Method for combined production of benzyl alcohol, benzaldehyde and benzoic acid through oxidizing toluene
A technology for benzaldehyde and benzyl alcohol, applied in the field of preparation of aromatic compounds, can solve the problems of polluted product quality, low production efficiency, difficult products, etc., and achieves the effects of safe separation process, reduced generation probability, and improved utilization rate
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0067] The catalyst dissolved in fresh toluene added to the system is HfO 2 , N-hydroxyl o-sulfonyl benzamide, metal phthalocyanine (R) with general formula (IV) structure 1 = H, R 2 =F, M=Fe) and metalloporphyrins (R 1 =R 3 =OH, R 2 =H, M=Ru) with a total concentration of 600 ppm. When the device is in steady state operation, the flow rate of fresh toluene added to the oxidation reactor is 6.1mL / h. At this time, the average residence time of the oxidation reactor in terms of liquid phase substances is 1.6h, and the pressurized pure oxygen is continuously introduced into the oxidation reactor. In the reactor, the reaction temperature of the system is maintained at 179° C., and the reaction pressure is 0.8 MPa. The volume ratio of the amount of water added to the hydrolysis reactor to the oxidation reaction solution entering the hydrolysis reactor is 0.33:1, and pressurized pure oxygen is continuously introduced to maintain the reaction temperature in the hydrolysis reacto...
Embodiment 2
[0069] The catalyst that dissolves in the fresh toluene that adds in the primary oxidation reactor is the metal phthalocyanine (R with general formula (IV) structure 1 = H, R 2 =CH 3 CH 2 , M=Co), the total concentration is 45ppm. When the device is in steady state operation, the flow rate of fresh toluene added to the oxidation reactor is 11.7mL / h. At this time, the average residence time of the oxidation reactor in terms of liquid phase substances is 2.4h, and the pressurized pure oxygen is continuously introduced into the oxidation reactor. In the reactor, the reaction temperature of the system is maintained at 185° C., and the reaction pressure is 2.2 MPa. The volume ratio of the amount of water added to the hydrolysis reactor to the oxidation reaction liquid entering the hydrolysis reactor is 0.90:1, and the reaction temperature in the hydrolysis reactor is maintained at 110°C, and the reaction pressure is 2.0MPa. At this time, the liquid phase residence time in the hy...
Embodiment 3
[0071] The catalyst dissolved in fresh toluene added to the primary oxidation reactor is Mn(Ac) 2· 4H 2 O, metal phthalocyanine (R) with general formula (IV) structure 1 = NO 2 , R 2 =H, M=Co), the metalloporphyrin (R 1 =R 3 = H, R 2 =CH 3 CH 2 , M=Cu) mixture with a total concentration of 120ppm. When the device is in steady state operation, the flow rate of fresh toluene added to the oxidation reactor is 15.3mL / h. At this time, the average residence time of the oxidation reactor in terms of liquid phase substances is 1.5h, and the pressurized pure oxygen is continuously introduced into the oxidation reactor. In the reactor, the reaction temperature of the system is maintained at 175° C., and the reaction pressure is 0.7 MPa. The volume ratio of the amount of water added to the hydrolysis reactor to the oxidation reaction solution entering the hydrolysis reactor is 0.28:1, and pressurized pure oxygen is continuously introduced to maintain the reaction temperature in ...
PUM
Abstract
Description
Claims
Application Information
- R&D Engineer
- R&D Manager
- IP Professional
- Industry Leading Data Capabilities
- Powerful AI technology
- Patent DNA Extraction
Browse by: Latest US Patents, China's latest patents, Technical Efficacy Thesaurus, Application Domain, Technology Topic, Popular Technical Reports.
© 2024 PatSnap. All rights reserved.Legal|Privacy policy|Modern Slavery Act Transparency Statement|Sitemap|About US| Contact US: help@patsnap.com