JP2008238025A - Residual concrete treatment device and residual concrete treatment method - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To provide a residual concrete treatment device and a residual concrete treatment method where treatment in which residual concrete is fractionated into water and remaining matter other than the water (aggregates such as sand and gravel) and residue (precipitates such as cement powder), and the water and the matter other than the water are reutilizable can be achieved with a simple structure and at a low cost as possible. <P>SOLUTION: The residual concrete treatment device comprises: a stirring part 1 stirring residual concrete and an additive; a separation part 2 separating the stirred matter stirred at the stirring part 1 into water and remaining matter other than water; and a storage tank 3 storing the water separated at the separation part 2. The stirring part 1 is provided with: a cavernous shaft body 10; a rotary body 11 rotating integrally with the cavernous shaft body 10; and a helical blade 12 arranged inside the rotary body 11. The separation part 2 receives the stirred matter exhausted from the opening of the rotary body 11, pours the water separated from the stirred matter to the storage tank 3, and recovers the remaining matter other than the water at a filtration bag 61. By this device, a cleaning stage where residual concrete is cleaned with cleaning water, a neutralization stage where stored water is neutralized with a neutralizer, and a flocculation stage where the stored water (neutralized water) is flocculated with a flocculant are performed. <P>COPYRIGHT: (C)2009,JPO&INPIT

Description

  This invention is the remainder of the concrete (remaining concrete) generated during concrete placement work, the remaining concrete generated by the business activities of the ready-mixed concrete manufacturer and the secondary product manufacturer using ready-mixed concrete, the town, etc. In recent years, the remaining concrete generated at the end of the construction work for river construction in public works using ready-mixed concrete, buildings using ready-mixed concrete, and renovation work for structures have been separated and sorted. The present invention relates to a residual con treatment apparatus and a residual con treatment method for effectively reusing a precipitate containing aggregates and suspended matters such as cement powder and treated water.

  In recent years, it has been unavoidable that residual concrete remains at the bottom of mixer trucks and high-pressure pump trucks due to concrete placement work, such as construction and civil engineering, which has been increasing in towns, etc. To install and re-use equipment for installation and re-use due to problems of installation space and equipment costs, as well as construction work such as truck and sling work for installation, unic and crane work Since it is dangerous to perform the installation work in the inside, in reality, it is appropriate when it is solidified to a certain extent by being buried, returned, or left at an appropriate place on the construction site. It has been crushed to size and treated as waste concrete.

  The washing water after washing the mixer truck, the pump truck, and other equipment has been discharged in a state of flowing down into a gutter or a drain outlet on the side of the road.

  The remaining kon that has been buried, returned, or left standing exhibits an alkalinity of pH 11 or more, and has been discharged into the ground as alkaline turbid water that has penetrated underground or becomes rainwater.

  Although there are some manufacturers that have installed processing equipment, etc. for raw concrete manufacturers and secondary product manufacturers that handle concrete, there are also suppliers that release almost in the state of running down into rivers and streams, etc. Have been deported.

  In the method of solidifying the residual concrete at the construction site and processing it as it is or by crushing it, cement such as sand, gravel or other aggregates cannot be used again for raw concrete. It is not enough to make effective use of the product widely, and in order to entrust the disposal to a waste contractor when discarding the remaining solid waste, the collection transporter, the processing contractor, the manifest slip, the processing contract agreement, Revenue stamp costs, waste disposal costs, etc. are required, and many labors and expenses are expended. Depending on the prefecture, there are many problems such as applying an industrial waste tax to the waste to be treated.

  Also, in the technology of washing the remaining components with a mixer and separating the aggregates, the aggregate can be reused, but since there is only one entrance for the mixer, the remaining components are continuously fed into the mixer for processing. However, in the case of continuous processing, it is preferable to stop the processing one by one from the viewpoint of safety and quality, and to put in the remaining components and wash with water. At the construction site, there was a problem with processing capacity.

  For such various problems, for example, as an apparatus for efficiently treating construction sludge generated in the field, sludge obtained by settling and separating coarse solids in a storage section storing construction sludge, such as Trommel It is sent to the sludge fractionation device, and the contained solid content is further separated. Next, the sludge containing only fine solids is mixed with the flocculant with the flocculant addition device, and the flocified sludge is squeezed with the dehydration treatment device, and the dehydrated cake There is a coagulant adding device for sludge that is separated into water and water (see, for example, Patent Document 1).

  In addition, the fresh ready-mixed concrete is supplied to the first separator of the vibration sieve type, and the aqueous solution of the cement setting retarder passes through the layer to be separated on the sieve and drops with the cement from the sieve. The crude aggregate is separated while being sprayed, and the raw fresh concrete is separated into fine aggregate and sludge water mainly composed of cement water using a screw type, trommel type or vibrating sieve type second separator. There is a reuse method (see, for example, Patent Document 2).

  Further, the residual raw waste water discharged from the concrete mixer truck is allowed to flow down along the inclined chute and is introduced into the trommel separator from one end surface of the trommel separator. There is a gravel recovery system from residual raw concrete wastewater that is allowed to fall naturally into a sedimentation tank formed by excavating the site directly under the separator, while discharging gravel from the gravel outlet formed on the other end surface of the trommel separator. Yes (see, for example, Patent Document 3).

Furthermore, the remaining ready-mixed concrete is discharged into the car wash chute, diluted, washed and supplied to the octatron melt with sludge water, separated into gravel, sand and sludge water by the octatron melt, and the separated ready-mixed concrete is separated into a sand separator. There is a method for treating residual ready-mixed concrete in which clean sand is separated, a part of the separated sludge water is sent to a car wash chute, and the remaining part is separated into sludge and filtered water by a dehydrator (for example, see Patent Document 4). .
JP 2006-167583 A JP-A-9-123156 JP-A-8-299845 JP-A-6-134748

  However, in the apparatus described in Patent Document 1, a storage unit that settles and separates the coarse solid content from the construction sludge stored in the storage unit, a sludge separation device such as a trommel that separates the solid content from the coarse solid content, a fine solid Since the coagulant adding device for mixing the coagulant with the sludge containing only the fraction and the dehydration processing device for separating the flocked sludge into the dewatered cake and the water are provided, the entire device becomes large and the processing cost is increased accordingly.

  In the method described in Patent Document 2, an aqueous solution of a cement setting retarder is sprayed on the ready-mixed concrete supplied to the first separation device to separate the cement and the coarse aggregate, and the fine aggregate and the cement are separated by the second separation device. In addition, the technology for separating sludge water into detoxified water and cement is not disclosed because the sludge water is separated into sludge water mainly composed of water and reused as raw concrete raw material. .

  The system described in Patent Document 3 collects gravel from residual raw concrete wastewater discharged from a concrete mixer truck, and does not disclose a method for treating not only wastewater but also raw concrete.

  In the treatment method described in Patent Document 4, octatron melt is used to dilute and clean fresh concrete while pouring with sludge water, and to separate gravel, sand, and sludge water, a sand separator that separates clean sand from residual fresh concrete, Since it is equipped with a flow rate adjustment tank that supplies concrete to the sand separator at a constant flow rate and a dehydrator that separates the remaining sludge water into sludge and filtered water, this also requires a large amount of equipment, and the processing cost increases accordingly.

