• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    A process for producing shaped articles of cellulose is disclosed, wherein a solution of cellulose in dimethylsulphoxide (DMS0) and formaldehyde, at a formaldehyde/cellulose weight ratio of 0.2 to 2, and at a cellulose concentration of at least 6% by weight based on the volume of DMSO, is spun into a coagulant bath. The coagulant bath contains water, DMSO and ammonia or an ammonium salt, with the DMSO present in an amount of about 25 to 60 weight percent of the mixture of DMSO and water. The ammonia or ammonium salt is present in an amount, calculated as ammonia, of at least 1 gram per liter in the mixture of DMSO and water. The use of the coagulant bath of the present invention permits the cellulosic solution to be formed into shaped articles, and especially into filaments which are useful in the textile field. Other shaped articles which can be made from the cellulosic solution include fibers, threads, membranes, films, and sheets.
    公开号:SU797596A3
    申请号:SU772503806
    申请日:1977-07-15
    公开日:1981-01-15
    发明作者:Родье Анри
    申请人:Рон-Пуленк-Текстиль (Фирма)；
    IPC主号:
    专利说明:

    (54)
    METHOD OF OBTAINING FIBERS AND FILMS BASED ON CELLULOSE
    F® MSF ™
    ; EGE i 5 with agitation. The dissolution of cellulose, observed with a polarizing microscope, is complete. The viscosity of the solution is 559 P Pr 20®C. The number of undissolved particles (NP) is 90, and the breaking rate (Lo). This solution is subjected to extrusion through a filter with 200 holes of 0.055 mm in diameter into a sedimentation bath at 25 ° C, which is the water / DMSO mixture in a weight the proportions are 70:30, to which d is 5 g / l ammonia. The filaments pass 90 cm in the bath and then are mechanically removed with the aid on which they run several turns. The threads pass through two successive drafts between different pairs of cylinders, first by 32% in air, and second by 20% boiling water, with the circumferential speed of the last pair of cylinders being 15 m / min. Then they are washed in water, coated with oil before winding on bobbins and dried. The yarns have the following characteristics: Number, dtex 3.7 Condition specific strength, g / tex21.7 Condition elongation /% 11.4 Strength in wet state / g / tex 16.8 Elongation in wet condition ,% 13 P and M e R 2. Operate with the same solution as in example 1 at 120 s, in which dry nitrogen is bubbled in to bring the formaldehyde / cellulose wearing to .0.25. A solution with a viscosity of 590 P at and IP 84 is extruded at through a spinneret with 200 holes with a diameter of 0.055 mm and a precipitation bath at which is a water / DMSO mixture in a weight ratio of 70:30, to which is added 1.7 g / l ammonia. After passing 90 cm in the bath, the nrti are removed from it with the help of a x x undercut node, on which they describe several turns. They are then drawn as in Example 1, but at 24% in air and 21% in boiling water. After washing in water, oil. Vani, winding on a bobbin and drying, thread, have the following characteristics:. Number, dtex3.5 Specific strength in conditional condition, g / tex21.5 Elongation in conditional condition,% 11.8 Specific strength in wet state, g / tex 12 Elongation in wet state,% 13.4. Example 3. The procedure is the same as in Example 2, but with a precipitation bath, which is a water / DMSO mixture in a ratio of 70:30, but to which 39 g / l of ammonia is added. Air exhaust is 20%, while boiling water in air is 17%. The yarns obtained have the following characteristics: Number, dtex Specific strength in the conditioned state, g / tex Elongation in the conditioned state,% Specific strength in the wet state, g / tex Elongation in the wet state,% R & M 4 The same solution was used as in Example 1, and it was extruded, through the same die, into a precipitation bath, which was a water / DMSO mixture in a weight ratio of 53:47, to which 3.5 g / l of ammonia was added. Wetting in air is carried out by 23%, and Tweeter ,. in boiling water - by 15%. The circumferential speed on the last pair of cylinders is 14.5 m / min. Threads have the following characteristics: Number, dtex3 Specific strength in the conditioned state, g / tex20 Elongation in the conditioned state,% 13.5. Specific strength in the wet state, g / tex 12 Elongation in the wet state,% 15. P Example 5. The procedure is the same as / in example 1, but extrusion is carried out through a spinneret with 128 holes 0.05 mm in diameter into a precipitation bath at 35 ° C, which is a water / DMSO mixture in a weight ratio of 70 : 30 and containing 100 g / l of sesquio carbonate g mmoni: (ttH 1 / COj) HaO. Exhaust in the air is carried out at 36% and extraction in boiling water - at 10%. The yarns obtained have the following characteristics: Number dtex2 Specific strength in the conditioned state, g / tex 22 Elongation in the conditioned state,% 13
    Specific strength in the wet state, g / tex 13 Elongation in the wet state,% 15. Example. 80 g of Kraft bleached mass, dried at SP 1050 and 6% humidity, then added to 1000 cm DMSO (500 ppm of water) containing 94 g of 96% paraform hygene (formaldehyde / cellulose ratio 1.20).
