ライフサイエンスコーパス: COD

1 COD was also consumed during the process, but heterotrop

2 cular nucleation" in which 2(COD)Ir(+) and 1(COD)Ir.POM(8-) yield the transition state of the rate-de

3 rs catalyzed by the combination of Ni(COD)2 (COD = 1,5-cyclooctadiene) and an N-heterocyclic carbene

4 le ligands and Ru3(CO)12 or Ru(methylallyl)2(COD) direct hydroformylation and hydrogenation of alkene

5 ernative termolecular nucleation" in which 2(COD)Ir(+) and 1(COD)Ir.POM(8-) yield the transition stat

6 Treatment of 1 with [Ir(COD)Cl](2) (COD = 1,5-cyclooctadiene) afforded 1-[Ir(COD)Cl], a comp

7 e dimeric complexes 1, [R(3)Si(mu-Cl)(eta(2)-COD)Pt](2) [R(3)Si = Et(3)Si, MeCl(2)Si, Me(2)ClSi, "(Et

8 Exchange of the 1,3-COD ligand by PMe3 led to [Si(II)(Xant)Si(II)]Ni(PMe3)2,

9 low isomerization to 1,3-cyclooctadiene (1,3-COD), along with the formation of a new complex that inc

10 he catalytic isomerization of 1,5-COD to 1,3-COD, only in the case of the zinc species is the cyclooc

11 ansfer from [2,5-Ph(2)-3,4-Tol(2)(eta(5)-C(4)COD)]Ru(CO)(2)D to N-aryl imines to give amine complexes

12 ene], and the bis-silyl complexes 2, (eta(4)-COD)Pt(SiR(3))(2) (R(3)Si = Cl(3)Si, MeCl(2)Si, Me(2)ClS

13 etent for the catalytic isomerization of 1,5-COD to 1,3-COD, only in the case of the zinc species is

14 etallic complex with 1,5-cyclooctadiene (1,5-COD) results in slow isomerization to 1,3-cyclooctadiene

15 n reveals closely analogous, solution Ir(1,5-COD)(+) or Ir(1,5-COD)Cl-mediated, mechanisms of nanopar

16 lly and mechanistically well-studied, Ir(1,5-COD).P(2)W(15)Nb(3)O(62)(8-) to Ir(0)(~300).(P(2)W(15)Nb

17 nanoparticle growth pathway involving Ir(1,5-COD)Cl(solvent) and Ir(0)(n) in solution.

18 cle formation mechanism consisting of Ir(1,5-COD)Cl(solvent) dissociation from the gamma-Al(2)O(3) su

19 ased nucleation from that dissociated Ir(1,5-COD)Cl(solvent) species, fast Ir(0)(n) nanoparticle capt

20 rom Ir(0)(n)/gamma-Al(2)O(3) and with Ir(1,5-COD)Cl(solvent), the first kinetically documented mechan

21 analogous, solution Ir(1,5-COD)(+) or Ir(1,5-COD)Cl-mediated, mechanisms of nanoparticle formation.

22 e system explored is the precatalyst, Ir(1,5-COD)Cl/gamma-Al(2)O(3) (characterized via ICP, CO adsorp

23 Significantly, the Ir(1,5-COD)Cl/gamma-Al(2)O(3) + H(2) --> Ir(0)(n)/gamma-Al(2)O(

24 ion and growth pathway involving only Ir(1,5-COD)Cl/gamma-Al(2)O(3) and also disprove a solution-base

25 x 10(4) h(-1) M(-1)), where A is the Ir(1,5-COD)Cl/gamma-Al(2)O(3) precatalyst and B is the resultan

26 formation kinetics, starting from the Ir(1,5-COD)Cl/gamma-Al(2)O(3) precatalyst, are closely fit by t

27 e development of a well-characterized Ir(1,5-COD)Cl/gamma-Al(2)O(3) precatalyst, which, when in conta

