Generating furnace tar treatment method
A treatment method and technology of a generator, which are applied in the removal of tar by water, coke ovens, petroleum industry, etc., can solve the problems of odor and incomplete combustion, waste, environmental pollution of phenol resources, etc., and achieve effective utilization and environmental protection. Pollution, the effect of improving one's own value
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Embodiment 1
[0011] moisture
[0012] The processing method of generator tar is characterized in that its manufacturing steps are as follows:
[0013] 1) Put the grade I tar whose properties are shown in Table 1 into a high-position bubbling dehydration kettle with a lifting hopper, heat the material to 92°C, and mix the amount of air blown in with the tar 200m 3 The / t ratio is blown into the air for dehydration, and the water content of the dehydrated grade I tar is less than 0.2%, and it flows into the coker by its own gravity.
[0014] 2) The dehydrated grade I tar is heated and carbonized in the coker to 650°C, and the coke produced is discharged into the cooling box, cooled to below 100°C and discharged from the device; the tar vapor distilled from the top of the coker flows into the tar after being condensed and cooled storage tank.
[0015] 3) The tar is pumped into the alkali washing tank and mixed with a 15% sodium hydroxide aqueous solution, the reaction temperature...
Embodiment 2
[0020] The processing method of generator tar is characterized in that its manufacturing steps are as follows:
[0021] 1) Put the grade II tar whose properties are shown in Table 1 into a high-position bubbling dehydration kettle with a lifting hopper, heat the material to 98°C, and mix the amount of air blown in with the tar 200m 3 The / t ratio is blown into the air for dehydration, and the water content of the dehydrated grade II tar is less than 0.2%, and it flows into the coker by its own gravity.
[0022] 2) The dehydrated grade II tar is heated and carbonized in the coker to 500°C, and the coke produced is discharged into the cooling box, cooled to below 100°C and discharged from the device; the tar vapor distilled from the top of the coker flows into the tar after being condensed and cooled storage tank.
[0023] 3) The tar is pumped into the alkali washing tank and mixed with a 15% sodium hydroxide aqueous solution, the reaction temperature is 60°C, and the ratio of ...
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