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 e commercial Fe-IMAC kit and the Strata X-AW sorbent.

3 graphitized carbon black Carbograph 4 as the sorbent.

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

5 can be recovered from the iron nanocomposite sorbent.

6 ing on the extraction selectivity of the PPL sorbent.

7 pH-dependent speciation of both sorbate and sorbent.

8 xygenated compounds were retained on the PPL sorbent.

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

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

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

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

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

14 f tryptic peptides on solid-phase extraction sorbent.

15 ention of (phospho)lipids by the copolymeric sorbent.

16 R-Lipid as dispersive solid phase extraction sorbent.

17 , but it remains a challenge for traditional sorbents.

18 ong known ion exchange materials and natural sorbents.

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

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

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

22 their potential usefulness as catalysts and sorbents.

23 orbents but considerably lower than chemical sorbents.

24 ase performed superior compared to ten other sorbents.

25 ow regeneration energies found in many solid sorbents.

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

27 driving forces in DNA extraction by the PIL sorbents.

28 pport the rational design of next-generation sorbents.

29 aj wines using method with coumarin-specific sorbents.

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

31 Furthermore, ion ratios between sorbent ((56)Fe(16)O(-)) and sorbate ((12)C(14)N(-) and

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

33 in the absence of electron exchange with the sorbent, adsorption to polar mineral surfaces considerab

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

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

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

37 (PAS) that uses a sulfur-impregnated carbon sorbent and a diffusive barrier.

38 C18 was used as sorbent and an extra cleaning step with n-hexane was add

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

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

41 capture and release may complement existing sorbent and processing systems.

42 stic electrostatic potential mapping of both sorbent and sorbate structures provided insights to expl

43 th a reversed phase functionalized polymeric sorbent and spiking samples with inorganic salt were per

44 on-desorption behaviors of peptides on CX-RP sorbent and the coexisting, perplexing effects of pH, an

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

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

47 he extent of 2-line ferrihydrite per mass of sorbent and was resilient to desorption at high ionic st

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

49 C, were evaluated as ammonia gas (NH(3)(g)) sorbents and compared to biochar (BC) and a metal-organi

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

51 2 commonly occurs in the presence of mineral sorbents and organic matter (OM) in soils and sediments;

52 experiments involving PBAT addition to model sorbents and soils showed increased PBAT extraction effi

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

54 ameters generally available for carbonaceous sorbents and/or parameters freely available from online

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

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

57 ial platform materials for sensor, catalyst, sorbent, and environmental applications, among others.

58 n temperature and time, sample pH, amount of sorbent, and extraction temperature and time were optimi

59 traction approaches using on-chip disposable sorbents, and (iv) automatic dynamic permeation tests mi

60 ived sorbents, comparison with commonly used sorbents, and the implementation of thermochemical analy

61 The Fe(3)O(4)/HCO sorbent appears to be an efficient and environment-frien

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

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

64 ption of many emerging contaminants to these sorbents are lacking because existing models were develo

65 A large number of promising nanoclay-based sorbents are yet to satisfy environmental biocompatibili

66 lies that in systems, where NOM is the major sorbent, arsenate and monothioarsenate can have higher m

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

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

69 aration and characterisation of the reported sorbents, as high-performance adsorbents, were not only

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

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

72 costing methods such as Enzyme-Linked Immuno-Sorbent Assay (ELISA), High-Performance Liquid Chromatog

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

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

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

76 equential solid phase extraction on nonionic sorbent at steadily lowered pH values: 7, 5, 3, 2, which

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

78 A new bio-MSPE sorbent based on the use of C. micaceus and gamma-Fe(2)O

79 A sorbent based on UVM-7 mesoporous silica was used as sol

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

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

82 less than 6%) compared with conventional SPE sorbents (C18 and styrene-divinylbenzene polymeric types

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

84 rading process and found that this composite sorbent can upgrade biogas at a lower cost (~$0.97 per G

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

86 l for industrial implementation if the right sorbents can be found.

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

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

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

90 ion exchange, and mixed-mode cation exchange sorbent chemistry.

