Method for producing 1,6-hexanediol by cracking sorbierite
A technology of hexanediol and sorbitol, which is applied in the field of high-temperature and high-pressure hydrocracking production, can solve the problems of high price, high cost, and complicated manufacturing process, and achieve unique process conditions, mild reaction conditions, and significant economic and social benefits Effect
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Embodiment 1
[0025] A method for producing 1,6-hexanediol by cracking sorbitol, comprising the following steps:
[0026] (1) Handling of raw materials
[0027] mixing sorbitol with water, the weight ratio of the mixed sorbitol in water is 30-50%, and the pH is controlled at 11-13;
[0028] (2) Heating
[0029] Heat the mixture to 170-210°C;
[0030] (3) Cleavage reaction
[0031] The heated mixture is subjected to a high temperature and high pressure hydrocracking reaction in the presence of a nickel / cobalt catalyst, the temperature of the cracking reaction is controlled to be 180-230°C, the reaction pressure is 8-11Mpa, and the reaction time is 25-40 minutes;
[0032] (4) Lysate dehydration
[0033] After the cleavage reaction is completed, all the water in the cleavage product is removed;
[0034] (5) Separation of 1,6-hexanediol
[0035] The 1,6-hexanediol in the cracked product after dehydration is separated from other products, and the 1,6-hexanediol product is collected.
[00...
Embodiment 2
[0038] A method for producing 1,6-hexanediol by cracking sorbitol, comprising the following steps:
[0039] (1) Handling of raw materials
[0040] Sorbitol is mixed with water, the weight ratio of the mixed sorbitol in water is 45%, sodium hydroxide is added to control the pH at 11.8, and the described sorbitol is made of common corn starch, which is liquefied and saccharified to generate glucose. produced by rehydrogenation;
[0041] (2) Heating
[0042] Heat the mixture to 190°C;
[0043] (3) Cleavage reaction
[0044] The heated mixture is subjected to a high-temperature and high-pressure hydrocracking reaction in the presence of a nickel / cobalt catalyst. The temperature of the cracking reaction is controlled to be 200°C, the reaction pressure is 10Mpa, and the reaction time is 30 minutes;
[0045] (4) Lysate dehydration
[0046] After the cleavage reaction is completed, all the water in the cleavage product is removed through the dehydration tower;
[0047] (5) Separ...
Embodiment 3
[0051] A method for producing 1,6-hexanediol by cleavage of sorbitol, wherein the weight ratio of sorbitol solution in the aqueous phase is 50%, the pH is 11, the temperature of the cleavage reaction is 230°C, and the reaction pressure is 11Mpa, The reaction time was 25 minutes. The dehydration and separation described in steps (4), (5) are carried out continuously in the dehydration rectification tower. Others are the same as embodiment 1.
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