ライフサイエンスコーパス: sorbent

1 om high salt water (HSW) simulant (54 mg U/g sorbent).

2 tes that frequently escape detection (water, sorbents).

3 xygenated compounds were retained on the PPL sorbent.

4 drich-humic acid (AHA) utilized as reference sorbent.

5 atter, and not n-hexane, was adsorbed by the sorbent.

6 e, primary secondary amine sorbent, and C-18 sorbent.

7 olid phase extraction (SPE) with a polymeric sorbent.

8 eference mixes) and three with the CaL spent sorbent.

9 in predicting the colloidal stability of the sorbent.

10 ecyl bonded silica (C18), as the clean-up co-sorbent.

11 matter was predicted to be the dominant soil sorbent.

12 c, Ca-based, calcium aluminate supported CO2 sorbent.

13 mide, as an efficient solid-phase extraction sorbent.

14 ing on the extraction selectivity of the PPL sorbent.

15 pH-dependent speciation of both sorbate and sorbent.

16 their potential usefulness as catalysts and sorbents.

17 orbents but considerably lower than chemical sorbents.

18 ase performed superior compared to ten other sorbents.

19 s (MOFs), as the primary classes of chemical sorbents.

20 driving forces in DNA extraction by the PIL sorbents.

21 es of ionic strength or metal-loading on the sorbents.

22 rks (MOFs) into a series of porous inorganic sorbents.

23 the properties of the dissolved ligands and sorbents.

24 nergy input that is required for traditional sorbents.

25 o efficient extract clean-up with ZrO2-based sorbents.

26 ore efficient for CO2 capture than PEI-based sorbents.

27 ) and primary-secondary amine (PSA, 25mg) as sorbents.

28 the interaction of CO2 with the solid-amine sorbent, 3-aminopropyl silane (APS), bound to mesoporous

29 uptake of the pellets was 0.29 g of CO2/g of sorbent, a value that is 45% higher than that measured f

30 es containing neutral, anionic, and cationic sorbents able to trap several pollutants classes like ph

31 e of the best sorbent was 0.33 g of CO2/g of sorbent (after 10 cycles).

32 Through magnetic force, the sorbent, after extraction, was isolated from the sample

33 investigated and developed with a practical sorbent-air contacting process in mind if society is to

34 actions of CH4 , C2 H6 , and CO2 , different sorbents allow for optimal H2 S removal and hydrocarbon

35 yma River basin with a use of three nonionic sorbents: Amberlite XAD-8 resin, PPL- and C18 - SPE cart

36 Sorbent amendment with activated carbon (AC) is a novel

37 including extraction pH, extraction time and sorbent amount were evaluated and optimized.

38 of several parameters such as pH, amount of sorbent and 1,10-phenanthroline, stirring time, concentr

39 e was constructed with a side hole above the sorbent and an extended tip that fits inside the restric

40 ieved by injecting a mixture solution of the sorbent and disperser solvent into the aqueous sample.

41 ree times 250muL samples through the MEPSPEP sorbent and elution with 100muL of 50% MeOH) were combin

42 d by solid-phase extraction with a C18 RP as sorbent and methanol as eluting solvent.

43 pture capacity of the original, powdered CO2 sorbent and the pelletized material.

44 The sample was dispersed on C18 silica sorbent and then the on-line MSPD-SPE-HPLC/FLD method wa

45 ction followed by clean-up with EMR-Lipid(R) sorbent and trichloracetic acid.

46 bents were also prepared from the commercial sorbents and analyzed.

47 amples are usually preconcentrated via solid sorbents and are then detected by gas chromatographic te

48 Various SPE sorbents and extraction protocols were evaluated, and fo

49 2 commonly occurs in the presence of mineral sorbents and organic matter (OM) in soils and sediments;

50 anganese (Mn) oxides are among the strongest sorbents and oxidants in environmental systems.

51 roperties of sol-gel derived microextraction sorbents and the hydrophilic property of the cellulose f

52 s magnesium sulfate, primary secondary amine sorbent, and C-18 sorbent.

53 icity and hydrophobicity, surface pKa of the sorbent, and chemical structure of the parent amine and

54 hetical processes for the deployment of such sorbents are discussed, as well as the limited array of

55 After mercury capture, these sorbents are disposed in landfill, and the stability of

56 or aminopolymer architecture, the PPI-based sorbents are found to be more efficient for CO2 capture

57 Lime-based sorbents are used for fuel- and flue-gas capture, thereb

58 , highly efficient, organic-inorganic hybrid sorbent as the extraction medium.

