ライフサイエンスコーパス: adsorbent

1 was used in the structure of fabricated nano-adsorbent.

2 n the collection medium was used as the SERS adsorbent.

3 osolids drying and the need for supplemental adsorbent.

4 mportant to its application as a viable P(i) adsorbent.

5 a step for photochemical regeneration of the adsorbent.

6 t pH 2.5, five draw-eject cycles and 8 mg of adsorbent.

7 tion have prevented production of an optimal adsorbent.

8 e nuclear industrial effluent as a potential adsorbent.

9 at 125 degrees C effectively regenerated the adsorbent.

10 e higher than those of other boron-selective adsorbents.

11 s (BET surface area and pore volume) for the adsorbents.

12 oposed as a new capacity target for hydrogen adsorbents.

13 g-term stability of amine-functionalized CO2 adsorbents.

14 he kinetics of Cd(II) adsorption by the four adsorbents.

15 demonstrate the versatility of beta-CD-based adsorbents.

16 o ensure valid comparisons between different adsorbents.

17 ethods motivate efforts to develop effective adsorbents.

18 decrease ammonium adsorption for any of the adsorbents.

19 obtained because of the bleaching ability of adsorbents.

20 ial in catalysis, and as supercapacitors and adsorbents.

21 chemical industry as selective catalysts or adsorbents.

22 industrial processes, mostly as catalysts or adsorbents.

23 commercial processes, mostly as catalysts or adsorbents.

24 nsumption for activation and regeneration of adsorbents.

25 these respects as compared with traditional adsorbents.

26 and rationally design superior catalysts and adsorbents.

27 s can be achieved with micro and meso porous adsorbents.

28 f these industrially important catalysts and adsorbents.

29 , and its modified versions were compared as adsorbents.

30 red with those ones obtained with commercial adsorbents.

31 ategy for the design of next-generation O(2) adsorbents.

32 for the design and development of selective adsorbents.

33 rate and affinity surpass those of existing adsorbents.

34 lead to the development of novel sensors and adsorbents.

35 orities for screening and defining selective adsorbents.

36 orption through development of polymer-based adsorbents.

37 ive strategy to develop high-performance gas adsorbents.

38 m energy needed to completely regenerate the adsorbent (100% desorption efficiency) using microwave r

39 the magnetic nature of the constructed nano-adsorbent, a magnet bar was used to separate the nano-ad

40 Results showed that SP and SP-XL adsorbents achieved optimum lysozyme adsorption at pH 9

41 ications, it is essential to understand both adsorbent-adsorbate and adsorbate-adsorbate interactions

42 ing strategy for grouped adsorption data for adsorbent-adsorbate pairs under different equilibrium co

43 breakthrough time and adsorption capacity of adsorbents/adsorbates with different dielectric properti

44 he extraction processes including: amount of adsorbent, adsorption and desorption times, type and vol

45 ration optimizations including pH, dosage of adsorbent, adsorption-desorption time, concentration and

46 is more than 340% higher than the industrial adsorbent Ag(0)@MOR under identical conditions.

47 ficiency, including sample pH, contact time, adsorbent amount, and sample volume were studied and opt

48 Different factors (the pH, adsorbent amount, contact time, type of eluent, matrix a

49 Various analytical parameters such as pH, adsorbent amount, mixing time, eluent solution, sample v

50 analyze the interaction strength between the adsorbent and adsorbate, and adsorption site heterogenei

51 lline, hydrated aluminosilicate with natural adsorbent and ion exchange properties, which removes har

52 horizontal lineC of pretreated barley straw adsorbent and pi* carbon atom in benzene ring attached t

53 n capacity is usually underutilized, wasting adsorbent and reducing productivity.

54 , absorption time, the concentration of nano-adsorbent and temperature were calculated to be 6, 21 mi

55 d in origami design which integrates the gas adsorbent and the electrochemical detection zone in a si

56 Understanding the interactions between an adsorbent and the uremic toxins is critical for designin

57 tcombustion CO2 capture processes with solid adsorbents and discusses a variety of carbon-based mater

58 e, chitosan, and lignosulfonate were used as adsorbents and flocculants.

59 akes them promising candidates for efficient adsorbents and host-guest applications.

