US2018022691A1PendingUtilityA1
High Purity Ethylenediamine for Semiconductor Applications
Est. expiryJul 21, 2036(~10 yrs left)· nominal 20-yr term from priority
H10P 72/0402B01J 20/18B01J 20/2808B65D 81/20C07C 211/10C07C 209/86B08B 9/08C07C 209/84H01L 21/67017B01J 19/14
53
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Claims
Abstract
Ethylenediamine (EDA) compositions and methods for making the EDA that is suitable for use in thin-film semiconductor processing applications, are disclosed. The EDA is purified to remove water and trace metals. Water levels below about 50 ppm by weight are achieved by passing liquid through 3A type molecular sieve in a packed bed. Metallic impurities are removed by distillation and the resulting product is packaged in specially dried and optionally pre-conditioned containers.
Claims
exact text as granted — not AI-modified1 . Ethylenediamine wherein the ethylenediamine is greater than about 99.9 weight percent pure and contains less about 50 ppm water and less than about 100 ppb trace metals.
2 . The ethylenediamine of claim 1 wherein the ethylenediamine contains less than about 50 ppb of aluminum, chromium, copper, iron, magnesium, manganese, molybdenum, nickel, titanium and zinc.
3 . The ethylenediamine of claim 1 wherein the ethylenediamine contains less than about 10 ppm of water.
4 . The ethylenediamine of claim 1 wherein the ethylenediamine contains less than about 5 ppm of water.
5 . The ethylenediamine of claim 1 wherein the ethylenediamine contains less than about 1 ppm of water.
6 . The ethylenediamine of claim 1 wherein the ethylenediamine contains less than about 5 ppm of halides.
7 . The ethylenediamine of claim 6 wherein the halide is chlorine.
8 . The ethylenediamine of claim 1 wherein the ethylenediamine contains less than about 5 ppb of alkali metals.
9 . The ethylenediamine of claim 8 wherein the alkali metal is sodium.
10 . A composition comprising the ethylenediamine of claim 1 .
11 . A method for treating ethylenediamine comprising contacting ethylenediamine with a molecular sieve comprising type 3A zeolite under conditions sufficient to reduce the amount of water in the ethylenediamine to less than about 50 ppm; and, distilling the ethylenediamine under conditions sufficient to reduce the amount of trace metals to less than about 100 ppb.
12 . The method of claim 11 wherein the ethylenediamine is greater than about 99.9 weight percent pure.
13 . The method of claim 11 wherein the ethylenediamine flows through a bed of type 3A zeolite
14 . A method for treating a container comprising introducing an inert gas into the container while heating the container to a temperature of greater than about 120° C., introducing the ethylenediamine of claim 9 into the container; and removing the ethylenediamine.
15 . The method of claim 14 wherein the container comprises stainless steel.
16 . A container containing the ethylenediamine of claim 2 .
17 . The container of claim 16 comprising an inert headspace gas selected from helium, nitrogen, argon, and mixtures thereof.Cited by (0)
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