Method for preparing disodium terephthalate and high-purity hydrogen through one-step low-temperature conversion of PET polyester waste plastics
A disodium terephthalate and low-temperature conversion technology, applied in chemical instruments and methods, carboxylic anhydride preparation, hydrogen, etc., can solve problems such as high content, loss of ethylene glycol, difficult disposal of tar, etc., to achieve rapid processing and avoid Glycol loss, effect of high market value
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Embodiment 1
[0038] Preparation method of reforming catalyst: use impregnation method to prepare catalyst, according to 5wt.% theoretical Ru loading, add a certain amount of biochar and precursor ruthenium chloride to absolute ethanol, stir and impregnate at room temperature for 12 hours, Continue stirring at 80°C until absolute ethanol evaporates to dryness, and dry the obtained sample (Ru / C) in an oven at 105°C; at 500°C, 10% H 2 Reduction in -90% Ar for 5 hours.
[0039] One-step low-temperature transformation of PET polyester waste plastics in a high-pressure reactor to prepare disodium terephthalate and high-purity hydrogen: Weigh 0.7g PET polyester plastic particles, 70ml deionized water, 0.07g Ru / C catalyst and 0.874g NaOH, run for 120 minutes at 180°C, no initial pressure, and reaction pressure 0.5MPa. After the reaction was completed, rapid cooling was carried out, and the generated gas was collected with an air bag and analyzed by gas chromatography, and the yield of hydrogen wa...
Embodiment 2
[0041] The preparation method of the reforming catalyst is the same as in Example 1.
[0042] One-step low-temperature transformation of PET polyester waste plastics in a high-pressure reactor to prepare disodium terephthalate and high-purity hydrogen: Weigh 0.7g PET polyester plastic particles, 70ml deionized water, 0.07g Ru / C catalyst and 0.874g NaOH, run for 120 minutes at 200°C, no initial pressure, and reaction pressure 1MPa. After the reaction was completed, rapid cooling was carried out, and the gas produced was collected by an air bag and analyzed by gas chromatography, and the yield of hydrogen was 18.31mol / kg PET , The hydrogen concentration is 98.77%. After recycling the liquid phase product and solid catalyst for 5 times, filter the liquid phase product and solid catalyst; add terephthalic acid to the filtered aqueous solution until the terephthalic acid cannot be dissolved to remove the residual Na 2 CO 3 and a small amount of NaOH to obtain refined disodium te...
Embodiment 3
[0044] The preparation method of the reforming catalyst is the same as in Example 1.
[0045] One-step low-temperature transformation of PET polyester waste plastics in a high-pressure reactor to prepare disodium terephthalate and high-purity hydrogen: Weigh 0.7g PET polyester plastic particles, 70ml deionized water, 0.07g Ru / C catalyst and 0.874g NaOH, run for 120 minutes at 220°C, no initial pressure, and reaction pressure 1.5MPa. After the reaction was completed, rapid cooling was carried out, and the generated gas was collected with an air bag and analyzed by gas chromatography, and the yield of hydrogen was 22.45mol / kg PET , The hydrogen concentration is 97.99%. After recycling the liquid phase product and solid catalyst for 5 times, filter the liquid phase product and solid catalyst; add terephthalic acid to the filtered aqueous solution until the terephthalic acid cannot be dissolved to remove the residual Na 2 CO 3 and a small amount of NaOH to obtain refined disodi...
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