    The mixture is brought to stirring for 1 h, then this temperature is maintained for 3 h all the time with stirring.
    In the resulting solution. Bleed a stream of dry nitrogen at up to the formaldehyde / cellulose ratio down to 0.30.
    The resulting solution has a viscosity of 2100 n at 20 ° CMp250 and 1c87.
    At 20 s, the solution is extruded through a 50-hole die with a diameter of 0.8 mm vertically into a funnel, from which it flows downwards into a precipitation bath at 17 s, which is a water / DMSO mixture at 70:30, to which 5 g / l ammonia. The spinning speed is 50 m / min, and the vertical passage of the filaments is 110 cm. Then the filaments are transferred to a mechanical organ, on which they perform several turns, are washed in water with irrigation at.
    After oiling and drying, the threads have the following characteristics: Number, dtex 2.5
    Selected fortress in air-conditioned state, g / tex 15 Elongation in conditioned state,% 20 Specific strength in wet state, g / tex 11 Elongation in wet state,% 2-8 Exit 7. The solution of example 1 was poured onto a glass plate and leveled using a doctor blade. The pulp is precipitated by means of a precipitation bath with, by representing a mixture of water / DMSO at 40% of the latter / to which 5 g / l of ammonia is added.
    A transparent film is obtained, which is washed in cold water with the elimination of the solvent, then immersed in a 2% aqueous solution of glycerin for 15 minutes, and dried on a plate of 500 ps.
    A film with a thickness of 0.090 m is obtained which is clear, light and colorless, having a form and characteristics close to the appearance and characteristics of cellophane.
    Example 8: 240 g of sulfate paste for viscose with SP 450, dried at 110 ° C for 12 hours, are added to 472 g of DMSO and 288 g of paraformaldehyde (the ratio of paraformal to
    dehydrate / cellulose 1,2). The temperature of the mixture was adjusted to 1300 s for 1 hour with slow stirring, then held at 3 hours. The dissolution of cellulose, observed in a polarizing microscope, is satisfactory (), the viscosity of the solution is 1200 P at 20 s. The ratsvor is filtered cold on a 50 micron nickel network under a pressure of 2 kg / cm.
    The solution is passed through a funnel (edge spacing: 14/100 mm) into a precipitation bath at 23 ° C, which is a water / DMSO mixture in a 70:30 proportion, to which 5 g / l of ammonia is added.
    After passing 13.5 cm in the bath (contact time 4 s), the mechanically transferred gel is washed in water at, then in water at room temperature and dried on a plate.
    Get a clear film with a thickness of 16 microns. Its appearance and characteristics are close to the appearance and characteristics of cellophane.
    Lost width and swelling gel
    5 less than in the viscose method.
    Example 9. Starting from the same solution as in Example 6.
