USRE32943E - Process for cooking lignocellulosic material in the presence of hydroxyanthracenes and derivatives thereof - Google Patents
Process for cooking lignocellulosic material in the presence of hydroxyanthracenes and derivatives thereof Download PDFInfo
- Publication number
- USRE32943E USRE32943E US06/233,962 US23396281A USRE32943E US RE32943 E USRE32943 E US RE32943E US 23396281 A US23396281 A US 23396281A US RE32943 E USRE32943 E US RE32943E
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- United States
- Prior art keywords
- cooking
- dihydroxyanthracene
- sodium salt
- cooking aid
- aid
- 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
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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
- D21C3/22—Other features of pulping processes
- D21C3/222—Use of compounds accelerating the pulping processes
Definitions
- This invention relates to a process for the production of pulp. More particularly, the invention relates to a process for the production of pulp from lignocellulosic materials by carrying out the cooking in the presence of a small amount of a novel type of cooking aid selected from the group consisting of hydroxyanthracenes and derivatives thereof.
- the cooking aid can be added to a cooking liquor in any of the conventional alkaline or sulfite or the like cooking processes.
- alkaline cooking process or simply “alkaline process” herein used includes various alkaline cooking processes such as a kraft process, a soda process, a sodium carbonate process and the like.
- sulfite cooking process or simply “sulfite process” herein used includes various sulfite cooking processes such as an alkaline sulfite process, a neutral sulfite process, a bisulfite process, and the like.
- the object of the present invention is to provide a novel process for the production of pulp free from the disadvantages mentioned above.
- the novel process of the present invention is characterized by the selective use of a specific type of a cooking aid comprising at least a member selected from the group consisting of hydroxyanthracenes and derivatives thereof. More particularly, in one aspect of the present invention, there is provided a process for producing alkaline pulp by carrying out the cooking of lignocellulosic materials such as wood, bagasse, hemp and the like in an alkaline cooking liquor in the presence of a small amount of hydroxyanthracene or a derivative thereof which is added as a novel type of cooking aid.
- a process for producing sulfite pulp by carrying out the cooking of said lignocellulosic materials in a cooking liquor comprising sulfite in the presence of a small amount of the same cooking aid as mentioned above.
- hydroxyanthracene or a derivative thereof added to the cooking liquor functions as a cooking aid to promote the dissolution of lignin into the cooking liquor as well as to prevent the degradation of cellulose and hemicellulose throughout the cooking treatment.
- this novel cooking aid the cooking yield and also the quality of the resulting pulp are improved, and the rate of cooking is increased. Incidental to the increased rate of cooking, the amounts of cooking chemicals and steam required for heating are also substantially reduced.
- Typical compounds which can be advantageously employed as said cooking aid in the practice of the present invention include hydroxyanthracenes and derivatives thereof having the following general formula: ##STR1## wherein m is 0, 1 or 2, n is 1 or 2, R is COOA, SO 3 A or H, and A is H or Na; providing that
- R when m is 1, R is at least one of COOA or SO 3 A and R cannot attach to (substitute on) the middle ring;
- R is H
- the compounds defined by the above general formula include those wherein R represents H, COOX wherein X is H or Na, or SO 3 Y wherein Y is H or Na; A represents H or Na; m represents 0, 1 or 2; and n represents 1 or 2.
- R represents H in the above general formula refers to a case in which at least one carbon atom in the anthracene nucleus loses its double bond to change from CH to CH 2 in the same position.
- the compounds defined by the above general formula include those obtained by the addition of at least one hydrogen atom to the carbon atom in the anthracene nucleus to have it lose its double bond and change from its CH form to CH 2 form in the same position.
- These compounds generally include dihydroxyanthracene, dihydroxydihydroanthracene, .[.carboxydihydroanthracene.]., .Iadd.carboxydihydroxyanthracene.Iaddend., as well as .[.dihydroanthracenesulfonic.]. .Iadd.dihydroxyanthracene sulfonic .Iaddend.acids including their sodium salts, dihydroxyanthracene carboxylic acids including their sodium salts, which are most advantageously employed in the practice of the present invention.
