ライフサイエンスコーパス: COD

1 COD was also consumed during the process, but heterotrop

2 COD was classified as being a result of lymphoma, other

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

4 ers(added) at no food waste, to 152 L kg(-1) COD fibers(added) at 29% food waste, an increase of 190%

5 he fiber mixture from a low of 52.7 L kg(-1) COD fibers(added) at no food waste, to 152 L kg(-1) COD

6 , and the methane yield reached 225 L kg(-1) COD(added) at 29% food waste on a COD basis, with a soli

7 , by grafting [(COD)Pt(OSi(OtBu)(3))(2)] (1, COD = 1,5-cyclooctadiene) on partially dehydroxylated si

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

9 chemical oxygen demand (COD) of 100 +/- 2% (COD(out)/COD(in)).

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

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

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

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

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

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

16 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

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

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

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

20 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

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

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

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

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

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

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

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

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

29 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

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

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

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

33 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

34 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

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

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

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

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

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

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

41 ee's catalyst ([(COD)Ir(py)(PCy(3))][PF(6)], COD = 1,5-cyclooctadiene, py = pyridine, Cy = cyclohexyl

42 While 78% Cr(VI), 91% Fe(III), 91% COD, 89% BOD and 73% Chloride were removed by kaolin und

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

44 mum removal of Cr(VI) (100%), Fe(III) (98%), COD (95%), BOD (94%) and Chloride (78%) was obtained at

45 re averaged over 1-s intervals to generate a COD trace.

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

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

48 5 L kg(-1) COD(added) at 29% food waste on a COD basis, with a solids retention time of 42 days.

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

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

51 and genetic features of GUCA1A-associated AD-COD/CORD from a large Japanese cohort.

52 GUCA1A-associated AD-COD/CORD has never been reported in the Japanese populat

53 riants, two of which were novel, underlie AD-COD/CORD with progressive retinal atrophy, and the preva

54 alues for influent TSS (61-820 mg L(-1)) and COD (384-1505 mg L(-1)), demonstrating a robust system f

55 e morphologically important faces of COM and COD.

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

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

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

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

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

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

62 D/N ratio of C17.8N1 wastewater had the best COD and NH(3)-N removal, as compared to the lower COD/N

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

64 ation estimates had high RSD (>44%) for BOD, COD, and ammonium between sites, suggesting that their a

65 stimates using hydrochemical parameters BOD, COD, and dissolved ammonia were evaluated for accuracy a

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

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

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

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

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

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

72 sources, namely, nitrate and organic carbon (COD).

73 -terpinen-4-ol) using Crabtree's catalyst ([(COD)Ir(py)(PCy(3))][PF(6)], COD = 1,5-cyclooctadiene, py

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

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

76 We were able to classify COD in 248 (88%) of 283 decedents.

77 overall cohort, lymphoma was the most common COD, with a cumulative incidence of 10.3% at 10 years, f

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

79 arameters showed the following correlations: COD (r = -0.84), TS (r = -0.83), and BOD (r = -0.81), wh

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

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

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

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

84 sence of dienes, such as 1,5-cyclooctadiene (COD) or norbornadiene (NBD), yielded long sought-after c

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

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

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

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

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

90 d, little is known of their causes of death (CODs) in the rituximab era.

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

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

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

94 nations, theoretical chemical oxygen demand (COD(th)) as well as theoretical and stoichiometric metha

95 ) < 30 mg L(-1), and chemical oxygen demand (COD) < 150 mg L(-1).

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

97 = 0.87), and between chemical oxygen demand (COD) and AA concentrations (R(2) = 0.87).

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

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

100 7-day Pb toxicity to chemical oxygen demand (COD) and NH3-N removal, bacterial viability, and communi

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

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

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

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

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

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

107 om 2.5 to 15 g total chemical oxygen demand (COD) L.d(-1).

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

109 ass balance based on chemical oxygen demand (COD) of 100 +/- 2% (COD(out)/COD(in)).

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

111 ter streams with low chemical oxygen demand (COD) to nitrogen (C/N) ratios.

112 (pH 4, 5, and 7) and chemical oxygen demand (COD) to nitrogen (COD/N) ratio of 3.6:1, 7.1:1, 14.2:1,

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

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

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

116 C and AnA(mox)MDC in terms of power density, COD removal and salt removal in desalination chamber.

117 -driven algorithm, centroid of distribution (COD), to detect head motion.

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

119 We report that Ni(COD)(DQ) (COD=1,5-cyclooctadiene, DQ=duroquinone), an air-stable 1

120 with autosomal dominant (AD) cone dystrophy (COD) and cone-rod dystrophy (CORD).

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

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

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

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

125 The highest percentage for COD and NH(3)-N removal achieved was 96.0% and 93.2%, re

126 At 10 g COD L.d(-1), where the highest difference in performance

127 rease in methane production per OLR) at 10 g COD L.d(-1), whereas both systems were inhibited at 15 g

128 tive to SP as OLR increased from 3.5 to 10 g COD L.d(-1).

129 ould effectively treat FW at OLRs up to 10 g COD.L day(-1) by improving hydrolysis rates, microbial d

130 whereas both systems were inhibited at 15 g COD L.d(-1).

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

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

133 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.

