Thread Content
This post was last edited by Refiner on 2018-7-4 08:51. After starting the catalyst preparation fans and putting the pre-heated dry gas into use, it was not possible to increase the circulation rate; the reaction temperature dropped, the amount of slurry increased immediately, the flow rate at the compressor inlet decreased right away, the system pressure rose, and the pressure difference between the two vessels decreased. The situation became increasingly unfavorable, until finally the reaction temperature dropped to 490 degrees, and the compressor no longer had any room for adjustment and could not continue operating. Switching to pre-heated steam immediately improved all conditions. After repeating the switching several times, the situation improved with pre-heated dry gas, but it was still not as effective as using pre-heated steam. Of course, this is because the catalyst’s properties deteriorated after heating with burning oil before operations started, and no fresh material was added immediately; but it can’t be that serious, right? Solve! ! ! !
What is the difference between the flow rate of the pre-heated dry gas and the flow rate of the pre-heated steam?
1. Was the liquid cut off before dry gas was put into use? 2. Does switching to the backup unit result in a decrease in burning capacity, which in turn affects the carbon pile and causes the reaction temperature to drop?
I’ve never encountered this situation. Logically, using pre-heated dry gas should increase the flow rate at the compressor inlet, as it increases the circulation volume
Incomplete combustion of the catalyst and low activity result in low cracking efficiency, while the use of dry gas further reduces the depth of the reaction
Is there any change before and after increasing the dry gas volume?
The flow rates of the pre-lift dry gas and pre-lift steam should be different; increase the dry gas flow rate and see.
Has the problem been solved? Please share the specific reasons