Production of a chemical feedstock as a secondary product from a commercial nuclear reactor can increase the economic viability of the reactor and enable the deployment of nuclear energy as part of the low-carbon energy grid. Currently, commercial nuclear reactors produce underutilized energy in the form of neutrons and gamma photons. This excess energy can be exploited to drive chemical reactions, increasing the fraction of utilized energy in reactors and providing a valuable secondary product from the reactor. Gamma degradation of cellulosic biomass has been studied previously. However, real-time, on-line monitoring of the breakdown of biomass materials under gamma radiation has not been demonstrated. Here, we demonstrate on-line monitoring of the reaction of cellobiose with hydrogen peroxide under gamma radiation using Raman spectroscopy, providing in situ quantification of organic and inorganic system components.
Production of a chemical feedstock as a secondary product from a commercial nuclear reactor can increase the economic viability of the reactor and enable the deployment of nuclear energy as part of the low-carbon energy grid. Currently, commercial nuclear reactors produce underutilized energy in the form of neutrons and gamma photons. This excess energy can be exploited to drive chemical reactions, increasing the fraction of utilized energy in reactors and providing a valuable secondary product from the reactor. Gamma degradation of cellulosic biomass has been studied previously. However, real-time, on-line monitoring of the breakdown of biomass materials under gamma radiation has not been demonstrated. Here, we demonstrate on-line monitoring of the reaction of cellobiose with hydrogen peroxide under gamma radiation using Raman spectroscopy, providing in situ quantification of organic and inorganic system components.
Nuclear
energy provides a low-carbon alternative to reliably meet
energy needs regardless of weather conditions or geological location.[1,2] It represents a key piece of a diverse energy portfolio that can
effectively meet the current goals of lowering the carbon footprint
of energy production while maintaining energy security.[3,4] However, nuclear energy is more expensive than many of the renewable
energy generation technologies such as wind and solar, primarily due
to the high capital investment required in plant construction, although
modern reactors are bridging this gap.[1,2,5]As an option to increase the economic viability
of next-generation
nuclear energy, production of a secondary product, such as a chemical
feedstock, would provide an additional product stream and, with that,
a secondary source of income.[1,4,6] A second major barrier to advancing nuclear energy production is
public perception, and the ability of unused radiation from nuclear
reactors to convert recalcitrant, low-value biomass into desirable
products may improve public perception of nuclear reactors.[7] Combined with net-zero goals in chemical feedstock
production, dual-use nuclear systems for energy and commodity production
can have a significant impact on meeting carbon footprint reduction
goals.[5]Currently, nuclear reactors
are primarily commodified by using
their heat to generate steam for electricity production. There is
a large amount of unused energy in the form of photon and neutron
radiation that could be exploited to drive chemical processes to produce
feedstock materials as a secondary product of a nuclear plant.[4,8,9] Chemical processing with radiation
is not a new concept. In fact, it has been recognized for over half
a century that gamma radiation is an excellent source of high-energy
photons to drive photochemical reactions.[8,9] Dow
Chemical produced commercial quantities of ethyl bromide using gamma
irradiation from a 60Co source in the 1960s and 1970s because
it was the most cost-effective means of production to meet the demand.[10,11] Numerous other processes have received attention, including the
production of ozone and carbon monoxide.[9,12] However, direct
implementation of such processes with nuclear reactors to develop
hybrid reactors has not yet seen widespread implementation.Because of potential economic and environmental advantages, there
is a new emphasis on studying feedstock production which can be enhanced
by excess gamma, electron, and neutron radiation.[8,13−19] Lignocellulosic feedstocks have the potential to be a renewable
fuel and chemical source,[13,20−22] and γ-radiation has been investigated for use in the conversion
of waste and low-value materials, such as plant straw, into higher-value
chemicals.[23−27] For example, Driscoll et al. discussed the feasibility of including
ionizing radiation into a wood-based biorefinery.[28] Chung et al. reported the radiation-enhanced degradation
of various types of lignocellulosic materials to produce ethanol.[29] Unrealized potential exists for utilizing the
radiation from nuclear reactors in order to convert lignocellulosic
materials into valuable chemicals.A target system for enhancement
via γ-radiation is biomass
in solution with an oxidant. Hydrogen peroxide is a common oxidant
for use in the chemical conversion of biomass,[30] including cellobiose.[31,32] However, hydrogen
