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A particular use for the humic acids in lignite comprises their conversion into long chain alkyl ammonium salts thereof, and especially with substituted ammonium salts in which at least one substituent is a straight hydrocarbon chain having from 12 to 22 carbon atoms. Process of solubilizing lignite and producing humates Publications (1
[2 Oxidation Process and Characteristic Evaluation of Humic Acids from Two Typical Lignites of humic acids (HAs) in lignites, the experimental conditions including oxidation time, H 2 O 2 concentration, and the solid−liquid ratio were investigated. Under the optimum oxidation conditions, the contents of HAs of YL and HB lignite were 45.4
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The method of the present disclosure includes providing an organic compost material, combining the organic compost material with a crop to be grown, heating the organic compost material, combining the organic compost material with water, and extracting an aqueous liquid comprising humic acid and fulvic acid. The organic compost material may include straw and manure and
[The humic liquid is produced from lignite extraction using alkali solution. Conventional humic acid is obtained by acidifying a humic solution using HCl. The purpose of this research is the formation of solid humic acid from lignite by ion exchange method using cation resin. The results showed that the addition of cation resin was able to reduce the pH from 14 to pH 2 as well as the
Humic acid salts are produced, with a high output of useful products, by a liquid-phase oxidation of the mixture of an alkaline agent with a lignin-containing plant raw material having the total content of dry substances of 12-20 %, said oxidation being carried out in two stages. In a first stage, pre-oxidation is carried out at a temperature of 50-190 DEG C. and a pressure of 0.5-3
[Process for preparing regenerated humic acids from coal by means of the continuous oxidation on fluidized bed, characterized in that a coal of lignite, sub-bituminous or bituminous type is submitted to a preliminary oxidation under mild conditions in order to reduce the hydrogen content of said coal by an amount of 5 to 25% of hydrogen initially present in the starting coal, and that
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