59 ater vapor interactions with the prehydrated sorbents, as compared with the sorbent samples in phenol

60 n the development of advanced carbon dioxide sorbents, as well as other nitrogen-functionalized syste

61 LISA-derived assay called enzyme-linked apta-sorbent assay (ELASA).

62 ossible by conventional enzyme-linked immuno-sorbent assay (ELISA) analysis.

63 ng a complete IFN-gamma enzyme-linked immune-sorbent assay (ELISA) onto a commercial PCB electrochemi

64 idated independently by enzyme-linked immuno sorbent assay (ELISA) tests.

65 ties were determined in enzyme linked immune sorbent assay on immobilized integrins, using fibronecti

66 atient serum assays and enzyme-linked immuno-sorbent assays (ELISA).

67 properties by AFM and molecularly imprinted sorbent assays.

68 In this approach, the dispersion of the sorbent at a very low milligram level was achieved by in

69 MAD) resin as a solid-phase extraction (SPE) sorbent at pH 8.

70 A novel organic-inorganic hybrid sorbent based on adsorbing quarternized poly vinylpyridi

71 ic phase sorptive extraction (FPSE), a novel sorbent-based microextraction method, was evaluated as a

72 e and gypsum (reference mix); (II) CaL spent sorbent, bauxite and gypsum; (III) CaL spent sorbent plu

73 The sorbent behaviors of CMIP were characterised using spect

74 ignificant potential to improve these hybrid sorbents by controlling the impregnation conditions, whi

75 Dispersive solid-phase clean-up sorbents (C18, GCB, Florisil, chitosan and graphene) wer

76 Finally, this sorbent can be used as a simple, rapid, reliable, select

77 mpeting ions demonstrates that our optimized sorbents can achieve a recovery efficiency of approximat

78 t adsorption rate, high amine efficiency and sorbent capacity well exceeding the highest value report

79 The extract of the neutral sorbent cartridge contained most of the targeted chemica

80 For this purpose two different P&T sorbent cartridges have been evaluated.

81 Sorbent characterization was investigated by SEM, FT-IR,

82 hich chemical compounds are collected with a sorbent-coated fiber and then desorbed into an analytica

83 The oligo dT20-modified PA sorbent coating demonstrated superior extraction perform

84 The PIL sorbent coating featuring halide anions and carboxylic a

85 The selectivity of the PIL sorbent coating for DNA was demonstrated in the presence

86 ic liquid (PIL) and a polyacrylate (PA) SPME sorbent coating was optimized to enhance the extraction

87 or extraction performance than the native PA sorbent coating with quantification cycle (Cq) values 33

88 olymerization technique, eight different PIL sorbent coatings were generated and their DNA extraction

89 Of the studied SPME sorbent coatings, the PIL containing carboxylic acid moi

90 d using antimony ion imprinted polymer (IIP) sorbent combined with electrothermal atomic absorption s

91 Fully polymeric and biobased CO2 sorbents composed of oxidized nanofibrillated cellulose

92 stones on their reactivity and the effect of sorbent concentration, pH, redox potential, and the sulp

93 to-sorbent reproducibility (%RSD<8) and each sorbent could be used up to 30 times (%RSD<6).

94 ption trends for all sorbates and carbonized sorbents could be very well described by a single regres

95 Activated Carbon (AC) or other carbon sorbent (CS) injection into coal combustion flue gases c

96 The SnS50 hybrid sorbent demonstrated a high, although slightly reduced,

97 The magnetic-MWCNTs-PVA cryogel-mu-SPE sorbent developed, with a large surface area and macro-p

98 The method used a sorbent dilution series with solid supported lipid membr

99 eding up sample flow through the solid phase sorbent during phenol extraction and, furthermore, preve

100 g linear partition coefficients onto various sorbents (e.g., organic carbon, soils, clay) are reliabl

101 plers, different deployment times, different sorbents, etc.) and as the SVOC community looks to asses

102 The modified PA sorbent extracted sufficient mRNA from total RNA at conc

103 ents: C18 and florisil, and eight cleanup co-sorbents: florisil, silica, silica/alumina, Envi Carb, E

104 In aquatic systems, CDOM may act both as sorbent for AAs and as photosensitizer, creating microen

105 in designing high-capacity but expensive CO2 sorbent for developing practical or cost-effective CO2 t

106 The MIP was evaluated as a sorbent for extraction and preconcentration of SPI from

107 xyapatite (HA) has been shown to be a strong sorbent for F(-); however, low permeability of synthetic

108 ough BC is known as an important sedimentary sorbent for HOCs, its affinity for PBDEs has been poorly

109 eloped as an alternative for costly AC-based sorbent for mercury capture.

