ライフサイエンスコーパス: reactor

1 by pH oscillations in a well-stirred, closed reactor.

2 ying the "Vocus" ion source and ion-molecule reactor.

3 rogenation are investigated in a two-chamber reactor.

4 om wood pyrolysis was investigated in a flow reactor.

5 1-22) semi-polar GaN in a conventional MOVPE reactor.

6 entration when using this immobilized enzyme reactor.

7 organisms and a purposely designed biomining reactor.

8 cles (NPs) in a continuous flow millifluidic reactor.

9 hode placed in a bench-scale electrochemical reactor.

10 ry agnostic computer-controlled tubular flow reactor.

11 fuel pellet fragment from a commercial power reactor.

12 de (NOx) concentrations in an oxidation flow reactor.

13 n inhibited the NOB in a long-term lab-scale reactor.

14 different environmental conditions in a flow reactor.

15 elected for transport into a flow-drift tube reactor.

16 methanol over Cu-SSZ-13 in a continuous-flow reactor.

17 rried out in a sub-nanoliter (0.8 nL) volume reactor.

18 for the hydrogenation of ethylene in a flow reactor.

19 lution X-ray powder diffraction on a working reactor.

20 yte in this manner was demonstrated with the reactor.

21 dge was incinerated in a pilot fluidized bed reactor.

22 issue: the catalytic hydrogel membrane (CHM) reactor.

23 on of the flue gas before it entered the AWL reactor.

24 seconds and form nanoparticles inside a flow reactor.

25 between biofilm and planktonic phases of the reactor.

26 particles as they are formed inside the flow reactor.

27 at on the zeolite during operation in a flow reactor.

28 potential indicator of a healthy and stable reactor.

29 tegy to produce C3 oxygenates using a tandem reactor.

30 he reagents are passed through a copper coil reactor.

31 moval of residual materials from the damaged reactors.

32 egradation by ~70% than open circuit control reactors.

33 t solution pH is critical for operating FCDI reactors.

34 alysts and accumulating in the downstream of reactors.

35 ar to that in traditionally used metal oxide reactors.

36 improvement of materials and thermochemical reactors.

37 , performance was stable and similar between reactors.

38 brication, self-cleaning surfaces, and micro-reactors.

39 ancy and imparted process stability to these reactors.

40 ent levels of observed carbon storage across reactors.

41 reased to selectively retain granules in the reactors.

42 ma-facing armour components in future fusion reactors.

43 ion of the control rods of pressurized water reactors.

44 m (Am) and curium (Cm) for recycle into fast reactors.

45 photolysis were investigated in tandem flow reactors.

46 ds and can be scaled in either batch or flow reactors.

47 ack of universal design of the chromium (Cr) reactors.

48 nstabilities called disruptions within these reactors(2,3) is one of the most pressing challenges(4,5

49 n-stream operation) conducted in a fixed-bed reactor (550 degrees C, 100 kPa, space velocity 4650 mL

50 at was first discovered as a poison in early reactors(7,8), and (157)Gd (2.5 x 10(5) barns), which is

51 rbana, IL) were operated in sequencing batch reactors (8 day solids residence time, SRT) subjected to

52 At the end of the fuel's useful life in a reactor, about 96% of the SNF is still UO(2).

53 e following a nuclear incident (explosion or reactor accident) assume that uranium-bearing particulat

54 A model for the consumption of 1 in a flow reactor accurately predicted the outcome of a laboratory

55 d 16S rRNA (V1-V3) gene amplicon sequencing, reactors achieved similar and stable nutrient recovery a

56 rhodium catalyst in a simple packed bed flow reactor achieving comparable yields and levels of enanti

57 etween reaction time and position within the reactor, allow for the redefinition of a flow module to

58 Flow electrochemical reactors also provide high surface-to-volume ratios and

59 trophic methanogenesis in a laboratory batch reactor, anaerobic ammonia oxidation in a wastewater rea

60 Using a gas-flow reactor and a NO(x) analyzer, the production of gaseous

61 anaerobic ammonia oxidation in a wastewater reactor and aerobic pyrite oxidation in acid mine draina

62 two reactor types: a traditional light-water reactor and an advanced sodium-cooled reactor design, a

63 um power densities are hindered by different reactor and electrode sizes, solution conductivities, an

64 Utilizing a uniquely designed pilot-scale reactor and real-time recycled water, we evaluated treat

65 ployed effluent from a pilot-scale anaerobic reactor and soluble microbial products (SMPs) generated

66 ed, highlighting both the versatility of the reactor and the benefits of performing kinetic analysis

67 plets serving as single-cell enzymatic micro-reactors and a commercially available flow cytometer, an

68 aminated water commonly found in light-water reactors and in other nuclear processes.