  This invention was made in view of the problems in such conventional devices, methods, and systems, with the aim of reducing the waste discharged from the construction site, and paying attention to the effective use of the remaining components, It can be separated efficiently without solidifying the remaining components, and aggregates, suspended matter including cement powder, etc. contained in the remaining components can all be reused, and the aggregate, cement powder, and water can be reused continuously. In addition to being able to obtain water in a safe state, without being outsourced to a processing contractor, etc., it is possible to obtain such a thing with the simplest possible structure and low cost. An object of the present invention is to provide a remaining-con processing apparatus and a remaining-con processing method.

In order to achieve the above-mentioned object, the residual-con treatment apparatus of the present invention separates water and a residue other than water from the stirring unit that stirs the residual component and the additive, and the stirring material stirred in the stirring unit. A separation unit and a storage tank for storing water separated by the separation unit;
The stirring unit includes a hollow shaft body that is rotatably supported, and a cylindrical rotating body in which the hollow shaft body is inserted and rotated around the hollow shaft body, with one end opened and the other end closed. And a spiral blade that is attached over the outer wall of the hollow shaft body and the inner wall of the rotating body and conveys the agitated material from the closed side of the rotating body to the opening side in accordance with the direction of rotation of the hollow shaft body. Is supplied into the hollow shaft body from one end side of the hollow shaft body located on the opening side of the rotating body, and is introduced into the rotating body from the other end side of the hollow shaft body,
The separation unit receives the agitated material discharged from the opening of the rotating body, puts water separated from the agitated material into the storage tank, and collects residues other than water.

  In the case of processing the residual component with this residual component treatment apparatus, as described in the residual component treatment method described later, first, the residual component and washing water as an additive are introduced into the rotating body from the hollow shaft body as described above and rotate. The remaining container and washing water are agitated in the rotating body to wash the remaining container, and this agitated material is conveyed from the closed side of the rotating body to the opening side by the spiral blades, discharged from the opening of the rotating body, and separated by the separation unit. It is accepted. In the separation unit, the water separated from the agitated material enters the storage tank, and the residue other than water is collected. At this time, the rotating body functions as a cleaning tank for cleaning the remaining components.

  Next, the water in the storage tank after washing and the neutralizing agent as an additive are similarly introduced from the hollow shaft body into the rotating body, and the water and the neutralizing agent are stirred in the rotating rotating body. The blade is conveyed from the closed side of the rotating body to the opening side by the blades, is discharged from the opening of the rotating body, and is received by the separation unit. In the separation unit, the water separated from the agitated material enters the storage tank, and the residue other than water is collected. Such treatment is repeated until the water is neutralized. At this time, the rotating body functions as a neutralization tank for neutralizing water.

  Further, the water in the storage tank after neutralization (neutralized water) and the flocculant as an additive were similarly introduced into the rotating body from the hollow shaft body, and the water and the flocculant were stirred and generated in the rotating rotating body. Aggregates are conveyed from the closed side of the rotating body to the opening side by the spiral blades, discharged from the opening of the rotating body, and received by the separation unit. In the separation unit, the water separated from the agglomerates enters a post-treatment water tank, and residues other than water are collected. At this time, the rotating body functions as a coagulation tank for purifying water.

  In this remaining control apparatus, it is preferable that a stirring piece protruding toward the hollow shaft body is attached to the inner wall of the rotating body in the spiral space partitioned by the spiral blades provided in the rotating body. By providing a stirring piece in the rotating body, the stirring object is repeatedly lifted by the stirring piece to some extent as the rotating body rotates and then falls off the stirring piece. Such operations are repeated, so that not only cleaning, neutralization and agglomeration efficiency are further increased, but also their action is promoted.

  The stirring pieces are preferably attached at an angular interval of 180 ° with respect to the hollow shaft body. Thereby, the washing | cleaning by a stirring piece, neutralization, and a coagulation effect | action can be improved more.

  Moreover, it is preferable to provide a rotational drive means for rotationally driving the hollow shaft body or the rotating body. In this case, since the rotating body automatically rotates by the rotation drive means, compared with the case where the rotating body is manually rotated, the remaining container and washing water during cleaning, water and neutralizing agent during neutralization, and neutralization during aggregation Easily agitate water and flocculant.

  In addition, it is connected to one end of the hollow shaft body and the additive supply side, and lifts and lowers the remaining container and the additive through the hollow shaft body from the outlet formed on the other end side of the hollow shaft body into the rotating body. It is preferable to provide a possible residual container / additive input part. By this structure, the operation | work which supplies a residual container and an additive (washing water, the water of the storage tank before neutralization, the water of the storage tank after neutralization) to a rotary body becomes easy.

  Further, the remaining shaft of the hollow shaft body is connected to one end portion on the additive supply side, and the remaining portion can be moved up and down through the hollow shaft body and ejected from the jet port formed on the other end side of the hollow shaft body into the rotating body. It is preferable to include a condenser charging part and an additive charging part that causes the additive to be ejected through the hollow shaft from the other end of the hollow shaft into the rotating body. With this configuration, the remaining container is supplied from the remaining container charging section, and the additives (washing water, water in the storage tank before neutralization, and water in the storage tank after neutralization) are supplied into the rotating body from the additive charging section. Work becomes easy.

  In addition, until the water in the storage tank is neutralized, the water in the storage tank is circulated to the residual condenser / additive input section or the additive input section. It is desirable that a Japanese medicine is supplied into the rotating body.

  In addition, after the water in the storage tank is neutralized, the neutralized water in the storage tank is circulated to the residual condenser / additive charging section or additive charging section, and the neutralized water and addition of the storage tank are added from this charging section. It is desirable that the flocculant as a product is supplied into the rotating body.

  The separation unit includes a hopper arranged to receive the agitated material discharged from the opening of the rotating body before neutralization, and an inclined channel arranged on the storage tank. One end is connected to the lower opening of the hopper, and the other end is attached with a filter bag for storing the residue, and a large number of water is allowed to flow down to the storage tank while the agitated material flows in the portion located on the storage tank. It is preferable to have micropores. With this configuration, water contained in the agitated material is accumulated in the storage tank, and the residue is accommodated in the filter bag.

  In addition, the separation unit includes a flow path for flowing the aggregate discharged from the opening of the rotating body after neutralization, and a treated water tank arranged corresponding to the flow path, and the flow path has one end at a lower portion of the hopper. It is preferable that the other end is attached to the other end with a filter bag for accommodating residues other than water from the aggregate after neutralization, and the filtered water from the filter bag is preferably stored in the treated water tank. With this configuration, water contained in the aggregate is accumulated in the treated water tank, and the residue is accommodated in the filter bag.

  In addition, the separation unit flows the stirrer discharged from the opening of the rotating body into the slant channel before neutralization, among the slant channel for agitation and the agglomerate channel connected to the hopper. After the summation, it is preferable to provide a switching valve that is controlled so that the aggregate discharged from the opening of the rotating body flows in the flow path. In this case, since the flow of the water before neutralization and the water after neutralization is controlled by the switching valve, the stirrer and aggregate can be efficiently separated into water and other residues and residues.

  In addition, it is preferable that the remaining-con processing apparatus is constructed in a container that is detachably mounted on the transporter or on a movable carriage. This not only facilitates the movement and installation of the remaining-con processing apparatus, but also facilitates the remaining-con processing at the construction site.

