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Production of MTBE (Methyl Tertiary Butyl Ether) from Methanol and Butylene by Catalytic Conversion

Group:2 Supervisor :Dr. Khalid Mehmood Co superviser: Engr. Iqra Saleem Group Members • • • •

Aqib Amir* Muhammad Numan Asim Rafique Muhammad Nasir

2015-CH-434 2015-CH-415 2015-CH-428 2015-CH-445

Why we choose MTBE • To address prevailing conditions of Smog in last few years • Octane booster • Improves air quality by reducing emission of CO and other HCs • Favorable over MMT(methylcyclopentadienyl manganese tricarbonyl)[1] How ?

Direct Effect

Oxygen allows more complete fuel combustion

How much?

• Fuel ethers reduce CO and total Hydrocarbon emissions by same % as their content in gasoline

Source:[1] International Journal of Energy Engineering 2017, 7(3): 65-73 [2] The European fuel oxygenates association

Scope in Pakistan Replacement on MMT(methyl cyclopentadienyl manganese tri carbonyl)[1] Continuous increase in gasoline consumption Gasoline production-Pakistan 60

50

Thousands of bbl per day

• •

50

45

40

30

20

10

0

source: The U.S. Energy Information Administration

Process Flow Diagram

Source: Proceedings of the Third International Conference on Modeling, Simulation and Applied Optimization Sharjah,U.A.E,2009

Source: Proceedings of the Third International Conference on Modeling, Simulation and Applied Optimization Sharjah,U.A.E,2009

Mass balance across Reactor

Mass In = 1130221.13 kgs

5

6 Mass out = 1130221.13 kgs

Distillation column 910 D= 123793.22 Kgs

6

Total mass in= 1130221 Kgs

7

W= 1006427.9 Kgs

Absorber 13

12

Mass in= 123793.22 Kgs

10

11

Mass out= 257786.7357 Kgs

Flash Drum 15 10 Mass out= 9432.9047 Kgs

10 14

10 16

Mass in= 257786.7357

Mass out= 248353.8310 Kgs

Methanol recovery column 10 21

Mass out= 76838.3296 Kgs

Mass in= 248353.8310 Kgs

10 17

18 10 Mass out= 171515.5014 Kgs

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