Fireside Corrosion on Heat Exchanger Surfaces and Its Effect on the Performance of Gas-Fired Instantaneous Water Heaters

The heat exchanger in a gas instantaneous water heater is a thermal device used for heat transfer from the high-temperature flue gas to the low-temperature water. The fireside corrosion, due to the reaction of acidic condensate formed on the heat exchanger surfaces and its metallic material, is one of the major hazards for gas instantaneous water heaters. This paper focuses on identifying and quantifying the fireside corrosion on the surface of heat exchangers in gas-fired instantaneous water heaters. Durability tests lasting for 2000 cycles were undertaken for five gas-fired instantaneous water heaters, which were different in terms of the heat input and coating of heat exchangers. The corrosion deposits on the surface of the heat exchangers were surveyed by several methods. The results show that the corrosion deposit grew as the test duration increased. The fins of the heat exchanger with a lead coating had been corroded and copper was exposed. Cu4(OH)6SO4 was the main corrosion product of heat exchangers without a lead coating, whereas PbSO4 was the main corrosion product of heat exchangers with a lead coating. The experiments demonstrate that the corrosion rate decreased with the increase of the heat input. The experiments also show that the thermal efficiency of gas instantaneous water heaters decreased by 2.4% to 6% at the end of the test duration.

[1]  Youliang He,et al.  Fluoropolymer composite coating for condensing heat exchangers: Characterization of the mechanical, tribological and thermal properties , 2015 .

[2]  Kwangkook Jeong,et al.  Theoretical prediction of sulfuric acid condensation rates in boiler flue gas , 2012 .

[3]  Lai‐Chang Zhang,et al.  Solid particle erosion of alumina ceramics at elevated temperature , 2013 .

[4]  P. Angell,et al.  Sulphate-reducing bacterial activity as a parameter to predict localized corrosion of stainless alloys , 2000 .

[5]  Y. Shida,et al.  Particle erosion behaviour of boiler tube materials at elevated temperature , 1985 .

[6]  T. Jonsson,et al.  Investigating corrosion memory: The influence of previous boiler operation on current corrosion rate , 2017 .

[7]  G. Scheffknecht,et al.  Fireside Corrosion of Applied and Modern Superheater-alloys Under Oxy-fuel Conditions , 2013 .

[8]  Khalil Ranjbar,et al.  Effect of flow induced corrosion and erosion on failure of a tubular heat exchanger , 2010 .

[9]  D. Leonard,et al.  Alloy Corrosion Considerations in Low-Cost, Clean Biomass Cookstoves for the Developing World , 2017 .

[10]  W. Tao,et al.  Gas-side fouling, erosion and corrosion of heat exchangers for middle/low temperature waste heat utilization: A review on simulation and experiment , 2017 .

[11]  A. Bahadori Estimation of combustion flue gas acid dew point during heat recovery and efficiency gain , 2011 .

[12]  Minyu Ma,et al.  Fouling corrosion in aluminum heat exchangers , 2015 .

[13]  J. M. Blanco,et al.  Increase in the boiler's performance in terms of the acid dew point temperature : Environmental advantages of replacing fuels , 2008 .

[14]  Kiyoshi Saito,et al.  Experimental study on titanium heat exchanger used in a gas fired water heater for latent heat recovery , 2010 .

[15]  G. Tang,et al.  Prediction of sulfuric acid dew point temperature on heat transfer fin surface , 2016 .

[16]  C. Monticelli,et al.  The inhibition of copper corrosion in 0.1 M NaCl under heat exchange conditions , 1996 .

[17]  I. Gurrappa,et al.  Cathodic protection of cooling water systems and selection of appropriate materials , 2005 .

[18]  G. H. Damon Acid Corrosion of Steel , 1941 .

[19]  Hans Müller-Steinhagen,et al.  Problems and Costs due to Heat Exchanger Fouling in New Zealand Industries , 1993 .

[20]  F. Frandsen,et al.  Effect of Water Vapor on High-Temperature Corrosion under Conditions Mimicking Biomass Firing , 2015 .

[21]  Robert Scharler,et al.  Investigation of the corrosion behaviour of 13CrMo4–5 for biomass fired boilers with coupled online corrosion and deposit probe measurements , 2015 .

[22]  Minghou Xu,et al.  Effect of HCl and CO on sulfur trioxide formation mechanisms during oxy-fuel combustion , 2018, Fuel Processing Technology.

[23]  K. Haberger,et al.  High performance forced air cooling scheme employing microchannel heat exchangers , 1995 .

[24]  S. Bürger,et al.  Implementation of Guide to the Expression of Uncertainty in Measurement (GUM) to Multi-Collector TIMS Uranium Isotope Ratio Metrology , 2010 .

[25]  R. Idem,et al.  Studies on corrosion and corrosion inhibitors for amine based solvents for CO2 absorption from power plant flue gases containing CO2, O2 and SO2 , 2011 .

[26]  D. H. Fatmehsari,et al.  Stress corrosion cracking in Type.316 plates of a heat exchanger , 2016 .

[27]  W. Tao,et al.  Mechanism research on coupling effect between dew point corrosion and ash deposition , 2013 .

[28]  Cuiwei Du,et al.  Materials science: Share corrosion data , 2015, Nature.

[29]  Douglas T. Queheillalt,et al.  The effects of topology upon fluid-flow and heat-transfer within cellular copper structures , 2004 .

[30]  Q. Zhao,et al.  Desulfurized flue gas corrosion coupled with deposits in a heating boiler , 2018 .

[31]  S. Srikanth,et al.  Analysis of failures in boiler tubes due to fireside corrosion in a waste heat recovery boiler , 2003 .