US1700595A - Cellulose composition for esterification and process of preparing same - Google Patents
Cellulose composition for esterification and process of preparing same Download PDFInfo
- Publication number
- US1700595A US1700595A US172567A US17256727A US1700595A US 1700595 A US1700595 A US 1700595A US 172567 A US172567 A US 172567A US 17256727 A US17256727 A US 17256727A US 1700595 A US1700595 A US 1700595A
- Authority
- US
- United States
- Prior art keywords
- cellulose
- fiber
- paper
- mercerized
- nitrocellulose
- 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
- 229920002678 cellulose Polymers 0.000 title description 36
- 239000001913 cellulose Substances 0.000 title description 36
- 238000000034 method Methods 0.000 title description 19
- 239000000203 mixture Substances 0.000 title description 7
- 230000032050 esterification Effects 0.000 title description 2
- 238000005886 esterification reaction Methods 0.000 title description 2
- 239000000835 fiber Substances 0.000 description 40
- 239000000020 Nitrocellulose Substances 0.000 description 18
- FJWGYAHXMCUOOM-QHOUIDNNSA-N [(2s,3r,4s,5r,6r)-2-[(2r,3r,4s,5r,6s)-4,5-dinitrooxy-2-(nitrooxymethyl)-6-[(2r,3r,4s,5r,6s)-4,5,6-trinitrooxy-2-(nitrooxymethyl)oxan-3-yl]oxyoxan-3-yl]oxy-3,5-dinitrooxy-6-(nitrooxymethyl)oxan-4-yl] nitrate Chemical compound O([C@@H]1O[C@@H]([C@H]([C@H](O[N+]([O-])=O)[C@H]1O[N+]([O-])=O)O[C@H]1[C@@H]([C@@H](O[N+]([O-])=O)[C@H](O[N+]([O-])=O)[C@@H](CO[N+]([O-])=O)O1)O[N+]([O-])=O)CO[N+](=O)[O-])[C@@H]1[C@@H](CO[N+]([O-])=O)O[C@@H](O[N+]([O-])=O)[C@H](O[N+]([O-])=O)[C@H]1O[N+]([O-])=O FJWGYAHXMCUOOM-QHOUIDNNSA-N 0.000 description 18
- 229920001220 nitrocellulos Polymers 0.000 description 18
- 229940079938 nitrocellulose Drugs 0.000 description 16
- 229920003043 Cellulose fiber Polymers 0.000 description 12
- 239000000243 solution Substances 0.000 description 12
- 238000006396 nitration reaction Methods 0.000 description 9
- 239000004627 regenerated cellulose Substances 0.000 description 8
- 239000002253 acid Substances 0.000 description 7
- 230000001172 regenerating effect Effects 0.000 description 7
- 230000014759 maintenance of location Effects 0.000 description 6
- ZOOODBUHSVUZEM-UHFFFAOYSA-N ethoxymethanedithioic acid Chemical compound CCOC(S)=S ZOOODBUHSVUZEM-UHFFFAOYSA-N 0.000 description 5
- 238000011065 in-situ storage Methods 0.000 description 5
- 230000000802 nitrating effect Effects 0.000 description 5
- 239000012991 xanthate Substances 0.000 description 5
- 239000003153 chemical reaction reagent Substances 0.000 description 4
- 229920002522 Wood fibre Polymers 0.000 description 3
- 238000002360 preparation method Methods 0.000 description 3
- 230000008929 regeneration Effects 0.000 description 3
- 238000011069 regeneration method Methods 0.000 description 3
- 239000002025 wood fiber Substances 0.000 description 3
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 2
- 238000003490 calendering Methods 0.000 description 2
- 238000010790 dilution Methods 0.000 description 2
- 239000012895 dilution Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- POAOYUHQDCAZBD-UHFFFAOYSA-N 2-butoxyethanol Chemical compound CCCCOCCO POAOYUHQDCAZBD-UHFFFAOYSA-N 0.000 description 1
- 229920000742 Cotton Polymers 0.000 description 1
- 229920000297 Rayon Polymers 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 1
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 description 1
- 241000838698 Togo Species 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 150000002148 esters Chemical class 0.000 description 1
- 239000004922 lacquer Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000007800 oxidant agent Substances 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 238000009738 saturating Methods 0.000 description 1
- 238000004513 sizing Methods 0.000 description 1
- WBHQBSYUUJJSRZ-UHFFFAOYSA-M sodium bisulfate Chemical compound [Na+].OS([O-])(=O)=O WBHQBSYUUJJSRZ-UHFFFAOYSA-M 0.000 description 1
- GRVFOGOEDUUMBP-UHFFFAOYSA-N sodium sulfide (anhydrous) Chemical compound [Na+].[Na+].[S-2] GRVFOGOEDUUMBP-UHFFFAOYSA-N 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 235000011149 sulphuric acid Nutrition 0.000 description 1
- 239000001117 sulphuric acid Substances 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08B—POLYSACCHARIDES; DERIVATIVES THEREOF
- C08B1/00—Preparatory treatment of cellulose for making derivatives thereof, e.g. pre-treatment, pre-soaking, activation
- C08B1/02—Rendering cellulose suitable for esterification
- C08B1/04—Rendering cellulose suitable for esterification for the preparation of cellulose nitrate
Definitions
- This invention relates to the preparation of a cellulose composition for esterification, being more especially related to the preparation of a composition for nitration, and has for its object the preparation of a composition which when nitrated has a low acid retention and gives a high yield of nitrocellulose.
