Skip to main page content
U.S. flag

An official website of the United States government

Dot gov

The .gov means it’s official.
Federal government websites often end in .gov or .mil. Before sharing sensitive information, make sure you’re on a federal government site.

Https

The site is secure.
The https:// ensures that you are connecting to the official website and that any information you provide is encrypted and transmitted securely.

Access keys NCBI Homepage MyNCBI Homepage Main Content Main Navigation
. 2024 Sep 21;17(18):4630.
doi: 10.3390/ma17184630.

Valorization of Iron (II) Oxalate Dihydrate Coming from Pickling Processes through Thermal Conversion

Affiliations

Valorization of Iron (II) Oxalate Dihydrate Coming from Pickling Processes through Thermal Conversion

Emiliano Salucci et al. Materials (Basel). .

Abstract

The valorization of industrial byproducts is an emerging practice that aims to transform waste materials generated during production processes into valuable resources. In this work, a preliminary study was carried out on the thermal conversion of an industrial solid byproduct resulting from the pickling of metal surfaces, mainly containing iron (II) oxalate. In a fixed-bed reactor, the thermal conversion was investigated as a function of the operating temperature and overall time. The starting material and the products obtained after heat treatment were characterized in detail, using numerous qualitative and semi-quantitative techniques. The aim of this research was to determine the optimal operating conditions for the transformation of the industrial byproduct into a high-quality product. By varying the operating conditions, it was found that complete conversion of iron (II) oxalate to magnetite was achieved at high temperatures (i.e., 773 K and 873 K) after one hour of treatment. The resulting product had a low degree of crystallization, which increased slightly with an increasing reaction time at a temperature of 873 K, reaching a maximum of about 11%. The magnetite obtained can be used in the future as a starting material for chemical looping processes as a chemical/energy carrier for the production of hydrogen.

Keywords: Iron (II) oxalate; circular economy; thermal treatment.

PubMed Disclaimer

Conflict of interest statement

The company had no role in the design of the study; in the collection, analyses, or interpretation of data; in the writing of the manuscript; or in the decision to publish the results.

Figures

Figure 1
Figure 1
XRD diffractograms that display (a) reflections of Fe(C2O4) 2H2O and (b) the principle crystallographic plane.
Figure 2
Figure 2
Schematic representation of the reactor system: (1) nitrogen bottle, (2) flowmeter, (3) reactor, (4) heating jacket, (5) thermoregulator, (6) heat exchanger.
Figure 3
Figure 3
Thermal decomposition results for oxalate: (a) thermogravimetric analysis coupled with differential scanning calorimetry and (b) thermogravimetric analysis coupled with mass spectrometry.
Figure 4
Figure 4
XRD pattern of the ((FeC2O4) 2H2O) starting material and after treatment at (a) T = 573 K for 30 min, 60 min, and 120 min; (b) T = 673 K for 30 min, 60 min, and 120 min; (c) T = 773 K for 30 min, 60 min, and 120 min; (d) T = 873 K for 30 min, 60 min, and 120 min. The crystalline phases with ICDD codes are indicated: 1 = ((FeC2O4) 2H2O, 010910997; and 2 = Fe3O4, 010861341.
Figure 4
Figure 4
XRD pattern of the ((FeC2O4) 2H2O) starting material and after treatment at (a) T = 573 K for 30 min, 60 min, and 120 min; (b) T = 673 K for 30 min, 60 min, and 120 min; (c) T = 773 K for 30 min, 60 min, and 120 min; (d) T = 873 K for 30 min, 60 min, and 120 min. The crystalline phases with ICDD codes are indicated: 1 = ((FeC2O4) 2H2O, 010910997; and 2 = Fe3O4, 010861341.
Figure 5
Figure 5
(a) Quantitative evaluation of the degree of crystallinity (DOC) after thermal conversion at different reaction times and temperatures and (b) qualitative evaluation of the degree of crystallinity after thermal conversion at different times and temperatures.

References

    1. Zaferani H.S., Sharifi M., Zaarei D., Shishesaz M.R. Application of eco-friendly products as corrosion inhibitors for metals in acid pickling processes—A review. J. Env. Chem. Eng. 2013;1:652–657. doi: 10.1016/j.jece.2013.09.019. - DOI
    1. Sefaja J., Dernikovic B., Malina J., Locrecek B. Investigation of steel corrosion in pickling solutions: Solutions with inhibitors. Surf. Technol. 1983;20:247–263. doi: 10.1016/0376-4583(83)90008-0. - DOI
    1. Liu Y., Wang L., Liu L., Han W., Sun X., Li J., Shen J. Hydrochloric acid pickling process optimization in metal wire working. Int. J. Simul. Syst. Sci. Technol. 2015;16:1.1–1.6. doi: 10.5013/IJSSST.a.16.05.01. - DOI
    1. Regel-Rosocka M. A review on methods of regeneration of spent pickling solutions from steel processing. J. Hazard. Mater. 2010;177:57–69. doi: 10.1016/j.jhazmat.2009.12.043. - DOI - PubMed
    1. Yang J.B., Cai N.S., Li Z.S. Hydrogen production from the steam-iron process with direct reduction of iron oxide by chemical looping combustion of coal char. Energy Fuels. 2008;22:2570–2579. doi: 10.1021/ef800014r. - DOI

LinkOut - more resources