Claims
- 1. A process for the production of an .alpha.-nitrosoketal dimer of the formula ##STR37## wherein R.sup.1 and R.sup.2 are selected from the group consisting of C.sub.1 -C.sub.10 alkyl or phenyl and/or combinations thereof, or in combination together R.sup.1 and R.sup.2 are a part of the C.sub.5 -C.sub.12 cyclic structures, and
- R.sup.3 and R.sup.4 are independently selected from the group consisting of C.sub.1 -C.sub.10 alkyl, cyclohexyl and C.sub.1 -C.sub.4 alkyl substituted cyclohexyl radicals, comprising the steps of:
- a. nitrosating, in the presence of a catalytic amount of a suitable acid and at a temperature of between about -70.degree. and 25.degree. C and at a pressure of between about one atmosphere and 200 psi, an alkoxyalkene of the formula ##STR38## wherein R.sup.1 and R.sup.2 are selected from the group consisting of C.sub.1 -C.sub.10 alkyl, phenyl and wherein both R.sup.1 and R.sup.2 are part of a C.sub.5 -C.sub.12 carbo-cyclic structure, and R.sup.3 is selected from the group consisting of C.sub.1 -C.sub.10 alkyl, cyclohexyl and C.sub.1 -C.sub.4 alkyl substituted cyclohexyl; with at least one molar equivalent of an alkyl nitrite of the formula
- R.sup.4 ONO
- wherein R.sup.4 is selected from the group consisting of C.sub.1 -C.sub.10 alkyl, cyclohexyl and C.sub.1 -C.sub.4 alkyl substituted cyclohexyl; and
- b. isolating the dimer thus formed.
- 2. The process of claim 1 wherein the alkyl nitrite is present in amount of 2-10 moles per mole of alkoxyalkene.
- 3. The process of claim 1 wherein the acid catalyst is sulfuric acid, sulfur trioxide, boron trifluoride etherate, ethyldimethoxycarbonium fluoroborate.
- 4. The process of claim 1 wherein the reaction is carried out in liquid sulfur dioxide using an alkyl nitrite in an amount of 1.10-1.50 moles per mole.
- 5. The process for the production of 1,1-dimethoxy-2-nitrosocyclohexane dimers comprising the steps of (a) nitrosating 1-methoxycyclohexene with 2-10 molar equivalents of methyl nitrite in the presence of 1.10-2.0 mole % of ethyldimethoxycarbonium fluoroborate catalyst at temperature between -30.degree. and 25.degree. C., and pressure of one atmosphere to 200 psi and;
- b. evaporation of the excess of methyl nitrite, followed by addition of petroleum ether or other inert solvent, and filtration of the product.
Parent Case Info
This is a continuation-in-part of application Ser. No. 460,836, filed Apr. 15, 1974, now abandoned.
US Referenced Citations (4)
Number |
Name |
Date |
Kind |
2371418 |
Beckham et al. |
Mar 1945 |
|
2394430 |
Crowder et al. |
Feb 1946 |
|
3222380 |
Manning et al. |
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3647777 |
Hudson et al. |
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|
Continuation in Parts (1)
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Number |
Date |
Country |
Parent |
460836 |
Apr 1974 |
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