- the object of the present invention is to produce a relatively strong, dense paper or tissue from mercerized cellulose fiber without the use of unmercerized fiber, whereby the desiderata of lower acid retention and higher yield may be realized; I have found that this object maybe attained by treating the mercerized fiber with a solution of nitrocellulose or with a cellulose derivative capable of being regenerated into cellulose, and then, if other than nitrocellulose be employed, regenerating the cellulose in situ on the fiber. For instance, a mercerized fiber paper may be formed, then passed'through a solution of cellulose xanthate, and the cellulose regenerated in' situ in the paper. The fibers thus become encased in and bonded togo to increase the strength and density of the paper. When a paper thus permeated with regenerated. cellulose is nitrated, it is found that the acid retention isappreciably lower, .and the nitrocellulose yield appreciably higher than when mercerized bulk pulp is nitrated.
- a mercerized fiber paper permeated with regenerated cellulose may be accomplished by several different procedures.
- one method of procedure may be substantially. as follows. Mercerized cellulose fiber is run out on a paper machine into thin sheets orrtissue. The paper thus formed is loose and bulky, but these characteristics may be made less pronounced by incorporating a small proportion of unmercerized fiber, either beaten or unbeaten but preferably the latter, intothe mercerized fiber. The paper is then saturated with a cellulose anthate solution of sufiicient cellulose concentration to yield about 2% to 5% regenerated cellulose, when regenerated in the paper. The paper is then partially or completely dried and immersed in a cellulose-regenerab ing reagent, e.
- a solution of sodium bisulphate and sulphuric acid toeftect a regeneration of cellulose in situ in the paper.
- the paper may then be washed, steeped, if desired, in a sulphur-removing reagent, e. g., a
- the dry paper is formed similarly to beater-sizing.
- cellulose xanthate solution is added to the mercerized fiber in the beater engine, and after it has been uniformly disseminated throughout the pulp, a regenerating reagent is added.
- the pulp may then be washed and run out on a paper machine into thin pa er, which is dried and preferably calendere
- the cellulose may also be regenerated from cellulose derivatives other than viscose.
- the regeneration of cellulose may occur from other esters or from cuprammo-- nium cellulose, but cellulose xanthate is preferred, because it is less expensive and easier to treat successfully.
- nitro-cellulose employed as the cellulose derivative, its regeneration into cellulose need not be effected, as no acidgrouping which might afiect nitration or the quality of the nitrocellulose is present in the paper. In suchcase, the
- mercerized fiber is treated with a solution of cellulose nitrate in an ether-alcohol mixture, for example, and the solvent then evaporated and recovered, thus leaving the fibers encased and bonded together with cellulose nitrate,
- the nitrocellulose may be regenerated into cellulose as is effected when cellulose derivatives other than nitrocellulose are employed. This may be accomplished, for example, by steeping the paper in a denitrating bath, e. g., a so dium sulphide solution, whereupon the paper may be washed and dried.
- a denitrating bath e. g., a so dium sulphide solution
- bulk mercerized fiber which has been treated with regenerated cellulose'or nitrocellulose when nitrated in bulk form gives improved results over bulk mercerized fiber alone.
- bulk mercerized fiber which has been treated with regenerated cellulose or nitro cellulose maybe fluifed mechanically tore-vVIS cotton linters, or may be formed as a relatively thick, loosely felted, uncompacted web on a Fourdrinier wire or a cylinder machine, and nitrated in. such form.
- the mercerized fiber has been prepared for nitration without the introduction of foreign materials which would be nitrated along with the cellulose and contaminate the nitrocellulose.
