PMID-sentid	Pub_year	Sent_text		comp_official_name	comp_offsetprotein_name	organism	prot_offset
29527891-6	2018	The observed reaction rates were independent from the partial pressure of hydrogen and hydrogen consumption only stopped in supplemental microcosm experiments where salinity was increased above 35 g L-1.	Hydrogen	87-95	immunoglobulin kappa variable 1-16	Homo sapiens	199-202	
12947681-2	2001	1H NMR chemical shift non-equivalence of the methyl doublet of alpha-phenylethylamine was 0.08 ppm(base-line separation) in solvent CDCl3, when the concentration of the sample was 0.051 mol.L-1, the molar ratio between chiral solvating agent and the sample was 0.33.	Hydrogen	0-2	immunoglobulin kappa variable 1-16	Homo sapiens	190-193	
31113708-2	2019	Under the optimized working volume ratio of 1:4, starch concentration of 7 g L-1 and initial pH of 7.0, the highest H2 production of 1643.5 mL L-1 and lipid yield of 515.6 mg L-1 were achieved.	Hydrogen	116-118	immunoglobulin kappa variable 1-16	Homo sapiens	77-80	
31113708-2	2019	Under the optimized working volume ratio of 1:4, starch concentration of 7 g L-1 and initial pH of 7.0, the highest H2 production of 1643.5 mL L-1 and lipid yield of 515.6 mg L-1 were achieved.	Hydrogen	116-118	immunoglobulin kappa variable 1-16	Homo sapiens	143-146	
31113708-2	2019	Under the optimized working volume ratio of 1:4, starch concentration of 7 g L-1 and initial pH of 7.0, the highest H2 production of 1643.5 mL L-1 and lipid yield of 515.6 mg L-1 were achieved.	Hydrogen	116-118	immunoglobulin kappa variable 1-16	Homo sapiens	143-146	
29911268-5	2019	The best hydrogen production potential was obtained at a COD of 50 g L-1 without nutrient addition.	Hydrogen	9-17	immunoglobulin kappa variable 1-16	Homo sapiens	69-72	
29911268-6	2019	This condition produced 528 mL H2 L-1.	Hydrogen	31-33	immunoglobulin kappa variable 1-16	Homo sapiens	34-37	
30104721-4	2018	Here, we present a polyoxoanion, [P2W18O62]6-, that can be reversibly reduced and protonated by 18 electrons/H+ per anion in aqueous solution, and that can act either as a high-performance redox flow battery electrolyte (giving a practical discharged energy density of 225 Wh l-1 with a theoretical energy density of more than 1,000 Wh l-1), or as a mediator in an electrolytic cell for the on-demand generation of hydrogen.	Hydrogen	415-423	immunoglobulin kappa variable 1-16	Homo sapiens	276-279	
30104721-4	2018	Here, we present a polyoxoanion, [P2W18O62]6-, that can be reversibly reduced and protonated by 18 electrons/H+ per anion in aqueous solution, and that can act either as a high-performance redox flow battery electrolyte (giving a practical discharged energy density of 225 Wh l-1 with a theoretical energy density of more than 1,000 Wh l-1), or as a mediator in an electrolytic cell for the on-demand generation of hydrogen.	Hydrogen	415-423	immunoglobulin kappa variable 1-16	Homo sapiens	336-339	
29306713-2	2018	Butyrate-type fermentation was the most appropriate fermentation type for the synergistic system and exhibited the accumulative hydrogen volume of 658.3 mL L-1 and hydrogen yield of 131.7 mL g-1 COD.	Hydrogen	128-136	immunoglobulin kappa variable 1-16	Homo sapiens	156-159	
29200586-7	2017	At a bicarbonate concentration of 50 mmol L-1, current density increased to 10.7 A m-2 at an anode potential of -0.2 V. This increase in current density could be due to oxidation of formed acetate in addition to oxidation of hydrogen, or enhanced growth of hydrogen oxidizing bacteria due to the availability of acetate as carbon source.	Hydrogen	225-233	immunoglobulin kappa variable 1-16	Homo sapiens	42-45	
29200586-7	2017	At a bicarbonate concentration of 50 mmol L-1, current density increased to 10.7 A m-2 at an anode potential of -0.2 V. This increase in current density could be due to oxidation of formed acetate in addition to oxidation of hydrogen, or enhanced growth of hydrogen oxidizing bacteria due to the availability of acetate as carbon source.	Hydrogen	257-265	immunoglobulin kappa variable 1-16	Homo sapiens	42-45	
29744302-3	2017	The reduction of TCE under 90 mA current, 1 mL min-1 flow rate, and 1 mg L-1 initial TCE concentration, was inhibited in the presence of humic acids due to competition for direct electron transfer and/or reaction with atomic hydrogen produced at the cathode surface by water electrolysis.	Hydrogen	225-233	immunoglobulin kappa variable 1-16	Homo sapiens	73-76	
27639056-4	2016	When the initial hydrogen partial pressure was 0.5 atm, the methane yield at high ammonia load (7 g NH4+-N L-1) was 41.0% and 22.3% lower than that at low ammonia load (1 g NH4+-N L-1) in mesophilic and thermophilic condition, respectively.	Hydrogen	17-25	immunoglobulin kappa variable 1-16	Homo sapiens	107-110	
27639056-4	2016	When the initial hydrogen partial pressure was 0.5 atm, the methane yield at high ammonia load (7 g NH4+-N L-1) was 41.0% and 22.3% lower than that at low ammonia load (1 g NH4+-N L-1) in mesophilic and thermophilic condition, respectively.	Hydrogen	17-25	immunoglobulin kappa variable 1-16	Homo sapiens	180-183	
27639056-8	2016	Furthermore, the thermophilic methanogens at 0.5 atm of hydrogen partial pressure were more tolerant to high ammonia levels (>=5 g NH4+-N L-1), compared with mesophilic methanogens.	Hydrogen	56-64	immunoglobulin kappa variable 1-16	Homo sapiens	141-144