Disclosure of Invention
Aiming at the problems that the sealing performance of the existing heating facial mask is higher due to the fact that a heating material reacts with air, and the heat of the heating material exposed in the air is rapidly dissipated, the invention aims to provide the sandwich facial mask capable of producing hydrogen, generating heat and preserving heat, which generates heat in the hydrogen production process, has good stability when placed in the air and high heat preservation performance.
The invention provides the following technical scheme:
a sandwich facial mask capable of producing hydrogen, generating heat and preserving heat comprises a surface base material layer, a water-permeable bottom base material layer and a hydrolysable hydrogen production material arranged between the surface base material layer and the bottom base material layer;
the outer surface of the surface base material layer is also provided with a heat-insulating layer;
the hydrolysable hydrogen production material is solid powder and comprises 10-90 parts by weight of at least one of sodium borohydride and metal hydride, 5-60 parts by weight of neutralizing agent and 5-50 parts by weight of adsorbing material.
Compared with the prior art, the facial mask is provided with the surface base material layer and the water-permeable bottom base material layer, the hydrolysable hydrogen production material is arranged between the surface base material layer and the bottom base material layer, the heat insulation layer is arranged on the outer side of the surface base material layer, the hydrolysable hydrogen production material can contact with water or alcohol to react to generate hydrogen and generate heat, and when the facial mask is used, one side of the bottom base material layer of the facial mask is wetted or the face is coated with water and then wetted to provide water required by the reaction. Therefore, the hydrolyzable hydrogen-producing material needs to react with water or alcohol, the stability of the mask in the air is improved, the sealing process requirement is reduced, the hydrolyzable hydrogen-producing material is positioned in the middle, the heat dissipation to the air is slow, the heat loss is low, and the heat loss of heat generated by the reaction of the hydrolyzable hydrogen-producing material is further reduced by the heat-insulating layer.
As the improvement of the invention, the metal hydride is at least one of calcium hydride, lithium hydride and sodium hydride with the grain diameter of 0.5-500 μm. The specific surface area of the powdered metal hydride contacted with water is large, and the efficiency of hydrogen production by hydrolysis can be improved.
As the improvement of the invention, the neutralizing agent is at least one of citric acid, oxalic acid and phosphoric acid solid powder with the grain diameter of 1-500 mu m; the adsorbing material is at least one of diatomite with the particle size of 1-500 mu m, a molecular sieve, zeolite, active carbon and foamy carbon solid powder. Citric acid and the like can neutralize alkaline substances generated by the reaction of metal hydride or sodium borohydride, maintain the neutral environment of the mask and reduce the reaction irritation of the mask. The adsorbent material provides reaction sites and can adsorb and remove the smell in the hydrogen gas.
As a modification of the invention, the hydrolyzable hydrogen production material also comprises 2 to 5 parts of hydrophilic fumed silica with the particle size of 20 to 100 nm. The hydrophilic nano silicon dioxide has extremely strong hydrophilic performance, can assist water capture, enhances the water capture and wetting capacity of the hydrolysable hydrogen production material, and improves the reaction efficiency. Meanwhile, the hydroxyl on the surface of the hydrophilic nano silicon dioxide has low activity and is not enough to react with sodium borohydride or metal hydride, so that the stability of the hydrolyzable hydrogen production material is ensured.
