US2662012A - Preparation of straw cellulose - Google Patents
Preparation of straw cellulose Download PDFInfo
- Publication number
- US2662012A US2662012A US151299A US15129950A US2662012A US 2662012 A US2662012 A US 2662012A US 151299 A US151299 A US 151299A US 15129950 A US15129950 A US 15129950A US 2662012 A US2662012 A US 2662012A
- Authority
- US
- United States
- Prior art keywords
- straw
- cellulose
- sodium
- sodium hydroxide
- preparation
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
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
- D21C3/022—Pulping cellulose-containing materials with inorganic bases or alkaline reacting compounds, e.g. sulfate processes in presence of S-containing compounds
Definitions
- fi he present invention relates to the treatment of straw and more particularly to a process for the 11reparation ;oi straw cellulose suitable for -manufacturinghigh gr ade paper.
- lthe wood is digested in an aquleou s alkaline solution containing 20 sodium hydroxide and sodiumsulphide based on the 'weight of thedry wood the quantity of water usedjoeing dependent on the type of apparatus and process einployed generally this quantity of water varies between two and seven times t ee-we t f th 'w 'sl- J E e i 2 lulose isin the neighborhood of 50% of the dry wood; o e er, sarn'e process applied to straw w s bo t 50% 1 th r sa e the paper manufactured frorn this cellulose is of poor quality-in that it liasa l0w tensile strength
- straw is introduced into an aqueous alkaline-solutionanddsdiested therein for --from;-2 to 3 hours, :preferably ior about 2 hoursand 15 minutes.
- *Ihe-temperature of the solution is maintamed between ll5 -C.--and 130 (3., preferably atabout 120? G.
- the total alkaline agents employed are not less than 7% and-not more than 9% "basedon the 'weight'of the dry straw and consist of about 80% sodium hydroxide and about 20% sodium sulphide. These percentage ranges can be satisfied if the sodium hydroxide: varies from 5.6% to 7.2% While thesodium sulphide varies from 124% to 1.8%.
- An'ra t e opti rmrementaa 9 t kaline agents based on the Weight of the art straw are 6.4% sodium hydroxide and 116% so'dium sulphide.
- the straw was digested in an aqueous alkaline solution maintained at different temperatures.
- the straw-liquid ratio was 1:2, and the alkaline solution contained 6.4% sodium hydroxide and 1.6% sodium sulphide, based on the weight of the dry straw.
- the air-dry straw contained moisture and the digesting operation was conducted for two and one-quarter hours. Table I given below confirms the fact that the highest yield of cellulose and the lowest consumption of chlorine was obtained at 120 C..
- the breaking length in km. refers to the length of paper that breaks under its own weight when freely suspended from a support.
- a process for the preparation of straw cellulose suitable for manufacturing paper which comprises digesting the straw for a period of time not more than about 3 hours and not less than about 2 hours in an aqueous solution consisting essentially of sodium hydroxide and sodium sulphide maintained in a temperature range between C. and 130 C. and having a total content of alkaline agents from 7% to 9% based on the weight of the dry straw, said alkaline agents consisting of about 80% sodium hydroxide and about 20% sodium sulphide, the
- a process for the preparation of straw cellu lose suitable for manufacturing paper which comprises digesting the straw for a period of time not more than about 3 hours and not less than about 2 hours in an aqueous alkaline solution maintained at a temperature of about C. and consisting of about 6.4% sodium hydroxide and about 1.6% sodium sulphide, each based on the weight of the dry straw, the straw-liquid ratio being about 1:2.
