JPH08509782A - Waste recycling method and apparatus therefor - Google Patents

Abstract

(57) [Summary] A disposable diaper (49) is cleaned using the first and second washing machines (13), (15) to remove and recover the plastic (87) and cellulose (53) for regeneration. To do. The disposable paper diaper is put into the first washing machine, and is cleaned in a washing liquid composed of water, alkali and detergent while being stirred by rotating the basket (37) and blowing air from the blower (23). Cellulose separates from the plastic during cleaning. Cellulose is drained from the first washer with water and the plastic remains in the first washer. The plastic is further cleaned in the first washer. Cellulose and water are sent to a second washing machine by a pump (17), where they are cleaned in a washing liquid consisting of alkali and detergent while being stirred. The second washer has a screen (48) through which water and dirt are discharged while cellulose remains inside. Wood pulp and rubber products, glass products, plastic products and other materials can also be treated and cleaned for recycling purposes.

Description

[Detailed Description of the Invention] Waste recycling method and apparatus therefor Field of the invention The present invention relates to a reprocessing method and equipment for separating, cleaning and recovering a specific material from waste such as disposable diapers and old newspapers. Background of the Invention Disposable disposable diapers are made from plastic and cellulose. The plastic acts as a moisture resistant lining on the outside of the diaper and the cellulose forms a bulky absorbent medium on the inside. The disposable diaper is generally provided as a bag. Cellulose absorbs and retains water, and plastic reliably prevents leakage from the bag. In recent years, what used the polymeric absorber instead of cellulose is provided. The polymer absorber has the characteristic of absorbing as much as 1000 times its own mass of water. Such disposable diapers have become extremely popular. As a matter of course, the disposable paper diaper is used only once, and is discarded after being contaminated with waste such as waste and secretions. Newspapers from old newspapers that are discarded after being read are also being recycled. The first step in recycling materials such as newsprint is usually to remove contaminants by cleaning. For newsprint, clean the paper to remove the ink. According to the conventional newsprint recycling method, a process of immersing newsprint in a water tank is performed. Next, the newsprint is sequentially transferred to another water tank and gradually cleaned. The final treatment of the disposable paper diaper as described above is carried to the local landfill site. From the viewpoint of environmental protection, this disposal problem of disposable diapers is accused of being uneconomical both in terms of production and disposal. The production of disposable disposable diapers requires cellulose from forest resources, while the disposal of disposable diapers uses valuable space for land resources. Many communities are witnessing the ongoing consumption of existing landfills, knowing that finding new landfills is politically difficult. Therefore, the need to recycle the material in disposable disposable diapers is emphasized. Also in the cleaning of newsprint, in the conventional method, the ink is not easily removed even when the newsprint is transferred from one tank to another, and it is difficult to satisfactorily clean the newsprint. Summary of the Invention It is therefore an object of the present invention to provide a method and equipment for recycling materials from waste, ie for recovering and regenerating plastics and cellulose from, for example, disposable diapers. Yet another object of the present invention is to provide a method for recycling plastic and cellulose containing work pieces by separating plastic and non-cellulosic materials from cellulose and cleaning these materials. Yet another object of the present invention is to provide a method for cleaning and recovering contaminated cellulose and wood pulp products such as newsprint. Yet another object of the present invention is to provide a method for cleaning rubber products such as old tires for recycling. Yet another object of the present invention is to provide a method of cleaning glassware for recycling. Yet another object of the present invention is to provide a method for treating organic waste such as food and industrial waste. The method of the present invention cleans cellulosic materials and non-cellulosic materials such as plastics, rubber, glass, etc. from waste. A washer is used to wash the waste. Charge waste, water, alkali and surfactant into perforated basket of washer. Stir the charge by moving the basket. Water, alkalis, surfactants and pollutants are discharged outside through the openings in the basket, while the work piece remains in the basket. According to one aspect of the invention, the workpiece to be cleaned comprises a cellulosic material and a non-cellulosic material. The step of moving the basket separates the cellulosic material from the non-cellulosic material. The discharging step comprises discharging the cellulosic material through the openings in the basket while holding the non-cellulosic material in the basket. The cellulosic material is transferred to a second washer having a second perforated basket. The cellulosic material, water, alkali and surfactant are agitated by moving the basket. While holding the cellulosic material in the second basket, water, alkali and surfactant are drained through the openings in the second basket. According to another aspect, the object to be cleaned is a rubber product such as an old tire. The rubber product is crushed into rubber particles before being carried into the basket. According to yet another aspect, the object to be cleaned is a contaminated cellulose or wood pulp product such as newsprint. A sufficient amount of alkali is added in the step of adding the substance to be treated, water, alkali and a surfactant, and the pH of the mixture comprising the substance to be treated, water, alkali and a surfactant is in the range of 10.5 to 14. Adjust within. In addition to moving the basket to stir the object to be processed, air may be introduced into the basket to further enhance the stirring effect. By injecting ozone into the basket during stirring, the object to be treated can be sterilized. The waste recycling facility according to the present invention recovers cellulose and non-cellulose from the waste. This facility has a first washer, a second washer, and a transfer means. The first cleaning machine is for cleaning the object to be processed, and has a first chamber and a first basket. The first chamber serves as a water storage chamber and has a drainage channel for discharging its contents. The first basket serves as a storage chamber for the object to be processed and is stored in the first chamber. The first basket has a large number of apertures to allow the mixture of cellulosic material and water to pass through while leaving the non-cellulosic material in the first basket. The first basket can be moved to agitate the work piece therein. The second cleaning machine is also for cleaning the object to be processed and has a second chamber and a second basket. The second basket is housed in the second chamber. The second chamber serves as a water storage chamber and has a drainage channel for discharging its contents. The second basket has a number of smaller openings than the openings in the first basket and allows water to pass through the openings, but the cellulosic material remains inside. The second basket can be moved to agitate its contents. The second washing machine has a charging means for accommodating the cellulosic material in the second washing machine. The transfer means is for transferring the mixture of the cellulosic material and water from the first washer to the charging means of the second washer. The transfer means has an inlet connected to the drainage channel of the first chamber and an outlet connected to the charging means of the second chamber. According to one aspect of the regeneration treatment facility of the present invention, the first basket is provided in alignment with the first mesh, and the first mesh is provided with a first basket opening having an appropriate size. , A mixture of cellulosic material and water is discharged through the opening, while the plastic remains in the first basket. A second basket is provided in alignment with the second mesh, and a second basket aperture of appropriate size is provided in the second