US1319360A - Erik ludvig rinman - Google Patents
Erik ludvig rinman Download PDFInfo
- Publication number
- US1319360A US1319360A US1319360DA US1319360A US 1319360 A US1319360 A US 1319360A US 1319360D A US1319360D A US 1319360DA US 1319360 A US1319360 A US 1319360A
- Authority
- US
- United States
- Prior art keywords
- lye
- boiling
- caustic soda
- cellulose
- during
- 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
- HEMHJVSKTPXQMS-UHFFFAOYSA-M sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 390
- 235000011121 sodium hydroxide Nutrition 0.000 description 170
- 238000009835 boiling Methods 0.000 description 82
- 229920002678 cellulose Polymers 0.000 description 42
- 239000001913 cellulose Substances 0.000 description 42
- 238000000034 method Methods 0.000 description 42
- 239000000126 substance Substances 0.000 description 26
- 239000002994 raw material Substances 0.000 description 22
- 239000002023 wood Substances 0.000 description 16
- BVKZGUZCCUSVTD-UHFFFAOYSA-N Carbonic acid Chemical compound OC(O)=O BVKZGUZCCUSVTD-UHFFFAOYSA-N 0.000 description 14
- 238000000605 extraction Methods 0.000 description 14
- 239000002699 waste material Substances 0.000 description 14
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound [Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 description 12
- 229910052753 mercury Inorganic materials 0.000 description 12
- QAOWNCQODCNURD-UHFFFAOYSA-L sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 10
- NINIDFKCEFEMDL-UHFFFAOYSA-N sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 8
- 229910052717 sulfur Inorganic materials 0.000 description 8
- 239000011593 sulfur Substances 0.000 description 8
- 239000003513 alkali Substances 0.000 description 6
- 229920005610 lignin Polymers 0.000 description 6
- CSCPPACGZOOCGX-UHFFFAOYSA-N acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- 238000000197 pyrolysis Methods 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 239000002585 base Substances 0.000 description 2
- 239000007844 bleaching agent Substances 0.000 description 2
- 238000009993 causticizing Methods 0.000 description 2
- 239000003518 caustics Substances 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 239000011248 coating agent Substances 0.000 description 2
- 238000000576 coating method Methods 0.000 description 2
- 230000000875 corresponding Effects 0.000 description 2
- 230000003247 decreasing Effects 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- OKKJLVBELUTLKV-UHFFFAOYSA-N methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 2
- 239000003921 oil Substances 0.000 description 2
- 238000005086 pumping Methods 0.000 description 2
- 235000013311 vegetables Nutrition 0.000 description 2
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
Definitions
- Thepresent process consists principally in this that the caustic soda lye used is treated during the boiling of the material by means of a contact substance furthering reduction. Mercury is especially adapted as such contact material.
- a caustic soda lye When carrying out the present process it has proved particularly ad-. vantageous to use as boiling lye a caustic soda lye considerably more diluted than the so-called sulfate lye now ordinarily used.
- an ordinary sulfate lye contains about 100 to 120 gr. Na O and Na s in the form of active alkali, there is preferably used ac cording to the present invention a caustic soda lye containing about gr Na O per liter lye.
- the lye thus supplied may be highly concen trated, from 10% NaOH to a higher concentration, if care only be taken that it is supplied in such manner that it is allowed to mix with the other lye before influencing the raw material or the wood.
- the boiling lye In order to modify during the boiling the influence of the caustic soda lye it is suitable to provide for the boiling lye always containing a certain quantity of a waste lye from a previous boiling or, still better, a waste liquor freed from lignin substance capable of being precipitated with carbonic acid.
- This may suitably be effected for instance by producing the caustic sode lye of about 8 per cent. concentration with which the boiling is begun, by dissolving and after ward causticizing soda, for instance soda obtained by dry distillation of waste liquor, in a waste lye from a previous boiling having a specific gravity of from 1.036 to 1.074 and which has been freed from lignin by being treated with carbonic acid, if desired.
- water may be used as dissolving agent when making the lye, such a solution being more easily filtered.
- the extraction from the vegetable raw material, particularly from wood, is facilitated by relieving the wood from the air inclosed in the same before admitting the lye to the wood. This may be effected by drenching the wood with water. It may also be effected by placing the boiler under vacuum before filling the lye into the same. This vacuum may be used for drawing the boiling lye into the boiler.
- the mercury used as contact substance during the boiling according to the present invention is not consumed except by wear. It is therefore sufficient once every fourteen days, or even at still longer periods, to give the boiler a very thin coating with mercury, for instance by filling the same with for instance 0.0001 normal I-IgC'l solution, until the mercury has been precipitated on the walls of the boiler.
- the boiling lye being preferably pumped around in a closed circuit when carrylng out the present process, it is suitable during this pumping to cause the boiling lye to contact with mercury placed as contact substance in suitable manner.
