are associated with C−N�C, N−(C)3, nitrogen of −NH2, and charging effects, respectively (Figure 2d).48 Moreover, as shown in Figure 2e, the O 1s peaks originated from three peaks at 531.9, 532.6, and 533.4 eV, corresponding to C−O, O−H, and adsorbed oxygen, respectively.49,50 The RCN shows a sharper and stronger peak at 531.9 eV, which could be due to the strong oxidizing property of potassium persulfate to attack the bi-coordinated N within the CN heterorings during thermal polymerization, thus leading to the substitution N sites by O atoms.51 The O doping is further demonstrated by elemental analysis (Table S2). The ratio of O increases from 3.91% in UCN to 11.64% in RCN, while no noticeable S content is detected (0.254%). In addition, the signals at 292.8 and 295.6 eV are assigned with K 2p orbitals (Figure S6), while the former peak could imply the presence of potassium azide (KN3) and existence of N−K bonds in RCN.52,53 The content of K in RCN is further determined to be 15.2% by inductively coupled plasma (ICP) analysis. We adopt solid-state 13 C NMR spectroscopy to clarify the intrinsic structure of UCN and RCN (Figure 2f). The peaks of UCN at 156.6 (C2) and 164.6 ppm (C3) are indicative of the CN3 moieties and CN2-(NHx), respectively.54,55 As compared with UCN, the relative intensity of the C2 peak alters, suggesting the decrease of C2 atoms in heptazine units. Additionally, the position of C3 peak shifts 1.2 ppm for RCN, revealing that the coordination environment around C3 atoms has altered. Combined with the shift of tertiary nitrogen in XPS, it is possible that potassium ions exist in the form of coordination within the CN matrix, while the two signals at 122.1 (C1) and 171.7 ppm (C4) correspond to the cyano group C atom and neighbor C bonded with the cyano groups.37,50 When the well-designed RCN is utilized for glucose photo- oxidation into gluconic acid, it certifies exceptional perform- ance for gluconic acid production. The RCN shows >60% glucose conversion after 6 h, while UCN presents negligible glucose conversion (Figure 3a). In the meanwhile, the gluconic acid yield gradually grows with time and arrives at the maximum at 5 h, which accounts for ∼40% gluconic acid yield by converted glucose. As the reaction time increases, gluconic acid selectivity of RCN declines, but >60% gluconic acid selectivity of RCN remains after 6 h reaction (Figure 3b). It is noted that some other byproducts (e.g., glucaric acid, fructose, arabinose, and formic acid) could be detected during the photo-oxidation process (Figure S7), which can be regarded as the inherent reason for the decline in gluconic acid selectivity by over-oxidation process.56 Extra experiment using increased glucose concentration (10 g/L) is carried out (Figure S8). The reaction of glucose photo-oxidation to gluconic acid exhibits Figure 3. (a) Glucose conversion and gluconic acid yield of UCN and RCN under 6 h reaction. (b) Gluconic acid selectivity of RCN upon 6 h reaction. (c) Stability experiments of RCN of glucose photo-oxidation into gluconic acid upon 18 h. (d) Experiments of scavenger of RCN after adding BQ, IPA, EDTA-2Na, and NaN3. (e) DMPO-• O2 − and (f) DMPO-• OH ESR spectra of RCN in methanol dispersion and aqueous solution, respectively. Reaction conditions: 10 mg photocatalyst, 2 g/L glucose solution with a volume of 10 mL (pH ∼ 7), and 300 W Xenon lamp under air. ACS Catalysis pubs.acs.org/acscatalysis Research Article https://doi.org/10.1021/acscatal.2c05931 ACS Catal. 2023, 13, 2637−2646 2640
