US1639947A - Art of making metallo-organic compounds - Google Patents
Art of making metallo-organic compounds Download PDFInfo
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- US1639947A US1639947A US631940A US63194023A US1639947A US 1639947 A US1639947 A US 1639947A US 631940 A US631940 A US 631940A US 63194023 A US63194023 A US 63194023A US 1639947 A US1639947 A US 1639947A
- Authority
- US
- United States
- Prior art keywords
- tin
- art
- alkyl
- alloy
- metal
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- 229910052751 metal Inorganic materials 0.000 description 30
- 239000002184 metal Substances 0.000 description 30
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 description 22
- 229910045601 alloy Inorganic materials 0.000 description 19
- 239000000956 alloy Substances 0.000 description 19
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 14
- 238000006243 chemical reaction Methods 0.000 description 14
- 150000002739 metals Chemical class 0.000 description 14
- 229910052708 sodium Inorganic materials 0.000 description 14
- 239000011734 sodium Substances 0.000 description 14
- 239000003054 catalyst Substances 0.000 description 9
- 238000005275 alloying Methods 0.000 description 7
- 238000009835 boiling Methods 0.000 description 7
- NEHMKBQYUWJMIP-UHFFFAOYSA-N chloromethane Chemical compound ClC NEHMKBQYUWJMIP-UHFFFAOYSA-N 0.000 description 7
- 229910052736 halogen Inorganic materials 0.000 description 7
- 150000002367 halogens Chemical class 0.000 description 7
- 150000001875 compounds Chemical class 0.000 description 6
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 4
- 229910052783 alkali metal Inorganic materials 0.000 description 4
- 150000001340 alkali metals Chemical class 0.000 description 4
- -1 alkyl chlorid Chemical compound 0.000 description 4
- VXKWYPOMXBVZSJ-UHFFFAOYSA-N tetramethyltin Chemical group C[Sn](C)(C)C VXKWYPOMXBVZSJ-UHFFFAOYSA-N 0.000 description 4
- 229910052725 zinc Inorganic materials 0.000 description 4
- 239000011701 zinc Substances 0.000 description 4
- 239000004215 Carbon black (E152) Substances 0.000 description 3
- 125000000217 alkyl group Chemical group 0.000 description 3
- 150000002430 hydrocarbons Chemical class 0.000 description 3
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 229930195733 hydrocarbon Natural products 0.000 description 2
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 description 2
- 238000002360 preparation method Methods 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 1
- 241000209140 Triticum Species 0.000 description 1
- 235000021307 Triticum Nutrition 0.000 description 1
- 229910052784 alkaline earth metal Inorganic materials 0.000 description 1
- 150000001342 alkaline earth metals Chemical class 0.000 description 1
- 125000004429 atom Chemical group 0.000 description 1
- RDHPKYGYEGBMSE-UHFFFAOYSA-N bromoethane Chemical compound CCBr RDHPKYGYEGBMSE-UHFFFAOYSA-N 0.000 description 1
- 235000013339 cereals Nutrition 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 125000001495 ethyl group Chemical group [H]C([H])([H])C([H])([H])* 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 229910052732 germanium Inorganic materials 0.000 description 1
- GNPVGFCGXDBREM-UHFFFAOYSA-N germanium atom Chemical compound [Ge] GNPVGFCGXDBREM-UHFFFAOYSA-N 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 125000001183 hydrocarbyl group Chemical group 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 238000002386 leaching Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 230000000737 periodic effect Effects 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 238000010992 reflux Methods 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
- MRMOZBOQVYRSEM-UHFFFAOYSA-N tetraethyllead Chemical group CC[Pb](CC)(CC)CC MRMOZBOQVYRSEM-UHFFFAOYSA-N 0.000 description 1
- 150000003606 tin compounds Chemical class 0.000 description 1
- 238000010792 warming Methods 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07F—ACYCLIC, CARBOCYCLIC OR HETEROCYCLIC COMPOUNDS CONTAINING ELEMENTS OTHER THAN CARBON, HYDROGEN, HALOGEN, OXYGEN, NITROGEN, SULFUR, SELENIUM OR TELLURIUM
- C07F7/00—Compounds containing elements of Groups 4 or 14 of the Periodic Table
- C07F7/22—Tin compounds
- C07F7/2208—Compounds having tin linked only to carbon, hydrogen and/or halogen
Definitions
- This invention relates to the art of mak ing metallo-orga'nic compounds, and will be fully understood from the following'description:
- the methods followed have been based upon the action of iodids, or unstable compounds of zinc. etc. Thesemethods have been characterized by high cost and uncertain yields. and at-' tended with variousoperating difliculties.