mesh to allow water to drain through the aperture, while the cellulosic material is Remains in the second basket. Further provided are methods for treating organic waste such as food and factory waste. A washer suitable for washing fabrics or clothes is used. The washer has a basket that is perforated to allow water to pass through while leaving waste. Organic waste, water and either acid or alkali are added to the basket. Move the basket to stir the organic waste. Blow air into the basket while moving the basket to agitate the organic waste. Wastes are recycled using a washing machine (washing machine) for washing clothes that is generally commercially available. The washer contains a perforated basket, which is filled with water, surfactant (detergent) and other necessary additives along with the waste to be treated, and then the basket is moved to stir the feed. Waste is cleaned. The removed contaminants are discharged through the openings in the basket with water and additives, while the active substances, such as cellulosic material, remain in the basket. Brief description of the drawings FIG. 1 is a side view schematically showing an equipment configuration according to a preferred embodiment of the present invention. FIG. 2 is an enlarged vertical sectional view showing a portion of the first basket and the first chamber in the first cleaning machine. FIG. 3 is a cross-sectional view showing one basket. FIG. 4 is an enlarged vertical sectional view showing a part of a basket and an associated chamber in the second washing machine. FIG. 5 is a perspective view showing a suspender used for discharging the cleaned cellulose. FIG. 6 is a perspective view showing a separator used to pressurize moisture from the cleaned cellulose. FIG. 7 is a perspective view showing an equipment configuration according to another embodiment of the present invention. FIG. 8 is an enlarged perspective view showing the tank of FIG. FIG. 9 is a perspective view showing a configuration of a washing machine designed for treating organic waste such as food and factory waste. FIG. 10 is a block diagram showing the configuration of the wastewater treatment device. FIG. 11 is an end view showing the basket arrangement of each last chamber or module in the continuous process washer shown in FIG. Description of the preferred embodiment The method and equipment for recycling waste according to the present invention recycles waste such as disposable diapers contaminated with discharges and secretions. The disposable diaper is mainly composed of plastic and cellulose. The plastic forms a moisture-resistant barrier, and the cellulose disposed inside the plastic functions as a medium for retaining and absorbing the liquid. The method and equipment of the present invention regenerates plastic and cellulose in soiled disposable diapers. The plastic and cellulose are separated from each other in the initial cleaning process. The plastic and cellulose are then separately cleaned to remove all contaminants. The pollutants are mainly discharged to sewage treatment facilities and treated appropriately and sanitarily. The cleaned plastic and cellulose are supplied to the market and can be reused in industrial products. FIG. 1 is a schematic side view showing a facility 11 used to carry out a preferred embodiment of the present invention and its method. This equipment includes a first washing machine 13, a second washing machine 15, a transfer pump 17 provided between these first and second washing machines, a first supply conveyor 19, and a second washing machine. It has a supply conveyor 21 and a blower 23. The first and second washers 13, 15 are of substantially the same type. These washing machines are continuous batch type washing machines (washing machines) mainly used for washing (washing) textile products such as clothes. These washing machines are known and are commercially available. The washer used in the preferred embodiment is a continuous batch washer (washer) model 7 6032 manufactured by Peralin Milner, Inc., Kenner, Louisiana, USA. Each washing machine has a plurality of chambers 25 for washing the objects to be treated. The chamber 25 is waterproofed so as to retain the wash water. With reference to FIG. 2, each chamber is formed of a side wall 27 and a cylindrical outer wall 29. The chambers 25 of the respective washing machines are arranged in a line so that the side walls 27 are adjacent to each other. Each chamber 25 in the washer has a basket 37 for holding the product to be washed. Each basket 37 has a cylindrical outer wall 39 and two side walls 41. The vertical axis extends between the side walls 41. The baskets 37 in each washer are arranged such that their longitudinal axes are parallel. Each washer has an inlet 31 connected to the basket at one end and an outlet 33 connected to the basket at the other end. Each basket 37 communicates with an adjacent basket through an opening 35 in the side wall 41. The object to be cleaned is introduced into the washer from each inlet 31, is moved one by one while the washer 37 is being washed, moves from room to room through the opening 35, and from each machine through each outlet 33. Is discharged. Each washer has a motor 36 for rotating a basket 37 about its longitudinal axis within a fixed chamber 25. All baskets rotate in unison in the same direction. The object to be treated is stirred by the rotation of the basket, and the cleaning is efficiently performed. As shown in FIG. 3, each basket 37 is provided with ribs 43 to enhance the stirring effect of the object to be treated. The ribs 43 are provided on the inner surface of the outer wall 39 at intervals. During rotation of the basket 37, the ribs 43 raise and lower the product. The basket 37 rotates about 300 degrees in one direction and then about 300 degrees in the opposite direction. By such normal and reverse rotation, the stirring effect is further improved. The time required for the forward rotation over about 300 degrees in one direction and the reverse rotation over about 300 degrees in the reverse direction is about 11 seconds. The objects to be processed are transferred from one basket to the next by a known method of rotating the basket over 300 degrees. As the basket rotates more than 300 degrees, the work piece enters a known scoop on the basket and is transferred from there to the next adjacent basket. When the basket is the last basket, the object to be processed is discharged to the outside of the washing machine. The outer wall 39 of each basket 37 is provided with a large number of openings 45, 47. Apertures 45 allow drainage from the basket. The basket openings 45, 47 in the first and second washers 13, 15 have different dimensions. The openings in the first two baskets 37A, 37B in the first washer 13 are sized to hold the plastic material of the diaper but allow cellulose, secretions and water to pass through. It has been found that a stainless steel SUS 304 wire mesh 46 having 30 0.012 inch diameter wires per inch (about 2.5 cm) is satisfactory. The apertures 47 in all baskets 37C in the second washer 15 are sized to retain cellulose inside the basket but allow water and secretions to pass through (see FIG. 4). It has been found that a stainless steel SUS 316 wire mesh 48 having 40 0.01 inch (about 0.25 mm) diameter wires per inch (about 2.5 cm) is satisfactory. The wire mesh 46, 48 and apertures 45, 47 in FIGS. 2 and 4 are shown schematically for clarity of aperture. Basket 37 is designed to provide an appropriately sized aperture. Baskets in washers are manufactured with openings of relatively large size in the outer wall. A wire mesh of the appropriate size is welded to the inner surface of the outer wall 39 of the basket to provide the appropriate aperture size. Alternatively, the wire mesh can be attached to the outer wall by fitting a button attached to the wire mesh into several openings in the outer wall 39. A drain port 55 is provided at the bottom of each chamber 25. The drainage pipe 57 connects the drainage port 55 and the next chamber adjacent to the inlet 31 side. As a result, the cleaning water flows from one chamber to another chamber in a direction opposite to the flow direction of the object to be processed transferred from chamber to chamber. That is, the object to be treated moves from the inlet 31 toward the outlet 33, and the cleaning water flows conversely from the outlet toward the inlet. Water is preserved by such an opposing flow. The clean water supply port 59 is provided in the last chamber, but may be provided in another chamber if necessary (see FIG. 1). The last chamber adjacent to the object outlet 33 has a drainage channel leading to the conditioning tank 