- the compounds Nos. 1, 2 and 9 are particularly preferred as the cooking aid in the present invention.
- novel cooking aid compounds are preferably used in an amount in the region of 0.005-3% by weight based on the bone dry weight of the raw material chips or the lignocellulosic materials to be added to the cooking liquor. If the compound is used in an amount in the region of 0.01-0.1% by weight based on the same standard, optimum results will be obtained.
- the compounds represented by the general formula, such as dihydroxyanthracenes, can easily be synthesized from naphthoquinone and butadiene by making use of Diels-Alder reaction.
- the preparation of these compounds is illustrated by the known preparations of Compounds 1-12, as follows.
- Compound (1) can be prepared as afore-described from naphthoquinone and butadiene by the Diels-Alder reaction. This process is disclosed on page 2, left column, lines 27-32 of U.S. Pat. No. 1,890,040.
- Compound (2) can be prepared by the process as disclosed on page 277 of Elsevier's Encyclopedia of Organic Chemistry, Volume 13.
- Compound (3) can be prepared by the process as disclosed on page 278 of the same reference identified in (b).
- Compound (11) can be prepared by the process as disclosed on page 650 of the same reference identified in (b).
- Compound (12) can be prepared by the process as disclosed on page 703 of the same reference identified in (b).
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- Polysaccharides And Polysaccharide Derivatives (AREA)
- Materials For Medical Uses (AREA)
Abstract
An improved process for the production of pulp from lignocellulosic material characterized by the employment of a cooking aid is disclosed. The cooking of the lignocellulosic material is carried out in the presence of a small amount of a compound selected from the group consisting of hydroxyanthracenes and derivatives thereof.
Description
This is a continuation-in-part of Ser. No. 758,837, filed Dec. 2, 1977, now abandoned.
This invention relates to a process for the production of pulp. More particularly, the invention relates to a process for the production of pulp from lignocellulosic materials by carrying out the cooking in the presence of a small amount of a novel type of cooking aid selected from the group consisting of hydroxyanthracenes and derivatives thereof. The cooking aid can be added to a cooking liquor in any of the conventional alkaline or sulfite or the like cooking processes. The term "alkaline cooking process" or simply "alkaline process" herein used includes various alkaline cooking processes such as a kraft process, a soda process, a sodium carbonate process and the like. Similarly, the term "sulfite cooking process" or simply "sulfite process" herein used includes various sulfite cooking processes such as an alkaline sulfite process, a neutral sulfite process, a bisulfite process, and the like.
In the field of producing pulp from lignocellulosic material such as wood, bagasse, hemp and the like, numerous attempts have been made, repeatedly, from ancient times to improve the cooking yield, the rate of cooking and the quality of the product pulp, aiming at the economical production of good quality pulp with decreased consumption of raw material and of energy. For example, instead of the conventional kraft process in which lignocellulosic material such as wood is subjected to treatment by a cooking liquor comprising essentially sodium hydrate and sodium sulfide, a modified process thereof which is usually called a "polysulfide process" and is characterized by being subjected to treatment with a cooking liquor comprising a sodium polysulfide is currently more popularly employed. Various other modifications, for example, the addition of borohydride, hydrazine, hydroxylamine or the like have also been proposed and tried. Most such modified processes, however, have not been useful in a practical manner because in some cases total or partial change of the processing equipment is required. In other cases, there is a significant increase in production costs. In still other cases, the process is not applicable to soft woods or to hard woods, or both. Thus, except for said polysulfide process, none of the above-mentioned prior art processes is more than a laboratory model.
The object of the present invention is to provide a novel process for the production of pulp free from the disadvantages mentioned above.
