Equipment and method for utilizing cold energy in demethanizer with multi-stream plate fin reboiler
A demethanizer, plate-fin type technology, applied in the field of cold energy utilization equipment in the demethanizer, can solve problems such as uneven flow and heat distribution, affecting the stable operation of the device, affecting product quality indicators, etc., to achieve cold capacity integration Take advantage of optimization, improve stability and quality of the product, avoid the effect of setting a large number
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no. 1 approach
[0043] This embodiment relates to equipment for utilization of cold energy in a demethanizer with a multi-flow plate-fin reboiler, such as figure 1 As shown, the equipment at least includes raw natural gas 3, reflux lean natural gas 5, high-pressure normal temperature mixed refrigerant 6, main cold box 8, low-temperature separator 9, coaxial booster expander 12, demethanizer 15 and multiple flow plates Finned reboiler 22; the main cold box 8 and the multi-stream plate-finned reboiler 22 have multiple feed ports and discharge ports respectively, and the demethanizer 15 has a multi-stream stream inlet, and the demethanizer 15 The last tray of the lower part is provided with a reboiled condensate exit tower port 16 and a reboiled condensate return tower port 17, and the bottom of the demethanizer 15 is provided with a C 2 + Mixed hydrocarbon outlet 27,
[0044] The raw material natural gas 3 is connected with the fourth inlet of the main cold box 8 through a pipeline, and the f...
no. 2 approach
[0051] The first embodiment of the present invention relates to a method for utilizing cold energy in a demethanizer with a multi-flow plate-fin reboiler, referring to figure 1 , including the following steps:
[0052] S1, the high-pressure and normal-temperature mixed refrigerant 6 from the outside is used as the main heat source at the bottom of the demethanizer 15, and enters the multi-flow plate-fin reboiler 22 for pre-cooling;
[0053] S2, return the lean natural gas 5 as the secondary heat source at the bottom of the demethanizer 15, and enter the multi-flow plate-fin reboiler 22 for precooling;
[0054] S3, the mixed refrigerant precooled in step S1 is introduced into the main cold box 8 for cooling and supercooling; then the mixed refrigerant J-T valve 24 throttles down the pressure and lowers the temperature and returns to the main cold box 8 to give the cooling capacity. After the mixed refrigerant reheats, it flows out of the main cold box 8 to become a low-pressur...
no. 3 approach
[0064] On the basis of the first embodiment, further, the top of the demethanizer 15 is provided with a low-temperature lean natural gas outlet 30, and the low-temperature lean natural gas outlet 30 passes through the pipeline and the second feed port of the main cold box 8, The second outlet of the main cold box 8 is connected to the inlet of the coaxial booster expander 12 through a pipeline, and the outlet of the coaxial booster expander 12 is connected to C 2 + Mixed hydrocarbon lean natural gas recovery tank 1.
[0065] Further, the side wall of the middle and upper part of the demethanizer 15 is provided with a side boiling condensate outlet 28 from the tower and a side boiling condensate inlet 29 back to the tower. The condensate inlet 29 forms a circulation loop with the sixth feed port and the sixth discharge port of the main cold box 8 .
[0066] Further, a raw natural gas boundary valve 7 is installed on the connecting pipeline between the raw natural gas 3 and th...
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