Circulation aid for primary fractional quench loops
The invention directed to a method of reducing the increase in viscosity and the drop in the heat transfer coefficient that commonly occurs with quenching media which is repeatedly circulated through a hot reaction vessel. The method comprises adding a preserving composition to the quenching media. The composition comprises: a) high temperature polymerization inhibitor, b) a tar dispersant, and c) a viscosity reducer. The method allows the quenching media to remain effective longer than would otherwise be the case. By doing so this prevents having to devote excessive resources for such problems as: controlling heat recovery, viscosity increases, product downgrades or having to operate equipment at temperatures beyond their optimum performance designs.
1. A method of utilizing quenching media, the method comprising the steps of:
repeatedly circulating a quenching media through a hot circulation system, the quenching media comprising an amount of reactive monomers exceeding about one percent (by weight) of a cracked material as it passes through the hot circulation system, and
adding a composition to the quenching media, the composition comprising:
a) high temperature polymerization inhibitor having a first amount,
b) a tar dispersant, and
c) a viscosity reducer having a second amount,
wherein the first amount is about equal to or less than the second amount, the first amount and the second amount determined by weight percentages, and
wherein the composition reduces viscosity in the quenching media more than a phenol-formaldehyde resin alone.
2. The method of claim 1 , wherein the composition further comprises a high boiling point solvent having a boiling point above 150° C.
3. The method of claim 1 , wherein the high temperature polymerization inhibitor is 1-naphthol or hindered phenol.
4. The method of claim 1 , wherein the tar dispersant is alkyl substituted phenol formaldehyde resin.
5. The method of claim 1 , wherein the viscosity reducer is alpha olefin-alkyl maleate co-polymer.
6. The method of claim 1 , wherein the composition is added to the quenching media to result in an amount of 100-10000 ppm.
7. The method of claim 1 , wherein the quenching media is quench oil.
8. The method of claim 1 , wherein the hot circulation loop is a primary fractionator quench oil loop in an ethylene plant.
9. The method of claim 1 , wherein the hot circulation loop is one selected from the list consisting of a primary fractionator in ethylene plant or an EDC/VCM application.
10. The method of claim 1 , wherein the residence time of the quenching media in the reaction vessel varies between 1 hour and 10 days.
11. The method of claim 1 , wherein the temperature of the quenching media in the reaction vessel is between 20 and 300° C.
12. The method of claim 1 , wherein a ratio (by weight) of the high temperature polymerization inhibitor to viscosity reducer is 1:1.
13. The method of claim 1 , wherein a ratio (by weight) of the high temperature polymerization inhibitor to viscosity reducer is 1:4.
14. The method of claim 1 , wherein the tar dispersant is free of phenol-formaldehyde resin.
15. The method of claim 1 , wherein the tar dispersant is a polyacrylate copolymer.
16. A method of utilizing quenching media, the method comprising the steps of:
repeatedly circulating a quenching media through a hot circulation system, the quenching media comprising an amount of reactive monomers exceeding about one percent (by weight) of a cracked material as it passes through the hot circulation system,
and adding a composition to the quenching media, the composition comprising:
a) high temperature polymerization inhibitor
b) a tar dispersant being free of a phenol-formaldehyde resin, and
c) a viscosity reducer
wherein the polymerization inhibitor has a first amount and the viscosity reducer has a second amount such that the first amount is about equal to or less than the second amount, the first amount and the second amount determined by weight percentages,
wherein the composition reduces viscosity in the quenching media more than a phenol-formaldehyde resin alone.
17. The method of claim 16 , wherein the tar dispersant is polyacrylate copolymer.
18. The method of claim 16 , wherein the ratio of the high temperature polymerization inhibitor to the viscosity reducer is about 1:1.
19. The method of claim 16 , wherein the ratio of the high temperature polymerization inhibitor to the viscosity reducer is about 1:4.
20. The method of claim 1 , wherein the first amount is less than the second amount.