Rapid fuel gas condensation system with double-tower direct spray
A condensing system and direct technology, applied in direct contact heat exchangers, indirect heat exchangers, petroleum industry, etc., can solve the problem of insufficient condensation of condensable gases, reduce bio-oil yield, increase process difficulty and cost, etc. problems, to achieve the effect of meeting the requirements of rapid cooling, speeding up the condensation speed, and fast cooling speed
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Embodiment 1
[0023] Please refer to figure 1 , the double-tower direct spray cracking gas rapid condensation system of the present invention comprises a first-stage spray tower 10 provided with a high-temperature pyrolysis gas inlet 101 and a pyrolysis gas outlet 102, a pyrolysis gas inlet 302 and a non-condensable gas The second-stage spray tower 30 of the outlet 303, the connecting pipe 130 connecting the pyrolysis gas outlet 102 of the first-stage spray tower 10 and the pyrolysis gas inlet 302 of the second-stage spray tower 30, and the first-stage spray The bio-oil storage tank 108 connected to the condensed bio-oil outlet of the tower 10, the bio-oil storage tank 308 connected to the condensed bio-oil outlet of the second-stage spray tower 30, the first atomized spraying subsystem (in this embodiment Including a first atomizing spray unit 104, a first circulating oil pump 106 connected to a first bio-oil storage tank 108, and a first heat exchange unit connected between the first circ...
Embodiment 2
[0031] As another kind of scheme of the present invention, other parts are identical with embodiment 1, and difference is:
[0032] The condensing medium used for the first atomizing spray unit 10 and the second atomizing spray unit 30 can come from outside the system, that is, the bio-oil generated by the system itself is not used, so the system can not be provided with the first heat exchanger 10 and the second heat exchanger 30.
[0033] Moreover, the high-temperature pyrolysis gas inlet 101 of the first-stage spray tower 10 is arranged below the pyrolysis gas outlet 102, that is, the first-stage spray tower also adopts a reverse spraying path with the gas.
Embodiment 3
[0035] As another kind of scheme of the present invention, other parts are identical with embodiment 1, and difference is:
[0036] Using a heat exchanger, a circulating oil pump and a bio-oil storage tank, the bio-oil produced by the first-stage spray tower 10 and the second-stage spray tower 30 all enters the same bio-oil storage tank, and part of the bio-oil is produced by the same bio-oil storage tank. A circulating oil pump is sent to the same heat exchanger for cooling and then sent to the first atomizing spray unit 104 and the second atomizing spray unit 304 respectively.
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