Polyether glycol or polyether monohydric alcohol preparation method
A technology for polyether polyols and monohydric alcohols, applied in chemical instruments and methods, organic compound/hydride/coordination complex catalysts, physical/chemical process catalysts, etc., capable of solving the hydrophobicity of polyether polyols or monohydric alcohols Reduce, unable to reach a high proportion of terminal primary hydroxyl groups, reduce moisture resistance of polyurethane and various other physical properties and other issues
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0062] Add 100.4 grams of propylene glycol-propylene oxide adduct (PPG-1000, weight average molecular weight is about 1000, provided by Jiangsu Haian Petrochemical Company) in a 500 ml autoclave (produced by Weihai Automatic Control Company) equipped with agitator and temperature control device And 0.02 grams of catalyst A1 [1,2-(C 6 f 5 ) 2 BC 6 f 4 B(C 6 f 5 ) 2 ]. After replacing the air in the kettle with nitrogen, dehydrate at 100°C for two hours under reduced pressure, and then add 200.5 grams of propylene oxide dropwise at a reaction temperature of 70-100°C to keep the reaction pressure not exceeding 3 atmospheres, and the reaction takes about 5 hours. After the polymerization was completed, it was neutralized with an aqueous sodium hydroxide solution. 3.0 g of synthetic diatomaceous earth and water were added, and the mixture was treated at 100°C for 3 hours. The mixture is taken out from the autoclave, filtered, and dehydrated to obtain 298.3 grams of liquid ...
Embodiment 2
[0064] Except that the catalyst is changed to A2 [1,4-(C 6 f 5 ) 2 BC 6 f 4 B(C 6 f 5 ) 2 ] Outside, other experimental conditions are identical with embodiment 1, can obtain 295.3 grams of liquid polyoxypropylene propylene glycol ring-opening polymer D2, productive rate is about 98.2%, Mw=3059, Mw / Mn=1.32, terminal primary hydroxylation rate 91%.
Embodiment 3
[0066] Except that the catalyst is changed to A3, other experimental conditions are the same as in Example 1, and 280.3 grams of liquid polyoxypropylene propylene glycol ring-opening polymer D3 can be obtained, with a yield of about 93.3%, Mw=2850, Mw / Mn=1.42, and the end The primary hydroxylation rate is 83%.
PUM
Login to View More Abstract
Description
Claims
Application Information
Login to View More 