  • 5. ∼10% glucose conversion and ∼55% gluconic acid selectivity after 6 h, suggesting that the higher glucose concentration has a moderately negative influence on gluconic acid production. The effect of different K amounts has been studied (Figure S9), and it is found that RCN-0.5 and RCN-1.5 can achieve glucose photo-oxidation into gluconic acid with ∼33 and ∼45% glucose conversions, respectively. The gluconic acid selectivity shows decreasing trend with reaction time, and there are ∼58 and ∼40% gluconic acid selectivities of RCN-0.5 and RCN-1.5 within 6 h of reaction, respectively, suggesting that a moderate amount of K doping would be beneficial for the gluconic acid production. Additionally, the photocatalytic performance for K-doped CN and O-doped CN are carried out (Figure S10). It is found that K-doped CN can achieve ∼30% glucose conversion and ∼18% gluconic acid yield upon 6 h illumination, while O-doped CN realizes ∼10% glucose conversion and the main product becomes arabinose with a yield of ∼8% under the same reaction conditions. The results reveal that K doping plays an important role in gluconic acid production from glucose photo-oxidation. As shown in Figure 3c, RCN exhibits excellent recyclability in terms of glucose conversion and gluconic acid selectivity during the 18 h cycling test. More importantly, the yield and selectivity of gluconic acid of this work stands out with those reported in the literature, since it is under mild neutral conditions instead of harsh conditions (e.g., alkaline solution) and without the help of any noble metals or additional oxidants (Table S3). As a result of the scavenger experiments, primary reactive species of photo-oxidation reaction have been further demonstrated, where 1,4-benzoquinone (BQ), isopropanol (IPA), ethyl- enediaminetetraacetic acid disodium salt (EDTA-2Na), and sodium azide (NaN3) have been utilized as captures of • O2 − , • OH, h+ , and 1 O2, respectively (Figure 3d). Glucose conversion decreases from 62.87 to 12.51, 31.66, 43.84, and 51.61% for 6 h reaction with the addition of BQ, IPA, EDTA- 2Na, and NaN3, respectively. It implies that • O2 − , • OH, h+ , and 1 O2 are favorable for the glucose photo-oxidation into gluconic acid, while • O2 − and • OH are the major active species, which could play important roles for glucose photo- oxidation into gluconic acid. 5,5-Dimethyl-1-pyrroline N-oxide (DMPO) is adopted as a spin trap to conduct electron spin resonance (ESR) spectra to further prove the major reactive species in RCN involved in photo-oxidation. Increased illumination time enhances the typical signal of • O2 − , suggesting more • O2 − are generated (Figure 3e). As such, dark condition cannot produce a signal of • OH, but light illumination produces an increasing signal of DMPO-• OH (Figure 3f), revealing more • OH are produced during the Figure 4. (a) Potential Gibbs free energy landscape for 2e-ORR over K, O-codoped CN system (black line). For comparison, the reactions are also calculated over pristine (green), K-doped (red), and O-doped (blue) CN systems. The structures for each step are shown below the potential Gibbs free energy landscape. (b) Charge density difference Δρ(r) for adsorbed O2 over each system is shown. The upper figure shows the top view, and the down figure shows the side view. Cyan and yellow contours represent regions of electron depletion and accumulation, respectively (isovalue of ±0.002 electron Å−3 ). (c) Bader charge of the atoms in the surface layer is marked on each atom. All colors of the frames for structures in (a), Δρ(r) in (b), and structures with Bader charges in (c) are consistent with the color in the reaction landscapes. Atom color codes: C (gray), N (blue), O (red), and K (purple). ACS Catalysis pubs.acs.org/acscatalysis Research Article https://doi.org/10.1021/acscatal.2c05931 ACS Catal. 2023, 13, 2637−2646 2641
