ライフサイエンスコーパス: reactor

1 t- and substrate-filled flask (tube-in-flask reactor).

2 he first wall/blanket applications in fusion reactor.

3 under two engine loads in an oxidative flow reactor.

4 ith a polymer microfluidic chip based enzyme reactor.

5 taken from a full-scale nitritation-anammox reactor.

6 ropane metathesis at 150 degrees C in a flow reactor.

7 uring atmospheric combustion in a laboratory reactor.

8 absence of water vapor using an aerosol flow reactor.

9 dfill was treated as a perfectly mixed batch reactor.

10 chemical reductants into the polymerization reactor.

11 ctangular reactors and 4 mum for the tubular reactor.

12 parallel fluid streams in a 2D microfluidic reactor.

13 sponds to an increase in conductivity of the reactor.

14 by the inverted conductivity tomogram of the reactor.

15 ed to make a judicious choice for a suitable reactor.

16 d within 2 h at 130 degrees C in a microwave reactor.

17 ion of organic reagents into the pressurized reactor.

18 allowing the concept of a nanoscale chemical reactor.

19 sed on an immobilized whole cells-packed bed reactor.

20 lamine (DMA) was investigated in a flow tube reactor.

21 tantalum vapor in a sophisticated metal-atom reactor.

22 capsulated reagents are prestored within the reactor.

23 ultrafast polymerisation, in a scalable flow reactor.

24 emperature and high-pressure continuous flow reactor.

25 rban aquifer also serves as a biogeochemical reactor.

26 y irradiation of enriched uranium in nuclear reactors.

27 d whole-cell systems) is to use them in flow reactors.

28 wo different species enriched in both of the reactors.

29 n the design and use of biocatalysis in flow reactors.

30 sing fuel for the next generation of nuclear reactors.

31 March 2011 caused partial meltdowns of three reactors.

32 t constituted the abundant community in both reactors.

33 onditions typical of the operation of fusion reactors.

34 were cross-reactive carbohydrate determinant reactors.

35 in laboratory plasma experiments and fusion reactors.

36 ns was explored using sequential-spike batch reactors.

37 f high-throughput acoustophoretic biological reactors.

38 strial separations and as catalytic membrane reactors.

39 f dominant microbial population in separated reactors.

40 for efficient water splitting in solar fuels reactors.

41 uence of six chemical reactions in five flow reactors.

42 ver very large areas in very compact, simple reactors.

43 uated this novel concept in laboratory batch reactors.

44 re regulators, static mixers, and packed-bed reactors.

45 re structural components in advanced nuclear reactors.

46 tions were used to identify ED05 single-dose reactors.

47 promising plasma facing material for fusion reactors.

48 n/detection results were obtained with micro-reactors (2mm diameter and 1.1mm in depth) drilled on a

49 ; (2) a high degradation rate in the dynamic reactor; (3) production of intermediate products (MgO/Mg

50 Among Pla a 3 reactors, 89.6% were Pru p 3(pos) and 86.8% Jug 3(pos) ,

51 ibody adsorption in comparison to unmodified reactors (95% monoclonal antibody recovered vs. 0% recov

52 Using this type of reactor, a fully automated strategy has been developed f

53 We demonstrate our reactors' ability to amplify both DNA and RNA targets us

54 g the March, 2011 Fukushima Dai-ichi nuclear reactor accident in Japan spread rapidly across the Nort

55 T-2 catalyst in a continuous-flow packed-bed reactor achieved nearly 60000 turnovers with no apparent

56 and river waters in biogeochemical microcosm reactors across field-validated redox conditions.

57 compared to 0.46 bar (0.7 V) for the tubular reactor after 52 days.

58 and attached growth packed-bed (AGR) anammox reactors after 220 days of operation.

59 and 6.3 nmol/L for two live and two abiotic reactors after 519 days, respectively.

60 coincided with the permanent shutdown of the reactors after the accident in 2011.

61 reported in an electrochemical flow-through reactor and approached the kinetic limit.

62 als was studied by use of a coated-wall flow reactor and cavity-enhanced spectroscopy.