- the utility of the process herein described is that the advantage of mercerizing fiber in bulk form, as well as theadvantage arising from a desirable physical condition of fiber.v
- a composition comprising merceriz cellulose fiber and regenerated cellulose deposited on' said fiber.
- composition comprisin mercerized erivative deposited. on said fiber.
- a paper comprising mercerized cellulose fiber permeated with regenerated celluose.
- a paper comprising mercerized cellulose fiber permeated with a cellulose derivaive.
- a calendered paper comprising mercerized cellulose fiber permeated with regener-- ated cellulose.
- a process which comprises running mercerized fiber out on a paper machine, permeating the paper with a cellulose 'derlvative, and regenerating cellulose in situ in the paper.
- a process which comprises running meating the paper with a cellulose derivative, regenerating cellulose in situ in the paper, and nitrating the paper.
- a process which comprises running mercerized fiber out on a paper machine, saturating the paper with a solution of cellulose xanthate, drying the paper, regenerating cellulose in situ in the paper, and nitrating'the paper.
- a process step which comprises permeating paper composed of mercerized cellulose fiber, with a cellulose derivative.
- Y 13 The process step which comprises permeating paper composed of mercerized cellulose fiber, with regenerated cellulose.
- a process which comprises permeating 16 A process which comprises fixing regenerate-d cellulose on mercerized cellulose fiber, running the fiber out on a paper machine, and nitrating the paper.
- a process which comprises incorporating a solution of cellulose xanthate into mercerized cellulose fiber, adding a regenerating reagent to the fiber, thereby regenerating cellulose on the fiber; and running the fiber out on a paper machine. 7 In testimony whereof I aflixed my signature.
Landscapes
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Biochemistry (AREA)
- Materials Engineering (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Chemical Or Physical Treatment Of Fibers (AREA)
Description
Patented Jan. 29, 1929.
' UNITED STATES PATENT OFFICE.
GEORGE A. RICHTER, OF BERLIN, NEW HAMPSHIRE, ASSIGNOR T BROWN COMPANY OF BERLIN, NEW HAMPSHIRE, A CORPORATION OF MAINE.
CELLULOSE comrosmon non ESTERIFICATION "AND rnocnss or PREPARING SAME.
No Drawing.
This invention relates to the preparation of a cellulose composition for esterification, being more especially related to the preparation of a composition for nitration, and has for its object the preparation of a composition which when nitrated has a low acid retention and gives a high yield of nitrocellulose.
One process of preparing cellulose fiber for nitration is disclosed and claimed in application, Serial No. 140,677, filed October 9, 1926. In accordance with that process, wood fiber, but more particularly a high alpha cellulose wood fiber, is mercerized prior to nitration. When high alpha cellulose wood fiber is mercerized in bulk form, particularly in the presence of a small quantity of an oxidant, and then nitrated, the resulting nitrocellulose yields solutions of lower viscosity and of markedly better color than those prepared from nitrated, unmercerized fiber.
When mercerized fiber is nitrated in bulk form, however, the acid retention is appreciably higher, and the yield appreciably lower 2 than when unmercenzed fiber is first made into thin paper or tissue, which is then mercerized and nitrated as disclosed and claimed in application, Serial No. 140,675, filed October 9, 1926, by Milton 0, Schur and Royal H. Rasch. The quality of nitrocellulose obtainable from mercerized bulk fiber, and the i hysical and mechanical characteristics "of aments, films, lacquers, and kindred products prepared from such nitrocellulose, are,
5' however, apparently as good as when similar 5 fiber in tissue form is nitrated. Apparently, the higher acid retention and lower yield accompanyingthe nitration of mercerized bulk fiber are imputable to the higher absorptivity I 40 of the bulkfiber. Thus, owing to the higher retention of acid by the bulk her, a greater loss of the fiber apparently takes place during nitration and when after centrifuging it is submerged in water,-"my theory being that the wash water'efiects a slower dilution and washing out of the acid in the bulk fiber than when tissue is washed, and that during such slower dilution acidconcentrations are roduced in the bulk fiber, which favor 'a ydrolysis of nitrocellulose. "If, however, it
is attempted to form thin paper from the ,gether by regenerated cellulose, which serves Application filed March 3, 1927. Serial lilo. 172,567.
fiber, preferably in beaten condition, with the mercerized fiber.
