Method for continuously producing monochloroacetone by micro-droplet reactor
A chloroacetone and reactor technology, which is applied in the field of continuous production of high-purity monochloroacetone in a microdroplet reactor, can solve the problems of reduced output, high system energy consumption, low purity of monochloroacetone, etc., and achieves a reduction in polychlorinated products. Generate, operate efficiently and continuously, and purify the effect easily
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0023] Prepared into 35wt% HCl solution under normal temperature and pressure, and passed Cl 2 Saturate to form a dispersed phase, Cl in the dispersed phase 2 The molar concentration is 0.02mol / L. The mass fractions of acetone and cyclohexane in the continuous phase were 20% and 80%, respectively. The dispersed phase and the continuous phase were injected by two syringe pumps into a microchannel made of PTFE and a diameter of 1 mm, respectively. The volume flow ratio of the two phases was 1:1, the reaction temperature was 20 °C, and the total volume flow was 2ml / min, the reaction time was 5 min, and the reaction pressure was 0.2 MPa. The liquid-liquid two-phase leaving the microchannel is layered in a liquid-liquid stratifier, and the cyclohexane phase containing monochloroacetone is put into a rectifying tower for rectification separation, and the content of the obtained monochloroacetone is as high as 99.5%.
Embodiment 2
[0025] Prepare 35% HCl solution at normal temperature and pressure, and pass Cl 2 Saturate to form a dispersed phase, Cl in the dispersed phase 2 The molar concentration is 0.02mol / L. The mass fractions of acetone and cyclohexane in the continuous phase were 20% and 80%, respectively. The dispersed phase and the continuous phase were injected into a microchannel made of PTFE and a diameter of 1 mm by two syringe pumps respectively. The volume flow ratio of the two phases was 1:1, the reaction temperature was 30 °C, and the total volume flow was 2ml / min, the reaction time was 5 min, and the reaction pressure was 0.2 MPa. The liquid-liquid two-phase leaving the microchannel is layered in a liquid-liquid stratifier, and the cyclohexane phase containing monochloroacetone is put into a rectifying tower for rectification separation, and the content of the obtained monochloroacetone is as high as 99.1%.
Embodiment 3
[0027] Prepare 35% HCl solution at normal temperature and pressure, and pass Cl 2 Saturate to form a dispersed phase, Cl in the dispersed phase 2 The molar concentration is 0.02mol / L. The mass fractions of acetone and cyclohexane in the continuous phase were 20% and 80%, respectively. The dispersed phase and the continuous phase were injected by two syringe pumps into a microchannel made of PTFE and a diameter of 1mm, respectively. The volume flow ratio of the two phases was 1:2, the reaction temperature was 30 °C, and the total volume flow was 4ml / min, the reaction time was 5 min, and the reaction pressure was 0.2 MPa. The liquid-liquid two-phase leaving the microchannel is layered in a liquid-liquid stratifier, and the cyclohexane phase containing monochloroacetone is put into a rectifying tower for rectification separation, and the content of the obtained monochloroacetone is as high as 99.2%.
PUM
Property | Measurement | Unit |
---|---|---|
diameter | aaaaa | aaaaa |
Abstract
Description
Claims
Application Information
- R&D Engineer
- R&D Manager
- IP Professional
- Industry Leading Data Capabilities
- Powerful AI technology
- Patent DNA Extraction
Browse by: Latest US Patents, China's latest patents, Technical Efficacy Thesaurus, Application Domain, Technology Topic, Popular Technical Reports.
© 2024 PatSnap. All rights reserved.Legal|Privacy policy|Modern Slavery Act Transparency Statement|Sitemap|About US| Contact US: help@patsnap.com