28 The kinetics of the Ir(1,5-COD)Cl/gamma-Al(2)O(3) to Ir(0)(~900)/gamma-Al(2)O(3) co

29 stic studies allow comparisons of the Ir(1,5-COD)Cl/gamma-Al(2)O(3) to Ir(0)(~900)/gamma-Al(2)O(3) su

30 is central question for the prototype Ir(1,5-COD)Cl/gamma-Al(2)O(3) to Ir(0)(~900)/gamma-Al(2)O(3) sy

31 e gamma-Al(2)O(3) support (i.e., from Ir(1,5-COD)Cl/gamma-Al(2)O(3)), solution-based nucleation from

32 onstant k4), where A is nominally the Ir(1,5-COD)Cl/gamma-Al2O3 precursor, B the growing Ir(0) partic

33 ystem of H2 reduction of the precursor [(1,5-COD)Ir x P2W15Nb3O62](8-).

34 uster preparations from five different [(1,5-COD)Ir(+)]n [anion(n-)] precursors.

35 le catalyst precursor, [A] = [(Bu4N)5Na3(1,5-COD)Ir(I).P2W15Nb3O62], forming soluble/dispersible, B =

36 ately 300 nanoparticles from (Bu4N)5Na3[(1,5-COD)Ir.P2W15Nb3O62] (abbreviated hereafter as (COD)Ir.PO

37 imum coulombic efficiency of 26.87% with 91% COD removal was achieved.

38 The coupling of a COD platform to a droplet absorbance detection set-up re

39 of 39%, a n-butyrate yield of 23% (both on a COD basis), a maximum total fermentation production rate

40 in, we describe the implementation of such a COD platform to perform high precision nanoliter assays.

41 parent second-order in the precatalyst, A = (COD)Ir.POM(8-), not the higher order implied by classic

42 e morphologically important faces of COM and COD.

43 ely offset annual freshwater consumption and COD discharge driven by per capita GDP growth, but that

44 ge percent error of Coulombic efficiency and COD removal rate predictions were 1.77 +/- 0.57% and 4.0

45 olid samples, with high suspended solids and COD concentrations, using an optimized closed reflux col

46 l oxygen demand (COD)/L (16% of total SMP as COD) because many SMPs have considerably higher MWs.

47 D)Ir.P2W15Nb3O62] (abbreviated hereafter as (COD)Ir.POM(8-), where POM(9-) = the polyoxometalate, P2W

48 near molecular level, for poorer adhesion at COD crystal faces, which explains the benign character o

49 Metabolic modeling analysis shows that at COD:N of 4:1 the denitrifying cells slowly generate elec

50 study was 0.82 mg CH(3)OH COD/mg AOB biomass COD-d, which is 1.5 times the highest value reported wit

51 In addition, TEA-soy sizes had a BOD5/COD ratio of 0.44, much higher than 0.03 for PVA, indica

52 leophilic attack of water to the metal-bound COD.

53 The bound COD participates in C-H activation by capturing the hydr

54 H-transfer rather than Si-transfer to bound COD provides experimental support for the sequence of in

55 catalyst, (dfmpe)Ni(COD) and (dfmpe)Ni(bpy), COD = 1,5-cyclooctadiene and bpy = 2,2'-bipyridine, were

56 used in place of Ni(COD)2/SIPr.HBF4/KO(t)Bu (COD = 1,5-cyclooctadiene) as a more robust catalyst for

57 l rate of cholesterol oxidation catalyzed by COD was investigated at 37 degrees C using cholesterol/1

58 The initial rate of cholesterol oxidation by COD in fluid state 1-palmitoyl-2-oleoyl-phosphatidyletha

59 cyclochiral conformers of the Ir(I) chelated COD was 5 kcal mol(-1) higher as an included organometal

60 iral twisted-boat conformers of the chelated COD included in the already chiral cavity of the contain

61 lude the structurally characterized complex (COD)Pt(OTf)2 (1) and the known dimer [PtCl2(C2H4)]2, act

62 At saturating acetate concentrations (COD>164 ppm), the miniature SCMFC could rapidly detect t

63 Voided urine, however, often contains COD in the form of single micron-sized crystals.

64 oxygen demand) in effluent water, cumulative COD and dilution water requirements for cumulative pollu

