JPWO2012165488A1 - Method and apparatus for cleaning and separating mixed materials - Google Patents

Abstract

It is an object of the present invention to efficiently wash and remove salts and harmful substances from waste materials containing salts and harmful substances so that the waste materials can be disposed and recycled. In the present invention, the mixed material (8) is charged into the separation liquid tank (7), and separated into a low specific gravity material (3) that floats due to a specific gravity difference from the separation liquid and a high specific gravity material (9) that settles, At least one of the low specific gravity material (3) and the high specific gravity material (9) is washed with the washing liquid (1), and the washing / separation method of the mixed material (8) supplying the washing waste liquid to the separation liquid tank (7) is provided. .

Description

  The present invention relates to a cleaning separation method and a cleaning separation apparatus for mixed materials composed of a plurality of types of materials including waste materials such as rubble, and in particular, salts and harmful substances are removed from mixed materials containing salts and harmful substances. The present invention relates to a method and an apparatus for cleaning and removing the mixed material.

  In recent years, with the diversification of life and industrial materials such as plastics and metal products, waste disposal has become very important. In particular, industrial waste discharged from factories, construction and demolition sites contains plastic materials in addition to conventional wood and concrete, and recycling of these waste materials (waste) is important. .

  Under such circumstances, when hazardous chemical substances leaked from factories or other facilities, or when harmful substances were mixed due to a large-scale fire, they were further immersed in seawater due to natural disasters such as typhoons and tsunamis. In this case, a large amount of waste material is generated temporarily, but in many cases it is difficult to recycle or landfill at the final disposal site.

  Therefore, at the final disposal site, in order to prevent leakage of harmful substances due to moisture such as raindrops that have fallen on the waste material, the waste material is landfilled in a state of being placed on an impermeable sheet, A method of treating the leachate by guiding it to one place is used (for example, see Non-Patent Document 1). In addition, there is a method of forcibly purifying with washing water in order to accelerate leakage of harmful substances from waste materials (for example, see Patent Document 1), and a method of regenerating treated water from washing waste water or leachate and recycling it as washing water. It has been proposed (see, for example, Patent Document 2). In addition, if the waste material contains only salt, there are many cases where it does not adversely affect the natural world even if it is leached, but thermal recycling, that is, direct incineration or RDF (Refuse Derived Fuel) When trying to do so, chlorine gas is generated in the incinerator or incinerator, and the furnace is damaged by salt, so that salt removal is necessary.

  In order to prevent this, as one of the methods for separating and recovering waste, as in the case of hazardous materials, the waste is dispersed in a separation liquid such as water, and the waste is separated by the difference in specific gravity. Is employed (see, for example, Patent Document 3). This method is widely used because it can be easily separated due to the specific gravity difference inherent to the material, but the solvent used for separation also has an effect of leaching out salts and soluble organic substances. This makes it possible to remove salts (especially chloride salts) and harmful substances that cause problems in furnace corrosion and generation of harmful gases during thermal recycling. However, in this process, the concentration of the salt or soluble organic substance in the separation liquid gradually increases, and the leaching cleaning efficiency gradually decreases. Therefore, a method of injecting and diluting the separation liquid can be employed, but in that case, it is necessary to drain an amount corresponding to the injection. That is, increasing the injection amount of the separation liquid is not preferable because not only the necessary separation liquid amount increases but also the drainage amount increases. On the other hand, reducing the injection amount of the separation liquid increases the risk of reaching a concentration that is difficult to release into the environment due to an increase in the concentration of salts and soluble organic substances in the separation liquid. Become.

  Further, since the salt and soluble organic matter in the separated liquid that has been leached remain in the separated waste, there is a considerable amount of waste, and in the recovery and reuse of the waste material, as illustrated in Patent Document 4, the cleaning liquid It is preferable to wash the waste material. However, the method of Patent Document 4 still requires a cleaning liquid, so that there remains a problem that the amount of waste liquid increases.

  On the other hand, a method of solidifying the waste by mixing it with cement or the like, and a method of washing the waste carbide, which is a raw material of RDF, with water and reusing the washed waste water generated in the reverse osmosis membrane have been proposed ( For example, see Patent Documents 4 and 5). At present, it is not easy to remove salt, so there are many cases where it is left outdoors and relies on natural cleaning with rain. Since it occurs in large quantities, reliance on rainwater leaching and cleaning requires a long time, and there is a problem that it is necessary to secure a large number of storage locations for waste materials.