peroxide alone does not often meet the desired yield for biomass conversion,[33] so hydrogen peroxide treatment is often used
in combination with a catalyst,[34,35] an acidic or alkaline
medium,[33,36] or the addition of external energy (e.g.,
heat, pressure).[37] The insufficient conversion
achieved with unassisted oxidation is discussed further in the Supporting Information, with Figure S2 showing the minimal conversion of cellobiose in
hydrogen peroxide when left to react at ambient temperatures. Here,
the additional energy imparted to the system comes from γ-radiation.The focus of this study is the degradation under γ-radiation
of cellobiose, a model system for one of the main components of lignocellulosic
biomass. Lignocellulose is made up of three main macropolymers: (1)
cellulose, a polymer chain of repeating cellobiose (two d-glucose units connected by β-1 → 4 linkage) units;
(2) hemicellulose, a polymer chain of C6 or C5 monosaccharides such as mannose and xylose; and (3) lignin, a polyaromatic
constituent material. Of the three main constituents, cellulose is
typically the most abundant.[38] Anticipated
degradation products of oxidized cellobiose are shown in Figure . Deng et al. proposed
two mechanisms for the formation of glucose from cellobiose in the
aqueous phase and in the presence of a supported noble metal catalyst:
(1) cleavage of the 1,4′-glycosidic bond between the two monomeric
units through hydrolysis to form 2 mol of glucose and (2) cleavage
of the glycosidic bond followed by hydrogenation to 1 mol of glucose
and 1 mol of dihydroxy-glucose.[31] In the
presence of γ-radiation, a mechanism for radical-induced cleavage
of the glycosidic bond was proposed by Von Sonntag et al.,[39] producing glucose isomers and various carbohydrate-derived
fragments.
Figure 1
Proposed degradation pathway from cellobiose to levoglucosan.
Proposed degradation pathway from cellobiose to levoglucosan.This study extends beyond the scope of previous
studies by integrating
on-line monitoring of the γ-radiation-enhanced degradation process.
Coupling this recently advanced approach to processes that have been
explored decades ago can allow researchers to completely reimagine
and advance these chemical processes. On-line monitoring provides
an in situ and real-time analysis of the chemical process, allowing
for more efficient research and development, as well as enabling real-time
control and quality assurance of deployed processes. On-line monitoring
also contributes to increased safety, particularly in complex and
dynamic systems such as hybrid nuclear reactors where both radiological
and chemical hazards must be monitored.[1,40−42]On-line monitoring of dynamic chemical systems allows for
the characterization
of complex solution chemistry in real-time.[43−46] Many approaches to the real-time
monitoring of biomass conversion have been successfully deployed using
a wide variety of techniques, including but not limited to amperometry,[47,48] calorimetry,[49] microbial growth,[50] and spectroscopy, which is further explored
here in the presence of γ-radiation.[51−56]Optical spectroscopy provides a uniquely powerful route for
on-line
monitoring that can identify and quantify a wide range of chemical
targets, their speciation, and their oxidation states, often utilizing
mature and commercially available technology.[57] Raman spectroscopy is a good example of this, where probes are physically
robust, resisting harsh chemical and radiation conditions.[58,59] Raman systems also require infrequent calibration, reducing the
interruption to experiments or exposure of workers to harsh conditions.[60] Raman spectroscopy utilizes vibrational approaches
that have been demonstrated as useful in previous work, providing
valuable insights into reaction parameters such as pH and analyte
concentration in both inorganic and organic systems.[43,46,61−67] Both infrared and Raman spectroscopy have been used successfully
in paper and pulp biomass analysis, including on-line monitoring as
summarized by Workman.[68]Here, Raman
spectroscopy is used to simultaneously monitor inorganic
and organic components of an oxidative reaction system for cellobiose,
with hydrogen peroxide as the oxidant. Both hydrogen peroxide and
cellobiose are Raman active molecules.[64,65,68−71] Raman spectroscopy has been used successfully to
monitor biomass treatment in real-time,[51−55] including in a hydrogen peroxide solution.[54] By developing and utilizing chemometric modeling,
on-line monitoring analysis is further advanced. The chemometrics
approach can significantly enhance the accurate analysis of optical
data and allow for automated conversion of data into quantitative
information.[66,72−74] Chemometric
modeling of spectroscopic data has been successfully applied to the
analysis of biomass such as lignin, cellulose, and pulp products,
reducing the reliance on slow and costly off-line analyses.[20,75] Here, partial least squares (PLS) chemometric models are built using
Raman spectra for the measurement of two species in a solution, tracking
the change in analyte concentration during an ongoing irradiation
of cellobiose, a model lignocellulose system. Overall, this provides
powerful insights into the radiation-enhanced chemical process and
lays the foundation for advancing the use of radiation as an energy
commodity.