The novel process of the present invention is characterized by the selective use of a specific type of a cooking aid comprising at least a member selected from the group consisting of hydroxyanthracenes and derivatives thereof. More particularly, in one aspect of the present invention, there is provided a process for producing alkaline pulp by carrying out the cooking of lignocellulosic materials such as wood, bagasse, hemp and the like in an alkaline cooking liquor in the presence of a small amount of hydroxyanthracene or a derivative thereof which is added as a novel type of cooking aid. In another aspect of the present invention, there is provided a process for producing sulfite pulp by carrying out the cooking of said lignocellulosic materials in a cooking liquor comprising sulfite in the presence of a small amount of the same cooking aid as mentioned above. As a result of effecting the cooking of such lignocellulosic materials as mentioned above in the presence of a specific amount of said novel cooking aid according to the present invention, the solution velocity of lignin from said lignocellulosic materials is substantially increased, and in turn the rate of cooking is also substantially increased. The cooking yield in pulp production is also substantially improved as compared with the prior art process using the same degree of cooking. This is because hydroxyanthracene or a derivative thereof added to the cooking liquor functions as a cooking aid to promote the dissolution of lignin into the cooking liquor as well as to prevent the degradation of cellulose and hemicellulose throughout the cooking treatment. As a result of using this novel cooking aid, the cooking yield and also the quality of the resulting pulp are improved, and the rate of cooking is increased. Incidental to the increased rate of cooking, the amounts of cooking chemicals and steam required for heating are also substantially reduced.
Typical compounds which can be advantageously employed as said cooking aid in the practice of the present invention include hydroxyanthracenes and derivatives thereof having the following general formula: ##STR1## wherein m is 0, 1 or 2, n is 1 or 2, R is COOA, SO3 A or H, and A is H or Na; providing that
when m is 1, R is at least one of COOA or SO3 A and R cannot attach to (substitute on) the middle ring;
when m is 0 or 2, R is H;
when R is H and m is 2, two carbon atoms of the anthracene nucleus lose their double bonds, and each such carbon atom takes the form of CH2 instead of CH, in which case one H of each CH2 is not counted as an R and may be substituted by OA.
Representative compounds included within the generic formula and which can be used in the practice of the present invention include the following:
(1) 1,4-dihydro-9,10-dihydroxyanthracene and its Na salt; ##STR2## (2) 1-hydroxyanthracene and its Na salt; ##STR3## (3) 2-hydroxyanthracene and its Na salt; ##STR4## (4) 9-hydroxyanthracene and its Na salt; ##STR5## (5) 9,10-dihydroanthranol and its Na salt; ##STR6## (6) 1,2-dihydroxyanthracene and its Na salt; ##STR7## (7) 2,3-dihydroxyanthracene and its Na salt; ##STR8## (8) 2,6-dihydroxyanthracene and its Na salt; ##STR9## (9) 9,10-dihydroxyanthracene and its Na salt; ##STR10## (10) 9,10-dihydroanthracene-9,10-diol and its Na salt; ##STR11## (11) 9,10-dihydroxyanthracene-2-carboxylic acid and its Na salt; ##STR12## (12) 9,10-dihydroxyanthracene-1-sulphonic acid and its Na salt; ##STR13##
The compounds defined by the above general formula include those wherein R represents H, COOX wherein X is H or Na, or SO3 Y wherein Y is H or Na; A represents H or Na; m represents 0, 1 or 2; and n represents 1 or 2. The case wherein R represents H in the above general formula refers to a case in which at least one carbon atom in the anthracene nucleus loses its double bond to change from CH to CH2 in the same position. Namely, the compounds defined by the above general formula include those obtained by the addition of at least one hydrogen atom to the carbon atom in the anthracene nucleus to have it lose its double bond and change from its CH form to CH2 form in the same position.
These compounds generally include dihydroxyanthracene, dihydroxydihydroanthracene, .[.carboxydihydroanthracene.]., .Iadd.carboxydihydroxyanthracene.Iaddend., as well as .[.dihydroanthracenesulfonic.]. .Iadd.dihydroxyanthracene sulfonic .Iaddend.acids including their sodium salts, dihydroxyanthracene carboxylic acids including their sodium salts, which are most advantageously employed in the practice of the present invention.
