BRPI0701613A - processes and systems for reducing hardwood to alkaline pulp - Google Patents
processes and systems for reducing hardwood to alkaline pulpInfo
- Publication number
- BRPI0701613A BRPI0701613A BRPI0701613-1A BRPI0701613A BRPI0701613A BR PI0701613 A BRPI0701613 A BR PI0701613A BR PI0701613 A BRPI0701613 A BR PI0701613A BR PI0701613 A BRPI0701613 A BR PI0701613A
- Authority
- BR
- Brazil
- Prior art keywords
- lignin
- hardwood
- boil
- boiling
- content
- Prior art date
Links
- 239000011121 hardwood Substances 0.000 title abstract 9
- 238000000034 method Methods 0.000 title abstract 3
- 229920005610 lignin Polymers 0.000 abstract 10
- 238000009835 boiling Methods 0.000 abstract 5
- 239000002002 slurry Substances 0.000 abstract 3
- 230000007423 decrease Effects 0.000 abstract 2
- 239000012530 fluid Substances 0.000 abstract 2
- 239000000463 material Substances 0.000 abstract 2
- 229920002678 cellulose Polymers 0.000 abstract 1
- 239000001913 cellulose Substances 0.000 abstract 1
- 239000000126 substance Substances 0.000 abstract 1
Classifications
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21C—PRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
- D21C3/00—Pulping cellulose-containing materials
- D21C3/02—Pulping cellulose-containing materials with inorganic bases or alkaline reacting compounds, e.g. sulfate processes
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21C—PRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
- D21C3/00—Pulping cellulose-containing materials
- D21C3/02—Pulping cellulose-containing materials with inorganic bases or alkaline reacting compounds, e.g. sulfate processes
- D21C3/022—Pulping cellulose-containing materials with inorganic bases or alkaline reacting compounds, e.g. sulfate processes in presence of S-containing compounds
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21C—PRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
- D21C3/00—Pulping cellulose-containing materials
- D21C3/22—Other features of pulping processes
- D21C3/24—Continuous processes
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21C—PRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
- D21C3/00—Pulping cellulose-containing materials
- D21C3/22—Other features of pulping processes
- D21C3/26—Multistage processes
- D21C3/266—Multistage processes the same pulping agent being used in all stages
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21C—PRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
- D21C1/00—Pretreatment of the finely-divided materials before digesting
- D21C1/06—Pretreatment of the finely-divided materials before digesting with alkaline reacting compounds
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21C—PRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
- D21C3/00—Pulping cellulose-containing materials
- D21C3/22—Other features of pulping processes
- D21C3/222—Use of compounds accelerating the pulping processes
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21C—PRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
- D21C3/00—Pulping cellulose-containing materials
- D21C3/22—Other features of pulping processes
- D21C3/26—Multistage processes
Landscapes
- Chemical & Material Sciences (AREA)
- Inorganic Chemistry (AREA)
- Paper (AREA)
Abstract
PROCESSOS E SISTEMAS PARA REDUZIR PARA POLPA ALCALINA MADEIRAS DE LEI. A presente invenção refere-se a rejeitos de polpa de madeira de lei, a um determinado número capa, que podem ser reduzidos submetendo a polpa de madeira de lei a condições de fervura especificadas no final da fervura. A esse respeito, foi descoberto que g-lignina reage mais rapidamente do que g-lignina e que existe uma proporção mais alta de g-lignina no final de uma fervura de madeira de lei, em comparação com a g-lignina presente no início da fervura. Desse modo, foi descoberto que ao ferver madeiras de lei, condições de fervura relativamente mais severas (por