Intelligent reaction system and process for synthesizing dimethyl carbonate through liquid-phase oxidative carbonylation of methanol
A technology of liquid-phase oxidation of dimethyl carbonate, which is applied in the fields of carbon monoxide and oxygen preparation, chemical/physical/physical-chemical reactors, chemical/physical/physical-chemical processes, etc., can solve the problems of low system reaction efficiency and achieve improvement Effects of reaction efficiency, mass transfer enhancement, and guaranteed reaction rate
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Embodiment 1
[0098] Methanol liquid phase oxide synthesis of dimethyl carbonate is carbonate using the above system and process.
[0099] Catalysts in the process are polyvinylpyridine load chloride catalysts;
[0100] The feed molar ratio of oxygen and carbon monoxide is 7: 9, and the liquid phase methanol is 0.6h. -1 ;
[0101] In the process, the reaction tower reaction temperature is 100 ° C, and the reaction pressure is 1 MPa;
[0102] The first micro-interface generator inner gas ratio is 700: 1, and the second micro interface generator is 300: 1.
Embodiment 2
[0104] Methanol liquid phase oxide synthesis of dimethyl carbonate is carbonate using the above system and process.
[0105] Catalysts in the process are polyvinylpyridine load chloride catalysts;
[0106] The feed molar ratio of oxygen and carbon monoxide is 7: 9.3, and the liquid phase methanol is 0.65 h. -1 ;
[0107] In the process, the reaction tower reaction temperature is 108 ° C, and the reaction pressure is 1.1 MPa;
[0108] The first micro-interface generator inner gas ratio is 740: 1, the second micro interface generator inner gas ratio is 360: 1.
Embodiment 3
[0110] Methanol liquid phase oxide synthesis of dimethyl carbonate is carbonate using the above system and process.
[0111] Catalysts in the process are polyvinylpyridine load chloride catalysts;
[0112] The feed molar ratio of oxygen and carbon monoxide is 7.5: 9, and the liquid phase methanol is 0.67 h. -1 ;
[0113] In the process, the reaction tower reaction temperature is 116 ° C, and the reaction pressure is 1.2 MPa;
[0114] The first micro-interface generator inner gas ratio is 780: 1, the second micro interface generator inner gas ratio is 420: 1.
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