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Applied Chemistry for Engineering, Vol.29, No.6, 799-804, December, 2018
결정화조작에 의한 접촉분해경유 유분에 함유된 2,6-디메틸나프탈렌의 분리.정제
Separation and Purification of 2,6-Dimethylnaphthalene Present in the Fraction of Light Cycle Oil by Crystallization Operation
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초록
결정화조작에 의해 접촉분해경유(LCO) 유분 중에 함유된 2,6-디메틸나프탈렌(2,6-DMN)의 분리.정제를 검토했다. LCO 유분을 원료로, 이소프로필알코올을 결정화 용매로 각각 사용하여 solute crystallization (SC)을 수행했다. 결정화 조작온도의 상승과 용매/원료의 체적비(S/F)의 증가는 2,6-DMN의 순도를 향상시켰으나, 역으로 수율의 저하를 초래시켰다. LCO 유분(13.9% 2,6-DMN)과 이소프로필알코올을 사용한 SC, SC에 의해 회수한 결정과 메틸아세테이트를 사용한 re-crystallization 1 (RC 1), RC 1에 의해 회수한 결정과 메틸아세테이트를 사용한 RC 2의 3단계로 결정화조작을 행한 결과, 19.5%의 수율로 99.9% 2,6-DMN의 결정을 회수할 수 있었다. SC, RC 1, RC 2의 각 조작을 통해 얻어진 실험적 결과를 이용하여 LCO 유분 중에 함유된 2-6-DMN의 분리.정제공정을 검토했다.
The separation and purification of 2,6-dimethylnaphthalene (2,6-DMN) present in the light cycle oil (LCO) fraction was investigated by a crystallization operation. Solute crystallization (SC) was performed using LCO fraction and iso-propyl alcohol as a raw material and a SC solvent, respectively. Increasing the operation temperature and volume ratio of the solvent to the raw material (S/F) resulted in improving the purity of 2,6-DMN, whereas the yield decreased. As a result of the crystallization operation in three steps containing the SC using LCO fraction (13.9% 2,6-DMN) and isopropyl alcohol, the re-crystallization 1 (RC 1) using the crystals recovered by SC and methyl acetate, and RC 2 using the crystals recovered by RC 1 and methyl acetate, the crystal with 99.9% 2,6-DMN was recovered with 19.5% yield. Furthermore, the separation and purification process of 2,6-DMN present in the LCO fraction was reevaluated by using the experimental results obtained through each operations of SC, RC 1, and RC 2.
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