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After a half semester of Industrial Systems classes, you are feeling extremely confident about your ability to make a profit producing and selling chemical products.

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After a half semester of Industrial Systems classes, you are feeling extremely confident about your ability to make a profit producing and selling chemical products. You decide to partner with someone in your class and turn your knowledge into $$$. Your choice chemical for this venture is Resorcinol, produced from benzene and propylene in two steps. The overall reaction can be summarized as: C6H6+C3H6+O2C6H4(OH)2+(CH3)2CO Task 3 - Mass Balance (Reaction). Your hourly production rate is AAA kg/hr. Assume your reaction has BB\% conversion, CC\% yield, and propylene is supplied DD\% in excess. Of the two exiting steams, the liquid stream is pure resorcinol, and the vapour stream is acetone, all unreacted materials, all by-products, and it contains 5% of all the resorcinol produced. Complete the mass balance for your product, including the side reaction from Task 1. Summarize your results in 2 tables: a mole balance table and a mass balance in a table. Use units of kg/hr and kmol/hr. Show your calculations in the appendices but put the tables in the executive summary. Iask 4 - Mass Balance (Separation). To recover the resorcinol from the vapour stream, the mixture is fed to a flash drum (separating vessel). The drum is able to separate 80% of the resorcinol from the inlet stream as a liquid containing 1% acetone (by mass). The rest of the acetone, reactants, by-products and resorcinol exit the flash drum as a vapour. Complete the mass balance (with block diagram and stream table) and calculate the % composition of the vapour. Re-calculate the overall yield of the process, given the quantity of resorcinol lost in this step. Put this adjusted yield value in the executive summary. Task 5 - The synthesis reaction takes place at an optimal temperature of 105C. To improve the plant's overall thermal efficiency, a heat-recovery system is installed which exchanges heat from the product stream exiting the reactor with the reactants going in. If the products exit the heat exchanger at 40C, and the reactants enter the heat exchanger at 25C, and the heat transfer efficiency is 88%, at what temperature do the reactants enter the reactor? Task 6 - The synthesis reaction is highly exothermic; therefore, steam can be created in the jacket of the reactor to maintain a stable temperature. Find the enthalpies of the main reaction and side reaction (or use Hess' law if you can't find them). Based on those enthalpies, and the rates of product and byproduct formation, calculate the rate at which steam can be produced by this reaction. Include the heat required to bring your reactants up to the required 105C (based on Task 5). Give your answer in kg/hr. Cite your sources correctly! Task 7- Based on the data from Task 3, select an appropriate pipe size from the NPS schedule for your resorcinol reactor-exit stream. Fluid velocity should be no more than Em/s to avoid excessive pressure loss. Cite your source for the resorcinol liquid density. Task 8 . Using a target discharge pressure of FF psig and resorcinol flow rate from Task 3, select a pump to move the product from the reactor, through the recovery heat exchanger and into storage. Follow the link below and use the data sheets to select a suitable pump from Goulds. State the suitable pump model, motor size (in HP), RPM, impellor size and state the NPSH the pump would require. You may assume that the pumps perform the same for resorcinol as for water. AAA=558.9ResorcinolBB=83CC=12E=16DD=170FF=119Reactian:-C6H6+C3H6+O2C6H4(OH)2+(CH3)2CO

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