留出速度はγ-Al2O3＞ZrO2＞SiO2＞TiO2の順であった。ま

留出速度はγ-Al2O3＞ZrO2＞SiO2＞TiO2の順であった。
また、留出速度は触媒濃度6wt%の時に、最も高い値を示した。
それ以上の系：触媒過多による生成Lc6の物質移動律速。
それ以下の系：触媒不足によるOLUの解重合反応律速。 状態になっていると思われる。

今後は連続式装置での実験に移行し、引き続き評価を実施していく。

ผลลัพธ์ (อังกฤษ) 1:

Distillate output speed is γ-Al2O3: ZrO2: SiO2] was in the order of TiO2.Also, distillate speed showed highest value 6 wt % catalyst concentration during the. More series: generation Lc6 with acid catalyst material moving legal speed. It the following series: OLU due to lack of catalyst solution polymerization reaction rate speed. Seems to have been turned off.Future experiments in the continuous system, and will continue to conduct evaluation.

ผลลัพธ์ (อังกฤษ) 2:

Distillation rate was in the order of γ-Al2O3> ZrO2> SiO2> TiO2.
In addition, distillation rate when the catalyst concentration 6wt%, showed the highest value.
More system: mass transfer rate-limiting of production by the catalyst excessive Lc6.
Less of the system: depolymerization reaction rate-limiting of OLU by catalyst shortage. It seems to have become a state. The process proceeds to experiment in the continuous type apparatus in the future, we will continue to implement the evaluation.

ผลลัพธ์ (อังกฤษ) 3:

Al distillate rate gamma 2, 3 O ZrO 2 in the order of TiO SiO 2. Sup. 2. At the rate of distillate of catalytic concentration of 6 wt%, which showed the highest value. It: more than 6 Lc transfer limitation of materials by catalyst. It: the depolymerization reaction system controlled by OLU catalyst. There seems to be. In the continuous equipment in future too shift experiment, evaluation was carried out. At