Patent Application
20190118233
The present invention relates to a method of recovering pulp fibers from a used absorbent article which includes the pulp fibers and super absorbent polymers, such as a paper diaper, etc. More specifically, the present invention relates to a recovering method of pulp fibers from a used absorbent article with small damages to the recovered pulp fibers.
An absorbent article, such as a paper diaper, etc., is normally composed of an absorbent body which includes pulp fibers and super absorbent polymers, and an outer wrapping body which covers the absorbent body, and is made of a nonwoven fabric or a plastic film. Such an absorbent article is discarded and incinerated after being used, however, in recent years, in consideration of the environmental aspect, it has been considered to recover and recycle the materials which configure an absorbent article.
Japanese Unexamined Patent Publication No. 2010-84031 discloses a treatment method of a used paper diaper which disinfects and processes the used paper diaper, characterized by including: throwing lime, hypochlorite, and the used paper diaper in a treatment tank, stirring the same for a predetermined period of time while supplying minimum amount of water capable of stirring the same in the treatment tank, discharging liquid in the treatment tank to an outside of the treatment tank and dehydrating the same, and recovering discharged waste water so as to be subjected to water quality treatment and to be discarded.
In the method disclosed in Japanese Unexamined Patent Publication No. 2010-84031, sufficient amount of lime is thrown in for inactivating the super absorbent polymers, and ozone or chlorine compound is used as the disinfecting agent (the sterilizing agent). Accordingly, not only the inside of the treatment tank is to be under high pH (12.4) environment by lime, and pulp fibers are to be converted to alkali cellulose and deteriorated, but also since ozone or chlorine compound is used for sterilization, there may be cases in which the pulp fibers are damaged, the deterioration progresses by repeating recycling, and the pulp fibers are deteriorated to a level that recycling is no longer possible.
The present invention provides a method of efficiently recovering pulp fibers which does not deteriorate the property of the pulp fibers with high safety.
The inventors focused on inactivating the super absorbent polymers by an ion exchange between base dissociated ions (Na+) of the super absorbent polymers and hydrogen ions generated by electrolysis of water, by an electric field formed between electrodes, as well as enabling destruction and sterilization of a cell membrane by an electric field energy, whereby completed the present invention.
The present invention is a method of recovering pulp fibers from a used absorbent article which includes the pulp fibers and super absorbent polymers, the method characterized in including:
a step of extracting a mixture of the pulp fibers, the super absorbent polymers, and water from the used absorbent article,
a step of inactivating the super absorbent polymers by applying voltage to the mixture of the pulp fibers, the super absorbent polymers, and the water by using a pair of electrodes, and
a step of separating the pulp fibers from a mixture of the pulp fibers, inactivated super absorbent polymers, and the water.
The present invention includes the following aspects.
[1] A method of recovering pulp fibers from a used absorbent article which includes the pulp fibers and super absorbent polymers, the method comprising:
a step of extracting a mixture of the pulp fibers, the super absorbent polymers, and water from the used absorbent article,
a step of inactivating the super absorbent polymers by applying voltage to the mixture of the pulp fibers, the super absorbent polymers, and the water by using a pair of electrodes, and
a step of separating the pulp fibers from a mixture of the pulp fibers, inactivated super absorbent polymers, and the water.
[2] The method according to [1], further comprising a step of adding water to the used absorbent article before the step of extracting the mixture of the pulp fibers, the super absorbent polymers, and the water from the used absorbent article.
[3] The method according to [1] or [2], further comprising a step of recovering a waste liquid which includes a urine-derived component which is discharged from the super absorbent polymers in the step of inactivating the super absorbent polymers.
[4] The method according to any one of [1] to [3], further comprising a step of recovering a waste liquid which includes a urine-derived component by filtering or dehydrating a residue after the mixture of the pulp fibers, the super absorbent polymers, and the water is extracted from the used absorbent article.
[5] The method according to any one of [1] to [4], further comprising a step of recovering a waste liquid which includes a urine-derived component by further dehydrating the mixture of the pulp fibers, the inactivated super absorbent polymers, and the water, after the step of inactivating the super absorbent polymers and before the step of separating the pulp fibers.
[6] The method according to any one of [3] to [5], further comprising a nutrient salt recovering step of recovering a urine-derived nutrient salt from the waste liquid which includes the urine-derived component.
