A kind of device and method for preparing propyl propionate by column flashing type heat pump reactive distillation
A technology of propyl propionate and reactive distillation, applied in the field of rectification, which can solve the problems of heat exchange mismatch, insufficient heat utilization, energy waste, etc., to reduce condensation heat exchange load, save heating heat source, and reduce energy consumption Effect
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0031] Attached figure 1 In the shown process flow, the reactive distillation tower 1 adopted has 45 trays, the propionic acid feed inlet is the 7th tray, and the propanol feed inlet is the 31st tray; The operating pressure is 101.3kPa, the temperature at the top of the reaction distillation tower top area 16 is 104°C, the temperature at the bottom of the reaction distillation tower bottom recovery area 18 is 117°C, the power of the first compressor 9 is 213kW, and the first throttle valve The outlet pressure of 11 is 19kPa.
[0032] The raw material propionic acid is heated to the bubble point by the raw material propionic acid preheater 6 at 50 kmol / h, and is then fed from the upper part of the reaction separation zone 17 of the reactive distillation column, and 50 kmol / h of propanol with a low boiling point is preheated and exchanged by the raw material propanol After the device 5 is heated to the bubble point, it is mixed with 10 kmol / h of propanol and propyl propionate m...
Embodiment 2
[0036] Attached figure 1 In the shown process flow, the reactive distillation tower 1 adopted has 48 trays, the propionic acid feed inlet is the 8th tray, and the propanol feed inlet is the 32nd tray; The operating pressure is 101.3kPa, the temperature at the top of the top separation zone 16 of the reactive distillation column is 104°C, the temperature at the bottom of the bottom recovery zone 18 of the reactive distillation column is 117°C, the power of the first compressor 9 is 226kW, and the first throttling The outlet pressure of valve 11 is 17kPa.
[0037] After the raw material propionic acid is heated by the raw material propionic acid preheater 6 at 100 kmol / h, it is fed from the upper part of the reaction separation zone 17 of the reactive distillation column, and 100 kmol / h of propanol with a low boiling point is heated by the raw material propanol preheating heat exchanger 5 Finally mix with the propanol and propyl propionate mixture 20kmol / h that returns from the...
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, Popular Technical Reports.
© 2024 PatSnap. All rights reserved.Legal|Privacy policy|Modern Slavery Act Transparency Statement|Sitemap|About US| Contact US: help@patsnap.com