Cost Model of Industrial Fluidized Bed Boilers
Fluidized bed combustion in industrial applications offers many advantages from the resource utilization and the air quality points of view. A cash flow model is developed to predict the economic consequences of an investment in an industrial coal-fired atmospheric fluidized bed combustion boiler. T...
Gespeichert in:
| Veröffentlicht in: | J. Sol. Energy Eng.; (United States) 1983-06, Vol.109 (2), p.113-126 |
|---|---|
| Hauptverfasser: | , |
| Format: | Artikel |
| Sprache: | eng |
| Schlagworte: | |
| Online-Zugang: | Volltext |
| Tags: |
Tag hinzufügen
Keine Tags, Fügen Sie den ersten Tag hinzu!
|
| container_end_page | 126 |
|---|---|
| container_issue | 2 |
| container_start_page | 113 |
| container_title | J. Sol. Energy Eng.; (United States) |
| container_volume | 109 |
| creator | Keenan, John D Maguire, Mark |
| description | Fluidized bed combustion in industrial applications offers many advantages from the resource utilization and the air quality points of view. A cash flow model is developed to predict the economic consequences of an investment in an industrial coal-fired atmospheric fluidized bed combustion boiler. The return on investment is calculated for boilers in the range of 50,000 to 500,000 lb hr. The investment costs range from $3.8 to $28.8 million, with calculated returns on investment from 8.4% to 14.2%. These returns are not adequate to justify the investment decision. A sensitivity analysis shows that the most influential variables are the costs of the fossil fuels-the net difference between the displaced natural gas and residual fuel oil vs. the coal used in the fluidized bed boiler. |
| doi_str_mv | 10.1061/(ASCE)0733-9402(1983)109:2(113) |
| format | Article |
| fullrecord | <record><control><sourceid>proquest_osti_</sourceid><recordid>TN_cdi_proquest_miscellaneous_23140503</recordid><sourceformat>XML</sourceformat><sourcesystem>PC</sourcesystem><sourcerecordid>23140503</sourcerecordid><originalsourceid>FETCH-LOGICAL-a407t-b3063e357584ca4a2516b8f4b37d2ba6ad55ff88ea79141ee107e6179344100b3</originalsourceid><addsrcrecordid>eNp9kEFLwzAYhoMoOKf_oXjQ7dD5fU3aNB6EOTedTDyo4C2kbYodXTOb9qC_3sSpRwMfeeF7eEheQs4RJggJXoymT7P5GDiloWAQjVCkdIwgLl1EOt4jAxSMhjwVfJ8M_rhDcmTtGgDSJOUDMpkZ2wUPptB1YMpg2RS97dpK1cGi7qui-tRFcO3HVLVu7TE5KFVt9cnPPSQvi_nz7C5cPd4uZ9NVqBjwLswoJFTTmMcpyxVTUYxJlpYso7yIMpWoIo7LMk214gIZao3AdYJcUMYQIKNDcrrzutdV0uZVp_O33DSNzjsZRxBHInLQ2Q7atua917aTm8rmuq5Vo01vZUSRQQzUgVc7MG-Nta0u5batNqr9kAjSlymlL1P6kqQvSfoy3UZIF9ELXncC5fxybfq2cb-X96v5_Ea4Lh0J_kQ-I_3O-Ov-X_0F87l9UA</addsrcrecordid><sourcetype>Open Access Repository</sourcetype><iscdi>true</iscdi><recordtype>article</recordtype><pqid>23140503</pqid></control><display><type>article</type><title>Cost Model of Industrial Fluidized Bed Boilers</title><source>American Society of Civil Engineers:NESLI2:Journals:2014</source><creator>Keenan, John D ; Maguire, Mark</creator><creatorcontrib>Keenan, John D ; Maguire, Mark ; Dept. of Civil and Urban Engrg., Univ. of Pennsylvania, Philadelphia, PA</creatorcontrib><description>Fluidized bed combustion in industrial applications offers many advantages from the resource utilization and the air quality points of view. A cash flow model is developed to predict the economic consequences of an investment in an industrial coal-fired atmospheric fluidized bed combustion boiler. The return on investment is calculated for boilers in the range of 50,000 to 500,000 lb hr. The investment costs range from $3.8 to $28.8 million, with calculated returns on investment from 8.4% to 14.2%. These returns are not adequate to justify the investment decision. A sensitivity analysis shows that the most influential variables are the costs of the fossil fuels-the net difference between the displaced natural gas and residual fuel oil vs. the coal used in the fluidized bed boiler.