69 with high specificity and identified severe reactors and low threshold with high specificity and hig

70 effects of short and long vertically mounted reactors and temperature profiles on trapping of Cl to e

71 cs in triplicate full-scale sequencing batch reactors and ultimately strengthens our basic understand

72 uction from the core of the algal microscale reactor, and demonstrate that enhanced levels of hydroge

73 magnets for accelerators and compact fusion reactors, and largely depends on the vortex pinning land

74 ion of PC, implementation of continuous-flow reactors, and promotion of deactivation through addition

75 er in aerobic reactors relative to anaerobic reactors, and protozoa numbers significantly inversely c

76 ery and resilience can vary across replicate reactors, and that nitrification recovery need not coinc

77 s that need consideration to optimize any Cr reactor applications to ensure the accuracy of delta(2)H

78 hotoisomerization of 1,2-azaborine in a flow reactor are reported that furnish aminoborylated cyclobu

79 atch, organic electrosynthesis via microflow reactors are advantageous because they allow shorter rea

80 otrophic Fe(II)-oxidizing populations in the reactors are due to distinct metabolic potential that su

81 Similar multivariable experimental reactors are employed beyond biology in the study of act

82 stochastically entrapped inside a femtoliter reactor array device for the fluorogenic assay of neuram

83 atalytic fractionation (RCF) in flow-through reactors as an analytical tool to depolymerize lignin in

84 We designed a reconfigurable flow reactor associating online monitoring and process contro

85 The reaction was carried out in a fixed bed reactor at 0.1 MPa over a temperature range of 275-375 d

86 H(2), and a RhCo(x)/MCM-41 catalyst (second reactor at 200 degrees C) enabling CO insertion for the

87 ved with a Fe(3)Ni(1)/CeO(2) catalyst (first reactor at 600-800 degrees C) for CO(2)-assisted dehydro

88 Studies were conducted in a flow-tube reactor at atmospherically relevant ozone (O(3)) exposur

89 the sandy beach as an aerobic biocatalytical reactor at the land-ocean interface.

90 t the dropwise feeding of substrate into the reactor at very low dilution rates leads to transient be

91 ted during the last 14 days by operating all reactors at low F:M and C:N (henceforth termed F:M-C:N).

92 tant to the long-term decommissioning of the reactors at the FDNPP (and environmental clean-upon), is

93 The reactor avoids mixing reactant gases by transferring oxy

94 s of the scale-ups that are based on a batch reactor (BR) and a three compartment cell (TCC) are high

95 on resulted in the same abundant taxa in the reactors, but drift, which mostly affected low-abundant

96 igured to an autonomous self-optimizing flow reactor by implementation of an optimization algorithm i

97 Oxidation is performed in an online reactor by sulfate radicals.

98 reased almost one fold in single-chamber BES reactors, by adding a conjugated polyelectrolyte (CPE-K)

99 e organic reaction chemistry in the membrane reactor can be performed in organic solvents and without

100 iates because the batch-type electrochemical reactor can only handle a very limited current density d

101 The results confirm that UV-C flow reactors can efficiently inactivate coronaviruses throug

102 Herein we demonstrate a packed bed flow reactor capable of achieving highly regio- and stereosel

103 eport the design and operation of a chemical reactor capable of approaching thermodynamically reversi

104 A reactor capable of efficiently collecting kinetic data i

105 ing applications, such as nanoscale chemical reactors, catalysis, batteries, solar energy harvest, ga

106 chniques have been coupled in a new homemade reactor-cell designed in a joint CSIC-LCS collaboration.