As an improvement of the invention, the metal hydride or the sodium borohydride is used after being treated by the following processes: adding hydrophilic fumed silica with the particle size of 20-100 nm into an acetone solution with the concentration of 10-40 g/L of polyethylene glycol to uniformly disperse, wherein the dispersion concentration is 10-25 g/L, then dispersing metal hydride or sodium borohydride into the acetone solution with the dispersion concentration of 50-450 g/L, standing, evaporating, dissolving, drying and crushing to obtain the treated metal hydride or sodium borohydride. The hydroxyl contained in the polyethylene glycol has low reaction activity and cannot react with sodium borohydride or metal hydride, but the polyethylene glycol has good hydrophilic performance and is beneficial to enhancing the water capturing capacity of the hydrolysable hydrogen production material. The inventor finds that the stability of the hydrolyzable hydrogen production material treated by the process is obviously enhanced within a period of time, probably because the polyethylene glycol has a long-chain structure and is fully dissolved in acetone, the long-chain structure of the polyethylene glycol is wound with the hydrophilic nano-silica and the hydrogen-containing compound and generates a synergistic effect with the three-dimensional network structure of the hydrophilic nano-silica, so that the bonding strength of the hydrophilic fumed silica and the metal hydride or the sodium borohydride is improved, and meanwhile, the effects of water accumulation and water accumulation (lake formation) are achieved in the presence of a large amount of water, and the hydrogen production reaction is promoted; in a dry air environment, the metal hydride or the sodium borohydride and the hydrophilic nano silicon dioxide jointly play a role in water binding, and the contact reaction of the metal hydride or the sodium borohydride and water is prevented. However, as the standing time is increased, water accumulation and water accumulation are increased, and when water absorption reaches a certain degree, the contact chance of the metal hydride or sodium borohydride and water is increased, so that the stability is reduced after the proper standing time is exceeded, and the hydrogen production effect is reduced.
As the improvement of the invention, the surface substrate layer is one of non-woven fabric, plastic film and cotton cloth; the bottom surface base material layer is one of a non-woven fabric, a cotton cloth and a permeable film with water permeability; the heat-insulating layer is made by coating aluminum powder or silver powder on the outer side surface of the surface substrate layer. The heat-insulating layer is made of aluminum powder or silver powder, cannot be consumed along with reaction, and is stable in heat-insulating capacity.
As the improvement of the invention, the bottom surface substrate layer and the surface substrate layer are correspondingly jointed at the outer edge, the edge of the eye hole, the edge of the nose hole and the edge of the mouth hole respectively; the bottom surface base material layer and the surface base material layer are uniformly distributed with a plurality of joints at respective non-edges; and the mutually corresponding joint of the bottom surface base material layer and the surface base material layer is pressed to form a pattern consisting of pressing lines and/or pressing surfaces.
A method for preparing the sandwich facial mask comprises the following steps:
(1) Coating aluminum powder or silver powder on one side surface of the surface base material layer to form a heat insulation layer;
(2) Laying a hydrolysable hydrogen production material on the other side surface of the surface base material layer according to a set thickness;
(3) Laying the bottom surface base material layer on the horizontally spread hydrolyzable hydrogen production material to obtain a three-layer sandwich structure;
(4) Carrying out lamination treatment on the three-layer sandwich structure obtained in the step (3) to obtain a one-piece sandwich membrane with laminated patterns;
(5) And (5) cutting the sandwich membrane obtained in the step (4) to obtain the sandwich facial mask.
As an improvement of the method, the thickness of the sandwich facial mask is 0.6-10 mm.
The method for using the sandwich facial mask is characterized by comprising the following steps of:
(1) Pasting other facial masks containing pure water or water and glycerol on the outer side surface of the bottom surface base material layer of the Wen Gaxin facial mask or uniformly spraying a certain amount of water or solution or emulsion taking water as a main component on the outer side surface of the bottom surface base material layer;
(2) Attaching the outer side surface of the bottom surface base material layer of the sandwich facial mask treated in the step (1) to the face;
(3) Keeping the attaching for 10-15 minutes, then taking down the sandwich facial mask, and then washing the face with clean water.
The sandwich facial mask provided by the invention is matched with moisture or wet moisture provided by other facial masks to react, heat is provided and hydrogen is generated, and the sandwich facial mask can be directly washed by clear water after being used.
The invention has the following beneficial effects:
the sandwich facial mask disclosed by the invention can generate hydrogen production reaction after contacting with water, releases heat, is low in heat loss and high in storage stability in air, and the hydrogen production material is independently arranged between the bottom surface base material layer and the surface base material layer, so that other nutrient components can be prevented from being polluted and prevented from being polluted.
