Two-tower type pressure reducing coke tar distillation process and apparatus therefor
A technology of tar and process, which is applied in the field of large-scale coal tar processing new projects, can solve the problems of difficult on-site operation, large project investment, and operation complexity, etc., and achieve full utilization of waste heat, low gas consumption, and improved operation environmental effects
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[0037] The present invention will be described in further detail below in conjunction with the accompanying drawings and specific embodiments.
[0038] Such as figure 1 As shown, the raw tar first enters the tar / heavy oil heat exchanger 18 to exchange heat with the heavy oil fraction, and then enters the tar preheater 9, where it is heated to 125-135°C by heat transfer oil, and then enters the pre-dehydration tower 1.
[0039] The temperature at the top of the pre-dehydration tower is about 110-125°C. The light oil fraction and water escaping from the top of the tower are first cooled to 50-60°C by 1# light oil air cooler 7, and then cooled to 40°C by 1# light oil cooler 10. ~45°C, it flows into the 1# light oil separator 26, and the separated light oil is used as the reflux of the dehydration tower, and the separated water flows into the ammonia water tank after further separating the oil. The tar at the bottom of the pre-dehydration tower flows into the dehydration tower 2...
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