exemplo., temperaturas de fervura mais altas) no final da fervura diminuem o conteúdo de g-lignina, que, por sua vez, diminui a percentagem de rejeitos de polpa, a um determinado número capa. Em modalidades preferidas, métodos e sistemas são postos à disposição para produzir, continuamente, polpa de celulose química de uma pasta fluida fluida de material de madeira de lei triturado, submetendo a pasta fluida fluida de material de madeira de lei triturado a um primeiro estágio de fervura, sob condições suficientes para reduzir o conteúdo de lignina de siringila (s-lignina) no material de madeira de lei, em comparação com o conteúdo de lignina de guaiacila (g-lignina) no mesmo, e, depois, submeter a pasta fluida fluida de material de madeira de lei triturado a um segundo estágio de fervura, sob condições suficientes para reduzir o conteúdo de g-lignina remanescente no mesmo depois do primeiro estágio de fervura.PROCESSES AND SYSTEMS FOR REDUCING ALKALINE PULP WOODS. The present invention relates to hardwood tailings of a certain cap number which can be reduced by subjecting the hardwood to specified boiling conditions at the end of the boil. In this respect, it has been found that g-lignin reacts faster than g-lignin and that there is a higher proportion of g-lignin at the end of a hardwood boil compared to g-lignin present at the beginning of the study. boil. Thus, it has been found that when boiling hardwoods, relatively more severe boiling conditions (eg, higher boiling temperatures) at the end of boiling decrease the g-lignin content, which in turn decreases the percentage. of pulp tailings at a certain cover number. In preferred embodiments, methods and systems are provided for continuously producing chemical cellulose pulp from a milled hardwood fluid slurry by subjecting the milled hardwood fluid slurry to a first stage of crushing. boil under conditions sufficient to reduce the content of syringyl lignin (s-lignin) in the hardwood material compared to the guaiacyl lignin (g-lignin) content in it and then subject the slurry flow of hardwood material ground to a second boil stage, under conditions sufficient to reduce the remaining g-lignin content therein after the first boil stage.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US79143106P | 2006-04-13 | 2006-04-13 | |
US11/709,278 US20070240837A1 (en) | 2006-04-13 | 2007-02-22 | Hardwood alkaline pulping processes and systems |
Publications (1)
Publication Number | Publication Date |
---|---|
BRPI0701613A true BRPI0701613A (en) | 2008-03-11 |
Family
ID=38794811
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
BRPI0701613-1A BRPI0701613A (en) | 2006-04-13 | 2007-04-12 | processes and systems for reducing hardwood to alkaline pulp |
Country Status (14)
Country | Link |
---|---|
US (2) | US20070240837A1 (en) |
JP (1) | JP5101917B2 (en) |
CN (1) | CN101054777B (en) |
AU (1) | AU2007200969B2 (en) |
BR (1) | BRPI0701613A (en) |
CA (1) | CA2581993A1 (en) |
CL (1) | CL2007001000A1 (en) |
ES (1) | ES2319035B1 (en) |
FI (1) | FI20070280A (en) |
PT (1) | PT103701B (en) |
RU (1) | RU2414555C2 (en) |
SE (1) | SE531540C2 (en) |
UY (1) | UY30266A1 (en) |
ZA (1) | ZA200701944B (en) |
Families Citing this family (19)
Publication number | Priority date | Publication date | Assignee | Title |
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CA2640429C (en) * | 2006-01-27 | 2014-04-01 | University Of Massachusetts | Systems and methods for producing biofuels and related materials |
JP5119471B2 (en) * | 2008-02-28 | 2013-01-16 | 王子ホールディングス株式会社 | Method of cooking lignocellulosic material |
SE532932C2 (en) * | 2008-03-20 | 2010-05-11 | Metso Fiber Karlstad Ab | Supply system comprising parallel pumps for a continuous vapor phase boiler without top separator |
BRPI0916598A2 (en) * | 2008-07-28 | 2017-05-30 | Qteros Inc | methods and compositions for increasing product production in microorganisms |
