Method for reducing fouling in furnaces
View Patent ↗Heat exchanger fouling in organic chemical production processes may be reduced using an antifoulant additive. The antifoulant additive may have one component selected from the group consisting of an alkylphosphate ester, and an alpha olefin maleic anhydride copolymer; or it may have two components selected from the group consisting of a metallic overbase, an alkylphosphate ester, and an alpha olefin maleic anhydride copolymer, wherein at least one of the two components in not an overbase. An additive having three components: a metallic overbase, an alkylphosphate ester, and an alpha olefin maleic anhydride copolymer; is also within the scope of the disclosure.
1. A process for reducing heat exchanger fouling in an organic chemical production process comprising adding to an organic chemical production process stream an antifoulant additive wherein the antifoulant additive comprises a metallic overbase, an alkylphosphate ester, and an alpha olefin maleic anhydride copolymer wherein the feed range of the antifoulant additives is from about 200 to about 800 ppm.
2. The process of claim 1 wherein the metallic overbase is a magnesium overbase or an aluminum overbase.
3. The process of claim 1 wherein the alkyl phosphate ester is selected from the group consisting of: isododecyl phosphate esters, isooctyl phosphate esters; and mixtures thereof.
4. The process of claim 3 wherein the alkyl phosphate ester is selected from the group consisting of: (ethyl)hexyl thiophosphate ester, di(ethyl)hexyl thiophosphate ester, octyl thiophosphate ester, butyl thiophosphate ester, nonyl thiophosphate ester, t-butyl thiophosphate ester, and mixtures thereof.
5. The process of claim 1 wherein the alpha olefin maleic anhydride copolymer has the general formula:
wherein R is a hydrocarbon substituent having from about 6 to about 30 carbons.
6. The process of claim 5 wherein R has from about 10 to 26 carbons.
7. The process of claim 6 the copolymer has a molecular weight (Mw) of from about 2,000 to about 12,000 Daltons.
8. The process of claim 1 wherein the antifoulant additives are used in processes wherein process feed steams are contacted with heat ranging from about 60° C. to about 870° C.
9. The process of claim 8 wherein the organic chemical production process stream is a hydrocarbon or a halohydrocarbon.
10. The process of claim 9 wherein the organic chemical production process produces a compound selected from the group consisting of ethylene dichloride, vinyl chloride monomer, and polyvinyl chloride.
11. The process of claim 10 wherein the organic chemical production process produces vinyl chloride monomer.