Method for synthesizing butanol
A technology for n-butanol and butylene oxide, applied in the field of synthesizing n-butanol, can solve the problems of complex process and high cost of n-butanol, and achieve the effects of simple process, good economic benefit and reduced process cost.
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Examples
Embodiment 1
[0012] Load 4.5 mL of supported Ni catalyst into the fixed-bed reactor and keep H 2 : The molar ratio of 1,2-epoxybutane is 5: 1,1,2-epoxybutane is injected into the reactor and mixed with hydrogen through an advection pump, and the mixture is contacted with a supported nickel catalyst to obtain n-butylene alcohol. Reaction conditions: reaction temperature 50°C, reaction pressure 1MPa, reaction bed liquid weight space velocity 0.5h -1 . The obtained product was analyzed by GC / MS, and the conversion rate of 1,2-epoxybutane was 93.45%, and the selectivity of n-butanol was 73.29%.
Embodiment 2
[0014] Load 4.5 mL of supported Pd catalyst into the fixed-bed reactor and keep H 2 The molar ratio of :1,2-butylene oxide is 10:1. Reaction conditions: reaction temperature 160°C, reaction pressure 5MPa, reaction bed liquid weight space velocity 0.1h -1 . Other steps are the same as in Example 1. The obtained product was analyzed by GC / MS, and the conversion rate of 1,2-epoxybutane was 90.59%, and the selectivity of n-butanol was 70.20%.
Embodiment 3
[0016] Load 4.5 mL of supported Pt catalyst into the fixed-bed reactor and keep H 2 The molar ratio of :1,2-butylene oxide is 10:1. Reaction conditions: reaction temperature 160°C, reaction pressure 5MPa, reaction bed liquid weight space velocity 1.0h -1 . Other steps are the same as in Example 1. The obtained product was analyzed by GC / MS, and the conversion rate of 1,2-epoxybutane was 90.03%, and the selectivity of n-butanol was 71.17%.
PUM
Login to View More Abstract
Description
Claims
Application Information
Login to View More