On the other hand, the remaining-con processing method of the present invention includes a hollow shaft body that is rotatably supported, and the hollow shaft body that is inserted into the hollow shaft body so as to be rotatable around the hollow shaft body. A cylindrical rotating body that is attached to the outer wall of the hollow shaft body and the inner wall of the rotating body, and a spiral blade that conveys the agitated material from the closed side to the opening side of the rotating body according to the rotation direction of the hollow shaft body. Using the stirring section
The remaining condenser and washing water are supplied from one end side of the hollow shaft body located on the opening side of the rotating body of the stirring unit to the hollow shaft body, and the remaining condenser and washing water are rotated from the other end side of the hollow shaft body. While being introduced into the body and stirring the remaining container and washing water by the rotation of the rotating body, the stirring material is conveyed from the closed side of the rotating body to the opening side by the spiral blade, and the stirring material discharged from the opening of the rotating body is And a washing process for separating the residue other than water,
The water and neutralizing agent separated in the washing step are introduced into the rotating body from the hollow shaft body in the same manner as described above, and the stirring material is stirred by the spiral blade while stirring the water and the neutralizing agent by rotating the rotating body. A neutralization step of repeating until the water is neutralized, transporting from the closed side to the open side, and separating the stirred product discharged from the opening of the rotating body into water and a residue other than water,
Water (neutralized water) separated by the neutralization step and the flocculant are introduced into the rotating body from the hollow shaft body in the same manner as described above, and the agglomerates are formed by the spiral blade while stirring the water and the flocculant by the rotation of the rotating body. A coagulation step for conveying the aggregate from the closed side of the rotating body to the opening side and separating the aggregate discharged from the opening of the rotating body into water and a residue other than water;
It is characterized by providing.

  In this residual con treatment method, the rotating body functions as a washing tank in the washing process, as a neutralization tank in the neutralization process, and as a coagulation tank in the aggregation process as described above.

According to the present invention, the following effects can be obtained.
(1) According to the inventions described in claims 1 and 13, the waste discharged from the construction site can be reduced, and the remaining components can be effectively used. In other words, it can be separated efficiently without solidifying the remaining kon, aggregate, cement powder, etc. contained in the remaining kon can be reused, and all the aggregate, cement powder, and water can be reused continuously. In addition to being able to be separated without requiring much effort, without entrusting it to a processing company, and the treated water is harmless and can be obtained in a safe state, such a structure can be obtained with a simple structure and at a low cost. realizable. Furthermore, a series of processes of washing, neutralization and aggregation can be performed efficiently in a short time.
(2) According to the invention described in claim 2, not only washing, neutralization and aggregation efficiency are further enhanced, but also their action is promoted.
(3) According to invention of Claim 3, the washing | cleaning by a stirring piece, neutralization, and a coagulation effect | action can be improved more.
(4) According to the invention described in claim 4, compared with the case where the rotating body is manually rotated, the remaining container and washing water at the time of washing, water and neutralizing agent at the time of neutralization, and neutralizing water at the time of aggregation The flocculant can be stirred easily.
(5) According to the invention described in claim 5, it is easy to supply the remaining components and additives (washing water, water in the storage tank before neutralization, water in the storage tank after neutralization) into the rotating body. Become.
(6) According to the invention described in claim 6, the remaining components are added from the remaining components input part, and the additives (washing water, water in the storage tank before neutralization, water in the storage tank after neutralization) are added into the additive. The operation of supplying the rotating body from the respective parts becomes easier.
(7) According to the ninth aspect of the present invention, water and residue (aggregates such as sand and gravel) contained in the stirred product can be efficiently separated with a simple structure.
(8) According to the invention of the tenth aspect, water and residue (precipitate such as cement powder) contained in the aggregate can be efficiently separated with a simple structure.
(9) According to the eleventh aspect of the present invention, it is possible to efficiently separate the agitated material and the agglomerate into water and a residue or residue other than water.
(10) According to the twelfth aspect of the present invention, not only the remaining component processing apparatus can be easily moved and installed, but also the remaining component processing at a construction site or the like is facilitated.

  Hereinafter, the present invention will be described in more detail with reference to embodiments.

  As shown in FIG. 1, the basic processing flow of the remaining-con processing apparatus and the remaining-con processing method of the present invention is divided into a cleaning process, a neutralization process, and an aggregation process. In general, in the cleaning process, the remaining container and washing water are supplied into the rotating body (cylinder member), the remaining container is washed by the rotation of the rotating body, and the water separated from the agitated material is stored in the storage tank by the separation unit. Residues other than water (aggregates such as sand and gravel) are collected and reused.

  In the neutralization process, the water and neutralizing agent in the storage tank after washing are supplied into the rotating body, the water is neutralized by the rotation of the rotating body, and the water separated from the agitation is stored in the storage tank by the separation unit. Residues other than water (smaller aggregates) are collected and reused. Such treatment is repeated until the water is neutralized. This neutralization step is performed immediately after the start of the cleaning step, and the cleaning step and the neutralization step are substantially parallel.

  In the flocculation step, the water in the storage tank after neutralization (neutralized water) and the flocculant are supplied into the rotating body, the water is aggregated by the rotation of the rotating body, and the water separated from the aggregate by the separation unit is treated water tank The residue is collected for use and reused. Residues other than water (precipitates such as cement powder) are collected and reused. The precipitate is a variety of raw material components (limestone, clay, silica, iron oxide, gypsum, etc.) necessary for the production of cement.

  The outline | summary of the residual component processing apparatus for performing such a washing | cleaning process, a neutralization process, and an aggregation process is demonstrated. The schematic block diagram of the remaining-con processing apparatus which concerns on the one Embodiment is shown in FIG.2 and FIG.3. This residual-con treatment apparatus includes a stirring unit 1 that stirs the residual con and the additive, a separation unit 2 that separates the stirrer stirred by the stirring unit 1 into water and a residue other than water, and before neutralization. The storage tank 3 for storing the water separated from the agitated product in the separation unit 2, the treated water tank 4 for collecting the water separated in the separation unit 2 from the aggregate after neutralization, and the agitation unit 1 for the remaining components and additives And a remaining component / additive charging unit (hopper) 5 to be supplied to the vehicle.

  The agitating unit 1 includes a hollow shaft 10 that is rotatably supported, and a cylinder in which the hollow shaft body 10 is inserted and rotated around the hollow shaft body 10. One end is open and the other end is closed. And a spiral blade that is attached over the outer wall of the hollow shaft body 10 and the inner wall of the rotary body 11 and conveys the agitated material from the closed side of the rotary body 11 to the opening side according to the rotation direction of the hollow shaft body 10. 12, and a stirring piece 13 that is attached to the inner wall of the rotating body 11 in the spiral space partitioned by the spiral blades 12 provided in the rotating body 11 and protrudes toward the hollow shaft body 10.

  The hollow shaft body 10 is rotatably supported by a bearing 15 </ b> A on one end side and rotatably supported by a bearing 15 </ b> B on the other end side via a rotating shaft 40. When the hollow shaft body 10 rotates, the rotating body 11 also rotates integrally with the spiral blade 12. The hopper 5 is connected to one end portion of the hollow shaft body 10 located on the opening side of the rotating body 11.