63 A fragment ion search applied to batch-reactor and environmental samples revealed another trans

64 Among other factors iron-rich reactor and feedstream impurities cause these catalyst p

65 and delta) was investigated using flow tube reactor and in situ Diffuse Reflectance Infrared Fourier

66 y scale apparatus used consists of a tubular reactor and product collection system and analysis train

67 rst describe the process carried out in each reactor and then present an integrated system that produ

68 er was approximately 0.4 mum for rectangular reactors and 4 mum for the tubular reactor.

69 Cross-reactors and botanicals for fragrances were derived from

70 osmic events, particle accelerators, nuclear reactors and clinical radionuclides, it has been used in

71 isotope is encumbered by the aging of these reactors and concerns about international transportation

72 in the supernatant despite completely sealed reactors and constant flushing with anaerobic gases.

73 ns were isolated from the sludge in the UASB reactors and identified by 16 S rRNA analysis.

74 s (phenotype 2) and iii) as in (ii) plus non-reactors and inconclusive reactors to the skin tests wit

75 ctivation, but its application is limited to reactors and open areas that can accommodate lamps/LEDs

76 ncepts proposed to improve the efficiency of reactors and separation units as well as to utilise CO2

77 experimental method involving olivine micro-reactors and show that the rate of serpentinization is s

78 in an upflow anaerobic sludge blanket (UASB) reactor, and examined the effects of NZVI/PS on anaerobi

79 ogen halides, with emphasis on the catalyst, reactor, and process design.

80 Based on the performance of the reactor, and the ability of the lipase to alter free fat

81 lized to examine microbial metabolism in the reactor, and the Illumina MiSeq high-throughput sequenci

82 miniature chemical reactions, droplet-based reactors, and eliminates contamination of manipulator co

83 helium release at fluxes expected in fusion reactors, and hence that accounting for the mobility of

84 erience helium swelling for advanced nuclear reactor applications.

85 rous metallic materials for advanced nuclear reactor applications.

86 is carried out within the premises of a one-reactor approach, i.e. minimizing the number of vacuum c

87 on flux available at the 20 MW OPAL research reactor are described.

88 However, large facilities such as a nuclear reactor are necessary.

89 ow, microfluidic reactions in capillary tube reactors are described, which are capable of synthesizin

90 Here, stainless steel reactors are used to simulate the downhole chemistry of

91 and DFO-Bz-trastuzumab into the microfluidic reactor at a total rate of 20 muL/min in ratios varying

92 dy sampled 35 digester sludge from different reactors at multiple time points together with the feed

93 e present a photonic enzymatic lab-on-a-chip reactor based on cross-linked enzyme crystals (CLECs), a

94 ect use of Haber Bosch produced nitrogen for reactor-based production of microbial protein can be an

95 er conditions and harvested from sand-packed reactors before conducting suspended growth batch kineti

96 or higher hydrocarbons in a continuous flow reactor below 375 degrees C over H-SAPO-34 catalyst via

97 In reactors bioaugmented by Pseudonocardia dioxanivorans CB

98 N2 and H2O at ambient conditions in a single reactor by coupling hydrogen generation from catalytic w

99 from activated sludge in a sequencing batch reactor by maintaining sustained limiting extant nitrite

100 grating hybrid nanocatalysis in microfluidic reactors' by Juan Carlos Colmenares et al., Chem.

101 oparticles and a chemical transient kinetics reactor capable of measurements under non-steady-state c

102 the design and evaluation of a microfluidic reactor capable of synthesizing a single clinical dose o

103 onyl chloride with dibenzylamine in a single reactor coil with an in-line quench is presented.

104 lowing fluorinated amines through sequential reactor coils mediates diazoalkane formation and [3+2] c

105 t can assemble a continuous flow system from reactor coils, syringes, pumps, in-line liquid-liquid se

106 on space, cryofocused, then eluted on a (3)D reactor column for E right harpoon over left harpoon Z i

107 Z) and enantiomeric (R,S) oxime into a third reactor column where isomerization occurs.

108 asal Outcome Test score was higher in severe reactors compared with nonsevere reactors (P = .05).

