US3887426A - Process for producing cellulose pulp by digestion with a diol or triol solvent and an aniline or phenol salt - Google Patents
Process for producing cellulose pulp by digestion with a diol or triol solvent and an aniline or phenol salt Download PDFInfo
- Publication number
- US3887426A US3887426A US341508A US34150873A US3887426A US 3887426 A US3887426 A US 3887426A US 341508 A US341508 A US 341508A US 34150873 A US34150873 A US 34150873A US 3887426 A US3887426 A US 3887426A
- Authority
- US
- United States
- Prior art keywords
- solution
- digester
- lignin
- solvent
- cellulose pulp
- 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
Images
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
- D21C3/20—Pulping cellulose-containing materials with organic solvents or in solvent environment
Definitions
- the digestion produces no malodorous effluent gases, and therefore is no atmospheric polution.
- monohydroxyl alcohols such as octyl alcohol and lauric alcohol glycerol which is a saturated aliphatic triol ethylene glycol which is a saturated aliphatic diol anisole benzyl alcohol diphenyl diphenyl oxide ethers and esters with melting points below 100C, or mixtures of these solvents.
- reaction temperature is of the order of 160 to 190C.
- the digestion products are removed from the reactor through a pipe 4 and filtered on a continuous filter 5.
- the filtrate contains alkaline lignin in solution in glycol. This solution is fed through a pipe 6 into a mixer 17.
- the cellulose pulp collected on the filter 5 is washed by a counter-current stream of water arriving through a pipe 18.
- the effluent wash waters from the filter 5 are conveyed through a pipe 7 into a distillation column 8.
- the head fraction from the column 8 is condensed, by means not shown, the resulting condensed water being recycled for washing the cellulose pulp, further water for washing arriving through the pipe 18 in the form of all or part of the water condensed in the condenser 3.
- the condensate passes into a phase separator 37, which splits the condensate into two liquids, a supernatant phase, which consists of phenol, which is a byproduct of the reaction, and a subjacent liquid phase which consists of water.
- the water flows out of the phase separator through a pipe 38.
- Phenol-containing vapors produced during the digestion pass from the top of the digester into line 73, provided with valve 74, and thus to the heat exchanger 62.
- the cellulose pulp After the cellulose pulp has been washed on the screen 51 in the digester 50, it is removed through an outlet 79, after which it can be bleached in the known way.
- the digester 50 is now empty and can be used for digesting a further batch of wood chips. During the digestion of this further batch in the digester 50, the cellulose pulp is being washed in the digester 50, and so on, the cycles being repeated.
- FIG. 3 shows only two digesters 50, 50', the system can of course if desired contain more than two digesters. The same quantity of reagent, organic solvent and wash water is reused again and again, apart from inevitable losses.
- the yield was 3.6 g of crude cellulose pulp.
- the solution is drained out of the digester, the cellulose pulp is washed in the digester, from which it is then removed, the lignin in the solvent is precipitated as calcium lignate, which is removed from the solvent and washed, the lignin in the wash waters is also precipitated and recovered as calcium lignate, the purified wash waters are distilled, giving distilled water and a tail fraction, which is combined with the recovered solvent, the wash waters before distillation passing through the heat exchanger for cooling the solution in the digester during the digestion.