Japanese Unexamined Patent Publication No. 11-179316 Japanese Unexamined Patent Publication No. 2001-79508 Japanese Unexamined Patent Publication No. 56-56246 Japanese Laid-Open Patent Publication No. 11-76983 Japanese Unexamined Patent Publication No. 2006-21956

Akihiro Taji, Tetsuo Kobayashi, “Dioxin treatment equipment in leachate”, Chemical Equipment, August 2003, p45

  In the method of solidifying cement in Patent Document 4, it is practically difficult to reliably process a large amount of washing water, and the washing water generated when washing waste directly is other than salt, that is, In the case where harmful substances, oils, surfactants, and the like are contained, there is a possibility that cement solidification may be hindered and quality may be deteriorated.

  In addition, as in Patent Document 5, the method of carbonizing once and then separating the reverse osmosis membrane can carbonize harmful substances and oils and surfactants that damage the reverse osmosis membrane. Similarly, the amount of carbonization that can be carbonized is limited due to problems in equipment, and RDF conversion only confines harmful substances in the carbide, and the harmful substances contained in the carbide are harmless. Therefore, there is a risk of causing harm as a by-product when carbide is incinerated in a furnace as RDF.

  An object of the present invention is to separate salts and harmful substances from mixed waste materials and to efficiently wash the waste materials so that the waste materials can be safely disposed or recycled. In particular, in the case of large-scale fires and natural disasters, it adheres to a large amount of wood and plastics, and in thermal recycling, it efficiently cleans and removes salt and harmful substances that cause damage to the furnace. It is to release safely and reuse.

In order to solve the above problems, the present invention has the following configuration.
(1) A separation step of putting a mixed material composed of a low specific gravity material and a high specific gravity material into a separation liquid tank and separating the mixture into a low specific gravity material that floats due to a specific gravity difference from the separation liquid and a high specific gravity material that settles;
A cleaning step of cleaning the mixed material with a cleaning liquid before the separation step, or a cleaning step of cleaning at least one of the low specific gravity material and the high specific gravity material with a cleaning liquid after the separation step; and A method for cleaning and separating a mixed material, the method including a supply step of supplying cleaning waste liquid from the cleaning step to the separation liquid tank.
(2) The mixed material cleaning / separating method according to (1), wherein the cleaning step is a cleaning step of cleaning at least one of the separated low specific gravity material and high specific gravity material with a cleaning liquid after the separation step. .
(3) The mixing according to (1) or (2), wherein at least one of the low specific gravity material and the high specific gravity material is caused to flow in a direction opposite to a direction in which the separation liquid flows in the separation liquid tank. Method for cleaning and separating materials.
(4) discharging at least a part of the washing waste liquid supplied to the separation liquid tank as a washing separation waste liquid, separating the washing separation waste liquid into a permeated liquid and a concentrated liquid by a semipermeable membrane, The method for cleaning and separating mixed materials according to any one of (1) to (3), wherein the permeate is discharged into a river or the sea, or reused as the cleaning liquid.
(5) The mixed material cleaning and separating method according to any one of (1) to (4), wherein the mixed material contains any one of a salt, a harmful substance, an oil component, and a surfactant.
(6) The method for washing and separating mixed materials according to (5), wherein the salt contains a chloride salt.
(7) The method for cleaning and separating mixed materials according to (5) or (6), wherein the harmful substance contains any one of a radioactive substance, a poisonous substance, and a pathogen.
(8) The at least one additive selected from the group consisting of an aggregating agent, an adsorbent, and an ion exchanger is added to the washing / separating drainage or the processing liquid of the washing / separating drainage according to (4) to (7). The method for cleaning and separating the mixed material according to any one of the above items.
(9) At least one selected from the group consisting of flotation or sedimentation treatment, sand filtration, microfiltration, and ultrafiltration after adding the additive to the washing separation waste liquid or the treatment liquid of the washing separation waste liquid The method for cleaning and separating a mixed material according to (8), wherein one solid-liquid separation process and a separation process using a semipermeable membrane are sequentially performed.
(10) The concentrated liquid is separated into a second permeated liquid and a second concentrated liquid by a second semipermeable membrane, and the second permeated liquid is reused as the cleaning liquid. 9. The method for washing and separating mixed materials according to any one of 9).
(11) The method for cleaning and separating a mixed material according to any one of (1) to (10), wherein a salt concentration of the cleaning liquid is 0.1% by weight or less.
(12) a separation liquid tank that separates a mixed material composed of a low specific gravity material and a high specific gravity material into a low specific gravity material that floats due to a specific gravity difference from the separation liquid and a high specific gravity material that settles;
A cleaning unit for cleaning the mixed material with a cleaning liquid in a front stage of the separation liquid tank, or a cleaning unit for cleaning at least one of the separated low specific gravity material and the high specific gravity material with a cleaning liquid in a subsequent stage of the separation liquid tank; And a mixed material cleaning / separating device comprising: a supply line for supplying the cleaning waste liquid collected from the cleaning section to the separation liquid tank.
(13) The cleaning / separation apparatus for mixed materials according to (12), further including a cleaning / separating drainage line that discharges at least a part of the cleaning drainage supplied to the separation liquid tank as cleaning / separating drainage.
(14) A semipermeable membrane that separates the washing separation drainage liquid into a permeate and a concentrate, and a discharge line that discharges the permeate to a river or the sea, or a reflux line that recirculates to the cleaning liquid. 13) A cleaning and separating apparatus for mixed materials according to 13).