- the boiling lye used with the present process is most advantageously regenerated according tothe process described in the U. S. Patent No. 1,196,290 for dry distillation of the waste liquors from the soda cellulose manufacture with strong bases for producing acetone, wood spirit, oils and so forth.
Landscapes
- Paper (AREA)
- Polysaccharides And Polysaccharide Derivatives (AREA)
Description
ERIK LUDVIG- RINMAN, OF DJURSHOLM, SWEDEN.
PROCESS OF PRODUCING SODA CELLULOSE, PARTICULARLY WOOD CELLULOSE.
N 0 Drawing.
To all whom it may concern:
Be it known that I, ERIK LUDVIG RINMAN, a subject of the King of Sweden, residing at Djursholm, in the Kingdom of Sweden, have invented a new and useful Improvement in Processes of Producing Soda Cellulose, Particularly Wood Cellulose, of which the following is a specification.
By the use of the co-called sulfate process it is possible to produce qualities of cellulose which it has heretofore not been possible to obtain by the use of a caustic soda lye free from sulfur. It is well known that cellulose produced by boiling with soda lye free from sulfur is more difiieult to bleach and is colored more yellow than ordinary sulfate cellulose. The present invention, however, re-
the process.
fersto a process by means of which also with the use of caustic soda lye free from sulfur qualities of cellulose are obtained which have quite the same appearance and which are at least equally good as those obtained by means of the sulfate process.
Thepresent process consists principally in this that the caustic soda lye used is treated during the boiling of the material by means of a contact substance furthering reduction. Mercury is especially adapted as such contact material. When carrying out the present process it has proved particularly ad-. vantageous to use as boiling lye a caustic soda lye considerably more diluted than the so-called sulfate lye now ordinarily used. While an ordinary sulfate lye contains about 100 to 120 gr. Na O and Na s in the form of active alkali, there is preferably used ac cording to the present invention a caustic soda lye containing about gr Na O per liter lye.
The said quantity of alkali, and even a greater quantity, being consumed during the boiling, however, a quantity of lye about twice as great as the one now ordinarily used would appear to be necessary for every boiling. It is also possible thus to carry out It is also possible, however, to proceed in such manner that the boiling is begun with the ordinary quantity of fresh lye but with about half the necessary quantity of alkali, that is to say, to use a lye containing about 60 gr. M 0 in the form of free NaOH per liter lye. During the boil- Specification of Letters Patent. t t 0 1;, 21, 1919,
Application filed May 2a, 1918. Serial No. 236,103.
increased over the suitable amount, that is to say, over about 60 gr. Na O per liter lye. The lye thus supplied may be highly concen trated, from 10% NaOH to a higher concentration, if care only be taken that it is supplied in such manner that it is allowed to mix with the other lye before influencing the raw material or the wood.
Cellulose, and particularly wood cellulose, being very little affected by a caustic soda lye of at most 8 per cent. concentration provided that;the temperature is not over 170 (1., it is important, for obtaining agood yield of cellulose, that the process be performed in such manner that the principal extraction of the incrustating substances is made at a temperature of from l-lO C. to 170 C. The time of boiling, however, must then naturally be somewhat lengthened. The lengthening of the time of boiling may be decreased by using artificial pressure during the said extraction, so that the total excess of pressure during the boiling amounts to 10 to 11 kg. per square cm. This additional pressure may suitably be obtained by means of compressed air. The lengthening of the boiling time may be reduced in this manner to amount only to about. half an hour over the usual boiling time.
In order to modify during the boiling the influence of the caustic soda lye it is suitable to provide for the boiling lye always containing a certain quantity of a waste lye from a previous boiling or, still better, a waste liquor freed from lignin substance capable of being precipitated with carbonic acid. This may suitably be effected for instance by producing the caustic sode lye of about 8 per cent. concentration with which the boiling is begun, by dissolving and after ward causticizing soda, for instance soda obtained by dry distillation of waste liquor, in a waste lye from a previous boiling having a specific gravity of from 1.036 to 1.074 and which has been freed from lignin by being treated with carbonic acid, if desired. On the other hand, for producing the necessary quantity of caustic soda lye of a higher concentration, if such lye is used, water may be used as dissolving agent when making the lye, such a solution being more easily filtered.
The extraction from the vegetable raw material, particularly from wood, is facilitated by relieving the wood from the air inclosed in the same before admitting the lye to the wood. This may be effected by drenching the wood with water. It may also be effected by placing the boiler under vacuum before filling the lye into the same. This vacuum may be used for drawing the boiling lye into the boiler.
The mercury used as contact substance during the boiling according to the present invention is not consumed except by wear. It is therefore sufficient once every fourteen days, or even at still longer periods, to give the boiler a very thin coating with mercury, for instance by filling the same with for instance 0.0001 normal I-IgC'l solution, until the mercury has been precipitated on the walls of the boiler. The boiling lye being preferably pumped around in a closed circuit when carrylng out the present process, it is suitable during this pumping to cause the boiling lye to contact with mercury placed as contact substance in suitable manner.
