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The experiments have been conducted to eliminate the resistance to crystal growth due to the volume diffusion by increasing the solution flow rate through the growth chamber.
Similarly, by increasing the solution pH from 3.0 to 7.0, adsorption capacity of Cd2+ and Cu2+ increased from 2.7 to 14.4 mg g−1 and 3.4 to 12.4 mg g−1, respectively.
While the nano/microstructure formed by the deposited calcium phosphate layer is controlled by increasing the solution pH to above 6.5 and increasing the duration of immersion experimentally, the nanostructure imposed by the dimensions of the fibers was controlled by the polymer concentration (12% w/v), applied voltage (25 kV) and capillary tip to collector distance (35 cm).
The PAMPS-core micelle with the PNIPAM-corona was obtained by insolubilizing the PAMPS block with ferric ion (Fe3+) at room temperature, and the PNIPAM-core micelle with the PAMPS-corona was obtained by increasing the solution temperature above the lower critical solution temperature (LCST) of the PNIPAM block in the absence of the Fe3+ ion.
Moreover, by increasing the solution pH from 3.0 to 7.0, adsorption capacity elevated from 2.7 to 14.4 mg/g.
Limiting the mass transport to the emitter electrode is a means to suppress analyte electrolysis and can be accomplished for instance by increasing the solution flow rate, by reducing the electrode contact area, or by using a pulsed electrospray source [ 20, 21].
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Moreover, the inhibition effects, which were characterized by reductions in the flame propagation speed, the maximum explosion overpressure (ΔPmax), and the maximum pressure rising rate ((dP/dt)max), could be improved by increasing the water/NaCl solution concentration and mist amount.
The retention coefficient (R%) of the alumina membrane increased from 35.24% to 54.2% by increasing the NaCl solution concentration from 2,000 to 5,000 ppm.
By increasing the HAuCl4 solution amount to 5 ml, Au-NPs with sizes of 50 to 80 nm are grown (Figure 3b, Table 1).
The column was equilibrated in 0.05% acetic acid/water (solution A) and elution of the components was achieved by increasing the concentration of solution B (100% acetonitrile) from 0 to 100% in 30 min at a flow rate of 1 ml/min.
As can be seen in Fig. 5, by increasing the activity of solution, the removal efficiency of 90Sr is decreased.
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