Academician A. E. ARBUZOV and M. G. IMAEV
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Submitted 1957-01-01 | RussiaRxiv: ru-195701.22801 | Translated from Russian

Abstract

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CHEMISTRY

Academician A. E. ARBUZOV and M. G. IMAEV

SAPONIFICATION AND TRANSESTERIFICATION OF FULL ESTERS OF PHOSPHOROUS ACID

It was shown by one of us ($^1$) that the action of acidified water on full esters of phosphorous acid of the type $\mathrm{P(OR)_3}$ is a typical catalytic reaction.

We studied the saponification by pure water of trimethyl, triethyl, tri-$n$-propyl, tri-$n$-butyl, and triphenyl phosphites. It was found that all the esters listed are readily saponified by pure water with the evolution of heat.

Pure water was obtained by secondary distillation of ordinary distilled water and had a specific electrical conductivity (at $25^\circ$) of $2.2 \cdot 10^{-6}\ \mathrm{ohm}^{-1}\cdot\mathrm{cm}^{-1}$.

The saponification reaction is irreversible and does not depend on the mass of the reacting substances.

We studied (by the dilatometric method) the rate of saponification of the esters by pure water at equimolecular ratios.

The rate of saponification depends, above all, on the size of the radical entering into the composition of the ester. Thus, trimethyl phosphite is saponified 10 times faster than triethyl phosphite; 30 times faster than triphenyl phosphite; 90 times faster than tri-$n$-propyl phosphite; 200 times faster than tri-$n$-butyl phosphite—other conditions being equal.

In terms of the rate of saponification, they are arranged in the following sequence:

[
\mathrm{P(OCH_3)_3 > P(OC_2H_5)_3 > P(OC_6H_5)_3 > P(OC_3H_7\text{-}n)_3 > P(OC_4H_9\text{-}n)_3}
]

Especially interesting is the difficult saponification of tri-$n$-propyl and tri-$n$-butyl phosphites in comparison with triphenyl phosphite. All experiments on the saponification of esters were carried out at a temperature of $25^\circ$. The results are given in Table 1.

Table 1

Reactions Saponification time, min.: 25% of ester Saponification time, min.: 50% of ester Saponification time, min.: 75% of ester Saponification time, min.: 100% of ester
$(\mathrm{CH_3O})_3\mathrm{P} + \mathrm{H_2O}$ 8 8–9 10 61
$(\mathrm{C_2H_5O})_3\mathrm{P} + \mathrm{H_2O}$ 68–75 81–82 90 240
$(n\text{-}\mathrm{C_3H_7O})_3\mathrm{P} + \mathrm{H_2O}$ 750–810 840–850 870 1110
$(n\text{-}\mathrm{C_4H_9O})_3\mathrm{P} + \mathrm{H_2O}$ 2010 2110 2140 2400
$(\mathrm{C_6H_5O})_3\mathrm{P} + \mathrm{H_2O}$ 245 265 285 $\sim 365$

The rate of saponification also depends on the temperature at which the reaction is carried out. The influence of temperature on the rate of the saponification reaction is the usual one, as for most chemical reactions.

We studied the influence of the reaction product on the rate of saponification of esters, using triethyl phosphite as an example. To the initial mixture of equimolecular amounts

phosphite and water, various amounts of diethylphosphorous acid were added before the beginning of the experiment. All experiments were carried out at a temperature of 25°. The composition of the initial mixture was ((\mathrm{C_2H_5O})_3\mathrm{P} + \mathrm{H_2O} + x(\mathrm{C_2H_5O})_2\mathrm{POH}). The results are given in Table 2. As is seen from Table 2, preliminary addition of diethylphosphorous acid to the initial mixture accelerates the course of the reaction.

Table 2

(x) Time of saponification, min. Time of saponification, min. Time of saponification, min. Time of saponification, min.
(x) 25% ester 50% ester 75% ester 100% ester
0.000 68—75 81—82 90 240
0.002 23 32—33 45 100
0.050 up to 5 up to 5 7 50
0.200 11

Saponification of esters (\mathrm{P(OR)_3}), with the exception of triphenyl phosphite, is strongly slowed in the presence of small amounts of inorganic or organic bases, as is seen from Table 3.

Saponification of trimethyl phosphite in the presence of (1.9 \cdot 10^{-5}) mol of caustic soda was slowed by 7–8 times, triethyl phosphite in the presence of (2.0 \cdot 10^{-5}) mol—by 2 times, tri-(n)-butyl phosphite in the presence of (2.1 \cdot 10^{-6}) mol—by 3 times, and triethyl phosphite in the presence of 0.1 mol of pyridine—by 14 times.

