DE2444786B2 - PROCESS FOR THE PRODUCTION OF ALKYLTIN TRICHLORIDES - Google Patents

Description

Alkyltin trichlorides are important precursors to SnCl ₄ + R ₃ Al -> R ₃ SnCI + AICl ₃ (5)

Manufacture of polyvinyl chloride stabilizers. The *> 3SnCl ₁ + 2R ₃ Al - * 3R ₂ SnCl ₂ + 2AlCl ₃ (6)
Transfer of alkyl groups to the tin atom

can be done in different ways 3 SnCl ₄ + R ₃ Al -> 3 RSnU ₃ + AlCI ₃ (7)

(W. P. Neumann: The organic chemistry of the various organotin halo-

o ¹ ^ ⁸ · J, ^er vl ^nand , ^Έ Γ ^Κ ? * ^V f ^rlag) . ^Stutt ? ^art can genide produce '^1967'. In the by equation

? - | ⁶ ~ ³ ^ ⁾ - ,. ^In most cases, however, a mixture of “5 * _{and (6)” was achieved}

high alkylated tin carbohydrates The good in particular venture actually satisfactory ... if

for the production of the alkyltin chlorides _{from tin the resulting AlCl 3} with complex formation with

tetrachloride and alkylaluminum _{bonds Here h or amines from the} reaction mixture

formed a mixture of trialkyltin chloride and _removed .... _The implementation (7) could

Tetraalkyltin The lower alkylation levels are 30; _{h can be realized} . "
then by so-called comproportioning

accessible (loc. cit., pp. 41-43). Alkyltin Trichlorides The surprising finding has now been obtained one z. B. by comproportioning makes that the above implementation (7) is Tetraalkyltin with tin tetrachloride: can be realized if the invention

R <? N α. ie "ri - ^ 4RQ _n ^ i 35 characteristics observed.

K + ₄ at jsnu ₄ -> ₃ 4KSnU _He fi _n d _un gsgemäße process for preparing

The production of AlkylzinntrihalogenUe after of Alkylzinntrichloriden by monoalkylation of

However, this process is based on a few alkyl groups. Tin tetrachloride is characterized in that one

(e.g. the vinyl group) is restricted and only proceeds with aluminum trialkyls or alkylaluminum halides

in a special solvent (POCyPsO ₁ ). The 40 in the form of their Donar complexes with ethers or

The reason for this difficulty is to be seen in the fact that tertiary amines are used in monoalkyltin compounds

the stoichiometric full Comproportionation amounts between 20 and 12O ⁰ C

necessary step with tin tetrachloride.

R SnCl + SnCl -> 2RSnCl ^ ' ^Ke ^ special embodiment of the invention

^{224 3} 45 according to the method is characterized in that

can only be realized in exceptional cases. There are carried out the reaction between 40 and 7O ⁰ C

however, methods have been developed according to which Al becomes.

Kyltin trichlorides in addition to dialkyltin or trialkyl are suitable for the process according to the invention

rmnchloriden arise (DT-PS 11 61 893, GB-PS the Donar complexes of the alkylaluminum compounds

7 39 883). From such mixtures, alkyl tin 50 gen z. B. with diethyl ether, di-n-butyl ether, tetra

trichloride z. B. can be obtained by distillation. hydrofuran, dioxane, anisole etc., triethylamine, py-

However, this method is used due to the high boiling point eridine or dimethylaniline etc.

points of the longer-chain alkyl tin trichlorides strong. B. those with tetrahydro-

limited and can technically only for the furan or pyridine, the SnCl ₄ alkylate to one

production of the short-chain (^ C ₄ ) alkyl tin trichlorides 55 product mixture R _{n SnCl 4} - ,, {n - \ to 4), in which each

Use. but always the alkyltin trichloride the main

The easiest way to make a component of alkyltin trichlorides.

to deliver, the exchange of a chlorine atom would be as particularly favorable in the sense of the invention

SnCl ₄ through an alkyl group, a targeted mono-moderate process turns out to be the di-n-butyl ether

alkylation. With the technically easily accessible 60 complex with both trialkylaluminum and with

Aluminum trialkylene is a monoalkylation of the alkyl aluminum halide. One obtains alkyl tin

SnCl ₄ has not yet succeeded in a satisfactory manner. It leaves trichlorides with a content of about 90-93% by weight.

