High-selectivity reactor and method for preparing butanedioic anhydride through maleic anhydride liquid-phase hydrogenation
A maleic anhydride liquid-phase method and succinic anhydride technology, applied in chemical instruments and methods, organic chemistry, chemical/physical processes, etc., can solve the problem that succinic anhydride cannot take into account selectivity and large-scale industrial production, and achieve catalyst Small filling volume, avoiding hot spots, and improving selectivity
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[0028] Example 1
[0029] A non-adiabatic reactor A, the specific form is a tubular fixed-bed reactor, and an adiabatic reactor B, the specific form is a fixed-bed reactor. 5.15t / h maleic anhydride 1 and γ-butyrolactone 2 are mixed in a volume ratio of 1:10, and mixed with hydrogen 3 (supplemented new hydrogen + circulating hydrogen) in a volume ratio of 1:2, and then enter the non-adiabatic Reactor A. The reaction mass entered the non-adiabatic reactor from top to bottom, the inlet temperature was 80°C, and the operating pressure of the reactor was 3.0 MPa. In non-adiabatic reactor A, the inner diameter of a single tube of the tube bundle is 190 mm, with 420 tubes, and the tubes are filled with catalyst, and the volumetric space velocity is 0.5 h -1 . The shell side was cooled with circulating water 7 at 30°C, and the flow rate was 90.0 t / h, and it was operated in parallel with the reaction material. The outlet temperature of the non-adiabatic reactor A is 95.0°C, and the...
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[0030] Example 2
[0031]Set up a non-adiabatic reactor A, the specific form of which is a tubular fixed-bed reactor, and an adiabatic reactor B, which is a fixed-bed reactor in the specific form. 5.15t / h maleic anhydride 1 and γ-butyrolactone 2 are mixed in a volume ratio of 1:10, and hydrogen 3 (supplementary new hydrogen + circulating hydrogen) is mixed in a volume ratio of 1:2, and then enters the non-adiabatic Reactor A. The reaction mass entered the non-adiabatic reactor from top to bottom, the inlet temperature was 60 °C, and the operating pressure of the reactor was 3.0 MPa. The inner diameter of a single tube of the tube bundle in the non-adiabatic reactor A is 190 mm, and there are 420 tubes. The tubes are filled with catalyst, and the volume space velocity is 0.66 h-1. The shell side was cooled with circulating water 7 at 30°C, and the flow rate was 90.0 t / h, and it was operated in parallel with the reaction material. The outlet temperature of the non-adiabatic r...
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