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Experimental kinetic data of conversion of acetic acid is obtained for various ranges of parameters such as catalyst loading in g/cc of reactant mixture volume, temperature in the range of 323.15 353.15 K, average diameter of catalyst particle varied from 425 μm to 925 μm and RPM of magnetic stirrer.
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Data conversion includes purging or cleansing of existing data, reconciling or balancing of the old data and the data in the new system, creation of new/additional data, and the conversion of old data to the new system.
The first step will be exploratory to determine most appropriate "transformation" of the data: conversion of quantitative data into narrative data ("qualitized") or conversion of qualitative data into numerical codes ("quantitized") that can be represented statistically.
However, the submission of large amounts of NGS data, conversion of data format, and limited availability of species bring problems.
Calculation of capillary pressure data needs conversion of the measured fluid productions to the local saturation values.
On the basis of the determined data the conversion of the substrates was calculated (Figure 2).
Further pre-processing included calculation of a digital terrain model (DTM) from the ground returns, removal of overlaps from the raw data, and conversion of height coordinates (zvalues) of the vegetation returns from absolute elevation into distance-to-ground using the DTM [15].
Further pre-processing included calculation of a digital terrain model (DTM) from the ground returns, removal of overlaps from the raw data, and conversion of height coordinates (zvalues) of the vegetation returns from absolute elevation into distance-to-ground using the DTM [ 15].
Taken together, these data demonstrate conversion of dimeric to monomeric cystatin F within the endocytic pathway.
The starting point is a data bank of conversion values for hydrogenating runs of synthetic feeds prepared with the representative reactive species in the First Stage scenario.
In this work, we present a new CFD model used to determine true kinetic data of hydrothermal conversion of a heavy oil model compound, hexadecane, in a continuous flow reactor.
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