</description><identifier>ISSN: 0733-9402</identifier><identifier>EISSN: 1943-7897</identifier><identifier>DOI: 10.1061/(ASCE)0733-9402(1983)109:2(113)</identifier><language>eng</language><publisher>United States: American Society of Civil Engineers</publisher><subject>01 COAL, LIGNITE, AND PEAT ; 014000 - Coal, Lignite, & Peat- Combustion ; BOILERS ; CALCULATION METHODS ; CARBONACEOUS MATERIALS ; CHEMICAL REACTIONS ; COAL ; COMBUSTION ; COST BENEFIT ANALYSIS ; ENERGY SOURCES ; ENVIRONMENTAL EFFECTS ; FLUIDIZED BED BOILERS ; FLUIDIZED-BED COMBUSTION ; FLUIDS ; FOSSIL FUELS ; FUEL GAS ; FUEL OILS ; FUELS ; GAS FUELS ; GASES ; INDUSTRIAL PLANTS ; INVESTMENT ; LIQUID FUELS ; MATERIALS ; NATURAL GAS ; OILS ; ORGANIC COMPOUNDS ; OTHER ORGANIC COMPOUNDS ; OXIDATION ; PETROLEUM PRODUCTS ; PROFITS ; RESIDUAL FUELS ; SENSITIVITY ; TECHNICAL PAPERS ; THERMOCHEMICAL PROCESSES</subject><ispartof>J. Sol. Energy Eng.; (United States), 1983-06, Vol.109 (2), p.113-126</ispartof><rights>Copyright © 1983 ASCE</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-a407t-b3063e357584ca4a2516b8f4b37d2ba6ad55ff88ea79141ee107e6179344100b3</citedby><cites>FETCH-LOGICAL-a407t-b3063e357584ca4a2516b8f4b37d2ba6ad55ff88ea79141ee107e6179344100b3</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktopdf>$$Uhttp://ascelibrary.org/doi/pdf/10.1061/(ASCE)0733-9402(1983)109:2(113)$$EPDF$$P50$$Gasce$$H</linktopdf><linktohtml>$$Uhttp://ascelibrary.org/doi/abs/10.1061/(ASCE)0733-9402(1983)109:2(113)$$EHTML$$P50$$Gasce$$H</linktohtml><link.rule.ids>314,776,780,881,27901,27902,75936,75944</link.rule.ids><backlink>$$Uhttps://www.osti.gov/biblio/5205292$$D View this record in Osti.gov$$Hfree_for_read</backlink></links><search><creatorcontrib>Keenan, John D</creatorcontrib><creatorcontrib>Maguire, Mark</creatorcontrib><creatorcontrib>Dept. of Civil and Urban Engrg., Univ. of Pennsylvania, Philadelphia, PA</creatorcontrib><title>Cost Model of Industrial Fluidized Bed Boilers</title><title>J. Sol. Energy Eng.; (United States)</title><description>Fluidized bed combustion in industrial applications offers many advantages from the resource utilization and the air quality points of view. A cash flow model is developed to predict the economic consequences of an investment in an industrial coal-fired atmospheric fluidized bed combustion boiler. The return on investment is calculated for boilers in the range of 50,000 to 500,000 lb hr. The investment costs range from $3.8 to $28.8 million, with calculated returns on investment from 8.4% to 14.2%. These returns are not adequate to justify the investment decision. A sensitivity analysis shows that the most influential variables are the costs of the fossil fuels-the net difference between the displaced natural gas and residual fuel oil vs. the coal used in the fluidized bed boiler.