Detailed Description
The following further describes the embodiments of the present invention.
The starting materials used in the present invention are commercially available or commonly used in the art, unless otherwise specified, and the methods in the following examples are conventional in the art, unless otherwise specified.
The sandwich facial mask has the following structure:
a sandwich facial mask capable of generating hydrogen, generating heat and preserving heat comprises a surface base material layer 1, a water-permeable bottom surface base material layer 3 and a hydrolysable hydrogen production material layer 2 arranged between the surface base material layer and the bottom surface base material layer, wherein the hydrolysable hydrogen production material layer is formed by filling and laying solid powdered hydrolysable hydrogen production materials between the surface base material layer and the bottom surface base material layer in a pressing mode, and a heat preservation layer 4 is arranged on the outer surface of the surface base material layer.
Wherein, the surface substrate layer is a non-woven fabric layer, and can be replaced by a plastic film layer or a cotton fabric layer; when the surface base material layer is a plastic film layer, the plastic film is preferably made of food-grade PP plastic. The bottom surface base material layer is a permeable film layer, and can be replaced by a permeable non-woven fabric layer or a permeable cotton fabric layer; the heat-insulating layer is made by coating aluminum powder on the outer surface of the surface base material layer, and can be coated with silver powder instead.
As shown in fig. 2 and 3, the bottom surface substrate layer and the surface substrate layer of the sandwich facial mask are correspondingly jointed at the outer edge, the edge of the eye hole, the edge of the nose hole and the edge of the mouth hole respectively, and a plurality of joints are uniformly distributed at the non-edge of each layer; the bottom surface base material layer and the surface base material layer are pressed at the joint corresponding to each other to form a pattern consisting of pressing lines 5 and a pressing surface 6.
The preparation method of the sandwich facial mask comprises the following steps:
(1) Coating aluminum powder or silver powder on one side surface of the surface substrate layer to form a heat-insulating layer with the thickness of 0.2 mm;
(2) Uniformly paving a hydrolyzable hydrogen production material on the other side surface of the surface base material layer according to a set thickness to form a hydrolyzable hydrogen production material layer with the thickness of 0.3mm;
(3) And laying the bottom surface base material layer on the horizontally spread hydrolyzable hydrogen production material, and correspondingly jointing the bottom surface base material layer and the surface base material layer at the outer edge, the eye hole edge, the nose hole edge and the mouth hole edge respectively to obtain a three-layer sandwich structure. The thickness of the bottom surface base material layer is 0.15mm;
(4) Carrying out lamination treatment on the three-layer sandwich structure obtained in the step (3) to obtain a one-piece sandwich membrane with lamination patterns, wherein the total thickness is 0.9mm, so that the bottom surface substrate layer and the surface substrate layer are uniformly jointed at non-edges to form uniformly distributed joints, patterns consisting of lamination lines and lamination faces are generated, and the thickness of a surface membrane at the lamination patterns is 0.6mm;
(5) And (5) cutting the sandwich membrane obtained in the step (4) to obtain the sandwich facial mask.
It should be noted that the thickness of the sandwich face film is determined by the thickness of the bottom surface base material layer, the heat insulation layer and the laid hydrolyzable hydrogen production material, and the suitable thickness range of the whole laminated face film is 0.6-1 mm.
The composition of the hydrolyzable hydrogen-producing material of the sandwich mask of the present invention is shown in the following examples, but is not limited to the scheme of the following examples.
Example 1
The first hydrolysable hydrogen-producing material comprises 5g of a mixture of 20g of calcium hydride powder with the particle size of 70 microns, 45g of citric acid with the particle size of 200 microns and 35g of diatomite with the particle size of 100 microns;
the mixture is prepared by crushing and uniformly mixing citric acid and diatomite, drying at 60 ℃, cooling, mixing and crushing with calcium hydride, and uniformly mixing in a mixer at the rotating speed of 500rpm for 10 min.
