Moulded bodies, in particular fibres and the structures thereof exhibiting thermoregulation properties
a technology of thermoregulation properties and moulding bodies, which is applied in the direction of monocomponent protein artificial filaments, melt spinning methods, conjugated cellulose/protein artificial filaments, etc., can solve the problems of limited temperature regulation material in the entire fiber, low amount of temperature regulation material that can be inserted into the fiber, and comparatively low amount of phase change material that can be fixed to the surface of the structure. , to achieve the effect of enhancing the thermoregulation potential
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example 1
[0023] 15779 g of a 60%-solution of n-methylmorpholin-n-oxide are given into a dissolving vessel with agitator of 37 l volume together with 1160 g cellulose of an average polymerisation degree 500 and 464 g (=40% related to the employed amount of cellulose) micro-encapsulated phase change material of a phase change temperature of 28° C. (Thermasorb® TY 83 of Frisby Technologies Inc.) under addition of 6.8 g propylgallate. The micro-encapsulated phase change material has been screened before to a grain size of maximally 50 μm. The dissolving vessel will be evacuated to 20 mbar and is heated from 20° C. to 94° C. in the course of 6 hours at a stirrer RPM of 18 min−1 und the evaporating water is condensed in a connected condenser. The spinning solution obtained exhibits a viscosity of 1560 PAS and a refractive index of 1.484. At a spinning pump RPM of 25 min−1 the spinning solution is at 80° C. extruded through a spinneret having a number of nozzles of 150 and a nozzle diameter of 200 ...
example 2
[0025] 100 g casein are dispersed in 250 ml water and crosslinked by addition of 2 g glutaraldehyde and 0.1 g MgCl2 at 25° C. After squeezing out to a moisture content of 50%, the casein is suspended in 430 g of 60%-NMMNO. 0.5 g propylgallate are added as a stabilizer. 100 g of a micro-encapsulated phase change material such as, for example, Lurapret® TX PMC 28 from BASF AG are added to the suspension what corresponds to an amount of 100 weightpercent of phase change material related to the protein in the solution. The suspension is transferred into a spinning solution in a kneading machine with a jacket heating under a vacuum of 30 mbar and at a temperature of 90° C. by distilling off of 130 g water. The homogeneity of the spinning solution is checked with an optical microscope and turns out, as a rule, 15 minutes after the end of the distillation. The spinning solution is extruded at a spinning temperature of 80° C. in filaments through a spinneret having 150 nozzles each of a dia...
example 3
[0026] 50 g casein are dispersed in 250 ml water and crosslinked by addition of 1 g glutaraldehyde and 0.1 g MgCl2 at 25° C. After squeezing out to a moisture content of 50%, the casein is suspended in 430 g of 60%-NMMNO. Additionally 25 g of dry ground sulphite cellulose (DP 760) as well as 100 g of a micro-encapsulated phase change material such as, for example, Lurapret® TX PMC 28 from BASF AG are added. This corresponds to an amount of 133% PCM related to cellulose. 0.5 g propylgallate are added as a stabilizer. This suspension is transferred into a spinning solution in a kneading machine with a jacket heating under a vacuum of 30 mbar and at a temperature of 90° C. by distilling off of 140 g water. The homogenisation of the spinning solution is achieved 15 minutes after the end of the distillation and is checked with an optical microscope. The resulting spinning solution is extruded through a spinneret having 150 nozzles each of a diameter of 90 μm via an air slot into an aqueo...
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