34. That is, the water in the last room is drained to the adjustment tank 34. The drainage channel 34a from the adjustment tank 34 is connected to the water supply port 39a on the first chamber. Water is thus supplied from the conditioning tank to the first chamber. In the first two chambers of the first washing machine 13, a drain pipe 61 extends from the drain port 55. Each of these drain pipes 61 is connected to the inlet of the pump 17. The pump 17 is a well-known pump suitable for pumping a solid or fibrous material that is entrained in a fluid substance together with the fluid substance, and is generally commercially available. The outlet of the pump 17 is connected to a line 63 extending towards the conveyor 21 for the second washer 15. The pipe 63 discharges the fluid to the conveyor 21 at a position inside the drain tank 65. A valve 67 is provided in each of the drain pipes 61 extending from the first two chambers of the first washing machine 13. Valve 67 controls the fluid output from these first two chambers. A check valve 69 is provided in the conduit 63 from the pump 63. Check valve 69 prevents fluid from flowing back into the pump or chamber. Each of the washing machines 13 and 15 has supply conveyors 19 and 21 for introducing the objects to be washed into the first basket, respectively. Each of the washers 13, 15 has a funnel 71 for receiving the object to be processed and transferring it to the inlet 31. The supply conveyors 19 and 21 carry the material to be processed to the funnel 71 from the drainage tanks 73 and 65 which are usually installed on the ground, and the material to be processed is discarded from the funnel. Each supply conveyor has a perforated surface to allow dewatering of the work piece before it is loaded into the washer. Each drainage tank 73, 65 is provided with a floor drainage pipe 75 connected to the sewage treatment facility. Instead of the conveyor, other carrying-in means such as a sling or a chute can be used. Each washing machine is also provided with a blower 23 for blowing air into each chamber. The blower 23 is connected to the room via the air passage 76. The air passage 76 is connected to the chamber at a position below the basket, and blows air bubbles into the basket. With reference to FIG. 3, which partially shows the outer wall 29 of the chamber, the air duct 76 is connected to a plenum attached to the outer wall 29. An opening 30 is provided to allow air to enter the chamber from the plenum. The opening 30 extends from one side wall 27 of the chamber to the other side wall so that air is dispersed across the basket. The opening 30 is formed at a position that makes an angle of about 45 degrees from the bottom of the chamber. This eliminates the influence of the material to be deposited on the bottom of the chamber on the air flow. By sending air to the cleaning process, the biodegradation of waste products and secretions in disposable diapers is initiated and promoted. The blower itself is publicly known and generally commercially available. The blower preferably used is about 5.4 to 13.5 km / min. ³ The amount of air can be supplied to each washing machine. Each washing machine is provided with a zonal generator 24 in addition to the blower (see FIG. 1). The ozone generator 24 itself is publicly known and commercially available, and a type in which a spark gap is provided in the housing is generally known. Ozone is generated when a spark is formed between the electrode gaps. The ozone generated by the ozone generator 24 is sent to each air passage 76 by the pump 26. The object to be treated is sterilized by ozone in each washing machine. By using ozone, chlorine bleaching can be omitted. Ozone is also supplied to the adjustment tank 34. The outlet of each washing machine is a ramp or a ramp 77, and the object to be treated that has left the last chamber falls from the ramp and is stored in a storage tank 79. The object to be treated contained in the storage tank 79 of the second washing machine is transferred to a sling or sling 81 (see FIG. 5) for drainage, and further transferred to a separator 83 (see FIG. 6). The sling 81 is made of a mesh-shaped material and performs wastewater treatment while the object to be treated is conveyed by the cable 85. The separator 83 itself is known and is generally commercially available. The separator pressure-extracts and separates water from the object to be processed. The separator 83 may be covered with the same mesh screen as in the second washing machine 15. Cellulose is compressed by the separator but is retained within the effective volume of the separator by the mesh screen. The method of the present invention is described below. Referring to FIG. 1, the disposable paper diaper 49 is placed on the conveyor 49 of the first washing machine at the collection site. The accumulation area is in the drainage tank 73, and some amount of drainage is performed here. Disposable disposable diapers are contaminated with excrements or secretions such as urine and feces. No pretreatment such as shredding or cutting the paper diaper is required. The disposable diaper 49 is placed in the first basket 37A of the first chamber of the first washing machine 13. Here, the disposable diaper is mixed with water, an alkali and a detergent (or a surfactant). Fresh, clean, cold (about 24 ° C) water is supplied from a water inlet 59 connected to the first chamber. A suitable alkali is, for example, orthosilicic acid. The pH value of the mixture is brought to the desired level, i.e. 10. An amount of alkali necessary and sufficient for adjusting the range of 5 to 14 is added. Higher pH values are required for objects with higher oil lipids. It has been experimentally confirmed that a pH level of 13-14 is desirable. The detergent is pH 7 neutral. The first basket is rotated forward and backward about its longitudinal axis to agitate the mixture. The cellulose in the diaper separates from the plastic while being agitated. In addition, the process of cleaning dirt from cellulose and plastic is initiated. The high pH provided by the addition of alkali facilitates the separation of dirt from cellulose and plastics. The neutral detergent keeps the separated dirt dissolved in water and prevents the dirt from redepositing on the cellulose and plastic. The air supplied by the blower 23 and the ozone supplied by the ozone generator 24 are introduced as bubbles from the bottom of the chamber into the basket, enhancing the stirring effect of the mixture and facilitating the separation of cellulose from the plastic. The agitation effect enhanced by the air further serves to promote the mixing of the compound in the cleaning liquid, so that the compound is rapidly replaced throughout the cleaning liquid and penetrates into the object to be treated. The blowing time reduces the cleaning time. In addition, air oxidizes a mixture of water and thus provides a suitable environment for achieving biological degradation of waste. Ozone sterilizes plastics and cellulose. Furthermore, by blowing air from the outside of the basket, it is possible to prevent the basket opening from being clogged by the object to be cleaned. After cleaning the diaper in the first basket for a predetermined time, for example, about 10 minutes, the drain valve 67 is opened to drain the first chamber and the first basket 37A (and the second chamber and the second basket 37B). To do. The plastic 51 remains in the first basket due to the screen mesh, but the sludge-like fluid is discharged from the basket 37A and the chamber. The sludge-like fluid consists of water, separated cellulose, dirt and alkali and detergent. Then, the first basket is rotated more than 300 degrees with respect to the other baskets in the first washing machine, and the contents are transferred to the next second basket 37B. The contents of the second basket are also washed as in the first basket described above to separate residual cellulose from the plastic. After the cleaning cycle in the second basket is completed, drain valve 67 is opened to drain second basket 37B and the second chamber. Since the first washing machine 13 is of a continuous type, every time the washing process in the first basket 37A is completed and the water is discharged and the contents are transferred to the second basket, the dirty paper diaper to be processed next is 49 is placed in the first basket. This creates a continuous stream of material to be processed throughout the system. The transport conveyors 19 and 21 are intermittently operated only when the object to be processed is to be loaded into the first basket. Both drain valves 67 open and close simultaneously. The contents of the second basket are then transferred