WO2010014631A2 (en) * | 2008-07-28 | 2010-02-04 | University Of Massachusetts | Methods and compositions for improving the production of products in microorganisms |
US7867363B2 (en) * | 2008-08-27 | 2011-01-11 | Metso Fiber Karlstad Ab | Continuous digester system |
US20100086981A1 (en) * | 2009-06-29 | 2010-04-08 | Qteros, Inc. | Compositions and methods for improved saccharification of biomass |
WO2011081658A2 (en) * | 2009-12-15 | 2011-07-07 | Qteros, Inc. | Methods and compositions for producing chemical products from c. phytofermentants |
GB2478791A (en) * | 2010-03-19 | 2011-09-21 | Qteros Inc | Ethanol production by genetically-modified bacteria |
US8951388B2 (en) * | 2011-04-08 | 2015-02-10 | Pec-Tech Engineering And Construction Pte Ltd | Method and system for efficient production of dissolving pulp in a kraft mill producing paper grade pulp with a continuous type digester |
FI127420B (en) * | 2011-06-23 | 2018-05-31 | Andritz Oy | Process for producing cellulose pulp |
AR088750A1 (en) * | 2011-08-30 | 2014-07-02 | Cargill Inc | PULP ELABORATION PROCESSES |
JP5783453B2 (en) * | 2011-09-21 | 2015-09-24 | 川崎化成工業株式会社 | Calculation method of addition effect of anthraquinone compound in pulping. |
CN103410036B (en) * | 2013-08-15 | 2015-11-18 | 齐鲁工业大学 | A kind of production method of high-yield hardwood pulp |
CN103835173B (en) * | 2014-03-17 | 2015-09-16 | 昆明理工大学 | A kind of big dragon bamboo pre-preg diethanol amine-anthraquinone pulping by cooking method |
CN104407098B (en) * | 2014-09-23 | 2016-04-20 | 黄伟洪 | A kind of method of Fast Evaluation birch soda anthraquinone process technique |
CN105568740B (en) * | 2014-10-15 | 2017-12-12 | 亚太森博(山东)浆纸有限公司 | Low whiteness sulfate leaf wood pulpboard of a kind of high intensity and preparation method thereof |
CN105568739B (en) * | 2014-10-15 | 2017-12-12 | 亚太森博(山东)浆纸有限公司 | A kind of unbleached sulfate leaf wood pulpboard and preparation method thereof |
BR112020007605A2 (en) * | 2017-10-17 | 2020-09-29 | Auburn University | phenols as additives in kraft pulping |
Family Cites Families (26)
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US2858211A (en) * | 1956-02-13 | 1958-10-28 | Condi Engineering Corp | Apparatus for wood chip digestion |
SE407244B (en) * | 1976-02-05 | 1979-03-19 | Mo Och Domsjoe Ab | PROCEDURE FOR THE PREPARATION OF CELLULOSA MASSES OF LOVED IN TWO STEPS |
US4436586A (en) * | 1982-01-22 | 1984-03-13 | Kamyr, Inc. | Method of producing kraft pulp using an acid prehydrolysis and pre-extraction |
FI874289A (en) * | 1986-10-02 | 1988-04-03 | Terry James Fullerton | FOERFARANDE FOER FRAMSTAELLNING AV TRAEMASSA. |
US5173153A (en) * | 1991-01-03 | 1992-12-22 | Union Camp Patent Holding, Inc. | Process for enhanced oxygen delignification using high consistency and a split alkali addition |
JP3029043B2 (en) * | 1990-11-22 | 2000-04-04 | 王子製紙株式会社 | Cooking method for lignocellulosic material |
US5326433A (en) * | 1991-02-06 | 1994-07-05 | Ahlstrom Recovery Inc. | Multi-level sulfide content white liquor production and utilization in cellulose pulping |
NO920692L (en) * | 1991-05-24 | 1992-11-25 | Kamyr Inc | TREATMENT OF ORGANIC SULFUR GASES, SPECIFICALLY IN POWER SYSTEMS AND PROCESSES |
US6132556A (en) * | 1993-05-04 | 2000-10-17 | Andritz-Ahlstrom Inc. | Method of controlling pulp digester pressure via liquor extraction |
US5575890A (en) * | 1993-05-04 | 1996-11-19 | Kamyr, Inc. | Method for selectively increasing the sulfide ion concentration and sulfidity of kraft cooking liquor during kraft cooking of wood |
US5536366A (en) * | 1993-05-04 | 1996-07-16 | Ahlstrom Machinery Inc. | Digester system for implementing low dissolved solids profiling |
US5489363A (en) * | 1993-05-04 | 1996-02-06 | Kamyr, Inc. | Pulping with low dissolved solids for improved pulp strength |
US5824188A (en) * | 1993-05-04 | 1998-10-20 | Ahlstrom Machinery Inc. | Method of controlling the pressure of a continuous digester using an extraction-dilution |