109 These observations indicate that antenna-reactor complexes may greatly expand possibilities for d

110 This reactor concept is generic in that it offers a viable an

111 bservations and findings, a novel continuous reactor concept is proposed in which the escaping MeBr a

112 Nuclear reactor concepts are not expected to reach the very high

113 etworks operating outside well-stirred batch reactor conditions.

114 ages (0.7 and 0.9 V) using a new rectangular reactor configuration compared to a previous tubular des

115 isms and the effect of synthesis conditions (reactor configuration, precursor and dispersion gas flow

116 s was accomplished with a microphotochemical reactor consisting of a knitted reaction coil and a low-

117 to learn several important skills including reactor construction, charging of a back-pressure regula

118 ighly abundant, whereas the ammonium sulfate reactor contained nitrifiers and heterotrophs capable of

119 minant putative sulfate reducer within these reactors, correlated to representatives of this core mic

120 ectron acceptor in continuously stirred tank reactors (CSTRs) operated over 7 years.

121 trate, the NMR measured water content in the reactor decreased to 76% of its initial value.

122 targets will be consumed at 1 M per day per reactor, demanding a 5000x unit cost reduction to $0.20

123 c)SiO2 catalyst in the H2 permeable membrane reactor demonstrated a stable approximately 30 % C2+ sin

124 Taking advantage of the tube-in-tube reactor design built with semipermeable Teflon AF-2400 t

125 These results show that the new rectangular reactor design, which had increased rates of hydrogen pr

126 g Microtiter Well Plates (MWP) and Drip Flow Reactors (DFR), two models characterized by the absence

127 rent generation in lab-scale electrochemical reactors did not oscillate, but was correlated with carb

128 r substrate-limiting and aerobic pilot-scale reactors directly at a wastewater treatment plant.

129 braries of thousands of unique, miniaturized reactors, droplet microfluidics provides a powerful meth

130 sical processes of CsMP formation inside the reactors during the meltdowns based on atomic-resolution

131 nfluence bacterial community composition and reactor efficacy.

132 alidated by analyzing a variety of different reactor effluents and feeds.

133 engineering, such as substrate, medium, and reactor engineering, can be utilized to improve the effi

134 eering, biocatalytic cascade engineering and reactor engineering.

135 Flow reactors enhance the mass and heat transfer, resulting i

136 erated two laboratory-scale sequencing batch reactors enriched with Candidatus Accumulibacter phospha

137 working temperatures in water-cooled nuclear reactor environments.

138 Using flow-through electrolytic reactors equipped with Ti/IrO2-Ta2O5 mesh electrodes, we

139 Here we present analyses of flow-through reactor experiments showing that dissolved inorganic car

140 on pathways, electrochemical cells and batch reactor experiments with sulfide-pretreated graphite pow

141 Key organisms in the SCN(-) reactor expressed proteins involved in SCN(-) degradatio

142 y 3 kilograms per day using small continuous reactors, extractors, evaporators, crystallizers, and fi

143 riments with a field portable oxidation flow reactor (F-OFR) to study the evolution of emissions over

144 as precipitation of solids ('clogging') and reactor failure.

145 minerals in a fluidized bed crystallization reactor (FBCR).

146 In the lepidocrocite reactors, Fe(II) oxidation by dissolved O2 promotes the

147 ing H2 into or removing H2 from the membrane reactor feed and permeate gas streams.

148 he aqueous phase of anaerobic model landfill reactors filled with carpet or clothing were monitored u

149 bial Fuel Cell as a standalone, self-powered reactor for in situ wastewater electrolysis, recovering

150 ly designed robust and safe laboratory scale reactor for syntheses under sealed-vessel conditions at

151 coal energy delivery, and catalytic membrane reactors for greener chemical synthesis.

152 Biomass was sampled from both reactors for metagenomics and metaproteomics, yielding a

153 ed liquid marbles can act as ideal miniature reactors for photodynamic therapy of cancer cells.