to the third basket. The cellulose in the first two baskets has already been separated and drained, so the content of the third basket is only plastic 51 and does not contain cellulose. While continuously moving through the remaining chambers of the first washer 13, the plastic is washed in warm water (eg about 54 ° C), alkali and detergent to remove all dirt. Sand is introduced from the water supply port 60 at a substantially intermediate position of the first washing machine 13 to form a slurry composed of sand, plastic, and water. The sand cleans the plastic and shapes it. Because sand provides a friction point, basket rotation and agitation of the plastic by air ingress are more efficient and clean the plastic well. As the sand, those of the type used for sandblasting are suitable. The sand moves with the plastic from the introduced basket to the last basket in the first washer. A wire mesh of SUS316 is attached to the inner surface of the outer wall of the basket. This wire mesh holds the plastic inside the basket and prevents small plastic chunks from entering the drains of each chamber. Two layers of wire mesh are attached to the last basket. The inner wire mesh layer consists of SUS304, which holds the plastic during the wash cycle (and basket rotation) but allows the sand to pass through. The outer circumference of the wire mesh inner layer is covered with a wire mesh outer layer made of SUS316. A space of about 30 to 45 cm is provided between the inner layer and the outer layer of these wire meshes (the arrangement configuration of such wire meshes will be described later with reference to FIG. 11). Sand is stored in this space. Sand does not pass through the outer layer of wire mesh. In this way the sand is separated from the plastic in the last basket. The sand contained between the two layers of wire mesh is collected and reused for introduction into the washing machine through the water supply port 60. The plastic is removed from the washer and loaded onto a wet conveyor. The transfer from the washing machine may be carried out manually or by mechanical means. On the conveyor the plastics can be sorted by color etc. One problem with conventional plastic recycling methods has been to remove the ink from the plastic. Inks are primarily used to print information on plastics. If the ink removal is not complete, the recycled plastic will have the color of the ink, reducing the commercial appeal of the recycled plastic. In the present invention, since the ink is removed from the plastic by the sanding action of the sand, the plastic is regenerated in its original color state, and the plastic can be freely colored and reused. This method of removing ink from plastics is applicable not only to the plastic components of disposable diapers but also to any type of plastics. For example, candy plastic wrap can be treated by this method to remove the ink. In some cases, the plastic is laminated with multiple layers of plastic or paper. Instead of sand, a water-soluble aromatic solvent such as mineral spirits or paint remover can be used to remove the rubber material and labels attached to the plastic. Alternatively, sand and an aromatic solvent may be used in combination. In the washing process, a sterilizing agent can be added to sterilize the plastic. Ozone from ozone generator 24 can be used for this purpose. Alternatively, chlorine bleaching may be used. However, the use of sand reduces the need for ozone and bleaching. The sludge consisting of a mixture of water and cellulose discharged from the first two baskets of the first washing machine 13 is sent to the pump 17, and is a conveyer conveyor to the second washing machine 15 via the pipe 63. It is pressure-fed to the second conveyor 21. The sludge charging point for the second conveyor 21 is in the drainage tank 65, and in this drainage tank most of the water and excretions are separated from the cellulose. The water / cellulose sludge 89 is then loaded into the first basket in the second washer 15. Cellulose is washed with warm water (about 77 ° C), alkali and detergent. After completion of the cleaning cycle, the drain valve 91 in the first chamber is opened, and the waste water from the first chamber is sent to the sewage treatment facility through the drain pipe 90. The wire mesh in the valve of the second washer has smaller openings than the wire mesh in the first washer, and cellulose remains in the basket. The cellulose in the first basket is then transferred to the second basket where it is again washed with hot water, alkali and detergent. The pH value of the mixture is brought to the desired level, ie 10. Sufficient alkali is added to raise it to the range of 5-14. It has been experimentally confirmed that a pH value of 13 to 14 is suitable. The cellulose is then rinsed with warm water in a third basket and bleached in a fourth basket. Cellulose is bleached and sterilized by a bleaching agent such as chlorine bleaching agent, hydrogen peroxide or oxalic acid. The cellulose is then rinsed with water and further rinsed with water and sour or sodium fluorocarbonate to a pH value of about 6. 5-7. Lower to 0. Cellulose is discharged from the last basket of the second washing machine 15 and is put into a carrying process by the lifting tool 81 as shown in FIG. The hanging tool 81 is formed of a net and drains water while holding the cleaned cellulose. The suspending tool is suspended from the cable 85 and moves from the outlet of the second washing machine 15 toward the inlet of the separator 83. The contents in the hanger are thrown into the separator inlet. The separator 83 compresses the cellulose into blocks 93 to extract and separate water in the cellulose. The mesh screen in the separator allows moisture to pass through while leaving the cellulose inside. The resulting cellulosic block 93 is then transported by conveyor 95 from the separator to a shipping or storage point. After being compressed in the separator, cellulose can be put into a dryer to completely remove residual water. The dryer is publicly known, and a commercially available dryer may be partially modified and used. The dryer has a rotating basket. The basket aperture is reduced by installing a mesh screen of the same type as in the second washer. The mesh screen holds the cellulose in the basket. Apart from cellulose, plastics can be dried in a dryer. In paper diapers of recent years, the amount of cellulose required for moisture absorption is reduced by using a substance generally called a polymer absorber in the art. The polymeric absorber generally consists of an acrylic polymer. The polymer absorber absorbs tens to hundreds or thousands of times its own weight of water. The polymer absorber is separated from the plastic in the first washing machine 13 together with the cellulose, and then transferred to the second washing machine 15 together with the cellulose. In the second washer the polymeric absorber is neutralized and separated from the cellulose. That is, the cellulose is washed in a mixed solution of water and sodium fluosilicate or sodium chloride before or after washing the cellulose with an alkali and a detergent. Sodium fluosilicate neutralizes the polymeric absorber and facilitates its separation from the cellulose. The water that enters the wastewater treatment facility from the washing machines 13 and 15 is naturally contaminated by the dirt attached to the disposable diaper. This sewage can be sent to the sewage treatment plant of each municipality and treated by the sewage treatment plant of the municipality. Alternatively, a private sewage treatment plant may be used to treat the wastewater from the reclaiming treatment. Another method will be described below. In this method, the first washer 13 is provided with four modules or chambers and the second washer 15 is provided with five modules or chambers. The soiled disposable diaper is put into the first basket or the first module of the first washing machine 13. Water and acid at about 38 ° C. are also added to the first module. The pH of the cleaning solution is about 5. Sufficient acid to add 5 is added. Next, the basket is rotated and air is blown from the blower 23. During the cleaning process in the first module, the disposable diaper remains almost intact and only some of the dirt is washed away. Waste water and dirt are discharged from the module through the drain pipe, and the disposable diaper remains in the first module or basket. Wastewater and waste are sent to wastewater treatment facilities. The polymeric absorber and other water-absorbing polymers inside the diaper are efficiently reduced to small dimensions by the acid. The washing step in the first module halves the