18.2 Isopropanol manufacture
18.2.2 Process technology (Figure 18.1)
Figure 18.1 Flow sheet of Isopropanol manufacture
18.2.3 Uses of Isopropanol :
There may be many uses of iso-propanol, industrial as well as common uses. It finds use in pharmaceutical applications because of the low toxicity of any residues. Isopropanol is also used as a chemical intermediate in some industrial processes. It is also used as a gasoline additive.
18.2.4 Technical questions
1. Why refrigerated brine is used in the sulfonation reactor?
Ans: The reaction temperature is room temperature (25 – 30 oC). Therefore, refrigerated fluid is used. Brine is used here, as refrigerated is antifreeze and can allow solution to reach lower temperatures without freezing problem.
2. Why a partial condenser but not total condenser is used to separate C3 from alcohol + ether?
Ans: Apart from costs, the total condenser produces a single stream and this is of no use as propylene must be separated and sent as a gas back to the sulfonation reactor. All this is achieved in a single process unit by using partial condensation principle.
3. Why is isopropyl ether circulated back to the sulfonation reactor?
Ans: To suppress the side reaction and hence decomposition of sulfonation to less valued product.
4. Present the working principle of an azeotropic distillation column?
Ans: The azeotropic distillation column is fed with the azeotrope mixture and another component which forms a low boiling heterogenous azeotrope with the feed (azetropic mixture) components as one of the products and a purer compound as the other product. The low boiling azeotrope is then sent to a gravity settler that separates the heterogeneous phases into two products namely the azeotropic agent and an impure mixture of the original components. The impure mixture is actually fed to one of the distillation columns in the process flow sheet at a location that matches with the purity of the stream.
5. What happens to the water in which acid gets dissolved in the hydrolyzer cum stripper column?
Ans: Here, the stream is a weak acid stream that is fed to a multiple effect evaporator to concentrate the weak acid solution to a strong acid solution. The strong acid solution then can be used as one of the raw materials in the process.
6. Can you do heat integration for the partial condenser with the sulfonation reactor?
Ans: No, the reason is that sulfonation reaction is highly exotermic and heat needs to be quickly removed. This is not possible when vapors are used as the cooling stream as gas phase heat transfer coefficients are significantly lower than the liquid phase heat transfer coefficients.
7. Can a partial condenser be used for the ether column?
Ans: Yes, the reason is that there is no hard and fast rule that isopropyl ether be added in the liquid phase to the sulfonation reactor. In fact, it should be added as a vapour phase only and therefore, partial condenser should be used in place of total condenser to save costs as well as meet the process specifications.
18.3 Acetone manufacture from isopropanol
18.3.2 Process Technology (Figure 18.2)
Figure 18.2 Flow sheet of acetone manufacture from isopropanol
18.3.3 Uses of Acetone :
Aceone is used as a polar, aprotic solvent in a variety of organic reactions. One important property for which it is used as laboratory solvent is because does not form an azeotrope with water.
Acetone is also used in various medical and cosmetic applications. It also forms an important component in food additives and food packaging.
18.3.4 Technical questions
1. Is pure isopropanol required as feedstock in the reactor?
Ans: This question is asked due to the fact that isopropanol production process involves the formation of an azeotrope with 87 % Isopropanol and 13 % water. Therefore, if the azeotrope itself can be used as feedstock, then one can save azeotropic column costs if an acetone plant is constructed next to the isopropanol.
Yes, isopropanol azeotrope can be used as a feed stock. In this case, the water will not react and will condense in the condenser after the reactor.
2. Can’t we feed the product gases directly to the water absorber eliminating the condenser?
Ans: The condenser removes the condensable components from the product vapors. If condenser is not used, then the hot vapors move to the absorber and absorber load and degree of separation should be pretty high and hence higher cost. Therefore, it’s better to use the water cooling condenser.
3. Apply lechartlier principle and suggest what pressures be operated in the reactor. Eventually comment on the existing pressures?
Ans: If we apply Lechartlier principle, dehydrogenation reaction is favoured by lower pressures. However, higher pressures are used in this case. If the pressure of the system does not play a critical role in the conversion, then higher pressures are favoured as they reduce the size of the reactor significantly for the throughput available. Also, higher pressures are favourable for absorption and reduce the water load in the absorption column.
4. Why is water from the isopropanol fractionators cooled and sent to the water absorber unit?
Ans: This is due to the fact that absorption is favoured at lower temperature and higher pressure.
5. Why is isopropanol again sent to the compressor along with the feed?
Ans: The operating pressures of the absorber, acetone fractionator and isopropanol fractionators reduce sequentially as the stream progresses to the right side. Therefore, the last column produces the product with about atmospheric pressure only. Therefore, to bring it back to 5 atm as in the reactor conditions, the stream has to be compressed along with the feed stream.