Selective removal of sodium and calcium from low-rank coal

Process integration, simulation and experimental investigation

Song Zhou, Tahereh Hosseini, Xiwang Zhang, Nawshad Haque, Lian Zhang

Research output: Chapter in Book/Report/Conference proceedingConference PaperResearchpeer-review

Abstract

This paper addresses the selective removal of sodium and calcium from low-rank sub-bituminous coal, thereby improving fusion temperatures of ash to reduce its slagging and fouling propensity in the pulverised coal-fired boilers. Process simulation has been conducted based on the lab-scale experimental results. Three potential low-rank coal demineralisation processes have been simulated, a single-stage water washing process incorporating evaporator to recycle the waste water, a three-stage counter-current water washing process combined with an evaporator for water recovery, and a three-stage water washing process using reverse osmosis to demineralise the recycling water. The washing experiments were implemented to determine the optimum leaching conditions. Optimum condition was found to be residence time of 30 minutes; particle size of 1-4 mm and a liquid to solid mass ratio of 1.25. The process simulation was conducted using Aspen Plus. The simulation result sindicated that, the total removal extent of sodium increased stably with the increase in the recycle number. In contrast, the mobilisation of calcium was marginal and was mainly achieved in the first stage, which can be attributed to the low solubility of CaSO4 and organic calcium in water. For three-stage counter-current water washing, a total of 60% of sodium and 0.7% of calcium were removed, resulting in a significant reduction in ash content and increase in its fusion temperatures. Additionally, low-rank coal washing processes could produce maximum 0.14 t water/t raw coal, due to the high moisture content in the parent coal, making it economically viable. However, such a conclusion needs to be further validated via pilot-scale demonstration experiments. In particular, the water recovery from low-rank coal-water slurry through the use of the industry-scale centrifugal needs to be confirmed.
Original languageEnglish
Title of host publicationChemeca 2016
Subtitle of host publicationChemical Engineering - Regeneration, Recovery and Reinvention
Place of PublicationMelbourne, VIC
PublisherEngineers Australia
Pages849-858
Number of pages10
ISBN (Print)9781922107831
Publication statusPublished - 2016
EventChemeca: Australasian Conference on Chemical Engineering 2016: Chemical Engineering - Regeneration, Recovery and Reinvention - Adelaide, Australia
Duration: 25 Nov 201628 Nov 2016

Conference

ConferenceChemeca: Australasian Conference on Chemical Engineering 2016
CountryAustralia
CityAdelaide
Period25/11/1628/11/16

Keywords

  • Experimental study
  • Low-rank washing
  • Process integration and simulation
  • Sodium and calcium removal

Cite this

Zhou, S., Hosseini, T., Zhang, X., Haque, N., & Zhang, L. (2016). Selective removal of sodium and calcium from low-rank coal: Process integration, simulation and experimental investigation. In Chemeca 2016: Chemical Engineering - Regeneration, Recovery and Reinvention (pp. 849-858). [3405679] Melbourne, VIC: Engineers Australia.
Zhou, Song ; Hosseini, Tahereh ; Zhang, Xiwang ; Haque, Nawshad ; Zhang, Lian. / Selective removal of sodium and calcium from low-rank coal : Process integration, simulation and experimental investigation. Chemeca 2016: Chemical Engineering - Regeneration, Recovery and Reinvention. Melbourne, VIC : Engineers Australia, 2016. pp. 849-858
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title = "Selective removal of sodium and calcium from low-rank coal: Process integration, simulation and experimental investigation",
abstract = "This paper addresses the selective removal of sodium and calcium from low-rank sub-bituminous coal, thereby improving fusion temperatures of ash to reduce its slagging and fouling propensity in the pulverised coal-fired boilers. Process simulation has been conducted based on the lab-scale experimental results. Three potential low-rank coal demineralisation processes have been simulated, a single-stage water washing process incorporating evaporator to recycle the waste water, a three-stage counter-current water washing process combined with an evaporator for water recovery, and a three-stage water washing process using reverse osmosis to demineralise the recycling water. The washing experiments were implemented to determine the optimum leaching conditions. Optimum condition was found to be residence time of 30 minutes; particle size of 1-4 mm and a liquid to solid mass ratio of 1.25. The process simulation was conducted using Aspen Plus. The simulation result sindicated that, the total removal extent of sodium increased stably with the increase in the recycle number. In contrast, the mobilisation of calcium was marginal and was mainly achieved in the first stage, which can be attributed to the low solubility of CaSO4 and organic calcium in water. For three-stage counter-current water washing, a total of 60{\%} of sodium and 0.7{\%} of calcium were removed, resulting in a significant reduction in ash content and increase in its fusion temperatures. Additionally, low-rank coal washing processes could produce maximum 0.14 t water/t raw coal, due to the high moisture content in the parent coal, making it economically viable. However, such a conclusion needs to be further validated via pilot-scale demonstration experiments. In particular, the water recovery from low-rank coal-water slurry through the use of the industry-scale centrifugal needs to be confirmed.",
keywords = "Experimental study, Low-rank washing, Process integration and simulation, Sodium and calcium removal",
author = "Song Zhou and Tahereh Hosseini and Xiwang Zhang and Nawshad Haque and Lian Zhang",
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Zhou, S, Hosseini, T, Zhang, X, Haque, N & Zhang, L 2016, Selective removal of sodium and calcium from low-rank coal: Process integration, simulation and experimental investigation. in Chemeca 2016: Chemical Engineering - Regeneration, Recovery and Reinvention., 3405679, Engineers Australia, Melbourne, VIC, pp. 849-858, Chemeca: Australasian Conference on Chemical Engineering 2016, Adelaide, Australia, 25/11/16.