weight and volume of the diaper. After cleaning in the first module, the diaper is transferred to the basket of the second module. Here, the paper diaper is washed in a mixed cleaning solution of warm water of about 90 ° C., a neutral surfactant and a sufficient amount of alkali. The pH of the cleaning solution is about 12. Increased to 5. The basket is rotated and blown to agitate the diaper. Thus, the disposable diaper is crushed and separated into cellulose and plastic. Most of the cellulose is discharged from the basket and pumped to the second washer. Some cellulose remains with the plastic in the basket, but these are transferred to the basket of the third module. Here the cellulose and plastic are rinsed with water. In the third module the cellulose is discharged from the basket and pumped to the second washer. The plastic left in the third basket is sent to the basket of the fourth or last module. In the last module the plastic is rinsed again with water and then discharged from the washer. An inner basket can be attached to the fourth module, which removes insoluble dirt from the plastic. This configuration is shown in FIG. 11, which will be described in more detail below. In both the first and second washing machines, the object to be treated placed inside the basket is agitated by the rotation of each basket and the blowing of air from the bottom of the module into the basket. The cellulose put into the second washing machine 15 is washed as described above. The super absorbent polymer reduced in the first washing machine is separated from the cellulose, passes through the basket opening, and is discharged from the basket. As the cellulose passes through the module in the second washer, the superabsorbent polymer is more and more completely separated from the cellulose. Thus, the cellulose discharged from the outlet end of the second washing machine is in a clean state in which the super absorbent polymer is completely separated. FIG. 7 shows a reproduction system 101 according to another embodiment. The system of FIG. 7 uses batch-type first and second washers 103, 105 rather than the continuous-type washers described above with reference to FIG. Both the first and second washers have a single basket and chamber inside. This system is preferably used when the amount of disposable diapers to be reclaimed does not justify the expense of purchasing the continuous washer of FIG. The basket of the first washing machine 103 is covered with a wire mesh similar to the wire mesh 46 in the above-described first continuous washing machine 13, which holds the plastic inside and discharges cellulose through the outside. The first washing machine 103 has a drain pipe 107 for discharging all waste water and cellulose. This drain pipe is T-shaped, and one branch pipe thereof leads to the pump 109, and the other branch pipe thereof leads to the waste water treatment facility 111. Drain valves 113 and 115 for controlling the flow rates in these two branch pipes are provided, respectively. The pipe 117 is connected to the output side of the pump 109. A check valve 119 is provided in pipe 117 near pump 109. The outlet end of the pipe 117 opens toward the upper side of the tank 121 arranged on the second washing machine 105. The tank 121 is shown in FIGS. 7 and 8 and is used to drain the cellulose before it is loaded into the second washer 105. The tank 121 is supported above the second washer 105 by a support structure 122. The tank 121 has an open top surface and has four side surfaces 123 and 125 and a bottom surface 127. One of the sides acts as an openable door 125. The tank 121 further has a bottom surface 129 made of wire mesh, and a space is provided between these double bottom surfaces. The wire mesh bottom surface 129 allows drainage but retains cellulose. A drain port 131 is provided on the bottom surface 127. The drainage port 131 is connected to a wastewater treatment facility via a drainage pipe 133. A water jet device 135 is provided in the tank 121 below the bottom of the wire mesh, and the wire mesh 129 is cleaned by spraying the water jet. The tank 121 is movable between the storage position and the discharge position. In the storage position, the tank 121 is substantially horizontal to store the cellulose therein, but is slightly inclined to bring the drainage port 131 to the lowermost position. The tank 121 is moved to the discharge position by the action of the hydraulic piston mechanism 137, and is brought into an inclined state as shown by a phantom line in FIGS. 7 and 8. At the discharge position, the door 125 is opened, and the cellulose is dropped and thrown into the basket of the second washing machine 105 through the charging port 139. The second washing machine 105 has a top inlet 139, a drain pipe 141, and a drain valve 143. The basket of the second washing machine 105 is covered with a wire mesh similar to the wire mesh in the above-described continuous type second washing machine 15, which allows cellulose and moisture to pass through and discharge while retaining cellulose inside. The washing machines 103 and 105 are each provided with a blower 145 for sending air to the object to be processed. The ozone generator 24 and pump 26 of FIG. 1 can be used in the configuration of FIG. 7 to supply ozone to each washer 103, 105. In order to recycle the disposable diaper in the system of FIG. 7, first, the load of the disposable diaper is put into the first washing machine 103. A door 147 for loading and unloading is provided in the first washing machine. When the first washing machine 103 has a capacity of about 125 kg, the primary washing of the diaper is carried out for 10 minutes in a washing liquid composed of water at about 24 ° C. and about 224 g of alkali. Then, the drain valve 113 leading to the pump 109 is opened to drain the first washing machine, and the sludge composed of water and cellulose is pumped to the tank 121 by the pump 109. After draining for 2 minutes, the drain valve 113 is closed. Next, the content of the first washing machine 103 is washed for 10 minutes in warm water (for example, about 54 ° C.) to which about 112 g of alkali and detergent are added. Then, the drain valve 113 is opened for 2 minutes, and the sludge is pumped from the first washing machine 103 to the tank 121 by the pump 109. Pump 109 always operates when drain valve 113 is open. In this way all the cellulose is discharged from the first washer, leaving only the plastic. Sand (and / or aromatic solvent) is introduced into the first washer to remove ink and other contaminants from the plastic. As described above, the plastic is washed with water, a surfactant and a sterilizing agent such as ozone (and alkali if necessary) and further stirring. After washing the plastic, the sand is discharged from the basket openings and separated from the plastic. When the basket openings are of appropriate size (eg with a double wall construction as described above with respect to washer 13) the sand is separated in the first washer 103 or in another washer. To be done. The sludge made up of water and cellulose, which is pumped by the pump 109, is put into the tank 121. Cellulose is then introduced into the second washer 105 through the inlet 139, where it is washed with water (about 77 ° C.), about 224 g of alkali and detergent for 10 minutes. After that, the drain valve 143 is opened for 2 minutes, and the waste water and the waste are allowed to flow into the waste water treatment facility 111. After further washing the cellulose with water (about 77 ° C.), about 280 g of alkali and detergent for 10 minutes, the drain valve 143 is opened for 2 minutes. After rinsing the cellulose with water (about 77 ° C.) for 2 minutes, the drain valve is opened for 2 minutes. Then, wash with about 1 liter of bleach-added water (about 66 ° C.) for 2 minutes, and then open the drain valve for 2 minutes. You may use ozone as a germicide. After rinsing the cellulose with water at about 54 ° C. for 2 minutes, open the drain valve for 2 minutes. Next, after rinsing the cellulose with water at about 43 ° C. for 2 minutes, the waste water from the washing machine to the waste water treatment facility is treated for 2 minutes. The cellulose is then washed for 5 minutes in a rinse consisting of water at about 24 ° C. and about 168 g of acid. Drain the washing machine and carry out the cleaned cellulose. Cellulose is conveyed by the suspending tool 81, further sent to the separator 83, and water is extracted and separated by the above-mentioned capacity. Not only are plastics and cellulose recyclable from disposable disposable diapers, but the method and system of the present invention are recyclable from many other disposable