High-pressure condensate oil field natural gas gathering and transportation method, device and gathering and transportation system
A natural gas and oil field technology, applied in pipeline systems, gas/liquid distribution and storage, mechanical equipment, etc., can solve problems such as high maintenance and salvage costs, high initial investment, and large pollution, and reduce the risk of hydrate freezing and blocking. Good economic and environmental benefits, and the effect of reducing production costs
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Embodiment 1
[0032] This embodiment mainly illustrates the technical principle of the method of the present invention.
[0033] This embodiment provides a method for gathering and transporting natural gas in a high-pressure condensate oil field, which is characterized in that it includes:
[0034] Step a: Obtain the target parameters of the mixed fluid produced in the oilfield at the wellhead of the oilfield. The mixed fluid includes natural gas, water and condensate oil.
[0035] Specifically, the high-pressure condensate oil field is a special oil field, and its output is a mixed fluid with multiple components, including natural gas, water, and condensate oil. The target parameters include flow rate, pressure and temperature; wherein, the flow rate includes the total flow rate of the mixed fluid and the flow rates of the individual fluids that make up the mixed fluid.
[0036] Step b: Determine the diameter of the delivery pipeline according to the target parameters and the delivery dis...
Embodiment 2
[0047] This embodiment mainly describes the process of the actual simulation analysis performed according to the method of the present invention, and the simulation analysis is based on the multiphase flow transient simulation analysis software OLGA.
[0048] Step a: Obtain and input the flow rate of the mixed fluid, the pressure at the starting point and the end point of the delivery, and the temperature at the starting point;
[0049] Specifically, the input oil phase flow rate is 53m3 / d, the water phase flow rate is 18m3 / d, the gas phase flow rate is 1.9×104m3 / d, the starting point pressure is 6.4Mpa, the ending point pressure is 4MPa or the starting point pressure is 10Mpa, and the ending point pressure is 8Mpa, The starting temperature was 29°C.
[0050] Step b: According to the relevant parameters input in step a, determine that the pipe diameter of the delivery pipeline is 80mm, and the pipe length is 10km;
[0051] Step c: The multiphase flow transient simulation anal...
Embodiment 3
[0057] This embodiment provides a natural gas gathering and transportation device, which applies the above-mentioned natural gas gathering and transportation method, which includes:
[0058] The delivery pipeline, one end of the delivery pipeline is connected to the wellhead of the oil field;
[0059] The feeding mechanism is arranged at the wellhead connected to the oil field on the conveying pipeline, and the feeding mechanism is used for adding polymerization inhibitor to the mixed fluid in the conveying pipeline.
[0060] Specifically, the delivery pipeline is directly connected to the wellhead without other structures in between, thereby reducing the complexity of the delivery structure, and at the same time making full use of the pressure energy at the wellhead to reduce energy consumption for delivery. At the same time, the natural gas gathering and transportation device of this embodiment applies the above-mentioned natural gas gathering and transportation method, and ...
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