The compounds Nos. 1, 2 and 9 are particularly preferred as the cooking aid in the present invention.
These novel cooking aid compounds are preferably used in an amount in the region of 0.005-3% by weight based on the bone dry weight of the raw material chips or the lignocellulosic materials to be added to the cooking liquor. If the compound is used in an amount in the region of 0.01-0.1% by weight based on the same standard, optimum results will be obtained.
The compounds represented by the general formula, such as dihydroxyanthracenes, can easily be synthesized from naphthoquinone and butadiene by making use of Diels-Alder reaction. The preparation of these compounds is illustrated by the known preparations of Compounds 1-12, as follows.
(a) Compound (1) can be prepared as afore-described from naphthoquinone and butadiene by the Diels-Alder reaction. This process is disclosed on page 2, left column, lines 27-32 of U.S. Pat. No. 1,890,040.
(b) Compound (2) can be prepared by the process as disclosed on page 277 of Elsevier's Encyclopedia of Organic Chemistry, Volume 13.
(c) Compound (3) can be prepared by the process as disclosed on page 278 of the same reference identified in (b).
(d) Compounds (4) through (10) can be prepared by the processes disclosed on pages 279, 281, 291, 300, 301, 302 and 304, respectively, of the same reference identified in (b).
(e) Compound (11) can be prepared by the process as disclosed on page 650 of the same reference identified in (b).
(f) Compound (12) can be prepared by the process as disclosed on page 703 of the same reference identified in (b).
These compounds when used as cooking aids are easy to dissolve in the cooking liquor. In order to carry out the process of the present invention, no special change is required with respect to the cooking conditions except that a specified amount of said cooking aid is merely added to an ordinary cooking liquor.
The following examples will illustrate the preferred embodiments of the present invention.
600 g. of softwood chips were placed in a 4-liter capacity autoclave, to which was added a kraft process cooking liquor having 17% active alkali and 25% sulfidity. Then, dihydroxydihydroanthracene, i.e., 1,4-dihydro-9,10-dihydroxyanthracene, in an amount of 0.05% by weight based on the bone dry weight of the chips was added to the same cooking liquor and cooking was carried out at 165° C. for 75 minutes.
For comparative purposes, the same experiment was repeated except that said dihydroxydihydroanthracene was omitted. The results of these experiments were as shown in Table 1, below.
TABLE 1
______________________________________
Kraft process cooking
Kraft process cooking
with dihydroxydihydro-
without dihydroxydihydro-
anthracene (present anthracene
invention) (prior art)
______________________________________
Cooking 48.6 46.5
yield (%)
Kappa 42 51
number
Burst 6.9 6.2
index*
Breaking
8.2 7.0
length
(km)
Tear 170 170
factor
______________________________________
*determined by JIS P8210(Testing Method for Strength of Paper Pulp)
700 g. of hardwood chips were placed in a 4-liter capacity autoclave, to which a soda process cooking liquor having a 15.5% (as Na2 O) caustic soda and dihydroxyanthracene, i.e., 9,10-dihydroxyanthracene, in an amount of 0.02% by weight based on the bone dry weight of the chips was added and cooking was carried out at 155° C. for 75 minutes.
Next, for comparative purposes, the same experiment was repeated except that said dihydroxyanthracene was omitted. The results of these experiments are shown in Table 2, below.
TABLE 2
______________________________________
Soda process cooking
Soda process cooking without dihydroxy-
with dihydroxyanthracene
anthracene
(present invention) (prior art)
______________________________________
Cooking
53.9 53.0
yield (%)
Kappa 50 78
number
Burst 4.3 3.0
index*
Breaking
6.1 4.5
length
(km)
Tear 110 100
factor
______________________________________
*determined by JIS P8210(Testing Method for Strength of Paper Pulp)
700 g. of hardwood chips were placed in a 4-liter capacity autoclave, to which was added a sodium carbonate process cooking liquor containing 10% sodium carbonate and 0.1% by weight, based on the bone dry weight of the chips, of sodium dihydroxyanthracenecarboxylate, i.e., 9,10-dihydroxyanthracene-2-carboxylic acid (Na salt), and cooking was carried out at 180° C. for 20 minutes. Then, the cooked chips were beaten by a disk refiner to a freeness of 450 cc.