  According to the present invention, it is possible to efficiently remove contained salt and harmful substances which are obstacles for recycling or reusing waste materials.

FIG. 1 is a schematic flow diagram showing a first embodiment of a method for cleaning and separating mixed materials according to the present invention. FIG. 2 is a schematic flow diagram showing a second embodiment of the mixed material cleaning and separating method according to the present invention. FIG. 3 is a schematic flow diagram showing another aspect of the second embodiment of the method for cleaning and separating mixed materials according to the present invention.

  Hereinafter, preferred embodiments of the present invention will be described with reference to the drawings. However, the scope of the present invention is not limited to these.

<First Embodiment>
FIG. 1 shows a first embodiment of a cleaning / separating apparatus for separately cleaning a mixed material according to the present invention. In the first embodiment, the mixed material 8 is put into the separation liquid tank 7 and is separated into a low specific gravity material 3 that floats due to a specific gravity difference from the separation liquid and a high specific gravity material 9 that settles (separation step). The cleaning liquid 1 is supplied to the cleaning liquid tank 2, and the low specific gravity material 3 floated and separated in the cleaning section is cleaned with the cleaning liquid 1 sent through the cleaning liquid line 4, and the high specific gravity material 9 is a high specific gravity material. After being taken out from the take-out line 6, it is similarly washed with the washing liquid 1 fed through the washing liquid line 4 (washing process). The cleaning drainage liquid after cleaning the low specific gravity material 3 or the high specific gravity material 9 is sent to the separation liquid tank 7 through the cleaning drainage line 5 (supply process), and as a separation liquid, It is subjected to specific gravity separation.

  In the present invention, the separation liquid in the cleaning liquid 1 and the separation liquid tank 7 is generally water or an aqueous solution. However, when a specific gravity separation threshold value is to be changed, a hydrocarbon solvent, alcohol, or a mixture thereof. Also, it is possible to use a liquid in which the specific gravity is changed by dissolving the solute. In the case of water, it is preferable to use natural water such as rain water, river water, ground water, etc., because costs can be reduced, but tap water can also be used. For example, when impurities such as turbidity are contained, turbidity, etc. It is also possible to apply the process.

  When rainwater is used for the cleaning liquid 1, rainwater can be collected in the cleaning liquid tank 2 using a rainwater collecting / collecting unit (not shown), or it can be directly mixed with rainwater without the cleaning liquid tank 2 or the cleaning liquid line 4. 8 can be washed, but in order to keep the amount of the washing liquid stable, it is preferable to provide the washing liquid line 2 from the washing liquid tank 2 or river or ground water.

