Olena Galkina
Water supply, sewerage and water purification
Department O.M. Beketov National University of Urban Economy
A
STATISTICAL MODEL FOR DETERMINING THE CORROSION RATE IN COKE-PLANT COOLING SYSTEMS
The
introduction of biologically treated phenolic wastewater eliminates carbonate
deposits in heat exchangers [1]. Using phenolic water with corresponding
reduction in the consumption of fresh water when using corrosion protection
inhibitors for byproduct-coking industry. The corrosion rate of carbon steel in the media
data reaches 1.5-2 mm/yr. The method can not be used without corrosion protection.
The aim of treatment is to develop a statistics model based
on corrosion rate of inhibitor protection of coke-plant heat exchangers when
using biologically treated phenolic wastewater in the circulating water.
Research [2] shows that the
optimal ratio of artesian and phenolic waters is 80:20%. However, even at this
ratio artesian and phenolic wastewater as supply water requires the addition of
corrosion inhibitors to the water-circulation system. Laboratory investigations
have been showed the absence of scale on the surface of the samples with
increasing evaporation coefficient. Established to decrease the corrosion rate
to 0.3-0.55 g/m2 h range.
Investigation
was conducted on water used in Kharkiv coke-plant cooling systems.
Circulating water, biochemically purified phenol wastewater and fresh water
from an artesian source were
used in experiments. This water was supply in the coke plant’s water-circulating system. The data on water quality have been reproduced in the laboratory as well as
experiments on real objects could lead to irreversible consequences.
Chromates,
silicates, and organic amines are common inhibitors. [3]. The reagent consisting of corrosion inhibitors (phosphates and silicates)
and a nitrification inhibitor (based on HCNS) was established [4]. The results
of reagent and optimum supplying water ratio using, slows total corrosion of
carbon steel to acceptable levels of 0.2–0.3 mm/yr with unchanging corrosion.
Depending
on the research of the corrosion rate of the water parameters and the
corrosion inhibitor amount in the circulating water. It is well accepted that the
corrosion rate can be modeled by statistics methods [5]. A model was found by using standard statistics
methods. R-squared value is 98,462 pct and mean absolute
error of proposed model is 3,8 pct. So proposed statistical model for determining the corrosion rate has the
following form:
, (1)
where Ding – inhibitor
administered dose, mg/dm3; Ky – evaporation coefficient; S – salinity, mg/dm3; pH – pH; A – alkalinity, mmol/dm3.
Proposed statistical model for determining the corrosion rate of
the water parameters and the corrosion inhibitor amount
in the circulating water adequate and suitable for use in
solving various tasks improve the efficiency of in coke-plant cooling systems circulating water. Further, these models can be used for corrosion rate evaluation and prediction of reverse
operation of the system.
References
1.
Vinarskii, N.S. and Papkov, G.I., Using coke-plant
wastewater in watercirculation systems, Express
Inform., 1978, ser.10, no. 1, pp. 7–10.
2.
Smilka O. The Complex Approach to Corrosion
Protection of Steel in Coke-Plant Cooling Systems / O. Smilka // Chemistry Journal. – Vol. 1, No. 4. – 2015.– pp. 124-132.
Available at: http://files.aiscience.org/journal/article/html/70410025.html.
3.
The Effects and Economic Impact of Corrosion //
Corrosion: Understanding the Basics. – ASM International, 2000. – Ch. 1. –
20 р. Available at: http://www.asminternational.org/documents/10192/1849770/06691G_Chapter_1.pdf.
4.
Ukrainian patent 109035 // Nesterenko S.V., Smilka O. P. and etc. – 2015.
5.
Mustaffa, Z. Developments in Reliability-Based
Assessment of Corrosion / Z. Mustaffa // Developments in Corrosion Protection; Aliofkhazraei, M., Ed.; Intech, 2014.
– pp 681-696.