products and materials. Before reprocessing the regenerated material into a new product, it is first necessary to remove oil, grease, dirt, etc. from the material and clean it. Many products are similar to disposable diapers in that they contain cellulosic and non-cellulosic materials (eg, plastics, metal parts, etc.). It has been found that peanut cans, frozen juice cans, cardboard boxes and other items are renewable. In the case of peanut cans and frozen juice cans, the metal rim and the plastic lid are held and cleaned in the first washer, and the cellulose or paper forming the can wall of a rigid paper is used in the second washer as described above. It is washed as in the case. In the case of a cardboard box, in the first washer, metal and plastic (eg, metal stops and plastic load labels) are separated from the cellulose forming the walls of the box. Cellulose is sent from the first washer to the second washer where it is washed. Boxes of grain (eg, prismatic ones such as oat containers) can be regenerated into cellulose (box wall) and plastic (inner liner). Cartons of milk and juice can also be regenerated into cellulose and plastic. Cups and other disposable food containers are also renewable in cellulose and plastic. By rotating the basket and agitating the air to agitate the objects to be processed, the cellulose forming the walls of these containers is cut small enough to allow it to pass through the mesh of the first basket, from non-cellulose. Allows the separation of cellulose. Plastic packages such as those found in candy and cigarette packages can also be processed. Similarly, plastic containers can be washed and regenerated. An example of a plastic container that is difficult to recycle is a container for automobile oil. Although this container is made of a renewable plastic material, it is difficult to remove oil from the plastic for cleaning and is not suitable for the recycling process of the present invention. One method for treating plastic oil containers is to grind the container into small pieces. Small pieces that are crushed to the same size as the tire described below are washed in the washing machine 13. The small pieces are washed in a mixed washing solution of water and sand, a neutral surfactant and an alkali at about 82 ° C. Washing removes oil from the pieces. At the same time, the sand removes paint, labels and other non-plastic materials that adhere to the plastic pieces. It has been found that contaminated wood pulp products, such as newsprint and waste paper, can also be recycled according to the method and system of the present invention. Newspapers are obtained from newspapers. The waste paper includes disposable office paper such as type paper and copy paper. According to the present invention, the ink on the paper surface is removed. Newsprint, for example, is similar to the cellulose found in disposable diapers and can be cleaned by similar systems and methods for cleaning cellulose. Both newsprint and cellulose are made from wood pulp. In order to recycle used paper such as newsprint, a load of newsprint is put into the second washing machine 15, 105. The newsprint is washed by the same washing step as the cellulose washing in the above-mentioned second washing machine. However, slightly elevated temperatures (eg, about 85 ° C.) of water are used to help disperse the ink on the newsprint. Ink is removed from the paper by this washing process, and is flowed to the wastewater treatment facility 111. The paper remains in the basket due to the wire mesh 48 in the second washer, and the ink and water are discharged through the wire mesh. The cleaned newsprint is carried out from the second washer 15 and 105 and put into the hanging tool 81 and the separator 83 to remove residual moisture. One of the conventional problems with the method of recycling newsprint has been that the quality of the final product (and thus its commercial value) is determined by the storage status of the disposable newsprint. Dirty, tanned newspapers have significantly less commercial value than relatively clean (apart from ink) newspapers. The present invention can clean dirty, tanned newspapers to enhance their commercial value. By washing the newspaper in the washing machine obtained by partially improving the clothes washing machine, all contaminants in the newspaper can be washed off. Newspapers turn yellow when tanned due to the high acid content of the paper. High acid content is a by-product of the papermaking process. Contrary to the papermaking process, the present invention uses alkaline to clean newsprint and raise its pH to high levels. The use of alkaline cleaning solutions and ozone and / or chlorine bleaching bleach newsprint, enhancing its commercial appeal. The alkali also activates the cellulose and reduces the brittleness of the cellulose fibers. As a result of washing the newspaper with an alkaline washing solution, it is no longer acid paper. Therefore, the recycled newsprint does not deteriorate immediately like acid paper. Not only can materials containing cellulose be regenerated, but the present invention can also regenerate materials that do not contain cellulose at all. For example, disposable automobile rubber tires can be recycled according to the invention. In the conventional method of treating a disposable tire, the tire is stored in a landfill or the like, or cut for incineration in an incinerator. Tire storage requires land for non-manufacturing. Water remains inside the tires, providing a hotbed for insects such as mosquitoes to breed. Tire burning is wasteful and causes air pollution. Tires must be cleaned prior to reconditioning. Old tires are contaminated with grease, road oil and other dirt. Polyester belt materials and treads are especially difficult to remove as they have accumulated grease, oil and other stains. According to the tire recycling process of the present invention, the tire is cut into small pieces or pieces of rubber. A shredder that has been publicly known and is commercially available is used. In a preferred example, the strip is about 0. 3-2. The size is 5 cm. Many tires have steel and other types of belts, but the entire tire, including these belts, is cut into small pieces. The tire pieces are put directly into the second washing machine 15. The pieces are washed in water, detergent (or other surfactant) and alkali. The same washing steps as described above for cellulose are carried out in the second washing machine. The basket rotation and blast agitate the pieces to remove dirt, grease and oil from the pieces. Ozone injected into the washer 15 along with air sterilizes the tire pieces. The washed tire pieces are discharged from the washing machine and dried. Drying is done by placing the tire pieces in a dryer. The tire pieces are retained in the basket by coating the mesh of SU S316 inside the dryer basket. After drying, the cleaned rubber pieces can be mixed with fresh rubber material to make a new rubber product. The cleaned rubber can be sulfurized or melted, for example. Further, the present invention allows other non-cellulosic materials such as glass containers to be washed for regeneration. A glass container such as a bottle is placed in the first basket of the second washing machine. Warm water at about 71 ° C. and a neutral detergent or surfactant are added to the first basket. Since glass is water impermeable, strong surfactants are not required. The glass container is agitated by rotating the first basket and blowing air into the first basket from the blower. During stirring, the glass container breaks at least partially, and possibly all of it. A SUS3 16 mesh that lines the inside of the first basket holds all of the glass shards within the first basket. During the agitation, all of the levels attached to the glass container are separated from the glass. The cellulose or paper lining passes through the mesh and exits the first basket. Ozone can be injected into the room to sterilize the glass. If it is necessary to further clean the glass, the subsequent washing steps in the mesh-coated basket can be repeated. After cleaning, the glass is taken out of the washing machine and dried in a hanging device, a rotary dryer or high temperature air. The glass thus cleaned is melted and molded into a new container or other product to complete the recycling process. A conventionally known method is adopted for the processing for melting and molding. The present invention further provides a treatment method for mixing organic waste such as food and industrial waste (see Figure 9). In order to decompose the organic waste, the material is put into the first basket 153 of the first mixer 151. As the mixing machine, generally, a