- the experiments recorded in the literature where alloys containing sodium have been used pressure has been avoided, the alloybeing heated with an alkyliodidunder a reflux condenser (Lowig. Annalen (1. Chem. '84. 308; Lowig, J our. Prak. Chem. 60,
- the metal to be used is, in advantageous condition for reaction, (as for instance in alloy with a highly electiopositive metal, as an alkali metal -or alkaline earth metal), subjected to a reagent involving a direct transfer of-hydrocarbon radicals, as-more particularly pointed out hereinafter.
- a metal of the second sub-group of the. fourth periodic group (tin, lead, germanium), sodium for instance is. preferably employed as the alloy ingredient.
- the metals mentioned will be referred to herein as metals of the tin sub-group.
- tin in the proportion of 80-94% is suitably alloyed wlth sodium 111 the complemental proportions of 4%, (preferably 86% of tin and 14% of sodium, corresponding to the formula Na Sn,) and the alloy is subdivided to suitable size, as for instance about the size of wheat grains, and introduced into a reaction vessel capable of withstanding pressure, and equipped with suitable heating and cooling means, as a jacket or coils, also stirring means, so as to afiord a .close temperature control, as it is desired that-local rises or irregularities in ART OF MAKING METALLO-ORGANIC 192:. Serial no. 031340.
- the vessel may be mounted for rotation and contain 59 balllls or the like inthe manner of a ball m1 Methyl chlorid being introduced into the reaction vessel in suitable amount (before or after the introduction of the alloy. as de- 55' sired), and the alloy being suitably subdivided, the reaction is. ready to proceed. Ordinarily, to start the reaction, slight warming, say up to about C. is desirable, but after the reaction is well under way, 00 more or less cooling is ofdinarily required.
- the methyl chlorid although lowboiling, can be held under pressure, and. at'
- ppfactically pure tin tetramethyl can be taken 70
- methyl chlorid other desired alkyl chlorids or bromids can be employed; for instance ethyl 'chlorid or ethyl bromid may be used and the corresponding tin l5 tetraethyl obtained.
- a catalyst may be employed, as for example zinc. In using the zinc, this, to .the amount of about 0.5 to 3% may convenient lybe initially alloyed with the tin and sodium. The use of a catalyst promotes the reaction of the alkyl halid, and particularly where the sodium or the like is not in molecular proportion with the tin or lead.
- the reaction in order to facilitate the reaction, it is desirable to employ more than the calculated molecular equivalent of ,the methyl -ch1orid or other hydrocarbon ha'lid used.
- the excess may be recovered, as by distilling ofi, or it. may be advantageous to use an exhaust pump.
- the methyl chlorld so recovered. is condensed or re-compressed and condensed and may be employed 1n suba sequent reactions.
- the surplus methyl chlorid. having een removed, e reactlon densation, and a final filtration and drying may be carried out if desired.
- the desired product may, if preferred, be removed from the reaction vessel by ordinary distillation.
- the residue in the reaction vessel contains tin and sodium chlorid.
- the Sodium chlorid may be removed, and the tin in divided condition may be dried and after alloying be used'for subsequent reactions.
- tin as in the illustration detailed, other metals, as for example .lead, may be employed, and the corresponding metallo-organic compound obtained; "While the invention is directed especially to the production of compounds in which all the valences of the metal are satisfied by hydrocarbon groups, such as tin tetramethyl, lead tetraethyl etc., it is also applicable for the preparation of compounds in which only a portion of the valences of the metallic atom are satisfied with hydrocarbon radicals.
- hydrocarbon groups such as tin tetramethyl, lead tetraethyl etc.
- tin tetramethyl which comprises alloying tin With sodium in the proportions of about 86% of tin and 14% of sodium, subdividing the alloy, and reacting upon the alloy with methyl chlorid under pressure at a temperature between about 30 and 100 C. in the presence of zinc as a catalyst.
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Catalysts (AREA)
Description
Patented Aug. 23, 1927.
UNITED STATES PATENT OFFICE.
CHARLES A. KRA'US AND CONRAL O. OAIILIS, OF WORCESTER, MASSACHUSETTS, AS- SIGNORS TO STANDARD DEVELOPMENT COMPANY," A CORPORATION 01' DELA- wens.
Io Drawing. Application fled April 13,
This invention relates to the art of mak ing metallo-orga'nic compounds, and will be fully understood from the following'description: In the preparation of hydrocarbon compounds of metals heretofore the methods followed have been based upon the action of iodids, or unstable compounds of zinc. etc. Thesemethods have been characterized by high cost and uncertain yields. and at-' tended with variousoperating difliculties. Inthe experiments recorded in the literature, where alloys containing sodium have been used pressure has been avoided, the alloybeing heated with an alkyliodidunder a reflux condenser (Lowig. Annalen (1. Chem. '84. 308; Lowig, J our. Prak. Chem. 60,
304: Klippel. Jour. Prak; Chem. 81, 287
Ladenburg, 7 5. 78).
