Regarding the operation of the isooctane plant
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Our company has an isooctane production facility. Since it’s a new facility, there hasn’t been much in-depth research done on it. I would like to ask about the control parameters for n-butane and isobutane; any guidance on the operating methods as well as the factors that influence each other would be greatly appreciated. Thank you.
n-Butane is a substance that serves no purpose in the entire apparatus; the less of it there is, the better, whether as a raw material or within the apparatus. In the feedstock, it is desirable to maintain a ratio of isobutane to olefins of 1.1 to 1.2, with a circulating isobutane concentration of around 75%-78%
Although I don’t understand these numbers, I still want to give a like
n-Butane does not participate in the reaction throughout the process; an excess of it will increase energy consumption. Isobutane is the raw material for the reaction; the theoretical ratio of isobutane to olefins is one to one, but in actual production, a slightly higher amount of isobutane is required than olefins.
n-Butane does not participate in the reaction throughout the process; an excess of it will increase energy consumption. Isobutane is the raw material for the reaction; the theoretical ratio of isobutane to olefins is one to one, but in actual production, a slightly higher amount of isobutane is required than olefins.