    The solution was applied to the glass plate using a hand-held dispenser adjusted to a liquid film. Then the glass plate and the film are immersed in the precipitating bath prc,.
    5 which is a mixture of 60 hours of water, 25 hours of daSO2 and 20 hours of a 50% aqueous solution of NHo. Leave in the bath for 5 minutes, then wash the film for 1 hour in the distilled stream.
    0 water. A membrane with a thickness of 230 m is obtained. Its ultrafiltration properties are examined at a relative pressure of 2 bar, on the one hand, using pure water, and, on the other hand, using a solution at 5 g of bovalbumin.
    5 with a molecular weight of 70,000 per liter of aqueous solution at 9 g / l of NaCf and the degree of waste with this last solution is calculated by the formula:
    initial concentration 0 concentration of ultrafiltrate
    initial concentration X100 o / o
    The resulting costs are respectively 230 l / day / m for clean water and 222 l / day / m for bovalbumin saline. The degree of waste is 96%.
    PRI me R 10. 70 g of pulp with a degree of polymerization
    1500 and 6% humidity are introduced into 1000 cm of dimethyl sulfoxide containing 100 ppm of water and left overnight at room temperature. A portion of the dimethylsulfoxide 5 is distilled to remove the water and the volume is adjusted. Reduce the temperature to 130 ° C, then add 96 g of paraformaldehyde (formaldehyde / cellulose ratio 1, stirring. Maintain this temperature for 3 hours and 30 minutes while stirring.
    The resulting solution has a viscosity of 3300P when the number of insoluble particles is 100 and the compaction factor is 83. This solution is poured onto a glass plate as in Example 7 A clear, clear and colorless film is obtained.
    The proposed method allows fast coagulation of the filaments and is industrially applicable. The properties of the fibers are at the level of the properties of viscose fibers. invention formula
    The method of producing cellulose-based fibers and films by molding a solution of cellulose in an aqueous mixture of dimethyl sulfoxide and paraformaldehyde into a precipitation bath (characterized in that, in order to improve the process technology and the properties of fibers and films, a ratio of paraformaldehyde to cellulose 0.2-1.37, and as a precipitation bath, use an aqueous 23.8-47 wt.% dimethyl sulfoxide solution containing 0.175, 7% NHij by weight of the solution in the form of ammonium hydroxide or ammonium salts.
    Sources of information taken into account in the examination
    i.Johnson D.C.Choi son M.D. Haigh F.C. YPS Technical Paper, Series 5, 1975, Prototype.
    权利要求:
    Claims (1)
    [1]
    Claim
    A method of producing fibers and films based on cellulose by molding a cellulose solution in an aqueous mixture of dimethyl sulfoxide and paraformaldehyde into a precipitation bath, characterized in that, in order to improve the process technology and the properties of the fibers and films, a 7-10% cellulose solution is used with a ratio of paraformaldehyde to cellulose 0. 2-1.37, and an aqueous 23.8-47 wt.% Solution of dimethyl sulfoxide containing 0.175.7% NH ^ of the weight of the solution in the form of ammonium hydroxide or ammonia salts is used as a precipitation bath.
    Sources ’information taken into account during the examination
    Ϊ.Johnson D. C.; Nicholson M.D. ,
    Haigh F.C. YPS Technical Paper,
    Series 5, 1975, prototype.
