Abstract:We evaluated the suitability, contribution to the national economy, and environmental impact of hydrocyclone and Multi-Gravity Separation (MGS) processes using fine-sized coal taken from Downloaded by [The University Of Melbourne Libraries] at 22:43 22 June 2016 2 the Soma coal sludge pond. The lignite coal tailings were treated by a two-stage concentration scheme for the recovery of fine clean coal. Pre-enrichment experiment parameters were determined by Taguchi experimental design method, and the results wer… Show more
“…While the drum is rotating, the centrifugal force from drum rotation affects gravity separation so that coarse particles or high density, high ash content, are spiraled outside and settled on drum surface then slowly swiped up by scrapers to be discharged at the outer end. Meanwhile, the fine or light density particles less affected by centrifugal force, form a flowing film above the heavier seam then is conveyed by the shaking of the drum and continually washing water flow to the lower tilt inner end [ [273] , [274] , [275] ]. MGS was applied for the treatment of ultrafine coal as well as tailing pond deposits [ 276 , 277 ].…”
“…The result showed that drum inclination was determined as a major available on the reduction of ash content and other minor parameters are solid concentration, drum rotation speed, shaking amplitude, wash water rate, and feed rate [ 274 ]. Also, Özbakir et al (2017) proposed a regression model with flow independent inputs (i.e., drum rotation speed, wash water rate, drum inclination, and solid concentration) and two dependent outputs (i.e., ash content and coal yield) variables [ 275 ]. The results showed that ash content and the yield were decreased when lower water flow rate, higher drum rotation speed, higher drum inclination, and solid concentration were used [ 275 ].…”
“…While the drum is rotating, the centrifugal force from drum rotation affects gravity separation so that coarse particles or high density, high ash content, are spiraled outside and settled on drum surface then slowly swiped up by scrapers to be discharged at the outer end. Meanwhile, the fine or light density particles less affected by centrifugal force, form a flowing film above the heavier seam then is conveyed by the shaking of the drum and continually washing water flow to the lower tilt inner end [ [273] , [274] , [275] ]. MGS was applied for the treatment of ultrafine coal as well as tailing pond deposits [ 276 , 277 ].…”
“…The result showed that drum inclination was determined as a major available on the reduction of ash content and other minor parameters are solid concentration, drum rotation speed, shaking amplitude, wash water rate, and feed rate [ 274 ]. Also, Özbakir et al (2017) proposed a regression model with flow independent inputs (i.e., drum rotation speed, wash water rate, drum inclination, and solid concentration) and two dependent outputs (i.e., ash content and coal yield) variables [ 275 ]. The results showed that ash content and the yield were decreased when lower water flow rate, higher drum rotation speed, higher drum inclination, and solid concentration were used [ 275 ].…”
“…As a result, they managed to reduce the ash content from 30.4% to 12%. Özbakir et al (2017) used a combined optimization of hydrocyclone and multi-gravity separation device to remove ash and sulfur from the coal preparation plant tailings [17]. As a result, they managed to reduce the ash content from 54.82% to 24.52%.…”
This study, it is aimed to find out the beneficiation of Malatya-Arguvan lignite by gravity methods. First of all, the washability of lignite has been investigated with sink-float experiments. It has been determined that lignite washability from washing curves is generally difficult but may be possible with controlled washing at a density of 1.68 g /cm 3 . Then, to remove ash and sulfur from lignite by shaking table, spiral and Falcon concentrator tests were conducted. Clean coals are obtained from all other methods except Falcon were found to decrease in ash and sulfur content and increase in calorific value. Clean coals with the lowest ash and sulfur content were obtained with a spiral concentrator. Reichert spiral results showed that the ash content decreased from the lignite of 37.77% to 26.50% and the sulfur content from 3.85% to 2.08%. The calorific value increased from 2576 kcal/kg to 4590 kcal/kg. Arguvan lignite has very limited usage due to its lower calorific value, high ash and sulfur content. Although enrichment has been carried out, it has been concluded that lignite needs to be further improved by using different methods.
“…In order to fully present the capability of the device, the working model needs to be developed. A significant part of the research focused on developing models, be that based on statistical correlations, aerodynamic equations, or computational fluid dynamics (CFD) methods, to fully address the problem of process optimisation and to assess achievable effectiveness of the proposed solutions [36][37][38][39][40].…”
The dry separation methods for coal beneficiation have been regaining attention in the past decades. A number of improved or newly designed devices have been developed—one of them is a negative pressure pneumatic separator (NPPS). The said method of separation is based on the differences in the physical properties between coal and gangue minerals, such as the grain density, size, and shape. The aim of the hereby presented work was to develop working models describing the operation of the NPPS. To validate the models, the calculation results were compared with experimental results of the tests carried out in the previous study on the topic. Based on the findings it can be inferred that the models accurately predict the separation results, i.e., the majority of results are within the range of estimated measurement uncertainties. Consequently, the models allow one to optimise the process to obtain the products with desirable properties.
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