  In such a remaining container processing apparatus, first, in the cleaning step shown in FIG. 2A, the remaining container is put into the hopper 5 together with the cleaning water. The charged residual condenser and washing water are ejected from the ejection port (see reference numeral 10a in FIG. 18) formed on the other end side of the hollow shaft body 10 to the closed side in the rotating body 11 through the hollow shaft body 10. The In parallel with this, the rotating body 11 is rotated by the motor 16 through the hollow shaft body 10. The rotating direction of the rotating body 11 is a direction in which the agitated material is conveyed to the opening side of the rotating body 11 by the spiral blade 12. Along with the rotation of the rotating body 11, the remaining container is conveyed from the closed side of the rotating body 11 to the opening side while being washed with the washing water by the spiral blade 12.

  The agitated matter discharged from the opening of the rotating body 11 by the rotation of the rotating body 11 is received by the separation unit 2. As will be described in detail later, the separation unit 2 includes a hopper 20 arranged to receive the agitated material, and the agitated material received by the hopper 20 is accommodated in the filter bag 61. As described later, in the separation unit 2, the agitated material is separated into water and a residue (aggregate) other than water, but the separated water is collected in the storage tank 3, and the residue other than water is collected by the filter bag 61. Is done. Further, the filtrate from the filter bag 61 is accumulated in the overflow tank 50 described later. The water stored in the storage tank 3 is circulated to the hopper 5 by the pump 22 and used as cleaning water.

  The neutralization process shown in FIG. 2 (b) is started with the point in time when the agitated material begins to be discharged from the opening of the rotating body 11. In this neutralization step, the washed water (water in the storage tank 3) and the neutralizing agent are put into the hopper 5. The neutralizing agent is accommodated in the container 23 and is transferred to the hopper 5 by the pump 24. Water and neutralizing agent are ejected from the ejection port on the other end side of the hollow shaft body 10 to the closed side in the rotating body 11 through the interior of the hollow shaft body 10 as described above. The water is neutralized while the water and the neutralizing agent are agitated in the rotating rotating body 11. The agitated material is conveyed from the closed side of the rotating body 11 to the opening side by the spiral blade 12, discharged from the opening of the rotating body 11, and received by the hopper 20 of the separation unit 2. The agitated material received by the hopper 20 is accommodated in the filter bag 61. As described above, in the separation unit 2, the agitated material is separated into water and a residue other than water (smaller aggregate), but the separated water is accumulated in the storage tank 3, and the residue other than water is stored in the filter bag 61. To be recovered. Further, the filtrate from the filter bag 61 is accumulated in the overflow tank 50. The water stored in the storage tank 3 is circulated to the hopper 5 by the pump 22 and used as cleaning water.

  Since the pH of the water in the storage tank 3 is detected by the sensor, the above process is repeated until neutralization (until the pH value becomes approximately 7). When the water in the storage tank 3 is neutralized, the charging of the water in the storage tank 3 and the neutralizing agent to the hopper 5 is stopped, and the water in the rotating body 11 is discharged from the opening and almost neutralized. The process ends.

  In the flocculation step shown in FIG. 3, the water (neutralized water) and the flocculating agent in the storage tank 3 after neutralization are put into the hopper 5. The flocculant is accommodated in the container 26 and is transferred to the hopper 5 by the pump 27. Water and the flocculant are ejected from the ejection port on the other end side of the hollow shaft body 10 to the closed side in the rotating body 11 through the inside of the hollow shaft body 10 as described above. Water and the flocculant are stirred in the rotating rotator 11, and aggregates (floc) are generated in the rotator 11.

  The aggregate is conveyed from the closed side of the rotating body 11 to the opening side by the spiral blade 12, discharged from the opening of the rotating body 11, and received by the hopper 20 of the separation unit 2. The agglomerates received by the hopper 20 are now accommodated in a filter bag 21, and water separated from the agitated material by the filter bag 21 enters the treated water tank 4, and residues other than water (precipitates such as cement powder) are collected. Collected in the filter bag 21. The water accumulated in the treated water tank 4 is circulated to the hopper 5 by the pump 25 and used as cleaning water. When the water in the storage tank 3 is almost exhausted, the addition of the water in the storage tank 3 and the coagulant to the hopper 5 is stopped, and the coagulation process is completed when the water in the rotating body 11 is almost exhausted from the opening. .

  By a series of processes of this washing process, neutralization process, and agglomeration process, the remaining components are collected as precipitates such as aggregates such as sand and gravel and cement powder, and the water used for the treatment is purified and treated water tank 4 It collects in.

  Since the water in the treated water tank 4 after the completion of the coagulation process is sufficiently purified, it may be discharged into the river as it is, or may be stored in the treated water tank 4 and used as washing water at the next remaining container treatment. May be used.

  Thus, according to this residual-con processing apparatus, the rotating body 11 of the stirring unit 1 serves as a washing tank in the washing process, and serves as a neutralization tank (substantially washing / neutralization tank) in the neutralization process. Then, since it functions as a coagulation tank, a series of processes of washing, neutralization and coagulation can be performed efficiently in a short time.

  In the above-mentioned remaining-con processing apparatus, the position of the hopper 5 as the remaining-container / additive adding unit is fixed, but it may be movable up and down. For example, as described later, the pipe connected to the hopper 5 is a bellows pipe that can be expanded and contracted. When the remaining condenser is introduced, the position of the hopper 5 is lowered, and after the introduction, the position of the hopper 5 is raised. In addition to the easy charging of the container, the remaining container, washing water, and the like are easily supplied into the rotating body 11 by natural fall.

  Moreover, although the said residual-cone processing apparatus is provided with only one hopper 5 as a residual-container and additive addition part, the residual-container injection part which spouts residual condenser through the hollow shaft 10 in the rotary body 11, and an additive It may be provided with an additive charging part for jetting the liquid into the rotating body 11 through the hollow shaft body 10. 4 and 5 show schematic configuration diagrams of the remaining-con processing apparatus according to this case.

  Since this remaining-container processing apparatus has the same configuration as the apparatus shown in FIGS. 2 and 3 except that it includes a hopper 6 as a remaining-container input unit and a hopper 7 as an additive input unit, description thereof will be omitted. Both the hopper 6 and the hopper 7 are connected to one end of a hollow shaft body 10 located on the opening side of the rotating body 11. Further, the pipe connected to the hopper 6 is an expandable / contractible bellows pipe.

  Since the cleaning process, neutralization process and agglomeration process by this residual condenser treatment apparatus are almost the same as described above, only the differences will be described.

  In the cleaning step (a) of FIG. 4, the remaining container is put into the hopper 6 and the washing water is put into the hopper 7. The water in the storage tank 3 is circulated to the hopper 7 by the pump 22 as cleaning water. 4 (b), the neutralizing agent in the container 23 is introduced into the hopper 7 by the pump 24, and the water in the storage tank 3 is circulated to the hopper 7 by the pump 22 as cleaning water. In the flocculation step of FIG. 5, the flocculant in the container 26 is charged into the hopper 7 by the pump 27 and the water in the treated water tank 4 is circulated to the hopper 7 by the pump 25 as cleaning water.

  Next, regarding the remaining-con processing apparatus having the structure shown in FIGS. 2 and 3, the partially broken perspective view is shown in FIG. 6, the plan view (top view) is shown in FIG. FIG. 8 is a sectional view taken along line AA, FIG. 9 is a sectional view taken along line BB in FIG. 7, FIG. 10 is a sectional view taken along line CC in FIG. 7, and FIG. The figure is shown in FIG. However, the same elements as those shown in FIGS. 2 and 3 are denoted by the same reference numerals.

