Process and device for continuous acidification of acidification section in production of sebacic acid
A sebacic acid and process technology, applied in the field of continuous acidification process and its process equipment, can solve problems such as restricting the development of enterprises and industries, waste of water resources, energy, and inability to achieve continuous production, and achieve quality assurance, stable operation, and overcoming problems. The effect of corrosion and acidification crystallizing tank
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Embodiment 1
[0027] According to the sebacic acid production continuous acidification process of the present invention, comprises the following steps:
[0028]The decolorizing liquid is heated to 92°C with steam in the storage tank, pumped into the acidifier through a rotameter with a pipeline pump, and at the same time, sulfuric acid is added to the acidifier at a ratio of 15% to control the pH value of the feed liquid at 2. The liquid flows from the acidifier to the first heating tank by virtue of the high level difference, and the heater is used in the first heating tank to heat the feed liquid to above 100°C, so that the feed liquid is mixed and boiled, and the feed liquid flows to the second heating tank by itself. Continue heating to further make the feed liquid fully boil. The feed liquid flows from the second heating tank to the acidification crystallization tank. 27 revolutions per minute, after the feed liquid passes through the fourth to seventh stage acidification crystallizati...
Embodiment 2
[0030] According to the sebacic acid production continuous acidification process of the present invention, comprises the following steps:
[0031] The decolorizing liquid is heated to 96°C with steam in the storage tank, pumped into the acidifier through a rotameter with a pipeline pump, and at the same time, sulfuric acid is added to the acidifier at a ratio of 18%, and the pH value of the feed liquid is controlled at 1.5. The liquid flows from the acidifier to the first heating tank by virtue of the high level difference, and the heater is used in the first heating tank to heat the feed liquid to above 100°C, so that the feed liquid is mixed and boiled, and the feed liquid flows to the second heating tank by itself. Continue heating to further make the feed liquid fully boil. The feed liquid flows from the second heating tank to the acidification crystallization tank. 30 revolutions per minute, after the feed liquid passes through the fourth to seventh stage acidification cr...
Embodiment 3
[0033] According to the sebacic acid production continuous acidification process of the present invention, comprises the following steps:
[0034] The decolorization liquid is heated to 97°C with steam in the storage tank, and then pumped into the acidifier through a rotameter with a pipeline pump. At the same time, 20% sulfuric acid is added to the acidifier to control the pH value of the feed liquid at 1.5. The liquid flows from the acidifier to the first heating tank by virtue of the high level difference, and the heater is used in the first heating tank to heat the feed liquid to above 100°C, so that the feed liquid is mixed and boiled, and the feed liquid flows to the second heating tank by itself. Continue heating to further make the feed liquid fully boil. The feed liquid flows from the second heating tank to the acidification crystallization tank. 25 revolutions per minute, after the feed liquid passes through the acidification crystallization tank from the fourth to t...
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