For comparative purposes, the same experiment was repeated except that said sodium dihydroxyanthracenecarboxylate was omitted. The results of these experimints are shown in Table 3, below.
TABLE 3
______________________________________
Sodium carbonate process
Sodium carbonate process
cooking with sodium cooking without sodium
dihydroxyanthracene-
dihydroxyanthracene-
carboxylate carboxylate
(present invention) (prior art)
______________________________________
Cooking
82.0 78.9
yield (%)
Burst 1.8 1.7
index*
Breaking
3.2 2.5
length
(km)
Folds, 20 14
double
Ring 14.2 13.5
crush
resistance
Concora
19.5 19.0
crush
resistance
______________________________________
*determined by JIS P8210(Testing Method for Strength of Paper Pulp)?
400 g. of flax was placed in a 4-liter capacity autoclave, to which was added a cooking liquor containing 18% sodium sulfite and 3% caustic soda, both based on the weight of raw material, and sodium dihydroxyanthracenesulfonate, i.e., 9,10-dihydroxyanthracene-1-sulfonic acid (Na salt), in an amount of 0.05% based on the bone dry weight of the raw material, and cooking was carried out at 180° C. for 4 hours. Separately, for comparative purposes, the same experiment was repeated except that said sodium dihydroxyanthracenesulfonate was omitted. The results of these experiments are shown in Table 4, below.
TABLE 4
______________________________________
Sulfite cooking with
Sulfite cooking without
sodium dihydroxyanthra-
sodium dihydroxyanthra-
cenesulfonate cenesulfonate
(present invention) (prior art)
______________________________________
Cooking 62.5 58.5
yield (%)
Kappa 8 12
number
Breaking
8.9 7.6
length
(km)
Tear 190 170
factor
______________________________________
Claims (11)
1. An improved cooking process for the production of pulp from lignocellulosic material comprising cooking lignocellulosic material in a cooking liquor,
the improvement comprising admixing in said cooking liquor an amount, sufficient to increase the cooking rate of said lignocellulosic material, of a cooking aid comprising at least one member selected from the group consisting of compounds having the formula: ##STR14## .[.wherein m is 0, 1 or 2, n is 1, or 2, R is COOA, SO3 A or H, and A is H or Na; providing that when m is 1, R is at least one of COOA or SO3 A and R cannot attach to the middle ring; when m is 0 or 2, R is H; and.].
.Iadd.wherein, m is 1 when R is COOA or SO3 A and R cannot attach to the middle ring, m is 2 when R is H, and A is H or Na; and .Iaddend.
when R is H and m is 2, two carbon atoms of the anthracene nucleus lose their double bonds, and each such carbon atom takes the form of CH2 instead of CH, in which case one H of each CH2 is not counted as an R and may be substituted by OA.
2. The process of claim 1, wherein said cooking aid is at least one member selected from the group consisting of .[.dihydroxyanthracene,.]. dihydroxydihydroanthracene, .[.carboxydihydroanthracene and dihydroanthracene sulfonate.]. .Iadd.dihydroxyanthracene sulfonic acids and their sodium salt and dihydroxyanthracene carboxylic acids and their sodium salts. .Iaddend.
3. The process of claim 1, wherein said cooking aid is used in an amount of from about 0.005 to about 3% by weight based on the bone dry weight of lignocellulosic material.
4. The process of claim 1, wherein said cooking aid is used in an amount of from about 0.01 to about 0.1% by weight based on the bone dry weight of lignocellulosic material.
