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1 osolids drying and the need for supplemental adsorbent.
2 build-up that reduces the useful life of the adsorbent.
3 the interaction strength between CO2 and the adsorbent.
4 ed with adsorbing and desorbing gas from the adsorbent.
5 tion of the n-components onto a fixed-bed of adsorbent.
6 ethylene glycol bis-mercaptoacetate as a new adsorbent.
7 the need to reduce the hygroscopicity of the adsorbent.
8 e as a nonporous, unfunctionalized reference adsorbent.
9 ion, and FT-IR were used to characterise the adsorbent.
10 t and environmental importance of this novel adsorbent.
11 m food samples using tea waste as a low cost adsorbent.
12 en soil organic matter (SOM) is the dominant adsorbent.
13 an adsorption capacity of 120 mg of CO2/g of adsorbent.
14  of copper with an integrated copper removal adsorbent.
15 dic conditions used to elute metals from the adsorbent.
16 titanium dioxide-based binding agent) as the adsorbent.
17 hane exclusion on silver-exchanged zeolite A adsorbent.
18 nsumption for activation and regeneration of adsorbents.
19  these respects as compared with traditional adsorbents.
20 and rationally design superior catalysts and adsorbents.
21 s can be achieved with micro and meso porous adsorbents.
22 f these industrially important catalysts and adsorbents.
23 o ensure valid comparisons between different adsorbents.
24 mensional (3D) porous graphene hydrogel (GH) adsorbents.
25 customize metal-organic frameworks (MOFs) as adsorbents.
26 anisms for developing high-performance CO(2) adsorbents.
27  those potentially offered by advanced solid adsorbents.
28  property that is matched by few microporous adsorbents.
29 rest in exploring high-performance solid CO2 adsorbents.
30  sites can influence the amine efficiency of adsorbents.
31 ethods motivate efforts to develop effective adsorbents.
32 SPEDA, and AMPTS, respectively, were used as adsorbents.
33 ometry observed in most amine-functionalized adsorbents.
34 e areas, and potential applications as novel adsorbents.
35 sted metal ions than the Al(2)O(3) and Au NP adsorbents.
36 demonstrate the versatility of beta-CD-based adsorbents.
37  decrease ammonium adsorption for any of the adsorbents.
38 obtained because of the bleaching ability of adsorbents.
39 ial in catalysis, and as supercapacitors and adsorbents.
40  chemical industry as selective catalysts or adsorbents.
41 industrial processes, mostly as catalysts or adsorbents.
42 commercial processes, mostly as catalysts or adsorbents.
43 m energy needed to completely regenerate the adsorbent (100% desorption efficiency) using microwave r
44 much higher than that of currently available adsorbents (5-280 mg/g, generally less than 100 mg/g).
45 ications, it is essential to understand both adsorbent-adsorbate and adsorbate-adsorbate interactions
46 termine the adsorption isotherms for a given adsorbent-adsorbate interaction at temperature/pressure
47 breakthrough time and adsorption capacity of adsorbents/adsorbates with different dielectric properti
48 he extraction processes including: amount of adsorbent, adsorption and desorption times, type and vol
49 ration optimizations including pH, dosage of adsorbent, adsorption-desorption time, concentration and
50 is more than 340% higher than the industrial adsorbent Ag(0)@MOR under identical conditions.
51                          The Au NP-Al(2)O(3) adsorbent allows effective removal of mercury species sp
52 osan could be collected using the PXP or PUF adsorbent alone, with low breakthrough; however, the rec
53 -II)-As(III) complexes on a sulfhydryl model adsorbent (Ambersep GT74 resin) in the absence and prese
54 ficiency, including sample pH, contact time, adsorbent amount, and sample volume were studied and opt
55                   Different factors (the pH, adsorbent amount, contact time, type of eluent, matrix a
56 ration of mercury ions by an Au NP-Al(2)O(3) adsorbent, analysis of mercury ions down to the subppq l
57 analyze the interaction strength between the adsorbent and adsorbate, and adsorption site heterogenei
58    Conformational flexure and both adsorbate/adsorbent and intermolecular interactions can be identif
59  horizontal lineC of pretreated barley straw adsorbent and pi* carbon atom in benzene ring attached t
60 ssed onto a cartridge containing 500mg XAD-2 adsorbent and re-extracted for GC analysis.
61 procedure, due to most efficient solid-phase adsorbent and results in high sensitive quantification.
