Comprehensive recovery method of effective components in N-haloacetyl-7-ACA crystallization mother liquor
A technology of -7-ACA and haloacetyl, which is applied in the field of comprehensive recovery of active ingredients in N-haloacetyl-7-ACA crystallization mother liquor, can solve problems such as waste, large COD, and increased processing costs, and reduce environmental pollution. Pollution, the effect of improving economic benefits
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Embodiment 1
[0036] (1) Recovery of N-bromoacetyl-7-ACA
[0037] Get N-bromoacetyl-7-ACA crystallization mother liquor, wherein N-bromoacetyl-7-ACA concentration is 2.2g / L, triethylamine salt concentration is 12.1g / L (in triethylamine), pH is 1.5, The temperature is 23°C, it is cooled to 4.0°C, and 30% sodium hydroxide solution is added to adjust the pH to 2.5; then the macroporous adsorption resin column bed is passed through the macroporous adsorption resin at a flow rate of 3BV / h (the macroporous adsorption resin model is XAD16N, and the loading capacity is 1L, The ratio of height to diameter is 9), and the amount of loading on the column is 20L in total, and 20L of the adsorption residue (triethylamine concentration 12g / L) is collected at the same time; then, use 0.12mol / L sodium bicarbonate solution to desorb and adsorb on the After desorption of N-bromoacetyl-7-ACA on the resin, 1.1L of desorption liquid was collected after desorption, and the concentration of N-bromoacetyl-7-ACA was...
Embodiment 2
[0041] (1) Recovery of N-bromoacetyl-7-ACA
[0042] Get N-bromoacetyl-7-ACA crystallization mother liquor, wherein N-bromoacetyl-7-ACA concentration is 3g / L, triethylamine salt concentration is 15g / L (in triethylamine), pH is 1.5, temperature 23 ℃, it is cooled to 4.0 ℃, and 30% sodium hydroxide solution is added to adjust the pH to 2.5; Ratio is 9), the amount of loading on the column is 20L in total, and 20L (triethylamine concentration 15g / L) of the residual liquid of adsorption is collected simultaneously; N-bromoacetyl-7-ACA, 1.6L of desorption solution was collected after desorption, and the concentration of N-bromoacetyl-7-ACA was 36g / L; the temperature of the desorption solution was raised to 20°C, and 6M hydrochloric acid was added to adjust the pH of the system to 1.5, N-bromoacetyl-7-ACA was crystallized, centrifuged, washed and dried to obtain 52 g of N-bromoacetyl-7-ACA solid, with a purity of 99% and a yield of 86.7%.
[0043] (2) recovery of triethylamine
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Embodiment 3
[0046] (1) Recovery of N-chloroacetyl-7-ACA
[0047] Get N-chloroacetyl-7-ACA crystallization mother liquor, wherein N-chloroacetyl-7-ACA concentration is 10.7g / L, triethylamine salt concentration is 91.5g / L (in triethylamine), pH is 1.0, The temperature is 5°C, its temperature is controlled at 4.0°C, and 30% sodium hydroxide solution is added to adjust the pH to 3.0; then pass through a macroporous adsorption resin column bed at a flow rate of 0.5BV / h (the macroporous adsorption resin model is LX-1180, The loading capacity is 1L, the height-to-diameter ratio is 15), and the column volume is 3L in total. After the adsorption is completed, wash the column with 0.5BV of purified water, and collect 3.5L of the adsorption residue (triethylamine concentration: 78.1g / L); then, use 0.20 The mol / L sodium bicarbonate solution desorbs the N-chloroacetyl-7-ACA adsorbed on the resin at a flow rate of 0.5BV / h. After the desorption is completed, 0.6L of the desorption solution is collected,...
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