Method for refining non-petroleum-based ethylene glycol
A glycol-based, non-petroleum technology, applied in the field of refining non-petroleum-based glycol, can solve the unspecified separation of butanediol and other problems
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Embodiment 1
[0039] Attached figure 1 In the process shown in , the mixed alcohol feed is the material obtained after dehydration and light component removal of the mixed product produced with biomass as raw material. The composition of the material is 85.1% ethylene glycol, 1,2- Propylene glycol 6.6%, 1,2-butanediol 2.2%, 2,3-butanediol 0.4%, 1,4-butanediol 0.7%, 1,2-pentanediol 0.2%, 1,2-hexanediol 0.2%, 0.1%, glycerol 0.5%, sorbitol 0.5%, other light and heavy components 3.5%.
[0040] The mixed alcohol feed is mixed with the fresh entrainer iso-octanol into the 45th theoretical plate of the azeotrope column. The weight ratio of entrainer (including fresh entrainer and reused entrainer stream 2 and stream 11) to ethylene glycol in the mixed alcohol feed was 3.39:1. There are a total of 90 theoretical plates in the azeotropic column. The azeotropic agent stream 2 reused at the top of the tower and the azeotrope stream 11 reused at the bottom of the tower respectively enter the azeot...
Embodiment 2
[0045] Attached figure 1 In the process shown in , the mixed alcohol feed is the material obtained after dehydration and light component removal of the mixed product produced with biomass as raw material. The composition of the material in weight percentage is ethylene glycol 23.20%, 1,2- Propylene glycol 55.09%, 1,2-butanediol 4.60%, 2,3-butanediol 1.40%, 1,4-butanediol 0.60%, 1,2-pentanediol 0.31%, 1,2-hexanediol Alcohol 0.49%, 0.15%, glycerol 2.10%, sorbitol 1.90%, other light and heavy components 10.16%.
[0046] The mixed alcohol feed is mixed with the fresh entrainer 2-nonanone into the 30th theoretical plate of the azeotrope column. The weight ratio of entrainer (including fresh entrainer and reused entrainer stream 2 and stream 11) to ethylene glycol in mixed alcohol feed is 7.04:1. There are a total of 90 theoretical plates in the azeotropic column. The azeotropic agent stream 2 reused at the top of the tower and the azeotrope stream 11 reused at the bottom of th...
Embodiment 3
[0051] Attached figure 1 In the process shown in , the mixed alcohol feed is the material obtained after dehydration and removal of light components from the mixed product produced with biomass as raw material. The composition of the material in terms of weight percentage is ethylene glycol 92.50%, 1,2- Propylene glycol 4.89%, 1,2-butanediol 1.42%, 2,3-butanediol 0.17%, 1,4-butanediol 0.12%, 1,2-pentanediol 0.06%, 1,2-hexanediol Alcohol 0.24%, 0.07%, other light and heavy components 0.53%.
[0052] The mixed alcohol feed is mixed with the fresh entrainer n-decyl alcohol and enters the 30th theoretical plate of the azeotrope column. The weight ratio of entrainer (including fresh entrainer and reused entrainer stream 2 and stream 11) to ethylene glycol in mixed alcohol feed is 0.60:1. There are a total of 90 theoretical plates in the azeotropic column. The azeotropic agent stream 2 reused at the top of the tower and the azeotrope stream 11 reused at the bottom of the tower ...
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