The object of the present invention is to produce a relatively strong, dense paper or tissue from mercerized cellulose fiber without the use of unmercerized fiber, whereby the desiderata of lower acid retention and higher yield may be realized; I have found that this object maybe attained by treating the mercerized fiber with a solution of nitrocellulose or with a cellulose derivative capable of being regenerated into cellulose, and then, if other than nitrocellulose be employed, regenerating the cellulose in situ on the fiber. For instance, a mercerized fiber paper may be formed, then passed'through a solution of cellulose xanthate, and the cellulose regenerated in' situ in the paper. The fibers thus become encased in and bonded togo to increase the strength and density of the paper. When a paper thus permeated with regenerated. cellulose is nitrated, it is found that the acid retention isappreciably lower, .and the nitrocellulose yield appreciably higher than when mercerized bulk pulp is nitrated.
The production of a mercerized fiber paper permeated with regenerated cellulose may be accomplished by several different procedures. Thus, one method of procedure may be substantially. as follows. Mercerized cellulose fiber is run out on a paper machine into thin sheets orrtissue. The paper thus formed is loose and bulky, but these characteristics may be made less pronounced by incorporating a small proportion of unmercerized fiber, either beaten or unbeaten but preferably the latter, intothe mercerized fiber. The paper is then saturated with a cellulose anthate solution of sufiicient cellulose concentration to yield about 2% to 5% regenerated cellulose, when regenerated in the paper. The paper is then partially or completely dried and immersed in a cellulose-regenerab ing reagent, e. g., a solution of sodium bisulphate and sulphuric acid, toeftect a regeneration of cellulose in situ in the paper. The paper may then be washed, steeped, if desired, in a sulphur-removing reagent, e. g., a
sodium sulphide solution, again washed, and
finally dried. Preferably, the dry paper is formed similarly to beater-sizing. In such case, cellulose xanthate solution is added to the mercerized fiber in the beater engine, and after it has been uniformly disseminated throughout the pulp, a regenerating reagent is added. The pulp may then be washed and run out on a paper machine into thin pa er, which is dried and preferably calendere The cellulose may also be regenerated from cellulose derivatives other than viscose. For
instance, the regeneration of cellulose may occur from other esters or from cuprammo-- nium cellulose, but cellulose xanthate is preferred, because it is less expensive and easier to treat successfully. When nitro-cellulose is employed as the cellulose derivative, its regeneration into cellulose need not be effected, as no acidgrouping which might afiect nitration or the quality of the nitrocellulose is present in the paper. In suchcase, the
" mercerized fiber is treated with a solution of cellulose nitrate in an ether-alcohol mixture, for example, and the solvent then evaporated and recovered, thus leaving the fibers encased and bonded together with cellulose nitrate,
which serves to strengthenand density the .paper. The paper is then preferably calendered, as previously. Where, however, it is undesirable to allow nitrocellulose to remain in the paper, asfor instance where. such paper is to be stored or shipped, the nitrocellulose may be regenerated into cellulose as is effected when cellulose derivatives other than nitrocellulose are employed. This may be accomplished, for example, by steeping the paper in a denitrating bath, e. g., a so dium sulphide solution, whereupon the paper may be washed and dried.
While fiber made into paper gives the best results upon nitration, nevertheless bulk mercerized fiber whichhas been treated with regenerated cellulose'or nitrocellulose when nitrated in bulk form gives improved results over bulk mercerized fiber alone. For incellulose fiber and a cellulose stance, bulk mercerized fiber which has been treated with regenerated cellulose or nitro cellulose maybe fluifed mechanically tore-v semble cotton linters, or may be formed as a relatively thick, loosely felted, uncompacted web on a Fourdrinier wire or a cylinder machine, and nitrated in. such form.
In any of the procedures hereinbefore' given, the mercerized fiber has been prepared for nitration without the introduction of foreign materials which would be nitrated along with the cellulose and contaminate the nitrocellulose. The utility of the process herein described is that the advantage of mercerizing fiber in bulk form, as well as theadvantage arising from a desirable physical condition of fiber.v
when nitration is being efl'ected,*are both I realized. In plant practice, it is more economical to mercerize and wash pulp in 19.1 e quantities in bulk form and to recovert e mercerizing solution, rather than to mercerize thin paper or tissue. By the process of the present invention, the economical advantages of mercerizing fiber in bulk form are enjoyed, and at the same time a paper of good nitrating characteristics may be manufactured therefrom. 1
Having thus described certain embodiments of this-invention, it is obvious that these may be varied without departing from the spirit or scope of invention'as set forth in the appended claims.
What I claim is;
1. A composition comprising merceriz cellulose fiber and regenerated cellulose deposited on' said fiber.
2. A composition comprisin mercerized erivative deposited. on said fiber.
' 3. A paper comprising mercerized cellulose fiber permeated with regenerated celluose.