65 or heteroleptic L2.Ir(I).1,5-cyclooctadiene (COD) complexes included in the aromatic cavity of Rebek'

66 An inhibitory role of 1,5-cyclooctadiene (COD) in nickel-catalyzed C-H functionalization processes

67 Oxygenation of 1,5-cyclooctadiene (COD) is achieved on an iridium center using water as a r

68 ination of bulk catastrophic optical damage (COD) due to locally high energy densities, heliotropic C

69 Network (SGN) is a clade-oriented database (COD) containing biological data for species in the Solan

70 Network (SGN) is a clade-oriented database (COD), which provides a more scalable and comparative fra

71 For 35 days, COD levels at the culvert outlets and downstream ranged

72 scan with lung cancer as the cause of death (COD) documented by the NLST endpoint verification proces

73 The decreased COD adsorption for p-nitrophenol at higher anodic potent

74 ting such droplets in compartment-on-demand (COD) platforms is the basis for rapid, automated screeni

75 es of chemical and biological oxygen demand (COD and BOD) in the aquatic systems into which they are

76 l elimination rates (chemical oxygen demand (COD) 90-95%, biological oxygen demand (BOD5) 94-98%, tot

77 reatment efficiency (chemical oxygen demand (COD) and ammonia removal), Ag dissolution measurements,

78 an 95% reductions in chemical oxygen demand (COD) and ammonium ion were achieved within 6 h.

79 7-day Pb toxicity to chemical oxygen demand (COD) and NH3-N removal, bacterial viability, and communi

80 only 10% of influent chemical oxygen demand (COD) and recovered up to 55% of incoming organic matter

81 MFCs removed 65-70% chemical oxygen demand (COD) at a hydraulic retention time (HRT) of 11 h and red

82 determination of the chemical oxygen demand (COD) in heterogeneous solid or semisolid samples, with h

83 y contribute to high chemical oxygen demand (COD) in textile effluents.

84 he rapid analysis of chemical oxygen demand (COD) in urban waste waters.

85 cted as a sensor for chemical oxygen demand (COD) in water.

86 e pH was 6.2 and its chemical oxygen demand (COD) level was 36,000 ppm.

87 te solution having a chemical oxygen demand (COD) of 320 mg/L.

88 anic carbon (TOC) or chemical oxygen demand (COD), though these parameters do not provide information

89 d for only 2.1 mg of chemical oxygen demand (COD)/L (16% of total SMP as COD) because many SMPs have

90 ubilization (0.16 mg chemical oxygen demand (COD)/mg volatile solids (VS), at 2.13 mg HNO2-N/L) being

91 ohydrate (COM) or calcium oxalate dihydrate (COD).

92 MOF-supported [Rh(dppe)(COD)]BF4 catalyzes the hydrogenation of 1-octene to n-oc

93 aic (PV) panel, which was shown to eliminate COD and total coliform bacteria in less than 4 h of trea

94 The estimated COD values in the samples were compared with those provi

95 l explained by chosen environmental factors (COD, nitrite-N, nitrate-N, dissolved inorganic phosphoru

96 The current efficiency for COD removal was 12% with the lowest specific energy cons

97 n (in the presence of a small excess of free COD).

98 -1) and n-butyrate production rate of 0.47 g COD l(-1) d(-1) in bioreactors that were fed with dilute

99 total fermentation production rate of 0.74 g COD l(-1) d(-1) and n-butyrate production rate of 0.47 g

100 3.38 +/- 0.42 g L(-1) d(-1) (7.52 +/- 0.94 g COD L(-1) d(-1)) with an n-caproate yield of 70.3 +/- 8.

101 H2 yield varied from 0.26 to 0.42 g H2-COD/g COD removed in the anode, and the bioanode volume-normal

102 ciency in the two-phase system were 228 mL/g COD added and 77.8%, respectively, which were 1.6 and 2.

