Epoxypropane purifying method
A technology of propylene oxide and purification method, applied in the direction of organic chemistry and the like, can solve the problems of low yield of propylene oxide and large loss of extractant, and achieve the effect of high extraction efficiency and good technical effect.
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Example Embodiment
[0047] [Example 1]
[0048] The crude propylene oxide solution (stream 1) and the solvent recovery tower kettle liquid (stream 5) exchange heat to 80℃ and enter the extractive distillation tower T-101. The extractive distillation tower uses n-octane as the extractant. The flow rate ratio of reagent stream 6 to crude propylene oxide solution feed 1) is 4, and deionized water (stream 12) is sprayed into the gas phase at the top of the tower. After condensation, the oil-water separation operation is carried out in the top phase separator D-101. There are multi-layer partitions in the phaser, and the separated oil layer (stream 8) and the recovered extractant (stream 6) are mixed as the reflux of the extractive distillation column (stream 13), and the separated water layer (stream 9) enters the washing tower T -103, the theoretical plate number of T101 tower is 70, the operating pressure is controlled at 200kPa, the temperature of the tower bottom is 100°C, and the composition of the...
Example Embodiment
[0059] [Example 2]
[0060] The crude propylene oxide solution (stream 1) and the solvent recovery tower kettle liquid (stream 3) exchange heat to 70°C and enter the extractive distillation tower T-101. The extractive distillation tower uses n-heptane as the extractant. The flow rate ratio of reagent stream 6 to crude propylene oxide solution feed 1) is 5:1, and medium-pressure steam (stream 12) is sprayed into the gas phase at the top of the tower. After condensation, the oil-water separation operation is carried out in the top phase separator D-101 , There are multiple baffles in the phase separator, the separated oil layer (stream 8) and the recovered extractant (stream 6) are mixed as the reflux of the extractive distillation column (stream 13), and the separated water layer (stream 9) enters the water washing Column T-103, T101 column has 75 theoretical plates, operating pressure is controlled at 200kPa, tower bottom temperature is 95°C, and the composition of crude propylen...
PUM
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.
© 2024 PatSnap. All rights reserved.Legal|Privacy policy|Modern Slavery Act Transparency Statement|Sitemap