Emission reduction of particulate matter from the combustion of biochar via thermal pre-treatment of torrefaction, slow pyrolysis or hydrothermal carbonisation and its co-combustion with pulverized coal

[Display omitted] •Straw was pretreated via torrefaction, slow pyrolysis and HTC to receive biochar.•Single- and co-firing of straw/biochar and coal were performed to attain PM10.•Thermal pretreatments to straw can highly reduce the ash-based PM1/PM10 emission.•Co-firing of straw/biochar and bitumin...

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Veröffentlicht in:Fuel (Guildford) 2019-03, Vol.240, p.278-288
Hauptverfasser: Wang, Wenyu, Wen, Chang, Li, Changkang, Wang, Meng, Li, Xiaomin, Zhou, Ying, Gong, Xun
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container_end_page 288
container_issue
container_start_page 278
container_title Fuel (Guildford)
container_volume 240
creator Wang, Wenyu
Wen, Chang
Li, Changkang
Wang, Meng
Li, Xiaomin
Zhou, Ying
Gong, Xun
description [Display omitted] •Straw was pretreated via torrefaction, slow pyrolysis and HTC to receive biochar.•Single- and co-firing of straw/biochar and coal were performed to attain PM10.•Thermal pretreatments to straw can highly reduce the ash-based PM1/PM10 emission.•Co-firing of straw/biochar and bituminous coal can obviously reduce PM1 emission.•The emission reduction of PM0.3 is linearly related to the Cl content in biofuels. Emission reduction of PM10 (of an aerodynamic diameter of 10 μm or less) was investigated via the combustion of biochar pre-treated from straw by torrefaction at 300 °C (T-300), slow pyrolysis at 500 °C (S-500), or hydrothermal carbonisation at 240 °C (H-240), and their co-combustion with Ping Ding Shan (PDS) bituminous coal in a drop tube furnace at 1400 °C. The generated PM10 was collected by a Dekati low pressure impactor (DLPI) sample system, and its mass/chemical composition was characterised. During single combustion of the straw and its pre-treated biochar, the emission amount of PM0.3 (aerodynamic diameter of ≤0.3 μm) from the biochar was linearly affected by the release of Cl during various pre-treatments and the formed KCl release into the gas phase during combustion. The emission of PM1-10 still changed linearly, mainly because of the increased ash content after pre-treatment. Co-combustion of biomass fuels and PDS coal presents an obvious reduction in PM10 emission, particularly PM0.3. The higher Cl content in biomass fuels is also linearly correlated with a greater reduction in PM0.3 emission. Aluminosilicates in coal, e.g. kaolinite, are responsible for the capture of gaseous species from biofuels and the subsequent coalescence of sticky minerals, reducing PM0.3 and PM1-10 emissions following co-combustion.
doi_str_mv 10.1016/j.fuel.2018.11.117
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Emission reduction of PM10 (of an aerodynamic diameter of 10 μm or less) was investigated via the combustion of biochar pre-treated from straw by torrefaction at 300 °C (T-300), slow pyrolysis at 500 °C (S-500), or hydrothermal carbonisation at 240 °C (H-240), and their co-combustion with Ping Ding Shan (PDS) bituminous coal in a drop tube furnace at 1400 °C. The generated PM10 was collected by a Dekati low pressure impactor (DLPI) sample system, and its mass/chemical composition was characterised. During single combustion of the straw and its pre-treated biochar, the emission amount of PM0.3 (aerodynamic diameter of ≤0.3 μm) from the biochar was linearly affected by the release of Cl during various pre-treatments and the formed KCl release into the gas phase during combustion. The emission of PM1-10 still changed linearly, mainly because of the increased ash content after pre-treatment. Co-combustion of biomass fuels and PDS coal presents an obvious reduction in PM10 emission, particularly PM0.3. The higher Cl content in biomass fuels is also linearly correlated with a greater reduction in PM0.3 emission. Aluminosilicates in coal, e.g. kaolinite, are responsible for the capture of gaseous species from biofuels and the subsequent coalescence of sticky minerals, reducing PM0.3 and PM1-10 emissions following co-combustion.