Correlation between the fouling of different crystal calcium carbonate and Fe2O3 corrosion on heat exchanger surface

2021 ◽  
pp. 1-14
Author(s):  
Lu Ren ◽  
Gui-hui Qiu ◽  
Hong-ying Yu ◽  
Peng Zhou ◽  
Tetsuo Shoji ◽  
...  
1975 ◽  
Vol 97 (4) ◽  
pp. 504-508 ◽  
Author(s):  
A. P. Watkinson ◽  
O. Martinez

Scaling of copper heat exchanger tubes has been studied under conditions that promote rapid and severe scaling. Artificially hardened water of high dissolved and suspended solids is recirculated through a heated test section operated at constant steam temperature. The effects of flow velocity, tube diameter, and bulk temperature on the asymptotic fouling resistance have been determined. Results are interpreted in terms of mathematical models of the scaling process.


2020 ◽  
Vol 373 ◽  
pp. 671-680 ◽  
Author(s):  
C.S. Oon ◽  
S.N. Kazi ◽  
M.A. Hakimin ◽  
A.H. Abdelrazek ◽  
A.R. Mallah ◽  
...  

1986 ◽  
Vol 108 (1) ◽  
pp. 147-152 ◽  
Author(s):  
R. Sheikholeslami ◽  
A. P. Watkinson

The performance of copper and mild steel plain heat exchanger tubes and an externally finned mild steel tube was studied under calcium carbonate scaling conditions. Under a constant heat flux for 70-h periods the fouling resistance generally increased linearly with time. The effect of velocity on the rate of scale formation is presented for the three tubes and results compared with the model of Hasson.


2020 ◽  
Vol 24 (6 Part A) ◽  
pp. 3477-3488
Author(s):  
He-Xin Liu ◽  
Jia-Fan Xiao ◽  
Hou-Zhang Tan ◽  
Yi-Bin Wang ◽  
Fu-Xin Yang

The control of fouling deposition on the main equipment has always been an im-portant issue concerned by scientific research and industrial application. How-ever, severe fouling deposits on the induced fan blade and the low temperature economiser were found in a 1000 MW coal-fired power plant with ultra-low emission. The deposit samples were collected and analysed through X-ray dif-fraction spectrometer, X-ray fluorescence, elemental analyser and SEM with en-ergy dispersive spectrometers. The result shows that the deposits are mainly composed of tschermigite (NH4)Al(SO4)2 ? 12H2O, letovicite (NH4)3H(SO4)2, cal-cium sulphate CaSO4, and quartz SiO2. The ammonium sulphate is the main component of the fouling deposits. It acts as an adhesive and makes an important contribution to the deposition. The analysis shows that the ammonia slip from denitrification system and the unreasonable temperature setting are the main reasons for fouling deposition. It is suggested that the high concentration of am-monium slip at denitrification system and the rapid condensation of the sulphuric acid mist at heat exchanger should be paid more attention in coal-fired power plants.


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