103 The H2 yield varied from 0.26 to 0.42 g H2-COD/g COD removed in the anode, and the bioanode volume-

104 o locally high energy densities, heliotropic COD growth, solid-liquid-gas phase transformations, stro

105 afluoropentan-2,4-dionatocopper(I) (Cu(hfac)(COD)) to yield 1,1,1,5,5,5-hexafluoropentan-2,4-dione (H

106 synthesized, and their cationic [rhodium(I)(COD)] complexes were prepared.

107 e type Rh(I)(NHC)(COD)X (where X is Cl or I, COD is cyclooctadiene, and NHC is a dimethylbenzimidazol

108 A similar biphasic change in COD activity was detected at the critical sterol mole fr

109 Subsequent stepwise reduction of influent COD caused a decrease in total polysaccharide and protei

110 The NO2(-) spiked cultures with an initial COD:N = 11:1 accumulated 3.3 +/- 0.57% of the total nitr

111 atch cultures under four conditions: initial COD:N ratios of 11:1 and 4:1 with and without nitrite sp

112 trates and 1 as the catalyst, intermediate [(COD)Pt(norbornene)2][OTf]2 (3) was identified and charac

113 Treatment of 1-[Ir(COD)Cl] with CO afforded the carbonyl complex 1-[Ir(CO)(

114 2) (COD = 1,5-cyclooctadiene) afforded 1-[Ir(COD)Cl], a complex with bond lengths and angles that wer

115 n of B(2)pin(2) with arenes catalyzed by [Ir(COD)(OMe)](2) and dtbpy occur faster with electron-poor

116 ion of complex 4a with the metal complex [Ir(COD)Cl]2 affords a heterobimetallic Zr/Ir product 14.

117 This complex is formed in low yield from [Ir(COD)(OMe)](2), dtbpy, COE, and B(2)pin(2).

118 independent synthesis in high yield from [Ir(COD)(OMe)](2), dtbpy, COE, and HBpin.

119 the active catalyst to be generated from [Ir(COD)Cl]2 and P(OPh)3 by cyclometalation of the phenyl gr

120 zed by an iridium complex generated from [Ir(COD)OMe]2 and chiral dinitrogen ligands that we recently

121 hydrogenation of 20 with the complex of [Ir(COD)2BArF] (26) and Taniaphos ligand P afforded the (3R,

122 ,N-ligand (MeO-BoQPhos) with 1000 ppm of [Ir(COD)Cl]2.

123 he combination of (eta(6)-mes)IrBpin3 or [Ir(COD)OMe]2 and a phenanthroline derivative is reported.

124 tsynthetic metalation of these MOFs with [Ir(COD)(OMe)]2 provided Ir-functionalized MOFs (BPV-MOF-Ir,

125 Treatment of 1 with [Ir(COD)Cl](2) (COD = 1,5-cyclooctadiene) afforded 1-[Ir(COD

126 arbene adducts with [M(COD)Cl]2 (M = Rh, Ir; COD = 1,5-cyclooctadiene) afforded zwitterionic rhodium(

127 The Crabtree catalyst (Ir[COD]PyPCy(3)PF(6)) proved to be highly effective in dias

128 Immobilization of [IrCl(COD)(IMes)], [IMes=1,3-bis(2,4,6-trimethylphenyl), imida

129 The zwitterionic iridium-COD complexes were tested as catalysts for the homogeneo

130 he COD loading increased from 0.39 to 1.1 kg COD/m(3)-d.

131 c loading rate increased from 0.39 to 1.1 kg COD/m(3)-d.

132 with minimal energy consumption (370 kWh/kg COD and 383 kWh/kg NH4(+)).

133 ve a minimum energy consumption of 62 kWh/kg COD, reduced foam formation due to less gas bubble produ

134 ns of ML4 (M = Pt, Pd, L = PPh3; M = Ni, L2= COD) and 2,2,2-crypt to give M@Pb12(2-) cluster anions (

135 iridium(I) complexes of the type [(WCA-NHC)M(COD)], in which the metal atoms exhibit an intramolecula

136 he resulting lithium-carbene adducts with [M(COD)Cl]2 (M = Rh, Ir; COD = 1,5-cyclooctadiene) afforded

137 imes that without FNA pretreatment (0.025 mg COD/mg VS, at 0 mg HNO2-N/L).