However, alkyl tin trichlorides by monoalkyl- This content can still be increased to 97% if

tion with alkylaluminum alkoxides from SnCl ₄ , the SnCl _{4 is also used} as an etherate complex,

(DT-OS 23 04 617, W.P. Neumann: Ann. 65 The inventive method for production

Chem., 653 [1962], 163). In the following, however, the large number of alkyltin trichlorides will be discussed in greater detail

economic advantage that the aluminum trialkyls are explained:

In the case of alkylation reactions with respect to other alkyls, the mixture is first mixed in a manner known per se

the alkylaluminum compounds in a suitable apparatus under protective gas with the desired donor. The alkylaluminum complex compound formed is then reacted, also under protective gas, with the SnCl ₄ or, if appropriate, a mixture of SnCl ₄ and di-n-butyl ether in such a molar ratio that one alkyl group is absent for each Sn atom, advantageously by the SnCl _{4 is placed} in the apparatus and the alkylaluminum complex compound is allowed to flow in with thorough mixing. Since this is an exothermic process, good cooling ensures that a low temperature is maintained during the reaction. The best results are obtained when the reaction of the reactants at temperatures between 20 and 120 ⁰ C, is preferably carried out at 40 ⁰ C. At a higher temperature, a larger proportion of by-products is created. There is also the risk of decomposition of the donor complexes of the aluminum compounds.

After the reaction and after-reaction have ended, the reaction mixture is expediently diluted with a suitable solvent and poured into ice water. A suitable solvent is e.g. B. Di-n-butyl ether. There is no need to dilute with di-n-butyl ether if it is added to the SnCl ₄ from the outset. The subsequent addition of di-n-butyl ether no longer has any influence on the product composition. The ether is only added for reasons of better work-up of the reaction product. B. di-n-butyl ether waived, so must, especially in the production of RSnCl ₃ with short-chain R, the aqueous phase several times with z. B. Di-n-butyl ether can be extracted. After phase separation and distilling off the di-n-bu-.tyl ether, alkyltin trichloride is obtained, which contains different amounts of more highly alkylated tin chlorides, respectively. Tetraalkyltin, are added.

example 1

In a 1-1 three-necked flask with stirrer, Claisen head, thermometer, reflux condenser and dropping funnel is added under stirring and cooling at 40 ⁰ C to 260.5 g (1 mol) of SnCl ₄ 171 g (C ₈ H _{17) 3} A1 ■ ( CiHj) ₁ O (corresponding to 0.33 mol of Tn-n-octylaluminum). The mixture is allowed after addition is complete for about 30 minutes at 40 ° C and stirring then also added dropwise under stirring and cooling at 40-5O ⁰ C 260 g (2MoI) of di-nbutyläther. After this addition has ended, the mixture is stirred for a further 15 minutes without heating or cooling and the reaction mixture is then added to 200 ml of ice water with cooling. The temperature at a maximum of 50-70 ⁰ C. After keeping the phase separation is distilled di-n-butyl ether at reduced pressure from the ether phase, and receives the C ₈ H ₁₇ SnCl ₃ as a light to dark brown colored liquid. The yield is 322 g (90%, based on Sn used).

Gas chromatographic analysis of a _{sample reacted with C 2} H ₅ MgCl showed a C ₈ H ₁₇ SnCl ₃ content of 93% by weight.

