PMID-sentid Pub_year Sent_text comp_official_name comp_offsetprotein_name organism prot_offset 29488201-2 2018 First of all, a chemical oxygen demand (COD) and color removal efficiency of 66 and 63% was achieved at initial pH of 6.8, 25 mmol L-1 of H2O2, and 2 g L-1 of Fe0 in the Fe0/H2O2 reaction. Oxygen 25-31 L1 cell adhesion molecule Homo sapiens 131-134 32996287-3 2021 The model shows that this system can achieve a biomass productivity of ~1.7 g L -1 hr -1 but is limited by a competitive trade-off between O 2 gas/liquid mass transfer and CO 2 transport to the cathode. Oxygen 139-142 L1 cell adhesion molecule Homo sapiens 78-88 31264511-6 2021 The reaction time in which oxygen evolution happpens depends on the concentration of catalyst used in the oxidation, verifying that the highest oxygen generation rates are obtained when applying [Fe]0 = 10.0 mg L-1. Oxygen 27-33 L1 cell adhesion molecule Homo sapiens 211-214 31264511-6 2021 The reaction time in which oxygen evolution happpens depends on the concentration of catalyst used in the oxidation, verifying that the highest oxygen generation rates are obtained when applying [Fe]0 = 10.0 mg L-1. Oxygen 144-150 L1 cell adhesion molecule Homo sapiens 211-214 31264511-8 2021 The stages of formation and decrease of oxygen are adjusted to zero-order kinetics, estimating the kinetics constants as a function of the catalyst concentration: kf = 29.48 [Fe]0-1.25 (mg O2 L-1 min-1) and kd = -0.006 [Fe]0 2.0 + 0.244 [Fe]0-3.69 (mg O2 L-1 min-1). Oxygen 40-46 L1 cell adhesion molecule Homo sapiens 192-195 31264511-8 2021 The stages of formation and decrease of oxygen are adjusted to zero-order kinetics, estimating the kinetics constants as a function of the catalyst concentration: kf = 29.48 [Fe]0-1.25 (mg O2 L-1 min-1) and kd = -0.006 [Fe]0 2.0 + 0.244 [Fe]0-3.69 (mg O2 L-1 min-1). Oxygen 189-191 L1 cell adhesion molecule Homo sapiens 192-195 31264511-8 2021 The stages of formation and decrease of oxygen are adjusted to zero-order kinetics, estimating the kinetics constants as a function of the catalyst concentration: kf = 29.48 [Fe]0-1.25 (mg O2 L-1 min-1) and kd = -0.006 [Fe]0 2.0 + 0.244 [Fe]0-3.69 (mg O2 L-1 min-1). Oxygen 189-191 L1 cell adhesion molecule Homo sapiens 255-258 32645597-7 2020 In the system containing 10 mg L-1 As(III) and 1.0 g L-1 Fe-Mn nodules, the maximum oxidation capacity of As(III) reached 3.22, 3.48 and 3.71 mg g-1, and the corresponding As(III,V) adsorption capacity reached 2.49, 2.40, and 2.39 mg g-1 in nitrogen, air and oxygen atmosphere, respectively. Oxygen 259-265 L1 cell adhesion molecule Homo sapiens 31-34 32645597-7 2020 In the system containing 10 mg L-1 As(III) and 1.0 g L-1 Fe-Mn nodules, the maximum oxidation capacity of As(III) reached 3.22, 3.48 and 3.71 mg g-1, and the corresponding As(III,V) adsorption capacity reached 2.49, 2.40, and 2.39 mg g-1 in nitrogen, air and oxygen atmosphere, respectively. Oxygen 259-265 L1 cell adhesion molecule Homo sapiens 53-56 32705548-6 2020 Design Expert 12.0.8.0 software has been used to design mathematical model to obtain optimum condition (14 V and 47 min) at pH of 7.35, which provides experimental removal efficiency (75.6% chemical oxygen demand, 78.7% total dissolved solids, 93.4% turbidity, and 63.2% chloride) with minimal electrode consumption of 1.38 mg L-1. Oxygen 199-205 L1 cell adhesion molecule Homo sapiens 327-330 32778291-5 2020 Up to 468 mL L-1 of hydrogen and 203 mg L-1 of poly-beta-hydroxybutyrate can be produced starting from an initial chemical oxygen demand of 1500 mg L-1. Oxygen 123-129 L1 cell adhesion molecule Homo sapiens 13-16 32778291-5 2020 Up to 468 mL L-1 of hydrogen and 203 mg L-1 of poly-beta-hydroxybutyrate can be produced starting from an initial chemical oxygen demand of 1500 mg L-1. Oxygen 123-129 L1 cell adhesion molecule Homo sapiens 40-43 32778291-5 