  The separation liquid from which the suspended solids and the like are removed by specific gravity separation in the separation liquid tank 7 is appropriately discharged out of the separation liquid tank as a washing separation waste liquid in order to keep the amount constant. If there is no problem in discharging into the environment, it can be released as it is, but if the concentration of harmful substances exceeds the emission regulations, it must be treated. Such a treatment method is not particularly limited, but a separation treatment into a permeate and a concentrated solution by a semipermeable membrane is preferable both when the permeate is discharged and when the washing separation drainage is reused. In particular, reuse as the cleaning liquid in the present invention is preferable because the supply amount of the cleaning liquid can be reduced.

  The washing / separation drainage discharged from the separation liquid tank 7 through the washing / separation drainage line 37 is removed by the screen 10 after removing relatively large suspended matters that have overflowed without being settled, and then the agitation tank 14 by the supply pump 11. Sent to.

  In the agitation tank 14, at least one additive 13 selected from the group consisting of a flocculant, an adsorbent, and an ion exchanger is added, and in the washing separation drainage (that is, the liquid after having been separated by specific gravity using the washing drainage). Adsorbs salts, harmful substances, oils and surfactants dispersed or dissolved in Thereafter, the flocculant and the adsorbent are separated by a solid-liquid separation operation. Specifically, depending on the drainage properties, after flotation or sedimentation separation solid-liquid separation, at least one solid-liquid separation selected from the group consisting of sand filtration, microfiltration and ultrafiltration ensures reliable flotation and sedimentation separation. The fine particles that cannot be removed can be efficiently separated. As a result, the quality of the treated water is improved and contamination of the subsequent semipermeable membrane can be prevented. For example, when there are many light oils and surfactants, flotation separation is suitable, but in the case of flotation separation, pressurized flotation separation that introduces pressurized microbubbles is effective. In the case of sand filtration, it is possible to apply gravity-type filtration that naturally flows down, and it is also possible to apply pressure-type filtration in which a pressure tank is filled with sand. As the sand to be filled, single-component sand can be applied. For example, anthracite, silica sand, garnet, pumice, and the like can be combined to increase filtration efficiency. The microfiltration membrane and the ultrafiltration membrane are not particularly limited, and a flat membrane, a hollow fiber membrane, a tubular membrane, a pleat type, or any other shape can be used as appropriate. The material of the membrane is not particularly limited, and polyacrylonitrile, polyphenylene sulfone, polyphenylene sulfide sulfone, polyvinylidene fluoride, polypropylene, polyethylene, polysulfone, polyvinyl alcohol, cellulose acetate, and ceramics can be used. However, depending on the raw water state, there are some that are prone to deterioration, so care must be taken. Moreover, even if it is a filtration system, any of the pressure filtration system which pressurizes and filters supply water, and the suction filtration system which sucks and filters the permeation | transmission side are applicable. Furthermore, it is also possible to apply a pressure flotation filtration in which a flotation unit is provided in the flotation tank 17 and pressure filtration flotation combined with sand filtration or a submerged membrane filtration unit.

  The flocculant, adsorbent, and ion exchanger that can be charged into the stirring tank 14 are not particularly limited, and can be appropriately selected depending on the components of the washing waste water. In general, inorganic flocculants such as polyaluminum chloride and ferric chloride are preferable because they are inexpensive and high removal efficiency can be obtained by using polymer flocculants, activated carbon, and ion exchangers. Can do. For example, in the case of oil, a plastic carrier is preferable because of its high removal performance, and in the case of a radioactive substance, zeolite and ferrocyanide are preferable because they selectively adsorb the radioactive substance.

  Hereinafter, the case where the filtration unit is provided following the separation process by the pressure levitation will be described. In the case of separation processing by pressurized levitation, as shown in FIG. 1, bubbles are generated in the fine bubble generating tank 15 using water in which air is dissolved in the pressurized water tank 16 using the pressurized air injection pump 27. Let Then, the generated bubbles and aggregates are brought into contact with the floating tank 17 and floated to separate the aggregates (scum) and separate and remove from the scum discharge line 18. The scum can be disposed as it is, or can be separated into sludge 33 and sludge recovery water 34 through the dehydration unit 12 as shown.