Landscapes
- Paper (AREA)
Priority Applications (10)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
BE756225D BE756225A (fr) | 1969-09-26 | Procede de fabrication de pate cellulosique | |
CH1452269A CH498244A (fr) | 1969-09-26 | 1969-09-26 | Procédé de fabrication de pâte cellulosique |
CH1819769A CH512635A (fr) | 1969-09-26 | 1969-12-05 | Procédé de fabrication de pâte cellulosique |
AT840870A AT300544B (de) | 1969-09-26 | 1970-09-17 | Verfahren zur Herstellung von Cellulosepulpe |
LU61717D LU61717A1 (fr) | 1969-09-26 | 1970-09-18 | |
CA093,735A CA977505A (en) | 1969-09-26 | 1970-09-22 | Process for producing cellulose pulp |
DE19702046944 DE2046944A1 (de) | 1969-09-26 | 1970-09-23 | Verfahren zur Herstellung von Cellulosepulpe |
FR707034610A FR2063171B1 (fr) | 1969-09-26 | 1970-09-24 | |
GB4588170A GB1328674A (en) | 1969-09-26 | 1970-09-25 | Manufacture of cellulose pulp |
US341508A US3887426A (en) | 1969-09-26 | 1973-03-15 | Process for producing cellulose pulp by digestion with a diol or triol solvent and an aniline or phenol salt |
Applications Claiming Priority (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CH1452269A CH498244A (fr) | 1969-09-26 | 1969-09-26 | Procédé de fabrication de pâte cellulosique |
CH1819769A CH512635A (fr) | 1969-09-26 | 1969-12-05 | Procédé de fabrication de pâte cellulosique |
US7467170A | 1970-09-23 | 1970-09-23 | |
US341508A US3887426A (en) | 1969-09-26 | 1973-03-15 | Process for producing cellulose pulp by digestion with a diol or triol solvent and an aniline or phenol salt |
Related Parent Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US7467170A Continuation | 1969-09-26 | 1970-09-23 |
Related Child Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US56022975A Continuation | 1969-09-26 | 1975-03-20 |
Publications (1)
Publication Number | Publication Date |
---|---|
US3887426A true US3887426A (en) | 1975-06-03 |
Family
ID=27429570
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US341508A Expired - Lifetime US3887426A (en) | 1969-09-26 | 1973-03-15 | Process for producing cellulose pulp by digestion with a diol or triol solvent and an aniline or phenol salt |
Country Status (9)
Country | Link |
---|---|
US (1) | US3887426A (fr) |
AT (1) | AT300544B (fr) |
BE (1) | BE756225A (fr) |
CA (1) | CA977505A (fr) |
CH (2) | CH498244A (fr) |
DE (1) | DE2046944A1 (fr) |
FR (1) | FR2063171B1 (fr) |
GB (1) | GB1328674A (fr) |
LU (1) | LU61717A1 (fr) |
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4017642A (en) * | 1975-07-28 | 1977-04-12 | George O. Orth | Process of making food for ruminant animals from wood and/or woody products |
US4100016A (en) * | 1975-10-24 | 1978-07-11 | C P Associates Limited | Solvent pulping process |
US4135967A (en) * | 1969-09-26 | 1979-01-23 | Societe Generale De Brevets Industriels Et Ohimiques | Process for producing cellulose pulp by solid phase digestion |
EP0041401A1 (fr) * | 1980-06-02 | 1981-12-09 | The Board Of Regents Of The University Of Washington | Méthode et mixture pour la production de pâtes cellulosiques |
US4594130A (en) * | 1978-11-27 | 1986-06-10 | Chang Pei Ching | Pulping of lignocellulose with aqueous alcohol and alkaline earth metal salt catalyst |
EP0763622A3 (fr) * | 1990-08-17 | 1999-08-25 | Alcell Technologies Inc. | Procédé et appareil pour la mise en pâte en continu en milieu solvant et le lavage |
US20190136448A1 (en) * | 2017-11-08 | 2019-05-09 | Earthrecycle Co., Ltd. | Method for Separating Cellulose |
US20210230375A1 (en) * | 2018-11-07 | 2021-07-29 | Earthrecycle Co., Ltd. | Method for separating cellulose |
Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1902916A (en) * | 1929-06-07 | 1933-03-28 | Firm Dr Otto C Strecker | Process for decomposing plant fiber material by cooking with phenolates |
US2022654A (en) * | 1933-03-07 | 1935-12-03 | Dreyfus Henry | Treatment of cellulosic materials |
US2772968A (en) * | 1951-06-06 | 1956-12-04 | Research Corp | Process of pulping cellulosic materials with triethylene glycol |
