Apparatus and process for preparing sorbents for mercury control at the point of use
View Patent ↗A system for treating a contaminated gas stream is provided that includes a comminution device 204 operable to effect size reduction of a plurality of sorbent particles and form a plurality of comminuted particles, a plurality of nozzles 224 distributed through the gas stream and operable to introduce the plurality of comminuted particles into the gas stream, and a particle removal device 104 operable to remove at least most of the introduced comminuted particles and form a treated gas stream. The comminution device is in direct fluid communication with the nozzles.
1. A method, comprising:
receiving, at a coal-fired plant site, a particulate sorbent material shipped from a remote location;
milling the received particulate sorbent material to produce a plurality of milled sorbent particles, the particulate sorbent material, prior to the milling step, having a first size distribution and the milled sorbent particles having a second size distribution, wherein the second size distribution is smaller than the first size distribution, wherein the second size distribution has a P 90 size ranging from about 0.5 to about 25 microns, and wherein the milling step occurs on-site with the coal-fired plant; and
thereafter introducing the milled sorbent particles into a contaminated flue gas stream from the coal-fired plant to remove one or more contaminants in the contaminated flue gas stream.
2. The method of claim 1 , wherein the milling step is performed by a jet mill and wherein the coal-fired plant is located on site.
3. The method of claim 1 , wherein the milled sorbent particles are introduced directly into the contaminated flue gas stream after the milling step.
4. The method of claim 1 , wherein the milled sorbent particles are free of intermediate storage after the milling step.
5. The method of claim 1 , wherein the one or more contaminants comprise an air toxic and wherein the time between the completion of the milling step to the introducing step is no more than about 30 seconds.
6. The method of claim 5 , wherein the particulate sorbent material is activated carbon and wherein the air toxic is at least one of arsenic, chromium, nickel, mercury, lead, selenium, a halogen, and a halide.
7. The method of claim 1 , wherein the first size distribution has a P 90 size ranging from about 10 microns to about 1 millimeter.
8. The method of claim 1 , wherein, in the milling step, a size reduction factor ranges from about 5 to about 200.
9. The method of claim 1 , wherein the time between the completion of the milling step to the introducing step is no more than about 30 minutes.
10. The method of claim 1 , wherein the milling step comprises the substeps:
supplying the particulate sorbent material having the first size distribution to an agitated media attrition mill;
supplying a high pressure fluid stream to the agitated media attrition mill;
in a grinding chamber of the mill, imparting, by one or more nozzles, a sonic or supersonic velocity to the fluid stream, causing the sorbent particles to be entrained in the fluid stream, thereby accelerating the particles and, through interparticle collisions, effecting reduction of the sizes of the particles; and
conveying the milled particles to a particle size separator, the separator rejecting oversized milled sorbent particles and outputting milled sorbent particles of a predetermined size distribution.
11. A method, comprising:
receiving, at a site of a coal-fired plant, a particulate sorbent material having a first size distribution and shipped from a remote location;
milling the received particulate sorbent material to produce a plurality of milled sorbent particles, the milled sorbent particles having a second size distribution, wherein the second size distribution is smaller than the first size distribution, wherein the second size distribution has a P 90 size ranging from about 0.5 to about 25 microns, and wherein the milling step occurs on-site with the coal-fired plant; and
introducing the milled sorbent particles into a contaminated gas stream, produced by coal combustion at the coal-fired plant, to remove one or more contaminants from the contaminated gas stream.
12. The method of claim 11 , wherein the milled sorbent particles are introduced directly into the contaminated gas stream after the milling step.
13. The method of claim 11 , wherein the milling step is performed by a jet mill.
14. The method of claim 11 , wherein the milled sorbent particles are free of intermediate storage after the milling step.
15. The method of claim 11 , wherein the one or more contaminants comprise an air toxic and wherein the time between the completion of the milling step to the introducing step is no more than about 1 hour.
16. The method of claim 15 , wherein the particulate sorbent material is activated carbon and wherein the air toxic is at least one of nickel, arsenic, chromium, mercury, selenium, lead, a halogen, and a halide.
17. The method of claim 11 , wherein the first size distribution has a P 90 size ranging from about 10 microns to about 1 millimeter.
18. The method of claim 11 , wherein, in the milling step, a size reduction factor ranges from about 5 to about 200.
19. The method of claim 11 , wherein the milling step comprises:
entraining the particulate sorbent in a high velocity gas stream; and
impacting the particulate sorbent at the velocity of the high velocity gas stream against at least one of another particle and a stationary comminution surface to effect size reduction.
20. A method, comprising:
providing a particulate sorbent material received from a location remote from a coal-fired plant site, the provided particulate sorbent material having a first size distribution;
providing a contaminated gas stream, the gas stream comprising one or more contaminants; and
in an agitated media attrition mill,
entraining the provided particulate sorbent in a high velocity gas stream; and
impacting the provided particulate sorbent, while entrained in the high velocity gas stream, against at least one of another particle and a stationary comminution surface to effect size reduction and produce a plurality of milled sorbent particles, the milled sorbent particles having a second size distribution, wherein the second size distribution is smaller than the first size distribution, wherein the second size distribution has a P 90 size ranging from about 0.5 to about 25 microns, and wherein the agitated media attrition mill is located on-site with the coal-fired plant; wherein the milled sorbent particles are introduced into the contaminated gas stream to remove the one or more contaminants.
21. The method of claim 20 , wherein the milled sorbent particles are introduced directly into the contaminated gas stream after the milling step.
22. The method of claim 20 , wherein the milling step is performed by a jet mill.
23. The method of claim 20 , wherein the milled sorbent particles are free of intermediate storage after the milling step.
24. The method of claim 20 , wherein the one or more contaminants comprise an air toxic and wherein the time between the completion of the milling step to the introducing step is no more than about 30 seconds.
25. The method of claim 24 , wherein sorbent material is activated carbon and wherein the air toxic is at least one of nickel, arsenic, chromium, mercury, selenium, lead, a halogen, and a halide.
26. The method of claim 20 , wherein the first size distribution has a P 90 size ranging from about 10 microns to about 1 millimeter.
27. The method of claim 20 , wherein, in the milling step, the size reduction factor ranges from about 5 to about 200.