[7] The method according to any one of [3] to [6], further comprising a microbial fuel cell step of throwing the waste liquid which includes the urine-derived component into a microbial fuel cell so as to reduce a TOC concentration while discharging the water and to recover electric power obtained by power generation.
[8] The method according to any one of [1] to [7], further comprising a sterilizing step of sterilizing the mixture of the pulp fibers, the inactivated super absorbent polymers, and the water, before the step of separating the pulp fibers.
[9] The method according to [8], wherein
the number of viable bacteria in the mixture after the sterilizing step is or less than 1×103.
[10] The method according to any one of [1] to [9], wherein
the super absorbent polymers are acrylic acid-derived super absorbent polymers.
[11] The method according to any one of [2] to [10], wherein
the step of adding the water to the used absorbent article is a step of immersing the used absorbent article in warm water of 50° C. or higher and lower than 100° C. [12] The method according to any one of [2] to [11], wherein
in the step of adding the water to the used absorbent article, a weight of the used absorbent article after being added with the water is or more than 90% of a maximum absorption weight of the used absorbent article.
[13] The method according to any one of [3] to [12], wherein
the step of extracting the mixture of the pulp fibers, the super absorbent polymers, and the water from the used absorbent article is a step of squeezing out the mixture of the pulp fibers, the super absorbent polymers, and the water from an outer wrapping body of the used absorbent article by letting the used absorbent article pass through a pair of rollers.
[14] The method according to any one of [1] to [13], wherein
the step of separating the pulp fibers is a step of separating the pulp fibers from the inactivated super absorbent polymers by letting the pulp fibers float in the water and precipitating the inactivated super absorbent polymers.
[15] The method according to any one of [1] to [14], further comprising a step of converting a residue after the mixture of the pulp fibers, the super absorbent polymers, and the water is extracted from the used absorbent article or the inactivated super absorbent polymers, to a solid fuel.
In the present invention, the super absorbent polymers are inactivated, desalted, and dehydrated by voltage application, whereby there is no need to use chemicals which deteriorate properties (the ash deposition amount), for the inactivation of the super absorbent polymers. Further, since the cell membranes of bacteria are destroyed and sterilized by voltage application, there is no need to use chemicals which deteriorate pulp fibers, for sterilization. In other words, according to the present invention, since chemicals are not used, there is no deterioration in the properties of pulp fibers (decrease in molecular weight, fiber breakage), and pulp fibers with high safety can be efficiently recovered.
The present invention relates to a method of recovering pulp fibers from a used absorbent article which includes the pulp fibers and super absorbent polymers.
The absorbent article is not particularly limited as long as the absorbent article includes pulp fibers and super absorbent polymers, and a disposable diaper, an incontinence pad, a urine absorbing pad, a sanitary napkin, a panty liner, etc., may be exemplified. In particular, as the absorbent article, an incontinence pad and a disposable diaper which are recovered collectively at facilities, etc., are preferable since there is no labor for sorting and the amount of pulp is relatively large.
As pulp fibers, although not particularly limited, fluff-like pulp fibers, chemical pulp fibers, etc., may be exemplified.
In the present description, pulp fibers which are recovered according to the method of the present invention is referred to as “recycled pulp”.
A super absorbent polymer is also referred to as SAP (Superabsorbent Polymer), which has a three dimensional network structure in which water soluble polymers are moderately crosslinked, is essentially water insoluble although absorbing several ten times to several hundred times of water, and has a function of not releasing water once absorbed even when some pressure is applied. As the super absorbent polymer, for example, acrylic acid type, starch type, or amino acid type, particulate or fibrous polymers may be exemplified. In the present invention, acrylic acid type super absorbent polymers are preferable from the viewpoint that an effect of lowering the pH by being converted to polyacrylic acid by the inactivation can be expected, and deterioration caused by the pulp fibers being converted to alkali cellulose can be prevented. The acrylic acid type super absorbent polymers have a sodium-substituted carboxyl group —COONa, and when water is absorbed, —COONa ionizes to —COO− and Na+, and dissociates the Na+ ion, the dissociated ion concentration in the super absorbent polymers is increased, water outside the super absorbent polymers enters into the super absorbent polymers by the osmotic pressure difference between inside and outside of the super absorbent polymers, and as a result, the super absorbent polymers swell and retain a large amount of water.