US2886483A (en) * | 1953-05-27 | 1959-05-12 | Rosenblads Patenter Ab | Heating system for cellulose digestion plants |
US3255071A (en) * | 1963-10-25 | 1966-06-07 | Theodor N Kleinert | Process for production of alkali cellulose in the absence of an aqueous liquid phase |
US3305432A (en) * | 1963-07-15 | 1967-02-21 | William R Matthews | Making of cellulose pulp |
US3408268A (en) * | 1966-10-27 | 1968-10-29 | Jefferson Chem Co Inc | Recovery of spent glycol by distillation in the presence of water |
US3428520A (en) * | 1965-08-12 | 1969-02-18 | Scott Paper Co | Pulping process with lignin recovery |
-
0
- BE BE756225D patent/BE756225A/fr unknown
-
1969
- 1969-09-26 CH CH1452269A patent/CH498244A/fr not_active IP Right Cessation
- 1969-12-05 CH CH1819769A patent/CH512635A/fr unknown
-
1970
- 1970-09-17 AT AT840870A patent/AT300544B/de not_active IP Right Cessation
- 1970-09-18 LU LU61717D patent/LU61717A1/xx unknown
- 1970-09-22 CA CA093,735A patent/CA977505A/en not_active Expired
- 1970-09-23 DE DE19702046944 patent/DE2046944A1/de active Pending
- 1970-09-24 FR FR707034610A patent/FR2063171B1/fr not_active Expired
- 1970-09-25 GB GB4588170A patent/GB1328674A/en not_active Expired
-
1973
- 1973-03-15 US US341508A patent/US3887426A/en not_active Expired - Lifetime
Patent Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1902916A (en) * | 1929-06-07 | 1933-03-28 | Firm Dr Otto C Strecker | Process for decomposing plant fiber material by cooking with phenolates |
US2022654A (en) * | 1933-03-07 | 1935-12-03 | Dreyfus Henry | Treatment of cellulosic materials |
US2772968A (en) * | 1951-06-06 | 1956-12-04 | Research Corp | Process of pulping cellulosic materials with triethylene glycol |
US2886483A (en) * | 1953-05-27 | 1959-05-12 | Rosenblads Patenter Ab | Heating system for cellulose digestion plants |
US3305432A (en) * | 1963-07-15 | 1967-02-21 | William R Matthews | Making of cellulose pulp |
US3255071A (en) * | 1963-10-25 | 1966-06-07 | Theodor N Kleinert | Process for production of alkali cellulose in the absence of an aqueous liquid phase |
US3428520A (en) * | 1965-08-12 | 1969-02-18 | Scott Paper Co | Pulping process with lignin recovery |
US3408268A (en) * | 1966-10-27 | 1968-10-29 | Jefferson Chem Co Inc | Recovery of spent glycol by distillation in the presence of water |
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4135967A (en) * | 1969-09-26 | 1979-01-23 | Societe Generale De Brevets Industriels Et Ohimiques | Process for producing cellulose pulp by solid phase digestion |
US4017642A (en) * | 1975-07-28 | 1977-04-12 | George O. Orth | Process of making food for ruminant animals from wood and/or woody products |
US4100016A (en) * | 1975-10-24 | 1978-07-11 | C P Associates Limited | Solvent pulping process |
US4594130A (en) * | 1978-11-27 | 1986-06-10 | Chang Pei Ching | Pulping of lignocellulose with aqueous alcohol and alkaline earth metal salt catalyst |
EP0041401A1 (fr) * | 1980-06-02 | 1981-12-09 | The Board Of Regents Of The University Of Washington | Méthode et mixture pour la production de pâtes cellulosiques |
EP0763622A3 (fr) * | 1990-08-17 | 1999-08-25 | Alcell Technologies Inc. | Procédé et appareil pour la mise en pâte en continu en milieu solvant et le lavage |
US20190136448A1 (en) * | 2017-11-08 | 2019-05-09 | Earthrecycle Co., Ltd. | Method for Separating Cellulose |
US10920372B2 (en) * | 2017-11-08 | 2021-02-16 | Earthrecycle Co., Ltd. | Method for separating cellulose |
US20210230375A1 (en) * | 2018-11-07 | 2021-07-29 | Earthrecycle Co., Ltd. | Method for separating cellulose |
Also Published As
Publication number | Publication date |
---|---|
LU61717A1 (fr) | 1971-01-18 |
FR2063171B1 (fr) | 1973-01-12 |
DE2046944A1 (de) | 1971-04-15 |
CA977505A (en) | 1975-11-11 |
CH498244A (fr) | 1970-10-31 |
GB1328674A (en) | 1973-08-30 |
AT300544B (de) | 1972-07-25 |
BE756225A (fr) | 1971-03-01 |
CH512635A (fr) | 1971-09-15 |
FR2063171A1 (fr) | 1971-07-09 |
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