138 ntinuous bioreactor, up to 59.89 +/- 1.12 mg COD/L of CH(3)OH was produced within an incubation time

139 showed a biodegradation capacity of 1.45 mg COD/gramwet-day at a TDS concentration of 91,351 mg/L.

140 0.33 +/- 0.14 mg-O2/L, and 0.14 +/- 0.02 mg-COD/mg-N, respectively.

141 itudinal phonon cooling effect on the molten COD wave front, and the formation of patterns due to las

142 Complexes of the type Rh(I)(NHC)(COD)X (where X is Cl or I, COD is cyclooctadiene, and NH

143 In addition, 2b/Ni(COD)(2) was utilized to synthesize a series of pseudo-tr

144 This was followed by a Ni(COD)(2)-mediated cyclization to set up the stereocenter

145 tanamidato]-Ni(eta1 -CH2Ph)(PMe3) (1) and Ni(COD)2 (bis(1,5-cyclooctadiene)-nickel) (2).

146 As20]3- ion was prepared from As7(3-) and Ni(COD)2 in ethylenediamine solutions and isolated as the B

147 ioselectivities up to 99% ee catalyzed by Ni(COD)(2) and (R)-DIFLUORPHOS.

148 tive cleavage of C-OMe bonds catalyzed by Ni(COD)(2)/PCy(3) with silanes as reducing agents is report

149 By using optimized reaction conditions, Ni(COD)(2)/PCy(3) was shown to be a versatile catalyst for

150 In contrast, Ni(COD)2-iPrPHOX-catalyzed anhydride alkylation proceeds th

151 ated with nickel bis(1,5-cyclooctadiene) (Ni(COD)(2)), 2a and 2b are capable of polymerizing ethylene

152 Although 3 decomposes Ni(COD)2, if the initiating species (1/2) are exposed to et

153 Two candidates for a precatalyst, (dfmpe)Ni(COD) and (dfmpe)Ni(bpy), COD = 1,5-cyclooctadiene and bp

154 d from allyl 2-diphenylphosphinobenzoate, Ni(COD)2, and (C6F5)3B.

155 ysts showed that the combination of DPPF, Ni(COD)(2), and acid is a highly active catalyst system for

156 or C-aryl glycosides, reactions employing Ni(COD)2/(t)Bu-Terpy in N,N-dimethylformamide (DMF) were ty

157 l-silicide colloids were synthesized from Ni(COD)(2) and octylsilane at low temperature; they were su

158 perior to those of catalysts derived from Ni(COD)2.

159 to 99% ee catalyzed by the combination of Ni(COD)(2) and (R)-BINAP and the coupling of ketones with a

160 A catalytic system comprised of Ni(COD)(2) and 1,1'-bis(diphenylphosphino)ferrocene (DPPF)

161 the first time using catalytic amounts of Ni(COD)(2), an N-heterocyclic carbene ligand, and PPh(3).

162 The reaction of Ni(COD)(2), IPr, and nitrile affords dimeric [Ni(IPr)RCN](2

163 yl ethers catalyzed by the combination of Ni(COD)2 (COD = 1,5-cyclooctadiene) and an N-heterocyclic c

164 s could be obtained by the combination of Ni(COD)2/PyBox in DMF (>20:1 alpha:beta).

165 idazolidin-2-ylidene) is used in place of Ni(COD)2/SIPr.HBF4/KO(t)Bu (COD = 1,5-cyclooctadiene) as a

166 bstituents can be obtained by an ordinary Ni(COD)2-promoted, Yamamoto-type coupling reaction.