Results and Discussion
Cellobiose was
chosen as the model lignocellulose system. Exposure
to hydrogen peroxide simulated an oxidative reaction for the cellobiose. 60Co provided γ-radiation so that the chemical changes
could be studied in a nonreactor system, providing insights into potential
future applications for hybrid nuclear reactors.[12] Two irradiations were conducted on solutions of 0.292 to
0.294 M cellobiose in 1.63 M hydrogen peroxide. Grab samples were
collected during the first irradiation and analyzed offline using
Raman spectroscopy and high-performance liquid chromatography (HPLC).
The second irradiation featured in situ Raman spectroscopy as well
as grab sample analysis by HPLC.
Initial System Characterization
Using Grab
Samples
An initial run was conducted with 0.292 M cellobiose
in 1.63 M hydrogen peroxide inside a stainless-steel vessel, shown
in Figure A. A 60Co source was positioned in front of the reaction vessels,
shown in Figure B,
creating the irradiation field. The dose rate applied to the samples
was 8.0 to 23.0 krad/h over the course of irradiation, with a total
dose delivered to the samples of 5.59 Mrads. Grab samples were acquired
throughout the exposure during scheduled down-times for the source,
for a total of 8 samples, and Raman spectra were taken for each sample.
The dose received by each grab sample is listed in Table .
Figure 2
(A) Stainless-steel reaction
vessels used during irradiation studies
with a 1/4 in. in diameter Raman probe and a foam spacer. (B) Position
of the reaction vessels in proximity to the gamma source within the
γ-irradiator facility. (C) Cuvette holder used in the collection
of grab sample spectra.
Table 1
Accumulated
Dose of Grab Samples of
Cellobiose in Hydrogen Peroxide Taken during Two Separate Irradiations
irradiation
with off-line monitoring
irradiation
with on-line monitoring
grab sample
duration (h)
cumulative
dose (Mrad)
grab sample
duration (h)
cumulative
dose (Mrad)
1
0.0
0.00
1
0.0
0.00
2
18.0
1.44 × 10–4
2
20.9
3.13 × 10–1
3
62.6
9.57 × 10–1
3
41.7
6.25 × 10–1
4
104.2
1.91
4
66.0
9.90 × 10–1
5
130.0
2.51
5
111.9
1.68
6
155.6
3.10
6
137.9
2.07
7
222.5
4.63
7
164.8
2.47
8
264.7
5.59
(A) Stainless-steel reaction
vessels used during irradiation studies
with a 1/4 in. in diameter Raman probe and a foam spacer. (B) Position
of the reaction vessels in proximity to the gamma source within the
γ-irradiator facility. (C) Cuvette holder used in the collection
of grab sample spectra.Each grab sample was centrifuged, and the
supernatant was transferred
to a 10 mm pathlength quartz cuvette, with a Raman probe secured orthogonally
to the cuvette face. A schematic of the spectral collection setup
is shown in Figure C, depicting the location of the sample cuvette to the Raman probe.
Spectra were collected with an integration time of 5 s, with 30 spectra
collected for each sample. The integration time was selected to acquire
an appreciable signal for low-intensity peaks, such as the peroxide
peak. The spectra were averaged into a single spectrum in order to
reduce noise and reveal low-intensity peaks.Figure A shows
the spectral response of the primary peroxide band, while Figure B shows the most
prominent cellobiose band. The peroxide response peak at 876 cm–1, belonging to the ν3 O–O
stretching, decreases as the dose increases, indicating the consumption
of hydrogen peroxide during the reaction.[69,70] Similarly, the C–H and CH2 stretching band near
2898 cm–1 also decreases, indicating the degradation
of cellobiose.[64,65,76] Overall, this initial scoping study built confidence into chosen
chemical constituents and concentration ranges of the training set.
It also confirmed that fluorescent degradation products (e.g., hydroxymethyl
furfural) were not present in detectable amounts.