110 ition, is modified to develop an inexpensive sorbent for oil spill remediation.

111 t work demonstrates that LDH is an effective sorbent for selective extraction of lithium from brines,

112 g electron microscopy (SEM) and applied as a sorbent for selective magnetic solid phase extraction of

113 To this end a XAD(R) resin was employed as sorbent for selenomethionine (Se-Met), selenomethylselen

114 as dispersive solid-phase extraction (dSPE) sorbent for the extraction of a group of six mycotoxins

115 ia a simple chemical method and applied as a sorbent for the preconcentration and extraction of trace

116 als for being used as solid phase extraction sorbent for the selective preconcentration and determina

117 ric magnetic nanoporous carbons (muMNPCs) as sorbents for automated solid-phase extraction (SPE).

118 Different polymeric and silica sorbents for clean up were tested and the combination of

119 y for the use of micro- and nanomaterials as sorbents for dispersive microsolid phase extraction (D-m

120 Whey microbeads are well suited to act as sorbents for encapsulation.

121 s higher than those reported for known solid sorbents for ethene/ethane separation.

122 hlight the development of carbon-based solid sorbents for postcombustion CO2 capture.

123 ated poly vinylpyridinium, were optimized as sorbents for secondary effluent organic matter (EfOM) in

124 suggest the possibility of exploiting these sorbents for separation of azeotropic mixtures of fluoro

125 nctionalized MMSNs hold promise as effective sorbents for sequestering U from acidic, alkaline or hig

126 ansfer polymerization and were introduced as sorbents for the cleanup and enrichment of a ProGRP sign

127 tion (SPE) cartridge to serve as tailor-made sorbents for the separation of thiabendazole in orange j

128 )-(oxyhydr)oxides, rendering flocs effective sorbents for trace metal(loid)s.

129 The optimised MIP was evaluated as a sorbent, for extraction and preconcentration of diazinon

130 oxy)phenol (triclosan)) were measured for 15 sorbents: fresh and carbonized wood shavings, pig manure

131 Separation of the sorbent from the spent sample cannot be conducted withou

132 on a minicolumn packed with Amberlite XAD-4 sorbent functionalised with 2-(2'-benzothiazolylazo)-p-c

133 se reflectance spectra on the surface of the sorbent has been proposed.

134 The sorbent has been synthesised in the presence of Sb(III)

135 capture capacity of the amine functionalized sorbents have been conducted under atmospheric condition

136 Key sorbent properties included the sorbent hydrophilicity and hydrophobicity, surface pKa o

137 The calcium looping (CaL) spent sorbent (i) can be a suitable limestone replacement in t

138 ing passive air samplers (PAS) consisting of sorbent-impregnated polyurethane foam (SIP) disks in par

139 s, consisting of polyurethane foam (PUF) and sorbent-impregnated PUF (SIP) disks, were deployed for o

140 odified material as a magnetically separable sorbent in selective enrichment of lead ions from water

141 the dispersion of the fine particles of the sorbent in the bulk aqueous sample.

142 n from shrimp shell waste was evaluated as a sorbent in the QuEChERS method in order to determine mul

143 rylmethyl radicals and then immobilized on a sorbent in water solution and investigated by double qua

144 The prepared muMNPCs are exploited as sorbents in a microcolumn format in a sequential injecti

145 ave attracted significant attention as solid sorbents in gas separation processes for low-energy post

146 MIPs have found use as sorbents in sample preparation attributed to the high se

147 st widely-applied and abundant catalysts and sorbents in the chemical industry.

148 than doubling the best thiol-functionalized sorbents in the literature.

149 The four contrasting sorbents included an organic matter (OM)-rich peat soil,

150 itions and the presence of competing natural sorbents, including particulate and dissolved organic ca

151 Understanding the mechanism of gas-sorbent interactions is of fundamental importance for th

152 Virus-sorbent interactions were governed by long-ranged electr

153 ew method was based on the dispersion of the sorbent into the sample to maximize the contact surface.