167 the well-defined soluble nickel precursor Ni(COD)(2) or Ni(CH(2)TMS)(2)(TMEDA) in the presence of a b

168 Ar(Mes2)]2, and the d(10) Ni(0) precursor Ni(COD)2, produces a porous metal-organic material featurin

169 In the presence of a phosphine scavenger, Ni(COD)2, the phosphine-ligated syn-dinickel complexes copo

170 Reaction conditions for the Ni(COD)(2)/PCy(3) catalyzed cross-coupling of aryl neopenty

171 Results from a mechanistic study on the Ni(COD)2-bipy-catalyzed alkylation of anhydrides are consis

172 silylene) nickel complex 5 [{(LSi)2P(TMS)}Ni(COD)], was obtained.

173 lyst can be utilized as an alternative to Ni(COD)(2)/PCy(3) to provide an inexpensive, robust, and co

174 om deltahedral clusters of germanium with Ni(COD)2 and/or Ni(PPh3)2(CO)2 in ethylenediamine yielded t

175 equired for catalysis when conducted with Ni(COD)2 in the same reaction system.

176 as the Bu4P+ salt (As, arsenic; Ni, nickel; COD, cyclooctadiene; Bu, butyl; P, phosphorus).

177 mol % cholesterol), the initial activity of COD changed with cholesterol mole fraction in a biphasic

178 These results indicate that the activity of COD is regulated by the extent of sterol superlattice fo

179 aces, which explains the benign character of COD and has implications for resolving one of the myster

180 cation of this approach for the detection of COD online and in continuous mode, the CuO/AgO-based nan

181 Of the 29 patients with a diagnosis of COD/CORD, four mutations were identified in the ORF15 mu

182 hat is, freshwater consumption, discharge of COD (chemical oxygen demand) in effluent water, cumulati

183 D)Cl(2) in the presence of a small excess of COD.

184 A), which were 239 +/- 74 and 89 +/- 7 mg of COD per gram of active biomass (Xa) per hour, respective

185 ow 2-D lipid composition window, an onset of COD activity at X(CHOL) approximately 0.40 and the elimi

186 Removal of COD was >95% at all applied voltages tested.

187 indicating its potential for the sensing of COD in clinical samples and pharmaceutical formulations.

188 trocatalytic response towards the sensing of COD with a wide linear response range of 2.0 x 10(-8)-2.

189 Between 1992 and 2007, 225 million tones of COD accumulated in Chinese water bodies, which would req

190 tained during this study was 0.82 mg CH(3)OH COD/mg AOB biomass COD-d, which is 1.5 times the highest

191 he methane yield was 2.40 +/- 0.52% based on COD and was limited by the availability of carbon dioxid

192 oate/ethanol ratio of 1.19 +/- 0.15 based on COD for a period of approximately 55 days.

193 The present work on COD and the previous study on phospholipase A(2) (sPLA(2

194 o date, of simplex males affected with RP or COD/CORD.

195 Storage played a minor role in the overall COD removal, which was likely dominated by aerobic bioma

196 C by using an improved cholesterol oxidase (COD) activity assay.

197 mined using a bacterial cholesterol oxidase (COD) as a model.

198 sed using soil bacteria cholesterol oxidase (COD) as a model.

199 ed at 37 degrees C by a cholesterol oxidase (COD) reaction rate assay and by optical microscopy.

200 l as to global organic pollution parameters (COD, BOD, and TOC).

201 e sensitive and selective codeine phosphate (COD) determination in the presence of paracetamol (PAR)

202 ctroanalytical sensing of codeine phosphate (COD).

203 H)2, 1, was obtained from the reaction of Pt(COD)2 and Bu(t)3SnH, followed by addition of CNBu(t).

204 The reaction of Pt(COD)2 with Bu(t)3SnH and CO gas afforded trans-Pt(SnBu(t

205 , 5, can be prepared from the reaction of Pt(COD)2 with Mes3SnH and CNBu(t).

206 sponding hydrosilanes, respectively, with Pt(COD)Cl(2) in the presence of a small excess of COD.

