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The proposed method is applied to the operation optimization of ethylene cracking furnace.
A feasible solution is provided for the multi-objective operation optimization of ethylene cracking furnace.
The ethylene cracking furnace system is crucial for an olefin plant.
The results will be helpful for the design and operation in cracking furnace.
The tubular reactor in a naphtha cracking furnace is modelled rigorously in this paper.
In this paper, a distributed parameter model for tubular reactor in the ethylene cracking furnace based on 3-D temperature reconstruction is developed.
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The results are helpful in the design of optimal operational conditions and ultimately in controlling of ethylene cracking furnaces which will be discussed briefly.
The experimental and simulation results confirm the great potential for the application of the SFT technology in steam cracking furnaces because of the lower average wall temperatures and the resulting reduction of coke formation in the reactor coil.
It is suggested that more sophisticated turbulence chemistry interaction models like the EDC model and more Detailed Reaction Kinetics should be used for combustion modeling in steam cracking furnaces under normal firing conditions.
Detailed experimental data in the form of describing slab cracking, the furnace temperatures, temperature distributions within the slab, vertical deflections and horizontal displacements are presented.
It is well known that hydrocarbon feed stock streams, such as naphtha, LPG, or gas oil are cracked in a furnace to produce mixtures of hydrocarbons of varying molecular weight [14, 15, 16, 17, 18, 19], a typical percentage composition (by weight) is presented in Table 1.
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