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

92 The PIL sorbent coating featuring halide anions and carboxylic a

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

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

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

96 onitrile (PAN)-based biocompatible thin film sorbent coatings are used, since such materials have bee

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

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

99 Therefore, these composite sorbents combine the high selectivity of liquid sorbents

100 luation of struvite-based wastewater-derived sorbents, comparison with commonly used sorbents, and th

101 f AFB(1) (190 ng/mL) was investigated at two sorbent contents (0.5% and 0.1% w/v) and three pHs (2, 5

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

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

104 A new home-made sorbent (CYXAD, CHYPOS 101 modified Amberlite XAD), was

105 r sorption to polar Al(2)O(3) and a nonpolar sorbent (DAX-8 resin).

106 This Review describes major types of sorbents designed to capture CO(2) from ambient air and

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

108 A sorbent dilution assay with solid supported lipid membra

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

110 mpounds were then eluted from the extraction sorbent, directed in the analytical column, and finally

111 OS and COS removed 46% and 50% (10 g/L of sorbent dose) but POS, OS + P and COS + P removed 96%, 1

112 COS + P removed 96%, 100% and 76% (1 g/L of sorbent dose) when the initial concentration of fluoride

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

114 d better binding performance when serving as sorbents during solid phase extraction (SPE).

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

116 These nanocomposite sorbents exhibit rapid sorption with saturation occurrin

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

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

119 A method to select the appropriate sorbent for a given contaminant based on the ability to

120 DVB) (Bakerbond) has surfaced as a promising sorbent for active sampling of analytes from aqueous mat

121 In this work, a selective sorbent for carbendazim was prepared by the thermal immo

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

123 ti-component assembly strategy and used as a sorbent for effective trapping of TcO(4)(-).

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

125 icate that oyster shells can be an effective sorbent for fluoride removal, with the added benefit of

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

127 s show that ferrihydrite can be an important sorbent for PFASs with six or more perfluorinated carbon

128 shown that activated carbon is an effective sorbent for removal of perfluorooctanoic acid (PFOA) and

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

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

131 etic nanoparticles were used as an efficient sorbent for separation of fluoroquinolones from sample m

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

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

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

135 as developed using maghemite as an efficient sorbent for the separation and preconcentration of antim

136 c acid)-based (NaPAA) hydrogels as effective sorbents for ammonium removal from domestic wastewater.

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

138 materials using this process and applied as sorbents for dissolved phosphorus and arsenic in water,

139 Iron (Fe) oxides in soils are strong sorbents for environmentally important compounds like so

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

141 ities for development of soft anion-adaptive sorbents for highly selective anion decontamination.

142 mework (MOF) materials are often promoted as sorbents for low-energy CCS by highlighting select adsor

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

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

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

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

147 a waste and tea waste hybrids as inexpensive sorbents for uranium removal from water solutions was in

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

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

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

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

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

153 anoclays show particular promise as advanced sorbents, improved dispersants, or biodegradation enhanc

154 anoparticles (Fe(3)O(4@)betaCD-Vinyl-TDI) as sorbent in magnetic u-SPE was developed for the determin

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

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

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

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

159 n and mixed-mode SPE clean-up with different sorbents in sample preparation.

160 mple coumarins, were used in three forms, as sorbents in solid phase extraction (SPE) cartridge or pi

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

162 using micro solid phase extraction by packed sorbent (in spinal syringe format) followed by HPLC-UV.

163 Carbonaceous sorbents include activated carbon, biochar, fullerenes,

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

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

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

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

168 n be substantially reduced if an appropriate sorbent is integrated in the atmospheric water generator

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

170 A novel sorbent, lithium aluminum layered double hydroxide chlor

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

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

173 carbon dioxide absorption rates for a given sorbent mass.

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

175 To tackle these shortcomings, a novel sorbent material was developed, consisting of PAC embedd

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

177 ir sorption/desorption kinetics when used as sorbent materials.

178 compare the enrichment capabilities of five sorbent materials: two commercial weak anion-exchange mi

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

180 er shells, creating Micro-Encapsulated CO(2) Sorbents (MECS), to improve the CO(2) absorption kinetic

181 ed as adsorbent in microextraction by packed sorbent (MEPS) for selective determination of pesticides

182 action techniques, microextraction by packed sorbents (MEPS) and micro solid phase extraction (mu-SPE

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

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

185 ing extraction efficiency (including type of sorbent, number of extraction cycles, pH, elution solven

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

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

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

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

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

191 le (as opposed to acting only as a selective sorbent or filter) are the principal focus, with example

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

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

194 rolactone fibers appeared the most efficient sorbent out of eight tested polymers.

