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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

Pending Publication Date: 2020-10-09
XIAN CHANGQING TECH ENG +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] The demethanizer realizes the separation of methane from ethane and above light hydrocarbon components by adopting the principle of rectification and separation, with a reboiler at the bottom of the tower and a condensing reflux at the top of the tower. At present, the reboiler at the bottom of the demethanizer for similar projects The forms of all the tubes and tubes are used in the reboiler, because the processing scale of the single set of equipment in this project is very large (1500×10 4 m 3 / d), ranking the top three in the world and the largest in Asia, if a conventional tube-and-tube kettle reboiler is used, 2 to 3 reboilers will be installed in parallel, not only the process is complicated, the investment is high, the floor area is large, and the installation and maintenance are inconvenient It is easy to cause uneven flow and heat distribution, which will affect the stable operation of the device, and then affect the quality index of the product

Method used

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  • Equipment and method for utilizing cold energy in demethanizer with multi-stream plate fin reboiler

Examples

Experimental program
Comparison scheme
Effect test

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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Abstract

The invention provides equipment and method for utilizing cold energy in a demethanizer with a multi-stream plate fin reboiler. The equipment for utilizing the cold energy in the demethanizer with themulti-stream plate fin reboiler at least comprises a raw material natural gas, a backflow lean natural gas, a high pressure normal temperature mixed refrigerant, a main cooling box, a low temperatureseparator, a coaxial pressure increased expansion machine, the demethanizer and the multi-stream plate fin reboiler. According to the equipment and method for utilizing the cold energy in the demethanizer with the multi-stream plate fin reboiler, by using the multi-stream plate fin reboiler as a demethanizer bottom reboiler, the defects of a large setting number, large floor area and inconvenientoverhead mounting of a traditional tubular heat exchanger are avoided; and by using a measure of supplementing other material flows, the maximum heat exchanging temperature of a plate-fin heat exchanger is reduced so that the defect of small heat transfer temperature difference of the plate-fin heat exchanger is overcome.

Description

technical field [0001] The invention belongs to the field of natural gas processing, and in particular relates to equipment and a method for utilizing cold energy in a demethanizer with a multi-flow plate-fin reboiler. Background technique [0002] Ethane is a high-quality raw material for ethylene, and the production cost of cracking ethane to produce ethylene is two-thirds of that of naphtha. Internationally, ethylene raw material C 2 -C 4 Accounted for about 48%, while my country is restricted by raw materials, mainly naphtha. Recovering ethane products from natural gas and using them as raw materials for ethylene production by steam thermal cracking has positive significance for increasing the output of ethylene products, reducing energy consumption of ethylene plants, and improving quality and efficiency. [0003] The total amount of Upper Paleozoic natural gas produced by Changqing Oilfield is large, and contains large-scale ethane and above heavy hydrocarbon compone...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): F25J3/02
CPCF25J3/0209F25J3/0233F25J3/0295F25J3/0238F25J2200/02F25J2270/12F25J2200/76F25J2200/40F25J2205/04F25J2240/02F25J2200/50F25J2270/66
Inventor 刘子兵常志波粱璇玑邱鹏范君来张璞薛岗薛政张磊赵东升
Owner XIAN CHANGQING TECH ENG
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