Figure 3
Preprocessed Raman spectra
of grab samples from an irradiation
of cellobiose in hydrogen peroxide, highlighting the regions for (A)
hydrogen peroxide and (B) cellobiose.
Preprocessed Raman spectra
of grab samples from an irradiation
of cellobiose in hydrogen peroxide, highlighting the regions for (A)
hydrogen peroxide and (B) cellobiose.In addition to interrogating the grab samples by Raman spectroscopy,
the samples were analyzed via HPLC to identify the major degradation
products. The chromatograms in Figure show the evolution of peaks with increasing dosage.
Four peaks were easily identified, and single component chromatograms
are shown in Figure S1. The main peak,
eluting at 5.7 min, was assigned to cellobiose, while the peak at
6.7 min was assigned to glucose, the monomer of cellobiose. The peak
at 9.6 min was assigned to levoglucosan (1,6-anhydroglucose), while
the peak at 10.05 min was identified as formic acid.
Figure 4
HPLC chromatograms of
grab samples at various dose rates.
HPLC chromatograms of
grab samples at various dose rates.The first chromatogram (labeled 0) shows the presence of small
peaks aside from cellobiose. This observation may be due to impurities
in the starting cellobiose (purity = >98%) or preliminary reactions
in the presence of the hydrogen peroxide that occurred during the
time between the offline HPLC analysis and the actual sampling. Notwithstanding
these considerations, the presence of cellobiose at all dose levels
suggests that a substantial portion of the reactant remained unreacted.
The presence of dissolved O2, which was shown to suppress
the homolytic cleavage of disaccharides, likely contributed to the
incomplete conversion.[77] However, as shown
in Figure , it is
obvious that a higher amount of radiation caused an increased conversion
of cellobiose. The second-order curve shows a good fit, with R2 = 0.994. All the calculated cellobiose conversion
points were found within the 95% confidence band of the fit. While
the temperature was not logged during ongoing irradiations, the low
sample concentration and narrow stainless-steel vessel design were
expected to allow for the efficient dissipation of heat such that
the sample remained at ambient temperature during irradiation.
Figure 5
Conversion
of cellobiose as a function of dose in grab samples.
Conversion
of cellobiose as a function of dose in grab samples.Glucose is the second most abundant compound present in the
samples.
It is formed by the hydrolysis of the β-O-4 bonds in cellobiose
(Figure ). The amount
of glucose, levoglucosan, and formic acid increased as the dose was
increased. It must be noted that levoglucosan and formic acid compounds
were not identified in cellobiose radiolysis studies in the absence
of hydrogen peroxide.[39,77]
Building
the Training Set
With Raman
and HPLC analyses of grab samples revealing clear changes in the system
in response to increasing dose, a training set was created to enable
on-line monitoring during an ongoing irradiation via the creation
of chemometric models.While on-line monitoring data was collected
in situ during irradiation, training set standards were generated
under controlled conditions in the laboratory. Training set samples
were designed to capture the spectral fingerprints of products and
reactants from the radiation-enhanced degradation, as identified in
the grab samples by HPLC and Raman spectroscopy analyses. The training
set consisted of samples of hydrogen peroxide ranging from 0 to 1.80
M, cellobiose ranging from 0 to 0.327 M, and combinations thereof.
Samples containing the degradation products included 0.0100 to 0.0500
M levoglucosan and 0.0500 to 0.288 M glucose. These concentration
ranges were chosen to encompass all expected concentrations of reactants
and products of interest that would be encountered during the on-line
monitoring. Initially, hydroxymethyl furfural was included as an anticipated
product of the cellobiose decomposition with peroxide, but it was
not observed in irradiation experiments and was ultimately not included
within the final training set. For each sample, 50 spectra were collected
at a 10 s integration time with the 1/4 in. Raman probe immersed in
the solution in a stainless-steel vessel to match the setup used during
irradiations is shown in Figure A. The integration time was increased relative to the
grab sample set due to the use of a different probe. Additional spectra
were collected to produce low-noise, averaged spectra that resulted
in improved chemometric model statistics. Figure A shows the major bands in Raman spectra
of cellobiose solutions, including the O–H stretching, which
is primarily from water. Figure B shows the response of the O–O stretching of
hydrogen peroxide, and Figure C shows the C–H stretching from cellobiose.