(1) Hydrogen production Capacity test
0.10g of the hydrolysable hydrogen production material of example 1 was subjected to contact reaction with 20mL of water mist formed by pure water, 50wt% water +30wt% glycerol +20wt% propylene glycol, and 20wt% water +50wt% glycerol +30wt% propylene glycol, the volume of hydrogen produced was measured, the hydrogen production amount was calculated, and then a hydrogen production curve of hydrogen production amount versus time was plotted, to obtain a hydrogen production curve (— tangle solidup-), which was reacted with water mist formed by 50wt% water +30wt% glycerol +20wt% propylene glycol (- ● -), and a hydrogen production curve (- ■ -), which was reacted with water mist formed by 20wt% water +50wt% glycerol +30wt% propylene glycol, as shown in fig. 4.
As can be seen from fig. 4, the hydrolyzable hydrogen producing material can react with the water mist formed by the mixed solution of water, and glycerin and propylene glycol, and the time to reach the maximum hydrogen production amount is rapid. Meanwhile, the reaction capability of the water mist formed by the hydrolysable hydrogen production material and water is stronger than that of the water mist formed by the alcohol-containing solution, the reaction is rapid, and the maximum hydrogen production amount is high.
(2) Stability on standing test
The hydrogen-producing hydrolyzable material of example 1 was exposed to a clean environment at 25 ℃ and a relative humidity of 45% for a certain period of time, and then 0.1g of the hydrogen-producing hydrolyzable material was reacted with 20mL of water mist formed by 50% water, 30% glycerol and 20% propylene glycol at 20 ℃ to plot hydrogen-producing curves at different standing times: 0 days of air exposure (- ■ -: hollow), 2 months of air exposure (- ● -: hollow), 4 months of air exposure (-a solidup), 6 months of air exposure
Exposing to air for 8 months
The results are shown in FIG. 5.
It can be seen from the figure that, as the standing time increases, the maximum hydrogen production amount gradually decreases, and the maximum hydrogen production amounts of 2 months, 4 months, 6 months and 8 months of exposure relatively decrease by about 2.6%, 8.5%, 12.0% and 15.4%, so that the hydrogen production capacity after being exposed in the air for 8 months still maintains more than eight times, and the hydrolysis hydrogen production efficiency is higher.
Example 2
A second hydrolyzable hydrogen production material, which is different from the second hydrolyzable hydrogen production material in example 1 in that the adsorbing material is molecular sieve Na 2 O·3(Al 2 O 3 )·5(SiO 2 )·8(H 2 O)。
The hydrogen production capacity and the standing stability of the hydrolyzable hydrogen producing material prepared in this example are comparable to those of example 1.
Example 3
A third material capable of hydrolyzing hydrogen production, which is different from the third material in example 1 in that oxalic acid is used as a neutralizing agent.
Example 4
And the fourth hydrolysable hydrogen-producing material comprises 5g of a mixture of 30g of calcium hydride powder with the particle size of 70 μm, 55g of citric acid with the particle size of 200 μm and 15g of diatomite with the particle size of 100 μm.
The hydrogen production capacity and the shelf stability of the hydrolyzable hydrogen production material prepared in this example are comparable to those of example 1.
Example 5
And the hydrolysable hydrogen-producing material five comprises 5g of a mixture of 20g of sodium borohydride powder with the particle size of 70 mu m, 45g of citric acid with the particle size of 200 mu m and 35g of kieselguhr with the particle size of 100 mu m.
The hydrolyzable hydrogen-producing material prepared in this example has a shelf stability comparable to that of example 1, and the hydrogen production rate at the start of the reaction is relatively reduced compared to example 1, but the hydrogen production capacity can reach and exceed that of example 1 over a longer reaction time.
Example 6
A sixth hydrolysable hydrogen production material, which is different from the sixth hydrolysable hydrogen production material in the embodiment 1 in that the calcium hydride powder in the mixture has the mass of 35g and the particle size of 100 μm; the mass of the citric acid powder is 30g, and the particle size is 20 mu m; the diatomaceous earth powder had a mass of 45g and a particle diameter of 200. Mu.m.
