Delayed coking system and method capable of producing coal-series and oil-series needle coke in time-sharing manner
A technology of oil-based needle coke and delayed coking, applied in the field of needle coke, can solve the problems of periodic fluctuation of the device system, fluctuation of fractionation tower operation, poor economic benefits, etc., achieve stable material balance and heat balance, and save equipment investment And the effect of occupying space and improving production capacity
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Embodiment 1
[0027] A delayed coking system capable of time-sharing production of coal-based and oil-based needle coke, including a raw material heating furnace 5, a carrier gas heating furnace 19, a coking tower A8, a coking tower B16, a coal-based fractionating tower 12, and an oil-based fractionating tower 13 , the input end of the raw material heating furnace 5 is respectively connected to the coal-based raw material feed branch pipe 1 and the oil-based raw material feed branch pipe 2 through the raw material feed pipe 4, and the output end of the raw material heating furnace 5 is connected to the raw material output pipe 6, and the raw material output pipe 6 passes through Four-way valve A7 is connected to coking tower A8 and coking tower B16; cracked gas output branch pipe A9 of coking tower A8 and cracked gas output branch pipe B10 of coking tower B16 are connected to coal series fractionation tower 12 and oil series fractionation tower 13 through four-way valve B11 The input end of ...
Embodiment 2
[0033] A delayed coking method capable of time-sharing production of coal-based and oil-based needle coke, using an attached figure 1 The process mainly includes the following steps:
[0034] (1) Preheat coking tower A, coking tower B, coal-based fractionating tower and oil-based fractionating tower with high-temperature inert gas from an external source, and the coal-based raw materials or oil-based raw materials are fed through the coal-based raw material feeding branch pipe and the oil-based raw material respectively. The material branch pipe enters the raw material heating furnace;
[0035] (2) After heating, the coking reaction is carried out under the conditions of variable temperature, variable pressure and / or variable cycle ratio. It is planned that coking tower A will produce oil-based needle coke, and coking tower B will produce coal-based needle coke. The coke generation cycle is 60 Hour;
[0036] (3) When coking tower A feeds into production, coking tower B is in a...
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