Claims Analysis
Total Claims: 11
Claim 1
Independent Claim
64 words
A method of removing chloromethyl methyl ether and/or bis-chloromethyl ether from inert gasses, such as air, contaminated with small amounts of such ether which comprises contacting the contaminated gas containing a small amount by volume of water vapor with an adsorbent bed comprising silica gel or activated alumina, or mixtures thereof, at such a temperature that said ether component of the gas is hydrolized.
Claim 2
Independent Claim
64 words
A method of removing chloromethyl methyl ether and/or bis-chloromethyl ether from inert gasses, such as air, contaminated with small amounts of such ether which comprises contacting the contaminated gas containing a small amount by volume of water vapor with an adsorbent bed comprising silica gel or activated alumina, or mixtures thereof, at such a temperature that said ether component of the gas is hydrolized.
Claim 3
Dependent Claim
18 words
A method according to claim 1 wherein the temperature is in the range of up to about 150°C.
Claim 4
Dependent Claim
19 words
A method according to claim 1 wherein the temperature is in the range of about 60° to about 80°C.
Claim 5
Dependent Claim
47 words
A method according to claim 1 wherein the contaminated gas is preheated to a temperature sufficiently above 70°C. before it is passed into contact with the adsorbent bed to assure that the temperature of the effluent gas stream discharged from the adsorber is at least about 65°C.
Claim 6
Dependent Claim
43 words
A method according to claim 1 wherein the contaminated gas is passed through silica gel heated to a temperature sufficiently above 70°C. to assure that the temperature of the effluent gas stream discharged from the silica gel adsorber is at least about 65°C.
Claim 7
Dependent Claim
43 words
A method according to claim 1 wherein the contaminated gas is passed through activated alumina heated to a temperature sufficiently above 70°C. to assure that the temperature of the effluent gas stream discharged from the activated alumina adsorber is at least about 65°C.
Claim 8
Dependent Claim
71 words
A method according to claim 4 wherein the preheated contaminated gas is supplied to the upper region of the adsorber above the column or adsorbent bed and is discharged from the bottom thereof, the rate of flow of the gas and the temperature thereof being correlated with the volume of adsorbent in the adsorber to assure substantially complete break-down of said ether component into hydrogen chloride, methylal and/or methanol and formaldehyde.
Claim 9
Dependent Claim
32 words
A method according to claim 6 wherein the gas effluent from the adsorber is subjected to a scrubbing aqueous stream, e.g., by passing countercurrent to a stream of water in a scrubber.
Claim 10
Dependent Claim
45 words
A method according to claim 4 wherein the contaminated gas stream is periodically heated to a temperature level at least 50°C. above the range mentioned in claim 4 for short periods of time to reduce or eliminate any adsorbed organic matter accumulated on the adsorbent.
Claim 11
Dependent Claim
58 words
A method according to claim 5 wherein the silica gel is in particulate form having a mesh size in the range of about 6 to 20, U.S. wire screen scale and the moisture content of the air contaminated with said ether(s) is about 0.1 to 10% by volume of the air as it passes to the silica gel.