154 ad applicability to using nanoscale chemical reactors for surface redox reactions on the subnanometer

155 ingle-stranded sequencing using microfluidic reactors), for accurate single-cell genome sequencing an

156 protocol for immediate and mild nonimmediate reactors, for both children and adults, with a surveilla

157 Reactors formed two distinct biofilms, one floccular bio

158 on K(g) concentrations in biomass flames and reactor gases, the product of atomic line strength and a

159 The antenna-reactor geometry efficiently harnesses the plasmon reson

160 undance of core microorganisms shared by all reactors (>80% of total community), many of which had li

161 Pla a 3 reactors had both local and systemic food-induced reacti

162 Herein, a hybrid adsorption-periphyton reactor (HAPR), combining a bioadsorbent based adsorptio

163 The reactor has been employed for the methylation of carboxy

164 a potential fuel for next generation nuclear reactor has been subjected to its structural stability i

165 from noble metals to aluminum based antenna-reactor heterostructures in plasmonic photocatalysis pro

166 t embedded aluminum in cuprous oxide antenna-reactor heterostructures that operate more effectively a

167 The choice of the solar reactor holds the key for the commercialization of therm

168 particles to yield a single particle in each reactor; (II) continued particle growth by depletion of

169 of the, thiol-ene based, immobilized enzyme reactor (IMER) is compared to that of a conventional, ag

170 occur during plasma instabilities in fusion reactors impart large heat fluxes onto the surrounding p

171 n incinerated on a bench-scale fluidized bed reactor in a series of experiments under variable condit

172 d the power consumed by a surface DBD-plasma reactor in air at atmospheric pressure.

173 ident Tolerant Fuel in commercially operated reactors in 2020.

174 me measurement of reactions kinetics in bulk reactors in mind, and was checked in terms of linearity,

175 ial plasma-facing material for future fusion reactors in terms of its response to high-flux, low-ener

176 We set up two batches of reactors in which (55)Fe(2+) tracer was added at two dif

177 All of the 167 reactors, including 23 who were classified as severe rea

178 fication of the process in a continuous-flow reactor increases the products' yields up to quantitativ

179 c acid concentrations downstream of the flow reactor indicates that the secondary products formed on

180 Both reactors inoculated with either suspended or immobilized

181 d final removal rates did not differ between reactors inoculated with immobilized and suspended cells

182 The membrane reactor is composed of a mixed ionic-electronic SrCe0.7

183 Fusion reactor is one of the most ideal energy resources to def

184 ncy over the ozone generated by a DBD-plasma reactor is studied by varying the frequency in the range

185 , the scale-up potential for continuous-flow reactors is described.

186 For both soils, the activity of BES reactors is moderately imaged by the inverted conductivi

187 at occur in mixed-species bioelectrochemical reactors, like microbial fuel cells (MFCs), make accurat

188 In batch reactors, LMG-N2-G was transformed, following pseudo-fir

189 monium oxidation in membrane-aerated biofilm reactors (MABRs) can make treatment of ammonium-rich was

190 tewater treatment (e.g., moving bed biofilms reactors-MBBRs) biofilm thickness is typically not under

191 liquor through the use of a membrane biofilm reactor (MBfR), with methane supplied through hollow fib

192 rypsin/Lys-C enzyme-immobilized multichannel reactor (MCR) consisting of 126 channels (8 mum inner di

193 open cultures of microbial consortia (i.e., reactor microbiomes) under anaerobic conditions is being

194 ion times are short relative to typical bulk reactor mixing times.

195 hen sequentially modified through additional reactor modules performing N-alkylation and arylation, d

196 ion metal-based catalysts, known as 'antenna-reactor' nanostructures, holds promise to expand the sco

197 cumulation of nitrite and nitrate within the reactor, observed midway through the experimental proces

198 from a diesel engine using an oxidation flow reactor (OFR).

199 droplet manipulation, 3D cell culture, micro reactor, oil spill clean-up, and oil/water separation.

200 h experiments using laboratory-scale biofilm reactors operated under aerobic and anaerobic conditions

201 Reactor operation shows that the maximum power density o

202 gs confirmed (14)C discharges during routine reactor operations, whereas those activities that were i

203 ee," 18 (45%) had at least 1 fragrance cross-reactor or botanical ingredient.

