Kyösti Rajaniemi

Mr. Kyösti Rajaniemi

Processes, MDPI

Research Focus & Metrics

Academic Career Length

8Years (2019-Present)

(Calculated once Scilit publication data is synced: current year − year of first publication + 1)

Representative Publications

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14 December 2021 in Resources
Verified
Journal Article
Open access
PDF file
KRKyösti Rajaniemi
Kyösti Rajaniemi
STSari Tuomikoski
Sari Tuomikoski
Ulla LassiUlla Lassi
Ulla Lassi
In the field of electrocoagulation (EC), various studies on pollutant removal and on the use of different EC technologies have already been made. An EC process generates sludge, which is considered waste, resulting in increased operational costs that come from waste disposal. Sludge contains valuable materials, such as the nutrients or metals removed during water purification, along with metals, such as aluminum or iron, which come from the electrodes used in an EC system. Based on the principles of circular economy or based on existing legislations, reducing the production of valuable wastes, and increasing the valorization rate of as many materials as possible are important endeavors. This study is mainly a review of the existing sludge valorization studies. This review highlights the valorization of sludge as a fertilizer (mainly as struvite), pigment, construction material (mainly as blocks), adsorbent, and catalyst. While it has already been found that EC sludge is valorizable, more studies on EC sludge valorization and on the quality of sludge produced from the effluent of EC processes are warranted.

14 January 2021 in Processes
Verified
Journal Article
Open access
PDF file
KRKyösti Rajaniemi
Kyösti Rajaniemi
THTao Hu
Tao Hu
ENEmma-Tuulia Nurmesniemi
Emma-Tuulia Nurmesniemi
STSari Tuomikoski
Sari Tuomikoski
Ulla LassiUlla Lassi
Ulla Lassi
Batch electrocoagulation (BEC), continuous electrocoagulation (CEC), and chemical precipitation (CP) were compared in struvite (MgNH4PO4·6H2O) precipitation from synthetic and authentic water. In synthetic water treatment (SWT), struvite yield was in BEC 1.72, CEC 0.61, and CP 1.54 kg/m3. Corresponding values in authentic water treatment (AWT) were 2.55, 3.04, and 2.47 kg/m3. In SWT, 1 kg struvite costs in BEC, CEC, and CP were 0.55, 0.55, and 0.11 €, respectively, for AWT 0.35, 0.22 and 0.07 €. Phosphate removal in SWT was 93.6, 74.5, and 71.6% in BEC, CEC, and CP, respectively, the corresponding rates in AWT were 89.7, 77.8, and 74.4%. Ammonium removal for SWT in BEC, CEC, and CP were 79.4, 51.5, and 62.5%, respectively, rates in AWT 56.1, 64.1, and 60.9%. Efficiency in CEC and BEC are equal in nutrient recovery in SWT, although energy efficiency was better in CEC. CP is cheaper than BEC and CEC.

1 December 2019 in Desalination and Water Treatment
Verified
Journal Article
Open access
KRKyösti Rajaniemi
Kyösti Rajaniemi
MRMari Raulio
Mari Raulio
STSari Tuomikoski
Sari Tuomikoski
ULUlla Lassi
Ulla Lassi