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The maximal degradation of MG was obtained to be 97.18% under the optimum conditions with the enzyme concentration of 1.50 U/mL, the dye concentration of 122.66 mg/L, pH of 6.75and the incubation time of 98.58 min.
When the system was powered by two MFCs of a larger internal resistance (146 Ω), the highest salt removal after 60 min (m60; 7.5 mg) was achieved by paralleling the two MFCs; with MFCs of a smaller resistance (12 Ω) being used, the highest m60 (16.5 mg) was obtained when the two MFCs were connected in series.
A yellowish powdered compound 1 (21 mg) was obtained.
The organic extract was evaporated to dryness and a dark oily residue (85 mg) was obtained.
After evaporation of the solvent, a dark oily residue (84 mg) was obtained.
Compound 6 (162 mg) was obtained from F2 by MCI CC (MeOH/H2O, 5→25 %).
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N-mG was obtained from Santa Cruz Biotechnology (Dallas, TX).
From 1,440 ml of media from the culture of A89CS3cpI, 0.41 mg of purified protein with 275.0 nkat/mg was obtained.
An efficient loading of HB on GO as high as 2 mg/mg was obtained.
After removing the contaminant oligopeptides using ultrafiltration, purified PAC with a specific activity of 16.3 U/mg was obtained and the overall purification factor for this one-step downstream purification process was up to 3 fold.
The biomass yield coefficient changed slightly at low 2C4NP concentrations, and the highest yield coefficient (0.505 mg/mg) was obtained at a 2C4NP concentration of 0.3 mM.
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CEO of Professional Science Editing for Scientists @ prosciediting.com