Method and device for preparing rosin ester by coupling catalytic esterification and separation
A technology for catalyzing esterification and rosin ester, applied in the field of deep processing of rosin, can solve the problems of high production cost, rosin ester pollution and low profit, and achieve the effects of avoiding pollution, reducing transfer resistance, and strengthening stirring and heat and mass transfer.
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0037] as attached Figure 1-4 As shown, the device for catalyzing esterification-separation coupling to prepare rosin ester method includes: dissolution kettle 1, esterification reactor 2, expander 3, gas-liquid separator 4, turbine compressor 5, separation tower 6, Return pump7.
[0038] The discharge port of the dissolution kettle 1 is connected with the feed port of the esterification reactor 2, and the dissolution kettle 1 is used for dissolving raw materials required for production. The esterification reactor 2 is cylindrical, and the top of the esterification reactor is provided with a feed inlet 21, a gas outlet 22, and the bottom is provided with a discharge outlet 23, and the esterification reactor 2 includes a heating pipe 24, which is a heating coil. It is arranged inside the esterification reactor; the gas distributor 25 includes an air inlet 251 and a plurality of nozzles 252 for exhaust; the expander 3 is connected to the gas outlet of the esterification reacto...
Embodiment 2
[0044] The reaction device that uses is identical with embodiment 1, and a kind of catalytic esterification-separation coupling prepares rosin ester method:
[0045] Add ethanol and rosin in a molar ratio of 3:1 to the melting tank 1, then add glycerin and dimethyl carbonate of 25% of the weight of rosin, heat and melt to form a mixed material, and feed CO2 to press the material into the esterification reactor Inner 2, then raise the temperature to 150°C, and continuously feed CO2 until the pressure inside the esterification reactor 2 is 0.01Mpa, then open the gas outlet valve of the esterification reactor 2, so that the water vapor and glycerin vapor generated during the esterification reaction , dimethyl carbonate vapor, and CO2 mixed gas-phase substances flow out continuously, the outflow volume is ≤12000m3 / h, the pressure is ≤10.0MPa, and enters the gas-liquid separator 4 after being throttled and expanded by the expander 3, and then expanded and dropped by the expander 3 ...
Embodiment 3
[0047] The reaction device that uses is identical with embodiment 1, and a kind of catalytic esterification-separation coupling prepares rosin ester method:
[0048] Glycerol (glycerol) and rosin are added into the melting pot 1 in a molar ratio of 5:1, and the added glycerin and rosin weight of 10% 200# solvent oil are heated and melted to form a mixed material. Enter the esterification reactor 2, then raise the temperature to 100°C, and continuously feed CO2 until the pressure in the esterification reactor 2 is 3.0Mpa, then open the gas outlet valve of the esterification reactor 2, so that the gas generated during the esterification reaction Water vapor, glycerin vapor, 200# solvent oil vapor, and CO2 mixed gas phase substances continuously flow out, the outflow volume is ≤12000m3 / h, and the pressure is ≤10.0MPa. After being throttled and expanded by the expander 3, it enters the gas-liquid separator 4. The expansion and pressure reduction or throttling expansion and pressur...
PUM
Property | Measurement | Unit |
---|---|---|
acid value | aaaaa | aaaaa |
acid value | aaaaa | aaaaa |
acid value | 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