Selective removal of sodium and calcium from low-rank coal : Process integration, simulation and experimental investigation. / Zhou, Song; Hosseini, Tahereh; Zhang, Xiwang; Haque, Nawshad; Zhang, Lian.

Chemeca 2016: Chemical Engineering - Regeneration, Recovery and Reinvention. Melbourne, VIC : Engineers Australia, 2016. p. 849-858 3405679.

Research output: Chapter in Book/Report/Conference proceedingConference PaperResearchpeer-review

TY - GEN

T1 - Selective removal of sodium and calcium from low-rank coal

T2 - Process integration, simulation and experimental investigation

AU - Zhou, Song

AU - Hosseini, Tahereh

AU - Zhang, Xiwang

AU - Haque, Nawshad

AU - Zhang, Lian

PY - 2016

Y1 - 2016

N2 - This paper addresses the selective removal of sodium and calcium from low-rank sub-bituminous coal, thereby improving fusion temperatures of ash to reduce its slagging and fouling propensity in the pulverised coal-fired boilers. Process simulation has been conducted based on the lab-scale experimental results. Three potential low-rank coal demineralisation processes have been simulated, a single-stage water washing process incorporating evaporator to recycle the waste water, a three-stage counter-current water washing process combined with an evaporator for water recovery, and a three-stage water washing process using reverse osmosis to demineralise the recycling water. The washing experiments were implemented to determine the optimum leaching conditions. Optimum condition was found to be residence time of 30 minutes; particle size of 1-4 mm and a liquid to solid mass ratio of 1.25. The process simulation was conducted using Aspen Plus. The simulation result sindicated that, the total removal extent of sodium increased stably with the increase in the recycle number. In contrast, the mobilisation of calcium was marginal and was mainly achieved in the first stage, which can be attributed to the low solubility of CaSO4 and organic calcium in water. For three-stage counter-current water washing, a total of 60% of sodium and 0.7% of calcium were removed, resulting in a significant reduction in ash content and increase in its fusion temperatures. Additionally, low-rank coal washing processes could produce maximum 0.14 t water/t raw coal, due to the high moisture content in the parent coal, making it economically viable. However, such a conclusion needs to be further validated via pilot-scale demonstration experiments. In particular, the water recovery from low-rank coal-water slurry through the use of the industry-scale centrifugal needs to be confirmed.

AB - This paper addresses the selective removal of sodium and calcium from low-rank sub-bituminous coal, thereby improving fusion temperatures of ash to reduce its slagging and fouling propensity in the pulverised coal-fired boilers. Process simulation has been conducted based on the lab-scale experimental results. Three potential low-rank coal demineralisation processes have been simulated, a single-stage water washing process incorporating evaporator to recycle the waste water, a three-stage counter-current water washing process combined with an evaporator for water recovery, and a three-stage water washing process using reverse osmosis to demineralise the recycling water. The washing experiments were implemented to determine the optimum leaching conditions. Optimum condition was found to be residence time of 30 minutes; particle size of 1-4 mm and a liquid to solid mass ratio of 1.25. The process simulation was conducted using Aspen Plus. The simulation result sindicated that, the total removal extent of sodium increased stably with the increase in the recycle number. In contrast, the mobilisation of calcium was marginal and was mainly achieved in the first stage, which can be attributed to the low solubility of CaSO4 and organic calcium in water. For three-stage counter-current water washing, a total of 60% of sodium and 0.7% of calcium were removed, resulting in a significant reduction in ash content and increase in its fusion temperatures. Additionally, low-rank coal washing processes could produce maximum 0.14 t water/t raw coal, due to the high moisture content in the parent coal, making it economically viable. However, such a conclusion needs to be further validated via pilot-scale demonstration experiments. In particular, the water recovery from low-rank coal-water slurry through the use of the industry-scale centrifugal needs to be confirmed.

KW - Experimental study

KW - Low-rank washing

KW - Process integration and simulation

KW - Sodium and calcium removal

UR - http://www.chemeca2016.org/

M3 - Conference Paper

SN - 9781922107831

SP - 849

EP - 858

BT - Chemeca 2016

PB - Engineers Australia

CY - Melbourne, VIC

ER -

Zhou S, Hosseini T, Zhang X, Haque N, Zhang L. Selective removal of sodium and calcium from low-rank coal: Process integration, simulation and experimental investigation. In Chemeca 2016: Chemical Engineering - Regeneration, Recovery and Reinvention. Melbourne, VIC: Engineers Australia. 2016. p. 849-858. 3405679