The method according to the present invention includes a step of extracting a mixture of the pulp fibers, super absorbent polymers, and water from a used absorbent article (hereinbelow, which is also referred to simply as “an extracting step”). The method of extracting the mixture of the pulp fibers, the super absorbent polymers, and the water from the used absorbent article is, although not limited thereto, preferably a method of squeezing out the mixture of the pulp fibers, the super absorbent polymers, and the water from an outer wrapping body (a nonwoven fabric, a film, rubber, etc.) of the used absorbent article, by letting the used absorbent article pass through a pair of rollers. In such a case, before letting the used absorbent article pass through a pair of rollers, in order to facilitate squeezing out of the mixture of the pulp fibers, the super absorbent polymers, and the water from the outer wrapping body, the used absorbent article may be let to pass through a pair of rolls for the purpose of crushing and perforating the outer wrapping body of the used absorbent article.
The method according to the present invention includes a step of inactivating the super absorbent polymers by applying voltage to the mixture of the pulp fibers, the super absorbent polymers, and the water by using a pair of electrodes (hereinbelow, which is also referred to simply as “a voltage applying step”). In a case in which the super absorbent polymers include a sodium-substituted carboxyl group (—COO−Na+), in this step, since the Na+ ions in the super absorbent polymers move toward the minus electrode by electrophoresis due to an electric field formed by the voltage application, Na+ ions are withdrawn from the super absorbent polymers, and the dissociated ion concentration in the super absorbent polymers decreases, whereby the water in the super absorbent polymers goes outside due to the osmotic pressure difference, and the super absorbent polymers dehydrate and contract. The —COO− in the super absorbent polymers combines with H+ ions generated by the ionization of the water so as to form —COOH, however, since the structure thereof can no longer expand the mesh therein due to the internal crosslinking by the hydrogen bonding being too strong, the super absorbent polymers are to be inactivated.
As the method of applying voltage, although not limited thereto, for example, the mixture of the pulp fibers, the super absorbent polymers, and the water may be sandwiched between horizontally arranged two pieces of wire gauze, and voltage may be applied between the two pieces of wire gauze. The applied voltage is not limited as long as the super absorbent polymers can be inactivated.
By the application of voltage, the waste liquid which is discharged from the super absorbent polymers passes through the wire gauze and falls under the wire gauze by gravity. The waste liquid which has fallen under the wire gauze is recovered in the waste liquid recovery-dedicated container which is disposed under the wire gauze. In the waste liquid, Na+ ions which are withdrawn from the super absorbent polymers, OH− ions which are generated by the ionization of the water, urine-derived salts, excrement-derived organic matter, etc., are included.
The voltage applying step may be performed by a batch type or in a flow type. When being performed by the flow type, for example, the voltage applying step may be performed by using the apparatus as shown in
When the inside of the treatment tank is to be under high pH (12.4) environment by lime, cellulose is to be swollen, and pulp fibers are to be converted to alkali cellulose and deteriorated, however, since the method according to the present invention uses the voltage application treatment for the inactivation of the super absorbent polymers, the pH does not change excessively, whereby the pulp fibers would not be deteriorated.
Even when the pulp fibers are regenerated from used diapers, since the deterioration can be suppressed, it is possible to minimize the decrease in quality even when the pulp fibers are repeatedly regenerated.
The method according to the present invention includes a step of separating the pulp fibers from the mixture of the pulp fibers, inactivated super absorbent polymers, and the water (hereinbelow, which is also referred to simply as “a separating step”).
The step of separating the pulp fibers from the mixture of the pulp fibers, the inactivated super absorbent polymers, and the water is not limited, however, the separating step is preferably a step of separating the pulp fibers from the inactivated super absorbent polymers by letting the pulp fibers float in the water and precipitating the inactivated super absorbent polymers. Since the inactivated super absorbent polymers have larger specific gravity than the pulp fibers, when the pulp fibers and the inactivated super absorbent polymers are placed in water, the pulp fibers and the inactivated super absorbent polymers are to be separated according to the specific gravity difference, and the pulp fibers which have lighter specific gravity float, and the inactivated super absorbent polymers precipitate, whereby the floated pulp fibers are scooped and recovered.