The boiling lye used with the present process is most advantageously regenerated according tothe process described in the U. S. Patent No. 1,196,290 for dry distillation of the waste liquors from the soda cellulose manufacture with strong bases for producing acetone, wood spirit, oils and so forth.
I claim:
1. The process of producing cellulose consisting in boiling the raw material with caustic soda lye and treating the lye during the boiling with a contact substance insoluble in caustic soda lye and furthering reduction.
2. The process of producing cellulose consisting in boiling the raw material with a caustic soda lye and treating the lye during the boiling with mercury.
3. The process of producing cellulose consisting in boiling the raw material with a caustic soda lye free from sulfur, and treating the lye during the boiling with a contact substance insoluble in caustic soda lye and furthering reduction.
4:. The process of producing cellulose consisting in boiling the raw material with a lye containing about 60 gram Na O per liter lye and treating the lye durin the boiling with. a contact substance insolu 1e in caustic soda lye and furthering reduction.
5. The process of producing cellulose, consisting in boiling the raw material with a caustic soda lye, effecting the principal extraction at a temperature of from 140 C. to 17 0 0., and treating the lye during the boiling with a contact substance insoluble incaustic soda lye and furthering reduction.
6. The process of producing cellulose, consisting in boiling the raw material with a caustic soda lye, effecting the principal extraction at a temperature of from 140 C. to 170 (3., subjecting the lye to a pressure exceeding that corresponding to the temperature used, and treating the lye during the boiling with a contact substance insoluble in caustic soda lye and furthering reduction.
7. The process of producing cellulose, consisting in boiling the raw material with a caustic soda lye, containing waste liquor from a previous boiling, efiecting the principal extraction at a temperature of from 140 C. to 17 0 .C., and treating the lye during the boiling with a contact substance insoluble in caustic soda lye and furthering reduction.
8. The process of roducing cellulose, consisting in boiling t e raw material with a caustic soda lye, containing waste liquor from a previous boiling relieved'of lignin, effecting the principal extraction at a temperature of from 140 C. to 170 (1, and treating the lye during the boiling with a contact substance insoluble in caustic soda lye and furthering reduction. a
9. The process of producing cellulose consisting in relieving the raw material from air inclosed in the same, boiling the raw material-with caustic soda lye and treating the lye during the boiling with a contact substance insoluble in caustic soda lye and furthering reduction.
ERIK LUDVIG RINMAN.
Publications (1)
Publication Number | Publication Date |
---|---|
US1319360A true US1319360A (en) | 1919-10-21 |
Family
ID=3386834
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US1319360D Expired - Lifetime US1319360A (en) | Erik ludvig rinman |
Country Status (1)
Country | Link |
---|---|
US (1) | US1319360A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2810647A (en) * | 1954-12-21 | 1957-10-22 | Valite Corp | Process of preparing fiber from pithcontaining plant materials |
-
0
- US US1319360D patent/US1319360A/en not_active Expired - Lifetime
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2810647A (en) * | 1954-12-21 | 1957-10-22 | Valite Corp | Process of preparing fiber from pithcontaining plant materials |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US2697703A (en) | Fractionation of lignocellulose materials | |
GB283910A (en) | Improved process for the extraction of cellulose or paper pulp from fibrous vegetable matter containing the same | |
US1319360A (en) | Erik ludvig rinman | |
US1387441A (en) | Process of producing cellulose | |
US2249174A (en) | Process for producing white wood pulp of high solution viscosity and purity | |
US1842712A (en) | Manufacture of wood pulp, etc. | |
US2676980A (en) | Process of making tanninlike materials and the resulting products | |
US1679441A (en) | Process of manufacturing pulp for paper production | |
US1842649A (en) | Process of treating cellulose material | |
US1764601A (en) | Product and process of making the same from sulphite waste liquors | |
US1829110A (en) | Purification of cellulose fiber | |
US1557338A (en) | Method of producing half stuffs and cellulose | |
US2407909A (en) | Purification of crude cellulosic material | |
US1606501A (en) | Treatment of residual liquor | |
US2026068A (en) | Process for the improvement of cellulose | |
US1705897A (en) | Bleaching of pulp | |
US1741540A (en) | Process for the production of high-alpha cellulose fiber for the manufacture of cellulose derivatives | |
US1792202A (en) | Process for treating the bagasse of sugar cane | |
US1840162A (en) | Process of opening-up resiniferous wood | |
US996225A (en) | Fiber-producing process and resulting fiber material. | |
US1792009A (en) | Process for the production of cellulose | |
US1898612A (en) | Manufacture of pulp and paper | |
SU1730299A1 (en) | Method of producing cellulose for chemical processing | |
US1967347A (en) | Process for producing a cellulose of high content of alpha cellulose | |
US1516917A (en) | Process of treating seaweed |