当前位置: X-MOL 学术Green Chem. › 论文详情
Our official English website, www.x-mol.net, welcomes your feedback! (Note: you will need to create a separate account there.)
Low energy recycling of ionic liquids via freeze crystallization during cellulose spinning
Green Chemistry ( IF 9.8 ) Pub Date : 2017-12-19 00:00:00 , DOI: 10.1039/c7gc02880f
Yanrong Liu 1, 2, 3, 4, 5 , Anne S. Meyer 6, 7, 8, 9, 10 , Yi Nie 1, 2, 3, 4, 5 , Suojiang Zhang 1, 2, 3, 4, 5 , Kaj Thomsen 7, 8, 9, 10, 11
Affiliation  

A new method for recycling ionic liquids (ILs) from a cellulose spinning process is suggested. The method involves the combination of freeze crystallization and evaporation of H2O from IL + H2O mixtures to recycle the ILs. Processes with EmimAc and EmimDep were used as references to develop this IL recycling method. EmimAc + 12.5 wt% H2O and EmimDep + 4 wt% H2O were selected for a quantitative mass and energy analysis of the cellulose spinning and IL recycling process (the maximal initial H2O levels in the ILs + H2O mixtures for cellulose dissolution were determined experimentally). The energy requirement for the freeze crystallization + evaporation method was compared to evaporation only for recycling of EmimAc and EmimDep. To produce 1 kg dry cellulose fiber, 45.4 MJ and 62.6 MJ are required for recycling EmimAc and EmimDep respectively by the freeze crystallization + evaporation recycling method. Using evaporation only, 66.9 MJ is required for EmimAc recycling and 99.9 MJ for EmimDep recycling per kg cellulose fiber produced. Thus, to fabricate 1 kg dry cellulose fiber using freeze crystallization + evaporation rather than evaporation, 21.5 MJ can be saved for EmimAc and 37.3 MJ for EmimDep recycling. We also show that compared to a classical Lyocell fiber production method using N-methylmorpholine-N-oxide (NMMO) as solvent, use of ILs is energy saving in itself. Hence, significantly less H2O is required in the cellulose spinning process with ILs than with NMMO, and in turn less H2O has to be evaporated for the solvent recycling.

中文翻译:

纤维素纺丝过程中通过冷冻结晶进行离子液体的低能回收

提出了一种从纤维素纺丝工艺中回收离子液体(ILs)的新方法。该方法涉及冷冻结晶和从IL + H 2 O混合物中蒸发H 2 O的组合,以回收IL。EmimAc和EmimDep的工艺被用作开发这种IL回收方法的参考。选择EmimAc + 12.5 wt%H 2 O和EmimDep + 4 wt%H 2 O进行纤维素纺丝和IL回收过程的定量质量和能量分析(ILs + H 2中的最大初始H 2 O水平)通过实验确定用于溶解纤维素的O混合物。将冷冻结晶+蒸发方法的能量需求与仅蒸发EmimAc和EmimDep的蒸发进行了比较。要生产1千克干纤维素纤维,需要45.4 MJ和62.6 MJ分别通过冷冻结晶+蒸发回收方法回收EmimAc和EmimDep。仅使用蒸发,每生产一公斤纤维素纤维,EmimAc循环需要66.9 MJ,EmimDep循环需要99.9 MJ。因此,使用冷冻结晶+蒸发而不是蒸发来制造1 kg干纤维素纤维,对于EmimAc可以节省21.5 MJ,对于EmimDep回收可以节省37.3 MJ。我们还表明,与使用N -methylmorpholine- N的经典莱赛尔纤维生产方法相比氧化物(NMMO)作为溶剂,使用离子液体本身就可以节省能源。因此,显著少ħ 2 O的需要与离子液体比用NMMO纤维素纺丝工艺,进而较少ħ 2 O具有待蒸发的溶剂回收再利用。
更新日期:2018-01-22
down
wechat
bug