Cryogenic rectification process-based method for producing air product, and air separation system
a cryogenic rectification and air separation technology, applied in the field of air separation, can solve the problems of compromising the overall energy consumption level of the air separation device, no longer viable to rely solely on this air booster, etc., and achieve the effect of greatly reducing production costs and improving energy efficiency
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Benefits of technology
Problems solved by technology
Method used
Image
Examples
embodiment 1
[0078]After feed air (1 bara) sequentially passes through the main air compressor 21 for pressurization to 6 bara (the first pressure range), the air pre-cooling apparatus 40 for pre-cooling and the air purification apparatus 50 for purification, one portion thereof is split off as a first air stream guided along the first air inlet line 101, through the heat exchange apparatus (the low-pressure plate heat exchanger 31) for heat exchange with a gas or liquid product produced by rectification (e.g., liquid nitrogen discharged from the top of the first column, and / or liquid nitrogen discharged from the top of the second column, and / or a liquid nitrogen fraction discharged from an upper part of the second column), and after cooling down (6 bara), into the first column 11 for rectification; and the other portion passes through the air booster 22 for pressurization to 50 bara (the third pressure range) before being split into a second air stream and a third air stream: the second air str...
embodiment 2
[0090]The cryogenic rectification process system is used to prepare high-pressure or ultra-high-pressure air: as shown in FIG. 2, the fifth air stream is guided along the fifth air inlet line 105 with its flow velocity and flow rate controlled by the first regulating valve 1051, and in the air product outlet line 113, is pressurized to a high pressure or ultra-high pressure by the liquid air booster pump 1131, and vaporized via heat exchange through the heat exchange apparatus (the high-pressure plate heat exchanger 32) to obtain the required high-pressure or ultra-high-pressure air product, which is pressurized feed air.
[0091]In some embodiments, the flow velocity and flow rate of the third air stream depressurized to the first pressure range are optionally controlled by the first regulating valve 1051, and in the air product outlet line 113, said air stream is pressurized to a high pressure or ultra-high pressure by the liquid air booster pump 1131, and vaporized via heat exchange...
PUM
Login to View More Abstract
Description
Claims
Application Information
Login to View More 

