Academician A. V. TOPCHIEV, Ya. M. PAUSHKIN, A. V. NEPRYAKHINA,
P. G. ANAN’EV, and N. N. DMITREVSKII
Submitted 1960-01-01 | RussiaRxiv: ru-196001.00685 | Translated from Russian

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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

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Submission history

Academician A. V. TOPCHIEV, Ya. M. PAUSHKIN, A. V. NEPRYAKHINA,