154 Adsorption using solid amine sorbents is an attractive emerging technology for energy

155 Exploring efficient and low-cost solid sorbents is essential for carbon capture and storage.

156 pping increases the focusing power of a weak sorbent like PDMS and allows narrow chromatographic peak

157 A novel sorbent, lithium aluminum layered double hydroxide chlor

158 arameters were optimized including amount of sorbent loading, extraction time, desorption solvent and

159 lline ferrihydrite in the absence of mineral sorbents, low-crystalline lepidocrocite in the presence

160 cribes the preparation of a Layered Silicate Sorbent (LSS) for CO2 capture using the layered silicate

161 Current syntheses for solid amine sorbents mainly based on physical impregnation or grafti

162 ction conditions were: sorbent material, C8; sorbent mass, 20mg; extraction time, 90 min; stirring sp

163 influence of several parameters, such as pH, sorbent mass, shaking time was examined.

164 carbon dioxide absorption rates for a given sorbent mass.

165 Mercury pulse injection tests on the sorbent material after leaching indicate that both sorbe

166 new dispersive solid phase extraction (dSPE) sorbent material in the determination of acrylamide in s

167 and its use as solid-phase extraction (SPE) sorbent material was demonstrated.

168 The optimum extraction conditions were: sorbent material, C8; sorbent mass, 20mg; extraction tim

169 n for Hg capture where the handling of spent sorbent materials and the possible secondary pollution n

170 and graphene oxide (GO) were investigated as sorbent materials for 11 polychlorinated biphenyl (PCB)

171 timization of selectivity in amidoxime-based sorbent materials, but may also afford insight to unders

172 rum that contained nitrate salts and organic sorbent materials.

173 These results suggest that PPI-based CO2 sorbents may allow for longer sorbent working lifetimes

174 A sol-gel hybrid sorbent, methyltrimethoxysilane-tetraethoxysilane (MTMOS

175 equilibrating water-organic vapors with soil sorbents might lead to overlooking slow chemical reactio

176 hetic dyes based on their sorption on silica sorbent modified with hexadecyl groups (C16) followed by

177 fouling effect observed for the high surface sorbents MWCNT and nano-PS.

178 forms on aquatic plant roots is an important sorbent of metal(loid)s and plays a role in the attenuat

179 nO2, which accounts for less than 20% of the sorbent on a mass basis.

180 nce of the physical properties of the carbon sorbents on nitrosamine adsorption was examined.

181 rmeability, combined or not with an ethylene sorbent, on tomato organoleptic and nutritional properti

182 Two kinds of PEI are present in the sorbent, one exposed PEI layer that is responsible for h

183 arameters such as sonication and the type of sorbent or extraction solvent were assayed.

184 ts in the use of graphene-based materials as sorbent or photocatalytic materials for environmental de

185 cases, trapping the gas-phase analytes into sorbents or containers.

186 Testing of the Br-Ash sorbent over a wider range of pH and liquid:solid ratios

187 Sorbent packed columns are used and sorption data are de

188 an Langmuir binding constant, and two global sorbent parameters; the total site density and the stand

189 ample, aminosilane-grafting) lead to limited sorbent performance in terms of stability and working ca

190 To model the effect of oxidation on the sorbent performance, thermal- and acid-oxidized sorbents

191 The PtGe2S5 sorbent performed the best overall with capture efficien

192 ries (82%) due to irreversible adsorption to sorbent phase.

193 sorbent, bauxite and gypsum; (III) CaL spent sorbent plus anodization mud and a mixture of fluidized

194 The 103 MHz SAW sensors are coated with thin sorbent polymer films to provide the appropriate limits

195 Key sorbent properties included the sorbent hydrophilicity a

196 imental parameters to be used for evaluating sorbent properties.

197 ng alternative in sorption studies to reveal sorbent properties.

198 rbon black (GCB) and primary-secondary amine sorbent (PSA).

199 most efficient conditions with a mixture of sorbents (PSA, C18, GBC and Zr-Sep(+)).

200 A sample of CaL spent sorbent, purged from a 200 kWth pilot facility, was test

201 0 degrees C, which regenerates the guanidine sorbent quantitatively.

202 sorbate and the specific surface area of the sorbent (R(2) > 0.89).