  This remaining container processing device is constructed in a container 300 that can be placed on a transport vehicle (such as a hook-roller vehicle), and wheels 301 are attached to the bottom rear side of the container 300 so as to be rotatable in all directions. A leg 302 projects from the front side. Further, a door 311 that can be opened and closed to the left and right is provided on the rear side of the container 300, and a staircase 312 is prepared so that the remaining containers can be easily put into the hopper 5. Further, on the front side of the container 300, a hook hook 303 for hooking a hook of a hook roller is attached.

  On the front side in the container 300, the stirring unit 1 is disposed below the stirring unit 1, that is, the rotating body 11, and the treatment water tank 4 is disposed next to the stirring unit 1, and on the rear side, below the hopper 5. An overflow tank 50 is arranged.

  The rotating body 11 constituting the stirring unit 1 has a regular hexagonal shape in this embodiment, and the spiral blade 12 disposed inside the regular hexagonal rotating body 11 has a shape as shown in FIG. 12, for example. Here, the spiral blade 12 includes two spiral blades 12A and 12B. Each spiral blade 12A and 12B has a shape corresponding to a regular hexagonal rotating body 11, and the two spiral blades 12A and 12B are alternately meshed with each other. Thus, the spiral blade 12 is configured as a whole. By configuring the spiral blade 12 with a plurality (about 2 to 4) of spiral blades, a plurality of spiral spaces (spiral transport paths) are formed, and therefore, stirring and cleaning are combined with the action of the stirring piece 13 described later. , Neutralization and aggregation efficiency can be further improved.

  A flat stirring piece 13 protruding toward the hollow shaft body 10 (not shown in FIG. 12, see FIG. 13) is closely attached to the spiral blade 12 at an angular interval of 180 °. Attached. The stirring piece 13 causes the “tapping” action, so that the washing, neutralization, and agglomeration actions can be further improved.

  Also, the spiral blade 12 shown in FIG. 13 is the same as that shown in FIG. Although the hollow shaft body 10 is shown in FIG. 13, the spiral blade 12 is attached in close contact with the outer wall of the hollow shaft body 10. On the distal end side of the hollow shaft body 10 (the closed side of the rotating body 11), a plurality of residual containers and additives (washing water, neutralizing agent, flocculant) charged from the hopper 5 are ejected into the rotating body 11. Is formed around (see FIG. 18).

  FIG. 14 shows a state in which the hollow shaft body 10 and the spiral blade 12 as shown in FIG. 13 are arranged in a regular hexagonal rotating body 11. One end (right side of the drawing) of the rotating body 11 is open, and the other end (left side of the drawing) is closed, and the tip of the hollow shaft body 10 extends to the closing side of the rotating body 11.

  In such a stirring unit 1, the spiral blade 12 is attached in close contact with the outer wall of the hollow shaft body 10 and the inner wall of the rotating body 11, and thus the spiral blade partitioned by the spiral blade 12 is provided in the rotating body 11. A space is formed, and this spiral space becomes a conveyance path for conveying the agitated material and the aggregate. The stirring piece 13 is attached in close contact with the inner wall of the rotating body 11 in such a spiral space. With this structure, the rotating body 11 is integrated with the hollow shaft body 10 via the spiral blade 12, and rotates integrally with the hollow shaft body 10 using the hollow shaft body 10 as a rotation axis.

  In addition to the regular hexagon as described above, the rotator 11 may be a regular octagonal rotator 11 ′ as shown in FIG. 15 (side view from the opening side). The spiral blades 12 disposed in the rotating body 11 'are combined so that the four spiral blades 12A, 12B, 12C, and 12D are engaged with each other, and the spiral blades 12A, 12B, 12C, and 12D are mixed with the stirring pieces 13A, 13B, 13C, 13D. In this case, the stirring pieces 13A, 13B, 13C, and 13D are positioned in a spiral space at an angular interval of 90 ° with respect to the hollow shaft (not shown in FIG. 15). In addition, what is necessary is just to set suitably the size of the hollow shaft body 10, the rotary body 11, the spiral blade | wing 12, etc. according to the input amount of the remaining capacitors to process.

  In addition to the regular hexagon and regular octagon, the rotator 11 may be a quadrilateral, an octagon or more polygon (particularly a regular polyhedron is preferable), or a cylinder.

  The rotating body 11 cannot be visually recognized from the outside, but may have a structure capable of maintenance. An example of the rotating body 11 corresponding to this is shown in FIG. In this rotating body 11, a cover 30 having a reinforced transparent window 31 is detachably attached to each outer wall corresponding to each side of a regular hexagon with screws. The mounting positions of the covers 30 are slightly shifted, so that not only the inside of the rotating body 11 can be visually recognized through the reinforced transparent window 31 but also the maintenance can be easily performed by removing the cover 30.

  In addition to the dead weight of the rotating body 11 including the hollow shaft body 10 and the spiral blades 12, the rotating body 11 is added with the weight of the remaining components and washing water introduced therein, so that the weight is considerably increased. Become. For this reason, it is conceivable that the rotating body 11 including the hollow shaft body 10 and the like that are rotatably supported bend in some cases. In order to prevent this, as shown in FIG. 17, you may attach the support tool 35 which supports the circumference | surroundings of the rotary body 11 of a regular hexagon as needed. One support tool 35 may be attached near the center of the rotating body 11, or a plurality of support tools 35 may be attached at equal intervals.

  On the other hand, in this embodiment, one end portion side of the hollow shaft body 10 is rotatably supported by the bearing 15A. FIG. 19 shows a support state by the bearing 15A on the one end portion side. The bearing 15 </ b> A is not specified as long as it can support the rotation of the hollow shaft body 10. For example, a ball bearing may be used. The hollow shaft body 10 does not rotate from the hopper 5 to the bearing 15A, but the portion from the bearing 15A to the tip is rotatably supported by the bearing 15A. That is, in the hollow shaft body 10, the non-rotating portion and the rotating portion are connected by a known means, and the rotating portion extends to the center in the rotating body 11.

  The support mechanism by the bearing 15B on the other end side of the hollow shaft body 10 is configured, for example, as shown in FIG. In this support mechanism, the rotary shaft 40 is coupled to the center of the closing end face of the rotating body 11 (not shown), and the end of the rotary shaft 40 is supported by the bearing 15B. A gear 41 is fitted on the rotary shaft 40, and a gear 42 that meshes with the gear 41 is attached to the rotary shaft 16 a of the motor 16. Therefore, by the operation of the motor 16, the rotating shaft 40 rotates through the gears 42 and 41, and the hollow shaft body 10 and the rotating body 11 rotate integrally. In this case, the motor 16, the gears 42, 41 and the like constitute a rotation driving means.

  In FIG. 20, the power of the motor 16 is transmitted to the rotary shaft 40 via the gears 42 and 41. However, the rotary shaft 16a of the motor 16 is directly connected to the center of the closing side end surface of the rotating body 11 as shown in FIG. May be.

  6 to 11, the rotating body 11 of the stirring unit 1 is installed so that the opening side thereof is somewhat upward. Further, the power of the motor 16 is transmitted to the rotating shaft 40 by the chain 45 here. In this case, the chain 45 is hung on the rotating shaft of the motor 16 and a sprocket (not shown) attached to the rotating shaft 40. A belt and a pulley may be used instead of the chain 45 and the sprocket.