60 h they have already found uses as catalysts, adsorbents and membranes precise determination of their

61 developments in inorganic materials; polymer adsorbents and related research pertaining to amidoxime;

62 nd its stability relative to other potential adsorbents and the selective nature of Tl(+) uptake by i

63 latest developments in ultra-microporous MOF adsorbents and their use as separating agents via thermo

64 Two types of co-adsorbents and two types of aptamer linkers were studied

65 s(III) with exceptional uptake (>100 mg As/g adsorbent), and during release, synergistic electrocatal

66 resulting composition and properties of the adsorbents, and thus played a crucial role in the adsorb

67 ly halloysite nanotubes (HNTs), an efficient adsorbent, AO-HNTs, is developed.

68 Those adsorbents are claimed to be the origin for optical prop

69 Supramolecular adsorbents are expected to fully expose their abundant a

70 These two adsorbents are highly suitable for use in direct recover

71 lly utilized in the development of selective adsorbents are reviewed: variation in surface complexati

72 Amidoxime-functionalized polymeric adsorbents are the current state-of-the-art materials fo

73 and 51.4 cm(3) (STP) cm(-3)) for a physical adsorbent at 400 ppm of CO2 and 298 K.

74 nd P2 phosphate functional groups toward the adsorbent at pH 5 and 8.5, as evidenced by the changes i

75 metal-organic frameworks also serve as good adsorbents at low temperatures.

76 Few hydrogen adsorbents balance high usable volumetric and gravimetri

77 ogenic distillation to the energy-efficient, adsorbent-based separation and purification in the futur

78 full CO2 desorption in conventional physical adsorbents but considerably lower than chemical sorbents

79 stantial energetic benefits over traditional adsorbents, but few guidelines currently exist for the d

80 Furthermore, the resulting adsorbent can be recycled multiple times without loss of

81 Our findings provide insight into how adsorbents can be combined to remediate groundwater cont

82 Biochar adsorbents can cost less and sequester carbon; however,

83 ults demonstrate how slight modifications to adsorbents can maximize their performance.

84 The design of stable adsorbents capable of selectively capturing dioxygen wit

85 ontrol humidity by adsorbing water; however, adsorbents capable of the dual functionality of humidifi

86 Cation adsorption curves for four adsorbents (clinoptilolite, biochar, Dowex 50, and Dowex

87 We deployed adsorbents coated with thin oil films for up to 4 months

88 is based on a nanoelectromechanical array of adsorbent-coated resonating double clamped beams.

89 The effects were studied of two different adsorbent combinations (com I; bentonite: activated carb

90 However, the development of ideal adsorbents combining high adsorption capacity with high

91 icacy together with stability of these novel adsorbents composed of both primary and/or secondary ami

92 ngle polymerization and the promise of novel adsorbents constructed from molecular receptors.

93 This microbe bead adsorbent contained a homogenous distribution of cells w

94 Provided adequate adsorbents corresponding to characteristics outlined in

95 y, high capture efficiency and low cost, the adsorbent demonstrates promise for industrial radioactiv

96 nstrate the scope and tunability of CD-based adsorbents derived from a single polymerization and the

97 ll focus on recent advancements in MOF-based adsorbent design for protection against chemical warfare

98 rs and organic linkers, offer a unique solid adsorbent design platform due to their great synthetic v

99 situ using powder X-ray diffraction, allows adsorbent design trade-offs to be overcome, coupling low

100 functionalities is an emerging strategy for adsorbents design to achieve the required affinity.

101 as the pH value, adsorption time, amount of adsorbent, desorption conditions (type, concentration an

102 e fabrication processes of the magnetic nano-adsorbent, different techniques of fourier-transform inf

103 periments indicate that, in contrast to many adsorbents, dmpn-Mg2(dobpdc) captures CO2 effectively in

104 Unique to members of this promising class of adsorbents, dmpn-Mg2(dobpdc) displays facile step-shaped

105 Performance parameters (time, pH, adsorbent dosage and initial ion concentrations) effecti

106 varying the parameters such as contact time, adsorbent dosage and temperature.

107 tions, such as pH, sample volume, flow rate, adsorbent dosage, and eluent type.