The method according to the present invention may further include a step of adding the water to the used absorbent article before the step of extracting the mixture of the pulp fibers, the super absorbent polymers, and the water from the used absorbent article (hereinbelow, which is also referred to simply as “a water adding step”). By adding water to the used absorbent article and making the super absorbent polymers sufficiently swollen, it is easier for the pulp fibers and the super absorbent polymers to be extracted from the used absorbent article, and it is possible to reduce the contact resistance between the mixture of the pulp fibers, the super absorbent polymers, and the water and the electrode in the voltage applying step, and further, it is easier for the electricity to flow in the mixture of the pulp fibers, the super absorbent polymers, and the water by the existence of the water, whereby the efficiency of the voltage application treatment is increased. In an absorbent article such as a paper diaper, etc., normally, since an absorbent body which is composed of pulp fibers and super absorbent polymers are sandwiched by upper and lower cover layers (which are the outer wrapping body), it is easy for the absorbent body to be pushed out. Further, by adding water, it is easier for the pulp fibers and the super absorbent polymers to be extracted from the used absorbent article, and as a result, there is little loss in the amount of the pulp fibers to be recovered, whereby the pulp fibers can be recovered efficiently.
The amount of the water to be added is not limited as long as the super absorbent polymers can be inactivated in the voltage applying step, however, the weight of the used absorbent article after being added with the water preferably is or more than 90% of the maximum absorption weight of the used absorbent article. When the used absorbent article is swollen so that the weight thereof is or more than 90% of the maximum absorption weight of the used absorbent article, the used absorbent article is to be greatly inflated, whereby it is easy to push out the absorbent body which is composed of pulp fibers and super absorbent polymers, and the absorbent body can be extracted efficiently.
In the present description, the maximum absorption weight corresponds to the weight after the absorbent article is immersed in tap water, according to the following procedure.
The method of adding the water is, although not limited thereto, preferably immersing the used absorbent article in the water. According to the method of immersing the used absorbent article in the water, the super absorbent polymers can be swollen, and at the same time, be washed. In a case in which the used absorbent article includes contaminants such as feces, etc., the contaminants such as feces, etc. can also be removed.
The temperature of the water is, although not limited thereto, preferably 55° C. or higher and lower than 100° C., more preferably 60° C. or higher and lower than 100° C., and even more preferably 70° C. or higher and lower than 100° C. By using warm water of 55° C. or higher, the water absorption efficiency of the super absorbent polymers can be increased, a part of bacteria is subjected to primary sterilization, and the hot melt adhesive agent which is used in the absorbent article is softened so that it is easier for the absorbent body to be pushed out, whereby the recovery efficiency of the pulp fibers is increased.
The immersing time is not limited as long as the super absorbent polymers can be inactivated in the voltage applying step, however, is preferably 1 minute or more, is more preferably 5 minutes or more, and even more preferably 10 minutes or more.
The method according to the present invention may further include a step of recovering a waste liquid which includes a urine-derived component which is discharged from the super absorbent polymers in the step of inactivating the super absorbent polymers (hereinbelow, which is also referred to simply as “a waste liquid recovering step”). In the waste liquid, Na+ ions which are withdrawn from the super absorbent polymers, OH− ions which are generated by the ionization of the water, urine-derived salts, excrement-derived organic matter, etc., are included. This step can be performed at the same time as the inactivating step. The recovered waste liquid is sent to a nutrient salt recovering step and/or a microbial fuel cell step which are described later and can be used effectively. By recovering and reusing materials other than the pulp fibers, the recycling rate of the used absorbent article is increased.
The method according to the present invention may further include a step of recovering a waste liquid which includes a urine-derived component by filtering or dehydrating a residue after the mixture of the pulp fibers, the super absorbent polymers, and the water is extracted from the used absorbent article (hereinbelow, which is also referred to simply as “a residue filtering/dehydrating step”). In the waste liquid which is recovered by filtering or dehydrating the residue, urine-derived salts, excrement-derived organic matter, etc., are included. The recovered waste liquid is sent to the nutrient salt recovering step and/or a microbial fuel cell step which are described later and can be used effectively. By recovering and reusing materials other than the pulp fibers, the recycling rate of the used absorbent article is increased.