62 lue for a DSSC employing N719 dye without co-adsorbents and a nonvolatile electrolyte.
63 orous semiconductors or metals and potential adsorbents and catalysts in which chemistry and metal-in
64 tcombustion CO2 capture processes with solid adsorbents and discusses a variety of carbon-based mater
65  polar functional groups) behave like apolar adsorbents and exhibit very interesting and unexpected m
66 te the first application of GNs as potential adsorbents and functionalized meso-silica for use in rem
67 akes them promising candidates for efficient adsorbents and host-guest applications.
68 talysts, chromatographic supports, selective adsorbents and light-harvesting devices, have clearly sh
69 artz fiber filters followed by PUF/XAD-4/PUF adsorbents and measured using gas chromatography-mass sp
70 h they have already found uses as catalysts, adsorbents and membranes precise determination of their
71 developments in inorganic materials; polymer adsorbents and related research pertaining to amidoxime;
72 gnet, the recycling process of both the MGNC adsorbents and the adsorbed Cr(VI) is more energetically
73 nd its stability relative to other potential adsorbents and the selective nature of Tl(+) uptake by i
74 latest developments in ultra-microporous MOF adsorbents and their use as separating agents via thermo
75 made from pure chemicals (113 mg of CO2/g of adsorbent) and TEPA-MCM-41(AF) made from alkaline fusion
76  or n-hexadecane (HD) phase by the water-wet adsorbent, and "delta" is an arbitrary divisor to conver
77 ing our everyday lives, namely as catalysts, adsorbents, and ion exchangers.
78                                        Those adsorbents are claimed to be the origin for optical prop
79             The review reveals that although adsorbents are considered to have great potential to red
80 cles 50-200 mum in diameter, Au NP-Al(2)O(3) adsorbents are easily prepared.
81                               Supramolecular adsorbents are expected to fully expose their abundant a
82 s may be the main reason primary amine based adsorbents are more effective under air capture conditio
83           Amidoxime-functionalized polymeric adsorbents are the current state-of-the-art materials fo
84  and 51.4 cm(3) (STP) cm(-3)) for a physical adsorbent at 400 ppm of CO2 and 298 K.
85  metal-organic frameworks also serve as good adsorbents at low temperatures.
86 as tested in various anoxic mixtures of both adsorbents at pH 7.0.
87 was studied employing a cost-effective novel adsorbent based on waste printed circuit boards.
88 ions of MOFs as materials for heat-pumps and adsorbent-based chillers and proton conductors are also
89 ogenic distillation to the energy-efficient, adsorbent-based separation and purification in the futur
90 ications of multilayer graphene as efficient adsorbent but also its possible environmental risk.
91 full CO2 desorption in conventional physical adsorbents but considerably lower than chemical sorbents
92                   CUS-MOFs behave like polar adsorbents but show the specificity of preferring alkene
93 stantial energetic benefits over traditional adsorbents, but few guidelines currently exist for the d
94 ften achieved using metal oxides as reactive adsorbents, but metal oxides perform poorly when subject
95  predicted to be efficient Xe/Kr solid-state adsorbents, but no experimental insights into the nature
96                   Furthermore, the resulting adsorbent can be recycled multiple times without loss of
97                                      Biochar adsorbents can cost less and sequester carbon; however,
98                  Additionally, we found that adsorbents can substantially impact phosphate sorption n
99 ontrol humidity by adsorbing water; however, adsorbents capable of the dual functionality of humidifi
100 ect of amphoteric Zr sites that enhances the adsorbent capacity, regenerability, and stability over c
101    Porous solids are important as membranes, adsorbents, catalysts, and in other chemical application
102                               Fe-zeolites as adsorbents/catalysts showed a good stability in both bat
103            Cation adsorption curves for four adsorbents (clinoptilolite, biochar, Dowex 50, and Dowex
104    The effects were studied of two different adsorbent combinations (com I; bentonite: activated carb
105 nism of selenite adsorption by the new mixed adsorbent composed of a few (amorphous and crystalline)
106 icacy together with stability of these novel adsorbents composed of both primary and/or secondary ami
107                               Carbon dioxide adsorbents, constituted by organofunctionalized magnesiu
108 riments to be a promising technique for fast adsorbent cooling and can be crucial to leverage the ful
109 uperior arsenic uptake performance of UiO-66 adsorbent could be attributed to the highly porous cryst
110 y, high capture efficiency and low cost, the adsorbent demonstrates promise for industrial radioactiv
111  as the pH value, adsorption time, amount of adsorbent, desorption conditions (type, concentration an
112 action and cleanup via silica-based magnetic adsorbent dispersion in milk samples followed by the mag
113 periments indicate that, in contrast to many adsorbents, dmpn-Mg2(dobpdc) captures CO2 effectively in
114 Unique to members of this promising class of adsorbents, dmpn-Mg2(dobpdc) displays facile step-shaped
115            Performance parameters (time, pH, adsorbent dosage and initial ion concentrations) effecti
116  as pH value, initial arsenic concentration, adsorbent dosage, contact time and ionic strength, on th
117 tion of all 32 solutes on the four different adsorbents: (Ea - EH) = 24.7 x V + 9.7 x S - 19.3 (R(2)
118                 The complexity of the porous adsorbent, especially the presence of the amorphous phas
119 mer has superior function as a selective gas adsorbent, even though its constituent monomers are very
120            At the same time, the nanolaminar adsorbent exhibits prompt adsorption kinetics, high adso
121 e retainers were used instead of more common adsorbent filter papers.
