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THE CHEMISTRY OF THERMAL CRACKINGLet us consider the cracking of n-hexane to propane, C3H8, and propene, C3H6 at room temperature (298 K). In chemistry there are two factors that determine whether a reaction can occur.
We will always deal with the thermodynamics of the reaction first, because if it says that the reaction cannot occur, it will not happen. A reaction can occur only if the change in Free Energy of the system from reactants to products, ΔG, is negative. ΔG = ΔH − TΔS where ΔH is the change in enthalpy for the reaction and ΔS is the change in entropy for the reaction. When ΔG < 0 ; then we consider whether the energy of the system is sufficient for the reagents to "climb" over the activation energy barrier to become the product. What we are saying is; when ΔG < 0, it is like a car parked on a level ground on top of a hill. The only obstacle that prevented the car from rolling down the hill is a bump in front of the car. If some one has enough strength to push the car across the bump the car should roll down the hill.
Let us now increase the temperature to about 400˚C (700 K).
Thermodynamics says that this reaction is possible. The change in entropy of the system is now sufficient to overcome the change in enthalpy. At 700 K the system is of sufficient energy to cross the activation energy barrier. So this reaction will take place. At lower temperatures the chains preferred to break up in the middle. At higher temperature it is more likely to be broken off at the ends. To obtain smaller molecules, cracking is conducted at high temperature of above 800˚C (that is 1100 K). Ethylene and propylene are obtained from the cracking of ethane and propane, which are by-products of the various cracking processes to yield gasoline. Ethylene and propylene are the raw materials for 50 - 60% of all organic chemicals. MECHANISM OF CRACKING ETHANE
In thermal cracking the by-products are hydrogen and methane. The alkenes formed are more likely to be reduced by hydrogen to give alkanes. So a short residence time would give a better yield of alkenes.
The important by-reactions in the cracking of ethane are;
STEAM CRACKINGWhen a large molecule is broken up into many smaller molecules the pressure of the system increases. (pV=nRT, so p increases with n). Increase in pressure encourages the formed of coke (or carbon). To minimise coke formation steam is added to reduce the partial pressure of the hydrocarbon. So steam cracking is used to prepare ethylene and propylene. The alkane gas is mixed with steam at ca 1000�C and the mixture is passed through Cr-Ni tubes. The mixture is then quenched to 300 �C, scrubbed to remove hydrogen sulphide and carbon dioxide and distilled. The by-products are butane and 1−butene. The difference in the boiling points of the C4s are about 9�C and so they cannot be separated by distillation.
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| CH3(CH2)5CH3 | � | CH3CH2CH3 + CH3CH2CH=CH2 | CH3CH2CH3 | � | CH4 + CH2=CH2 | CH3CH2CH3 | � | CH3CH=CH2 + H2 | CH3CH2CH=CH2 | � | 2 CH2=CH2 | CH3CH2CH=CH2 | � | CH2=CH-CH=CH2 + H2 |
SOME RESULTS OF STEAM CRACKING
| RAW MATERIAL | |||||
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Ethane | Propane | Butane | Naphtha | |
| steam/feed ratio by wt. % conversion Temperature / �C |
0.45 69 835 |
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0.75 92 800 | PRODUCTS | Weight % |
| Ethylene Propylene H2 + Methane C4 C5 Others |
80 2 14 4 |
42 21 27 10 |
38 15 23 24 |
24 16 15 12 26 7 | |
| Note: Naphtha feedstock (Wt %): C3 & C4 = 8; C5 = 22; C6 = 20; C7 = 17; C8 = 12; C9 = 12; C10−C15 = 9. n-alkanes = 30; iso-alkanes = 40; naphthenes = 18; aromatics = 12. | |||||
Butane and the aromatics are obtained by the catalytic reforming of naphtha. The aromatics obtained are benzene, toluene, and xylenes (o−xylene, m−xylene, and p−xylene). Toluene and xylene are used to blend with gasoline to give aviation fuel.
Let us consider the cracking of n-hexane, C6H14, to its branched isomer, neo-hexane (2,2-dimethylbutane), C6H14, at 298 K (that is room temperature).
| n−hexane | neo−hexane | n−hexane � neo-hexane | |
| ΔH˚ / kJ mol‾� ΔS˚ / kJ mol‾� K‾� ΔG˚ / kJ |
− 167 + 0.389 |
− 186 + 0.359 |
(− 186)− (− 167) = − 19 (0.359 - 0.389) = − 0.030 (− 19) − (298K)(− 0.030) = − 10 |
Thermodynamic allows this reaction to occur, but the system does not have the necessary energy to cross the activation energy barrier, to become the product. So the reaction do not take place.
Let us now increase the temperature to 700 K.
| n-hexane | neo-hexane | n-hexane � neo-hexane | |
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ΔfH�(700 K) / kJ mol‾� S�(700 K) / J K‾� mol‾� ΔG˚ / kJ |
−141 406 |
−158 373 |
−19 −0.033 −19 − (700 x −0.033) = 4.1 |
The decrease in entropy with temperature finally succumb to the lose in enthalpy. Now thermodynamics does not permit this reaction to occur, so there is no need to talk about the activation energy barrier.
| The Fisher-Tropsch Process | ||||
| 2 CO + 4 H2 | � | CH2=CH2 + 2 H2O | ΔH�298 = −211 kJ mol‾� | |
Oxidative coupling of methane | ||||
| 2 CH4 + � O2 | � | CH3CH3 + H2O | ΔH�298 = −177 kJ mol‾� | |
| CH3CH3 + � O2 | � | CH2=CH2 + H2O | ΔH�298 = −105 kJ mol‾� | Side products are carbon monoxide and carbon dioxide. |
From methanol | ||||
| 2 CH3OH | ↔ | CH3−O−CH3 + H2O | ΔH�298 = −23.6 kJ mol‾� | |
| CH3−O−CH3 | � | CH2=CH2 + H2O | ΔH�298 = −5.5 kJ mol‾� | |
| CH2=CH2 + CH3OH | � | CH2=CH−CH3 + H2O | ||
Some important commercial chemicals from the primary products of cracking - ethylene, propylene, benzene, toluene and xylenes - are given below.
| ORGANIC CHEMICALS Acrylonitrile Aniline Benzene 1,3−Butadiene Cumene Ethylbenzene Ethylene Ethylene dichloride Ethylene oxide 2−Ethylhexanol Isopropyl alcohol Propylene Styrene Urea 0-Xylene |
1990 1,180 450 770 1400 1,950 3,800 16,500 6,300 2,430 300 660 9,900 3,600 7,400 430 |
2000 1,550 850 1,090 2,000 3,740 6,000 25,100 9,900 3,870 370 660 14,400 5,400 6,900 490 |
NOTE: The bulk of the ethylene and propylene is used to manufacture plastic bottles for oils and supermarket plastic bags. So take care of the environment by reusing your plastic bags.
Reference: Kennesaw State University
Interesting reading: Shell Chemicals