</description><identifier>ISSN: 0016-2361</identifier><identifier>EISSN: 1873-7153</identifier><identifier>DOI: 10.1016/j.fuel.2018.11.117</identifier><language>eng</language><publisher>Kidlington: Elsevier Ltd</publisher><subject>Aluminosilicates ; Aluminum silicates ; Ash ; Biofuels ; Biomass ; Biomass burning ; Bituminous coal ; Charcoal ; Chemical composition ; Co-combustion ; Coal ; Coalescence ; Coalescing ; Combustion ; Drying ; Emissions ; Emissions control ; Fuels ; Heat treatment ; Histocompatibility antigen H-2 ; Hydrothermal carbonisation ; Kaolinite ; Low pressure ; Minerals ; Organic chemistry ; Particulate emissions ; Particulate matter ; PM10 ; Potassium chloride ; Pretreatment ; Pulverized coal ; Pyrolysis ; Slow pyrolysis ; Straw ; Torrefaction ; Tube furnaces ; Vapor phases</subject><ispartof>Fuel (Guildford), 2019-03, Vol.240, p.278-288</ispartof><rights>2018 Elsevier Ltd</rights><rights>Copyright Elsevier BV Mar 15, 2019</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c365t-71211bd47c235b27c713e1c77442e8e0fe9a2808d7c987f81c330192217a19433</citedby><cites>FETCH-LOGICAL-c365t-71211bd47c235b27c713e1c77442e8e0fe9a2808d7c987f81c330192217a19433</cites><orcidid>0000-0002-8539-8630</orcidid></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://dx.doi.org/10.1016/j.fuel.2018.11.117$$EHTML$$P50$$Gelsevier$$H</linktohtml><link.rule.ids>314,780,784,3550,27924,27925,45995</link.rule.ids></links><search><creatorcontrib>Wang, Wenyu</creatorcontrib><creatorcontrib>Wen, Chang</creatorcontrib><creatorcontrib>Li, Changkang</creatorcontrib><creatorcontrib>Wang, Meng</creatorcontrib><creatorcontrib>Li, Xiaomin</creatorcontrib><creatorcontrib>Zhou, Ying</creatorcontrib><creatorcontrib>Gong, Xun</creatorcontrib><title>Emission reduction of particulate matter from the combustion of biochar via thermal pre-treatment of torrefaction, slow pyrolysis or hydrothermal carbonisation and its co-combustion with pulverized coal</title><title>Fuel (Guildford)</title><description>[Display omitted] •Straw was pretreated via torrefaction, slow pyrolysis and HTC to receive biochar.•Single- and co-firing of straw/biochar and coal were performed to attain PM10.•Thermal pretreatments to straw can highly reduce the ash-based PM1/PM10 emission.•Co-firing of straw/biochar and bituminous coal can obviously reduce PM1 emission.•The emission reduction of PM0.3 is linearly related to the Cl content in biofuels. Emission reduction of PM10 (of an aerodynamic diameter of 10 μm or less) was investigated via the combustion of biochar pre-treated from straw by torrefaction at 300 °C (T-300), slow pyrolysis at 500 °C (S-500), or hydrothermal carbonisation at 240 °C (H-240), and their co-combustion with Ping Ding Shan (PDS) bituminous coal in a drop tube furnace at 1400 °C. The generated PM10 was collected by a Dekati low pressure impactor (DLPI) sample system, and its mass/chemical composition was characterised. During single combustion of the straw and its pre-treated biochar, the emission amount of PM0.3 (aerodynamic diameter of ≤0.3 μm) from the biochar was linearly affected by the release of Cl during various pre-treatments and the formed KCl release into the gas phase during combustion. The emission of PM1-10 still changed linearly, mainly because of the increased ash content after pre-treatment. Co-combustion of biomass fuels and PDS coal presents an obvious reduction in PM10 emission, particularly PM0.3. The higher Cl content in biomass fuels is also linearly correlated with a greater reduction in PM0.3 emission. Aluminosilicates in coal, e.g. kaolinite, are responsible for the capture of gaseous species from biofuels and the subsequent coalescence of sticky minerals, reducing PM0.3 and PM1-10 emissions following co-combustion.</description><subject>Aluminosilicates</subject><subject>Aluminum silicates</subject><subject>Ash</subject><subject>Biofuels</subject><subject>Biomass</subject><subject>Biomass burning</subject><subject>Bituminous coal</subject><subject>Charcoal</subject><subject>Chemical composition</subject><subject>Co-combustion</subject><subject>Coal</subject><subject>Coalescence</subject><subject>Coalescing</subject><subject>Combustion</subject><subject>Drying</subject><subject>Emissions</subject><subject>Emissions control</subject><subject>Fuels</subject><subject>Heat treatment</subject><subject>Histocompatibility antigen H-2</subject><subject>Hydrothermal carbonisation</subject><subject>Kaolinite</subject><subject>Low pressure</subject><subject>Minerals</subject><subject>Organic chemistry</subject><subject>Particulate emissions</subject><subject>Particulate matter</subject><subject>PM10</subject><subject>Potassium chloride</subject><subject>Pretreatment</subject><subject>Pulverized