  • 6. photocatalytic reaction. The results of ESR demonstrated the presence of • O2 − and • OH within the photo-oxidation process. The presence of • O2 − is ascribed to the ORR property of RCN, and H2O2 is indeed detected during the photocatalytic reaction (Figure S11). However, the valence band position of RCN is insufficient to directly oxidize H2O into • OH according to the band structure analysis (Figure S5b).57 Thus, the detected • OH most possibly comes from the in situ decomposition of H2O2 via photo-Fenton-like process, which indicates the dual functionality of RCN: generating and decomposing H2O2. Then, DFT calculations are carried out to further under- stand the enhanced 2e-ORR activity of RCN codoped with K and O atoms. The heptazine-based CNs are considered to be the model structure as it is determined experimentally. It is found by geometry optimization that the potassium ion prefers to intercalate into the space between the CN interlayer via bridging the layers, which is similar to other reported works.38,58 Since the sp2 -hybridized nitrogen atom is replaced by the oxygen atom for O-doping structure as demonstrated experimentally, the 2e-ORR activity over K, O-codoped CN as well as over pristine, K-doped and O-doped CN is investigated. The potential free energy landscapes are shown in the upper panel of Figure 4a. Along the reaction coordinate, the reference state in the first stage refers to each CN with H2 and O2 in the gas phase with 1 bar pressure. Oxygen adsorption step behaves differently within the four systems. For pristine (green) and K- doped (red) CN, the oxygen molecule can only be physically adsorbed over the surface, and both adsorption steps proceed endothermically. It can be explained by the charge density difference from Figure 4b (green frame) that the π orbital electrons deplete toward the surface of pristine CN, which implies that it induces repulsion between O2 and CN. The electron redistribution of O2 adsorption on K-doped CN (red frame) is slightly larger than on pristine CN, and the π orbital electrons accumulate toward the surface. However, the interaction between O2 and the surface of K-doped CN is still weak. It should be noted that O2 chemically adsorbs at the C site on O-doped and K, O-codoped CN by forming superoxide radicals (• O2 − ), which can act as an important intermediate for glucose photo-oxidation into gluconic acid. The dramatic electron redistribution between O2 and the surface of O-doped (blue frame) and K, O-codoped (black frame) CN in the charge density difference figure denotes the strong interaction between O2 and the surface. O2 adsorbs exothermically on K, O-codoped CN but still endothermically on O-doped CN. By analyzing the Bader charge (Figure 4c), it is found that the dopant O atom induces the charge increase for the neighboring C atom from +1.47 e in pristine CN to +1.66 e in the O-doped system and to +1.64 e in the K, O- codoped system. The stronger electronegativity for the C atom explains the lower adsorption energies of O2 on O-doped and K, O-codoped systems. However, the charge of nitrogen atom coordinated with the active C atom increases from −1.21 e in the O-doped CN to −1.06 e in the K, O-codoped CN, which makes the repulsion of N with the adsorbed O2 weaker in the codoped system. The following sequential hydrogenation steps with the formation of OOH and H2O2 can proceed exothermically compared with the reference state level. The effect from the coverage of adsorbed O2 is also studied (Figure S12), and it is found that the adsorption of two oxygen molecules at the same time is more difficult. To sum up, the K, Figure 5. (a) Concentration of in situ-generated H2O2 curve of RCN during the 6 h glucose photo-oxidation into gluconic acid process. (b) Gluconic acid selectivity and glucose conversion of RCN under different H2O2 concentrations in Ar atmosphere for 1 h irradiation. (c) Proposed mechanism of glucose photo-oxidation into gluconic acid on RCN. ACS Catalysis pubs.acs.org/acscatalysis Research Article https://doi.org/10.1021/acscatal.2c05931 ACS Catal. 2023, 13, 2637−2646 2642