  The separation unit 2 includes a hopper 20 disposed to receive the agitation discharged from the opening of the rotating body 11 before neutralization, and the aggregate discharged from the opening of the rotating body 11 after neutralization, and the storage tank 3. An inclined channel (pipe) 60 that is arranged on the top and flows the agitated material and an overflow tank 50 that is disposed corresponding to the inclined channel 60 are provided. One end of the inclined channel 60 is connected to the lower opening of the hopper 20, and the other end is attached with a filter bag 61 for storing the residue. It has a large number of micro holes 60 a for flowing down to the storage tank 3. The overflow tank 50 stores filtered water from the filter bag 61. By flowing the agitated material through the inclined channel 60, water and residue contained in the agitated material can be efficiently separated with a simple structure.

  In addition, the separation unit 2 includes a flow path (pipe) 65 through which aggregates discharged from the opening of the rotator 11 after neutralization and a treated water tank 4 disposed corresponding to the flow path 65. One end of the flow path 65 is connected to the lower opening of the hopper 20, and the other end is attached with a filtration bag 21 that stores a residue other than water from the aggregate after neutralization. The treated water tank 4 stores filtered water from the filter bag 21. By flowing the aggregate through the flow path 65, water and residue contained in the aggregate can be efficiently separated with a simple structure. The filter bags 21 and 61 may be sandbags, filter cloths, and filter filters, and are preferably inexpensive ones that can be used repeatedly.

  Further, the separation unit 2 inclines the agitated material discharged from the opening of the rotating body 11 before the neutralization out of the agitated material inclined channel 60 and the agglomerated channel 65 connected to the hopper 20. A switching valve 70 is provided that is controlled so as to flow the agglomerate discharged from the opening of the rotator 11 to the flow path 65 after flowing through the path 60 and neutralization. The switching valve 70 may be an automatic valve (for example, an electromagnetic valve) or a manual valve, but a series of processing operations become easier when switching control is performed with the automatic valve. By switching the inclined flow path 60 and the flow path 65 with the switching valve 70, the stirrer and the agglomerate can be efficiently separated into water and a residue or residue other than water.

  The storage tank 3 contains the water flowing down from the minute hole 60a of the inclined channel 60. The water level of the storage tank 3 is detected by the sensor at the upper and lower limits, and the pH of the water is detected by the sensor. Is done. The water in the storage tank 3 is transferred to the hopper 5 by the pump 22 in the cleaning process, the neutralization process, and the aggregation process.

  The treated water tank 4 contains the filtered water from the filter bag 21, and the upper and lower limits of the water level of the treated water tank 4 are detected by a sensor. The water in the treated water tank 4 is transferred to the hopper 5 by the pump 25 in the aggregation process.

  The overflow tank 50 accommodates not only filtered water from the filter bag 61 but also additives (washing water, etc.) spilled from the hopper 5. The upper and lower limits of the water level in the overflow tank 50 are detected by a sensor, and when the water level reaches the upper limit level, the water in the overflow tank 50 is transferred to the hopper 20 by the pump 51.

  The inner walls of the storage tank 3, the treated water tank 4, and the overflow tank 50 are preferably provided with a lining that prevents deterioration such as corrosion due to acidic liquid, alkaline liquid, and other liquids. Of course, it is preferable to use a corrosion resistant pipe for transferring the liquid.

  A power source (operation unit) 80 for controlling ON / OFF of the motor 16, the switching valve (automatic valve) 70, etc., and charging / stopping of the neutralizing agent and the flocculant is provided on the inner wall on the rear side of the container 300. Yes. The power source 80 may be a power source if it can be secured, and may be used if the transport vehicle itself has a power source. Three drug containers 81 are arranged obliquely below the power source 80. Here, one of the three chemical containers 81 contains a neutralizing agent, one contains an inorganic flocculant, and one contains an organic flocculant. The neutralizing agent and the inorganic / organic flocculant may be liquid or powder, and are transferred to the hopper 5 by a pump or piping corresponding to the liquid or powder.

  The remaining-con processing (remaining-con processing method) by the remaining-con processing apparatus configured as described above is as follows.

  First, in order to perform the cleaning process, the remaining container and cleaning water are put into the hopper 5. The remaining container may be put into the hopper 5 by the person going up the stairs 312 of the container 300, or may be put in by using a belt conveyor or directly from the mixer truck. If the treated water from the previous residual container treatment remains in the treated water tank 4, use the treated water. If there is no water in the treated water tank 4, use the washed water in the treated water tank 4, Or you may throw in into the hopper 5 directly with a bucket or a hose.

  The rotating body 11 is rotationally driven by the motor 16 in parallel with the addition of the remaining condenser and the washing water. The charged residual condenser and washing water pass through the hollow shaft body 10 and are ejected into the rotating body 11 from the ejection port 10a. The remaining container and the washing water supplied to the closed side of the rotating body 11 are stirred by the rotating spiral blade 12, and the agitated material is conveyed from the closed side of the rotating body 11 to the opening side while the remaining container is washed. At the time of this stirring, since the stirrer is lifted to a certain extent by the stirring piece 13 and repeatedly falls off the stirring piece 13, the cleaning action is promoted.

  The agitated matter discharged from the opening of the rotating body 11 is received by the hopper 20 and flows into the inclined flow path 60 switched by the switching valve 70 at the beginning. During this flow, water contained in the agitated material flows down and accumulates in the storage tank 3 from the microholes 60 a, and residues (aggregates such as sand and gravel) other than water are collected by the filter bag 61. The water in the storage tank 3 is alkaline, but this water is circulated to the hopper 5 by the pump 22 and reused as cleaning water. The filtered water from the filter bag 61 is accumulated in the overflow tank 50.

  The neutralization process starts from the time when the agitated material starts to be discharged from the opening of the rotating body 11. In the neutralization step, a neutralizing agent is put into the hopper 5. The neutralizing agent is transferred from the chemical container 81 to the hopper 5 through a pipe by a pump. Thereby, the water of the storage tank 3 and the neutralizing agent are supplied into the rotating body 11. The water and the neutralizing agent supplied to the closed side of the rotating body 11 are stirred by the spiral blade 12, and the agitated material is conveyed from the closed side of the rotating body 11 to the opening side while the water is neutralized. Also during this neutralization, the neutralizing action is promoted by the stirring piece 13 as described above.

  The agitated material discharged from the opening of the rotating body 11 is received by the hopper 20 and flows into the inclined flow path 60 in the same manner as in the cleaning process. In the course of this flow, water contained in the agitated material flows down and accumulates in the storage tank 3 from the micropores 60 a, and a residue (smaller aggregate) other than water is collected by the filter bag 61. As neutralization proceeds, the water in the storage tank 3 gradually changes from alkaline to acidic (the pH value gradually decreases), but this water is also circulated to the hopper 5 by the pump 22 and reused as washing water. Is done. The filtered water from the filter bag 61 is accumulated in the overflow tank 50.

  When the water in the storage tank 3 is neutralized (when the pH value becomes approximately 7), the process proceeds to the aggregation step. That is, when the water in the storage tank 3 is neutralized, the introduction of the water in the storage tank 3 and the neutralizing agent to the hopper 5 is stopped, and the agitated material is almost not discharged from the opening of the rotary body 11 (the rotary body 11). When the interior is almost empty), the neutralization process is finished. At the end of this neutralization step, the switching valve 70 is switched to the flow path 65.