The hydrogen production capacity and the shelf stability of the hydrolyzable hydrogen production material prepared in this example are comparable to those of example 1.
Example 7
A hydrolysable hydrogen production material seven, which is different from the embodiment 1 in that the mixture also comprises 2g of hydrophilic gas-phase nano silicon dioxide with the particle size of 20 nm.
The mixture is prepared by the following processes: weighing calcium hydride, citric acid and diatomite according to the formula ratio, firstly crushing and uniformly mixing the citric acid and the diatomite, then drying at 60 ℃, then uniformly mixing calcium hydride powder and hydrophilic gas phase nano-silica, cooling the materials for two times, then mixing and crushing, and then uniformly mixing in a mixer at the rotating speed of 500rpm for 10 min.
Compared with the hydrogen production material prepared in the example 1, the hydrogen production rate is equivalent, the maximum hydrogen production amount is improved by 2%, and the hydrogen production capacity after the hydrogen production material is exposed in the air for 8 months is reduced by 13.5%.
Example 8
The mixture comprises 20g of calcium hydride powder with the grain diameter of 70 mu m, 45g of citric acid with the grain diameter of 200 mu m and 35g of diatomite with the grain diameter of 100 mu m;
wherein the calcium hydride powder is used after being treated by the following processes: dispersing hydrophilic gas phase nano silicon dioxide with the particle size of 20nm in acetone solution with the concentration of 10g/L of polyethylene glycol, wherein the dispersion concentration is 12.5g/L, the ultrasonic dispersion is uniform, the ultrasonic power is 45w, the ultrasonic time is 90 minutes, then, uniformly dispersing calcium hydride powder in the acetone solution with the dispersion concentration of 50g/L, standing at room temperature for 24 hours, evaporating the solvent, drying and crushing to obtain the treated calcium hydride.
The mixture is prepared by the following processes: weighing calcium hydride, citric acid and diatomite according to the formula ratio, firstly crushing and uniformly mixing the citric acid and the diatomite, then drying at 60 ℃, cooling, then mixing and crushing with the treated calcium hydride, and then uniformly mixing in a mixer at the rotating speed of 500rpm for 10 min.
The hydrogen production rate of the hydrolysable hydrogen production material obtained in the embodiment is equivalent to that of the hydrolysable hydrogen production material obtained in the embodiment 1, the maximum hydrogen production is improved by 3.5%, and the hydrogen production capacity is reduced by 9.3% after the hydrolysable hydrogen production material is placed for 8 months.
Example 9
A hydrolyzable hydrogen producing material nine differs from example 8 in that the concentration of the acetone solution of polyethylene glycol during the calcium hydride powder treatment is 40g/L, the dispersion concentration of the calcium hydride powder is 25g/L, and the dispersion concentration of the calcium hydride powder is 100g/L.
The hydrogen production rate of the hydrolysable hydrogen production material of the embodiment is equivalent to that of the embodiment 1, the maximum hydrogen production amount is improved by 3.7%, and the hydrogen production capacity is reduced by 8.8% after the hydrolysable hydrogen production material is placed for 8 months.
Example 10
The material for preparing hydrogen can be hydrolyzed, and is different from the material in the embodiment 8 in that the mass of the calcium hydride powder used in the mixture is 25g, the concentration of acetone solution of polyethylene glycol in the treatment of the calcium hydride powder is 20g/L, the dispersion concentration of the calcium hydride powder is 10g/L, and the dispersion concentration of the calcium hydride powder is 40g/L.
The hydrogen production rate of the hydrolysable hydrogen production material of the embodiment is equivalent to that of the embodiment 1, the maximum hydrogen production is improved by 3.8%, and the hydrogen production capacity is reduced by 8.5% after the hydrolysable hydrogen production material is placed for 8 months.