107 Metagenomic analyses of the reactor communities revealed differences in the metaboli

108 hed by a factor of 10 in the nitrogen-fixing reactors (compared to controls) attaining 13% of the bac

109 ids retention time (SRT) coexist in the same reactor compartment and are subjected to the same influe

110 e reaction by gas-phase chemistry within the reactor compartment.

111 o dispersible photosynthetic microbial micro-reactors comprising segregated cellular micro-niches wit

112 In addition, the design of new reactor concepts proposed for the most efficient use of

113 trasting release dynamics and the current in-reactor conditions to influence future decommissioning c

114 Post-mortem examination of slaughtered reactors confirmed the presence of both pulmonary and/or

115 Metal oxide-filled reactors constructed with ceramic tubes or fused silica

116 U-Ca-bearing solids at pH 7 was observed in reactors containing 10 mM bicarbonate and Ca, suggesting

117 from passive disruption prediction to active reactor control and optimization.

118 geochemical model was calibrated from batch reactor data and used to identify optimum AMD-HFFF mixin

119 d the likely implications for future planned reactor decommissioning.

120 pCO(2) from 0.3 to 8 bar in lab-scale batch reactors decreased the maximum substrate utilization rat

121 All reactors demonstrated similar changes to their core micr

122 details the basic principles of microfluidic reactor design and performance, as well as the current s

123 used as model polymerizations to develop the reactor design rules and synthesize MWD profiles.

124 ent of this protocol, we constructed general reactor design rules by combining fluid mechanical princ

125 -water reactor and an advanced sodium-cooled reactor design, a likely candidate for future deployment

126 In previous work, lab-scale reactors designed to study microbial Fe(II) oxidation ra

127 ) (scCO(2)) under consideration of different reactor designs to guide process engineers from an envir

128 similar to that of a completely stirred tank reactor digesting similar wastes, but with much lower en

129 Developing self-fueled micro-reactor droplets with programmable autonomic behaviors p

130 or structural components in advanced nuclear reactors due to a high density of nano-oxides (NOs) and

131 ed with the adsorbed GICA using a packed bed reactor during eleven days at 70 degrees C.

132 following a period of activation within the reactor, during which time interaction with the solvent

133 Based on the result, a prototype catalytic reactor employing Pt/C-decorated carbon felt was designe

134 We show that a millisecond catalytic wall reactor enables stable methane conversion, C(2+) selecti

135 ble shape, size, and chemistry that combines reactor engineering principles and controlled polymeriza

136 iplinary collaborations between microfluidic reactor engineers and colloidal nanomaterial chemists.

137 Since the stirred reactor environment eliminates many of the temporal and

138 Subsequently, only two of the three reactors experiencing a switch back from high to low F:M

139 A long-term continuous reactor experiment showed that iso-caproate (4-methyl pe

140 In reactor experiments, i.e., at elevated temperatures, pre

141 Here, using batch reactor experiments, we demonstrate an unexpected accele

142 rates and poor process stability, leading to reactor failure after 40 days.

143 To avoid process instability and/or reactor failure, two metrics had to be met: (a) a methan

144 cation of glass beads (GBs) in fixed biofilm reactor (FBR) for the treatment of simulated methylene b

145 sludge was used to inoculate a 4 L gas-lift reactor fed with H(2) as the electron donor, CO(2) as th

146 ng free-living N(2)-fixing bacteria (NFB) in reactors fed with low nitrogen wastewater, analogous to

147 gies and far higher than observed in low C/N reactors (fed with organic matter and nitrogen).

148 Our reactors fixed appreciable quantities of nitrogen with a

149 3-10%) and CH(4) (4.3-14%) injected into the reactor following a water table rise partitioned into ga

150 le using a 60 L compound parabolic collector reactor for irrigation of two raw-eaten vegetables (lett

151 wells were characterized and mixed in batch reactors for 14 days.

152 oxicology of Ag-NPs, we ran sequencing batch reactors for 28 d to produce three batches of sludge: (1

153 quid marbles have potential to serve as mini-reactors for fabricating new materials, but this has bee

154 e examined sludges from full-scale anaerobic reactors for sulfur-reducing activity at pH 2.0-3.5 and

155 this comment is to show that the "aggregate reactor" framework recently proposed in an article publi

156 es shows them to exist as UO(2)-identical to reactor fuel, with confirmation of their nuclear origin

157 rial-production scales using continuous-flow reactors has become a topic of increasing interest.