5. The process of claim 3, wherein said cooking aid is 1,4-dihydro-9,10-dihydroxyanthracene or its sodium salt. .[.6. The process of claim 3, wherein said cooking aid is 1-hydroxyanthracene or its sodium salt..]. .[.7. The process of claim 3, wherein said cooking aid is 9,10-dihydroxyanthracene or its sodium salt..]. .[.8. The process of claim 3, wherein said cooking aid is 2-hydroxyanthracene or its sodium salt..]. .[.9. The process of claim 3, wherein said cooking aid is 9-hydroxyanthracene or its sodium salt..]. .[.10. The process of claim 3, wherein said cooking aid is 9,10-dihydroanthranol or its sodium salt..].
.[.11. The process of claim 3, wherein said cooking aid is 1,2-dihydroxyanthracene or its sodium salt..]. .[.12. The process of claim 3, wherein said cooking aid is 2,3-dihydroxyanthracene or its sodium salt..]. .[.13. The process of claim 3, wherein said cooking aid is
2,6-dihydroxyanthracene or its sodium salt..]. 14. The process of claim 3, wherein said cooking aid is 9,10-dihydroanthracene-9,10-diol or its sodium
salt. 15. The process of claim 3, wherein said cooking aid is
9,10-dihydroxyanthracene-2-carboxylic acid or its sodium salt. 16. The process of claim 3, wherein said cooking aid is,
9,10-dihydroxyanthracene-1-sulphonic acid or its sodium salt. 17. The process of each of claims 1, .[.6, 7, 8, 9, 10, 11, 12, 13,.]. .Iadd.2, .Iaddend.14, 15 or 16, wherein said cooking liquor is an alkaline process
cooking liquor. 18. The process of each of claims 1, .[.6, 7, 8, 9, 10, 11, 12, 13,.]. .Iadd.2, .Iaddend.14, 15 or 16, wherein said cooking liquor is a sulfite process cooking liquor.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP51-148492 | 1976-12-10 | ||
| JP14849276A JPS5374101A (en) | 1976-12-10 | 1976-12-10 | Pulp making method |
Related Parent Applications (2)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US75883777A Continuation-In-Part | 1976-12-10 | 1977-01-12 | |
| US05/940,582 Reissue US4181565A (en) | 1976-12-10 | 1978-09-08 | Process for cooking lignocellulosic material in the presence of hydroxyanthracenes and derivatives thereof |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| USRE32943E true USRE32943E (en) | 1989-06-06 |
Family
ID=15453954
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US06/233,962 Expired - Lifetime USRE32943E (en) | 1976-12-10 | 1981-02-12 | Process for cooking lignocellulosic material in the presence of hydroxyanthracenes and derivatives thereof |
Country Status (11)
| Country | Link |
|---|---|
| US (1) | USRE32943E (en) |
| JP (1) | JPS5374101A (en) |
| AU (1) | AU513517B2 (en) |
| BR (1) | BR7708218A (en) |
| CA (1) | CA1106557A (en) |
| DE (1) | DE2754991B2 (en) |
| FI (1) | FI68868C (en) |
| FR (1) | FR2373637A1 (en) |
| NO (1) | NO150087C (en) |
| NZ (1) | NZ185734A (en) |
| SE (1) | SE437171B (en) |
Families Citing this family (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS51112903A (en) * | 1975-03-26 | 1976-10-05 | Honshu Paper Co Ltd | Process for digesting lignocellulose material with sulphites |
| US4036680A (en) * | 1976-12-14 | 1977-07-19 | Canadian Industries, Ltd. | Delignification of lignocellulosic material with a soda pulping liquor containing a Diels Alder adduct of benzoquinone or naphthoquinone in admixture with a nitro aromatic compound |