122 fluences of parameters such as pH, amount of adsorbent, flow rates and sample volumes were investigat
123                             XAFS analysis of adsorbents following deployment in environmental seawate
124 les (MHAMS-MIONPs) were used as an efficient adsorbent for both removal and preconcentration of two i
125 by FTIR, SEM and elemental analysis and used adsorbent for column solid phase extraction of selenium
126              Results showed that the optimum adsorbent for D4 is a wood-based chemically activated ca
127 positions NbOFFIVE-1-Ni as the new benchmark adsorbent for direct air capture and CO2 removal from co
128 ro-waste OTS could be utilized as a low-cost adsorbent for efficient dye removal, and fungal treatmen
129 s hydrolytically stable MOF as a prospective adsorbent for humidity control in confined spaces, such
130               The adsorption capacity of the adsorbent for lead was found to be 73mgg(-1).
131 (dried/milled) bauxite ore as an inexpensive adsorbent for remediating fluoride-contaminated groundwa
132 ts, which can be considered as an attractive adsorbent for separation of CO2 from flue gas.
133 e bond with iminodiacetic acid (IDA)), as an adsorbent for the chromatographic process to capture lac
134  results we are able to propose an optimized adsorbent for the deep and selective removal of nitrogen
135 um dots (Fe3O4@Chi-GQDs) nanocomposite as an adsorbent for the preconcentration of Cu(II) in Thai foo
136      This work shows that GFH is a promising adsorbent for the removal and recovery of NTMP antiscala
137 iethanol amine (PHB-DEA) polymer was used as adsorbent for the sensitive and selective separation, pr
138  adsorbent was used for the first time as an adsorbent for the vortex assisted-solid phase extraction
139 ortant features that make NU-1000 a superior adsorbent for this application.
140  results suggest that illite is an important adsorbent for Tl in soils and sediments, considering its
141  and used for the first time as an effective adsorbent for vortex-assisted separation and preconcentr
142 orage applications, for instance, as methane adsorbents for a vehicular natural gas tank or other por
143 ighlights their potential as next-generation adsorbents for a wide array of CO2 separations.
144 of these materials render them promising new adsorbents for air separation processes.
145 nanoparticles (MNPs) are promising and novel adsorbents for As removal because of their great adsorpt
146 r dmpn-Mg2(dobpdc) one of the most promising adsorbents for carbon capture applications.
147 orks) and noncarbonaceous (inorganic) porous adsorbents for CO2 adsorption at different process condi
148  hence to the development of efficient amine adsorbents for CO2 capture from flue gas and ambient air
149  mesoporous silica are effective, reversible adsorbents for CO2, both from flue gas and in direct air
150 cation of safe and highly efficient GO-based adsorbents for dye or other organic pollutants in a wide
151  meso-silica materials (MCM-41 or SBA-15) as adsorbents for formaldehyde (H(2)CO) vapor from contamin
152 -Donawitz steel making plants were tested as adsorbents for H(2)S removal at room temperature (298 K)
153 tic framework for designing highly efficient adsorbents for removing CO2 from various gas mixtures, a
154 -1,3-benzenedicarboxylate) were evaluated as adsorbents for separating olefins from paraffins.
