Jesus Beltran-Heredia
Current Organizations / Institutes
The organizations/institutes from the scholar's latest article
Previous Organizations / Institutes
The organizations / institutes from the scholar's other articles in the past ten years
Research Subjects
Jesus Beltran-Heredia has a total of 113 co-authors. Here are the top co-authors by number of shared publications:
- Jesús Sánchez-Martín
Facultad de Educación y Psicología, Universidad de Extremadura, Badajoz, Spain
39 shared publications - Joaquin Ramon Dominguez
Chemical Engineering Department, Universidad de Extremadura, Av. Elvas s/n, 06006 Badajoz, Spain
25 shared publications - Juan L. Acero
Departamento de Ingeniería Química y Química Física, Instituto Universitario de Investigación del Agua, Cambio Climático y Sostenibilidad (IACYS), Universidad de Extremadura, Avenida de Elvas s/n, 06006 Badajoz, Spain
21 shared publications F. Javier Benitez
15 shared publications- José Alcides Peres
Centro de Química de Vila Real (CQVR), Departamento de Química, Universidade de Trás-os-Montes e Alto Douro (UTAD), Quinta de Prados, 5001-801 Vila Real, Portugal
13 shared publications - Teresa González
Chemical Engineering Department, Universidad de Extremadura, Av. Elvas s/n, 06006 Badajoz, Spain
10 shared publications
Latest Publications
- Open Access
- 15 July 2022
- Published by MDPI AG in Biology and Life Sciences Forum
- Vol. 14 (1) , 1
Degradation of Microcystis sp. in Surface Water by Ozone
Due to the gradual increase in the concentration of algae, in general, in continental surface water reservoirs, it is necessary to incorporate advanced technologies in drinking water treatment plants with a view to reduce/eliminate the algae present. This degradation of the algal mass will additionally lead to the destruction of the toxins that could be released into the aqueous medium during the course of potabilisation. In this work, degradation assays of Microcystis sp. in surface water by oxidation processes with ozone have been studied. Ozonation experiments have been carried out in a homogeneous regime (mixture of an aqueous solution with dissolved ozone and surface water) and heterogeneous regime (continuous bubbling of a gaseous current with ozone in surface water). Different aqueous matrices were used for the assays (distilled water, Guadiana river as it passes through Badajoz (Spain), Villar del Rey reservoir (Spain) and a stream that circulates through the campus of the University of Extremadura in Badajoz (Spain)), which were doped with different amounts of a culture of Microcystis sp., provided by the University of Coimbra (Portugal), to achieve the desired initial load of algal mass. The original aqueous matrices were filtered through 0.45 micrometer filters (Millipore). An ozonizer (Sander, model 300.5) was used, capable of generating from pure oxygen a mass flow rate of 6 g/h with an ozone concentration in the gas phase of 1.6% by volume. In the case of the experiments in a heterogeneous regime, the reactor was a cylindrical column 20 cm high and 8 cm in diameter, fitted with a microporous diffuser. To determine the content of algal mass present in the initial sample and in those treated by ozonation, a portable fluorimeter (Aquafluor, Turner) was used, which allows to measure the content of chlorophyll in vivo between 0.3 and 300 µg/L. Ozone analysis in the aqueous phase was performed by the Karman Indigo method and in the gas phase by iodometry. Experiments carried out in homogeneous regime show that in only 5 minutes the chlorophyll content is reduced by 50% for all types of aqueous matrices and for different initial contents of algal mass between 15 and 50 µg/L. For a time of 30 minutes, the conversion is between 80 and 90%, except for the Guadiana river matrix, which is between 70 and 80%. In the case of the heterogeneous regime, ozonation experiments have been carried out by varying the ozone concentration between 4.5 × 10−5 and 5.4 × 10−4 mol/L. It is observed that this variable has a strong positive influence on the degradation of the algae. Thus, for a time of 30 minutes, the degradation is total with the four matrices for the ozone concentration of 5.4 × 10−4 mol/L, while for the concentration of 4.5 × 10−5 mol/L the degradation is between 80 and 90%. A kinetic study has been carried out in both types of ozonation regime. In the case of the homogeneous regime, the model includes both the self-decomposition of ozone in water and the direct reaction of ozone with the algae, and in the case of the heterogeneous regime, the mass transfer of ozone from the gas to the liquid phase is also incorporated. The resolution of the model with the MATLAB software leads to a value of the kinetic degradation constant of the alga between 9 × 10−4 (Villar del Rey reservoir) and 1.4 × 10−3 (distilled water) L/(µg chlorophyll min).