  The water subjected to the pressure levitation treatment is stored in the pressure levitation treatment water tank 19, sent to the filtration unit 21 using the pressure pump 20, and processed by the filtration unit 21. In this case, the filtration unit 21 is preferably selected from the group consisting of sand filtration, filter cloth, microfiltration and ultrafiltration. However, when ultrafiltration with the best water quality is used, the latter semipermeable membrane unit is used. It is more preferable because contamination can be prevented. Although not shown, it is also preferable to increase the filtration efficiency in the filtration unit 21 by adding a flocculant or the like before the treatment in the filtration unit 21.

  After the filtrate of the filtration unit 21 is stored in the filtrate tank 23, it is sent to the first semipermeable membrane unit 25 by the pressurizing pump 24 and separated into a permeate and a concentrate. The permeate of the first semipermeable membrane unit 25 is discharged out of the system (river, sea, etc.) as a final treated water 31 from which salt and harmful substances have been removed, or a reflux line is provided. It can be reused as the cleaning liquid 1. Depending on the water quality, the concentrated liquid of the first semipermeable membrane unit 25 is pressurized by the booster pump 26 as needed, and then processed by the second semipermeable membrane unit 29, so that the second concentrated liquid and the second concentrated liquid Of permeate 30. Since the second permeate 30 is inferior in water quality to the permeate of the first semipermeable membrane unit 25, it is preferably reused as the cleaning liquid 1. On the other hand, the second concentrated liquid is preferably separated into a liquid that can be recovered and reused by the evaporation unit 28, etc., and a concentrated liquid or solid waste 35 and disposed of. The filtrate stored in the filtrate tank 23 may be discharged into the river or the sea as the discharge liquid 32 without being separated and reused by the semipermeable membrane unit 25, or by using the backwash pump 22. It may be processed again by the filtration unit 21.

In the present invention, the mixed material 8 is not particularly limited, and examples thereof include those containing any of salts, harmful substances, oils, and surfactants, and the mixed material 8 containing these includes the method of the present invention. Can be effectively cleaned and removed.
The salt is not particularly limited and may include alkali metals, alkaline earth metals, transition metal chloride salts, carbonates, sulfates, etc., and incinerators by reducing their concentrations. It is possible to prevent the deterioration of the battery and facilitate recycling. In particular, the chloride salt is converted to hydrogen chloride in the incinerator, and therefore it is highly necessary to remove it from the viewpoint of corrosion and toxic gas generation. In this specification, the terms “alkali metal”, “alkaline earth metal”, and “transition metal” are respectively referred to as “Group 1 elements” in the long-period periodic table (Nomenclature of Inorganic Chemistry IUPAC Recommendations 2005). , “Group 2 element” and “Group 3 to 11 element” are used synonymously.

  There is no restriction on the concentration of salt contained in the mixed material 8, and if it is contained even a little, the above-mentioned risk arises. However, if the salt concentration contained in the mixed material 8 exceeds 0.4% by weight, Since adverse effects are likely to occur, it is preferably suppressed to 0.4% by weight or less by washing. The cleaning liquid 1 used for this purpose is not particularly limited, and various waters such as rain water, river water, ground water, lake water, and tap water can be used. However, in view of cost performance and convenience, river water and lake water Can be used. Furthermore, since the amount of water taken in the cleaning liquid 1 can be reduced by reflux mixing the second permeate 30 as described above, it is preferable in terms of cost and environment. Although it is preferable to use water having a salt concentration of 0.1% by weight or less as the cleaning liquid 1, the semipermeable membrane has a very high salt removal rate of 99% or more. The concentration is usually 0.05% by weight or less, and it is very preferable because the cleaning liquid 1 having high quality can be obtained by circulating and reusing the permeated liquid obtained by subjecting the mixed waste water to the semipermeable membrane treatment. The salt concentration referred to here is the total evaporation residue concentration of a generally defined dissolved component (component that has passed through 0.45 μm filter paper).

  As for the harmful substances, oils and surfactants contained in the mixed material 8, the regulations differ depending on the recycling application of the mixed material 8, and therefore the concentration is appropriately reduced according to the regulations. In addition, examples of harmful substances include radioactive substances, poisonous substances, and pathogens, but the substances are not limited to these, and any substances that are regulated according to the location and application may be used.