The method according to the present invention may further include a step of recovering a waste liquid which includes a urine-derived component by further dehydrating the mixture of the pulp fibers, the inactivated super absorbent polymers, and the water, after the step of inactivating the super absorbent polymers and before the step of separating the pulp fibers (hereinbelow, which is also referred to simply as “a mixture dehydrating step”). In the waste liquid which is recovered by dehydrating the mixture, urine-derived salts, excrement-derived organic matter, etc., are included. The recovered waste liquid is sent to the nutrient salt recovering step and/or a microbial fuel cell step which are described later and can be used effectively. By recovering and reusing materials other than the pulp fibers, the recycling rate of the used absorbent article is increased.
The method of dehydrating the residue after the mixture of the pulp fibers, the super absorbent polymers, and the water is extracted from the used absorbent article, or of dehydrating the mixture of the pulp fibers, the inactivated super absorbent polymers, and the water is not particularly limited, and roll pressing, belt pressing, screw pressing, etc., can be exemplified.
The method according to the present invention may further include a nutrient salt recovering step of recovering a urine-derived nutrient salt from the waste liquid which includes the urine-derived component. The nutrient salt is salt which includes nitrogen, phosphorus, or potassium, applicable as a fertilizer, and more specifically, ammonium salt, phosphate, etc., may be mentioned. The recovered nutrient salt can be used as a fertilizer.
As the method of recovering the nutrient salt, although not limited thereto, a method of recovering nutrient salt which includes phosphorus by crystallizing phosphorus in the waste liquid as hydroxyapatite (hereinbelow, which is also referred to as “the HAP method”), and a method of recovering nutrient salt which includes phosphorus and/or nitrogen by crystallizing phosphorus and/or nitrogen in the waste liquid as magnesium ammonium phosphate (hereinbelow, which is also referred to as “the MAP method”).
The HAP method is a method which uses the crystallization phenomenon of hydroxyapatite (Ca10(OH)2(PO4)6) generated by the reaction of PO43−, Ca2+, and OH− in the waste liquid. The reaction formula is as follows.
10 Ca2++2 OH−+6 PO43−→Ca10(OH)2(PO4)6 (1)
In the HAP method, Ca2+ and OH− are added to an aqueous solution which includes phosphorus, so as to be in contact with the seed crystal in a supersaturated state (metastable region), whereby hydroxyapatite is crystalized on the seed crystal surface and phosphorous in the waste liquid is recovered. As the seed crystal, phosphorous ore, bone charcoal, calcium silicate hydrate, etc., can be used.
In this method, the concentration of Ca2+ of 5 millimol/liter or more, pH of 8 or higher, and preferably, the concentration of Ca2+ of 10 millimol/liter or more, pH of 9 or higher is required.
The MAP method is a method which uses the crystallization phenomenon of magnesium ammonium phosphate (MgNH4PO4.6H2O) generated by the reaction of PO43−, NH4+, and Mg2+ in the waste liquid. The reaction formula is as follows.
Mg2++NH4++PO43−+6 H2O→MgNH4PO4.6H2O (2)
In this method, the concentration of Mg2+ of 30 to 60 millimol/liter is preferable, and pH of 6.8 to 7.7 is preferable.
The method according to the present invention may further include a microbial fuel cell step of throwing the waste liquid which includes the urine-derived component into a microbial fuel cell so as to reduce a TOC concentration while discharging the water and to recover electric power obtained by power generation.
In the present description, a microbial fuel cell is a device which converts organic matter as fuel into electric energy by using microorganisms. In the microbial fuel cell, a negative electrode and a positive electrode are immersed in a solution of organic matter which is fuel, electrons generated when the organic matter is oxidatively decomposed by microorganisms are recovered at the negative electrode, the electrons move to the positive electrode via an external circuit, and the electrons are consumed by the reduction reaction of an oxidizing agent at the positive electrode. Electrons flow by the difference of oxidation-reduction potentials between the chemical reaction caused at the negative electrode and the chemical reaction caused at the positive electrode, and energy which corresponds to the product of the potential difference between both poles and the current which flows through the external circuit can be obtained at the external circuit.
In the microbial fuel cell step, the waste liquid is thrown into the microbial fuel cell so as to reduce the TOC concentration while discharging the water, and the electric power obtained by power generation is recovered. In the microbial fuel cell, microorganisms oxidatively decompose organic matter such as dirt, fine pulp, etc., which is included in the waste liquid, whereby the TOC concentration while discharging the water is reduced, and the power generation is performed.
