Six-tower reverse quadruple-effect methanol rectification method using pre-rectification tower as heat source
A pre-distillation tower and heat source technology, applied in the field of rectification, can solve the problems of difficult production requirements and high energy consumption, and achieve the effect of improving the utilization rate of raw materials
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Embodiment 1
[0036] like figure 1 As shown, the six-tower reverse four-effect methanol rectification method with the pre-rectification tower as the heat source is connected as follows: the bottom of the pre-rectification tower T1 is connected to the middle and lower part of the vacuum tower T2 through pipelines; the bottom of the vacuum tower T2 The bottom of the atmospheric tower T3 is connected to the middle and lower part of the medium-pressure tower T4 through pipelines; the bottom of the medium-pressure tower T4 is connected to the middle and lower part of the high-pressure tower T5 through pipelines; The side draw of the high-pressure tower T5 is connected to the middle and lower part of the recovery tower T6 through pipelines.
[0037]The present invention adopts four-effect rectification technology, and its technological process comprises the following steps: 1) crude methanol raw material enters pre-rectification tower T1, extracts noncondensable gas and methanol oil; the bottom p...
Embodiment 2
[0041] like figure 2 As shown, the improved device based on the six-tower reverse four-effect methanol rectification method based on the pre-rectification tower as the heat source, its main process flow is the same as figure 1 The multi-effect distillation process is basically the same, the difference is that the water tower T6 is not equipped with a reboiler, and forms a fully coupled state with the lower half of the high-pressure tower T5, and the top of the water tower T6 can obtain a mixed alcohol fuel product with a water content of less than 1000ppm. Qualified purified wastewater is obtained from the bottom of tower T5 and enters the subsequent wastewater treatment system.
[0042] Compared with the existing industrial process, the steam consumption per unit of methanol in this process scheme is 0.5-0.65, which is lower than the unit consumption of methanol / steam in the three-tower and four-tower process (unit consumption is 1.1-1.5), which is different from our propose...
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