4. A paper comprising mercerized cellulose fiber permeated with a cellulose derivaive.
5. A calendered paper comprising mercerized cellulose fiber permeated with regener-- ated cellulose.
6. A process which comprises runnin mercerized fiber out on a paper machine, an
permeating the paper with a cellulose derivaive.
7. A process which comprises running mercerized fiber out on a paper machine, permeating the paper with a cellulose 'derlvative, and regenerating cellulose in situ in the paper.
8. A process which comprises running meating the paper with a cellulose derivative, regenerating cellulose in situ in the paper, and nitrating the paper.
10. A process which comprises running mercerized fiber out on a paper machine, saturating the paper with a solution of cellulose xanthate, drying the paper, regenerating cellulose in situ in the paper, and nitrating'the paper.
11. A process step which comprises permeating paper composed of mercerized cellulose fiber, with a cellulose derivative.
12. A process which comprises permeating paper composed of mercerized cellulose fiber, with a cellulose derivative; and nitrating the same. Y 13. The process step which comprises permeating paper composed of mercerized cellulose fiber, with regenerated cellulose.
14. A process which comprises permeating 16. A process which comprises fixing regenerate-d cellulose on mercerized cellulose fiber, running the fiber out on a paper machine, and nitrating the paper.
17. A process which comprises incorporating a solution of cellulose xanthate into mercerized cellulose fiber, adding a regenerating reagent to the fiber, thereby regenerating cellulose on the fiber; and running the fiber out on a paper machine. 7 In testimony whereof I aflixed my signature.
GEORGE A. RICHTER;
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US172567A US1700595A (en) | 1927-03-03 | 1927-03-03 | Cellulose composition for esterification and process of preparing same |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US172567A US1700595A (en) | 1927-03-03 | 1927-03-03 | Cellulose composition for esterification and process of preparing same |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US1700595A true US1700595A (en) | 1929-01-29 |
Family
ID=22628247
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US172567A Expired - Lifetime US1700595A (en) | 1927-03-03 | 1927-03-03 | Cellulose composition for esterification and process of preparing same |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US1700595A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2613672A (en) * | 1946-07-11 | 1952-10-14 | Int Cigar Mach Co | Tobacco sheet material and method of producing the same |
-
1927
- 1927-03-03 US US172567A patent/US1700595A/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2613672A (en) * | 1946-07-11 | 1952-10-14 | Int Cigar Mach Co | Tobacco sheet material and method of producing the same |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| DE737527C (en) | Process for the production of fibrous webs from cellulose fibers which have been esterified while maintaining their structure | |
| US1919623A (en) | Production of useful products from cellulosic materials | |
| US2243765A (en) | Treatment of cellulosic textile materials | |
| US2379264A (en) | Process for producing potentially adhesive textile fibers | |
| US2231953A (en) | Process for the treatment of organic fibrous materials | |
| US2014761A (en) | Process for the manufacture of solutions from cellulose | |
| US1700595A (en) | Cellulose composition for esterification and process of preparing same | |
| DE1141973B (en) | Process for reducing the swelling value and increasing the abrasion resistance of structures, such as fibers, threads or fabrics, made of native or regenerated cellulose | |
| US2152182A (en) | Manufacture and treatment of textile materials | |
| US2008021A (en) | Drying and converting cellulose into derivatives thereof | |
| US2068631A (en) | Preparation of cellulose xanthate solutions | |
| US2159676A (en) | Process of producing viscose | |
| US1700596A (en) | Composition for conversion into cellulose derivatives and process of preparing same | |
| US1701543A (en) | Process of conditioning cellulose fiber for conversion into cellulose derivatives, and product of same | |
| US2058427A (en) | Textile material | |
| US2174894A (en) | Process of swelling cellulose fiber sheets | |
| US1859889A (en) | Process of conditioning alpha tissue of cellulose fiber for conversion into celluloserivatives and product of same | |
| US1831197A (en) | Low viscosity cellulose fiber and process of making | |
| US2516267A (en) | Process of sizing textiles and composition therefor | |
| US1729628A (en) | Process of conditioning cellulosic material for preparation of cellulose derivatives and product of same | |
| US1866917A (en) | Manufacture of cellulose material from hemp fibers | |
| US1820198A (en) | Noninflammable fabric and process of making the same | |
| US1933676A (en) | Preparation of cellulose acetate and the like | |
| US2159643A (en) | Method for producing cellulose esters | |
| USRE19280E (en) | Viscose and process for making |