Energy saving method and equipment for rectification separation
A rectification separation and equipment technology, which is applied in the field of energy-saving rectification separation and equipment, can solve the problems of consuming the heat load of the condenser, the heat load of the reboiler, inconvenient start-up operation, and no thermal coupling, etc., so as to reduce the heat load of condensation, The effect of saving heat removal heat load and reducing comprehensive energy consumption
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Embodiment 1
[0030] In this embodiment, the single-column rectification column is changed to a double-column double-pressure series connection, a condenser and an intermediate reboiler are thermally coupled, and an additional reboiler is adjusted. The flow diagram is shown in Figure 3.
[0031] It is composed of two rectification towers A and B, the bottom of tower A (1) is connected with a reboiler (3), the outlet at the bottom of the tower is connected with the inlet of tower B (2), and the outlet at the top of tower A is connected with The intermediate reboiler (4) is connected, the intermediate reboiler is connected with a reflux tank (8), the reflux tank is connected with the top inlet of the A tower through the reflux pump (6), and the intermediate reboiler is connected with the lower part of the B tower. One end of the adjustable reboiler (5) is connected to the bottom of the B tower, and the other end is connected to the still liquid outflow pipeline at the bottom of the B tower. P...
Embodiment 2
[0034] In this embodiment, the double-tower rectification tower is changed to a double-tower double-pressure series connection, a condenser and an intermediate reboiler are thermally coupled, and an additional adjustment is made to the reboiler. When the feed is in the A tower, the flow diagram is shown in Figure 4, and the process The flow process is as in Example 1. The fresh raw material first enters the A tower, and the product I is evaporated from the top of the tower. After being deheated and condensed by the condenser and the intermediate reboiler of the B tower, it enters the reflux tank for buffering, and part of the reflux returns to the top of the tower. For production of product I, the tower is equipped with a typical reboiler, and the still liquid is taken out and enters tower B. Tower B steams light product II from the top of the tower. The classic condenser removes heat and condenses, and enters the reflux tank for buffering. Part of the reflux returns to the top...
Embodiment 3
[0036]In this embodiment, the double-tower rectification tower is changed to a double-tower double-pressure series connection, a condenser and an intermediate reboiler are thermally coupled and an additional adjustment of the reboiler process is carried out. The process equipment is the same as in Example 1. When the feed is in the B tower, Referring to accompanying drawing 5, fresh raw material enters tower B at first, and product I is steamed out at the top of the tower, is deheated and condensed by the typical condenser of tower B, enters the reflux tank for buffering, and part of the reflux returns to the top of the tower, and the remainder is extracted as product I. An additional regulating reboiler is added at the bottom of the tower to ensure the normal operation of the B tower. The liquid in the bottom of the tower is taken out and enters the A tower. The boiler removes heat, condenses, enters the reflux tank for buffering, part of the reflux returns to the top of the t...
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