SYSTEMS AND METHODS FOR UTILIZING FLUE GAS
Systems and apparatuses for cooling flue gases emitted from an industrial facility, such as a coke oven in a coke manufacturing plant. A representative system includes a heat recovery steam generator (HRSG) having a steam generation system that converts liquid feedwater into steam by absorbing heat from the flue gases. The steam generation system includes a plurality of tubes that carry the liquid water feedwater and the steam. Some or all of the tubes include steel and a non-corrosive material cladded to the steel that helps to reduce corrosion caused by the high temperature flue gases and extremely corrosive contaminants within the flue gas that can corrode steel.
1 - 21 . (canceled)
22 . A coke plant, comprising:
a plurality of coke ovens configured to produce coke from coal and to emit flue gases;
a common tunnel fluidly coupled to each of the plurality of coke ovens and configured to receive the flue gases from each of the coke ovens;
and
a heat recovery steam generator (HRSG) fluidly coupled between the common tunnel and the desulfurization system, wherein the HRSG comprises:
an inlet duct configured to receive the flue gases at a first temperature from the common tunnel;
an outlet duct configured to provide the flue gases at a second temperature less than the first temperature to the desulfurization system, wherein the flue gases are configured to flow through the HRSG by flowing from the inlet duct to the outlet duct;
at least one economizer configured to receive liquid water and having a plurality of economizer tubes configured to transport liquid water, wherein the plurality of economizer tubes is configured to heat the liquid water using heat given off by the flue gases;
a plurality of evaporators configured to receive the heated liquid water from the at least one economizer and having a plurality of evaporator tubes configured to transport the liquid water, wherein the plurality of evaporators tubes is configured to heat the liquid water within the plurality of evaporator tubes using heat given off by the flue gases until the liquid water evaporates into steam and wherein individual of the plurality of evaporator tubes are coated with an anti-corrosion material.
23 . The coke plant of claim 22 , wherein the HRSG further comprises:
a superheater configured to receive the steam from the plurality of evaporators and having a plurality of superheater tubes configured to transport the steam, wherein the superheater is configured to superheat the steam within the plurality of superheater tubes using heat given off by the flue gases, and wherein a majority of the plurality of superheater tubes are coated with the anti-corrosion material.
24 . The coke plant of claim 23 , wherein the anti-corrosion material comprises an alloy.
25 . The coke plant of claim 23 , wherein the anti-corrosion material comprises silicon carbide or refractory.
26 . A method of modifying a heat recovery steam generator (HRSG) configured to receive high temperature and high pressure flue gases, wherein the flue gases are corrosive at temperatures above a critical temperature, wherein the HRSG includes at least one evaporator having a plurality of evaporator tubes, wherein individual of the plurality of evaporator tubes have evaporator tube surface temperatures greater than the critical temperature during operation of the HRSG, the method comprising:
detaching the individual evaporator tubes from the evaporator and removing the individual evaporator tubes from the HRSG; and
fluidly coupling a replacement evaporator tube to the evaporator at each location where an individual evaporator tube is detached from the evaporator, wherein each of the replacement evaporator tubes is clad with a material that is resistant to corrosion.
27 . The method of claim 26 wherein the HRSG includes at least one superheater having a plurality of superheater tubes and wherein individual of the plurality of superheater tubes have superheater tube surface temperatures greater than the critical temperature during operation of the HRSG, the method further comprising:
detaching the individual superheater tubes from the superheater and removing the individual superheater tubes from the HRSG; and
fluidly coupling a replacement superheater tube to the superheater at each location where an individual superheater tube is detached from the superheater, wherein each of the replacement superheater tubes is clad with the material that is resistant to corrosion.
28 . The method of claim 27 wherein:
the plurality of superheater tubes comprises straight segments and curved segments,
one of the replacement superheater tubes comprises a straight replacement superheater tube having an end portion that is free from the material resistant to corrosion,
detaching the individual superheater tubes from the superheater and removing the individual superheater tubes from the HRSG comprises detaching a given straight segment from a given curved segment and removing the given straight segment from the HRSG, and
fluidly coupling the replacement superheater tubes to the superheater comprises welding the end portion of the straight superheater replacement tube to the given curved segment.
29 . The method of claim 28 , further comprising:
after welding the end portion of the straight superheater replacement tube to the given curved segment, manually welding the material resistant to corrosion to at least the end portion.
30 . The method of claim 28 , further comprising:
after welding the end portion of the straight superheater replacement tube to the given curved segment, coating at least the end portion with refractory.
31 . The method of claim 26 , wherein the material resistant to corrosion comprises an alloy.
32 . The method of claim 31 , wherein the alloy comprises a Nickel-rich alloy.
33 . The method of claim 26 , wherein the material resistant to corrosion comprises silicon carbide.