204 llin G acylase in miniaturized stirred batch reactors or continuous flow microreactors.

205 r in severe reactors compared with nonsevere reactors (P = .05).

206 It was demonstrated that mutual shading of reactor panels has a decisive effect on the reactor temp

207 eristic or microbial community structure and reactor performance have not been able to be directly es

208 dynamics of ammonia oxidizing organisms and reactor performance in synthetic fully hydrolyzed urine

209 t incorporated biotic interactions predicted reactor performance outcomes more accurately than those

210 on characteristics, biofilm communities, and reactor performance.

211 the onset of cathode biofouling and improved reactor performance.

212 shly grown cells or starved cells to explain reactor performance.

213 e MCRs allowed for repeatable within/between-reactor preparation and performance.

214 articles originating from the failure of the reactor pressure vessels.

215 in MP medium maintained neutral pH in the MP reactor preventing caustic addition and thus salt accumu

216 Oscillatory flow reactors provide a surface energy-driven approach for au

217 oreactors receives a lot of attention as the reactor provides enhanced heat and mass transfer charact

218 ntainment regime behaves as a leaky chemical reactor regarding its effect on isotopic evolution intro

219 demonstrates that carbonation in BCA-amended reactors remained limited by CO2 supply, implying furthe

220 Both reactors removed more than 85% of the total inorganic ni

221 systems, examined within well-stirred batch reactors, represent conceptual and practical frameworks

222 While aerogel formation in FC-CVD reactors requires a catalyst (typically iron, Fe) and a

223 eic acid isolation membrane is placed at the reactor's inlet, and paraffin-encapsulated reagents are

224 When the amplification reactor's temperature increases to its operating level,

225 e activated sludge from the sequencing batch reactor (SBR) receiving synthetic domestic wastewater wa

226 vestigated in two lab-scale sequencing batch reactors (SBRs), using bisphenol A (BPA) as the TOrC.

227 o process considerations such as solvent and reactor selection.

228 tions (<5 min at 90 degrees C) and a similar reactor setup as for the amination.

229 Silanated reactors showed low antibody adsorption in comparison to

230 The results from lab-scale methanogenic reactors showed that this step accounts for much of the

231 After 200h of continuous use in a fixed-bed reactor, SiQT10 remained with approximately 90% activity

232 supported by a multi-prong quartz fork, the reactor size limit could be overcome by extending the su

233 e in the new device and a standard microwave reactor suggest that results obtained using microwave co

234 of Sphingobium sp. BiD32 was observed in the reactors, supporting the original hypothesis that contin

235 roteins were arrayed as ordered zones on the reactor surface allowing segregation of catalysts.

236 reviews practical implementations of plasma reactors, surveys the materials that have been produced

237 ococcoides populations in a continuously fed reactor system under changing chloroethene/ethane influe

238 nd pressures using a novel pressurized batch-reactor system with dual spectroscopic detectors: a near

239 of both the gas and liquid flowing into the reactor system.

240 ion temperature, detailed information on the reactor temperature as a function of time and geographic

241 reactor panels has a decisive effect on the reactor temperature.

242 roach for the production of bespoke chemical reactors, termed reactionware, using two different appro

243 o tune the conversion: three-hour-long batch-reactor tests conducted at 150 degrees Celsius, using ei

244 d, a multifunctional enzymatic amplification reactor that combines solid-phase nucleic acid extractio

245 We developed a microfluidic reactor that physically separates Geobacter sulfurreduce

246 y element production in the unique high flux reactors that operated at the Savannah River Site, USA (

247 To meet the design requirements of fusion reactor, the development of the structural materials whi

248 The O2 supplied to the reactor, the influence of the pH, the concentration of m

249 For coffee roasted in a spouted bed reactor, the summation of the 16 PAHs ranged from 3.5 to

250 s used for carrying the generated CO2 out of reactor, the total amount of CO2 released was improved b

251 mpling, the manufacture of the designed flow reactors, the enzyme immobilization procedure, and the o

252 For carpet and clothing reactors, the majority of PFAS release was not measured

253 In the SCN(-) reactor, Thiobacillus strains capable of SCN(-) degradat

254 Overall loss of activity in the reactors though was due to starvation, and final removal

255 ved performance was produced by coupling the reactor to a longer separation capillary ( approximately

