Full Text
Academician A. V. TOPCHIEV, Ya. M. PAUSHKIN, A. V. NEPRYAKHINA,
P. G. ANAN’EV, and N. N. DMITREVSKII
INHIBITION OF THE CRACKING OF HYDROCARBONS IN MOLTEN SODIUM AND POTASSIUM HYDROXIDE
Many metals in the molten or highly dispersed state react with hydrocarbons and hydrocarbon radicals with the formation of organometallic compounds, and also exert a catalytic effect on their transformations \((^{1–12})\). In this connection, a detailed study of the reactions of hydrocarbons with various metals in the most reactive, i.e., molten, state, including high temperatures, under conditions in which free radicals are formed, is of great interest.
In the present work, the transformation of \(n\)-heptane and cyclohexene in the presence of sodium and potassium hydroxide at atmospheric and elevated pressure was studied; for comparison, results are also given for the cracking of \(n\)-heptane in the presence of molten aluminum. Experiments under pressure were carried out in an autoclave, and at atmospheric pressure in a flow apparatus. Vapors of \(n\)-heptane were continuously passed through a layer of molten metal or a packing with potassium hydroxide, 150 mm high, placed in a reactor. The contact time of the vapors with the packing at 700–800° was \(\sim 0.5\) sec. Potassium hydroxide was deposited on activated carbon of grade KAD. The reaction products were collected and analyzed.
Characteristics of the starting products
Sodium: density 0.971, m.p. 97.7°, b.p. 880.9°; \(n\)-heptane: b.p. 98°, \(d^{20}_{4}\) 0.6803, \(n^{20}_{D}\) 1.3960; cyclohexene: b.p. 83–84°, \(d^{20}_{4}\) 0.8072, \(n^{20}_{D}\) 1.4480, iodine number 276; potassium hydroxide: chemically pure reagent, nomenclature No. 946; technical aluminum containing 99.5–99.7% aluminum, m.p. 659.8°.
From the data of Table 1 it is evident that sodium and potassium hydroxide have an inhibiting effect on the cracking of \(n\)-heptane even at 800°: in experiments with them the conversion is 5–7%, whereas in their absence it is 34–57%.
On contact with aluminum, deep transformations of \(n\)-heptane are observed; in this case the conversion increases with increasing temperature and residence time in the reaction zone: the conversion reaches 65.3% at 700° and approaches 100% at 800°, which is almost twice as high as in experiments without aluminum.
The gas from the cracking of \(n\)-heptane in contacts with sodium and KOH differs markedly in composition from the gas of thermal cracking: the bulk of the gas (60–85%) is represented by hydrogen with a low content of unsaturated hydrocarbons.
On contact of \(n\)-heptane with aluminum, gaseous and liquid reaction products characteristic of deep pyrolysis are obtained. Condensation products, including carbides, are also formed.
The condensate obtained from the cracking of \(n\)-heptane in contacts with sodium and with KOH consists of unchanged \(n\)-heptane, i.e., under these conditions no liquid reaction products are formed.
Table 1
Conditions and balance of cracking of n-heptane
| Temp., °C | Feed rate of raw material, ml/hour | Gas yield, wt. % | Condensate yield, wt. % | Conversion, wt. % | Temp., °C | Feed rate of raw material, ml/hour | Gas yield, wt. % | Condensate yield, wt. % | Conversion, wt. % |
|---|---|---|---|---|---|---|---|---|---|
| Experiments with sodium | Experiments with activated carbon KAD | ||||||||
| 200 | 68 | gas formation and cracking do not occur | gas formation and cracking do not occur | 600 | 107 | 5,7 | 91,8 | 9,7 | |
| 300 | 57 | 0,1 | 94,2 | 0,1 | 700 | 105 | 11,5 | 86,6 | 17,9 |
| 450 | 71 | 1,8 | 80,3 | 1,8 | 800 | 102 | 23,7 | 73,5 | 34,7 |