207 The recorded COD values of both the sensor and the standard method we

208 [((S,S)-Ph-5-Fc)Rh(COD)]BF4 showed high activity with low selectivity for t

209 [((S,S)-Ph-Quinox)Rh(COD)]BF4 showed high activity and selectivity against it

210 key step in the sequence was the Burk's [Rh(COD)(2R,5R)-Et-DuPhos]BF4-catalyzed asymmetric hydrogena

211 +) BF(4)(-)) followed by reaction with Rh(+)(COD)(2) BF(4)(-) gave precatalysts with limited aqueous

212 um catalysts such as [RhCl(PPh3)3] or [[RhCl(COD)]2] with PiPr2(OAr) or P(NMe2)3 co-catalysts allows

213 for substrates without 2-substitution [[RhCl(COD)]2]/P(NMe2)3 mixtures tend to give better results.

214 utility and selectivity of the catalyst [Ru(COD)(L(1))Br2] (1) bearing a fused pi-conjugated imidazo

215 complexes, such as Cp*RuCl(PPh 3) 2, Cp*RuCl(COD), and Cp*RuCl(NBD), were among the most effective ca

216 nce of catalytic Cp*RuCl(PPh 3) 2 or Cp*RuCl(COD), primary and secondary azides react with a broad ra

217 tO)(3)Si", PhMe(2)Si, and (Me(3)SiO)Me(2)Si; COD = cycloocta-1,5-diene], and the bis-silyl complexes

218 he cumulative methane production and soluble COD (SCOD) removal efficiency in the two-phase system we

219 These test results show that COD and NH4(+) can be removed after 2 h of electrolysis

220 This suggests that COD formation protects against stone disease because of

221 The COD reaction rate assay showed a sharp increase in chole

222 The COD removal rates were about 0.4 (total) or 0.2 (soluble

223 At X(PE) = 0, the COD activity changed abruptly at X(CHOL) approximately 0

224 At a fixed X(CHOL) of 0.50, the COD activity increased progressively with PE content and

225 by an acoustic phonon bouncing model and the COD velocity is extrapolated to be exponentially decreas

226 A (n = 12) were cases of lung cancer as the COD because of adenocarcinoma, and group B (n = 15) were

227 Frequency of lung cancer as the COD because of NSN and the time from randomization to di

228 B (n = 15) were cases of lung cancer as the COD because of other cell types.

229 nsfer rate increased by almost 5-fold as the COD loading increased from 0.39 to 1.1 kg COD/m(3)-d.

230 had one or more NSNs, and lung cancer as the COD occurred for 48 participants.

231 likely that patients with lung cancer as the COD occurred with solitary or dominant NSN as long as an

232 he remaining 10 patients, lung cancer as the COD was not because of NSN.

233 d (DI) water included reduction to below the COD detection limit after 60 min heating (90()C) with ad

234 in 16:0,18:1-PC and di18:1-PC bilayers, the COD initial-reaction rate displays a series of distinct

235 A decline in the COD reaction rate was found after the formation of chole

236 For the first time the COD propagation is analyzed temporally by an acoustic ph

237 of total methane increased linearly with the COD loading rate, the concentration of dissolved methane

238 Although free radical species contribute to COD removal, anodes designed to enhance reactive chlorin

239 with magnesium sulfate (MgSO(4)) previous to COD determination.

240 activity of reactive chlorine species toward COD with an increasing chloride ion concentration under

241 rating at peak power, the rate of wastewater COD removal, normalized to reactor volume, was 30-50 tim

242 While COD and ammonia removal decreased by as much as 30% or g

243 ta-oxidation of saturated fatty acids, while COD:N of 11:1 do it through the TCA cycle.

244 comparison, the NO2(-) spiked cultures with COD:N = 4:1 showed significantly higher (p = 0.028) N2O

245 hen the substrate is a sterol, as it is with COD, the enzyme activity reaches a local maximum at C(r)

246 th biological and filtration processes, with COD removal rates in the range 85-95%.

247 method suitable for complex substrates with COD levels ranging from 5 to 2500 g O(2) kg(-1) TS.

248 -1,3-bis(trimethylsilyl)propene reacts with (COD)2Ni to produce the dimeric purple complex {[1,3-(SiM

249 2,4,6-trimethylphenyl), imidazole-2-ylidene; COD=cyclooctadiene] catalyst onto silica particles modif