</description><subject>01 COAL, LIGNITE, AND PEAT</subject><subject>014000 - Coal, Lignite, & Peat- Combustion</subject><subject>BOILERS</subject><subject>CALCULATION METHODS</subject><subject>CARBONACEOUS MATERIALS</subject><subject>CHEMICAL REACTIONS</subject><subject>COAL</subject><subject>COMBUSTION</subject><subject>COST BENEFIT ANALYSIS</subject><subject>ENERGY SOURCES</subject><subject>ENVIRONMENTAL EFFECTS</subject><subject>FLUIDIZED BED BOILERS</subject><subject>FLUIDIZED-BED COMBUSTION</subject><subject>FLUIDS</subject><subject>FOSSIL FUELS</subject><subject>FUEL GAS</subject><subject>FUEL OILS</subject><subject>FUELS</subject><subject>GAS FUELS</subject><subject>GASES</subject><subject>INDUSTRIAL PLANTS</subject><subject>INVESTMENT</subject><subject>LIQUID FUELS</subject><subject>MATERIALS</subject><subject>NATURAL GAS</subject><subject>OILS</subject><subject>ORGANIC COMPOUNDS</subject><subject>OTHER ORGANIC COMPOUNDS</subject><subject>OXIDATION</subject><subject>PETROLEUM PRODUCTS</subject><subject>PROFITS</subject><subject>RESIDUAL FUELS</subject><subject>SENSITIVITY</subject><subject>TECHNICAL PAPERS</subject><subject>THERMOCHEMICAL PROCESSES</subject><issn>0733-9402</issn><issn>1943-7897</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>1983</creationdate><recordtype>article</recordtype><recordid>eNp9kEFLwzAYhoMoOKf_oXjQ7dD5fU3aNB6EOTedTDyo4C2kbYodXTOb9qC_3sSpRwMfeeF7eEheQs4RJggJXoymT7P5GDiloWAQjVCkdIwgLl1EOt4jAxSMhjwVfJ8M_rhDcmTtGgDSJOUDMpkZ2wUPptB1YMpg2RS97dpK1cGi7qui-tRFcO3HVLVu7TE5KFVt9cnPPSQvi_nz7C5cPd4uZ9NVqBjwLswoJFTTmMcpyxVTUYxJlpYso7yIMpWoIo7LMk214gIZao3AdYJcUMYQIKNDcrrzutdV0uZVp_O33DSNzjsZRxBHInLQ2Q7atua917aTm8rmuq5Vo01vZUSRQQzUgVc7MG-Nta0u5batNqr9kAjSlymlL1P6kqQvSfoy3UZIF9ELXncC5fxybfq2cb-X96v5_Ea4Lh0J_kQ-I_3O-Ov-X_0F87l9UA</recordid><startdate>19830601</startdate><enddate>19830601</enddate><creator>Keenan, John D</creator><creator>Maguire, Mark</creator><general>American Society of Civil Engineers</general><scope>AAYXX</scope><scope>CITATION</scope><scope>8FD</scope><scope>FR3</scope><scope>KR7</scope><scope>OTOTI</scope></search><sort><creationdate>19830601</creationdate><title>Cost Model of Industrial Fluidized Bed Boilers</title><author>Keenan, John D ; Maguire, Mark</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-a407t-b3063e357584ca4a2516b8f4b37d2ba6ad55ff88ea79141ee107e6179344100b3</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>1983</creationdate><topic>01 COAL, LIGNITE, AND PEAT</topic><topic>014000 - Coal, Lignite, & Peat- Combustion</topic><topic>BOILERS</topic><topic>CALCULATION METHODS</topic><topic>CARBONACEOUS MATERIALS</topic><topic>CHEMICAL REACTIONS</topic><topic>COAL</topic><topic>COMBUSTION</topic><topic>COST BENEFIT ANALYSIS</topic><topic>ENERGY SOURCES</topic><topic>ENVIRONMENTAL EFFECTS</topic><topic>FLUIDIZED BED BOILERS</topic><topic>FLUIDIZED-BED COMBUSTION</topic><topic>FLUIDS</topic><topic>FOSSIL FUELS</topic><topic>FUEL GAS</topic><topic>FUEL OILS</topic><topic>FUELS</topic><topic>GAS FUELS</topic><topic>GASES</topic><topic>INDUSTRIAL PLANTS</topic><topic>INVESTMENT</topic><topic>LIQUID FUELS</topic><topic>MATERIALS</topic><topic>NATURAL GAS</topic><topic>OILS</topic><topic>ORGANIC COMPOUNDS</topic><topic>OTHER ORGANIC COMPOUNDS</topic><topic>OXIDATION</topic><topic>PETROLEUM PRODUCTS</topic><topic>PROFITS</topic><topic>RESIDUAL FUELS</topic><topic>SENSITIVITY</topic><topic>TECHNICAL PAPERS</topic><topic>THERMOCHEMICAL PROCESSES</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Keenan, John D</creatorcontrib><creatorcontrib>Maguire, Mark</creatorcontrib><creatorcontrib>Dept. of Civil and Urban Engrg., Univ. of Pennsylvania, Philadelphia, PA</creatorcontrib><collection>CrossRef</collection><collection>Technology Research Database</collection><collection>Engineering Research Database</collection><collection>Civil