  Representative harmful radioactive substances include, for example, strontium, iodine, cesium, plutonium and the like. Toxic substances include poisonous substances specified by the Deleterious Substances Control Law and government ordinances, various insecticides and herbicides. Drugs are also included. Examples of pathogens include pathogenic E. coli, designated infectious pathogens, viruses, nematodes, roundworms, and the like.

  The semipermeable membrane unit applicable to the present invention is not particularly limited, but for easy handling, a hollow fiber membrane-like or flat membrane-like semipermeable membrane is housed in a casing to form a fluid separation element (element). It is preferable to use what was loaded in a pressure vessel. When the fluid separation element is formed of a flat membrane, for example, generally a semipermeable membrane is wound in a cylindrical shape together with a flow path material (net) around a cylindrical central pipe having a large number of holes. As commercial products, reverse osmosis membrane element TM700 series and TM800 series manufactured by Toray Industries, Inc. can be mentioned. These fluid separation elements may be one, and it is also preferable to configure a semipermeable membrane unit by connecting a plurality of fluid separation elements in series or in parallel.

  As the semipermeable membrane material, a polymer material such as cellulose acetate polymer, polyamide, polyester, polyimide, vinyl polymer can be used. In addition, the membrane structure has a dense layer on at least one side of the membrane, and on the asymmetric membrane having fine pores gradually increasing from the dense layer to the inside of the membrane or the other side, or on the dense layer of the asymmetric membrane. Any composite film having a very thin functional layer formed of another material may be used.

  In the semipermeable membrane unit, since the supply liquid is concentrated, a scale inhibitor, acid, or alkali is added to the supply liquid of each semipermeable membrane unit to prevent scale precipitation due to concentration or to adjust pH. It is possible to In addition, it is preferable to implement addition of a scale inhibitor upstream from pH adjustment so that the addition effect can be exhibited. In addition, an in-line mixer may be provided immediately after the addition of chemicals, or the addition port may be in direct contact with the flow of the supply liquid to prevent sudden changes in concentration and pH near the addition port. preferable.

The scale inhibitor is a compound that forms a complex with a metal, metal ion, or the like in a solution and solubilizes the metal or metal salt, and an organic or inorganic ionic polymer or monomer can be used. Synthetic polymers such as polyacrylic acid, sulfonated polystyrene, polyacrylamide, and polyallylamine can be used as organic polymers, and natural polymers such as carboxymethylcellulose, chitosan, and alginic acid. Ethylenediaminetetraacetic acid and the like can be used as organic monomers. Can be used. Moreover, polyphosphate etc. can be used as an inorganic type scale inhibitor. Among these scale inhibitors, polyphosphate and ethylenediaminetetraacetic acid (EDTA) are particularly preferably used from the viewpoints of availability, ease of operation such as solubility, and cost. The polyphosphate refers to a polymerized inorganic phosphate material having two or more phosphorus atoms in a molecule typified by sodium hexametaphosphate and bonded with an alkali metal, an alkaline earth metal and a phosphate atom. Typical polyphosphates include tetrasodium pyrophosphate, disodium pyrophosphate, sodium tripolyphosphate, sodium tetrapolyphosphate, sodium heptapolyphosphate, sodium decapolyphosphate, sodium metaphosphate, sodium hexametaphosphate, and potassium salts thereof. Etc.
On the other hand, sulfuric acid, sodium hydroxide, and calcium hydroxide are generally used as the acid and alkali, but hydrochloric acid, oxalic acid, potassium hydroxide, sodium bicarbonate, ammonium hydroxide, and the like can also be used. However, in order to prevent an increase in scale components, it is better not to use calcium or magnesium.

  In the first embodiment shown in FIG. 1, the cleaning liquid line 4 is provided so as to clean both the low specific gravity material 3 and the high specific gravity material 9, but the cleaning liquid line 4 is cleaned so that only one of them is cleaned. There is no problem. Further, all of the washing waste liquid may be supplied to the separation liquid tank 7 or a part thereof may be supplied. Generally, since the low specific gravity material 3 that is floated and separated is a material that can be recycled or incinerated (thermal recycle), the method of cleaning only the low specific gravity material 3 using the cleaning liquid line 4 is economically preferable. Furthermore, when the water quality of the separation liquid in the separation liquid tank 7 deteriorates, a part of the cleaning liquid 1 can be directly supplied to the separation liquid tank 7.

