Molecular Formula | C6H12O3 |
Molar Mass | 132.16 |
Density | 0.96(20.0000℃) |
Boling Point | 184.08°C (rough estimate) |
Flash Point | 47.9℃ |
Storage Condition | Room Temprature |
Refractive Index | 1.4730 (estimate) |
Hazard Symbols | T - Toxic |
Risk Codes | R61 - May cause harm to the unborn child R10 - Flammable R37 - Irritating to the respiratory system |
Safety Description | S53 - Avoid exposure - obtain special instructions before use. S45 - In case of accident or if you feel unwell, seek medical advice immediately (show the label whenever possible.) S24/25 - Avoid contact with skin and eyes. |
UN IDs | 1993 |
HS Code | 29153900 |
Hazard Class | 3.2 |
Packing Group | III |
patent type:
invention patent
Application (patent) number:
CN202011272033.3
application date:
20201113
Public/Announcement Number:
CN112546658A
Public/announcement date:
20210326
applicant (patent):
Nantong Baichuan New Materials Co., Ltd., Jiangsu Baichuan high-tech New Materials Co., Ltd.
inventor:
Zheng tiaijiang , Wu Xiaoming , Zhao Yue , take the Jia Wei , gu Yinjun , Xia Hai Feng , Wan Peng , yuan Qingqing , Huang Xiaolei
National and provincial code:
CN320682
Abstract:
The invention relates to a novel 2-methoxy-1-propanol acetate deesterification rectification and purification device, comprising an ester product column evaporation kettle, an ester product column, a catalyst recovery tank, a catalyst recovery pump, ester finished product condenser, Ester cooler, Ester Tower tail cooler, Ester finished product tank, Ester condensate intermediate tank, Ester product Tower reflux pump, Ester finished product condenser II, A novel 2-methoxy 1-propanol acetate deesterification rectification purification method, comprising the following steps: feeding, rectification, condensation, sampling detection, external reflux, catalytic purification, product collection, by adjusting the content of each component in the material system in the column, the separation effect of the evaporation kettle is improved, the content of 2 methoxy 1 propanol acetate is increased, and the purity of the product is improved, thus, the content of 2-methoxy-1-propanol acetate in the reconstituted fraction of the tower is reduced, the purity of the catalyst is improved, the frequency of replacement is reduced, and the loss is reduced.
Application (patent) number:
CN201010254308.0
application date:
2010-08-16
Public/Announcement Number:
CN101985418B
Public/announcement date:
2013.01.02
applicant (patent):
Jiangsu Tianyin Chemical Co., Ltd.; Dena (Nanjing) Chemical Co., Ltd.
inventor:
Qin Yisan , Chen Rongfu , Qin Xudong , Zhang Yijun , Zhang Xuejun , Hong-Wei Zhu , Jiang Dazhi , Cao Jianqiang
National and provincial code:
CN320282
Abstract:
The invention discloses a process for preparing 2-methoxy-1-propanol acetate, which takes 2-methoxy-1-propanol and acetic acid as raw materials, and is characterized in that: the solid acid catalyst was used in the fixed-bed continuous esterification reaction, and the esterification temperature was 70-150 ℃. The water generated in the esterification reaction was removed by azeotropic distillation, the unreacted 2-methoxy-1-propanol and acetic acid were removed and recovered to obtain 2-methoxy-1-propanol acetate. The method of the invention realizes continuous production of 2-methoxy-1-propanol acetate, the operation mode is simple, the production efficiency of 2-methoxy-1-propanol acetate is significantly improved, and the production cost is reduced, and can reduce the solid pollutants and wastewater discharge, has excellent large-scale industrial application value.