Figure 6
(A) Spectra
of mixtures of hydrogen peroxide and cellobiose in
deionized (DI) water showing the relative positions of the bands associated
with the hydrogen peroxide, cellobiose, and water O–H region;
(B) expanded region (650–1000 cm–1) showing
spectra of variable hydrogen peroxide concentrations; and (C) expanded
region (1500–4200 cm–1) showing spectra of
variable cellobiose concentrations.
(A) Spectra
of mixtures of hydrogen peroxide and cellobiose in
deionized (DI) water showing the relative positions of the bands associated
with the hydrogen peroxide, cellobiose, and water O–H region;
(B) expanded region (650–1000 cm–1) showing
spectra of variable hydrogen peroxide concentrations; and (C) expanded
region (1500–4200 cm–1) showing spectra of
variable cellobiose concentrations.
On-Line Monitoring of the Irradiation-Enhanced
Process
A second series of irradiations were completed with
a monitoring probe in place, acquiring spectra in real-time during
an irradiation. Two samples of ∼0.293 M cellobiose in 1.63
M hydrogen peroxide were simultaneously irradiated in separate stainless-steel
vessels at a rate of 15.0 krad/h for a total dose of 2.47 Mrads. The
setup was optimized to enable grab sample verification of the chemical
reaction without interrupting continuous on-line monitoring. Grab
samples were collected from the first vessel, containing 0.292 M cellobiose,
throughout the irradiation, for a total of 7 samples. The 1/4 in.
Raman probe was placed in the second vessel containing 0.294 M cellobiose
in order to collect spectra in situ throughout the irradiation. The
spectra were collected with an integration time of 10 s (to match
the training set integration time), and there was a delay of 10 to
30 s in between the spectral collection.Figure S3 presents the Raman spectra collected over the course
of the irradiation, focusing on the hydrogen peroxide and cellobiose
fingerprint regions. Cosmic rays and baseline drift, caused by bubble
formation on the Raman probe window, can be seen. The effect of these
interferences is discussed further below.
Chemometric
Modeling of In Situ Spectral Data
PLS models were built from
the training set spectra. Individual
models were built to quantify both peroxide and cellobiose. The spectra
included in the training set were preprocessed in order to account
for laser power fluctuation and other physical interferences. The
preprocessing of the spectral data consisted of the following: a first-derivative
using a 15 point cubic Savitzky–Golay smoothing of each spectrum,[78] normalization of all spectral intensities based
on the integrated area under the water band (3030 to 3310 cm–1 region), and mean centering of the data. Cross-validation was performed
using the venetian blinds method. The Savitsky–Golay filter
reduces instrument noise and cosmic ray peaks while also reducing
the signal of broad baseline features. The normalization accounts
for fluctuation in the laser power and alterations to the light path,
as discussed in detail below.The parity plot of the peroxide
model, shown in Figure A, demonstrates a linear relationship (R2 = 0.999) between the known solution concentration and the concentration
of the training set solutions as measured by the model. The root-mean-square
error of cross-validation (RMSECV), which can be considered an error
on the measurement, is 0.0258, which is very low relative to the starting
peroxide concentration of 1.63 M peroxide in the irradiated samples.
Similarly, the parity plot of the cellobiose model is shown in Figure B, providing a linear
fit with R2 = 0.999 and an RMSECV of 0.00272.
The low errors associated with the training set models’ cross-validation
indicate the model’s validity for use in measuring the unknown
concentrations in an irradiated sample. The statistics and details
for model performance are listed in Table .
Figure 7
Parity plots for PLS models for (A) hydrogen
peroxide and (B) cellobiose;
demonstrating a linear relationship (R2 = 0.999 and 0.9997, respectively) between the known and measured
results for each species.
