Device and method for extracting helium through natural gas low-temperature throttling
A natural gas and low-temperature technology, which is applied in the field of natural gas low-temperature throttling and extraction of helium, can solve the problems of high investment and complicated process flow, and achieve the effect of reducing energy consumption and optimizing cooling capacity of the device
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Embodiment 1
[0026] Such as figure 1As shown, a natural gas low-temperature throttling extracting helium device includes a cold box 2 and a flash tank 16, the cold box 2 is connected to the natural gas inlet pipeline 1, and the cold box 2 is provided with a first throttle valve The pipeline of 14 is connected with the flash tank 16, and the top gas phase outlet of the flash tank 16 is connected with the cold box 2 through a pipeline, and after the top gas phase of the flash tank 16 is condensed in the cold box 2, it is connected with the separation tank 19 connection, the gas phase outlet at the top of the separation tank 19 is connected to the cold box 2 through a pipeline, and after being reheated by the cold box 2, it is sent to the subsequent process through a pipeline, and the liquid phase outlet at the bottom of the separation tank 19 is provided with a second section The pipeline of the flow valve 23 is connected with the cold box 2, and after being reheated by the cold box 2, it is...
Embodiment 2
[0034] Such as figure 2 As shown, embodiment 2 is basically the same as embodiment 1, and its main difference is: the outlet end of the precooling section in the described cold box 2 is connected with the deheavy hydrocarbon tower 4 by pipeline, and the top of the deheavy hydrocarbon tower 4 The outlet of the gas phase is connected to the inlet end of the secondary precooling section in the cold box 2 through a pipeline, and the outlet end of the secondary precooling section in the cold box 2 is connected to the reflux tank 7 of the heavy hydrocarbon removal tower through a pipeline. The gas phase of the tower reflux tank 7 is connected with the condensation section in the cold box 2 through a pipeline; The upper part is connected, and the liquid hydrocarbons at the bottom of the heavy hydrocarbon removal tower 4 are sent to the subsequent process through the pipeline.
[0035] Based on the above-mentioned structural design differences, the main difference in the low-tempera...
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