| US4036681A (en) * | 1976-12-14 | 1977-07-19 | Canadian Industries, Ltd. | Delignification of lignocellulosic material with an alkaline pulping liquor containing a Diels Alder adduct of benzoquinone or naphthoquinone |
| JPS6059356B2 (en) * | 1977-12-05 | 1985-12-24 | 川崎化成工業株式会社 | Pulp manufacturing method |
| FR2435457A1 (en) * | 1978-06-29 | 1980-04-04 | Ugine Kuhlmann | HEXAHYDRO-1,2,3,4,4A, 9A ANTHRACENE-DIONE-9,10, ITS PREPARATION AND ITS APPLICATION TO THE DELIGNIFICATION OF LIGNOCELLULOSIC MATERIALS |
| JPS5512806A (en) * | 1978-07-04 | 1980-01-29 | Oji Paper Co | Alkali pulp producing method |
| FR2442912A1 (en) * | 1978-07-27 | 1980-06-27 | Ugine Kuhlmann | PROCESS FOR COOKING LIGNOCELLULOSIC MATERIALS FOR THE PRODUCTION OF PULP |
| JPS55128091A (en) * | 1979-03-23 | 1980-10-03 | Oji Paper Co | Pulping of lignocellulose material |
| JPS58125737U (en) * | 1982-02-18 | 1983-08-26 | 株式会社シマノ | caliper brake |
Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US1890040A (en) * | 1928-05-07 | 1932-12-06 | Gen Aniline Works Inc | Production of anthraquinone and derivatives thereof |
| US2883826A (en) * | 1953-01-07 | 1959-04-28 | Univ Minnesota | Process for conditioning plant fibers for spinning |
| US2920010A (en) * | 1956-11-05 | 1960-01-05 | Voiret Eugene Gilbert | Manufacture of wood pulp |
| CA986662A (en) * | 1973-05-01 | 1976-04-06 | David L. Mccandless | Pretreatment of lignocellulosic material with anthraquinone salts in alkaline pulping |
| JPS5143403A (en) * | 1974-10-09 | 1976-04-14 | Honshu Paper Co Ltd | Arukariparupuno seizohoho |
| JPS51109303A (en) * | 1975-03-24 | 1976-09-28 | Honshu Paper Co Ltd | ARUKARIISANSOSHORINYORU RIGUNOSERUROOSUBUTSUSHITSUNO DATSURIGUNINHO |
| JPS51112903A (en) * | 1975-03-26 | 1976-10-05 | Honshu Paper Co Ltd | Process for digesting lignocellulose material with sulphites |
| US4012280A (en) * | 1975-09-05 | 1977-03-15 | Canadian Industries, Ltd. | Delignification of lignocellulosic material with an alkaline liquor in the presence of a cyclic keto compound |
| US4036681A (en) * | 1976-12-14 | 1977-07-19 | Canadian Industries, Ltd. | Delignification of lignocellulosic material with an alkaline pulping liquor containing a Diels Alder adduct of benzoquinone or naphthoquinone |
Family Cites Families (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE326705C (en) * | 1919-10-17 | 1920-09-30 | Richard Hartmuth Dr | Process for the treatment of wood or cellulosic materials for the production of cellulose and synthetic resin, paint, asphalt and the like like |
| US1705424A (en) * | 1924-09-30 | 1929-03-12 | Strecker Otto Carl | Process for the production of cellulose by decomposition of vegetable fibers |
| US1658213A (en) * | 1924-09-30 | 1928-02-07 | Otto C Strecker | Process for the production of cellulose by decomposition of vegetable fibers |
| DE486533C (en) * | 1926-12-24 | 1929-11-19 | Otto C Strecker Fa Dr | Process for obtaining pulp |
| NL35585C (en) * | 1929-06-07 | |||
| DE569853C (en) * | 1929-08-07 | 1933-02-09 | E H Willi Schacht Dr Ing | Process for the production of a semi-pulp from straw and grass |