- 15 July 2022
- Published by MDPI AG in Biology and Life Sciences Forum
- Vol. 14 (1) , 1
Open AccessDegradation of Microcystis sp. in Surface Water by Ozone
Due to the gradual increase in the concentration of algae, in general, in continental surface water reservoirs, it is necessary to incorporate advanced technologies in drinking water treatment plants with a view to reduce/eliminate the algae present. This degradation of the algal mass will additionally lead to the destruction of the toxins that could be released into the aqueous medium during the course of potabilisation. In this work, degradation assays of Microcystis sp. in surface water by oxidation processes with ozone have been studied. Ozonation experiments have been carried out in a homogeneous regime (mixture of an aqueous solution with dissolved ozone and surface water) and heterogeneous regime (continuous bubbling of a gaseous current with ozone in surface water). Different aqueous matrices were used for the assays (distilled water, Guadiana river as it passes through Badajoz (Spain), Villar del Rey reservoir (Spain) and a stream that circulates through the campus of the University of Extremadura in Badajoz (Spain)), which were doped with different amounts of a culture of Microcystis sp., provided by the University of Coimbra (Portugal), to achieve the desired initial load of algal mass. The original aqueous matrices were filtered through 0.45 micrometer filters (Millipore). An ozonizer (Sander, model 300.5) was used, capable of generating from pure oxygen a mass flow rate of 6 g/h with an ozone concentration in the gas phase of 1.6% by volume. In the case of the experiments in a heterogeneous regime, the reactor was a cylindrical column 20 cm high and 8 cm in diameter, fitted with a microporous diffuser. To determine the content of algal mass present in the initial sample and in those treated by ozonation, a portable fluorimeter (Aquafluor, Turner) was used, which allows to measure the content of chlorophyll in vivo between 0.3 and 300 µg/L. Ozone analysis in the aqueous phase was performed by the Karman Indigo method and in the gas phase by iodometry. Experiments carried out in homogeneous regime show that in only 5 minutes the chlorophyll content is reduced by 50% for all types of aqueous matrices and for different initial contents of algal mass between 15 and 50 µg/L. For a time of 30 minutes, the conversion is between 80 and 90%, except for the Guadiana river matrix, which is between 70 and 80%. In the case of the heterogeneous regime, ozonation experiments have been carried out by varying the ozone concentration between 4.5 × 10−5 and 5.4 × 10−4 mol/L. It is observed that this variable has a strong positive influence on the degradation of the algae. Thus, for a time of 30 minutes, the degradation is total with the four matrices for the ozone concentration of 5.4 × 10−4 mol/L, while for the concentration of 4.5 × 10−5 mol/L the degradation is between 80 and 90%. A kinetic study has been carried out in both types of ozonation regime. In the case of the homogeneous regime, the model includes both the self-decomposition of ozone in water and the direct reaction of ozone with the algae, and in the case of the heterogeneous regime, the mass transfer of ozone from the gas to the liquid phase is also incorporated. The resolution of the model with the MATLAB software leads to a value of the kinetic degradation constant of the alga between 9 × 10−4 (Villar del Rey reservoir) and 1.4 × 10−3 (distilled water) L/(µg chlorophyll min).
- 1 November 2016
- Published by Taylor & Francis in Phycologia
- Vol. 55 (6) , 688-695
Microalgal removal with natural coagulants
Algal removal capacity via coagulation–flocculation with natural products was investigated in the laboratory using the jar-test technique. Traditional chemical coagulants such as aluminium sulphate...
- 1 November 2016
- Published by Taylor & Francis in Phycologia
- Vol. 55 (6) , 688-695
Microalgal removal with natural coagulants
Algal removal capacity via coagulation–flocculation with natural products was investigated in the laboratory using the jar-test technique. Traditional chemical coagulants such as aluminium sulphate...
- 1 October 2015
- Published by Springer Nature in Journal of Applied Phycology
- Vol. 28 (3) , 1589-1595
Removal of Oocystis algae from freshwater by means of tannin-based coagulant
- 1 October 2015
- Published by Springer Nature in Journal of Applied Phycology
- Vol. 28 (3) , 1589-1595
Removal of Oocystis algae from freshwater by means of tannin-based coagulant
- 1 January 2014
- Published by Elsevier
- p. 203-217
Heavy Metals Uptake from Aqueous Effluents by Novel Adsorbent Derived from Tannin Extracts
- 1 January 2014
- Published by Elsevier
- p. 203-217
Heavy Metals Uptake from Aqueous Effluents by Novel Adsorbent Derived from Tannin Extracts
- Open Access
- 27 November 2013
- Published by Springer Nature in Applied Water Science
- Vol. 4 (3) , 261-271
New lab-made coagulant based on Schinopsis balansae tannin extract: synthesis optimization and preliminary tests on refractory water pollutants
- 27 November 2013
- Published by Springer Nature in Applied Water Science
- Vol. 4 (3) , 261-271
Open AccessNew lab-made coagulant based on Schinopsis balansae tannin extract: synthesis optimization and preliminary tests on refractory water pollutants
- 1 August 2013
- Published by Elsevier in Industrial Crops and Products
- Vol. 49, 507-514
Optimization of tannin rigid foam as adsorbents for wastewater treatment
- 1 August 2013
- Published by Elsevier in Industrial Crops and Products
- Vol. 49, 507-514
Optimization of tannin rigid foam as adsorbents for wastewater treatment
- 1 July 2013
- Published by Elsevier in Chemical Engineering Journal
- Vol. 228, 575-582
Adsorbent tannin foams: New and complementary applications in wastewater treatment
- 1 July 2013
- Published by Elsevier in Chemical Engineering Journal
- Vol. 228, 575-582
Adsorbent tannin foams: New and complementary applications in wastewater treatment
- 4 April 2013
- Published by Springer Nature in Water, Air, & Soil Pollution
- Vol. 224 (5) , 1-12
Advanced Photochemical Degradation of Emerging Pollutants: Methylparaben
- 4 April 2013
- Published by Springer Nature in Water, Air, & Soil Pollution
- Vol. 224 (5) , 1-12
Advanced Photochemical Degradation of Emerging Pollutants: Methylparaben