Processes for operating a utility boiler and methods therefor
There is a process for operating a utility boiler. The process has the following steps: a) continuously adding one or more slag control agents, one or more oxygen-generating agents, and a fuel oil to a furnace of the utility boiler; b) providing air to the furnace; c) burning the fuel oil to generate heat and an exhaust gas; d) periodically or continuously varying the dosage rates of the one or more slag control agents and/or the one or more oxygen-generating agents to maintain to substantially maintain one or more emissions variables in the exhaust gas within pre-determined limits. There is also a method for reducing emissions from a utility boiler and a method for reducing slag deposits within a utility boiler.
1. A process for operating a utility boiler, comprising:
a) adding a fuel oil to a furnace of the utility boiler at an initial feed rate;
b) adding one or more slag control agents to the furnace at an initial dosage rate based upon the initial feed rate of the fuel oil;
c) optionally adding one or more oxygen-generating agents to the furnace at an initial dosage rate based upon the initial feed rate of the fuel oil;
d) providing air to the furnace;
e) burning the fuel oil to generate heat;
f) increasing the initial feed rate of the fuel oil to an increased feed rate;
g) reducing the initial dosage rate of the one or more slag control agents based upon the increased feed rate of the fuel oil;
h) adding one or more oxygen-generating agents if one or more oxygen-generating agents were not previously added in step (c), wherein the dosage rate of the one or more oxygen-generating agents is based upon the increased feed rate of the fuel oil, or, if one or more oxygen-generating agents were previously optionally added, increasing the dosage rate of the one or more oxygen-generating agents relative to the initial rate in step (c) based upon the increased feed rate of the fuel oil;
i) continue providing air to the furnace; and
j) continue burning the fuel oil to generate heat,
wherein the slag control agent is selected from the group consisting of magnesium hydroxide, magnesium oxide, magnesium carbonate, magnesium organometallic compounds, magnesium carboxylate, magnesium salicylate, magnesium napthenate, and magnesium sulfonate.
2. The process of claim 1 , wherein the one or more oxygen-generating agents is selected from the group consisting of calcium hydroxide, calcium oxide, calcium carbonate, calcium carboxylate, calcium nitrate, calcium organometallic compounds, calcium sulfonate, iron hydroxides, iron oxides, iron carbonates, iron carboxylates, iron organometallic compounds, iron sulfonates, barium hydroxide, barium oxide, barium carbonate, barium carboxylate, barium organometallic compounds, and barium sulfonate.
3. The process of claim 1 , wherein the one or more slag control agents and the one or more oxygen-generating agents are added to the fuel oil.
4. The process of claim 1 , wherein the one or more oxygen-generating agents was not previously added.
5. The process of claim 4 , wherein the one or more oxygen-generating agents is selected from the group consisting of calcium nitrate and calcium organometallic compounds.
6. The process of claim 1 , wherein the one or more oxygen-generating agents is selected from the group consisting of calcium nitrate and calcium organometallic compounds.
7. The process of claim 6 , wherein the one or more oxygen-generating agents is calcium nitrate.
8. The process of claim 1 , wherein the slag control agent is magnesium hydroxide.
9. A process for operating a utility boiler, comprising:
(a) continuously burning one or more slag control agents, one or more oxygen-generating agents, and a fuel oil in an excess of air in a furnace of the boiler to generate heat and an exhaust gas, wherein the one or more slag control agents and the one or more oxygen-generating agents are different compounds;
(b) varying the dosage rates of the one or more slag control agents and/or the one or more oxygen-generating agents with respect to the feed rate of the fuel oil; and
(c) maintaining the level of air in the furnace such that the excess air content in the exhaust gas is lower than required for complete burning of the fuel oil without the one or more oxygen-generating agents,
wherein the dosage rate of the one or more slag control agents is reduced or eliminated as the dosage rate of the one or more oxygen-generating agents is increased.
10. The process of claim 9 , wherein the level of air in the furnace is maintained such that the level of residual oxygen content in the exhaust gas is less than 3 wt % based on the weight of the exhaust gas.
11. The process of claim 9 , wherein the level of air in the furnace is maintained such that the level of residual oxygen content in the exhaust gas is less than 1 wt % based on the weight of the exhaust gas.
12. The process of claim 9 , wherein the dosage rate of the one or more oxygen-generating agents is increased when the feed rate of the fuel oil is increased.
13. The process of claim 9 , wherein the slag control agent is selected from the group consisting of magnesium hydroxide, magnesium oxide, magnesium carbonate, magnesium organometallic compounds, magnesium carboxylate, magnesium salicylate, magnesium napthenate, and magnesium sulfonate.
14. The process of claim 9 , wherein the one or more oxygen-generating agents is selected from the group consisting of calcium hydroxide, calcium oxide, calcium carbonate, calcium carboxylate, calcium nitrate, calcium organometallic compounds, calcium sulfonate, iron hydroxides, iron oxides, iron carbonates, iron carboxylates, iron organometallic compounds, iron sulfonates, barium hydroxide, barium oxide, barium carbonate, barium carboxylate, barium organometallic compounds, and barium sulfonate.
15. The process of claim 9 , wherein the slag control agent is magnesium hydroxide, wherein the one or more oxygen-generating agents is selected from the group consisting of calcium nitrate and calcium organometallic compounds.