Device for preparing fluorenone by means of liquid phase oxidation and preparation method thereof
A liquid-phase oxidation method and the technology of fluorenone, which are applied in the preparation of carbon-based compounds, chemical instruments and methods, and the preparation of organic compounds, etc., can solve the problems of increasing equipment, large amount of solvent and catalyst, and inability to carry out the reaction, so as to avoid Caking and clogging, easy control of fluorene oxidation reaction, sufficient effect of fluorene oxidation reaction
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0021] like figure 1 A device for preparing fluorenone by liquid-phase oxidation method is shown, including reactor 1, static mixer 2, material circulation equipment 3 and hot water circulation equipment 4, and the volume in static mixer 2 is about the same as that of reactor 1 About 1 / 10 of the internal volume, the reactor 1 is provided with a stirrer 5, the top of the reactor 1 is provided with a feeding port 11, a solvent inflow pipe 12, a vacuum input pipe 13 and a thermometer 15, and the bottom of the reactor 1 is provided with Outlet pipe 14, water bath 6 is arranged on the outside of the bottom of reactor 1, jacket 7 is arranged on the outside of static mixer 2, material circulation equipment 3 comprises material output pipe 31, material input pipe 32 and circulation pump 33, material output pipe 31 is connected with the bottom of the reactor 1 and the bottom of the static mixer 2, the material input pipe 32 is connected with the top of the reactor 1 and the top of the ...
Embodiment 2
[0023]The method for preparing fluorenone with the device of Example 1, after opening the vacuum input pipe 13, 40kg dimethyl sulfoxide and 0.55kg catalyst (sodium hydroxide or potassium hydroxide, etc.) are imported into the reactor 1 from the solvent inflow pipe 12 , close the vacuum input pipe 13, and then put 50kg of industrial fluorene into the reactor 1 from the feeding port 11, so that the fluorene, dimethyl sulfoxide and catalyst are dissolved and mixed into materials, and the hot water circulation equipment 4 is opened, and the steam input pipe 91 Input steam, let the water temperature in the water tank 9 be about 50~75 ℃, the temperature is controlled by the temperature control meter 94 on the water tank 9, when the water temperature is too high, input normal temperature water from the supplementary water input pipe 92 to cool down, and then use the hot water pump 43 Let the hot water circulate between the water tank 9-hot water output pipe 41-water bath 6 and the jac...
Embodiment 3
[0025] It is basically the same as Example 2, except that the consumption of industrial fluorene is 250kg, the consumption of dimethyl sulfoxide is 200kg, the consumption of catalyst is 2.5kg, and the flow rate of industrial oxygen is 6m 3 / hr, the fluorene cycle oxidation reaction time is 4 hours, and the yield of fluorene into fluorenone is above 99.7%.
[0026] The ratio of fluorene consumption and dimethyl sulfoxide consumption in embodiment 2 and embodiment 3 also can be 1: 0.9, 1: 1.0 or 1: 0.7 etc.; The ratio of fluorene consumption and catalyst consumption also can be 1: 0.013 or 1 : 0.015, etc., and 1: 0.03, 1: 0.05, 1: 0.08KG 1: 0.1, etc.; the fluorene cycle oxidation reaction time can also be 5 hours or 2.5 hours, etc., which are not listed here.
[0027] Dimethyl sulfoxide in Example 2 and Example 3 can also be replaced by other solvents.
[0028] Embodiment 2 and embodiment 3 compare with the reaction parameter of comparative document 1 and comparative document 2...
PUM
Login to View More Abstract
Description
Claims
Application Information
Login to View More 