158 ined direct (14)CH(4) emissions from nuclear reactors have complicated this approach since the middle

159 Nitrobacter, the key NOB populations in the reactor, have the ability to adapt to FNA and FA, respec

160 er delivered by magnetic-confinement tokamak reactors holds the promise of sustainable and clean ener

161 Results from experiments with a continuous reactor hosting a strain of the plant pathogenic bacteri

162 n a laminar diffusion inverted gravity flame reactor (IGFR) operated on ethylene and ethane.

163 GC), the results showed that the active BES reactor improved the total petroleum hydrocarbon (TPH) d

164 rometer is combined with a microfluidic chip reactor in a proof-of-principle experiment on the Hantzs

165 d with distance from the center inlet of the reactor in all experiments.

166 nderstand the practical implications of this reactor in DNMC.

167 are widely used as pico- to nanoliter volume reactors in chemistry and biology.

168 The FCDS assay screened 30 million micro-reactors in only 1 h, yielding a collection of esterase

169 tions were performed using an oxidation flow reactor, in which ~95% of peroxy radicals (RO(2)) react

170 total amount of CaCO(3) precipitated in the reactor increased with increasing residence time and wit

171 A pilot-scale plasma reactor installed into an 8 x 20 ft(2) mobile trailer wa

172 In this paper, we report a compact micro reactor integrating a thermostat with a re-useable glass

173 ed DNA hybridization transfer in a microflow reactor is demonstrated by moving paramagnetic beads bet

174 An integrated reactor is designed and fabricated to conduct all steps

175 component metallic fuel for advanced nuclear reactors is systematically investigated by taking into a

176 diation (CR), the blue light seen in nuclear reactors, is emitted by some radiopharmaceuticals.

177 h yield fission product generated in nuclear reactors, is one of the most difficult contaminants to a

178 lar International Thermonuclear Experimental Reactor (ITER) project(6) currently under construction,

179 the International Thermonuclear Experimental Reactor, ITER), as well as for other diverse scientific

180 been used in conjunction with a jet stirred reactor (JSR) and time-of-flight mass spectrometry to pr

181 temperature (620 degrees C) with acceptable reactor life, reduced complexity, and improved robustnes

182 plex heterogeneous multiphase systems and in reactors made of conductive materials while maintaining

183 and thermal efficiencies and low cost of the reactor materials are realized, indicating the technoeco

184 Results of this study suggest that optimized reactors may initiate operation at high shear to decreas

185 evaluated in bench-scale moving bed biofilm reactors (MBBRs), achieving soluble organic matter remov

186 ieved in a lab-scale upflow membrane biofilm reactor (MBfR) by coupling anammox with nitrite/nitrate-

187 Here we operated four membrane biofilm reactors (MBfRs) fed with nitrate, nitrite, oxygen at a

188 mblies were loaded in 3D nodal diffusion and reactor model code.

189 The results obtained from the 3D reactor model confirmed that the designed core with the

190 trikingly demonstrates that only with a full reactor model that includes autocatalysis with olefins a

191 e constants for H-SSZ-13 are used in a batch reactor model.

192 According to the type of flow reactors necessary, two main general approaches are poss

193 n this study, a laboratory-scale radial flow reactor of 23 cm diameter, with a 1 mm glass bead monola

194 An enzyme reactor of immobilized Aspergillopepsin I, a highly stab

195 the reactions that could power thermonuclear reactors of the future.

196 spectrometry coupled with an oxidation flow reactor (OFR) to characterize pollution levels and SOA p

197 In last decade, oxidation flow reactors (OFR) have emerged as a promising alternative t

198 l chambers (ECs) and portable oxidative flow reactors (OFRs) is difficult.

199 These modified "ARC" reactors operate with a transition-metal catalyst that r

200 he resulting photocatalyst for OCM in a flow reactor operated at room temperature under atmospheric p

201 d microreactor was minimized using optimized reactor operating parameters and intercolumn connectivit

202 We demonstrate that sealed UV-C flow reactors operating with fluences near 253 +/- 1 nm of 13

203 rmation and growth of CaP granules in a UASB reactor, operating at relatively low upflow velocity (<1

204 During over 650 days of reactor operation, NOB adaptation to both FNA and FA was

205 ylcarbamothioyl)oxy (oxa)helicenes in a flow reactor or nucleophilic substitution of dichloro (oxa)he

206 gnificantly faster than in traditional batch reactors or in segmented flow systems, which is exemplif

207 as a UV-C LED light delivery technology for reactors or tubing.