coal</subject><subject>Pyrolysis</subject><subject>Slow pyrolysis</subject><subject>Straw</subject><subject>Torrefaction</subject><subject>Tube furnaces</subject><subject>Vapor phases</subject><issn>0016-2361</issn><issn>1873-7153</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2019</creationdate><recordtype>article</recordtype><recordid>eNp9kcFq3DAQhk1poNs0L9CToNd6o5HslQy9lJC0gUAv7VnI8pjVYlvuSN6wfcQ-VeVsAj0FBiSY759_pL8oPgLfAofd9WHbLzhsBQe9Bcil3hQb0EqWCmr5ttjwTJVC7uBd8T7GA-dc6braFH9vRx-jDxMj7BaX1lvo2WwpebcMNiEbbUpIrKcwsrRH5sLYLvGFbH1we0vs6O3apdEObCYsE6FNI05phVIgwt4-jf_M4hAe2XyiMJyijywQ2586Ci9qZ6kNk4_2ycJOHfMpZtfyP-NHn_ZsXoYjkv-DXe7a4UNx0dsh4tXzeVn8urv9efO9fPjx7f7m60Pp5K5O-UMEQNtVyglZt0I5BRLBKVVVAjXyHhsrNNedco1WvQYnJYdGCFAWmkrKy-LTee5M4feCMZlDWGjKlkaABlU1tWgyJc6UoxBjfr2ZyY-WTga4WTMzB7NmZtbMDEAulUVfziLM-x89konO4-Sw84QumS741-T_AEnXpYk</recordid><startdate>20190315</startdate><enddate>20190315</enddate><creator>Wang, Wenyu</creator><creator>Wen, Chang</creator><creator>Li, Changkang</creator><creator>Wang, Meng</creator><creator>Li, Xiaomin</creator><creator>Zhou, Ying</creator><creator>Gong, Xun</creator><general>Elsevier Ltd</general><general>Elsevier BV</general><scope>AAYXX</scope><scope>CITATION</scope><scope>7QF</scope><scope>7QO</scope><scope>7QQ</scope><scope>7SC</scope><scope>7SE</scope><scope>7SP</scope><scope>7SR</scope><scope>7T7</scope><scope>7TA</scope><scope>7TB</scope><scope>7U5</scope><scope>8BQ</scope><scope>8FD</scope><scope>C1K</scope><scope>F28</scope><scope>FR3</scope><scope>H8D</scope><scope>H8G</scope><scope>JG9</scope><scope>JQ2</scope><scope>KR7</scope><scope>L7M</scope><scope>L~C</scope><scope>L~D</scope><scope>P64</scope><orcidid>https://orcid.org/0000-0002-8539-8630</orcidid></search><sort><creationdate>20190315</creationdate><title>Emission reduction of particulate matter from the combustion of biochar via thermal pre-treatment of torrefaction, slow pyrolysis or hydrothermal carbonisation and its co-combustion with pulverized coal</title><author>Wang, Wenyu ; 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Emission reduction of PM10 (of an aerodynamic diameter of 10 μm or less) was investigated via the combustion of biochar pre-treated from straw by torrefaction at 300 °C (T-300), slow pyrolysis at 500 °C (S-500), or hydrothermal carbonisation at 240 °C (H-240), and their co-combustion with Ping Ding Shan (PDS) bituminous coal in a drop tube furnace at 1400 °C. The generated PM10 was collected by a Dekati low pressure impactor (DLPI) sample system, and its mass/chemical composition was characterised. During single combustion of the straw and its pre-treated biochar, the emission amount of PM0.3 (aerodynamic diameter of ≤0.3 μm) from the biochar was linearly affected by the release of Cl during various pre-treatments and the formed KCl release into the gas phase during combustion. The emission of PM1-10 still changed linearly, mainly because of the increased ash content after pre-treatment. Co-combustion of biomass fuels and PDS coal presents an obvious reduction in PM10 emission, particularly PM0.3. The higher Cl content in biomass fuels is also linearly correlated with a greater reduction in PM0.3 emission. Aluminosilicates in coal, e.g. kaolinite, are responsible for the capture of gaseous species from biofuels and the subsequent coalescence of sticky minerals, reducing PM0.3 and PM1-10 emissions following co-combustion.</abstract><cop>Kidlington</cop><pub>Elsevier Ltd</pub><doi>10.1016/j.fuel.2018.11.117</doi><tpages>11</tpages><orcidid>https://orcid.org/0000-0002-8539-8630</orcidid></addata></record>
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source Elsevier ScienceDirect Journals Complete
subjects Aluminosilicates
Aluminum silicates
Ash
Biofuels
Biomass
Biomass burning
Bituminous coal
Charcoal
Chemical composition
Co-combustion
Coal
Coalescence
Coalescing
Combustion
Drying
Emissions
Emissions control
Fuels
Heat treatment
Histocompatibility antigen H-2
Hydrothermal carbonisation
Kaolinite
Low pressure
Minerals
Organic chemistry
Particulate emissions
Particulate matter
PM10
Potassium chloride
Pretreatment
Pulverized coal
Pyrolysis
Slow pyrolysis
Straw
Torrefaction
Tube furnaces
Vapor phases
title Emission reduction of particulate matter from the combustion of biochar via thermal pre-treatment of torrefaction, slow pyrolysis or hydrothermal carbonisation and its co-combustion with pulverized coal
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