partially improved washing machine provided for selecting clothes or fabrics is used. The first basket 153 is lined with SUS316 mesh as in the second washing machine 15 of FIG. The second and subsequent baskets in the mixer 151 are sequentially lined with a mesh having openings smaller than the mesh openings of the baskets before it. That is, the mesh openings in the second basket 153A of the mixer are smaller than the mesh openings in the first basket, the mesh openings in the third basket are even smaller than the mesh openings in the second basket, and Similarly, the size of the mesh opening is gradually reduced from the first basket toward the last basket. The mixer drain 155 provides reflux to the mixer or washer, rather than dropping fluid into the sewage treatment plant. The first four modules or chambers have drain pipes 155 connected to common pipe 157. The pipe 157 is connected to the input side of the pump 159. The pipe 161 connected to the output side of the pump opens toward the inside of the fourth chamber 163. The outlet end of tube 161 is shaped to allow fluid to drain into the basket of fourth chamber 163. That is, the fluid collected by the drains of the first four chambers is returned to the fourth chamber. Reflux with similar piping and pumps is also employed in the remaining chambers of the mixer, from the fifth chamber to the last chamber. Due to this reflux, the fluid from the last chamber is returned to the last chamber again. A blower 23 is provided as in the second washer of FIG. 1, but no ozone generator is present. In FIG. 9, the connections from the blower are shown only for the first few chambers for simplicity of illustration, but the air from the blower is forced into all the chambers. For mixing the waste, the waste is put into the first basket 153 of the mixer 151. Warm water at about 37-49 ° C and a small amount of alkali are placed in the first basket or chamber. Sufficient water is used to form a coagulum of waste. Excessive water forms a thin slurry. If a Milner Model 76032 continuous batch washer is used, in order to dispose of about 50 kg of waste, about 7. The water level is preferably 6 cm. The amount of alkali required will bring the pH of the mixture in the first basket to about 8. 0-8. Increase to 5. This promotes bacterial reproduction. In addition, certain foods such as dog foods can be added to speed the growth of bacteria. The first basket is then rotated as previously described. Further, air is blown into the first basket from the blower 23. In this way, the basket is rotated and air is blown to agitate the waste, thereby activating bacterial growth. After stirring for a predetermined time, for example, 20 minutes, the rotation of the first basket (the first basket and all other baskets if all baskets rotate in synchronization) is automatically stopped, and the drain pipe 155 is stopped. Open (and all drains connected to all other rooms). The liquid in the basket passes through the mesh of the first basket and is discharged to the drain pipe. The drain is then closed and the liquid is pumped into the fourth basket by pump 159. The contents of the first basket 153 are then automatically transferred to the second basket 153A (and the contents of each basket are transferred to the next basket). The stirring process by rotating the basket and blowing air is restarted. Thus, the treatment takes place while the waste is transported in the mixer. The substance 169 discharged from the mixer through the last basket is stored in a storage tank 171 where excess water is removed from an opening 173 in the bottom surface of the storage tank. The substance 169 thus treated can be used as a composting material. For example, the treated material is mixed with soil in the garden. Methane gas 175 is generated when treating the organic waste in the washing machine. This gas is discharged to the outside by the vacuum pump 177 and sent to the tank 179. The top surface of the chamber 25 in the washing machine is hermetically closed by a hood 181 to prevent leakage of methane gas. The methane gas contained in the tank 179 can be sold or can be used as a heat source for heating water injected into the washing machine from the water supply pipe 167. When methane gas is used as the hot water heat source, the methane gas is sent from the tank 179 to the burner 185 in the heater 183. Burner 185 burns methane to generate heat. Hot water is sent from the pipe 187 to the water supply pipe 167. The valve 189 controls the flow rate of water. Although the method of treating organic waste with an alkaline mixture has been described above, it is also possible to treat with an acidic mixture. Add acids such as acetic acid, carbonic acid and oxalic acid to the waste in the washer. The pH value is 2. 3-4. Sufficient acid is used to reduce to zero. In any of the above-mentioned methods of regeneration treatment, the wastewater discharged from the washing machine may be contaminated with heavy metals. To reduce the heavy metal content of the wastewater, the wastewater is exposed to ozone in the treatment unit 201 (see Figure 10). The waste water is transferred to the processing device 201 by the drain pipe 90 (or 111). Ozone is supplied from the ozone supply device 24 to the processing device. Ozone rises as bubbles in the wastewater and removes heavy metals. Wastewater from the treatment device 201 is flowed to a wastewater treatment facility through a pipe 203. From here the wastewater can be treated in a sewage treatment plant. The processor is regularly cleaned to remove accumulated contaminants. One chamber in the first and second washers 13, 15 of FIG. 1 can be modified to remove insoluble contaminants that are not affected by the treatment in the preceding chamber. This improvement chamber may be the last chamber adjacent to the outlet 33. The chamber is modified by a nest-like basket. The other parts of the chamber are the same as described above. Referring to FIG. 11, the basket configuration in the improvement chamber has an inner basket 211 and an outer basket 213. The inner basket 211 is attached inside the outer basket 213. The inner basket is attached to the outer basket so as to rotate integrally with the outer basket. A space 215 is provided between the inner basket and the outer basket. A rib 217 is provided on the inner peripheral side of each basket. The distance between the baskets is, for example, about 3 to 20 cm, but in any case, it is larger than the ribs 217 of the outer basket, so that all the objects to be processed located within the distance can freely pass over the ribs. The last chamber can be as large as 50% larger than the preceding chamber, so that the inner basket 211 in the last chamber can contain the entire quantity of the object to be treated. Both baskets are provided with a wire mesh having the desired aperture size. The inner basket mesh has a larger aperture size than the outer basket mesh. For example, when processing cellulose through a washer, the inner basket mesh is about 2. With 30 wires every 5 cm, the outer basket mesh is about 2. It has 40 to 60 wires every 5 cm. Enter the inner basket 211 through the opening 35 exiting the preceding chamber. As described above, the object to be treated is stirred by rotating the basket. Further air can be pumped in. An object to be treated, such as cellulose, passes through the mesh of the inner basket 211, but cannot pass through the mesh of the outer basket, and thus is held within the space between the baskets. Dirt such as husks, hair, and undigested food remains in the inner basket. The inner basket is provided with a non-perforated portion 219 that functions as a scoop to the outer basket. This portion 219 is located above the rib in FIG. Similarly, a non-opening portion 221 is provided above the rib so as to face the scoop 219. The non-opening portion 221 prevents the non-processed material in the space 215 from flowing back to the inner basket. The inner basket also has an open scoop 223. When the unprocessed material is removed from the chamber, the basket makes more complete rotation than during the agitation process. By this complete rotation, the cellulose located in the space 215 is moved to the scoop 219, prevented from re-entering the inner basket, and is carried out to the outside of the room. Cellulose is discharged from the lamp 77 (FIG. 1) and accumulated in the storage tank 79. The dirt in the inner basket is moved to the scoop 223 by the rotation and discharged from another lamp to another storage tank. The matters described above and shown in the drawings merely explain the principle of the present invention, and should not be interpreted restrictively in any sense.

