Low temperature rectification cascade system for rectifying CO to produce stable isotope 13C
A technology of stable isotope and low-temperature rectification, which is applied in the field of stable isotope separation of carbon, can solve the problems of large pressure drop in cascading devices, difficult construction, and high energy consumption of transportation equipment, and achieve the effect of continuous operation
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Embodiment 1
[0038] The cascade device in Example 1 consists of four-stage distillation towers. The process flow diagram of the cascade device is as follows figure 2 Shown. The CO raw material is measured by the flow meter F1 and transported from the line L3 to the middle of the first-stage tower T1. The T1 tower is filled with wire mesh corrugated packing, which is the reflux liquid condensed in the top condenser C1 and the bottom reboiler B1 The vaporized steam provides a surface for heat and mass transfer. Take out high-abundance carbon-12 from the top of T1 tower via line L2, take out a part of steam from the T1 tower kettle, measure it through valve V1 and flow meter F2 under the drive of pressure, and send it to the middle of tower T2 along line L4, T2 tower It is filled with metal wire mesh corrugated packing to provide heat and mass transfer surfaces for the refluxed liquid in the condenser C2 at the top of the tower and the vaporized vapor in the reboiler B2 at the bottom of the t...
Embodiment 2
[0044] The cascade device in Example 2 is composed of four-stage distillation towers. The process flow diagram of the cascade device is as follows Figure 4 Shown. The CO raw material is measured by the flow meter F1 and transported from the line L3 to the middle of the first-stage tower T1. The T1 tower is filled with wire mesh corrugated packing, which is the reflux liquid condensed in the top condenser C1 and the bottom reboiler B1 The vaporized steam provides a surface for heat and mass transfer. Take out high-abundance carbon-12 from the top of T1 tower via line L2, take out a part of steam from the T1 tower kettle, drive by pressure via valve V1 and flow meter F2, and then send it to the middle of tower T2 along line L4 ( Figure 4 Midpoint d), the T2 tower is filled with wire mesh corrugated packing to provide heat and mass transfer surfaces for the refluxed liquid in the condenser C2 at the top of the tower and the vaporized vapor in the reboiler B2 at the bottom of the ...
Embodiment 3
[0050] A kind of rectified CO to produce stable isotope 13 C's cryogenic rectification cascade system is a cascade device composed of two horizontally placed rectification towers with gradually narrower diameters. The rectification tower consists of a top condenser, a bottom reboiler and a rectification column. The rectification towers are connected by pipelines. The first-stage rectification tower inputs the raw materials from the middle part, and the vapor from the top of the later-stage rectification tower is transported to the middle part of the front-stage rectification tower by pressure through the pipeline. The liquid produced in the bottom of the front-stage rectification tower is vaporized in the pipeline It is transported to the middle of the post-rectification tower under pressure, and the vapor from the top of the post-rectification tower can enter the front-stage rectification tower at the feed point of the previous-stage rectification tower. The rectification towe...
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