108 Influences of Fe(2)O(3) loading, adsorbent dosage, contact time, pH, initial phosphate co

109 nalized magnetic nanoparticles are promising adsorbents due to their large surface areas and ease of

110 Oral intestinal adsorbents (enterosorbents) are orally administered mate

111 All adsorbents exhibited variable removal of the nonionic PF

112 A novel adsorbent (Fe(3)O(4)/HCO) was prepared via co-precipitat

113 PEDS consist of an adsorbent-filled sachet that is suspended in water to co

114 e retainers were used instead of more common adsorbent filter papers.

115 The equilibrium sorption of the adsorbents fitted well to the Langmuir model, and the so

116 XAFS analysis of adsorbents following deployment in environmental seawate

117 cled paper waste represents a cost-effective adsorbent for anionic contaminant removal under environm

118 by FTIR, SEM and elemental analysis and used adsorbent for column solid phase extraction of selenium

119 positions NbOFFIVE-1-Ni as the new benchmark adsorbent for direct air capture and CO2 removal from co

120 ro-waste OTS could be utilized as a low-cost adsorbent for efficient dye removal, and fungal treatmen

121 cavity make it an attractive supramolecular adsorbent for environmental applications.

122 s hydrolytically stable MOF as a prospective adsorbent for humidity control in confined spaces, such

123 The adsorption capacity of the adsorbent for lead was found to be 73mgg(-1).

124 on, an ideal scenario would involve a single adsorbent for multiple separations.

125 nut processing factory, have been used as an adsorbent for Pb(II) ions in water.

126 (dried/milled) bauxite ore as an inexpensive adsorbent for remediating fluoride-contaminated groundwa

127 able syringe filter holder and applied as an adsorbent for solid phase extraction of four aflatoxins

128 that TLSB is an eco-friendly and sustainable adsorbent for the extraction of Zn(II), Cd(II) and Hg(II

129 rs on a syringe tip and used as an efficient adsorbent for the first time.

130 um dots (Fe3O4@Chi-GQDs) nanocomposite as an adsorbent for the preconcentration of Cu(II) in Thai foo

131 (Fe(3)O(4) content: 40 wt.%) was used as an adsorbent for the removal of arsenic (As) from the conta

132 the potential to be developed as a low-cost adsorbent for the removal of Pb(II) from contaminated wa

133 iethanol amine (PHB-DEA) polymer was used as adsorbent for the sensitive and selective separation, pr

134 adsorbent was used for the first time as an adsorbent for the vortex assisted-solid phase extraction

135 results suggest that illite is an important adsorbent for Tl in soils and sediments, considering its

136 gesting that SSUP fiber might be a promising adsorbent for uranium extraction from the natural seawat

137 and used for the first time as an effective adsorbent for vortex-assisted separation and preconcentr

138 the material, BNNTs utilized as a recyclable adsorbent for water purification.

139 ffort is currently devoted to developing new adsorbents for a given separation, an ideal scenario wou

140 ighlights their potential as next-generation adsorbents for a wide array of CO2 separations.

141 of these materials render them promising new adsorbents for air separation processes.

142 nanoparticles (MNPs) are promising and novel adsorbents for As removal because of their great adsorpt

143 r dmpn-Mg2(dobpdc) one of the most promising adsorbents for carbon capture applications.

144 spectively, and all of them were examined as adsorbents for Cd(II) in this study.

145 Adsorption capacity of the four adsorbents for Cd(II) increased and gradually became sat

146 s aminosilicas, are among the most promising adsorbents for direct air capture applications, one of t

147 corporated into COF-616 to yield a family of adsorbents for efficient removal of several contaminants

148 rameworks (MOFs) hold substantial promise as adsorbents for highly efficient separation of hydrocarbo

149 )-treated ACFCs were effective and renewable adsorbents for low-concentration Hg(0) adsorption and re

150 -1,3-benzenedicarboxylate) were evaluated as adsorbents for separating olefins from paraffins.

151 functional porous materials to be adopted as adsorbents for the effective and energy-efficient separa

152 the possibility of using these compounds as adsorbents for the purification of unrefined vegetable o

153 s demonstrate that GH granules are promising adsorbents for the removal of antibiotic pollutants from

154 ared nanocomposites were studied as magnetic adsorbents for the removal of lead (cationic) and chromi

155 of using supramolecular receptors to design adsorbents for water purification.

