A comparable study on the hot-water treatment of wheat straw and okra stalk prior to delignification
Wheat straw and okra stalk were studied to evaluate their potential use for integrated lignocellulosic biorefining. Besides chemical pulp, a wide spectrum of value-added by-products were prepared by hot-water extraction of the feedstocks under varying conditions (140 °C for 60 and 240 min and 150 °C...
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Veröffentlicht in: | Biomass conversion and biorefinery 2018-06, Vol.8 (2), p.413-421 |
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description | Wheat straw and okra stalk were studied to evaluate their potential use for integrated lignocellulosic biorefining. Besides chemical pulp, a wide spectrum of value-added by-products were prepared by hot-water extraction of the feedstocks under varying conditions (140 °C for 60 and 240 min and 150 °C for 25 and 100 min) prior to sulfur-free soda-anthraquinone (AQ) pulping (NaOH charge 15 and 20% by weight on o.d. feedstock for wheat straw and okra stalk, respectively, with an AQ charge of 0.05% by weight on o.d. for both feedstocks). During the hot-water pre-treatment, the most significant mass removal, respectively, 12% (
w
/
w
) and 23% (
w
/
w
) of the initial wheat straw and okra stalk was obtained at 150 °C with a treatment time of 100 min. The hydrolysates were characterized in terms of pH and the content of carbohydrates (6–20% (
w
/
w
) of the initial amount), volatile acids (acetic and formic acids), and furans. The pre-treatment stage also facilitated the delignification stage, and, for example, the pulp yields (
w
/
w
), 57% (145 °C, 15 min, and kappa number 18) and 41% (165 °C, 180 min, and kappa number 32) were obtained for the pre-treated (150 °C, P200) wheat straw and okra stalk, respectively. Results clearly indicated that both non-wood materials were suitable for this kind of biorefining approach. |
doi_str_mv | 10.1007/s13399-018-0306-x |
format | Article |
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w
/
w
) and 23% (
w
/
w
) of the initial wheat straw and okra stalk was obtained at 150 °C with a treatment time of 100 min. The hydrolysates were characterized in terms of pH and the content of carbohydrates (6–20% (
w
/
w
) of the initial amount), volatile acids (acetic and formic acids), and furans. The pre-treatment stage also facilitated the delignification stage, and, for example, the pulp yields (
w
/
w
), 57% (145 °C, 15 min, and kappa number 18) and 41% (165 °C, 180 min, and kappa number 32) were obtained for the pre-treated (150 °C, P200) wheat straw and okra stalk, respectively. Results clearly indicated that both non-wood materials were suitable for this kind of biorefining approach.</description><identifier>ISSN: 2190-6815</identifier><identifier>EISSN: 2190-6823</identifier><identifier>DOI: 10.1007/s13399-018-0306-x</identifier><language>eng</language><publisher>Berlin/Heidelberg: Springer Berlin Heidelberg</publisher><subject>Biotechnology ; Carbohydrates ; Energy ; Furans ; Hydrolysates ; Lignocellulose ; Okra ; Organic chemistry ; Original Article ; Pretreatment ; Pulping ; Raw materials ; Refining ; Renewable and Green Energy ; Sodium hydroxide ; Straw ; Water treatment ; Wheat</subject><ispartof>Biomass conversion and biorefinery, 2018-06, Vol.8 (2), p.413-421</ispartof><rights>Springer-Verlag GmbH Germany, part of Springer Nature 2018</rights><rights>Copyright Springer Science & Business Media 