Table 3

Reactions Amount of base (in mol per 1 mol of ester) Temperature, °C Time of saponification, min. Time of saponification, min. Time of saponification, min. Time of saponification, min.
Reactions Amount of base (in mol per 1 mol of ester) Temperature, °C 25% phosphite 50% phosphite 75% phosphite 100% phosphite
((\mathrm{CH_3O})_3\mathrm{P} + \mathrm{H_2O}) (1.9 \cdot 10^{-5}\ \mathrm{NaOH}) 0 450 660 840 1590
((\mathrm{C_2H_5O})_3\mathrm{P} + \mathrm{H_2O}) (2.0 \cdot 10^{-5}\ \mathrm{NaOH}) 25 139 156 183 437
((\mathrm{C_2H_5O})_3\mathrm{P} + \mathrm{H_2O}) (8.5 \cdot 10^{-5}\ \mathrm{NaOH}) 25 155 185 230 470
((\mathrm{C_2H_5O})_3\mathrm{P} + \mathrm{H_2O}) (4.0 \cdot 10^{-4}\ \mathrm{NaOH}) 25 450 490 515 680
((\mathrm{C_2H_5O})_3\mathrm{P} + \mathrm{H_2O}) (0.1\ \mathrm{C_5H_5N}) 50 240—250 250—255 255—260 (\sim 325)
((n\text{-}\mathrm{C_4H_9O})_3\mathrm{P} + \mathrm{H_2O}) (2.1 \cdot 10^{-6}\ \mathrm{NaOH}) 50 150—170 170—173 180 220

Thus, the saponification rate decreases with increasing concentration of the base. Such slowing of the reaction is explained by removal from the reaction mass of the reaction catalyst—the free dialkylphosphorous acid—in the form of its salt with an organic base, or of a salt of monoalkylphosphorous acid with an inorganic base.

We also studied the saponification reaction of trialkyl phosphites in the medium of pyridine, acetone, dioxane, and alcohols. Of these solvents, only dioxane is practically indifferent.

Pyridine and acetone react with the reaction product, giving, respectively, the pyridine salt of dialkylphosphorous acid and an ester of (\alpha)-oxyalkylphosphinous acid with acetone, and therefore the rate of saponification of the esters in their medium decreases accordingly. Thus, for example, saponification of triethyl phosphite in the presence of 0.2 mol of acetone is slowed by 21 times.

We also studied (by the refractometric method) the rate of saponification of triethyl and tri-(n)-propyl phosphites in dioxane medium.

Kinetic analysis of their saponification in dioxane medium shows that this reaction is complex and cannot be expressed either by the first-order equation

[
\frac{dx}{dt}=k(a-x),
]

or by the equation for autocatalytic reactions

[
\frac{dx}{dt}=kx(a-x).
]

The rate constants for saponification of triethyl phosphite in the medium of 1.5 and 3 mol of dioxane, and of tri-(n)-propyl phosphite in the medium of 4 mol of dioxane, calculated by the equation for second-order reactions

[
\frac{dx}{dt}=k(a-x)^2,
]

are constant over a considerable period of time. At the beginning and end of the reaction, deviations from constancy of the rate constants are observed.

Table 4

No. Formulas B.p. (in °C at pressure, mm Hg) $n_D^{20}$ $d_4^{20}$ $MR$, found $MR$, calc. $P$ (in %), found $P$ (in %), calc. Yield* (in %)
1 $(\mathrm{CH_3O})_2(n\text{-}\mathrm{C_3H_7O})\mathrm{P}$ 47—8/14 1,4165 0,9939 38,45 38,34 20,60; 20,75 20,36 78
2 $(\mathrm{CH_3O})(\mathrm{iso}\text{-}\mathrm{C_5H_{11}O})_2\mathrm{P}$ 87—8/4 1,4305 0,9232 66,19 66,07 13,05; 13,05 13,11
3 $(\mathrm{CH_3O})(n\text{-}\mathrm{C_3H_7O})(\mathrm{iso}\text{-}\mathrm{C_5H_{11}O})\mathrm{P}$ 75—6/5 1,4275 0,9289 57,62 56,83 15,00; 14,86 14,88 23
4 $(\mathrm{CH_3O})(\mathrm{C_2H_5O})(n\text{-}\mathrm{C_3H_7O})\mathrm{P}$ 60—1/45 1,4160 0,9732 42,84 42,98 18,70; 18,56 18,65 22
5 $(\mathrm{C_2H_5O})_2(n\text{-}\mathrm{C_3H_7O})\mathrm{P}$ 72—4/23 1,4150 0,9547 47,27 47,59 17,20 17,19 40
6 $(\mathrm{C_2H_5O})2(\mathrm{iso}\text{-}\mathrm{C_5H$}O})\mathrm{P 83—7/15 1,4230 0,9357 56,71 56,83 15,13; 15,34 14,88 52
7 $(n\text{-}\mathrm{C_3H_7O})2(\mathrm{iso}\text{-}\mathrm{C_5H$}O})\mathrm{P 64—6/5 1,4290 0,9223 66,07 66,07 13,29; 13,37 13,11
8 $(n\text{-}\mathrm{C_3H_7O})(n\text{-}\mathrm{C_4H_9O})_2\mathrm{P}$ 94—6/2 1,4285 0,9242 65,85 66,07 13,40; 13,22 13,11
9 $(n\text{-}\mathrm{C_4H_9O})2(n\text{-}\mathrm{C_7H$}O})\mathrm{P 142—3/2 1,4355 0,9030 84,58 84,54 10,71; 10,87 10,60
10 $(n\text{-}\mathrm{C_4H_9O})(n\text{-}\mathrm{C_7H_{15}O})_2\mathrm{P}$ 167—8/3 1,4410 0,8997 98,15 98,39 9,39; 9,36 9,26 61

* Yields are not given for products of side reactions.