In proceeding in accordance with the presentinvention, the metal to be used, is, in advantageous condition for reaction, (as for instance in alloy with a highly electiopositive metal, as an alkali metal -or alkaline earth metal), subiected to a reagent involving a direct transfer of-hydrocarbon radicals, as-more particularly pointed out hereinafter. In the case of a metal of the second sub-group of the. fourth periodic group, (tin, lead, germanium), sodium for instance is. preferably employed as the alloy ingredient. For brevity, the metals mentioned will be referred to herein as metals of the tin sub-group.
.. As an example,
nn. d. Chem. Supplement 8,
tin in the proportion of 80-94% is suitably alloyed wlth sodium 111 the complemental proportions of 4%, (preferably 86% of tin and 14% of sodium, corresponding to the formula Na Sn,) and the alloy is subdivided to suitable size, as for instance about the size of wheat grains, and introduced into a reaction vessel capable of withstanding pressure, and equipped with suitable heating and cooling means, as a jacket or coils, also stirring means, so as to afiord a .close temperature control, as it is desired that-local rises or irregularities in ART OF MAKING METALLO-ORGANIC 192:. Serial no. 031340.
temperature should not occur. The vessel may be mounted for rotation and contain 59 balllls or the like inthe manner of a ball m1 Methyl chlorid being introduced into the reaction vessel in suitable amount (before or after the introduction of the alloy. as de- 55' sired), and the alloy being suitably subdivided, the reaction is. ready to proceed. Ordinarily, to start the reaction, slight warming, say up to about C. is desirable, but after the reaction is well under way, 00 more or less cooling is ofdinarily required. By the use of a closed, pressure-resistant vessel, the methyl chlorid, although lowboiling, can be held under pressure, and. at'
the said temperature or slightly-above, to 65 about (1,- and finally when well toward .the end, even as high as 100 C. 'On completionof the reaction, which requires about 2-24 hours, depending upon the conditions,
ppfactically pure tin tetramethyl can be taken 70 Instead of methyl chlorid, other desired alkyl chlorids or bromids can be employed; for instance ethyl 'chlorid or ethyl bromid may be used and the corresponding tin l5 tetraethyl obtained. I
If desired, a catalyst may be employed, as for example zinc. In using the zinc, this, to .the amount of about 0.5 to 3% may convenient lybe initially alloyed with the tin and sodium. The use of a catalyst promotes the reaction of the alkyl halid, and particularly where the sodium or the like is not in molecular proportion with the tin or lead.
' In general, in order to facilitate the reaction, it is desirable to employ more than the calculated molecular equivalent of ,the methyl -ch1orid or other hydrocarbon ha'lid used. In such case, after completion of the reaction, the excess may be recovered, as by distilling ofi, or it. may be advantageous to use an exhaust pump. The methyl chlorld so recovered. is condensed or re-compressed and condensed and may be employed 1n suba sequent reactions. The surplus methyl chlorid. having een removed, e reactlon densation, and a final filtration and drying may be carried out if desired. In the case of the lower boiling organic tin compounds, the desired product may, if preferred, be removed from the reaction vessel by ordinary distillation.
The residue in the reaction vessel contains tin and sodium chlorid. By repeated leaching and washing with water, the Sodium chlorid may be removed, and the tin in divided condition may be dried and after alloying be used'for subsequent reactions.
Instead of tin as in the illustration detailed, other metals, as for example .lead, may be employed, and the corresponding metallo-organic compound obtained; "While the invention is directed especially to the production of compounds in which all the valences of the metal are satisfied by hydrocarbon groups, such as tin tetramethyl, lead tetraethyl etc., it is also applicable for the preparation of compounds in which only a portion of the valences of the metallic atom are satisfied with hydrocarbon radicals.
While the invention has been described by reference to certain specific details," it will be understood that this is for the purpose of illustration and is not limitative; and changes may be made which come within the spirit and scope of the invention' What we claim is:
1. The improvement in the art of making tin tetramethyl, which comprises alloying tin With sodium in the proportions of about 86% of tin and 14% of sodium, subdividing the alloy, and reacting upon the alloy with methyl chlorid under pressure at a temperature between about 30 and 100 C. in the presence of zinc as a catalyst.
2. The improvementin the art of making tin tetramethyl, which comprises alloying tin with sodium, subdividing the alloyand reacting upon the alloy with methyl chlorid while maintaining the temperature above the normal boiling point of methyl chlorid.
3. The improvement in the art of making hydrocarbon compounds of metals of the tin sub-group, which comprises alloying the metal with sodium, sub-dividing the alloy and reacting upon the alloy with an alkyl chlorid in the presence of a catalyst, while maintaining the temperature above the normal boiling point of the alkyl chlorid.