156 ind V, the cyclic imide-dioxime group of the adsorbent forms a peculiar non-oxido V(5+) complex, exhi

157 pid and convenient for the separation of the adsorbent from sample solutions.

158 , a magnet bar was used to separate the nano-adsorbent from the solution and then inject to the furna

159 ity of the magnetic ZIF-4 made it a suitable adsorbent, guaranteeing an effective separation.

160 und to a octadecyl silica resin (C-18) as an adsorbent has been developed that allows for dilute HCl

161 The developed adsorbent has good stability which can be reused up to 7

162 ficiency along with stability of these novel adsorbents has also been demonstrated by their repetitiv

163 Amidoxime-based adsorbents have become highly promising for seawater ura

164 graphene oxide (GO) has been suggested as an adsorbent; however, a support is desirable to ensure a h

165 could act as both selective and cooperative adsorbents if guest binding at one site were to trigger

166 erformance proves the high stability of this adsorbent in an acidic, aqueous environment.

167 xysilane (TEOS-MTMOS) was used as a clean-up adsorbent in magnetic solid phase extraction (MSPE) for

168 a nanoparticles (core@mMIP) to be applied as adsorbent in microextraction by packed sorbent (MEPS) fo

169 s indicate that PCL NPs are an effective LPS adsorbent in powder and membrane forms, which have great

170 r the application of kaolinite as an arsenic adsorbent in the actual furnace.

171 ycol graft copolymer (PoleS-PEG) was used as adsorbent in the solid phase microextraction of selenium

172 ilibrium concentration and properties of the adsorbents in the existing MLR models is a possible reas

173 The trace metal uptake by the AI8 adsorbents in this trial also varied greatly from previo

174 Solid adsorbents, in particular ultra-microporous metal-organi

175 propylene from propane relative to any known adsorbent, including para-functionalized structural isom

176 ility issues facing amine-functionalized CO2 adsorbents, including amine-grafted and amine-impregnate

177 The adsorbent is fully regenerable, using oxalate solution.

178 Therefore, the use of such adsorbents is recommended for poultry processing.

179 lized water treatment, one major drawback of adsorbents is their limited recyclability due to inadequ

180 the presence of thrombin, the aptamer on the adsorbent layer captures the target on the electrode int

181 ich is of utmost importance as it determines adsorbent lifetime and operational costs of CO2 capture,

182 om 2.91 to <0.5 ppm in less than 3 min at an adsorbent loading of only 0.3 mg mL(-1) .

183 For SP adsorbent, lysozyme can be eluted ~100% with purificatio

184 propylene, respectively, indicate that these adsorbents maintain sufficient reversibility under mild

185 This chelating resin was used as a new adsorbent material for determination of Cd(II), Co(II),

186 ment of the H(2)BHT-functionalized polymeric adsorbent material that affords high uranium uptake capa

187 ely unsaturated metal sites are appealing as adsorbent materials due to their tunable functionality a

188 ndritic architectures supported in silica as adsorbent materials for direct CO2 capture from air.

189 chnologies, in addition to other attributes, adsorbent materials should be stable over many thousands

190 enge facing scientists is the development of adsorbent materials that exhibit ultrahigh porosity but

191 Activated carbons are the most widespread adsorbent materials used to remove organic pollutants fr

192 frameworks (MOFs) represent a newer class of adsorbent materials with significant industrial potentia

193 content decreased resulting from the use of adsorbent materials.

194 ted carbons and non-porous beta-cyclodextrin adsorbent materials.

195 The SENT adsorbent may be readily regenerated under mild conditio

196 rete, Si/Pyrex microfabricated chips: a dual-adsorbent micropreconcentrator-focuser for VOC capture a

197 Two adsorbents, Montmorillonite Clay (MC) and Granular Activ

198 Conventional adsorbents, namely zeolites and silica gel, are often us

199 Also, the adsorbent needs to have high radiation stability.

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 to assess the feasibility of the foam as an adsorbent of methylene blue dye.

203 Using the magnetic nano-adsorbent of silk fibroin-EDTA ligand and furnace atomic

204 ch made the desilicated material as the best adsorbent of the study.