203 (PXR)-like activities (mug standard-EQ/g of sorbent range), and weak estrogenic activity (ng E2-EQ/g

204 and weak estrogenic activity (ng E2-EQ/g of sorbent range).

205 l conditions were a pH of 6.0 and a magnetic:sorbent ratio of 2:1.

206 earch has regarded carbons merely as passive sorbents, recent studies show that PCM can promote chemi

207 g lifetimes due to an increased tolerance to sorbent regeneration conditions and suggest that the pre

208 imetric analysis (TGA) tests under realistic sorbent regeneration conditions, which necessarily invol

209 To further reduce costs, an aerobic thermal sorbent regeneration step was also examined due to the l

210 at significantly less energy is required for sorbent regeneration.

211 and variety of interactions provided by this sorbent rendered it highly efficient for the extraction

212 f CO2 is the best among all of the MgO-based sorbents reported so far.

213 W) to describe sorption of aromatic acids to sorbents representing different degrees of carbonization

214 o-porous structure, provided good sorbent-to-sorbent reproducibility (%RSD<8) and each sorbent could

215 t material after leaching indicate that both sorbents retain significant mercury capture capability e

216 rent rate constants were similar for all the sorbents, RHs and phenol activities studied.

217 e food matrices and compared with commercial sorbent (RP18 and Oasis HLB).

218 e prehydrated sorbents, as compared with the sorbent samples in phenol-free atmosphere at the same RH

219 Sorption to the "bulk" sorbents sediment organic matter (OM) and micro-PE occur

220 obtained data for adsorption capacity of the sorbent shows the high tendency of the sorbent toward th

221 surface of the samplers might have acted as sorbents, slowing the migration of the dissolved species

222 s eliminate open metal sites from dominating sorbent-solvate interactions and possibly masking the ef

223 The impact of sorbent, solvent, acid, preservative, elution, and evapo

224 In situ sediment amendment with sorbents such as activated carbon (AC) can effectively r

225 Alternative materials which can be used as sorbents, such as chitosan in the clean-up step, are che

226 Langmuir coefficients varied with sorbent surface chemistry.

227 nanospheres onto a positively charged model sorbent surface in the presence of varying DOM concentra

228 graphic irregularities on both the virus and sorbent surfaces.

229 liquid solvents appears effective as methane sorbents, systematic screening of over 87,000 zeolite st

230 alated BDTA and is particularly enhanced for sorbent systems with free surfactant or micelle in solut

231 ption of the studied metals in mixed sorbate-sorbent systems, but only under narrow ranges of ionic s

232 xhaustive description of the use of chemical sorbents targeted at this application.

233 was compared to three well-known commercial sorbents (Tenax TA, Carbopack X, and Carboxen 1000) unde

234 ts show that the commercial activated-carbon sorbents tested have a high capacity and selectivity for

235 This phenomenon led to a nano-structured CO2 sorbent that binds CO2 spontaneously in ambient air when

236 2) spontaneously depolymerizes, leading to a sorbent that can be easily regenerated without the therm

237 Herein we report a simple aqueous guanidine sorbent that captures CO2 from ambient air and binds it

238 we report the development of a synthetic CO2 sorbent that possesses a high cyclic CO2 uptake capacity

239 has seen a steep rise in the use of chemical sorbents that are cycled through sorption and desorption

240 Solvents and solid sorbents that interact strongly with CO2 are described,

241 nique star like nanostructure of synthesized sorbent, the tendency of the sorbent toward selective ex

242 ly generates substantial quantities of NO on sorbents, the amount generated by UiO-66-NH2 is signific

243 ll is slightly lower relative to neat liquid sorbents, the surface area enhancement gained via encaps

244 When whey microbeads are used as sorbents, they show excellent potential to immobilise sm

245 s and the most widely used as a catalyst and sorbent; this results in ca. 10% higher micropore volume

246 iendly since it avoids the synthesis step of sorbents, thus significantly saving time, chemicals, and

247 double hydroxide core-shell microspheres as sorbent to enable automation of the integrative extracti

248 shell (OTS) was evaluated as an inexpensive sorbent to remove methylene blue (MB) from aqueous solut

249 and employed as solid-phase extraction (SPE) sorbents to extract several aromatic acids (protocatechu

250 ea and macro-porous structure, provided good sorbent-to-sorbent reproducibility (%RSD<8) and each sor

251 order to investigate the selectivity of this sorbent toward Pb(II) ions, the effect of variety of ion

252 of synthesized sorbent, the tendency of the sorbent toward selective extraction of lead and copper i

253 f the sorbent shows the high tendency of the sorbent toward the mentioned ions in this nanostructure

254 the extract was vaporized through a Tenax TA sorbent tube via a nitrogen gas flow, in the FEDHS step.

