Reduction of hexavalent chromium from electroplating wastewater to trivalent chromium.

Electroplating wastewater contains hexavalent chromium of significant concentration and must not be disposed directly into bodies of water without treatment and meeting the necessary effluent quality standards set by the Department of Environment and Natural Resources (DENR). For Class C fresh water...

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Main Authors: Burdeos, Redelynn R., Lee, Blesmarie G., Santiago, Michelle I.
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Language:English
Published: Animo Repository 2000
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Online Access:https://animorepository.dlsu.edu.ph/etd_bachelors/10230
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Institution: De La Salle University
Language: English
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spelling oai:animorepository.dlsu.edu.ph:etd_bachelors-108752021-08-31T06:54:35Z Reduction of hexavalent chromium from electroplating wastewater to trivalent chromium. Burdeos, Redelynn R. Lee, Blesmarie G. Santiago, Michelle I. Electroplating wastewater contains hexavalent chromium of significant concentration and must not be disposed directly into bodies of water without treatment and meeting the necessary effluent quality standards set by the Department of Environment and Natural Resources (DENR). For Class C fresh water classification, the maximum tolerable amount of hexavalent chromium is 0.5 mg/L. Hexavalent chromium is a toxic chemical and is found to cause lung cancer. The main objective of this study was to economize a treatment process by physical and chemical methods applicable for small-scale electroplating industries (80L per day of wastewater). Sedimentation and filtration methods were used for the physical treatment while the chemical method involved the reduction-oxidation reaction. The treatment scheme of the hexavalent chromium in the wastewater was operated by batch and involved three stages. The first stage was involved the techniques of sedimentation, filtration and dilution techniques. The second stage was the addition of sodium metabisulfite (190.12 g/gmol) which was used as the reducing agent. In this stage, the hexavalent chromium was converted into trivalent chromium. The final stage consisted of addition of calcium hydroxide (74.08 g/gmol) at different pH values ranging from pH 9.2 to aid in the precipitation of the chrone hydroxide. The efficiency of the treatment scheme was determined by the % reduction of the hexavalent chromium by obtaining the analysis of the hexavalent chromium using the colorimetric method. The treatment scheme showed to be effective as indicated by 99.99% reduction of hexavalent chromium. 2000-01-01T08:00:00Z text https://animorepository.dlsu.edu.ph/etd_bachelors/10230 Bachelor's Theses English Animo Repository Electroplating--Waste disposal--Environmental aspects Biochemical and Biomolecular Engineering
institution De La Salle University
building De La Salle University Library
continent Asia
country Philippines
Philippines
content_provider De La Salle University Library
collection DLSU Institutional Repository
language English
topic Electroplating--Waste disposal--Environmental aspects
Biochemical and Biomolecular Engineering
spellingShingle Electroplating--Waste disposal--Environmental aspects
Biochemical and Biomolecular Engineering
Burdeos, Redelynn R.
Lee, Blesmarie G.
Santiago, Michelle I.
Reduction of hexavalent chromium from electroplating wastewater to trivalent chromium.
description Electroplating wastewater contains hexavalent chromium of significant concentration and must not be disposed directly into bodies of water without treatment and meeting the necessary effluent quality standards set by the Department of Environment and Natural Resources (DENR). For Class C fresh water classification, the maximum tolerable amount of hexavalent chromium is 0.5 mg/L. Hexavalent chromium is a toxic chemical and is found to cause lung cancer. The main objective of this study was to economize a treatment process by physical and chemical methods applicable for small-scale electroplating industries (80L per day of wastewater). Sedimentation and filtration methods were used for the physical treatment while the chemical method involved the reduction-oxidation reaction. The treatment scheme of the hexavalent chromium in the wastewater was operated by batch and involved three stages. The first stage was involved the techniques of sedimentation, filtration and dilution techniques. The second stage was the addition of sodium metabisulfite (190.12 g/gmol) which was used as the reducing agent. In this stage, the hexavalent chromium was converted into trivalent chromium. The final stage consisted of addition of calcium hydroxide (74.08 g/gmol) at different pH values ranging from pH 9.2 to aid in the precipitation of the chrone hydroxide. The efficiency of the treatment scheme was determined by the % reduction of the hexavalent chromium by obtaining the analysis of the hexavalent chromium using the colorimetric method. The treatment scheme showed to be effective as indicated by 99.99% reduction of hexavalent chromium.
format text
author Burdeos, Redelynn R.
Lee, Blesmarie G.
Santiago, Michelle I.
author_facet Burdeos, Redelynn R.
Lee, Blesmarie G.
Santiago, Michelle I.
author_sort Burdeos, Redelynn R.
title Reduction of hexavalent chromium from electroplating wastewater to trivalent chromium.
title_short Reduction of hexavalent chromium from electroplating wastewater to trivalent chromium.
title_full Reduction of hexavalent chromium from electroplating wastewater to trivalent chromium.
title_fullStr Reduction of hexavalent chromium from electroplating wastewater to trivalent chromium.
title_full_unstemmed Reduction of hexavalent chromium from electroplating wastewater to trivalent chromium.
title_sort reduction of hexavalent chromium from electroplating wastewater to trivalent chromium.
publisher Animo Repository
publishDate 2000
url https://animorepository.dlsu.edu.ph/etd_bachelors/10230
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