205 contact with alcoholic solutions acts as an adsorbent of trace elements (Cu and Pb) while releasing

206 de) than those reported previously for other adsorbents of benzoic acid such as activated carbon clot

207 ad in natural and engineered systems, potent adsorbents of contaminants and a source of energy for ir

208 aterials-HT, HS, and COGF-serve as efficient adsorbents of iodine due to the presence of the cationic

209 porous beta-cyclodextrin polymers (P-CDP) as adsorbents of MPs in aquatic matrixes.

210 stimulus applied to a structurally compliant adsorbent, offers a promising avenue for addressing some

211 Development of novel adsorbents often neglects the competitive adsorption bet

212 mechanical and chemical requirements of the adsorbent, one design concept prototyped continuously mo

213 torial effects of an aptamer linker and a co-adsorbent onto a gold electrode for optimal binding effi

214 d and fractionated chromatographically using adsorbent or ionic resins.

215 been expended to develop more cost-effective adsorbent- or membrane-based approaches to purify commod

216 porous aromatic frameworks (PAFs) yields the adsorbents PAF-1-NMDG and P2-NMDG in a simple two-step s

217 bents, and thus played a crucial role in the adsorbent performance.

218 Here we discuss the impact of the adsorbent physical and chemical properties, the feed gas

219 nd vegetables using an amphiphilic copolymer adsorbent, poly(styrene)-co-2-vinylpyridine which was sy

220 Co-MPs' adsorbent properties were tested and validated for their

221 can be utilized to design cooperative CO(2) adsorbents, providing further means of optimizing these

222 solution and/or because the tested adsorbate:adsorbent ratios are not varied sufficiently.

223 +/- 52 L/mg-P(i)), which is higher than P(i) adsorbents recently reported in literature.

224 or standard medical treatment and molecular adsorbent recirculating system (n = 47) at the Universit

225 mortality rate was observed in the molecular adsorbent recirculating system group (9.5% vs 50.0% with

226 rm mortality (up to day 14) of the molecular adsorbent recirculating system group was significantly r

227 ected organ system, this effect of molecular adsorbent recirculating system on mortality was particul

228 Molecular adsorbent recirculating system therapy has demonstrated

229 Among these high-risk patients, molecular adsorbent recirculating system treatment might bridge to

230 Molecular adsorbent recirculating system treatment was associated

231 or standard medical treatment and molecular adsorbent recirculating system.

232 Standard medical treatment and molecular adsorbent recirculating system.

233 upled with side-stream ammonium recovery and adsorbent regeneration could enable ammonium recovery fr

234 ion, a feature desirable for low-energy-cost adsorbent regeneration.

235 These data highlight advantages of P-CDP adsorbents relevant to MP removal during water and waste

236 erein, a novel class of high-performance CO2 adsorbent (rGO@MgO/C) is engineered based on the control

237 chromatography/mass spectrometry analysis of adsorbent samples collected from a constant volume sampl

238 The best results were observed with the adsorbent Sepra.

239 re (60-80 degrees C), solid-phase extraction adsorbent (Sepra, Isolute, Strata X and Oasis) and activ

240 usability studies of spent PNHM/Fe(3)O(4)-40 adsorbent showed ~83% of As(III) removal in the third ad

241 This metal-organic framework-based adsorbent shows very high selectivity toward uranium, as

242 yster and rice by the designed magnetic nano adsorbent silk fibroin-EDTA ligand (SF-Fe(3)O(4)-EDTA).

243 Adsorbent stability, which is of utmost importance as it

244 nt challenge due to the drawbacks of current adsorbents such as low uptake capacity, high cost, and n

245 scussion is presented on new developments in adsorbents, such as ionic liquids, metal oxides, metals,

246 rategy for designing efficient and selective adsorbents suitable for various separations.

247 o extensively adsorb onto positively charged adsorbent surfaces, virus adsorption in such systems in

248 ed methodology, the crucial issue is a novel adsorbent synthesized by grafting 3-mercaptopropyl trime

249 (aminomethyl)piperidine (2-ampd) produces an adsorbent that is capable of >=90% CO(2) capture from a

250 , much effort is focused on developing solid adsorbents that can efficiently capture CO(2) from flue

251 Developing O(2)-selective adsorbents that can produce high-purity oxygen from air

252 separation processes can be lowered by using adsorbents that discriminate molecules based on adsorpti

253 We report adsorbents that overcome these trade-offs.

254 to other primary amine-functionalized solid adsorbents that uptake CO2 primarily as ammonium carbama

255 Here we demonstrate a strategy to design adsorbents that utilizes the tunability of interlayer an

256 For SP-XL adsorbent, the recovery yield and purification factor of

257 onal layer of dye molecules on the exhausted adsorbent through interlayer attractive forces.

