Method for continuously preparing alkenyl succinic anhydride by microchannel reactor
A technology of microchannel reactor and alkenyl succinic anhydride, which is applied in the direction of chemical instruments and methods, chemical/physical/physical chemical reactors, chemical/physical/physical chemical processes, etc., can solve the problem of increasing catalyst removal procedures and pipeline length , can not be carried out continuously, etc., to achieve the effect of saving the process of catalyst recovery, continuous and efficient reaction, and reducing manual operation
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Embodiment 1
[0022] This embodiment provides a method for continuously preparing alkenyl succinic anhydride in a microchannel reactor, which specifically includes the following steps:
[0023] Step 1) heat-melt maleic anhydride in a reaction tank, and the heat-melt temperature is 75° C. to obtain a hot-melt maleic anhydride;
[0024] Step 2) by two metering pumps, the maleic anhydride hot melt and the sixteen internal olefins obtained in step 1 are pumped into the microchannel reactor simultaneously, wherein the mol ratio of the maleic anhydride and the sixteenth internal olefins is 1 : 1, the material of the microchannel reactor is silicon carbide;
[0025] Step 3) react in a microchannel reactor, the reaction temperature is 220°C, the reaction residence time is 0.5min, and the reaction pressure is 0.7MPa;
[0026] Step 4) After the reaction, the discharged product was purified by vacuum distillation to obtain alkenyl succinic anhydride as an oily amber liquid with a yield of 70%.
Embodiment 2
[0028] This embodiment provides a method for continuously preparing alkenyl succinic anhydride in a microchannel reactor, which specifically includes the following steps:
[0029] Step 1) heat-melt maleic anhydride in a reaction tank, and the heat-melt temperature is 75° C. to obtain a hot-melt maleic anhydride;
[0030] Step 2) by two metering pumps, the maleic anhydride hot melt obtained in step 1 and octadecylidene are pumped into the microchannel reactor simultaneously, wherein the mol ratio of maleic anhydride and octadecadene is 2.5 : 1, the material of the microchannel reactor is Hastelloy;
[0031] Step 3) react in a microchannel reactor, the reaction temperature is 240°C, the reaction residence time is 3min, and the reaction pressure is 0.1MPa;
[0032] Step 4) After the reaction, the discharged product was purified by vacuum distillation to obtain alkenyl succinic anhydride as an oily thick amber liquid with a yield of 75%.
Embodiment 3
[0034] This embodiment provides a method for continuously preparing alkenyl succinic anhydride in a microchannel reactor, which specifically includes the following steps:
[0035] Step 1) heat-melt maleic anhydride in a reaction tank, and the heat-melt temperature is 75° C. to obtain a hot-melt maleic anhydride;
[0036] Step 2) by two metering pumps, the maleic anhydride hot melt obtained in step 1 and the carbon dodecacene are pumped into the microchannel reactor simultaneously, wherein the mol ratio of the maleic anhydride and the carbon dodecacene is 2 : 1, the material of the microchannel reactor is stainless steel;
[0037] Step 3) react in a microchannel reactor, the reaction temperature is 270°C, the reaction residence time is 2min, and the reaction pressure is 0.2MPa;
[0038] Step 4) After the reaction, the discharged product was purified by vacuum distillation to obtain alkenyl succinic anhydride as an oily thick amber liquid with a yield of 78%.
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