2020 Up to 468 mL L-1 of hydrogen and 203 mg L-1 of poly-beta-hydroxybutyrate can be produced starting from an initial chemical oxygen demand of 1500 mg L-1. Oxygen 123-129 L1 cell adhesion molecule Homo sapiens 40-43 32645581-4 2020 The effluent chemical oxygen demand (COD) content decreased from 150 to 78 mg L-1, and remained below a discharge limitation of 80 mg L-1, and the stable COD removal efficiencies (from 56.0% to 47.9%) indicated that catalyst deactivation, which primarily resulted from the deposition of inorganic salts on the surface of the catalyst that limited interaction between ozone and active sites and/or prevented electrons transfer, was primarily inhibited by backflushing. Oxygen 22-28 L1 cell adhesion molecule Homo sapiens 78-81 32510356-6 2020 The lowest concentration of dissolved oxygen (3.6 mg L-1) was observed within the river plume. Oxygen 38-44 L1 cell adhesion molecule Homo sapiens 53-56 31606810-7 2020 CONCLUSION: MOLLI T1-mapping sequences may be used for detecting dissolved oxygen in vivo at 3 T with an [Formula: see text] in the range 4.18-4.8 x 10-3 s-1 mg-1 L and a corresponding LOD for dissolved oxygen of approximately 10 mg L-1. Oxygen 75-81 L1 cell adhesion molecule Homo sapiens 233-236 29488201-2 2018 First of all, a chemical oxygen demand (COD) and color removal efficiency of 66 and 63% was achieved at initial pH of 6.8, 25 mmol L-1 of H2O2, and 2 g L-1 of Fe0 in the Fe0/H2O2 reaction. Oxygen 25-31 L1 cell adhesion molecule Homo sapiens 152-162 29124366-5 2017 The water temperatures are consistently above 25 C, which impairs dissolved oxygen levels (3.1 to 6.7 mg L-1) and may suggest eutrophication. Oxygen 77-83 L1 cell adhesion molecule Homo sapiens 106-109 27623370-7 2016 The addition of silicone oil at 20% (on a volume basis) stabilized system performance, leading to dissolved O2 concentrations of 7 mg L-1 and steady ECs of 320 g m-3 h-1 in the PB. Oxygen 108-110 L1 cell adhesion molecule Homo sapiens 134-137 27380303-3 2016 DFT calculations suggested that superior HOMO distributions spread over the nitrogen-donor (as well as somehow oxygen- donor in L2) groups of L1 and L2 macrocycles were the key factor for the observed Kb value enhancement. Oxygen 111-117 L1 cell adhesion molecule Homo sapiens 142-151 29964573-5 2017 The effluent chemical oxygen demand (COD) concentration could be lowered to 23 mg L-1. Oxygen 22-28 L1 cell adhesion molecule Homo sapiens 82-85 29964576-2 2017 The experimental results under different conditions showed that shortcut nitrification in the MBR was achieved by controlling the dissolved oxygen (DO) concentration to low levels (0.5-1.0 mg L-1 to 0.3-0.7 mg L-1) and changing the effective volume of the MBR to control hydraulic retention time (HRT), with the HRT in the ABR equal to 6 h, sludge reflux ratio of 100%, NOx--N reflux ratio of 300%, and temperature of 30C+-2C. Oxygen 140-146 L1 cell adhesion molecule Homo sapiens 192-195 12833291-5 2003 Together with four methoxy groups anchored onto the primary face, the two P(III) centres of L 1 form a circularly arranged P(2)O(4) 12-electron donor set able to complex an Ag(+) ion in a dynamic way, each of the four oxygen atoms coordinating successively to the silver ion. Oxygen 218-224 L1 cell adhesion molecule Homo sapiens 92-95 1321161-1 1992 This study evaluated the effect of L-1-oleoyl-2-acetyl-sn-3-glycerol (OAG) on ouabain-sensitive Na,K-dependent oxygen consumption (Na,K-QO2) in intact renal proximal tubule cells (RPTC). Oxygen 111-117 L1 cell adhesion molecule Homo sapiens 35-38 2222041-3 1990 After simple clamping of the aorta, oxygen tension decreased significantly distal to the clamping site both after occlusion of the thoracic aorta at T3-4 (group 1) and after occlusion of the abdominal aorta at L-1 (group 2). Oxygen 36-42 L1 cell adhesion molecule Homo sapiens 210-213