| 500 | 51 | 2,5 | 75,1 | 2,5 | Experiments with aluminum | ||||
| 600 | 60 | 5,6 | 74,2 | 5,6 | 700 | 100 | 50,7 | 43,7 | 65,3 |
| 700 | 83 | 6,8 | 74,0 | 6,8 | 750 | 100 | 78,0 | 9,7 | 97,1 |
| 750 | 85 | 5,5 | 91,1 | 5,5 | 800 | 100 | 72,5 | 12,3 | 99,5 |
| 800 | 108 | 5,4 | 83,8 | 5,4 | 700 | 112 | 27,5 | 67,5 | 49,0 |
| Experiments without sodium | 700 | 66 | 36,9 | 58,7 | 71,0 | ||||
| 700 | 107 | 12,2 | 86,6 | 29,0 | 800 | 140 | 45,7 | 44,6 | 78,2 |
| 800 | 104 | 27,9 | 64,3 | 57,5 | 800 | 86 | 77,3 | 14,0 | 100,0 |
| Experiments with potassium hydroxide deposited on activated carbon KAD | 800 | 69 | 71,0 | 6,4 | 100,0 | ||||
| 600 | 100 | 1,4 | 98,6 | 1,4 | |||||
| 700 | 99 | 3,9 | 96,1 | 3,9 | |||||
| 800 | 96 | 7,4 | 92,6 | 7,4 |
Table 2
Composition of the gas from cracking of n-heptane
| Temp., °C | \(C_nH_{2n}\), vol. % | \(H_2\), vol. % | \(C_nH_{2n+2}\), vol. % | Weight of 1 l of gas, g | Temp., °C | \(C_nH_{2n}\), vol. % | \(H_2\), vol. % | \(C_nH_{2n+2}\), vol. % | Weight of 1 l of gas, g |
|---|---|---|---|---|---|---|---|---|---|
| Experiments with sodium | Experiments with potassium hydroxide deposited on activated carbon KAD | ||||||||
| 200 | gas formation does not occur | gas formation does not occur | 600 | 6,7 | 61,8 | 31,5 | 0,55 | ||
| 300 | 2,2 | 75,0 | 22,8 | 0,45 | 700 | 5,4 | 76,3 | 18,3 | 0,45 |
| 450 | 3,0 | 77,0 | 20,0 | 0,45 | 800 | 7,3 | 62,7 | 30,0 | 0,54 |
| 500 | 10,8 | 70,3 | 18,9 | 0,57 | Experiments with activated carbon KAD | ||||
| 600 | 7,3 | 78,5 | 14,2 | 0,30 | 600 | 22,9 | 47,9 | 29,2 | 0,82 |
| 700 | 2,5 | 83,5 | 14,0 | 0,34 | 700 | 22,5 | 43,1 | 34,4 | 0,74 |
| 750 | 1,0 | 84,6 | 14,4 | 0,25 | 800 | 30,0 | 39,0 | 31,0 | 0,90 |
| 800 | 0,5 | 83,6 | 15,9 | 0,27 | Experiments with aluminum | ||||
| Experiments without sodium | 700 | 50,2 | 15,3 | 34,5 | 1,17 | ||||
| 700 | 40,4 | 12,2 | 47,4 | 1,06 | 750 | 42,3 | 24,2 | 33,5 | 0,97 |
| 800 | 44,0 | 22,5 | 34,0 | 0,993 | 800 | 36,2 | 30,5 | 33,3 | 0,85 |
It may be assumed that in the initial stage at 300—800° the formation of sodium-organic compounds takes place with the evolution of hydrogen, which, at the moment of formation, adds to olefins, and in this way cracking, which is a chain process promoted by olefins, is inhibited.
\[ C_7H_{16}+Na \to C_7H_{15}Na+H;\quad C_nH_{2n}+2H \to C_nH_{2n+2} \]
or
\[ 2C_7H_{16}+C_nH_{2n}+2Na \to 2C_7H_{15}Na+C_nH_{2n+2}. \]
Table 3
Individual composition of the gas from cracking of n-heptane in molten aluminum
(in volume percent)
| Component | At 700° | At 800° | Component | At 700° | At 800° |
|---|---|---|---|---|---|
| Hydrogen | 16.15 | 31.3 | n-Butane | 0.24 | 0.13 |
| Methane | 26.50 | 30.6 | Butene + butene-1 | 1.84 | 1.83 |
| Ethane | 8.95 | 5.8 | Butene-2 cis, trans | 0.58 | 0.14 |
| Ethylene | 31.15 | 21.91 | Butene-2 + C₄H₆ cis, trans | 0.90 | 0.51 |
| Propane | 0.48 | 0.26 | iso-Pentane + 3-methylbutene-1 | 0.48 | 0.41 |
| Propylene | 11.15 | 6.5 | n-Pentane | 0.15 | — |
| iso-Butane | 0.34 | — | Pentene-1 | 1.11 | 0.61 |
Table 4
Characteristics of the condensate from cracking of n-heptane
| Temp., °C | Fractional composition, %: up to 98° | Fractional composition, %: 98° | Fractional composition, %: above 98° | $d_4^{20}$ | $n_D^{20}$ | Iodine number |
|---|---|---|---|---|---|---|
| Initial n-heptane | 0 | 100 | 0 | 0.6803 | 1.3960 | 0 |
| Experiments with sodium | ||||||
| 200 | 0 | 100 | 0 | 0.6808 | 1.3960 | 0 |
| 300 | 0 | 100 | 0 | 0.6870 | 1.3960 | 0 |
| 450 | 0 | 100 | 0 | 0.6814 | 1.3950 | 0 |
| 500 | 0 | 100 | 0 | 0.6825 | 1.3960 | 0 |
| 600 | 0 | 100 | 0 | 0.7000 | 1.4050 | 3.1 |
| 700 | 0 | 100 | 0 | 0.6846 | 1.3960 | 1.3 |