    类似技术:
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    同族专利:
    公开号 | 公开日
    NO147674C|1983-05-25|
    NL179223B|1986-03-03|
    DD131029A5|1978-05-24|
    BR7704612A|1978-06-06|
    MX147366A|1982-11-24|
    JPS6028846B2|1985-07-06|
    CA1078570A|1980-06-03|
    FI63972C|1983-09-12|
    PT66816B|1978-12-21|
    NO772531L|1978-01-17|
    PT66816A|1977-08-01|
    DE2732176C3|1981-08-13|
    FI772206A|1978-01-17|
    NL179223C|1986-08-01|
    SE7708259L|1978-01-17|
    CH624418A5|1981-07-31|
    ATA518177A|1979-07-15|
    DE2732176B2|1980-12-04|
    FI63972B|1983-05-31|
    BE856877A|1978-01-16|
    IT1081292B|1985-05-16|
    JPS5327647A|1978-03-15|
    FR2358432B1|1979-01-19|
    NL7707934A|1978-01-18|
    AT355182B|1980-02-25|
    OA06113A|1981-06-30|
    SE420613B|1981-10-19|
    US4173613A|1979-11-06|
    DE2732176A1|1978-01-19|
    ES460789A1|1978-05-01|
    FR2358432A1|1978-02-10|
    GB1540045A|1979-02-07|
    NO147674B|1983-02-14|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    US3236669A|1963-04-19|1966-02-22|Du Pont|Cellulose solutions in dimethyl sulfoxide and nitrogen dioxide|
    US3706526A|1971-12-06|1972-12-19|Cotton Inc|Process for treating cellulosic material with formaldehyde and sulfur dioxide|
    US4022631A|1975-05-19|1977-05-10|International Telephone And Telegraph Corporation|Process for producing regenerated cellulosic articles|
    US4044090A|1975-07-09|1977-08-23|International Telephone And Telegraph Corporation|Process for producing regenerated cellulosic product|
    US4028132A|1975-11-25|1977-06-07|International Playtex, Inc.|Cellulose solutions and products prepared therefrom|IT7826174D0|1978-07-27|1978-07-27|Snia Viscosa|PROCEDURE FOR THE PREPARATION OF BODIES FORMED OF REGENERATED CELLULOSE FROM SOLUTIONS OF CELLULOSE DERIVATIVES IN DIMETHYLSULPHOXIDE.|
    IT1112577B|1979-04-24|1986-01-20|Snia Viscosa|PROCESS PROCESSING FOR THE PREPARATION OF BODIES FORMED OF CELLULOSE REGENERATED FROM SOLUTIONS OF CELLULOSE DERIVATIVES IN ORGANIC SOLVENTS|
    FR2478116B1|1980-03-14|1985-06-14|Rhone Poulenc Textile|CONFORMABLE SOLUTIONS FROM CELLULOSE AND POLYAMIDE-IMIDE MIXTURES AND FORMAL ARTICLES OBTAINED|
    FI60569C|1980-03-28|1982-02-10|Valtion Teknillinen|FOERFARANDE FOER TILLVERKNING AV REGENERERADE CELLULOSAPRODUKTER OCH AOTERVINNING AV LOESNINGSKEMIKALIER|
    FR2483966B1|1980-06-10|1984-02-17|Rhone Poulenc Textile|
    JPS6254042B2|1982-11-18|1987-11-13|Terumo Corp|
    DE4134190A1|1991-10-16|1993-04-22|Tomka Ivan|METHOD FOR IMPROVING THE MECHANICAL PROPERTIES OF ONE-OR MULTILAYER FOILS|
    FR2748277B1|1996-05-06|1998-07-31|Elysees Balzac Financiere|PROCESS FOR MANUFACTURING CELLULOSIC ALVEOLAR PRODUCTS CELLULOSIC ALVEOLAR PRODUCTS|
    DE19623703C1|1996-06-14|1997-07-24|Freudenberg Carl Fa|Cellulose@ sponge production from acetylated cellulose|
    DE19623704C1|1996-06-14|1997-06-26|Freudenberg Carl Fa|Preparation of cellulose sponge cloth free from sulphur compounds|
    US5962005A|1997-04-17|1999-10-05|Rengo Co., Ltd|Transparent cellulose hydrogel and production process thereof|
    GB0020852D0|2000-08-24|2000-10-11|Ucb Sa|Cellulosic films and uses thereof|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    FR7622032A|FR2358432B1|1976-07-16|1976-07-16|
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