  • 7. O-codoped CN, namely, RCN, possesses superior performance for the generation of • O2 − and H2O2, which could play significant roles during glucose photo-oxidation into gluconic acid. In order to further explore the effect of in situ generated H2O2 on the gluconic acid selectivity from glucose photo- oxidation, the concentrations of H2O2 during the photo- catalytic reaction were measured (Figure 5a). It can be found that the H2O2 concentration gradually increases over time and arrives at a peak of 1535 μM at ∼1 h and gradually decreases until the end of 6 h photocatalytic reaction, most likely due to the exhaustion of oxygen in the reactor. Then, we performed experiments with a series of concentration gradients of H2O2 to figure out the effect of H2O2 concentrations on the selectivity of gluconic acid from glucose photo-oxidation process (Figure 5b). The selectivity of gluconic acid first increases and then decreases with the increasing concentration of H2O2 while achieving the highest selectivity of ∼80% at a H2O2 concentration of 1500 μM for 1 h irradiation under Ar atmosphere. The result indicates that • OH generated from H2O2 decomposition via photo-Fenton-like process could realize selective gluconic acid production, which also reveals that the moderate concentration of H2O2 produced by 2e- ORR plays a vital role to regulate gluconic acid selectivity. It is noted that the control experiment under the same reaction condition without photocatalyst shows no glucose conversion, indicting that the photo-Fenton-like process is indeed triggered by the rationally designed CN rather than the homogeneous catalysis process. In order to demonstrate the photo-Fenton- like function of RCN, ESR experiments adding H2O2 under a N2 atmosphere are performed (Figure S13). It is found that increased illumination time enhances the signal of the characteristic peaks of • OH when adding H2O2, while negligible • OH signal is detected without H2O2, indicating more • OH could be generated from the H2O2 decomposition by RCN via photo-Fenton-like process. A detailed mechanism is then proposed based on experimental and theoretical results for the glucose photo-oxidation into gluconic acid over RCN under light irradiation (Figure 5c). On the one hand, in situ- generated H2O2 and • OH can be realized via 2e-ORR and photo-Fenton-like process, respectively. In detail, oxygen can first combine with the electron to produce • O2 − , followed by the formation of the immediate radical (• OOH). Then, • OOH can react with the proton and the electron to generate H2O2, followed by the decomposition of H2O2 into • OH in situ via a metal-free photo-Fenton-like process. On the other hand, glucose is first converted into the intermediate state by the deprotonation process, accompanied by the release of H2O molecule. After that, the intermediate will combine with the • OH derived from H2O2, thus leading to the formation of the final product, gluconic acid. Herein, this work demonstrates the great potential of dually functional photocatalyst for glucose photo-oxidation into gluconic acid over the tandem reaction of ORR and in situ photo-Fenton-like process. ■ CONCLUSIONS In conclusion, we have successfully synthesized a dually functional CN photocatalyst with codoping of potassium/ oxygen. The rationally designed red CN not only achieves much stronger visible light absorption and highly efficient charge separation but also realizes tandem reaction of ORR and in situ photo-Fenton-like process. DFT calculations further demonstrate the superior performance of the modified CN for the generation of • O2 − and H2O2. Accordingly, the finely designed CN presents favorable glucose conversion (>60%) and gluconic acid selectivity (>60%) in the presence of only water as the solvent (without base or any additional oxidant). This work sheds new light for the photocatalyst design to selectively produce gluconic acid from glucose photo-oxidation under mild conditions through in situ photo- Fenton-like process. ■ METHODS Synthesis of UCN and RCN. RCN was prepared as follows: 10 g of urea and 1 g of potassium persulfate were grinded completely in a mortar to obtain a homogeneous mixture. Then, the mixture was put in a 100 mL crucible covered by a lid and calcined at 550 °C for 2 