Example 11
The difference from example 8 is that the adsorbent used is molecular sieve Na 2 O·3(Al 2 O 3 )·5(SiO 2 )·8(H 2 O)。
The hydrogen production rate of the hydrolysable hydrogen production material prepared in the embodiment is equivalent to that of the hydrolysable hydrogen production material prepared in the embodiment 1, the maximum hydrogen production amount is improved by 3.0%, and the hydrogen production capacity after the hydrolysable hydrogen production material is placed for 8 months is reduced by 11.3%.
In this example, the improvement capability of the standing stability of the molecular sieve used as the adsorption material is weaker than that of the diatomite, and the inventor speculates that the reason is that the surface of the diatomite also contains hydroxyl groups, and the hydroxyl groups of the hydrophilic fumed nano-silica and the polyethylene glycol of the treated calcium hydride form hydrogen bonds with the hydroxyl groups on the surface of the diatomite, so that the stability of the whole hydrolyzable hydrogen production material system is improved. Meanwhile, the inventor further uses activated carbon, zeolite, carbon foam and the like as adsorbing materials under the same conditions, so that the effect of improving the standing stability of the hydrolyzable hydrogen production material is weaker than that of the embodiment 8.
The use of sandwich masks containing the hydrolyzable hydrogen-producing material of the above example was tested.
The method of the sandwich mask containing the hydrolysable hydrogen-producing material of the above example is as follows:
(1) A layer of water is uniformly sprayed on the outer side of the bottom surface base material layer of the sandwich facial mask,
(2) Attaching the outer side surface of the bottom surface base material layer of the sandwich facial mask sprayed with water to the face;
(3) And (4) keeping the sandwich facial mask for 10-15 minutes, then taking off the sandwich facial mask, and washing the face with clear water.
Of course, other variations of the above method of application are possible, such as spraying an aqueous emulsion or nutrient solution on the bottom substrate layer, or spraying a mixed solution of water and glycerol; or other facial masks containing water or nutrient solution are stuck on the outer side of the bottom surface base material layer to replace the water or alcohol for providing the hydrolyzable hydrogen production reaction in the step (1).
(II) Effect of use
The sandwich mask containing the hydrolysable hydrogen-producing material of the above example was used in 55 female volunteer testers aged 28-33 years according to the above water spray application method, and was randomly divided into 11 groups, and the anti-wrinkle efficacy was evaluated after continuous use for 4 weeks, 6 weeks, and 8 weeks, and evaluated for one week, three weeks, and six weeks, in combination with canthus wrinkle visualization and photo display. Another random search was conducted for 5 female testers of the same condition as a control group using a mask pack without a layer of hydrolyzable hydrogen-producing material. The judgment basis of the smoothness of the fine lines of the skin is divided into 7 grades, which are respectively as follows: 0, no wrinkles; 1 slightly less visible shallow wrinkles; 2 slightly visible and noticeable shallow wrinkles; 3 obvious shallow wrinkles can be seen; 4 slightly visible and distinct shallow wrinkles with slightly deeper wrinkles; 5, slightly deep wrinkles can be seen; 6 visible and obvious deep wrinkles; very pronounced deep wrinkles were visible 7. The testers of both the experimental group and the control group were in grade 5 status before the experiment. The verification test was conducted to observe that the smoothness of fine lines of the user could be reduced by several grades after using the mask of the above examples and the control mask for a period of time, and generally, the more the grade was reduced, the better. The results are shown in Table 1.
As can be seen from the table below, a 1-grade reduction in fine grain smoothness was achieved substantially after 4 weeks of use, but with continued use for 6 weeks or more, the mask of the present invention achieved a 2-grade reduction in fine grain smoothness of even greater effectiveness, whereas the conventional water mask did not remain much reduced. The inventor believes that this should be the control group absorbing much more water floating on the skin surface and really absorbing very little; due to the effects of heating and hydrogen production, the mask disclosed by the invention can enable the skin to absorb more water and nutrients, and can further improve the reduction of the smoothness of fine lines of the skin.
Table 1 usage effect table