256 Here, we have developed a microfluidic flow reactor to measure growth rates directly and accurately

257 mination results (phenotype 1); ii) positive reactors to the skin test regardless of post-mortem exam

258 d to three bTB indicator traits: i) positive reactors to the skin test with positive post-mortem exam

259 s in (ii) plus non-reactors and inconclusive reactors to the skin tests with positive post-mortem exa

260 away from traditional spatially homogeneous reactors towards dynamic and non-equilibrium conditions,

261 prototype lab-scale CANDO+P sequencing batch reactor treating synthetic municipal wastewater, we obse

262 nitrification at low pH has been reported in reactors treating human urine, but it has been unclear w

263 e of 21-28 degrees C and 0.4-5.9 s in a flow reactor under dry conditions and in the presence of 3 x

264 re run for 52 consecutive weeks as semibatch reactors under variable environmental conditions.

265 depletion of the remaining precursor in the reactor until the particle reaches a stable size.

266 section and volume of the microphotochemical reactor used in this study was optimal to reach a sensit

267 e was experimentally verified in a flow cell reactor using a pair of carbon electrodes (10(2) cm geom

268 We benchmark our reactor using an aqueous-phase oxidation reaction: iron-

269 ich micro-particle (CsMP), formed inside the reactors via unknown processes.

270 tive microwave irradiation steps in the same reactor vial, avoiding the need for additional reaction

271 Estimated ion exchange reactor volumes to capture the nitrogen for 1 week from

272 obilized form than in the free one, when the reactor was applied in real white and red wine.

273 Subsequently, a bench-scale fluidized-bed reactor was developed, applying the optimized process co

274 A second reactor was fed ammonium sulfate to mimic breakdown prod

275 A Knudsen flow reactor was used to carry out the experiments under mole

276 The average desensitization duration among reactors was 1.67 days, and the average duration for gas

277 nd the average duration for gastrointestinal reactors was 2.29 days.

278 The community composition of both the reactors was also investigated to identify the presence

279 Release in live carpet reactors was primarily due to 5:3 fluorotelomer carboxyl

280 d lepidocrocite, whereas in the ferrihydrite reactors we observe a decrease in magnetite stoichiometr

281 nt contaminant concentration in flow-through reactors, we show that electrochemical oxidation is a vi

282 transmembrane pressures for the rectangular reactor were only 0.10 bar (0.7 V) or 0.05 bar (0.9 V) a

283 dominant flanking community members in both reactors were affiliated with the phyla Anaerolinea, Ign

284 The reactors were operated with 8 cycles per day and at two

285 a a 1, nPla a 2, and rPla a 3 ImmunoCAP ISAC reactors were studied.

286 Six 5.0-L fill-and-draw batch reactors were used with different feed compositions cont

287 , including 23 who were classified as severe reactors, were successfully desensitized in the outpatie

288 assing the fresh SOA through a photochemical reactor where it reacted with hydroxyl radicals.

289 s more pronounced close to the outlet of the reactor, where higher pH2O is anticipated.

290 successfully adapted into a continuous flow reactor which is applicable for large-scale chemical ind

291 thylformamide (DMF) in a continuous membrane reactor which retains the catalyst.

292 as chromatography using an innovative saliva reactor, which imitated human chewing under temperature

293 The Wisconsin High Pressure NMR Reactor (WiHP-NMRR) has enabled the observation of chang

294 , and (III and IV) continuously stirred-tank reactor with 6.25-10 min hydraulic retention times and c

295 ly efficient 3D wood-derived carbon monolith reactor with a low tortuosity is demonstrated for high-t

296 e for the first time by using a novel plasma reactor with a water electrode.

297 The apparatus consists of a titanium reactor with quartz windows, near-infrared and UV spectr

298 nt and gene expression in a granular anammox reactor with the objective of understanding the molecula

299 .5 times faster than in bioaugmented control reactors without an applied potential, and 12 times fast

300 t and potentially next generation of fission reactors worldwide.