The microorganisms to be used for the microbial fuel cell are not particularly limited, as long as the microorganisms oxidatively decompose organic matter and contribute to generation of electric energy, however, as the microorganisms to be used for the microbial fuel cell, hydrogen producing microorganisms are mainly used, and among which obligate anaerobic bacteria and facultative anaerobic bacteria are preferably used.
One example of the configuration of the microbial fuel cell is shown in
The pH of the discharged water from the microbial fuel cell step is preferably less than 8.0. When the pH of the discharged water from the microbial fuel cell step is too high, the power generation efficiency in the microbial fuel cell step is decreased.
The TOC concentration of the discharged water from the microbial fuel cell step is preferably 2000 mg/L or lower. When the TOC concentration of the discharged water from the microbial fuel cell step is 2000 mg/L or lower, it is possible to perform purification treatment simply by a general purification tank, etc., in the subsequent step. Further, in a case in which the draining is directly performed from the microbial fuel cell step, the TOC concentration of the discharged water is preferably 30 mg/L or lower.
The method according to the present invention may further include a sterilizing step of sterilizing the mixture of the pulp fibers, the inactivated super absorbent polymers, and the water, before the step of separating the pulp fibers.
According to the method of the present invention, in the voltage applying step, the cell membrane of the bacteria is destroyed and the bacteria are killed by the voltage application, whereby the voltage applying step also has a sterilizing function, and also serves as the sterilizing step. Accordingly, although the method does not necessarily have to be provided with the sterilizing step other than the voltage applying step, in a case in which pulp fibers with higher safety is required, the sterilizing step may be provided under condition ranges which do not deteriorate the properties of the pulp fibers.
The method of the sterilization is preferably not a chemical treatment, and a sterilizing method which does not leave residues such as a heat treatment, electricity, ultraviolet rays, ozone, etc., is preferable.
The number of viable bacteria in the mixture of the pulp fibers, the inactivated super absorbent polymers, and the water after the sterilizing step preferably is or less than 1×103. When the number of viable bacteria is or less than 1×103, pulp fibers with high safety can be obtained.
The method according to the present invention may further include a step of converting a residue after the mixture of the pulp fibers, the super absorbent polymers, and the water is extracted from the used absorbent article or the inactivated super absorbent polymers, to a solid fuel (hereinbelow, which is also referred to simply as “a solid fuel converting step”). In the residue after the mixture of the pulp fibers, the super absorbent polymers, and the water is extracted from the used absorbent article, a nonwoven fabric, a plastic film, rubber, etc., are included. The plastic materials recovered from the used absorbent article can be converted to solid fuel, whereby the plastic materials can be recycled. By recovering and reusing materials other than the pulp fibers, the recycling rate of the used absorbent article is increased. The solid fuel conversion can be performed by so-called RPF conversion technique.
The method according to the present invention may further include a step of washing the separated pulp fibers (hereinbelow, which is also referred to simply as “a pulp fiber washing step”).
As the method of washing the separated pulp fibers, although not limited thereto, for example, placing the separated pulp fibers in a mesh bag and rinsing the same with water may be mentioned. The rinsing can be performed in a batch system, in a semi-bath system, or in a circulation system. In a case in which the rinsing is performed in a batch system, for example, the rinsing may be performed by using a washing machine.
The condition of the washing is not particularly limited as long as substances other than the pulp fibers are sufficiently removed, and for example, the washing time is preferably 3 to 60 minutes, more preferably 5 to 50 minutes, and even more preferably 10 to 40 minutes. In a case in which the rinsing is performed in a batch system, the amount of the water to be used with respect to 100 parts by mass (absolute dry mass) of the pulp fibers is preferably 500 to 5000 parts by mass, is more preferably 800 to 4000 parts by mass, and even more preferably 1000 to 3000 parts by mass.
The method according to the present invention may further include a step of dehydrating the washed pulp fibers (hereinbelow, which is also referred to as “a pulp fiber dehydrating step”).
As the method of dehydrating the washed pulp fibers, although not limited thereto, for example, dehydrating the washed pulp fibers which are placed in a mesh bag by a dehydrating machine may be mentioned.
The condition of the dehydrating is not particularly limited as long as the moisture rate can be lowered to the target value, and for example, the dehydrating time is preferably 1 to 10 minutes, and is more preferably 2 to 8 minutes.
The method according to the present invention may further include a step of drying the dehydrated pulp fibers (hereinbelow, which is also referred to as “a pulp fiber drying step”).