Table 2
Statistics and Details for PLS Models
Created for the Training Set of Averaged Raman Spectra
analyte
RMSEC
RMSECV
R2 (cal, CV)
latent variables
spectral preprocessing
hydrogen
peroxide
0.0218
0.0258
0.9988,
0.9983
3
1st derivative; normalization
to water band; mean center
cellobiose
0.00206
0.00272
0.9997, 0.9995
2
1st derivative; normalization to water band;
mean center
Parity plots for PLS models for (A) hydrogen
peroxide and (B) cellobiose;
demonstrating a linear relationship (R2 = 0.999 and 0.9997, respectively) between the known and measured
results for each species.The PLS models described above were applied to the on-line Raman
spectral data of the irradiation. While training sets and initial
grab sample analyses indicated excellent potential for model performance,
a number of complicating factors were observed during the real-time
monitoring of the sample irradiation. Firstly, the probe was set in
the vessel such that the window face was horizontal. Bubbles formed
as a part of the chemical reaction and bubble collection on the probe
window periodically obscured solution interrogation. It is suspected
that this bubble formation reduced spectral intensity and altered
the ratios of analyte peaks. Furthermore, cosmic spikes were observed
likely due to stray radiation from nearby exposure facilities. These
spikes occur at random wavenumbers and often occurred directly on
or near an analyte peak, creating a high-intensity, false response
at wavenumbers of interest.[79] These spectra
are shown in Figure S3.In order
to reduce the impact of cosmic rays, the on-line run spectra
were averaged by 20. The dataset was otherwise preprocessed using
the same methods as the training set.To remove spectra that
were egregiously affected by the formation
of bubbles on the probe window and by the influence of cosmic rays,
a process of Q residual filtering was utilized. Q residuals are a form of metadata that can indicate whether
or not a spectral signature differs significantly from the spectra
captured in the training sets.[80] The Eigenvector
software used here outputs metadata and statistical analyses along
with results from applications of chemometric models. The resulting Q residuals observed after applying the hydrogen peroxide
and cellobiose models to the Raman data collected on-line during the
irradiation can be seen in Figure . The observed patterns in Q residuals
align with the theory that bubbles would periodically collect on the
windows and obscure Raman measurements, thereby increasing Q residuals. The pattern indicated the growth of bubbles
on the probe window and their migration off the window, which happened
through two processes: either the bubble grew large enough to migrate
off the probe on its own or the researcher paused the irradiation
briefly to tap the probe (dislodging bubbles) during the collection
of the grab sample from the first vessel. A cutoff was set to remove
results with a reduced Q residual greater than 5
× 10–3 because this data was compromised by
the presence of disturbances. The progression from raw spectra to
the Q residual filtered spectra can be seen in Figure S3. This process resulted in a matrix
of 138 averaged spectra for the peroxide model and 271 averaged spectra
for the cellobiose model. These spectra are pulled from throughout
the experiment’s duration, and they show a marked decrease
in cosmic rays directly interfering with the analyte bands, as shown
in Figure S3C,F. These factors indicate
that much of the variation in the concentrations measured by the model
arises from interferences such as bubble formation that occur throughout
the experiment and cosmic rays which cause temporally random false
readings by the model.
Figure 8
Q-residual values corresponding to the
hydrogen
peroxide and cellobiose data (displayed in Figure ), showing the effect of intermittent gas
bubble attachment and release at the optical probe tip.
Q-residual values corresponding to the
hydrogen
peroxide and cellobiose data (displayed in Figure ), showing the effect of intermittent gas
bubble attachment and release at the optical probe tip.
Figure 9
(A) On-line measurement of hydrogen peroxide during γ-irradiation
and (B) on-line and grab sample measurements of cellobiose during
irradiation experiments.
After preprocessing of the spectra and removal of compromised
spectra,
both peroxide and cellobiose were successfully measured using the
chemometric analysis. Figure A shows the measured value
of hydrogen peroxide by the model across the duration of the irradiation.
The negative slope aligns with the trend observed in the grab sample
and on-line run spectra, in which the peroxide response peak decreases
as the dose increases. Further evidence of model efficacy is seen
in Figure B, which
displays the model’s measurement of cellobiose as the irradiation
progresses. This plot displays the concentrations of cellobiose in
grab samples taken from the grab sample vessel during the ongoing
irradiation and measured off-line by HPLC analysis. An offset was
applied to the concentrations measured by the HPLC in order to standardize
the HPLC measurements to the known starting concentration of the solution
in the grab sample vessel before irradiation occurred. The final point
on this plot, shown in cyan blue, shows the HPLC measurement of the
solution in which the probe was immersed, demonstrating that the two
vessels compare favorably despite aliquots of solution being removed
from the grab sample vessel throughout the irradiation and the probe
vessel remaining undisturbed. The HPLC measurements show good agreement
with the line of best fit created by the chemometric model of Raman
spectra.(A) On-line measurement of hydrogen peroxide during γ-irradiation
and (B) on-line and grab sample measurements of cellobiose during
irradiation experiments.Overall, chemometric
PLS models constructed from spectra taken
on nonirradiated samples allowed for the measurement of peroxide and
cellobiose in situ during the course of the irradiation of cellobiose
in hydrogen peroxide. The models’ measurements are in good
agreement with the quantification performed using HPLC analysis. The
chemometric models successfully measured two major components of the
system: the oxidant, hydrogen peroxide and the source biomass, cellobiose.