' 4. The im rovement inthe art of making metallo-alky' compounds of metals of the tin suboup, which comprises alloying the metal with sodium, and reacting upon the metallo-alkyl compounds of metals of the tin sub-group, which comprises alloying the metal with sodium, and reacting upon the alloy with an alkyl chlorid while maintaining a temperature above the normal boiling point of the alkyl chlorid.
6. The improvement in the art of making metallo-alkyl compounds of metals of the tin sub-group, which comprises alloying the metal with sodium, and reacting upon the alloy with an alkyl halid in which the halogen has a lower atomic weight than iodin'. in the presence of a catalyst while maintaining a temperature above the normal boiling point of the alkyl halid.
7. The improvement in the art of making metallo-alkyl compounds of metals of the tin sub-group, which comprises subjecting the metal in alloy with sodium to the action of an alkyl halid whose halogen is of a lower atomic weight than iodin, in the presence of a catalyst while maintaining a temperature fibp e the normal boiling point of the alkyl 8. The improvement in the art of making metallo-alkyl compounds of metals of the tin sub-group, which comprises subjecting the metal in alloy with a highly electropositive metal to the action of an alkyl halid in which the halogen has a lower atomic weight than iodin, in the presence of a catalyst while maintaining a pressure above normal atmospheric pressure.
9. The improvement in the art of making metalloealkyl compounds of metals of the tin sub-group, which comprises subjecting the metal in alloy with ahighly electropositive metal to the action of an alkyl halid 1n which the halogen has a lower atomic weight than iodin, in the presence of a catalyst while maintaining a tem erature above the normal boiling point of t e alkyl halid.
'10. The improvement in the art of making metallo-alkyl compounds of metals of the the metal in alloy with an alkali metal to the action of an alkyl halid whose halogen is of lower atomic weight than iodin in the presence of a catalyst.
and
11. The improvement in the art of making 12. The improvement in the art of making -tin sub-group, which comprises subjecting metallo-alkyl compounds of metals of the tin sub-group, which comprises subjecting metallo-alkyl compounds of metals of the the metal in alloy with an alkali metal to tin sub-group, which comprises subjecting the action of an alkyl halicl whose halogen the metal in alloy'with an alkali metal to 10 is of lower atomic weight than iodin while the action of an alkyl halid whose halogen 5 maintaining a temperature above the normal is of lower atomic weight than-iodin.
boilingngoint of the alkyl halid. CHARLES A. KRAUS. 13. e improvement in the art of making CONRAL C. CALLIS.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US631940A US1639947A (en) | 1923-04-13 | 1923-04-13 | Art of making metallo-organic compounds |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US631940A US1639947A (en) | 1923-04-13 | 1923-04-13 | Art of making metallo-organic compounds |
Publications (1)
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US1639947A true US1639947A (en) | 1927-08-23 |
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US631940A Expired - Lifetime US1639947A (en) | 1923-04-13 | 1923-04-13 | Art of making metallo-organic compounds |
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Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2444270A (en) * | 1946-04-16 | 1948-06-29 | Gen Electric | Method of preparing organogermanium halides |
US2451871A (en) * | 1946-08-17 | 1948-10-19 | Gen Electric | Dimethyl germanium dichloride |
US2570686A (en) * | 1948-05-04 | 1951-10-09 | Metal & Thermit Corp | Process for making tin hydrocarbons |
US2625559A (en) * | 1949-02-04 | 1953-01-13 | Union Carbide & Carbon Corp | Preparation of methyl tin chlorides |
US2852543A (en) * | 1954-10-14 | 1958-09-16 | Ethyl Corp | Process for the preparation of alkyl tin chlorides |
US3113955A (en) * | 1961-08-17 | 1963-12-10 | Du Pont | Process for making tetramethyl lead |
US3446824A (en) * | 1965-12-10 | 1969-05-27 | Monsanto Co | Direct process for the preparation of organogermanium halides |
-
1923
- 1923-04-13 US US631940A patent/US1639947A/en not_active Expired - Lifetime
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2444270A (en) * | 1946-04-16 | 1948-06-29 | Gen Electric | Method of preparing organogermanium halides |
US2451871A (en) * | 1946-08-17 | 1948-10-19 | Gen Electric | Dimethyl germanium dichloride |
US2570686A (en) * | 1948-05-04 | 1951-10-09 | Metal & Thermit Corp | Process for making tin hydrocarbons |
US2625559A (en) * | 1949-02-04 | 1953-01-13 | Union Carbide & Carbon Corp | Preparation of methyl tin chlorides |
US2852543A (en) * | 1954-10-14 | 1958-09-16 | Ethyl Corp | Process for the preparation of alkyl tin chlorides |
US3113955A (en) * | 1961-08-17 | 1963-12-10 | Du Pont | Process for making tetramethyl lead |
US3446824A (en) * | 1965-12-10 | 1969-05-27 | Monsanto Co | Direct process for the preparation of organogermanium halides |
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