As the method of drying the dehydrated pulp fibers, although not limited thereto, for example, drying the dehydrated pulp fibers by using a drying machine such as a hot air drying machine, etc., may be mentioned.
The condition of the drying is not particularly limited as long as the pulp fibers are sufficiently dried, and for example, the drying temperature is preferably 100 to 200° C., more preferably 110 to 180° C., and even more preferably 120 to 160° C. The drying time is preferably 10 to 120 minutes, more preferably 20 to 80 minutes, and even more preferably 30 to 60 minutes.
The moisture rate of the pulp fibers after being dried is preferably 5 to 13%, more preferably 6 to 12%, and even more preferably 7 to 11%. When the moisture rate is too low, there may be cases in which the hydrogen bonding is stronger and the pulp fibers are to be too stiff, and on the contrary, when the moisture rate is too high, there may be cases in which fungi, etc., occur.
The moisture rate of the pulp fibers is measured as follows. Incidentally, this measurement is performed under the atmosphere of 20° C.±1° C.
Moisture rate (%)=(B−C)/(C−A)×100
Hereinbelow, the present invention is further explained with reference to the drawings, however, the present invention is not limited to the embodiment shown in the drawings.
The apparatus 1 is configured by including an extracting step 2, a voltage applying step 3, and a separating step 4.
The extracting step 2 includes a conveyor 21 and a pair of rollers 23. The used absorbent article 11 is conveyed while being placed on the conveyor 21 so as to be sent to the pair of rollers 23. At this time, the outer wrapping body 12 which configures the used absorbent article passes through between the pair of rollers 23, the mixture of the pulp fibers, the super absorbent polymers, and the water is squeezed out from the outer wrapping body by the pair of rollers 23, so as to stay before the pair of rollers 23. The mixture of the pulp fibers, the super absorbent polymers, and the water which stays before the pair of rollers 23 is regularly raked out, so as to be sent to the voltage applying step 3.
The voltage applying step 3 includes the first electrode 31 and the second electrode 32. The second electrode 32 is provided above the first electrode 31. The first electrode 31 is a belt conveyor made of wire mesh. The second electrode 32 is also made into a belt-like shape, and only has to be made of an electrically conductive material, and does not necessarily has to be made of wire mesh, although the second electrode 32 may be made of wire mesh. A predetermined voltage is applied between the first electrode 31 and the second electrode 32 (which is not shown). Either the first electrode 31 or the second electrode 32 may be the positive electrode. The lower half of the belt which configures the second electrode 32 moves at the same speed (from left to right in the drawing) as the upper half of the belt which configures the first electrode 31. The gap between the first electrode 31 and the second electrode 32 is set so as to be able to be adjusted, and preferably, the gap is adjusted so that the gap is narrowed as moving from left to right. The mixture of the pulp fibers, the super absorbent polymers, and the water 13 which is extracted from the used absorbent article in the extracting step is conveyed while being placed on the first electrode 31, and is sandwiched between the first electrode 31 and the second electrode 32, so as to be applied with voltage. From the super absorbent polymers which have been applied with voltage, waste liquid 14 which includes Na+ ions, OH− ions, urine-derived salts, excrement-derived organic matter, etc., is discharged. The discharged waste liquid 14 passes through the wire mesh which configures the first electrode 31, drops into the waste liquid recovery-dedicated container 33 which is provided under the first electrode 31, and is stored therein. From the exit port of the voltage applying step 3, the mixture of the pulp fibers, the inactivated super absorbent polymers, and the water 15 is discharged, so as to be sent to the separating step 4.
The separating step 4 includes the separation tank 41. In the separation tank 41, the mixture of the pulp fibers, the inactivated super absorbent polymers, and the water 15 which has been sent from the voltage applying step 3 is thrown. Additional water is thrown into the separation tank 41, and is stirred and left still, whereby since the inactivated super absorbent polymers have larger specific gravity than the pulp fibers, the inactivated super absorbent polymers are precipitated in the bottom of the separation tank 41, and the pulp fibers float. The floating pulp fibers are scooped.
The method of the present invention can be preferably used for recycling a used absorbent article, such as a paper diaper, etc.
| Number | Date | Country | Kind |
|---|---|---|---|
| 2016-079179 | Apr 2016 | JP | national |
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/JP2017/000862 | 1/12/2017 | WO | 00 |
