Chemistry of inorganic compounds – Nitrogen or compound thereof – Hydrogen containing
Reexamination Certificate
2002-03-05
2004-06-29
Langel, Wayne A. (Department: 1754)
Chemistry of inorganic compounds
Nitrogen or compound thereof
Hydrogen containing
Reexamination Certificate
active
06756024
ABSTRACT:
The invention relates to a method for preparing lithium amide.
Lithium amide is a strong base. It is often used as a reagent in synthetic organic chemistry, for example in condensation or alkylation reactions (Encyclopaedia of Reagents for Organic Synthesis, Vol. 5, 3031, L. A. Paquette, John Wiley 1995).
Usual preparation methods provide that the lithium metal be dissolved in liquid ammonia (T<−33° C.) and subsequently reacted under the catalysis of a transition metal compound (for example iron III nitrate: Gmelin, Lithium, Supplementary Volume 20, 279) to form lithium amide. The disadvantage of this operation is the low temperature and hydrogen formation.
The reaction of lithium metal and gaseous ammonia at temperatures above 400° C. is also known. The disadvantage of this is the high temperature and hydrogen formation.
U.S. Pat. No. 5,486,343 describes a method for preparing lithium amide in which lithium metal is reacted in a solvent with ammonia to form lithium bronze and subsequently the lithium bronze is thermally decomposed to form lithium amide, hydrogen and ammonia. The disadvantage here is also the release of hydrogen.
The object of the invention is to overcome the disadvantages of the prior art and in particular to provide a method for preparing lithium amide in which no hydrogen is released and which operates, as far as possible, at ambient temperature.
The object is achieved by means of a method for preparing lithium amide in which in a first method step lithium metal is reacted with ammonia to form lithium bronze and in a second method step the lithium bronze is reacted with a 1,3-diene or an arylolefin in the presence of a solvent;
Preferred 1,3-dienes or arylolefins are butadiene, isoprene, piperylene, dimethylbutadiene, hexadiene, styrene, methyl styrene, naphthalene or anthracene.
The first reaction step may be carried out solvent free. However, operations are preferably carried out in a solvent in the first reaction step as well. Acyclic or cyclic aliphatic hydrocarbons, aromatic hydrocarbons or ethers or mixtures of these substances are preferably used as the solvents. Examples of solvents are pentane, cyclopentane, hexane, heptane, octane, cyclohexane, toluene, xylene, cumene, ethyl benzene, tetraline, diethyl ether, tetrahydrofuran (THF), 2-methyl-THF, tetrahydropyran, diisopropyl ether, dibutyl ether, dioxan, methyl-tert-butyl ether or glycol ether. When THF is used as the sole solvent in the first reaction step, it is to be borne in mind that the THF may be subjected to a slow decomposition reaction, whereby ethene and lithium ethanoate are formed.
A preferred temperature of reaction for both reaction steps lies between 0 and 30° C.
The heat of reaction in the first reaction step can be controlled, for example, by way of the rate of dosage of the ammonia. When a solvent is used in the first reaction step, it is possible to dissipate the heat by way of the solvent through jacket cooling. The lithium bronze that is formed then floats on the solvent and can be separated for purification purposes and, if required, stored and transported.
The heat of reaction in the second reaction step can be controlled, for example, by way of the rate dosage of the 1,3 diene or arylolefin. The lithium amide that is formed is insoluble and heavier than the reaction solution. The hydrogenated 1,3 diene or arylolefin is dissolved in the solvent; the ammonia is discharged in gaseous form and can be reclaimed. The powdery lithium amide is separated from the solvent and, if required, dried.
The advantage of the method in accordance with the invention is that the reaction can be carried out at ambient temperature (whereby the product is not subject to any thermal loading), that the product is of greater purity (impurities can be separated with the solvent), that no hydrogen is formed, and that the ammonia, which is free of hydrogen, can be recovered.
The invention is further exemplified with the aid of the following examples.
REFERENCES:
patent: 1570467 (1926-01-01), Ewan
patent: 2202994 (1940-06-01), Nieuwland
patent: 2315830 (1943-04-01), Vingee et al.
patent: 2490851 (1949-12-01), Alexander
patent: 2612436 (1952-09-01), Overhoff et al.
patent: 3542512 (1970-11-01), Honeycutt
patent: 3987151 (1976-10-01), Astrauskas et al.
patent: 4206191 (1980-06-01), Morrison et al.
patent: 5486343 (1996-01-01), Schwindeman et al.
Dawidowski Dirk
Weiss Wilfried
Chemetall GmbH
Langel Wayne A.
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