155 functional porous materials to be adopted as adsorbents for the effective and energy-efficient separa
156  the possibility of using these compounds as adsorbents for the purification of unrefined vegetable o
157 s demonstrate that GH granules are promising adsorbents for the removal of antibiotic pollutants from
158 ared nanocomposites were studied as magnetic adsorbents for the removal of lead (cationic) and chromi
159           Several zeolites were evaluated as adsorbents for the removal of MTBE from water in a scree
160 ind V, the cyclic imide-dioxime group of the adsorbent forms a peculiar non-oxido V(5+) complex, exhi
161                 Two binding sites within the adsorbent framework are proposed for arsenic species, i.
162  many interesting fundamental insights, only adsorbents functionalized with alkylamines are shown to
163                    The as-synthesized UiO-66 adsorbent functions excellently across a broad pH range
164        Adsorption on a biochar and reference adsorbent graphite was conducted of triazine herbicides,
165 > metal Rydberg-like orbital, along with the adsorbent --> sigma*(H2) contribution, can contribute fr
166                          The Au NP-Al(2)O(3) adsorbent has a higher affinity for mercury species and
167                                    The Au NP adsorbent has a higher binding affinity (dissociation co
168 und to a octadecyl silica resin (C-18) as an adsorbent has been developed that allows for dilute HCl
169 ficiency along with stability of these novel adsorbents has also been demonstrated by their repetitiv
170 ide support in these polymer/oxide composite adsorbents has been largely overlooked and that the prop
171 ndency to form stronger interactions with an adsorbent have larger Ea and EH.
172 graphene oxide (GO) has been suggested as an adsorbent; however, a support is desirable to ensure a h
173  could act as both selective and cooperative adsorbents if guest binding at one site were to trigger
174 erformance proves the high stability of this adsorbent in an acidic, aqueous environment.
175 xysilane (TEOS-MTMOS) was used as a clean-up adsorbent in magnetic solid phase extraction (MSPE) for
176 itions were immersing 100mg of Carboxen 1000 adsorbent in the MAE extract.
177 ven to noncarbonaceous micro and meso porous adsorbents in chemical looping combustion involving insi
178 mesoporous silica-supported amine-containing adsorbents in the presence of carbon dioxide under dry c
179 propylene from propane relative to any known adsorbent, including para-functionalized structural isom
180 butions of the overall or specific adsorbate-adsorbent interactions to the adsorption.
181 Injection of powdered activated carbon (PAC) adsorbents into the flue gas of coal fired power plants
182                                          The adsorbent is fully regenerable, using oxalate solution.
183                   Therefore, the use of such adsorbents is recommended for poultry processing.
184 = 0.3 nM) for Hg(2+) ions than the Al(2)O(3) adsorbent (K(d) = 52.9 nM).
185 the presence of thrombin, the aptamer on the adsorbent layer captures the target on the electrode int
186 ed with porous, high surface area monolithic adsorbents (MAds).
187 propylene, respectively, indicate that these adsorbents maintain sufficient reversibility under mild
188                As strong naturally occurring adsorbents, manganese oxides may significantly influence
189       This chelating resin was used as a new adsorbent material for determination of Cd(II), Co(II),
190 tomaceous earth by introducing a novel virus adsorbent material, magnesium oxyhydroxide, into the fil
191 n efficient cleaning and regeneration of the adsorbent material, this novel electro-Fenton approach c
192 erefore presents a new benchmark for mercury adsorbent materials and provides a new perspective for r
193 ndritic architectures supported in silica as adsorbent materials for direct CO2 capture from air.
194    Activated carbons are the most widespread adsorbent materials used to remove organic pollutants fr
195 ted carbons and non-porous beta-cyclodextrin adsorbent materials.
196  content decreased resulting from the use of adsorbent materials.
197                                     The SENT adsorbent may be readily regenerated under mild conditio
198 r (Chelex-100 and the titanium dioxide based adsorbent Metsorb) is described for the simultaneous mea
199                                 Conventional adsorbents, namely zeolites and silica gel, are often us
200 ed water was done by pretreated barley straw adsorbent obtained from raw barley straw after modificat
201  provides sufficient functionality to enable adsorbent of heavy metals (Cd(2+), Co(2+), Cu(2+), Hg(2+
202  contact with alcoholic solutions acts as an adsorbent of trace elements (Cu and Pb) while releasing
203 ad in natural and engineered systems, potent adsorbents of contaminants and a source of energy for ir
204 aterials-HT, HS, and COGF-serve as efficient adsorbents of iodine due to the presence of the cationic
205 porous beta-cyclodextrin polymers (P-CDP) as adsorbents of MPs in aquatic matrixes.