  In the next flocculation step, the water and the flocculating agent in the storage tank 3 are put into the hopper 5. Here, since inorganic and organic coagulants are prepared, the inorganic coagulant is first introduced, and the organic coagulant is introduced into the hopper 5 from the chemical container 81 through the piping by a pump. Is done. That is, initially, the water of the storage tank 3 and the inorganic flocculant are supplied into the rotating body 11. The water and the inorganic flocculant supplied to the closed side of the rotating body 11 are agitated by the spiral blade 12, and the water is agglomerated to produce an agglomerate (floc). The organic flocculant is then supplied into the rotator 11 with a slight delay, and the agglomerates are largely solidified in the rotator 11. This agglomerate is conveyed from the closed side of the rotating body 11 to the opening side. Even during this aggregation, the agglomeration action is promoted by the stirring piece 13 as described above.

  Aggregates discharged from the opening of the rotating body 11 are received by the hopper 20, and then flow into the flow path 65 and are accommodated in the filter bag 21. Water contained in the aggregate is filtered by the filter bag 21 and flows down and collected in the treated water tank 4. Residues other than water (precipitates such as cement powder) are collected by the filter bag 21. Since the water in the treated water tank 4 is sufficiently purified to the extent that it can be discharged into a river or the like as it is, this water is circulated to the hopper 5 by the pump 25 and reused as washing water.

  When the water level in the storage tank 3 is lowered to the lower limit level, the introduction of the water and the flocculant in the storage tank 3 to the hopper 5 is stopped, and the aggregate is almost not discharged from the opening of the rotary body 11 (the inside of the rotary body 11 is When almost empty), the agglomeration process ends.

  The sand, gravel and other aggregates collected in the filtration bag 61 by such a series of washing, neutralization, and aggregation processes, precipitates such as cement powder collected in the filtration bag 21, and the treated water tank 4 were accommodated. Water can be reused for the production of ready-mixed concrete. Further, the water in the treated water tank 4 can be widely used not only as re-wash water for construction sites and treatment equipment, but also can be discharged into the river as it is.

  Further, regarding the remaining-con processing apparatus having a structure embodying the schematic configuration shown in FIGS. 4 and 5, a partially broken perspective view is shown in FIG. 22, a plan view (top view) is shown in FIG. 23, and a line E in FIG. A cross-sectional view at -E is shown in FIG. 24, and an enlarged view of the hollow shaft body is shown in FIG. However, the same reference numerals are given to the same elements as those in the remaining control unit.

  Since this remaining-container processing apparatus has substantially the same configuration as the remaining-container processing apparatus except that it includes a hopper 6 as a residual-container input unit and a hopper 7 as an additive-adding unit, the description of the same configuration will be omitted. Both the hopper 6 and the hopper 7 are connected to one end of a hollow shaft body 10 located on the opening side of the rotating body 11.

  The pipe connected to the lower port of the hopper 6 is an expandable / contractible bellows pipe 90, and the bellows pipe 90 is connected to the pipe below the hopper 7 via a check valve 91. The check valve 91 is for preventing washing water, a neutralizing agent, a flocculant, and the like charged into the hopper 7 from flowing back to the hopper 6 side. Further, another bellows pipe 92 is attached to the hopper 6, one end of the bellows pipe 92 is connected to the hopper 6, and the other end is disposed in the overflow tank 50.

  The hopper 6 is supported by an elevating mechanism 100 that can change the vertical position. The elevating mechanism 100 is composed of, for example, a hydraulic link mechanism, and can automatically control the vertical position of the hopper 6. Of course, the raising / lowering mechanism 100 may be a manual type that rotates a handle or steps on a jack, for example. Even if the hopper 6 moves up and down, the bellows pipes 90 and 92 expand and contract following this operation.

  The remaining-con processing by the remaining-con processing apparatus configured as described above is as follows. However, since this process is basically the same as the remaining-con processing apparatus, only the differences will be described.

  First, in order to perform the cleaning process, the remaining container is put into the hopper 6 and the washing water is put into the hopper 7. Here, since the staircase 312 is installed outside the door 311 of the container 300, when a person throws in the remaining container, the staircase 312 may be used. The hopper 6 is in a lowered position by the lifting mechanism 100 so that the remaining components can be easily charged when the remaining components are charged, and after the remaining components are charged, the remaining components are lifted so as to easily enter the hollow shaft body 10 through the bellows pipe 90. To do.

  In the cleaning process, the water in the storage tank 3 is circulated to the hopper 7, and when the neutralization process is started, the water in the storage tank 3 and the neutralizer are introduced into the hopper 7. When the flocculation process is started, the water in the storage tank 3 and the flocculating agent are put into the hopper 7.

  In the residual con treatment apparatus of the above embodiment, a neutralizer and a flocculant (inorganic or organic) are used as additives (see FIG. 26). In this case, neutralization is performed in the neutralization step as described above. An inorganic flocculant is charged at the beginning of the flocculation step, and then an organic flocculant is charged. As another form, the flocculant may be a blended flocculant prepared by mixing inorganic and organic substances into one kind of medicine. In this case, as shown in FIG. 27, the flocculant is input as it is in the aggregation step.

  Furthermore, a blended flocculant prepared by mixing a neutralizer, an inorganic flocculant and an organic flocculant into one kind of chemicals may be used. In this case, as shown in FIG. 28, when the storage tank 3 becomes full during the cleaning process, the switching valve 70 is switched to the flow path 65 and the flocculant is charged. As a result, the neutralization reaction process and the aggregation reaction process proceed simultaneously in the rotating body 11. Agitation / aggregate discharged from the opening of the rotating body 11 is received by the hopper 20 and flows to the flow path 65, and aggregated sediment such as cement powder is collected by the filter bag 21. It collects in the treated water tank 4.

  Since such a residual container processing apparatus is installed in the container 300, it can be a place where a power source can be secured by mounting the container 300 on a transport vehicle (for example, a hook roll vehicle) or a transport vehicle equipped with a power source. For example, it is possible to perform the remaining content processing anywhere. The rotating body 11 functions as a cleaning tank in the cleaning process, as a neutralization tank (substantially a cleaning / neutralization tank) in the neutralization process, and as a coagulation tank in the aggregation process. A series of sum and aggregation processes can be efficiently performed in a short time.

  Various modifications can be considered for such a remaining-con processing apparatus. For example, in a place where a large amount of residual condensate is generated, two rotating bodies are installed, and the washing process and the neutralizing process are performed with the first rotating body, and the aggregation process is performed with the second rotating body. For example, the remaining control can be performed without increasing the number of storage tanks and treatment water tanks and other equipment. Further, in this case, the second rotating body does not necessarily require the hopper 5 that is the remaining-container / additive adding portion, and therefore the second rotating body includes, for example, a hopper related to the first rotating body. This can be done simply by extending the introduction pipe from 5. That is, it is only necessary to provide a second rotating body.

  Moreover, although the said remaining container processing apparatus is installed in the one container 300, in order to respond | correspond to the processing of a lot of remaining containers, for example, a large rotary body is mounted in one container, and another 1 The storage tank and the treated water tank may be mounted on the container of the stand, or the storage tank, the treated water tank, and the aggregate collection container may be separately mounted on separate containers. In this case, what is necessary is just to connect the rotary body of each container, a storage tank, a processing water tank, and an aggregate collection container by piping etc. in a processing place. In addition, when collecting the aggregate, a container such as a drum can, a cart such as a unicycle, and a movable container for collecting the aggregate may be separately prepared.

  Or it becomes easy to make it move with a trolley | bogie by installing the remaining control processing apparatus on the trolley | bogie which can move.

