Extraction liquid and extraction method for sulphuric acid in sulfuric acid hydrolysate prepared with plant fibre
A plant fiber and extract technology, applied in liquid solution solvent extraction, sulfur trioxide/sulfuric acid, etc., can solve the problems of low adsorption capacity, high energy consumption of vacuum distillation, no practicality, etc., and achieve the effect of avoiding cost increase
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Embodiment 1
[0021] The plant fiber raw material is corn cob, and sulfuric acid is used to hydrolyze hemicellulose to prepare xylose. The hydrolysis reaction is carried out at 98° C., the sulfuric acid concentration is 5.8%, and the hydrolyzate and cellulose slag are obtained after 130 minutes of reaction. The composition of the extract is: amine extractant N 235 The concentration of kerosene is 1.05M, and the rest are diluent kerosene and phase regulator tributyl phosphate, and the volume ratio of kerosene and tributyl phosphate is 4:5. The temperature is 25°C, and the hydrolyzate is subjected to discontinuous 6-stage countercurrent extraction with the extract, and the liquid ratio (organic phase / water phase) is 2 to obtain the extract containing sulfuric acid and the sugar liquid containing little sulfuric acid; the extract containing sulfuric acid Concentrated ammonia water is used as the stripping agent for intermittent 5-stage countercurrent stripping. The liquid ratio (organic phase / ...
Embodiment 2
[0023] The plant fiber raw material is corn stalks, which are cut into 2 cm long, and the hemicellulose is hydrolyzed by sulfuric acid to prepare pentose. The hydrolysis temperature is 75° C., the concentration of sulfuric acid is 14.5%, and the time is 120 minutes to obtain sulfuric acid-containing sugar solution and lignin residue. The formula of the extract is: 40% triisooctylamine, 35% sulfonated kerosene, 25% secondary octanol. The temperature is 20°C, and the hydrolyzate is subjected to intermittent 8-stage countercurrent extraction with the extract, the liquid ratio (organic phase / water phase) is 2, and the extract containing sulfuric acid and the sugar liquid containing little sulfuric acid are obtained. The extraction rate of sulfuric acid is about 92%; temperature is raised to 60 DEG C, and the sulfuric acid-containing extract is carried out intermittent 6-stage countercurrent back extraction with water as stripping agent, the liquid ratio (organic phase / water phase) ...
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