h with a rate of 5 °C/min in air. Afterward, the solid sample was put in 80 °C hot water with continuous stirring overnight. After that, the powder was completely washed and centrifuged several times to remove the soluble substance and dried at 60 °C for 12 h. Finally, the final red powders were labeled as RCN. Control samples with different K amounts were synthesized by the same method with the addition of 0.5 and 1.5 g of potassium persulfate, which were named as RCN-0.5 and RCN-1.5, respectively. For comparison, UCN was synthesized by one-step calcination process of urea as the precursor. 10 g of urea was heated at 550 °C for 2 h under air, and the rate of heating was 5 °C/min. Final obtained powders were labelled as UCN. Detailed process of K-doped CN and O-doped CN preparation can be found in the Supporting Information. Characterizations. A Bruker D8 ADVANCE diffractom- eter was used to characterize the XRD patterns. FTIR spectra was obtained via a Nicolet iS 50 spectrometer. A PerkinElmer (Lambda) spectrometer was utilized to obtain the UV−vis spectra. The PL and TRPL spectra were obtained on F-4700 and FLS920 instruments with excited wavelength at 350 nm. XPS was performed by an equipment (Escalab, 250Xi), and 284.8 eV was adopted as the calibrated binding energy. NMR spectra were acquired via a Bruker AVANCE 600 MHz spectrometer. JSM 7500 and Talos 200 microscopes were utilized to obtain the FESEM and HRTEM images. The electrochemical measurements were obtained by a CHI660D workstation. Additionally, the sample-loaded FTO glass, Ag/ AgCl, and Pt were considered as the working, reference, and counter electrodes, which were placed in 0.1 M Na2SO4 aqueous solution. The elemental analysis was conducted on a Vario EL Cube (Germany) analyzer. The ESR spectra were obtained by the ESR spectrometer (JES-X320, JEOL) adopting DMPO as the spin trap. The ESR detection experiments were conducted in methanol solution for superoxide radicals (DMPO-• O2 − ) and in aqueous solution for hydroxyl radicals (DMPO-• OH). Photocatalytic Measurement. The photocatalytic tests were carried out in a 20 mL glass vial. Typically, 10 mg of the photocatalyst was distributed uniformly in 10 mL of glucose solution (2 g/L). The tightly sealed reactor was placed in dark condition with constant stirring for 1 h. Afterward, a 300 W Xenon lamp was used to initiate the photocatalytic reaction. High-performance liquid chromatography (1200 Agilent) was utilized to analyze glucose and other reaction products with an Aminex HPX-87H column and a refractive index detector. The flow rate of 0.5 mL/min was used for the mobile phase of 5 mM sulfuric acid. A three-time repeat of each experiment was ACS Catalysis pubs.acs.org/acscatalysis Research Article https://doi.org/10.1021/acscatal.2c05931 ACS Catal. 2023, 13, 2637−2646 2643
  • 8. also conducted in order to determine the error bar. The glucose conversion, gluconic acid selectivity, and gluconic acid yield are obtained as follows glucose conversion glucose glucose glucose 100 % O T O = [ ] [ ] [ ] × gluconic acid selectivity gluconic acid glucose glucose 100 % T O T = [ ] [ ] [ ] × gluconic acid yield gluconic acid glucose 100 % T O = [ ] [ ] × where [glucose]O and [glucose]T correspond to the molar concentrations of original glucose solution and at time T during the reaction. [gluconic acid]T represents the molar concentration of gluconic acid at time T during the reaction. The concentration of H2O2 during the glucose photo- oxidation into gluconic acid was determined by iodometry. After a certain time of reaction, the sample solution was collected, centrifuged, and filtered. After that, 0.1 mol L−1 solution of potassium hydrogen phthalate (C8H5KO4) and 0.4 mol L−1 solution of potassium iodide (KI) were ready for use. Then, these three solutions were mixed in a ratio of 1:1:1 and left to stand for 2 h, where H2O2 could react with iodide anions (I− ) under acidic condition to produce