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

196 Sorbent packed columns are used and sorption data are de

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

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

199 Overall, S-150 sorbents performed similarly to BC but were less effecti

200 drone-based sampler was shown to protect the sorbent phase from external contamination while preventi

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

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

203 e different humic acids (HAs) to redox-inert sorbents (polar Al(2)O(3) and nonpolar DAX-8 resin) affe

204 of 1.5 GtCO(2)/yr would require considerable sorbent production and up to 300 EJ/yr of energy input b

205 Key sorbent properties included the sorbent hydrophilicity a

206 ng alternative in sorption studies to reveal sorbent properties.

207 Magnetic nanomaterials were used as sorbents providing an extraction of the target compounds

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

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

210 0 degrees C, which regenerates the guanidine sorbent quantitatively.

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

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

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

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

215 pact, human-powered device incorporating the sorbent removes spiked contaminants from real water samp

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

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

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

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

220 atically minimizing the amount of sample and sorbent required per analysis, as well as affording sign

221 g(-1) for the iron and copper nanocomposite sorbents respectively, which is up to four times higher

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

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

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

225 For wastewater-derived sorbents, S solids heated to 150 degrees C (S-150) had t

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

227 ing and Freundlich isotherms did not predict sorbent saturation, but the extraction and reconstitutio

228 We introduce a synergistic sorbent separation method for the one-step production of

229 , desorption of peptides from the mixed-mode sorbent showed exponential and linear dependence, respec

230 The sorbents showed satisfactory reproducibility in 2.9% to

231 wo commercial weak anion-exchange mixed-mode sorbents (Strata X-AW and Oasis WAX) and three phosphope

232 diated carbon capture utilizing redox-active sorbents such as quinones is emerging as a more versatil

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

234 llulose cone tips were used as a hydrophilic sorbent supporting an aqueous electrolyte solution in a

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

236 graphic irregularities on both the virus and sorbent surfaces.

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

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

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

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

241 3)(g) indicated stronger bonds formed with S sorbents than BC.

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

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

244 ed simple and robust handling of the fibrous sorbent that could be used repeatedly up to at least 5 t

245 vironmentally ubiquitous organic matter (OM) sorbents that act as mediators of terrestrial and aqueou

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

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

248 class of sodium carbonate/silicone composite sorbents that selectively capture carbon dioxide (CO(2))

249 eluted from the nano/microfibrous composite sorbent, the parabens were retained.

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

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

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

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

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

255 ks (MOFs) have been successfully employed as sorbents to harvest water from air, making atmospheric w

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

257 The former technique combined with passive sorbent tube sampling is currently the primary method at

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

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

260 mercial off-the-shelf (COTS) gas sensors and sorbent tubes for further qualitative and semi-quantitat

261 gas and in parallel we collect the Hg(0) on sorbent tubes to be subsequently analyzed using ID-CV-IC

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

263 lisation and further headspace sampling onto sorbent tubes.

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

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

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

267 This highly selective sorbent was applied for the determination and preconcent

268 The sorbent was characterized by SEM, XRD, EDS, and FT-IR.

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

270 using magnetic dextran (Sephadex G-150) as a sorbent was developed for the extraction, separation and

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

272 The lab-made Si(PGDMS) sorbent was physicochemically and morphologically charac

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

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

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

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

277 ise offer potential for passive sampling, if sorbent/water partitioning coefficients (K(sw)) were to

278 Additional tests of the composite sorbent were carried out with pure CO(2) in a sealed pre

279 teraction with Co(II) and Hg(II) of bio-MSPE sorbent were investigated by FT-IR, SEM, and EDX.

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

281 extraction time, sample volume and amount of sorbent were optimized using central composite design (C

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

283 retained Cr(VI) ions on the magnetic dextran sorbents were eluted and detected by linear sweep voltam

284 Different sorbents were tested and optimized using central composi

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

286 eaction rates, and sorption isotherms of all sorbents were well-described by the Freundlich sorption

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

288 SA and C18 dispersive solid phase extraction sorbents which have been commonly used in this type of m

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

290 is have resulted in new generations of CO(2) sorbents, which may drive the future of DAC and its larg

291 ng to improve peptide extraction by the SPME sorbent while still preventing protein adsorption, thin

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 bents combine the high selectivity of liquid sorbents with the high specific sorption rates and low r

297 We characterized these composite sorbents with X-ray computed tomography, scanning electr

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

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