208 NO(3) on Pyrex glass in a photochemical flow reactor over a wide range of HNO(3) surface density (D(H

209 three parallel, full-scale sequencing batch reactors over the course of a year with respect to react

210 correlated with pRP4-gfp signals across all reactors (p < 0.05).

211 rs over the course of a year with respect to reactor performance, microbial community composition via

212 science, including stellar nucleosynthesis, reactor performance, nuclear medicine and defence applic

213 ermine the effect of different parameters on reactor performance, such as channel height, retention t

214 In wastewater-treatment reactors, photogranules grow in number as well as in siz

215 sed as a detector material(9,10), a burnable reactor poison(11) and a potential medical neutron captu

216 Antineutrino detectors, sensitive to reactor power and fuel changes, can complement the tools

217 eaction cycles at 85 degrees C under a batch reactor, preserving 83% of its initial activity.

218 s (MNSPs) formed in intermediate and high Ni reactor pressure vessel steels under high fluence neutro

219 ith nuclear material existing outside of the reactors primary containment.

220 how hydrogenation in the palladium membrane reactor proceeds at faster reaction rates and with much

221 The reactor provides highly reproducible reaction conditions

222 ndances were over 20 times higher in aerobic reactors relative to anaerobic reactors, and protozoa nu

223 than for the best case and the flow-through reactor scale-up.

224 m laboratory experiments in batch and column reactors showed that 3.6% to 11% of the total Fe in the

225 a MiSeq 16S rRNA gene amplicon sequencing of reactors showed that the microbial community was dominat

226 C-N cross-coupling reaction across multiple reactor sizes and geometries, it was demonstrated that e

227 et dimensions, uranium enrichment, and other reactor-specific features.

228 Batch reactor studies demonstrated substantial adsorption of P

229 he guidelines for enhancing the selectivity: reactor studies of complex catalyst materials at operati

230 ferent communities evolved in the respective reactors, suggesting diverse microbial pathways exist fo

231 ations in nature, we were surprised that the reactors supported multiple taxa presumed to be autotrop

232 Using a high-throughput custom reactor system, we implemented a reaction matrix to test

233 total N(2)O emissions in typical nitritation reactor systems between pH 6.5 and 8.

234 tests in batch and continuously stirred tank reactor systems suggested that it was feasible to achiev

235 whose chemical shifts report on the internal reactor temperature.

236 In a continuously mixed flow reactor test using groundwater, the CHM activity was sta

237 der construction, which aims to be the first reactor that produces more power from fusion than is inj

238 ved using a high temperature chromium-silver reactor that retains carbon, oxygen and fluorine whilst

239 concentrations in a membrane-aerated biofilm reactor that was fed with methane and ammonium.

240 arious protein mediators, become solid-state reactors that can localize at the critical interface of

241 ained-a crucial requirement for future large reactors that cannot afford training disruptions.

242 In this reactor, the addition of CTAB (cetrimonium bromide, a ca

243 In the "high-concentration" plasma reactor, the concentrations of PFAS precursors and long-

244 cterization of the photonic flux within each reactor, the cross-coupling was scaled successfully from

245 By analyzing 600,000 reactors, the practical limit of detection reached the o

246 Compared to control reactors, the strategy enhanced volatile solids destruct

247 ption-translation system within microfluidic reactors, the system is able to regenerate essential pro

248 ncept/accident tolerant fuel for light water reactors thus, understanding their chemical compatibilit

249 for space biomining and the principles of a reactor to advance human industry and mining beyond Eart

250 evaluated the performance of the biggest AWL-reactor to date that was installed at a coal-fired power

251 mmunity members, caused the community in one reactor to diverge from the other two.