I3 − (H2O2 + 3I− +2H+ → I3 − +2H2O). The amount of I3 − was then measured by a UV−visible spectrometer (Lambda, PerkinElmer) based on the characteristic absorption at 350 nm. Computational Details. DFT calculations are carried out with the Vienna Ab-initio Simulation Package (VASP).59−61 The Kohn−Sham orbitals are expanded with plane waves using a 450 eV energy cutoff, and the interaction between the valence electrons and the cores is described with the plane augmented wave approach.62,63 The number of valence electrons considered in the calculations are 7 (K), 6 (O), 5 (N), 4 (C), and 1 (H). The exchange−correlation effects are described within the generalized gradient approximation according to Perdew, Burke, and Ernzerhof.64 The D3 approach proposed by Grimme and co-workers is added to describe the vdW interactions.65,66 Structures are optimized with the conjugate gradient method, and geometries are considered to be converged when the electronic energy difference between subsequent steps is lower than 1 × 10−5 eV and the largest force is lower than 0.03 eV/Å. The pressure for H2 and O2 is set as 1 bar. The charge density difference plot is performed via VESTA.67 The Bader charge was calculated by using the algorithm developed by G. Henkelman’s group.68,69 ■ ASSOCIATED CONTENT * sı Supporting Information The Supporting Information is available free of charge at https://pubs.acs.org/doi/10.1021/acscatal.2c05931. Preparation process; FESEM image; TEM image; FTIR spectra; steady-state PL spectra; TRPL spectra; photo- current measurements and EIS Nyquist plots; Mott− Schottky plots; XPS spectra; HPLC measurements; glucose conversion and gluconic acid selectivity of higher glucose concentration and different K amounts; glucose conversion and gluconic acid yield of K-doped CN and O-doped CN; photograph of the H2O2 test paper; potential Gibbs free energy landscape; ESR spectra; fluorescence lifetimes; ICP and elemental analysis; and comparison of gluconic acid yield with those in the literature (PDF) ■ AUTHOR INFORMATION Corresponding Authors Heng Zhao − Department of Chemical and Petroleum Engineering, University of Calgary, Calgary, Alberta T2N 1N4, Canada; Email: heng.zhao1@ucalgary.ca Md Golam Kibria − Department of Chemical and Petroleum Engineering, University of Calgary, Calgary, Alberta T2N 1N4, Canada; orcid.org/0000-0003-3105-5576; Email: md.kibria@ucalgary.ca Jinguang Hu − Department of Chemical and Petroleum Engineering, University of Calgary, Calgary, Alberta T2N 1N4, Canada; orcid.org/0000-0001-8033-7102; Email: jinguang.hu@ucalgary.ca Authors Jiu Wang − Department of Chemical and Petroleum Engineering, University of Calgary, Calgary, Alberta T2N 1N4, Canada Lin Chen − Department of Physics and Competence Centre for Catalysis, Chalmers University of Technology, SE-412 96 Göteborg, Sweden; orcid.org/0000-0002-7905-9587 Pawan Kumar − Department of Chemical and Petroleum Engineering, University of Calgary, Calgary, Alberta T2N 1N4, Canada; orcid.org/0000-0003-2804-9298 Stephen R. Larter − Department of Geosciences, University of Calgary, Calgary Alberta T2N 1N4, Canada Complete contact information is available at: https://pubs.acs.org/10.1021/acscatal.2c05931 Author Contributions ∥ J.W. and L.C. contributed equally in this work. Notes The authors declare no competing financial interest. ■ ACKNOWLEDGMENTS This work was supported by the Canada First Research Excellence Fund (CFREF). ■ REFERENCES (1) Wu, X.; Luo, N.; Xie, S.; Zhang, H.; Zhang, Q.; Wang, F.; Wang, Y. Photocatalytic transformations of lignocellulosic biomass into chemicals. Chem. Soc. Rev. 2020, 49, 6198−6223. (2) Nwosu, U.; Wang, A.; Palma, B.; Zhao, H.; Khan, M. A.; Kibria, M.; Hu, J. Selective biomass photoreforming for valuable chemicals and fuels: A critical review. Renewable Sustainable Energy Rev. 2021, 148, 111266. (3) Zhang, Q.; Ge, Y.; Yang, C.; Zhang, B.; Deng, K. 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