US5522958A (en) * | 1994-07-18 | 1996-06-04 | Pulp And Paper Research Institute Of Canada | Two-stage kraft cooking |
US6776876B1 (en) * | 1994-10-13 | 2004-08-17 | Andritz Oy | Method of treating cellulosic pulp to remove hexenuronic acid |
FI102301B (en) * | 1994-10-13 | 1998-11-13 | Andritz Oy | Method for treating cellulosic pulps |
US6248208B1 (en) * | 1995-06-02 | 2001-06-19 | Andritz-Ahlstrom Inc. | Pretreatment of chips before cooking |
US6475338B1 (en) * | 1996-06-05 | 2002-11-05 | Andritz Inc. | Method of minimizing transition metal ions during chemical pulping in a digester by adding chelating agent to the digester |
US5885414A (en) * | 1997-08-18 | 1999-03-23 | Kvaerner Pulping Ab | Method of producing pulp with high alkali cooking in the last cooking stage |
US20010032711A1 (en) * | 1998-10-26 | 2001-10-25 | C. Bertil Stromberg | Pulp cooking with particular alkali profiles |
JP4298058B2 (en) * | 1999-05-28 | 2009-07-15 | 日本製紙株式会社 | Cooking method of lignocellulosic material |
JP4298059B2 (en) * | 1999-05-28 | 2009-07-15 | 日本製紙株式会社 | Cooking method of lignocellulosic material |
CA2318027C (en) * | 1999-09-13 | 2008-07-08 | Andritz-Ahlstrom Inc. | Treating pulp with yield or strength-enhancing additive |
BR0113699A (en) * | 2000-09-05 | 2004-06-08 | Univ Michigan Tech | Methods for simultaneous control of lignin content and composition, and cellulose content in plants |
JP4454822B2 (en) * | 2000-10-11 | 2010-04-21 | 日本製紙株式会社 | Pulp manufacturing method |
CN1542217A (en) * | 2003-11-04 | 2004-11-03 | 季 中 | Method for preparing paper pulp by pharmaceutically catalyzing plant fiber at normal temperature and pressure |
-
2007
- 2007-02-22 US US11/709,278 patent/US20070240837A1/en not_active Abandoned
- 2007-03-06 AU AU2007200969A patent/AU2007200969B2/en not_active Ceased
- 2007-03-06 ZA ZA200701944A patent/ZA200701944B/en unknown
- 2007-03-08 CA CA002581993A patent/CA2581993A1/en not_active Abandoned
- 2007-03-26 PT PT103701A patent/PT103701B/en not_active IP Right Cessation
- 2007-03-28 ES ES200700816A patent/ES2319035B1/en not_active Expired - Fee Related
- 2007-04-02 JP JP2007096441A patent/JP5101917B2/en not_active Expired - Fee Related
- 2007-04-10 CL CL200701000A patent/CL2007001000A1/en unknown
- 2007-04-10 UY UY30266A patent/UY30266A1/en not_active Application Discontinuation
- 2007-04-12 BR BRPI0701613-1A patent/BRPI0701613A/en not_active IP Right Cessation
- 2007-04-12 FI FI20070280A patent/FI20070280A/en not_active Application Discontinuation
- 2007-04-12 RU RU2007113735/12A patent/RU2414555C2/en not_active IP Right Cessation
- 2007-04-12 SE SE0700888A patent/SE531540C2/en not_active IP Right Cessation
- 2007-04-13 CN CN2007100981106A patent/CN101054777B/en not_active Expired - Fee Related
-
2012
- 2012-08-10 US US13/572,403 patent/US20120305209A1/en not_active Abandoned
Also Published As
Publication number | Publication date |
---|---|
UY30266A1 (en) | 2007-11-30 |
JP2007284860A (en) | 2007-11-01 |
FI20070280A (en) | 2007-10-14 |
AU2007200969A1 (en) | 2007-11-01 |
ES2319035B1 (en) | 2010-02-10 |
US20070240837A1 (en) | 2007-10-18 |
RU2414555C2 (en) | 2011-03-20 |
US20120305209A1 (en) | 2012-12-06 |
CL2007001000A1 (en) | 2008-05-30 |
SE531540C2 (en) | 2009-05-12 |
ZA200701944B (en) | 2008-08-27 |
JP5101917B2 (en) | 2012-12-19 |
RU2007113735A (en) | 2008-10-20 |
PT103701B (en) | 2008-01-28 |
CN101054777A (en) | 2007-10-17 |
PT103701A (en) | 2007-10-15 |
FI20070280A0 (en) | 2007-04-12 |
ES2319035A1 (en) | 2009-05-01 |
SE0700888L (en) | 2007-10-14 |
CN101054777B (en) | 2011-05-18 |
CA2581993A1 (en) | 2007-10-13 |
AU2007200969B2 (en) | 2011-11-03 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
B08F | Application dismissed because of non-payment of annual fees [chapter 8.6 patent gazette] | ||
B08K | Patent lapsed as no evidence of payment of the annual fee has been furnished to inpi [chapter 8.11 patent gazette] |