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

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

136 al methane yield was 0.14 +/- 0.06 L-CH(4)/g-COD fed, with 42% of the total methane dissolved in the

137 face organometallic chemistry, by grafting [(COD)Pt(OSi(OtBu)(3))(2)] (1, COD = 1,5-cyclooctadiene) o

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

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

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

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

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

143 sites for the adsorption of Cr(VI), Fe(III), COD, BOD, and chloride from tannery wastewater were inve

144 The conversion of [IrCl(COD)(IMes)] (COD = cis, cis-1,5-cyclooctadiene, IMes = 1,3-bis(2,4,6-

145 In COD, the central coordinates of the line of response of

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

147 ed on this theory, we revealed that influent COD/N ratio alone was not sufficient to predict the comp

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

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

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

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

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

153 her than those of reactions catalyzed by [Ir(COD)(OMe)](2) and 4,4'-di-tert-butylbipyridine (dtbpy).

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

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

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

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

158 eactions catalyzed by the combination of [Ir(COD)(OMe)](2) and 3,4,7,8-tetramethylphenanthroline (tmp

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

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

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

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

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

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

165 d SABRE homogeneous catalyst [Ir-IMes; [IrCl(COD)(IMes)], (IMes=1,3-bis(2,4,6-trimethylphenyl), imida

166 The conversion of [IrCl(COD)(IMes)] (COD = cis, cis-1,5-cyclooctadiene, IMes = 1

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

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

169 For (11)C-UCB-J, COD yielded 3.7% +/- 5.2% differences in V (T) compared

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

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

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

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

174 n average effluent quality of 58 +/- 27 mg/L COD and 25 +/- 12 mg/L BOD(5) at temperatures ranging fr

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

176 with FL in the rituximab era, their leading COD remains lymphoma, especially after disease transform

177 nd NH(3)-N removal, as compared to the lower COD/N ratio, and the shortest treatment time was obtaine

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

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

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

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

182 19-0.36 mg COD/mg TSS/d) and C:N (3.5-6.3 mg COD/mg TKN) conditions for a period of 74 days, followin

183 t different, low and high, F:M (0.19-0.36 mg COD/mg TSS/d) and C:N (3.5-6.3 mg COD/mg TKN) conditions

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

185 0.33 +/- 0.14 mg-O2/L, and 0.14 +/- 0.02 mg-COD/mg-N, respectively.

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

187 We applied the new COD framework to 23 human dynamic datasets, all containi

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

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

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

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

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

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

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

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

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

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

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

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

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

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

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

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

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

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

206 Due to its apparent stability, use of Ni(COD)(DQ) as a precatalyst allows reactions to be conveni

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

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

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

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

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

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

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

214 We report that Ni(COD)(DQ) (COD=1,5-cyclooctadiene, DQ=duroquinone), an ai

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

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

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

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

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

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

221 nd chemical oxygen demand (COD) to nitrogen (COD/N) ratio of 3.6:1, 7.1:1, 14.2:1, and 17.8:1 (C3.6N1

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

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

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

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

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

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

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

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

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

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

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

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

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

235 oxygen demand (COD) of 100 +/- 2% (COD(out)/COD(in)).

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

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

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

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

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

241 The parameters of pH, COD, and NH(3)-N were measured periodically during the e

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

243 ctroanalytical sensing of codeine phosphate (COD).

244 Conclusion: The proposed COD-based data-driven motion correction method outperfor

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

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

247 , 5, can be prepared from the reaction of Pt(COD)2 with Mes3SnH and CNBu(t).

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

249 uble Zintl cluster, [eta(4)-Ge(9)(Hyp)(3)]Rh(COD), that can catalytically hydrogenate cyclic alkenes

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

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

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

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

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

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

256 decreased soluble chemical oxygen demand (S(COD)) removal efficiency (11% to 31%) and reduced biofil

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

258 For (18)F-FDG dynamic studies, COD yielded differences of 3.6% +/- 10.9% in K (i) value

259 Substrate COD destruction efficiency reached 65%, and the methane

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

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

262 The COD complex proved substitutionally labile undergoing di

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

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

265 The COD(th), TMP, SMP values indicated IONPs efficacy for im

266 The COD/N ratio of C17.8N1 wastewater had the best COD and N

267 The COD/N ratios with a constant concentration of ammonia-ni

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

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

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

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

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

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

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

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

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

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

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

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

280 er for 9 weeks under aerobic conditions. The COD of MB wastewater showed a reduction of 86.48% from 2

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

282 A point-to-point change in the COD trace in 1 direction that exceeded a user-defined th

283 experimental results as to the impact of the COD/N ratio.

284 Results: The COD method yielded a 1.0% +/- 3.2% (mean +/- SD across a

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

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

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

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

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

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

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

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

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

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

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

296 The reaction of Li(2)[2] with (COD)PdMeCl and 4-(5-nonyl)-pyridine (py') generates the

297 -1,3-bis(trimethylsilyl)propene reacts with (COD)2Ni to produce the dimeric purple complex {[1,3-(SiM

298 system (quinoline-based silane ligand with [(COD)IrOMe](2) ) was optimal for biphenyl-based phosphine

299 2,4,6-trimethylphenyl), imidazole-2-ylidene; COD=cyclooctadiene)] was first activated in the presence

300 2,4,6-trimethylphenyl), imidazole-2-ylidene; COD=cyclooctadiene] catalyst onto silica particles modif