206     Metal-organic frameworks are nano-porous adsorbents of relevance to gas separation and catalysis,
207                                 Solid porous adsorbents offer major benefits, such as lower energy pe
208 d and fractionated chromatographically using adsorbent or ionic resins.
209 mission spectroscopy directly applied on the adsorbent or, with higher resolution, by indirect nanopl
210                                        A new adsorbent, polyhydroxybutyrate-b-polyethyleneglycol, was
211 on of PF Plus, the new pediatric medium with adsorbent polymeric beads, versus the charcoal-containin
212                                  Analyses of adsorbent pore size distribution and surface chemistry c
213 ing sites, R-SH and identical withFeOH, both adsorbents possessed nearly identical affinities for As(
214 hallenge to fundamental materials design, as adsorbent properties can be altered to achieve selective
215                 Effects of the adsorbate and adsorbent properties on Ea or EH then emerge that are un
216 ounds in soil, yet the effects of solute and adsorbent properties on sorption are poorly understood.
217  efficiency and showing stable adsorbate and adsorbent properties, this paper suggests that microwave
218                          The Au NP-Al(2)O(3) adsorbent provides a synergic effect and, thus, is effec
219 solution and/or because the tested adsorbate:adsorbent ratios are not varied sufficiently.
220          Albumin dialysis with the Molecular Adsorbent Recirculating System (MARS) (Gambro, Lund, Swe
221          Albumin dialysis with the molecular adsorbent recirculating system (MARS) decreases retained
222  or standard medical treatment and molecular adsorbent recirculating system (n = 47) at the Universit
223 mortality rate was observed in the molecular adsorbent recirculating system group (9.5% vs 50.0% with
224 rm mortality (up to day 14) of the molecular adsorbent recirculating system group was significantly r
225 ected organ system, this effect of molecular adsorbent recirculating system on mortality was particul
226                                    Molecular adsorbent recirculating system therapy has demonstrated
227    Among these high-risk patients, molecular adsorbent recirculating system treatment might bridge to
228                                    Molecular adsorbent recirculating system treatment was associated
229  or standard medical treatment and molecular adsorbent recirculating system.
230     Standard medical treatment and molecular adsorbent recirculating system.
231 iver support system as well as the Molecular Adsorbent Recycling System (MARS) in an ischemic porcine
232 s of the nanohybrids for easy separation and adsorbent recycling.
233 technologies, with the choice of M dictating adsorbent regeneration energy and the level of purity of
234     These data highlight advantages of P-CDP adsorbents relevant to MP removal during water and waste
235 erein, a novel class of high-performance CO2 adsorbent (rGO@MgO/C) is engineered based on the control
236 chromatography/mass spectrometry analysis of adsorbent samples collected from a constant volume sampl
237   We also used Al(2)O(3) and Au NP-Al(2)O(3) adsorbents sequentially for selectively removing Hg(2+)
238           This metal-organic framework-based adsorbent shows very high selectivity toward uranium, as
239  of proteins with individual chromatographic adsorbent sites is available only via inference from ens
240  a technological point of view, unlike solid adsorbents slurries can flow and be pumped.
241 nt challenge due to the drawbacks of current adsorbents such as low uptake capacity, high cost, and n
242 scussion is presented on new developments in adsorbents, such as ionic liquids, metal oxides, metals,
243                                 Unlike polar adsorbents, such as zeolite 13x and the metal-organic fr
244 rategy for designing efficient and selective adsorbents suitable for various separations.
245 gen bond (-CAHB) between ionized solutes and adsorbent surface groups as the possible adsorption mech
246 ase pH value near the pI of the zwitterionic adsorbent surface leads to full recovery of all plasmid
247 h can describe the order and disorder of the adsorbent surface.
248 s adsorption of the organic component on the adsorbent surface.
249 o extensively adsorb onto positively charged adsorbent surfaces, virus adsorption in such systems in
250 ed methodology, the crucial issue is a novel adsorbent synthesized by grafting 3-mercaptopropyl trime
251 es and soil amendments (biochars) are strong adsorbents that can impact the fate of organic compounds
252 separation processes can be lowered by using adsorbents that discriminate molecules based on adsorpti
253 s representative of the broad range of solid adsorbents that have received attention for CO2 capture.