258 , this material is one of the most promising adsorbents to date for this important separation.

259 rom these results can be leveraged to tailor adsorbents to the conditions of a given CO2 separation p

260 18 K than 298 K and 308 K, regardless of the adsorbent type.

261 he characteristics of lysozyme adsorption by adsorbents under various conditions, including adsorptio

262 the underlying deactivation pathways of the adsorbents upon exposure to high temperature, oxygen, dr

263 The efficacy of novel adsorbents used in conjunction with R134a requires a dee

264 mass spectra were directly recorded from the adsorbent using the Direct Analysis in Real Time interfa

265 e atmospheric CO2 adsorption by amine-loaded adsorbents using an easy handling and low-cost benchtop

266 n (BAC, microwave-absorbing) and a polymeric adsorbent (V503, microwave transparent) were completely

267 nFe2O4 and magnetic takovite-aluminosilicate adsorbent via precipitation methodology.

268 The maximum adsorption capacity of the adsorbent was calculated to be 69.9mgg(-1).

269 ite (PANI/GOx/C18-SiO(2)-Fe(3)O(4)) alginate adsorbent was developed and employed to extract fluoroqu

270 er samples using the SiO(2)/Al(2)O(3)/SnO(2) adsorbent was developed.

271 The commercial STREAMLINE Direct HST adsorbent was employed to investigate the adsorption cha

272 The capacity of the adsorbent was found 11.5 mg g(-1).

273 The maximum adsorption capacity of the adsorbent was found to be about 350mgg(-1).

274 this work, the efficiency of the synthesized adsorbent was investigated to determine its ability for

275 No thermal aging of adsorbent was observed over the investigated 17 cycles.

276 Results showed that used adsorbent was quite effective in removing Pb(II) from dr

277 This adsorbent was used for the first time as an adsorbent fo

278 The PANI/GOx/C18-SiO(2)-Fe(3)O(4) adsorbent was utilized to extract fluoroquinolones from

279 tal ions in tannery wastewater onto the nano-adsorbents was examined using Weber Morris intra-particl

280 chemically modified fumed silica, as a novel adsorbent, was designed for the preconcentration and det

281 surface, and magnetic characteristics of the adsorbent were investigated by XRD, EDX, FE-SEM, and VSM

282 eluent type, vortex time, amount of magnetic adsorbent were investigated.

283 The prepared adsorbents were characterized using different analytical

284 of adsorption of previously uncharacterized adsorbents were estimated as a function of both uptake a

285 The adsorption capacities of Cd(II) by the adsorbents were less at low pH, and all were enhanced wi

286 riations in the dielectric properties of the adsorbents were monitored using two microwave parameters

287 y where STREAMLINE SP and SP-XL high density adsorbents were selected as the adsorption carrier.

288 The prepared adsorbents were used for the removal of uranium from rea

289 f the reported sorbents, as high-performance adsorbents, were not only proved to be economically prom

290 ensity in diffuse reflectance spectra of the adsorbent, which was used for their direct determination

291 cities than have been achieved for classical adsorbents, while also reducing the amount of heat relea

292 TMOS is reusable up to 7 times as a clean-up adsorbent with good recovery (>85%).

293 The photocatalytic effect endows the adsorbent with high antibiofouling activity by producing

294 could be an affordable fluoride-remediation adsorbent with the potential to improve access to drinki

295 actical extraction of uranium from seawater, adsorbents with high adsorption capacity, fast equilibri

296 se moving constituents and engineer improved adsorbents with intrinsic thermal management for pressur

297 made recently not only in the development of adsorbents with optimal separation performance but also

298 evelopment of a new class of engineered foam adsorbents with the potential to revolutionize water tre

299 chal mesopores into existing microporous MOF adsorbents with tunable properties.

300 tructure and hydrophobicity, the use of this adsorbent yielded quantitative results for the extractio