2018</rights><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c353t-cbd2061897281275f27a86436971adf693740a0e6ca2cd327deed7371ce0550a3</citedby><cites>FETCH-LOGICAL-c353t-cbd2061897281275f27a86436971adf693740a0e6ca2cd327deed7371ce0550a3</cites><orcidid>0000-0001-9298-2168</orcidid></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktopdf>$$Uhttps://link.springer.com/content/pdf/10.1007/s13399-018-0306-x$$EPDF$$P50$$Gspringer$$H</linktopdf><linktohtml>$$Uhttps://link.springer.com/10.1007/s13399-018-0306-x$$EHTML$$P50$$Gspringer$$H</linktohtml><link.rule.ids>314,776,780,27903,27904,41467,42536,51298</link.rule.ids></links><search><creatorcontrib>Ullah, Saleem</creatorcontrib><creatorcontrib>Pakkanen, Hannu</creatorcontrib><creatorcontrib>Lehto, Joni</creatorcontrib><creatorcontrib>Alén, Raimo</creatorcontrib><title>A comparable study on the hot-water treatment of wheat straw and okra stalk prior to delignification</title><title>Biomass conversion and biorefinery</title><addtitle>Biomass Conv. Bioref</addtitle><description>Wheat straw and okra stalk were studied to evaluate their potential use for integrated lignocellulosic biorefining. Besides chemical pulp, a wide spectrum of value-added by-products were prepared by hot-water extraction of the feedstocks under varying conditions (140 °C for 60 and 240 min and 150 °C for 25 and 100 min) prior to sulfur-free soda-anthraquinone (AQ) pulping (NaOH charge 15 and 20% by weight on o.d. feedstock for wheat straw and okra stalk, respectively, with an AQ charge of 0.05% by weight on o.d. for both feedstocks). During the hot-water pre-treatment, the most significant mass removal, respectively, 12% (
w
/
w
) and 23% (
w
/
w
) of the initial wheat straw and okra stalk was obtained at 150 °C with a treatment time of 100 min. The hydrolysates were characterized in terms of pH and the content of carbohydrates (6–20% (
w
/
w
) of the initial amount), volatile acids (acetic and formic acids), and furans. The pre-treatment stage also facilitated the delignification stage, and, for example, the pulp yields (
w
/
w
), 57% (145 °C, 15 min, and kappa number 18) and 41% (165 °C, 180 min, and kappa number 32) were obtained for the pre-treated (150 °C, P200) wheat straw and okra stalk, respectively. Results clearly indicated that both non-wood materials were suitable for this kind of biorefining approach.</description><subject>Biotechnology</subject><subject>Carbohydrates</subject><subject>Energy</subject><subject>Furans</subject><subject>Hydrolysates</subject><subject>Lignocellulose</subject><subject>Okra</subject><subject>Organic chemistry</subject><subject>Original Article</subject><subject>Pretreatment</subject><subject>Pulping</subject><subject>Raw materials</subject><subject>Refining</subject><subject>Renewable and Green Energy</subject><subject>Sodium hydroxide</subject><subject>Straw</subject><subject>Water treatment</subject><subject>Wheat</subject><issn>2190-6815</issn><issn>2190-6823</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2018</creationdate><recordtype>article</recordtype><recordid>eNp1kE1LAzEQhoMoWGp_gLeA5-gk6W52j6X4BQUveg7TJNtuu93UJKXtvzeyoidPMwPPOzM8hNxyuOcA6iFyKeuaAa8YSCjZ6YKMBK-BlZWQl789L67JJMYNAAipZCVhROyMGr_bY8Bl52hMB3umvqdp7ejaJ3bE5AJNwWHauT5R39DjOg-ZDHik2FvqtwHziN2W7kPrM-2pdV276tumNZha39-Qqwa76CY_dUw-nh7f5y9s8fb8Op8tmJGFTMwsrYCSV7USFReqaITCqpzKslYcbVPWUk0BwZUGhbFSKOucVVJx46AoAOWY3A1798F_HlxMeuMPoc8ntYBsaMqVgkzxgTLBxxhco_PfOwxnzUF_-9SDT5196m-f-pQzYsjEzPYrF_42_x_6AozUeJs</recordid><startdate>20180601</startdate><enddate>20180601</enddate><creator>Ullah, Saleem</creator><creator>Pakkanen, Hannu</creator><creator>Lehto, Joni</creator><creator>Alén, Raimo</creator><general>Springer Berlin Heidelberg</general><general>Springer Nature B.V</general><scope>AAYXX</scope><scope>CITATION</scope><orcidid>https://orcid.org/0000-0001-9298-2168</orcidid></search><sort><creationdate>20180601</creationdate><title>A