255 ve to exhaustive sampling through a standard sorbent tube.

256 electronic cigarettes, such as impingers and sorbent tubes containing DNPH, significantly underestima

257 ng XAD4-coated quartz fiber filters and XAD2 sorbent tubes.

258 Our findings demonstrate that sorbent type, pH and reaction time are important factors

259 ronmental-friendly microextraction by packed sorbent ultra-high pressure liquid chromatography analys

260 d to date for low-temperature carbon dioxide sorbents under simulated flue gas conditions.

261 n mussels has been optimised in terms of the sorbents used for extracting and cleaning-up.

262 Here we report a family of solid amine sorbents using a grafting-from synthesis approach and sy

263 ation conditions, the CO2 uptake of the best sorbent was 0.33 g of CO2/g of sorbent (after 10 cycles)

264 The sorbent was able to exclude all the remained proteins in

265 This sorbent was applied for the extraction of dibutyl phthal

266 The modified nanoporous carbon sorbent was characterised by thermogravimetric analysis,

267 ection and sample clean-up with a mixed-mode sorbent was compared.

268 The maximum sorption capacity of the sorbent was found to be 71.4mgg(-1).

269 ged 61%, and was enhanced when hydrated lime sorbent was injected.

270 riginal powdered material, the synthetic CO2 sorbent was pelletized.

271 nvolving a solid phase extraction with a C18 sorbent was proposed (average analyte recoveries were be

272 Finally, the introduced sorbent was successfully applied for trace determination

273 raction (magnetic-MWCNTs-PVA cryogel-mu-SPE) sorbent was synthesized by incorporating magnetic partic

274 educed to As(III), and 53-68% of the Fe(III) sorbent was transformed, dominantly to siderite and gree

275 n (FUSLE) and a clean-up step with Envi-Carb sorbent was validated and applied to the quantification

276 The thermal stability of sorbents was confirmed by thermogravimetry experiments,

277 ber waterwash effluent with activated-carbon sorbents was developed to reduce the environmental impac

278 Sorbent-water distribution coefficients (Ks) calculated

279 ow rate on the extraction selectivity of the sorbent were marginal.

280 bent performance, thermal- and acid-oxidized sorbents were also prepared from the commercial sorbents

281 The sorbents were characterized and revealed the presence of

282 SPE and co-precipitation extraction with the sorbents were conducted and experimental parameters such

283 Different sorbents were tested and optimized using central composi

284 Different clean-up sorbents were tested, and the best results were obtained

285 Adsorption capacity of MOF-199 and two sorbents, when assessed for the 13 odorants at a 10% bre

286 DH) phases during reaction with the Al-oxide sorbent, whereas As(III) and As(V) formed inner-sphere s

287 ith a styrene-divinylbenzene copolymer (PPL) sorbent, which has become an established method for the

288 both the Br-Ash and commercial brominated AC sorbents, while the bromine leached into the aqueous pha

289 t commonly employed in proteomics: 100 A C18 sorbent with 0.1% formic acid as an ion-pairing modifier

290 ed oil sorption capacities of X-type zeolite sorbent with different surface functionalization (propyl

291 The sorbent with high amount of covalently tethered amines s

292 ess consists of three steps: (1) loading the sorbent with lithium chloride from brine; (2) intermedia

293 mRNA was enhanced by functionalizing the PA sorbent with oligo dT20 using carbodiimide-based amide l

294 ple preparation due to a shift to the use of sorbents with customizable size, shape, and chemical pro

295 uples the capacity and selectivity of liquid sorbents with high surface area to facilitate rapid and

296 onation depended little on the nature of the sorbent, with only birnessite producing an atypically la

297 Organic matter effects varied among sorbents, with the largest OM fouling effect observed fo

298 Both species were collected onto a solid sorbent within the preconcentrator and then released by

299 PPI-based CO2 sorbents may allow for longer sorbent working lifetimes due to an increased tolerance

300 tive removal capability of MOF-199 and other sorbents (zeolite (ZL) and activated carbon (AC)) was as