Landscapes
- Chemical & Material Sciences (AREA)
- Inorganic Chemistry (AREA)
- Paper (AREA)
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| NL2662012X | 1949-07-29 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US2662012A true US2662012A (en) | 1953-12-08 |
Family
ID=19875247
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US151299A Expired - Lifetime US2662012A (en) | 1949-07-29 | 1950-03-22 | Preparation of straw cellulose |
Country Status (3)
| Country | Link |
|---|---|
| US (1) | US2662012A (cs) |
| FR (1) | FR1021964A (cs) |
| NL (1) | NL147891C (cs) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2854334A (en) * | 1954-11-08 | 1958-09-30 | Hawaiian Dev Company Ltd | Rapid kraft pulping process for bagasse and other fibrous, non-woody lignocellulosic plant materials |
| US20110061825A1 (en) * | 2007-12-05 | 2011-03-17 | Shandong Fuyin Paper & Environmental Protection Technology Co., Ltd. | Grass type unbleached paper products and production method thereof |
| US20110297343A1 (en) * | 2008-12-09 | 2011-12-08 | Shandong Fuyin Paper & Enviromental Protection Technology Co., Ltd. | Raw paper and production method and application thereof |
| US20120006501A1 (en) * | 2010-06-25 | 2012-01-12 | Jeff Golfman | Method for Preparing Nonwood Fiber Paper |
Citations (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE313344C (cs) * | 1917-10-20 | |||
| US296935A (en) * | 1884-04-15 | Gael febdinand dahl | ||
| AT40620B (de) * | 1907-08-13 | 1910-01-25 | Erik Wilhelm Tillberg | Verfahren zur Herstellung von Zellulose aus Rinde. |
| US1626171A (en) * | 1926-06-29 | 1927-04-26 | Sidney D Wells | Process for cooking vegetable fiber |
| US1634603A (en) * | 1926-01-12 | 1927-07-05 | Grasselli Chemical Co | Process of making paper from straw and product |
| US1692774A (en) * | 1925-06-18 | 1928-11-20 | Ball Brothers Co | Paper and paper stock and method of producing the same |
| US1816456A (en) * | 1930-04-07 | 1931-07-28 | Zimmerman Max | Method of making straw pulp for straw board |
| US1920239A (en) * | 1931-05-14 | 1933-08-01 | Estape | Process of preparing cellulose |
| US2049567A (en) * | 1934-06-05 | 1936-08-04 | Du Pont | Manufacture of paper pulp |
| US2099400A (en) * | 1936-10-19 | 1937-11-16 | Champagne Paper Corp | Preparation of paper pulp |
| US2161763A (en) * | 1937-10-06 | 1939-06-06 | Champagne Paper Corp | Process of making paper pulp |
| US2482142A (en) * | 1943-10-02 | 1949-09-20 | Gardner H Chidester | Structural material of compressed resin impregnated paper sheets |
-
0
- NL NL147891D patent/NL147891C/xx active
-
1950
- 1950-03-22 US US151299A patent/US2662012A/en not_active Expired - Lifetime
- 1950-07-12 FR FR1021964D patent/FR1021964A/fr not_active Expired
Patent Citations (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US296935A (en) * | 1884-04-15 | Gael febdinand dahl | ||
| AT40620B (de) * | 1907-08-13 | 1910-01-25 | Erik Wilhelm Tillberg | Verfahren zur Herstellung von Zellulose aus Rinde. |
| DE313344C (cs) * | 1917-10-20 | |||
| US1692774A (en) * | 1925-06-18 | 1928-11-20 | Ball Brothers Co | Paper and paper stock and method of producing the same |
| US1634603A (en) * | 1926-01-12 | 1927-07-05 | Grasselli Chemical Co | Process of making paper from straw and product |
| US1626171A (en) * | 1926-06-29 | 1927-04-26 | Sidney D Wells | Process for cooking vegetable fiber |
| US1816456A (en) * | 1930-04-07 | 1931-07-28 | Zimmerman Max | Method of making straw pulp for straw board |
| US1920239A (en) * | 1931-05-14 | 1933-08-01 | Estape | Process of preparing cellulose |
| US2049567A (en) * | 1934-06-05 | 1936-08-04 | Du Pont | Manufacture of paper pulp |
| US2099400A (en) * | 1936-10-19 | 1937-11-16 | Champagne Paper Corp | Preparation of paper pulp |
| US2161763A (en) * | 1937-10-06 | 1939-06-06 | Champagne Paper Corp | Process of making paper pulp |
| US2482142A (en) * | 1943-10-02 | 1949-09-20 | Gardner H Chidester | Structural material of compressed resin impregnated paper sheets |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2854334A (en) * | 1954-11-08 | 1958-09-30 | Hawaiian Dev Company Ltd | Rapid kraft pulping process for bagasse and other fibrous, non-woody lignocellulosic plant materials |
| US20110061825A1 (en) * | 2007-12-05 | 2011-03-17 | Shandong Fuyin Paper & Environmental Protection Technology Co., Ltd. | Grass type unbleached paper products and production method thereof |
| US8303772B2 (en) * | 2007-12-05 | 2012-11-06 | Shangdong Fuyin Paper & Environmental Protection Technology Co., Ltd. | Method for preparing a grass-type unbleached paper product |
| US20110297343A1 (en) * | 2008-12-09 | 2011-12-08 | Shandong Fuyin Paper & Enviromental Protection Technology Co., Ltd. | Raw paper and production method and application thereof |
| US8771465B2 (en) * | 2008-12-09 | 2014-07-08 | Shandong Fuyin Paper & Environmental Protection Technology Co., Ltd | Raw Paper |
| US20120006501A1 (en) * | 2010-06-25 | 2012-01-12 | Jeff Golfman | Method for Preparing Nonwood Fiber Paper |
| US8795469B2 (en) * | 2010-06-25 | 2014-08-05 | Prairie Paper Ventures Inc. | Method for preparing nonwood fiber paper |
Also Published As
| Publication number | Publication date |
|---|---|
| FR1021964A (fr) | 1953-02-26 |
| NL147891C (cs) |
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