Engineering Abstracts</collection><collection>OSTI.GOV</collection><jtitle>J. Sol. Energy Eng.; (United States)</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Keenan, John D</au><au>Maguire, Mark</au><aucorp>Dept. of Civil and Urban Engrg., Univ. of Pennsylvania, Philadelphia, PA</aucorp><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Cost Model of Industrial Fluidized Bed Boilers</atitle><jtitle>J. Sol. Energy Eng.; (United States)</jtitle><date>1983-06-01</date><risdate>1983</risdate><volume>109</volume><issue>2</issue><spage>113</spage><epage>126</epage><pages>113-126</pages><issn>0733-9402</issn><eissn>1943-7897</eissn><abstract>Fluidized bed combustion in industrial applications offers many advantages from the resource utilization and the air quality points of view. A cash flow model is developed to predict the economic consequences of an investment in an industrial coal-fired atmospheric fluidized bed combustion boiler. The return on investment is calculated for boilers in the range of 50,000 to 500,000 lb hr. The investment costs range from $3.8 to $28.8 million, with calculated returns on investment from 8.4% to 14.2%. These returns are not adequate to justify the investment decision. A sensitivity analysis shows that the most influential variables are the costs of the fossil fuels-the net difference between the displaced natural gas and residual fuel oil vs. the coal used in the fluidized bed boiler.</abstract><cop>United States</cop><pub>American Society of Civil Engineers</pub><doi>10.1061/(ASCE)0733-9402(1983)109:2(113)</doi><tpages>14</tpages></addata></record> |
| fulltext | fulltext |
| identifier | ISSN: 0733-9402 |
| ispartof | J. Sol. Energy Eng.; (United States), 1983-06, Vol.109 (2), p.113-126 |
| issn | 0733-9402 1943-7897 |
| language | eng |
| recordid | cdi_proquest_miscellaneous_23140503 |
| source | American Society of Civil Engineers:NESLI2:Journals:2014 |
| subjects | 01 COAL, LIGNITE, AND PEAT 014000 - Coal, Lignite, & Peat- Combustion BOILERS CALCULATION METHODS CARBONACEOUS MATERIALS CHEMICAL REACTIONS COAL COMBUSTION COST BENEFIT ANALYSIS ENERGY SOURCES ENVIRONMENTAL EFFECTS FLUIDIZED BED BOILERS FLUIDIZED-BED COMBUSTION FLUIDS FOSSIL FUELS FUEL GAS FUEL OILS FUELS GAS FUELS GASES INDUSTRIAL PLANTS INVESTMENT LIQUID FUELS MATERIALS NATURAL GAS OILS ORGANIC COMPOUNDS OTHER ORGANIC COMPOUNDS OXIDATION PETROLEUM PRODUCTS PROFITS RESIDUAL FUELS SENSITIVITY TECHNICAL PAPERS THERMOCHEMICAL PROCESSES |
| title | Cost Model of Industrial Fluidized Bed Boilers |
| url | https://sfx.bib-bvb.de/sfx_tum?ctx_ver=Z39.88-2004&ctx_enc=info:ofi/enc:UTF-8&ctx_tim=2025-02-01T02%3A09%3A49IST&url_ver=Z39.88-2004&url_ctx_fmt=infofi/fmt:kev:mtx:ctx&rfr_id=info:sid/primo.exlibrisgroup.com:primo3-Article-proquest_osti_&rft_val_fmt=info:ofi/fmt:kev:mtx:journal&rft.genre=article&rft.atitle=Cost%20Model%20of%20Industrial%20Fluidized%20Bed%20Boilers&rft.jtitle=J.%20Sol.%20Energy%20Eng.;%20(United%20States)&rft.au=Keenan,%20John%20D&rft.aucorp=Dept.%20of%20Civil%20and%20Urban%20Engrg.,%20Univ.%20of%20Pennsylvania,%20Philadelphia,%20PA&rft.date=1983-06-01&rft.volume=109&rft.issue=2&rft.spage=113&rft.epage=126&rft.pages=113-126&rft.issn=0733-9402&rft.eissn=1943-7897&rft_id=info:doi/10.1061/(ASCE)0733-9402(1983)109:2(113)&rft_dat=%3Cproquest_osti_%3E23140503%3C/proquest_osti_%3E%3Curl%3E%3C/url%3E&disable_directlink=true&sfx.directlink=off&sfx.report_link=0&rft_id=info:oai/&rft_pqid=23140503&rft_id=info:pmid/&rfr_iscdi=true |