<Second Embodiment>
Next, a second embodiment of the cleaning / sorting device and cleaning / sorting method for mixed materials according to the present invention will be described.
As a second embodiment according to the present invention, an example of an apparatus for washing the mixed material 8 with the washing liquid 1 and washing the salt, harmful substances, oil, surfactant and the like and then sending it to the separation liquid tank 7 is shown in FIG. Shown in In addition, about the same member as said 1st embodiment, the same code | symbol is attached | subjected and description is abbreviate | omitted.

  2, the cleaning liquid 1 is supplied to the cleaning liquid tank 2, and the mixed material 8 is cleaned through the cleaning liquid line 4 in the cleaning section (cleaning process). The cleaning drainage liquid after cleaning the mixed material 8 with the cleaning liquid 1 is sent to the separation liquid tank 7 through the cleaning drainage line 5 (supply process). In the separation liquid tank 7, suspended substances and solids mixed by washing are separated into a low specific gravity material 3 and a high specific gravity material 9, and separated from the low specific gravity material take-out line 3 and the high specific gravity material take-out line 6 as necessary. It is removed (fractionation process).

  The washing / separating drainage discharged from the separation liquid tank 7 is subjected to the same processing as that of the first embodiment through the washing / separating drainage line 37, purified, and reused.

<Another aspect of the second embodiment>
FIG. 3 is a schematic flow diagram showing another aspect of the second embodiment of the method for cleaning and separating mixed materials according to the present invention. In the second embodiment, when the washing waste liquid stored in the separation liquid tank 7 after washing the mixed material 8 is heavily contaminated, the amount of washing liquid can be increased, but as shown in FIG. 3, the washing liquid tank It is also preferable to supply the cleaning liquid directly from 2 to the separation liquid tank 7 through the bypass line 36 to reduce the drainage treatment and regeneration load after cleaning and separation.

  In the present invention, as in the second embodiment shown in FIGS. 2 and 3 and the modified example thereof, it is possible to separate the specific gravity after the washing of the mixed material 8 after the washing. Then, as in the first embodiment shown in FIG. 1, the mixed material 8 is put into the separation liquid tank 7 and the specific gravity separation is performed, and then the low specific gravity material 3 and the high specific gravity material 9 are washed with the washing liquid. There is no problem. However, in the case of the method of the first embodiment, since the mixed material 8 is preliminarily washed in the separation liquid tank 7, it is washed with an uncontaminated washing liquid, which is very efficient. Furthermore, if the flowing direction of the mixed material 8 is opposite to the flowing direction of the separation liquid, the untreated mixed material 8 having a large contamination comes into contact with the most contaminated separation liquid, and the mixed material 8 is separated by specific gravity. However, it is more efficient because it flows toward the relatively uncontaminated separation liquid.

  Although the invention has been described in detail and with reference to specific embodiments, it will be apparent to those skilled in the art that various changes and modifications can be made without departing from the spirit and scope of the invention. This application is based on a Japanese patent application filed on May 31, 2011 (Japanese Patent Application No. 2011-121595), a Japanese patent application filed on May 31, 2011 (Japanese Patent Application No. 2011-121596), Incorporated herein by reference.

  The present invention relates to a cleaning method and apparatus for efficiently cleaning and removing salt and harmful substances from waste materials containing salts and harmful substances, and disposing of the waste materials and making them recyclable. Efficient cleaning is possible by separating and reusing the cleaning and separation effluent used to remove salts and harmful substances with a semipermeable membrane.