| 750 | 0 | 100 | 0 | 0.6820 | 1.3950 | 0.8 |
| 800 | 0 | 100 | 0 | 0.6803 | 1.3980 | 1.2 |
| Experiments without sodium | ||||||
| 700 | 1.3 | 85.0 | 13.7 | 0.6863 | 1.3985 | 15.0 |
| 800 | 5.3 | 82.4 | 12.3 | 0.6882 | 1.3985 | 12.0 |
| Experiments with potassium hydroxide deposited on activated carbon KAD | ||||||
| Initial n-heptane | 0 | 100 | 0 | 0.6859 | 1.3880 | 0 |
| 600 | 0 | 100 | 0 | 0.6854 | 1.3880 | 1.5 |
| 700 | 0 | 100 | 0 | 0.6853 | 1.3880 | 3.4 |
| 800 | 0 | 100 | 0 | 0.6859 | 1.3889 | 4.0 |
| Experiments with activated carbon KAD | ||||||
| 600 | 1.0 | 98.5 | 0.5 | 0.6878 | 1.3890 | 4.2 |
| 700 | 2.2 | 96.8 | 0.6 | 0.6886 | 1.3880 | 11.0 |
| 800 | 3.3 | 96.0 | 0.7 | 0.6849 | 1.3880 | 14.0 |
| In molten aluminum | ||||||
| 700 | 15.4 | 80.0 | 4.6 | 0.7031 | 1.4110 | 31.8 |
| 800 | 16.0 | 80.0 | 14.0 | 0.8535 | 1.5470 | 55.8 |
Conversion of cyclohexane
The experiments were carried out in an autoclave with a capacity of 50 ml. By gradual heating, the specified temperature of 400 or 500° was reached. In this process the pressure increased to 20–70 atm; these conditions were maintained for two hours, then the...
the heating was switched off, and the autoclave gradually cooled. The autoclave with the thermocouple was placed on a shaker, by means of which stirring was carried out. For each temperature, experiments were conducted in the presence of sodium and in its absence.
At 500° in the absence of sodium, cyclohexene began to be converted into a viscous resinous product (specific gravity 0.9103), with formation of 2% gaseous products. In the presence of sodium, small changes were observed: a decrease in the iodine number and formation of about 1.4% gas.
Table 5
Characteristics of cyclohexene heated in an autoclave
| Heating temperature | Iodine number | $n_D^{20}$ | $d_4^{20}$ | Note |
|---|---|---|---|---|
| Initial cyclohexene | 276 | 1.4480 | 0.8072 | |
| 400° with Na | 274 | 1.4480 | 0.8097 | Light-colored, homogeneous |
| 400° with Na | 278 | 1.4480 | 0.8122 | Dark |
| 500° with Na | 203 | 1.4570 | 0.8192 | Light-colored, homogeneous |
| 500° with Na | 74 | 1.4640 | 0.9103 | Dark, resinified |
| 500° with KOH | 117 | 1.4475 | 0.8097 | Slightly colored |
Thus, it has been shown for the first time that molten sodium and potassium hydroxide strongly inhibit the pyrolysis of n-heptane at 700–800° under atmospheric pressure, as well as the condensation of cyclohexene at 500° in an autoclave under pressure, whereas molten aluminum exerts an accelerating effect on the cracking of n-heptane at 700–800° and atmospheric pressure; i.e., cracking of n-heptane in a medium of molten aluminum proceeds to a greater depth, and 3–5 times more gas is formed than when the reaction is carried out in the absence of aluminum.
Received
7 IV 1960
CITED LITERATURE
- A. A. Balandin, Usp. Khim., 13, no. 5, 365 (1944).
- S. Berkman, D. Morrell, G. Egloff, Catalysis in Inorganic and Organic Chemistry, Moscow–Leningrad, 1949.
- M. D. Tilicheev, A. A. Polyakova, Khim. i tekhnol. topliv i masel, 1, 40 (1958).
- Kh. M. Minachev, N. F. Kononov, Usp. Khim., 26, no. 2, 176 (1957).
- W. P. Hettinger, C. D. Keith et al., Ind. and Eng. Chem., 47, 719 (1955).
- K. Ziegler, Usp. Khim., 26, no. 10, 1187 (1957).
- W. Emte, O. Grosskinsky, W. Klempt, FRG Patent 959554, 7 III 1957.
- A. G. Oblad, T. H. Milliken, E. R. Boedeker, U.S. Patent 2760847, 28 VIII 1956.
- G. Vittig, Usp. Khim., 27, no. 3, 291 (1958).
- R. Closson, J. Napolitano et al., Org. Chem., 22, 646 (1957).
- K. Ziegler, M. Plank, Chem. Eng. News, 3486 (1955).
- D. Hurd, Introduction to the Chemistry of Hydrides, Leningrad–Moscow, 1955.