LABORATORY-SCALED SIMULATION OF ACID MINE DRAINAGE TREATMENT USING OPEN LIMESTONE CHANNEL.

One of main environmental issues in mining industry is Acid Mine Drainage (AMD). AMD is characterized as water with high acidity value and elevated metal contents, as a result of oxidation of pyrite in presence of oxygen and water. To ensure that effluent water quality comply with effluent standa...

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Main Author: Nurfasiha
Format: Theses
Language:Indonesia
Online Access:https://digilib.itb.ac.id/gdl/view/78494
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Institution: Institut Teknologi Bandung
Language: Indonesia
id id-itb.:78494
spelling id-itb.:784942023-10-10T08:49:21ZLABORATORY-SCALED SIMULATION OF ACID MINE DRAINAGE TREATMENT USING OPEN LIMESTONE CHANNEL. Nurfasiha Indonesia Theses Acid Mine Drainage, Open Limestone Chanel, Limestone, Surface Area, Retention Time. INSTITUT TEKNOLOGI BANDUNG https://digilib.itb.ac.id/gdl/view/78494 One of main environmental issues in mining industry is Acid Mine Drainage (AMD). AMD is characterized as water with high acidity value and elevated metal contents, as a result of oxidation of pyrite in presence of oxygen and water. To ensure that effluent water quality comply with effluent standard, some AMD treatment means need to be done. One mean of AMD Passive Treatment is open limestone channel (OLC). An OLC is planned and constructed to neutralize AMD by using limestone. To evaluate the neutralizing productivity of an OLD, a laboratory-scaled simulation is made. This simulation is also done to study physical variables that affecting performance of an OLC to neutralize and enhance mine water quality. The study is made by using three different size of limestone (namely coarsegrained, medium-grained and fine-grained). The study shows that with increasing water-flow rate (Q1<Q2<Q3), pH values at the outlet of model with coarsegrained limestone (C50 = 11 mm) are 3,40, 2,93 and 3,22 respectively. pH values at the outlet of model with coarse-grained limestone (C50 = 7,12 mm) are 6,53, 5,72 and 5,99 respectively. pH values at the outlet of model with fine-grained limestone (C50 = 4,05 mm) are 6,51, 6,25 and 6,26 respectively. The results are indicating variables that affecting performance of OLC, i.e. surface area of limestone and retention time. As surface area of limestone increasing, pH value of water at outlet is higher; the longer retention time, the higher pH value of water at the outlet, as a result of increasing reaction between water and limestone. text
institution Institut Teknologi Bandung
building Institut Teknologi Bandung Library
continent Asia
country Indonesia
Indonesia
content_provider Institut Teknologi Bandung
collection Digital ITB
language Indonesia
description One of main environmental issues in mining industry is Acid Mine Drainage (AMD). AMD is characterized as water with high acidity value and elevated metal contents, as a result of oxidation of pyrite in presence of oxygen and water. To ensure that effluent water quality comply with effluent standard, some AMD treatment means need to be done. One mean of AMD Passive Treatment is open limestone channel (OLC). An OLC is planned and constructed to neutralize AMD by using limestone. To evaluate the neutralizing productivity of an OLD, a laboratory-scaled simulation is made. This simulation is also done to study physical variables that affecting performance of an OLC to neutralize and enhance mine water quality. The study is made by using three different size of limestone (namely coarsegrained, medium-grained and fine-grained). The study shows that with increasing water-flow rate (Q1<Q2<Q3), pH values at the outlet of model with coarsegrained limestone (C50 = 11 mm) are 3,40, 2,93 and 3,22 respectively. pH values at the outlet of model with coarse-grained limestone (C50 = 7,12 mm) are 6,53, 5,72 and 5,99 respectively. pH values at the outlet of model with fine-grained limestone (C50 = 4,05 mm) are 6,51, 6,25 and 6,26 respectively. The results are indicating variables that affecting performance of OLC, i.e. surface area of limestone and retention time. As surface area of limestone increasing, pH value of water at outlet is higher; the longer retention time, the higher pH value of water at the outlet, as a result of increasing reaction between water and limestone.
format Theses
author Nurfasiha
spellingShingle Nurfasiha
LABORATORY-SCALED SIMULATION OF ACID MINE DRAINAGE TREATMENT USING OPEN LIMESTONE CHANNEL.
author_facet Nurfasiha
author_sort Nurfasiha
title LABORATORY-SCALED SIMULATION OF ACID MINE DRAINAGE TREATMENT USING OPEN LIMESTONE CHANNEL.
title_short LABORATORY-SCALED SIMULATION OF ACID MINE DRAINAGE TREATMENT USING OPEN LIMESTONE CHANNEL.
title_full LABORATORY-SCALED SIMULATION OF ACID MINE DRAINAGE TREATMENT USING OPEN LIMESTONE CHANNEL.
title_fullStr LABORATORY-SCALED SIMULATION OF ACID MINE DRAINAGE TREATMENT USING OPEN LIMESTONE CHANNEL.
title_full_unstemmed LABORATORY-SCALED SIMULATION OF ACID MINE DRAINAGE TREATMENT USING OPEN LIMESTONE CHANNEL.
title_sort laboratory-scaled simulation of acid mine drainage treatment using open limestone channel.
url https://digilib.itb.ac.id/gdl/view/78494
_version_ 1822008597563834368