Recovery method for organic amine in polyphenylene oxide copper-amine complex catalyst
A recovery method and technology of organic amines, applied in the purification/separation of amino compounds, etc., to achieve the effect of reducing production unit consumption and improving recycling rate
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Embodiment 1
[0027] The main components of the raw materials to be treated include: 50% by weight of morpholine, 15% by weight of methanol, 20% by weight of toluene, and the rest are copper ions, water and oligomers.
[0028] First, preheat the raw material to 140°C, and quickly transfer it to the flash tank. The pressure of the flash tank is 1000Pa. Most of the organic components such as morpholine, methanol, toluene contained in the raw material are evaporated, and cooled to the bubble point temperature. After left and right, it is used as the rich gas feed of the absorption tower and enters the lower part of the absorption tower.
[0029] The absorption operation adopts a glass absorption tower with a height-to-diameter ratio of 30, which is filled with metal Raschig ring packing, and the top is connected to a condensing system and a vacuum pump. The liquid phase morpholine as absorbent enters from the upper part of the absorption tower. The two are reversely and fully contacted in the...
Embodiment 2
[0033] The main components of the raw materials to be treated include: 45% pyridine, 20% ethanol, 25% toluene, and the rest are copper ions, water and oligomers.
[0034] First, preheat the raw material to 118°C, and quickly transfer it to the flash tank. The pressure of the flash tank is 100Pa. Most of the organic components such as pyridine, ethanol, toluene contained in the raw material are evaporated, and cooled to about the bubble point temperature. Finally, as the rich gas feed of the absorption tower, it enters the lower part of the absorption tower.
[0035] The absorption operation adopts a glass absorption tower with a height-to-diameter ratio of 20, which is filled with metal Raschig ring packing, and the top is connected to a condensing system and a vacuum pump. Pyridine as absorbent enters from the upper part of the absorption tower. The two are reversely and fully contacted in the absorption tower, and the mass flow rate ratio of the gas-liquid two-phase is 2. ...
Embodiment 3
[0039] The main components of the raw materials to be treated include: 45% by weight of morpholine, 20% by weight of methanol, 20% by weight of toluene, and the rest are copper ions, water and oligomers.
[0040] First, preheat the raw material to 138°C, and quickly transfer it to the flash tank. The pressure of the flash tank is 5000Pa. Most of the organic components such as morpholine, methanol, and toluene contained in the raw material are evaporated, and cooled to the bubble point temperature. After left and right, it is used as the rich gas feed of the absorption tower and enters the lower part of the absorption tower.
[0041] The absorption operation adopts a glass absorption tower with a height-to-diameter ratio of 50, which is filled with metal Raschig ring packing, and the top is connected to a condensing system and a vacuum pump. The liquid phase morpholine as absorbent enters from the upper part of the absorption tower. The two are reversely and fully contacted in...
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