252 e the benefits of using a palladium membrane reactor to drive hydrogenation chemistry with electricit

253 Here, we utilize an aerosol flow reactor to perform direct investigation on the kinetics

254 ic catalysts with programmed continuous-flow reactors to rapidly generate libraries of polyester and

255 ment on graphitic carbon nitride as "subnano reactors" to precisely confine multiple Fe and Cu atoms

256 ved in an upflow anaerobic sludge bed (UASB) reactor treating source separated black water and is enh

257 beds and an upflow anaerobic sludge blanket reactor treating the leachate, was operated continuously

258 Replicate reactors treating domestic wastewater were operated unde

259 eutrino monitors to fuel divergence from two reactor types: a traditional light-water reactor and an

260 concentration, pH, operating potential) and reactor types?

261 The design leads to a reactor unconstrained by overall chemical equilibrium li

262 rsible hydrogen electrode within a flow cell reactor under ambient conditions.

263 zed uranium oxide nanoparticles using a flow reactor under controlled conditions of temperature, pres

264 it formed from materials associated with the reactor Unit 1 building explosion, with debris fragments

265 on), is the knowledge that core integrity of reactor Unit 1 was compromised with nuclear material exi

266 ibuted to being contaminated by fallout from reactor Unit 1.

267 ree of melting than that likely derived from reactor Unit 3.

268 Si-based material sourced from the different reactor Units have contrasting internal structure and co

269 ferent Fukushima Daiichi Nuclear Power Plant reactors (Units 1 and 3) is hereby examined to elucidate

270 kthrough curves in a flow-through, fixed-bed reactor using both simulated biogas and locally sourced

271 Miniaturization of a thermolysis reactor using commercially available components is prese

272 of a civilian Russian water-water energetic reactor (VVER) fuel at the end of its lifetime, and is n

273 s originate from initiation of the DNMC on a reactor wall and maintenance of the reaction by gas-phas

274 ning fluorine was determined to be sorbed to reactor walls and tubing using sorption experiments in w

275 Furthermore, we fully demonstrate that the reactor was able to remove ~73% of the H(n)PO(4)(n-3) pr

276 The reactor was employed for hydrogen production via the wat

277 In this study, a microfluidic reactor was fabricated to create diffusion-controlled co

278 The reactor was operated in semibatch mode at a pH 3.5 and 8

279 Subsequently, a "low concentration" plasma reactor was used to remove additional PFAAs.

280 an adenovirus surrogate for validation of UV reactors was evaluated.

281 orescence microscopy in a bioelectrochemical reactor, we demonstrate that membrane potential strongly

282 )Zr to the intense neutron flux of a nuclear reactor, we determine that (88)Zr has a thermal neutron

283 ized dirhodium catalyst employed in the flow reactor, we systematically study both (i) the effects of

284 sulting from sampling downstream of the UV-C reactor were below the limit of detection, the true log

285 s shows that if the hydrogen produced by the reactor were combusted to heat the high-temperature kiln

286 nitrogen discharged by the BTF when the two reactors were connected and liquid was in one-pass mode.

287 Bench-scale 3-D printed reactors were employed to determine the effect of differ

288 Positive SICST reactors were identified in 3% of the animals spread amo

289 Two sets of replicate 5-L sequencing batch reactors were operated at different, low and high, F:M (

290 , the microbial communities in the replicate reactors were similar.

291 anisms behind this phenomenon, five parallel reactors were studied at the single-cell level for about

292 "low-concentration" bench-scale batch plasma reactors were used to effectively degrade per- and polyf

293 troduced into a flow tube or flow-drift tube reactor where they react with analyte molecules in sampl

294 evelopment of DIYBOT (Digital Proxy of a Bio-Reactor), which enables remote monitoring of bioreactors

295 cle size by tuning the volume of the polymer reactors, which correlates with the number of polymer ch

296 We fabricated a microfluidic reactor with a nanoporous barrier to characterize electr

297 ing a three-dimensional printed miniaturized reactor with an integrated electrospray ionization needl

298 ltaneously is also realized by operating the reactor with multiple reaction slugs at the same time.

299 Performance of two versions of the ARC reactors with different combustion volumes was character

300 rse agrochemical active ingredients in batch reactors with three concentrations of the same activated

301 f venemycin are isolable from dialysis-based reactors without chromatography, and the enzymes can be