Table 5

No. Formulas B.p. (in °C at pressure, mm Hg) $n_D^{20}$ $d_4^{20}$ $MR$, found $MR$, calc. $P$ (in %), found $P$ (in %), calc.
1 $(\mathrm{CH_3O})(n\text{-}\mathrm{C_3H_7O})\ \mathrm{POH}$ 63/12 1,4120 1,0686 32,16 31,71 22,60; 22,80 22,43
2 $(\mathrm{CH_3O})(n\text{-}\mathrm{C_4H_9O})\ \mathrm{POH}$ 79—81/10 1,4174 1,0430 36,71 36,33 20,62 20,38
3 $(\mathrm{C_2H_5O})(n\text{-}\mathrm{C_3H_7O})\ \mathrm{POH}$ 97—9/24 1,4110 1,0354 36,48 36,33 20,21; 20,11 20,36
4 $(\mathrm{C_2H_5O})(\mathrm{iso}\text{-}\mathrm{C_4H_9O})\ \mathrm{POH}$ 90/12 1,4171 1,0115 41,32 40,95 18,46; 18,64 18,66
5 $(\mathrm{C_2H_5O})(\mathrm{iso}\text{-}\mathrm{C_5H_{11}O})\ \mathrm{POH}$ 93—4/8 1,4210 0,9964 45,87 45,56 17,43; 17,20 17,19
6 $(n\text{-}\mathrm{C_3H_7O})(n\text{-}\mathrm{C_4H_9O})\ \mathrm{POH}$ 81—3/3 1,4210 0,9988 45,75 45,56 17,00; 17,17 17,19
7 $(n\text{-}\mathrm{C_4H_9O})(n\text{-}\mathrm{C_7H_{15}O})\ \mathrm{POH}$ 151—2/2 1,4325 0,9481 64,71 64,04 12,80; 12,70 13,11

The saponification reaction of trialkyl phosphites without a solvent proceeds in a heterogeneous system. Therefore, kinetic analysis of this reaction did not give any definite results.

When trialkyl phosphites are saponified in an alcohol medium, the reaction proceeds rapidly with strong heating. However, not every alcohol can be used as a solvent, since when an alcohol whose radical differs from the radical of the phosphite is used, saponification is always accompanied by a side reaction—transesterification.

B. A. Arbuzov and V. S. Vinogradova (²) were the first to obtain a series of trialkyl phosphites with identical higher radicals by transesterification of triethyl phosphite with higher alcohols in the presence of a catalyst—phosphoric acid.

Dialkylphosphorous acids and alkali-metal alcoholates are catalysts for the transesterification of trialkyl phosphites with higher alcohols.

The synthesis of mixed phosphites of the type ((RO)_2(R'O)P) and ((RO)(R'O)_2P) was carried out by the method of partial transesterification of phosphite (P(OR)_3), respectively with one and two moles of higher alcohols per mole of phosphite, in the presence of one of the two above-mentioned catalysts.

Mixed phosphites, on the first fractionation (Table 4, No. 1) under high vacuum, are obtained in good yields.

On repeated distillations, redistribution of radicals is observed. Phosphites with three different aliphatic radicals disproportionate especially readily (Table 4, Nos. 3 and 4: ((RO)(R'O)(R''O)P)), obtained by the method of partial transesterification of the mixed phosphite ((RO)_2(R'O)P) with alcohols.

The physical constants of the esters synthesized by us for the first time are given in Table 4.

Mixed phosphites of the type ((RO)_2(R'O)P) are readily saponified by slightly acidified water, forming the corresponding alcohols and mixed dialkylphosphorous acids. In their saponification, the light radical is always split off in the form of an alcohol. Here too, on repeated distillations, disproportionation is observed. The physical constants of some of the mixed dialkylphosphorous acids first isolated by this method are given in Table 5.

Mixed dialkylphosphorous acids have been obtained by a number of investigators by transesterification of diethyl phosphite with higher alcohols both in the absence of any catalysts (³) and with a catalyst—alkali-metal alcoholates (⁴)—or with an acidic catalyst (²).

Kazan Chemical-Technological Institute
named after S. M. Kirov

Received
9 XI 1956

CITED LITERATURE

¹ A. E. Arbuzov, On Catalysis Phenomena in the Transformations of Certain Phosphorus Compounds, Kazan, 1914. ² B. A. Arbuzov, V. S. Vinogradova, Izv. AN SSSR, OKhN, 1952, 865; 1952, 505; 1951, 733. ³ L. M. Kosolapoff, J. Am. Chem. Soc., 73, 4989 (1951). ⁴ V. K. Kuskov, G. Kh. Gradis, DAN, 92, 323 (1953).

Submission history

Academician A. E. ARBUZOV and M. G. IMAEV