254 wered through development of selective solid adsorbents that operate at higher temperatures.
255  to other primary amine-functionalized solid adsorbents that uptake CO2 primarily as ammonium carbama
256                                As a flue gas adsorbent, the regeneration energy was estimated through
257 onal layer of dye molecules on the exhausted adsorbent through interlayer attractive forces.
258 hesized and for the first time applied as an adsorbent to remove aquatic arsenic contamination.
259 d potassium niobate (K4Nb6O17) nanolamina as adsorbent to remove toxic Sr(2+), Ba(2+) and Cs(+) catio
260   Surprisingly, it is found that CT from the adsorbent to the sigma*(H2) orbital is present in all st
261 rameworks could potentially be used as solid adsorbents to replace current cryogenic distillation tec
262 rom these results can be leveraged to tailor adsorbents to the conditions of a given CO2 separation p
263 does not require sophisticated cold traps or adsorbent traps, and allows collecting large numbers of
264 sence of ferrihydrite as a competing mineral adsorbent under reducing conditions and tested their sta
265 ade from alkaline fusion (112 mg of CO2/g of adsorbent) under the same testing conditions.
266     For mixture separations with microporous adsorbents, uphill diffusion can cause supra-equilibrium
267 -phase extraction (SPE) with Amberlite XAD-2 adsorbent used as stationary phase for determining phtha
268 d in hydroxylamine-treated polyacrylonitrile adsorbents used in the extraction of uranium from seawat
269 mass spectra were directly recorded from the adsorbent using the Direct Analysis in Real Time interfa
270 e atmospheric CO2 adsorption by amine-loaded adsorbents using an easy handling and low-cost benchtop
271 n (BAC, microwave-absorbing) and a polymeric adsorbent (V503, microwave transparent) were completely
272 nFe2O4 and magnetic takovite-aluminosilicate adsorbent via precipitation methodology.
273             The desorption of As(V) from the adsorbent was 17% when using 30% HCl and 85% with 1M NaO
274       The maximum adsorption capacity of the adsorbent was calculated to be 69.9mgg(-1).
275 dependence of As(III) binding to the organic adsorbent was developed.
276                     The maximum capacity the adsorbent was found to be 89.1 (+/-1.7) mug, 57.2 (+/-1.
277       The maximum adsorption capacity of the adsorbent was found to be about 350mgg(-1).
278                     Results showed that used adsorbent was quite effective in removing Pb(II) from dr
279                              Isobutane-laden adsorbent was then heated with resistance control.
280                                         This adsorbent was used for the first time as an adsorbent fo
281 surface, and magnetic characteristics of the adsorbent were investigated by XRD, EDX, FE-SEM, and VSM
282  of adsorption of previously uncharacterized adsorbents were estimated as a function of both uptake a
283 ylsilane and tetramethylorthosilicate; these adsorbents were evaluated for sulphonamides retention in
284 riations in the dielectric properties of the adsorbents were monitored using two microwave parameters
285       Three different magnetic phenyl silica adsorbents were synthesized by varying the molar ratio o
286                                        Novel adsorbents, wheat bran (WB) and modified wheat bran (M-W
287 mol Pb, and 2.0 mmol Zn per each gram of the adsorbent which are significantly higher values than its
288 enzene (AZ)-based silica-supported polymeric adsorbent which can simultaneously remove both PAHs and
289 ensity in diffuse reflectance spectra of the adsorbent, which was used for their direct determination
290 ol/g (10.2 wt %) at 298 K) compared to other adsorbents, which can be considered as an attractive ads
291  energy over CT complexes on various organic adsorbents, which show only moderate exothermic heats of
292 cities than have been achieved for classical adsorbents, while also reducing the amount of heat relea
293 TMOS is reusable up to 7 times as a clean-up adsorbent with good recovery (>85%).
294  could be an affordable fluoride-remediation adsorbent with the potential to improve access to drinki
295 sent a rapidly expanding new class of porous adsorbents with a large range of possibilities for desig
296 se moving constituents and engineer improved adsorbents with intrinsic thermal management for pressur
297             Here, we show that Zn-Ti-O-based adsorbents with nanofibrous morphology can sustain their
298 evelopment of a new class of engineered foam adsorbents with the potential to revolutionize water tre
299 anic frameworks can behave as 'phase-change' adsorbents, with unusual step-shaped CO2 adsorption isot
300  is generally applicable to most crystalline adsorbents, yielding information on distribution ratios

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