1: Cleaning liquid 2: Cleaning liquid tank 3: Low specific gravity material 4: Cleaning liquid line 5: Cleaning drainage line 6: High specific gravity material take-out line 7: Separation liquid tank 8: Mixed material 9: High specific gravity material 10: Screen 11: Supply pump 12: Liquid removal unit 13: Additive 14: Stirring tank 15: Fine bubble generation tank 16: Pressurized water tank 17: Floating tank 18: Scum discharge line 19: Pressurized levitated water tank 20: Pressure pump 21: Filtration unit 22 : Backwash pump 23: filtrate tank 24: pressurization pump 25: first semipermeable membrane unit 26: booster pump 27: pressurized air injection pump 28: evaporation unit 29: second semipermeable membrane unit 30: first 2 permeate 31: final treatment liquid 32: discharge liquid 33: sludge 34: sludge recovery liquid 35: solid waste 36: bypass line 37: washing separation drainage line

Claims (14)

A separation step of putting a mixed material composed of a low specific gravity material and a high specific gravity material into a separation liquid tank, and separating into a low specific gravity material and a high specific gravity material that are settling due to a difference in specific gravity with the separation liquid;
A cleaning step of cleaning the mixed material with a cleaning liquid before the separation step, or a cleaning step of cleaning at least one of the low specific gravity material and the high specific gravity material with a cleaning liquid after the separation step; and A method for cleaning and separating a mixed material, the method including a supply step of supplying cleaning waste liquid from the cleaning step to the separation liquid tank.   The method for cleaning and separating a mixed material according to claim 1, wherein the cleaning step is a cleaning step in which at least one of the low specific gravity material and the high specific gravity material separated in the subsequent stage of the separation step is cleaned with a cleaning liquid.   The method for cleaning and separating a mixed material according to claim 1 or 2, wherein at least one of the low specific gravity material and the high specific gravity material is caused to flow in a direction opposite to a direction in which the separation liquid flows in the separation liquid tank.   At least a part of the washing waste liquid supplied to the separation liquid tank is discharged as washing separation waste liquid, the washing separation waste liquid is separated into a permeated liquid and a concentrated liquid by a semipermeable membrane, and the permeated liquid is The method for cleaning and separating mixed materials according to any one of claims 1 to 3, which is discharged into a river or the sea, or reused as the cleaning liquid.   The method for cleaning and separating a mixed material according to any one of claims 1 to 4, wherein the mixed material contains any one of a salt, a harmful substance, an oil, and a surfactant.   The method for washing and separating a mixed material according to claim 5, wherein the salt contains a chloride salt.   The method according to claim 5 or 6, wherein the harmful substance contains any one of a radioactive substance, a poisonous substance, and a pathogen.   8. At least one additive selected from the group consisting of a flocculant, an adsorbent, and an ion exchanger is added to the cleaning / separating effluent or the processing liquid of the cleaning / separating effluent. Cleaning and sorting method for mixed materials.   After the additive is added to the washing / separation waste liquid or the treatment liquid of the washing / separation waste liquid, at least one solid liquid selected from the group consisting of flotation or sedimentation separation, sand filtration, microfiltration and ultrafiltration The method for cleaning and separating a mixed material according to claim 8, wherein a separation process and a separation process using a semipermeable membrane are sequentially performed.   10. The method according to claim 4, wherein the concentrate is separated into a second permeate and a second concentrate by a second semipermeable membrane, and the second permeate is reused as the cleaning liquid. A method for cleaning and separating the mixed material according to the item.   The method for cleaning and separating mixed materials according to any one of claims 1 to 10, wherein the cleaning liquid has a salt concentration of 0.1 wt% or less. A separation liquid tank that separates a mixed material composed of a low specific gravity material and a high specific gravity material into a low specific gravity material that floats due to a specific gravity difference from the separation liquid and a high specific gravity material that settles;
A cleaning unit for cleaning the mixed material with a cleaning liquid in a front stage of the separation liquid tank, or a cleaning unit for cleaning at least one of the separated low specific gravity material and the high specific gravity material with a cleaning liquid in a subsequent stage of the separation liquid tank; And a mixed material cleaning / separating device comprising: a supply line for supplying the cleaning waste liquid collected from the cleaning section to the separation liquid tank.   The cleaning / separation apparatus for mixed materials according to claim 12, further comprising a cleaning / separating drainage line for discharging at least a part of the cleaning drainage supplied to the separation liquid tank as cleaning / separating drainage. 14. A semi-permeable membrane that separates the washing separation waste liquid into a permeate and a concentrated liquid, and a discharge line that discharges the permeate to a river or the sea, or a reflux line that returns to the cleaning liquid. Washing and separating device for mixed materials.

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