Claims (1)

[Claims] 1 Cellulose, newsprint, rubber, glass or plus in disposable products A method of cleaning materials such as ticks,     Has a perforated basket that allows moisture to pass through but leaves the product inside A step of preparing a washing machine,     A process for putting the product, water, alkali and surfactant into the basket. And     Move the basket to agitate the product and contaminate the product during agitation A step of removing substances and cleaning,     Through the openings in the basket, the water and alkali, surfactants and The dyed material is discharged from the basket and only the cleaned product is And a step of allowing the residual material to remain in the sket. 2 When the product to be regenerated contains a cellulosic material and a non-cellulosic material At     The cellulosic material is formed by moving the basket to stir the product. Separated from the non-cellulosic material,     The discharging step further removes the cellulosic material through the openings in the basket. The non-cellulosic material remains in the basket as it drains from the basket The method according to claim 1, further comprising a step of pressing. 3 The washing machine is the first washing machine, and     The cellulosic material was placed in a second washer having a second perforated basket therein. Transporting process,     Adding water, alkali and a surfactant to the second basket;     Moving the second basket to stir the cellulosic material;     Through the opening of the second basket, the water, the alkali and the surfactant are removed. Discharging, leaving only the cellulosic material in the second basket The reproduction processing method according to claim 2, further comprising: 4 When the product to be recycled is a plastic product,     Put the product into the basket with water, alkali and surfactant The sand is further added to the basket in the step of Regeneration processing method. 5 When the product to be recycled is a rubber product such as old tire,     Before loading the product into the basket, the rubber product is crushed into rubber particles. A child, and the rubber particles are put into the basket. Regeneration processing method. 6 The product to be recycled is old newspaper or soiled wood pulp such as cellulose In some cases,     Put the product into the basket with water, alkali and surfactant In the process, it is necessary and sufficient to adjust the pH value of these mixtures to 10.5-14. The method according to claim 1, wherein an amount of alkali is added. 7 Inside the basket during the step of moving the basket to stir the product 7. The regeneration treatment method according to claim 1, 2, 4, 5, or 6, wherein air is blown into the air. Law. 8 Inside the basket during the step of moving the basket to stir the product Regeneration of claim 1, 2, 4, 5, 6, or 7, characterized in that ozone is injected into Processing method. 9 further comprising rinsing the product in the basket with water 7. The reproduction processing method according to claim 1, 2 or 6. 10 Recycle disposable products containing cellulosic and non-cellulosic materials Equipment for     Equipped with a first drainage channel that can contain water and discharge its contents A first chamber, and a mixture of the cellulosic material and water contained in the first chamber. The non-cellulosic material is perforated to allow the compound to pass through but remain inside. A first basket, and further by moving the first basket, The cellulosic material is agitated by agitating the disposable product contained within the cell. A first suitable for washing clothes, having a first stirring means for separating it from the lulose material. Washing machine,     Input means for receiving the cellulosic material and capable of containing moisture And a second chamber having a second drainage channel for discharging the contents thereof; Is accommodated in the chamber of the first basket and has an opening smaller than the opening of the first basket. A second opening is made to allow the cellulosic material to remain inside. And a second basket, and by moving the second basket, A second agitator for washing the cellulosic material by agitating the cellulosic material contained in the chamber A second washer suitable for washing clothes, having a stirring means;     An inlet connected to the first drainage channel and the thrower in the second washing machine An outlet connected to the stage, the mixture of the cellulosic material and water being added to the first Transfer means for transferring from the washing machine to the second washing machine. Characteristic recycling equipment. 11 A first mesh is provided on the first basket, and the first mesh is provided. Allows the mixture of the cellulosic material and water to pass through the non-cellulosic material When an opening is provided in the first basket which acts to allow the material to remain inside. Together, the second basket is provided with a second mesh, the second mesh To allow water to pass through, which is smaller than the opening in the first basket. The second basket that serves to keep the cellulosic material inside. The reprocessing facility according to claim 10, characterized in that an opening is provided in the retort. 12 Both the first and second washers have a plurality of chambers and a plurality of baskets. It is a continuous type washing machine that accommodates multiple loads of the disposable products at the same time. The regeneration treatment facility according to claim 10, wherein the regeneration treatment facility is capable. 13 Moisture extracted from the cellulosic material washed by the second washing machine 12. Separation means for separating are further provided, according to claim 10 or 11. One of the reprocessing facilities. 14 Blower for blowing air to the first washing machine during washing in the first washing machine Means are further provided to enhance the agitation effect and at the same time to prevent contamination of the disposable products. 12. A material which acts to initiate the biological degradation of dye material. Or any one of 12 reprocessing facilities. 15 For injecting ozone during cleaning in the first and second cleaning machines, 13. A zoning means is connected to these washing machines, as claimed in claim 10, 12. Or 14 of the reprocessing equipment. 16 A method for treating organic waste such as food and factory waste,     The organic waste has holes that allow water to pass through but remain inside. And a step of preparing a washing machine including a basket that is suitable for washing clothes,     Add the organic waste and water and either acid or alkali to the basket The process of throwing in,     Moving the basket to agitate the organic waste;     Blowing air into the basket while moving the basket, A method for treating organic waste, which comprises: 17 A step of recovering methane gas generated during stirring of the waste from the washing machine The method for treating organic waste according to claim 16, further comprising: 18 The basket is the first basket,     A second basket having an opening smaller than the opening in the first basket. And a step of providing     This organic waste after stirring the organic waste in the first basket Objects to the second basket and then move and move the second basket. A step of stirring the sent organic waste,     Blow air into the second basket while moving the second basket The method for treating organic waste according to claim 16, further comprising: 19 Before transferring the organic waste to the second basket, the first basket From the container, and the waste water is discharged from the organic waste by moving the second basket. Further comprising the step of charging the second basket into the second basket before stirring. 19. The method for treating organic waste according to claim 18.