Cleaning method for removing sulfur containing deposits from coke oven gas lines

Claim 2

Process for removing from gas lines for handling coal conversion process gases having properties similar to coke oven gas, hard to remove deposits deposited from said gases, said deposits containing high elemental sulfur content and multivalent compounds comprising (1) contacting said deposits with a cleaning composition comprising (a) a major portion of aliphatic amine capable of dissolving said elemental sulfur in the presence of water, (b) water in sufficient quantities to dissolve said multivalent compounds, and (c) sufficient oxidizing or reducing agent to change the valence of said multivalent compounds to a more uniform valent state to thereby be more readily dissolved by said water, (2) allowing said cleaning composition to remain in contact with said deposits for sufficient time to allow sufficient dissolution of said deposits to take place to allow removal of said deposits to take place, and (3) applying such force as is necessary to remove these partially dissolved deposits from said surface.

Claim 3

Process as in claim 1 wherein said cleaning composition comprises (1) from about 60 to about 90 volume percent aliphatic amine, (2) from about 10 to about 40 volume percent water, and (3) from about 1 to about 3 weight percent of a moderate oxidizing or reducing agent, such percentages based on the total composition.

Claim 4

Process as in claim 2 wherein said aliphatic amine is monoethanol amine, diethanol amine, triethanol amine, or diisopropanol amine, and wherein said moderate oxidizing agent or reducing agent is a water soluble hypochlorite, hypobromite, or hydroxylamine hydrochloride, hydroxylamine sulfate, stannous chloride or benzoyl peroxide.

Claim 5

Process as in claim 3 wherein the surface being cleaned is a gas line valve, and wherein said cleaning composition is first injected into said valve and then said valve is flushed out with a suitable liquid.

Claim 6

Process as in claim 1 wherein said process is repeated in order to substantially completely remove said deposits from said surface.

Claim 7

Process as in claim 1 wherein said deposits are contacted with said cleaning composition by spraying said cleaning composition onto said deposits over a period of time of at least two hours, such spraying being with such force to assist in the dissolving action.

Claim 8

Process as in claim 6 wherein said spraying is conducted as a fine, misty spray.

Claim 9

Process as in claim 7 wherein said spraying is conducted for a time period of between about 4 and about 10 hours.

Claim 10

Process as in claim 8 wherein said spraying is conducted for a time period of between about 6 and about 8 hours.

Claim 11

Process as in claim 6 wherein the time period for allowing said cleaning composition to remain in contact with said deposits after the spraying step is at least about 8 hours.

Claim 12

Process as in claim 9 wherein the time period for allowing said cleaning composition to remain in contact with said deposits after the spraying step is between about 16 hours and about 24 hours.

Claim 13

Process as in claim 6 wherein the amount of cleaning composition applied to said deposits is between about 2 and about 8 gallons of said cleaning composition for each 1 to 2 inch thickness of said deposits per square foot of area.

Claim 14

Process as in claim 1 wherein the temperature of said cleaning composition is maintained above freezing and below such temperature that substantial vaporization of said amine takes place.

Claim 15

Process as in claim 13 wherein said temperature is between about 50° F. and about 70° F.

Claim 16

Process for removing hard to remove deposits in coke oven gas lines containing elemental sulfur and multivalent compounds from a metal surface comprising (1) contacting said deposits by spraying with a cleaning composition for a time period of between about 4 and about 10 hours, said composition comprising (a) a major portion of aliphatic amine capable of dissolving said elemental sulfur in the presence of water, (b) water in sufficient quantities to dissolve said multivalent compounds, and (c) sufficient oxidizing or reducing agent to change the valence of said multivalent compounds to a more uniform valent state to thereby be more readily dissolved by said water, (2) allowing said cleaning composition to remain in contact with said deposits for sufficient additional time after said spraying to allow sufficient dissolution of said deposits to take place to allow removal of said deposits to take place, (3) applying such force as is necessary to remove the partially dissolved deposits from said surface, and (4) repeating steps (1), (2) and (3) as necessary to obtain substantially complete removal of said deposits from said surface.

Claim 17

Process for removing hard to remove deposits in coke oven gas lines containing elemental sulfur and multivalent compounds from a metal surface comprising (1) contacting said deposits by spraying with a cleaning composition for a time period of between about 4 and about 10 hours, said composition comprising (a) a major portion of aliphatic amine capable of dissolving said elemental sulfur in the presence of water, (b) water in sufficient quantities to dissolve said multivalent compounds, and (c) sufficient oxidizing or reducing agent to change the valence of said multivalent compounds to a more uniform valent state to thereby be more readily dissolved by said water, (2) allowing said cleaning composition to remain in contact with said deposits for sufficient additional time after said spraying to allow sufficient dissolution of said deposits to take place to allow removal of said deposits to take place, (3) applying such force as is necessary to remove the partially dissolved deposits from said surface, and (4) repeating steps (1), (2) and (3) as necessary to obtain substantially complete removal of said deposits from said surface.

Claim 18

Process as in claim 15 wherein said deposits initially contain both di- and tri-valent iron.