Communications the feed streams. The inner diameter was 1600 lm. At position 12 a tantalum orifice plate with nine orifices, each 100 lm, was installed. The sulfuric acid was injected here. At position 13 the main components were mixed. At position 14 a tantalum orifice plate with one orifice, 35 lm, was installed. The nitric acid was injected at this point. At position 16 a tantalum orifice plate with one orifice, 35 lm, was installed, and the benzene was injected at this position. At position 15 a tantalum orifice plate with nine orifices, each 100 lm, was installed. The reaction mixture left the first modular component here. After various retention times, the inner diameter was increased to 2000 lm. At position 17 a tantalum orifice plate with nine orifices, each 35 lm, was installed. No orifice plate was installed at position 18. After various retention times a T-piece was installed. At position 21 and 23 a tantalum orifice plate with nine orifices, each 100 lm, was installed. At position 22 a tantalum orifice plate with one orifice, 35 lm, was installed. Sulfuric acid, nitric acid or benzene were alternatively injected at this point. At position 25 a tantalum orifice plate with nine orifices, each 100 lm, was installed. Again, various retention times were realized.Using the described reactor parameters, screening was executed for adiabatic nitration. The reactor was insulated completely. Temperature indicators were installed along the piping for investigation of the reaction. The inlet temperatures of nitric acid, sulfuric acid and benzene were varied. Also influences of retention times, composition of the reaction mixture and dosing of nitric acid, sulfuric acid and benzene at position 22 were investigated. The received data from the microreactor were compared and fit very well to the data from an industrial scale plant. The results from the microreactor were used to improve the product quality in the industrial scale plant.
SummaryUsing the new modular microreactor it is possible to investigate different reactions quickly and without major financial expense. Due to the modularity of the reactor, it can be adapted to simulate industrial scale plants. Nearly all process parameters like temperature, pressure, etc. can be adjusted. Additionally, it is easy to simulate the influence of changes in the equipment. A screening of parameters is possible in less time and with fewer costs. In most cases the results can be directly scaled up and pilot scale plants are not required. Tests in industrial scale production plants are minimized. The new microreactor can be used for isothermal as well as for adiabatic nitrations.The results can normally be directly used in industrial scale plants for process improvement. Also new processes can be developed. A further application for the new reactor is the production of small quantities of products in the laboratory. In particular, thermally unstable and sensitive compounds can be produced as the whole reactor can be operated at very low temperatures.
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