Synthesis method of C22 tribasic ester
A technology of tribasic acid ester and synthesis method, applied in the preparation of carboxylate, chemical instruments and methods, preparation of organic compounds, etc., can solve problems such as unfavorable dibasic acid synthesis, complicated operation steps, unfavorable clean production, etc. Good economic value and practical value, short process flow, and the effect of avoiding solvent recovery and solvent residue problems
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0048] a. Add 100.0g methyl conjugated linoleate (95% purity) and 46.5g dimethyl fumarate (methyl conjugated linoleate / dimethyl fumarate molar ratio=1.0) to the installed thermometer and in a mechanically stirred vessel at N 2 Heating to reflux at a temperature of 150°C for 4 hours under protection, and cooling down to room temperature to obtain crude ester;
[0049] b. Distill the crude ester obtained in step a under reduced pressure at a temperature of 150° C. to distill unreacted methyl linoleate and dimethyl fumarate to obtain high-purity C 22 Trimethyl tribasic acid 135g, product yield 95.4%.
[0050] C 22 The acid value of trimethyl tribasic acid is 0.12mgKOH / g, and the kinematic viscosity at 40°C is 75.23mm 2 / s, temperature 100°C kinematic viscosity 10.31mm 2 / s, viscosity index 121, pour point -67°C, flash point (opening) 236°C, the product has excellent lubricating properties.
Embodiment 2
[0052] a. Add 100.0g methyl conjugated linoleate (95% purity) and 67.0g dibutyl fumarate (methyl conjugated linoleate / dibutyl fumarate molar ratio = 1.1) to the installed thermometer and in a mechanically stirred vessel at N 2 Heating to reflux at a temperature of 180°C for 2 hours under protection, and cooling down to room temperature to obtain crude ester;
[0053] b. Distill the crude ester obtained in step a under reduced pressure at a temperature of 180° C. to distill unreacted methyl linoleate and dibutyl fumarate to obtain high-purity C 22 Dibutyl monomethyl tribasic acid 150g, product yield 97.8%.
[0054] C 22 The acid value of dibutyl monomethyl tribasic acid is 0.05mgKOH / g, the kinematic viscosity at 40℃, 78.41mm 2 / s, temperature 100°C kinematic viscosity 10.85mm 2 / s, viscosity index 126, pour point -46°C, flash point (opening) 248°C, the product has excellent lubricating properties.
Embodiment 3
[0056] a. Add 100g methyl conjugated linoleate (purity 95%) and 137.3g dioctyl fumarate (methyl conjugated linoleate / dioctyl fumarate molar ratio=0.8) to the installation thermometer and In a mechanically stirred vessel, at N 2 Heating to reflux at 200°C for 2.5 hours under protection, cooling to room temperature to obtain the crude ester;
[0057] b. Distill the crude ester obtained in step a under reduced pressure at a temperature of 200° C. to distill unreacted methyl linoleate and dioctyl fumarate to obtain high-purity C 22 Dioctyl monomethyl tribasic acid 195g, product yield 95.2%.
[0058] C 22 The acid value of dioctyl monomethyl tribasic acid is 0.23mgKOH / g, and the kinematic viscosity at 40°C is 80.03mm 2 / s, temperature 100°C kinematic viscosity 11.08mm 2 / s, viscosity index 127, pour point -51°C, flash point (opening) 242°C, the product has excellent lubricating properties.
PUM
| Property | Measurement | Unit |
|---|---|---|
| acid value | aaaaa | aaaaa |
| pour point | aaaaa | aaaaa |
| flash point | aaaaa | aaaaa |
Abstract
Description
Claims
Application Information
Login to View More 