comparable study on the hot-water treatment of wheat straw and okra stalk prior to delignification</title><author>Ullah, Saleem ; Pakkanen, Hannu ; Lehto, Joni ; Alén, Raimo</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c353t-cbd2061897281275f27a86436971adf693740a0e6ca2cd327deed7371ce0550a3</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2018</creationdate><topic>Biotechnology</topic><topic>Carbohydrates</topic><topic>Energy</topic><topic>Furans</topic><topic>Hydrolysates</topic><topic>Lignocellulose</topic><topic>Okra</topic><topic>Organic chemistry</topic><topic>Original Article</topic><topic>Pretreatment</topic><topic>Pulping</topic><topic>Raw materials</topic><topic>Refining</topic><topic>Renewable and Green Energy</topic><topic>Sodium hydroxide</topic><topic>Straw</topic><topic>Water treatment</topic><topic>Wheat</topic><toplevel>online_resources</toplevel><creatorcontrib>Ullah, Saleem</creatorcontrib><creatorcontrib>Pakkanen, Hannu</creatorcontrib><creatorcontrib>Lehto, Joni</creatorcontrib><creatorcontrib>Alén, Raimo</creatorcontrib><collection>CrossRef</collection><jtitle>Biomass conversion and biorefinery</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Ullah, Saleem</au><au>Pakkanen, Hannu</au><au>Lehto, Joni</au><au>Alén, Raimo</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>A comparable study on the hot-water treatment of wheat straw and okra stalk prior to delignification</atitle><jtitle>Biomass conversion and biorefinery</jtitle><stitle>Biomass Conv. Bioref</stitle><date>2018-06-01</date><risdate>2018</risdate><volume>8</volume><issue>2</issue><spage>413</spage><epage>421</epage><pages>413-421</pages><issn>2190-6815</issn><eissn>2190-6823</eissn><abstract>Wheat straw and okra stalk were studied to evaluate their potential use for integrated lignocellulosic biorefining. Besides chemical pulp, a wide spectrum of value-added by-products were prepared by hot-water extraction of the feedstocks under varying conditions (140 °C for 60 and 240 min and 150 °C for 25 and 100 min) prior to sulfur-free soda-anthraquinone (AQ) pulping (NaOH charge 15 and 20% by weight on o.d. feedstock for wheat straw and okra stalk, respectively, with an AQ charge of 0.05% by weight on o.d. for both feedstocks). During the hot-water pre-treatment, the most significant mass removal, respectively, 12% (
w
/
w
) and 23% (
w
/
w
) of the initial wheat straw and okra stalk was obtained at 150 °C with a treatment time of 100 min. The hydrolysates were characterized in terms of pH and the content of carbohydrates (6–20% (
w
/
w
) of the initial amount), volatile acids (acetic and formic acids), and furans. The pre-treatment stage also facilitated the delignification stage, and, for example, the pulp yields (
w
/
w
), 57% (145 °C, 15 min, and kappa number 18) and 41% (165 °C, 180 min, and kappa number 32) were obtained for the pre-treated (150 °C, P200) wheat straw and okra stalk, respectively. Results clearly indicated that both non-wood materials were suitable for this kind of biorefining approach.</abstract><cop>Berlin/Heidelberg</cop><pub>Springer Berlin Heidelberg</pub><doi>10.1007/s13399-018-0306-x</doi><tpages>9</tpages><orcidid>https://orcid.org/0000-0001-9298-2168</orcidid></addata></record> |
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subjects | Biotechnology Carbohydrates Energy Furans Hydrolysates Lignocellulose Okra Organic chemistry Original Article Pretreatment Pulping Raw materials Refining Renewable and Green Energy Sodium hydroxide Straw Water treatment Wheat |
title | A comparable study on the hot-water treatment of wheat straw and okra stalk prior to delignification |
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