摘要:
A method of recycling a mixed textile, wherein the method comprises: i) supplying the mixed textile, wherein the mixed textile comprises cellulosic fibers and synthetic fibers, wherein the synthetic fibers comprise at least one synthetic plastic, ii) at least partially depleting the synthetic plastic from the cellulose, and iii) further processing the depleted mixed textile after depleting.
摘要:
A fabrication of natural cellulose fiber with flame-retarding capability comprises following steps. Blend pulp and solvent of N-methylmorpholine N-oxide (NMMO) to form slurry. Evaporate extra water content from slurry by a Thin Film Evaporator (TFE) to form dope. By Dry-Jet Wet Spinning, spin and extrude dope for coagulating and regenerating. Water-rinse and dry to form natural cellulose fiber. Soaking roll natural cellulose fiber by flame retardant of N-(hydroxymethyl)-3-(methoxy phosphorus acyl). Orderly dry, bake, neutralize, soaping clean, water rinse, baking dry, soaking rolled, alkaline clean, water rinse, dry and oil the natural cellulose fiber to produce natural cellulose fiber of flame retarding capacity. Because of cross-linking reaction for the flame retardant of N-(hydroxymethyl)-3-(methoxy phosphorus acyl) with natural cellulose fiber, the flame-retarding capability thereof meet requirements of testing standards in American ASTM D6413-1999 and ASTM D2863-1995. Moreover, the wastes thereof meet the requirements of environment protections without harm.
摘要:
The invention is concerned with a process for the purification of an aqueous solution of a tertiary amine-oxide containing impurities partially present in a dissolved and partially in a non-dissolved, colloidal state, and is characterized by a combination of the steps of (A) removing from the aqueous solution substantially all of said impurities present in a non-dissolved, colloidal state and (B) contacting said aqueous solution obtained in step (A) with an ion exchanger.
摘要:
An aqueous N-methylmorpholine-N-oxide solution which was used as a spinning bath in the production of cellulosic products is regenerated by contacting it with active coal, silicon dioxide or alumina adsorbent and filtering, thereby reducing turbidity, eliminating nitrosoamine, decolorizing the solution and removing transition metals like iron therefrom.
摘要:
There is disclosed a process for purifying aqueous solutions of N-methyl-morpholine N-oxide (NMMO), such as spinning bath solutions incurred in the production of cellulose products, in which process the solutions to be purified are contacted with an anion exchanger and the purified solutions are separated from the anion exchanger. The process is carried out in one step and the anion exchanger, as functional groups, exclusively contains quaternary tetraalkylammonium groups of the formulae--CH.sub.2 --N.sup..sym. (CH.sub.3).sub.3 X.sup..crclbar. or --CH.sub.2 --N.sup..sym. [(CH.sub.3).sub.2 (CH.sub.2 OH)]X.sup..crclbar.wherein X.sup..crclbar. represents the anion of an inorganic or organic acid. After this, the anion exchanger is regenerated with an aqueous acidic solution.
摘要:
A process is described for increasing the sulfuric acid concentration of solutions containing an alkali metal sulfate, sulfuric acid and alkaline earth metal ions. The solutions to be worked up are introduced into the anode compartment of an electrolysis cell. The anode compartment and the cathode compartment of the cell are each bounded by a cation exchange membrane. A center chamber is located between the two membranes. This center chamber is filled with an aqueous solution containing alkali metal ions. The concentration of alkaline earth metal ions in the solution in the center chamber must be kept below 5 mg/l during the electrolysis.
摘要:
A process and apparatus for converting alkali metal sulfate values, such as sodium or potassium sulfate values in spent rayon spin bath liquors, into alkali metal hydroxide and alkali metal sulfate/sulfuric acid by using two- or three-compartment electrodialytic water splitter cells. The process and apparatus incorporate the features of: (a) feeding a liquid comprising water to the base compartment of an electrodialytic water splitter, (b) feeding a liquid comprising alkali metal sulfate values to the remaining compartments of the electrodialytic water splitter (c) passing current through said electrodialytic water splitter to produce liquid comprising alkali metal sulfate and sulfuric acid in one of the remaining compartments and a liquid comprising alkali metal hydroxide in said base compartment. The liquid fed to the acid compartments of two- and three-compartment cells may contain H.sub.2 SO.sub.4. When more than about 5 weight percent H.sub.2 SO.sub.4 is present in the alkali metal sulfate solution use of a three-compartment water splitter is preferred. Improved results are obtained when the compartments of the two- and three-compartment water splitter are maintained at a temperature of at least 40.degree. C.
摘要翻译:通过使用二室或三室电渗析水分离器电池,将碱性金属硫酸盐值如废人造丝旋转浴液中的硫酸钠或硫酸钾值转化为碱金属氢氧化物和碱金属硫酸盐/硫酸的方法和装置。 该方法和装置包括以下特征:(a)将包含水的液体供给电渗析水分离器的基室,(b)将含碱金属硫酸盐值的液体供给电渗析分水器(c)的其余隔室, 使电流通过所述电渗析水分离器以产生其余一个隔室中的碱金属硫酸盐和硫酸的液体,以及在所述基室中含有碱金属氢氧化物的液体。 进料到两室和三室细胞的酸室的液体可能含有H2SO4。 当碱金属硫酸盐溶液中存在大于约5重量%的H 2 SO 4时,优选使用三室分水器。 当两室和三室水分离器的隔室保持在至少40℃的温度时,可获得改进的结果。
摘要:
Apparatus for spinning viscose rayon comprising an acid bath having an enclosure arranged for substantially completely trapping and collecting any gases emanating from said bath, a plurality of fiber-forming jets disposed substantially along beneath the surface of said acid bath, means for forcing aqueous xanthated alkali cellulose in liquid form into said jets and through said jets upwardly into said bath, and take-up means located within said enclosure above said bath for taking up the resulting fibers in an upward direction within said enclosure, and thence through an enclosed secondary hot bath for the purpose of stretching the cellulose-xanthate, regenerating it to cellulose, and for trapping and collecting gases and other chemicals.
摘要:
Liquid, e.g. synthetic film-spinning material, is introduced at 2 in the figure (not shown), to a vessel where it is mixed with granules of polyvinyl chloride introduced from a dosing device 3. The mixture is pumped (4) to a filter 1 furnished with horizontal filter elements each provided at the top only with metal fabric and covered already with a mixture of P.V.C. granules and viscose. When the pressure difference is excessive, filtration is interrupted and the contents of the filter passed back to the container for the liquid (not shown). The filter cake on the elements is freed from viscose by compressed air introduced at 5 and is then washed with water from pipe 6. Next, the elements are rotated by motor 7 to throw off the cake and suspend it in a little water, the resulting suspension being fed to an agitator 8 where soda lye is introduced from a container 9 and heating is effected by introducing steam. The suspension is agitated and pumped (10) to the inside of a screen 12 rotating partly submerged in water in a conical vessel 11. Here, impurities float off into a funnel 14, while the P.V.C. granules sink through the screen, and are dehydrated in a suction strainer or centrifuge 13 for return to the dosing device 3. Instead of P.V.C. there may be used polyethylene, polypropylene, polyacrylonitrile, metal powder or metal chips.