Recycling and helium-extracting co-production system and method for light hydrocarbons of helium-poor natural gas
A technology for light hydrocarbon recovery and natural gas, applied in gas fuel, refrigeration and liquefaction, lighting and heating equipment, etc., can solve the problems of insufficient process integration, low thermal design efficiency, and high energy consumption of equipment, and achieves reduction in energy consumption, The effect of reducing the number of equipment and reducing the loss of cooling capacity
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[0047] The gas composition of the raw material gas is shown in Table 1 and the working conditions:
[0048] Raw material gas processing capacity: 5.0×10 5 N m 3 / d
[0049] Raw gas pressure: 6MPa
[0050] Entry temperature: 20°C
[0051] Product quality requirements:
[0052] Saturation vapor pressure of liquefied petroleum gas: P≤1430kPa
[0053] Saturation vapor pressure of stable light hydrocarbons: 74kPa≤P≤200kPa, final boiling point of stable light hydrocarbons: T≤190℃
[0054] Table 1 Feed gas composition
[0055]
[0056] Economic data such as product yield and energy consumption and thermodynamic data are mainly used to make a comprehensive comparison between the cogeneration system of the present invention and a single process. The recovery rate and energy consumption comparison results are shown in Table 2. See Table 3 for temperature difference, minimum heat transfer temperature difference and load comparison.
[0057] Table 2 recovery rate and energy co...
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