Additional models could be constructed for Raman active degradation
products, such as levoglucosan or formic acid.[81]
Conclusions
Nuclear
energy reactors produce unused radiation that can be utilized
to drive chemical reactions. The coupling of a chemical plant of radiation-enhanced
chemical production alongside a nuclear reactor would create a hybrid
reactor with greater economic and environmental benefits than a nuclear
reactor alone. Here, chemometric modeling of the Raman spectra collected
during the on-line monitoring of the irradiation of cellobiose in
hydrogen peroxide provided quantitative information on inorganic and
organic compounds in the reaction solution. This work demonstrates
the ability of optical spectroscopic on-line monitoring to provide
valuable, quantitative, and real-time measurements of the radiation-enhanced
degradation. Such monitoring allows for more efficient chemical production,
as the chemical system can be optimized in response to the real-time
information provided by spectroscopic monitoring. Such on-line monitoring
also contributes to creating safer hybrid reactors. The exploration
of more complex biomass systems is warranted in order to provide support
for the construction of hybrid reactors in the future.
Experimental Section
Materials
Cellobiose
(>98%), hydrogen
peroxide (30% solution), and potential degradation products such as
levoglucosan, glucose, and hydroxymethylfurfural (HMF) were purchased
from Sigma–Aldrich (St. Louis, MO, USA).The irradiated
samples were composed of solutions of 0.292–0.294 M cellobiose
and 1.63 M hydrogen peroxide in 18 MΩ cm DI water.A set
of training solutions, used to build chemometric models,
was created. Samples were created to include the original analytes
and the expected degradation products that would be produced during
the irradiation. The samples contained hydrogen peroxide, cellobiose,
levoglucosan, HMF, and glucose in 18 MΩ cm DI water. This is
discussed further below.
High Exposure Facility
The samples
were irradiated in the High Exposure Facility (HEF) at the Pacific
Northwest National Laboratory. HEF is a gamma irradiation facility
that provides high-dose gamma irradiation with a variety of high-energy
gamma sources. The source employed in this work was 60Co
with a starting activity of 10,000 Ci. The stainless-steel vessels
and their position relative to the HEF exposure cone are shown in Figure B.
Equipment
Samples were analyzed using
HPLC equipped with a Waters 2414 refractive index detector. A Bio-Rad
Aminex HPX-87H ion exclusion column (300 mm × 7.8 mm) was used
for analyte separation. Sulfuric acid (0.005 M) was used as the eluent
at a flow rate of 0.55 mL/min. The eluent was filtered through a 0.2
μm filter and degassed. The calibration curves for each of the
known compounds contained five concentration levels ranging from 0.1
to 2.0 wt %. The R2 values were greater
than 0.99 for all of the reported analytes. Each calibration was verified
with an independently prepared standard run as the control. The recovery
of the calibration checks ranged from 93.6 to 108%. Acetic acid, methanol,
ethanol, acetone, and methylethylketone were selected as calibration
check compounds. The opening/closing continuing calibration verification
percent recoveries for these compounds were 94.8 to 102.8%. Curves
were plotted using OriginPro 2019b.Two Raman systems were utilized
in this work. Both were acquired from Spectra Solutions Inc. (Norwood,
MA, USA), each with a 671 nm excitation laser. Each system contained
a transmission VPH grating spectrograph with a thermoelectrically
cooled charge-coupled device detector to record the Raman signal from
the Raman probe over a spectral range of 200–3800 cm–1. The wavenumber reading for each spectrometer was calibrated using
naphthalene, and the resolution of each spectrometer was ∼5
cm–1.
Chemometric Analysis
Spectral preprocessing
was conducted using Matlab2019b (Mathworks, Natick, MA, USA), and
chemometric models were built using PLS Toolbox 8.7.1 (Eigenvector
Research Incorporated, Manson, WA, USA).
Authors: Amanda J Casella; Laura R H Ahlers; Emily L Campbell; Tatiana G Levitskaia; James M Peterson; Frances N Smith; Samuel A Bryan Journal: Anal Chem Date: 2015-04-30 Impact factor: 6.986
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