Process method for heating thickened oil by adopting thermo-acoustic heat pump in oil field station gathering and transportation
A process method and heat pump technology, applied in the pipeline system, lighting and heating equipment, machine operation mode, etc., can solve the problems of high economic operation cost, high energy consumption of heavy oil heating technology, etc., and achieve heat transfer and anti-scaling performance Good, long service life, small one-time investment effect
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Embodiment 1
[0023] Such as figure 1 As shown, the system for heating heavy oil using thermoacoustic heat pumps in oil field gathering and transportation in the present invention includes thermoacoustic driven double-acting traveling wave heat pumps, solar heaters, oilfield associated gas burners, heavy oil heat exchangers and control modules.
[0024] Such as figure 2 As shown, the thermoacoustic-driven double-acting traveling wave heat pump includes two parts: a double-acting traveling-wave engine and a double-acting traveling-wave heat pump. The double-acting traveling-wave engine consists of a main water cooler, a first regenerator, and a first heater , the first heat buffer pipe, and the secondary water cooler are sequentially connected in series. The heaters are sequentially connected in series. Among them, the first heater of the double-acting traveling wave engine is mainly heated by solar energy clean energy, supplemented by oil field associated gas combustion heating, so that ...
Embodiment 2
[0031] The system and process method used in this embodiment are as in embodiment 1. The difference from the above embodiment 1 is that the values of temperature, flow rate, density and viscosity of the heavy oil after pretreatment at the oilfield gathering station are larger than those in the above embodiment 1. .
[0032] The parameters of the heavy oil after pretreatment (when entering the heating device) and after heating in an oilfield gathering and transportation station are shown in Table 2:
[0033] Table 2 Heavy oil parameters before and after heating
[0034] project Before heating after heating temperature(℃) 49 71 Flow(m3 / h) 35 35.2 Pressure (MPa) 0.5 0.54 Density (kg / m 3 )
Embodiment 3
[0036] The system and process method adopted in this embodiment are as in embodiment 1. The difference from the above embodiment 1 is that the temperature and density of the heavy oil pretreated at the oil field gathering station are larger than those in the above embodiment 1, and the flow rate and viscosity are higher than those in the above embodiment 1. The numerical value is smaller than that of Example 1 above.
[0037] The parameters of heavy oil after pretreatment (when entering the heating device) and after heating in a gathering station of an oilfield are shown in Table 3.
[0038] Table 3 Heavy oil parameters before and after heating
[0039] project Before heating after heating temperature(℃) 53 69 Flow(m3 / h) 33 33.1 Pressure (MPa) 0.5 0.53 Density (kg / m 3 )
[0040] Through the comparison of the above examples, it is shown that after the heavy oil is heated by the thermoacoustic heat pump of the present invention, the visc...
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