Example 2

In the apparatus described in Example 1, 260 g (2 mol) of di-n-butyl ether are added with stirring to 260.5 g (1 mol) of SnCl _{4 over the course of 5 minutes.} Included

»S, the temperature rises to about 60 ⁰ C. As this Realctinns £, emic between 40 and 50 ⁰ C is found, take the further reaction with the (C ₈ H _{17) 3} A1 ■ (C ₄ Hj) ₂ O wherein 50 ⁰ C and otherwise as described in Example 1 before. The yield is 90%; _{the C 8} H _n SnCl ₃ content determined by gas chromatography is 97%.

Example 3

As described in Example 1, SnCl ₄ is reacted with (C _e H ₁₇ ) ₃ Al (C ₄ H _e ) 2O, but no further addition of di-n-butyl ether is used. After hydrolysis of the reaction mixture, the aqueous phase is extracted 2 to 3 times with 70-100 ml of di-n-butyl ether each time and the reaction product is isolated as described in Example 1. A yield of 90% is obtained; _{the C 8} H ₁₇ SnCl ₃ content determined by gas chromatography is 97%.

example Al-alkyl compound Donor temperature "/The end RSnCl, ⁰ C prey in% by weight ") 4th (C ₈ H ₁₇ ) ₃ A1 (C ₄ H,), 0 40 90 95 5 (C ₈ H ₁₇ ) ₃ A1 (C ₄ H ") _S O 70 85 91 6th (C ₈ H ₁₇ ) ₃ A1 (C ₂ Hs) ₈ O 30th 80 87 7th (C ₈ H ₁₇ ) ₃ A1 Dioxane 40 80 84 8th (C "H ₁₇ ) ₃ A1 THF ¹ ) 30th 80 72 9 (C ₈ H ₁₇ ) ₃ A1 Anisole 30th 80 91 10 CiH ₁₇ AlCl ₁ (C ₄ HJ ₂ O 40 90 99 11th (C ₈ H ₁₇ ) ₃ Al Pyridine 30th 60 77 12th (C ₈ H ₁₇ ) ₃ A1 (CA) ₃ N 30th 60 89 13th (C ₈ H ₁₇ ) ₃ A1 DMA «) 30th 60 79 14th (C ₁₈ H ₃₇ ) ₃ A1 (C ₄ H _e ) ₂ O 50 80 85 15th (C ₄ H,) ₃ A1 (C ₄ H,) ₂ O 40 85 87 16 (C ₄ H,) ₃ A1 THF ¹ ) 30th 80 68 17th (C ₄ H,) ₃ A1 (C ₂ H ₆ ) ₂ O 30th 70 65 18th (C ₄ H,) ₃ A1 Anisole 40 80 73 ^l ) tetrahydrofuran. *) Dimethylaniline. ') Area% in the gas chromatogram.

Claims (2)

have lierungsnütteln, limited. With alkyl patent claims, aluminum alkoxides can namely be made per aluminum alkoxides. miuhimatom transferred a maximum of two alkyl groups. 1. Process for the production of alkyl tin tetra- According to DT-AS 11 57 617 and 11 64 407 it is possible to use chlorides by monoalkylation of tin tetra-5 using the alkyl aluminum chloride. durchgeke η η ζ eich η et that ether complexes or alkyl aluminum amine comman aluminum trialkyls or alkyl aluminum plexes Tnalkylzmnverbindungen and dialkyltin halides in the form of their Donar complexes with bonds, or their mixtures depending on the stochio-ethers or tertiary alkyl amines - Metric or non-stoichiometric conversion to produce tin compounds in stoichiometric amounts between io. Under this method, Herstelung was seen 20 to 120 ⁰ C with tin tetrachloride reacted. of Monoalkylzinnverbmdungen not possible so far. 2. The method according to claim 1, characterized in a later publication indicates that the reaction between 40 (Liebigs Ann. Chem., 653 [1962], 160) writes W. P. and 70 ° C is carried out. New man even: ¹⁵ »It was now necessary to check whether the implementation of the Aluminum alkyls with tin tetrachloride are to be steered in such a way that one follows the equations