| ZA773044B (en) * | 1976-06-02 | 1978-04-26 | Australian Paper Manufacturers | Improvements in pulping processes |
-
1976
- 1976-12-10 JP JP14849276A patent/JPS5374101A/en active Granted
-
1977
- 1977-11-21 NZ NZ185734A patent/NZ185734A/en unknown
- 1977-11-23 SE SE7713266A patent/SE437171B/en not_active IP Right Cessation
- 1977-11-23 AU AU30870/77A patent/AU513517B2/en not_active Expired
- 1977-11-28 NO NO774067A patent/NO150087C/en unknown
- 1977-11-30 CA CA292,069A patent/CA1106557A/en not_active Expired
- 1977-12-02 FI FI773661A patent/FI68868C/en not_active IP Right Cessation
- 1977-12-09 DE DE2754991A patent/DE2754991B2/en active Granted
- 1977-12-09 BR BR7708218A patent/BR7708218A/en unknown
- 1977-12-09 FR FR7737226A patent/FR2373637A1/en active Granted
-
1981
- 1981-02-12 US US06/233,962 patent/USRE32943E/en not_active Expired - Lifetime
Patent Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US1890040A (en) * | 1928-05-07 | 1932-12-06 | Gen Aniline Works Inc | Production of anthraquinone and derivatives thereof |
| US2883826A (en) * | 1953-01-07 | 1959-04-28 | Univ Minnesota | Process for conditioning plant fibers for spinning |
| US2920010A (en) * | 1956-11-05 | 1960-01-05 | Voiret Eugene Gilbert | Manufacture of wood pulp |
| CA986662A (en) * | 1973-05-01 | 1976-04-06 | David L. Mccandless | Pretreatment of lignocellulosic material with anthraquinone salts in alkaline pulping |
| JPS5143403A (en) * | 1974-10-09 | 1976-04-14 | Honshu Paper Co Ltd | Arukariparupuno seizohoho |
| JPS51109303A (en) * | 1975-03-24 | 1976-09-28 | Honshu Paper Co Ltd | ARUKARIISANSOSHORINYORU RIGUNOSERUROOSUBUTSUSHITSUNO DATSURIGUNINHO |
| JPS51112903A (en) * | 1975-03-26 | 1976-10-05 | Honshu Paper Co Ltd | Process for digesting lignocellulose material with sulphites |
| US4012280A (en) * | 1975-09-05 | 1977-03-15 | Canadian Industries, Ltd. | Delignification of lignocellulosic material with an alkaline liquor in the presence of a cyclic keto compound |
| US4036681A (en) * | 1976-12-14 | 1977-07-19 | Canadian Industries, Ltd. | Delignification of lignocellulosic material with an alkaline pulping liquor containing a Diels Alder adduct of benzoquinone or naphthoquinone |
Non-Patent Citations (2)
| Title |
|---|
| Elsevier s Encyclopedia of Organic Chemistry, vol. 13, 1946, pp. 277 279, 281, 291, 300 302, 304, 650 & 703. * |
| Elsevier's Encyclopedia of Organic Chemistry, vol. 13, 1946, pp. 277-279, 281, 291, 300-302, 304, 650 & 703. |
Also Published As
| Publication number | Publication date |
|---|---|
| SE437171B (en) | 1985-02-11 |
| DE2754991B2 (en) | 1979-01-18 |
| NO774067L (en) | 1978-06-13 |
| NO150087C (en) | 1984-08-15 |
| FI68868C (en) | 1985-11-11 |
| CA1106557A (en) | 1981-08-11 |
| FR2373637A1 (en) | 1978-07-07 |
| NO150087B (en) | 1984-05-07 |
| BR7708218A (en) | 1978-09-05 |
| SE7713266L (en) | 1978-06-11 |
| NZ185734A (en) | 1980-11-28 |
| DE2754991A1 (en) | 1978-06-15 |
| FR2373637B1 (en) | 1979-04-27 |
| JPS5374101A (en) | 1978-07-01 |
| FI773661A (en) | 1978-06-11 |
| DE2754991C3 (en) | 1987-06-19 |
| AU3087077A (en) | 1979-05-31 |
| JPS5719239B2 (en) | 1982-04-21 |
| FI68868B (en) | 1985-07-31 |
| AU513517B2 (en) | 1980-12-04 |
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