Reaction device suitable for strong heat release system
A reaction device and system technology, applied in chemical/physical/physical chemical fixed reactors, mixers, chemical/physical/physical chemical processes, etc., can solve low reaction conversion rate, high safety risk, and reduced reaction selectivity and other problems, to achieve the effect of strengthening the mass transfer between liquid and liquid phases, good mass and heat transfer effects, and reducing the volume of the mixing chamber
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Embodiment 1
[0038] In the present embodiment, raw material is the red base KD solution that volume concentration is 50% and the sodium nitrite solution that volume concentration is 24%, flow rate is respectively 100L / h, 128L / h, and reaction device is placed in constant temperature ice-water bath, controlled temperature is T a= 0°C, the maximum temperature is set to T max =10°C, the reaction rate equation is
[0039]
[0040] Among them, the reaction activation energy E is 72.88kJ / mol, the gas constant unit R is 8.314J / (mol K), X is the conversion rate, and the heat of reaction-ΔH R is 95kJ / mol, and the heat transfer coefficient K is 200w / (m 2 ° C), C p The average specific heat capacity is 484J / (mol·K), the red base KD solution and the sodium nitrite solution respectively flow into two main pipes 3 through the metering pump 1 and branch into 2 n-1 branch, then enter 2 through pre-mixer 2 n-1 n-level column tube 6, the initial concentration C after mixing A,n 1087mol / m 3 , C B,n...
Embodiment 2
[0049] In this embodiment, the raw materials are red-based KD solution with a volume concentration of 55% and sodium nitrite solution with a volume concentration of 25%, and the flow rates are 400 L / h and 512 L / h respectively. Other conditions are identical with embodiment 1, and total initial concentration C A,n 1200mol / m 3 , C B,n 1862mol / m 3 , calculated by formula (4) to obtain the possible maximum reaction rate -r A,n 41.8mol / m 3 s (the temperature T is calculated using T max ), calculated by formula (1) d max 2.02×10 -3 m, take the inner diameter as 2mm, select 2.4×0.2mm stainless steel pipe, take the flow rate of n-level tube 6 as 0.7m / s, the number of n-level tube 6 can be 115, take 128, that is 2 n-1 =128, that is, n=8, it is 8-stage tubes 6, and the tubes of all levels adopt the shape of corrugated tubes.
[0050] The concentration at the inlet and outlet of each level of tubes can be obtained from the formula (1), and the minimum length of each level of tube...
Embodiment 3
[0059] In the present embodiment, raw material is the red base KD solution that volume concentration is 60% and volume concentration is 20% sodium nitrite solution, flow rate is respectively 200L / h, 256L / h, and other conditions are identical with embodiment 1, initial concentration C A,n 1304mol / m 3 , C B,n 1690mol / m 3 , calculated by formula (4) to obtain the possible maximum reaction rate -r A,n 41.8mol / m 3 s (the temperature T is calculated using T max ), calculated by formula (1) d max 2.02×10 -3 m, take the inner diameter as 2mm, select 2.4×0.2mm stainless steel pipe, take the flow rate of n-level tube 6 as 0.7m / s, the number of n-level tube 6 can be 59, take 64, that is 2 n-1 =64, that is, n=7, which is 7-level tubes 6, and the tubes of each level are in the shape of corrugated tubes.
[0060] The inlet and outlet concentrations of each stage of tubes can be obtained from formula (1), and the minimum length of each stage of tubes can be obtained from formulas (2),...
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