Processing technology for water/ash-containing tar
A processing technology and tar technology, which is applied to the processing technology field of water/ash tar, can solve the problems of waste of resources, difficult to remove, and low utilization value of tar, and achieve the effects of convenient operation, stable oil quality and simple process
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Embodiment 1
[0019] a. Stand for dehydration
[0020] Put the raw material tar containing moisture and ash powder in the storage tank 1 into the reaction kettle 2 equipped with steam heating through the delivery pump 12. The temperature of the reaction kettle is controlled at 80°C, and then polyoxypropylene polyoxyethylene glycol ether is added to cross-link type crude oil demulsifier (POI-2420) and keep stirring for 25 minutes to break the emulsified tar. The pump 12 directly sends the raw material tar to the static separation tank 4 for static dehydration. The weight ratio of the demulsifier to the raw material tar is 0.020:100, the temperature of the separation tank is 80° C., and the static separation time is 60 minutes to separate the water and the tar. layer, the water content of the tar after standing and separating is 4.0% by weight, and a heater is arranged in the storage tank 1, and the heating temperature is 80° C. to maintain the fluidity of the tar.
[0021] b. Flash dehydrat...
Embodiment 2
[0031] a. Stand for dehydration
[0032] Put the raw material tar containing water and ash powder in the storage tank 1 into the reaction kettle 2 equipped with steam heating through the delivery pump 12. The temperature of the reaction kettle is controlled at 85°C, and then polyoxypropylene polyoxyethylene glycol ether is added to cross-link type crude oil demulsifier (POI-2420) and keep stirring for 20 minutes to demulsify the emulsified tar. The raw tar after demulsification is sent to the standing separation tank 3 with heat preservation. If the raw tar is not emulsified, it will pass through The transfer pump 12 directly sends the raw material tar to the static separation tank 4 for static dehydration. The weight ratio of the demulsifier to the raw material tar is 0.020:100, the temperature of the separation tank is 80° C., and the static separation time is 80 minutes, so that the water and the tar Layering, the water content of the tar after standing and separating is 3....
Embodiment 3
[0043] a. Stand for dehydration
[0044] Put the raw material tar containing water and ash powder in the storage tank 1 into the reaction kettle 2 equipped with steam heating through the delivery pump 12. The temperature of the reaction kettle is controlled at 90°C, and then polyoxypropylene polyoxyethylene glycol ether is added to cross-link type crude oil demulsifier (POI-2420) and keep stirring for 30 minutes to demulsify the emulsified tar. The raw tar after demulsification is sent to the static separation tank 3 with heat preservation. If the raw tar is not emulsified, it will pass through The delivery pump 12 directly sends the raw material tar to the static separation tank 4 for static dehydration. The weight ratio of the demulsifier to the raw material tar is 0.015:100, the temperature of the separation tank is 90° C., and the static separation time is 100 minutes, so that the water and the tar Layering, the water content of the tar after standing and separating is 3.0...
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