  Moreover, in the said remaining container processing apparatus, although the filtration bags 21 and 61 are used for aggregate collection | recovery, you may use a more durable flexible container bag depending on the case. Furthermore, in the above-described remaining-con processing apparatus, the rotating body 11 is arranged with an angle so that the opening side faces upward. However, the angle of the rotating body 11 is adjusted according to the properties of the remaining control (the angle is variable). Thus, the processing capability can be changed efficiently even at the same rotational speed.

  In addition, in the remaining-con processing apparatus shown in FIGS. 22 to 25 in particular, the remaining con is supplied from the hopper 6 and additives such as washing water, a neutralizing agent, and a flocculant are supplied from the hopper 7. It is also possible to treat residual components with low moisture content (high viscosity). In this case, the remaining container is once immersed in washing water to increase the moisture content so that the remaining container is reliably introduced into the rotating body 11 from the jet port 10a of the hollow shaft body 10 (in order to increase fluidity). ), And is preferably put into the hopper 6. Alternatively, the remaining container having a low moisture content may be introduced from the hopper 6 together with the washing water. In short, it is important to ensure that the remaining components can be introduced into the rotating body 11 through the hollow shaft body 10.

  The remaining-con processing apparatus and the remaining-con processing method as described above have the following advantages.

  The first advantage is that the remaining alkaline components that have been neglected at construction sites and factories in the past have been buried, returned, or left at appropriate locations within the construction site, so that they can penetrate underground. And the situation where it was mixed with rainwater and turned into alkaline turbid water and spilled out of the field can be prevented, and all remaining components can be reused.

  The second advantage is that by reusing all the components of the remaining container, it is possible not only to affect the environment, but also to the collection and transportation company and the processing company when processing the waste. Waste disposal costs, manifest slips, etc. are no longer required, and some prefectures have spent a lot of time and money, such as applying an industrial waste tax to the waste to be treated. And so on.

  The third advantage is that by installing the container with the remaining container processing device on the transport vehicle or installing the remaining container processing device on the carriage, the truck, sling work, crane work, etc. related to the installation can be performed. Since it is not necessary, extra work and accidents can be prevented, installation work and costs related to installation are not required, installation can be simplified, and it can be quickly removed with a hook roll car etc. at the end of construction work. Work efficiency can be improved.

  As a fourth advantage, when the remaining waste processing equipment is mounted on a transport vehicle as a container or installed on a cart, it can be easily relocated to the next construction site and can be used continuously at the same time as relocation. The remaining containers can be separated and reused at the place.

  The fifth advantage is that the containers used for hook-rolling vehicles are originally made for the purpose of collecting and transporting waste, etc., so they are durable, and when collecting waste containers discharged from the site In addition, when the container is installed, the container with the remaining container processing device itself can be installed or removed during the collection and transportation work without any particular improvement.

  As a sixth advantage, as the above-described embodiment, the residual waste separation processing has been described. However, the residual waste treatment device is also used for dredging work that removes mud, sand, etc. across the riverbed, seabed, and lake bottom. It can be used without difficulty and can also purify water. In addition, it is effective for dredging work such as artificial ponds and water purification.

It is process drawing which shows the flow of a basic process of the remaining-con processing apparatus and remaining-con processing method of this invention. It is the schematic block diagram (a) which concerns on the washing | cleaning process of the residual-con processing apparatus which concerns on one Embodiment, and the schematic block diagram (b) which concerns on the neutralization process. It is a schematic block diagram which concerns on the aggregation process of the residual control apparatus. It is the schematic block diagram (a) which concerns on the washing | cleaning process of the residual-con processing apparatus which concerns on another embodiment, and the schematic block diagram (b) which concerns on the neutralization process. It is a schematic block diagram which concerns on the aggregation process of the residual control apparatus. FIG. 4 is a partially broken perspective view of a remaining-con processing apparatus having a structure that embodies the schematic configuration shown in FIGS. 2 and 3. It is a top view (top view) of the residual control apparatus. It is sectional drawing in line AA of FIG. It is sectional drawing in line BB of FIG. It is sectional drawing in line CC of FIG. It is sectional drawing in line DD of FIG. It is a perspective view of an example spiral blade arranged in the inside of a rotating body in the stirring part of the residual control apparatus. It is a perspective view of the state which attached the spiral blade of the other example arrange | positioned in the rotary body in the stirring part of the residual control apparatus to the hollow shaft body. It is a perspective view of the state which has arrange | positioned the spiral blade and hollow shaft body of FIG. 13 in the rotary body. It is a side view (figure seen from the opening side) which shows another form of the rotary body in the stirring part of the same residual-con processing apparatus. It is a perspective view which shows another form of the rotary body in the stirring part of the residual-con processing apparatus. It is a schematic side view which shows the mechanism which supports the rotary body in the stirring part of the residual-con processing apparatus. It is an enlarged view of the hollow shaft body in the stirring part of the residual-con processing apparatus. It is an enlarged view which shows the bearing by the side of the one end part of the hollow shaft body in the stirring part of the same residual-con processing apparatus. It is an enlarged view which shows an example of the bearing and rotary drive mechanism by the side of the other end part of a hollow shaft body in the stirring part of the residual-con processing apparatus. It is an enlarged view which shows another example of the rotation drive mechanism by the side of the other end part of the hollow shaft body in the stirring part of the residual-con processing apparatus. FIG. 6 is a partially broken perspective view of a remaining-con processing apparatus having a structure embodying the schematic configuration shown in FIGS. 4 and 5. It is a top view (top view) of the residual control apparatus. It is sectional drawing in line EE of FIG. It is an enlarged view of the hollow shaft body in the stirring part of the residual-con processing apparatus. It is a schematic block diagram in the case of using a neutralizing agent, an inorganic type flocculant, and an organic type flocculant as an additive in the residual con processing apparatus. It is a schematic block diagram in the case of using a neutralizing agent and an aggregating agent (inorganic / organic blend) as additives in the residual con treatment apparatus. It is a schematic block diagram in the case of using a flocculant (a neutralizing agent and inorganic type and organic type flocculant mixing | blending) as an additive in the same residual processing apparatus.

Explanation of symbols

DESCRIPTION OF SYMBOLS 1 Stirring part 2 Separation part 3 Reservoir tank 4 Treated water tank 5 Hopper (remaining container and additive addition part)
6 Hopper (remaining part charging part)
7 Hopper (additive input part)
DESCRIPTION OF SYMBOLS 10 Hollow shaft body 10a Spout 11 Rotating body 12 Spiral blade 13 Stirring piece 15 (A, B) Bearing 16 Motor (rotation drive means)
20 Hopper 21, 61 Filtration bag 40 Rotating shaft 50 Overflow tank 60 Inclined flow path 60a Micro hole 65 Flow path 70 Switching valve 300 Container

Claims (13)

An agitation part for agitating the residual components and additives, a separation part for separating the agitated substance stirred in the agitation part into water and a residue other than water, and a storage tank for storing water separated in the separation part With
The stirring unit includes a hollow shaft body that is rotatably supported, and a cylindrical rotating body in which the hollow shaft body is inserted and rotated around the hollow shaft body, with one end opened and the other end closed. And a spiral blade that is attached over the outer wall of the hollow shaft body and the inner wall of the rotating body and conveys the agitated material from the closed side of the rotating body to the opening side in accordance with the direction of rotation of the hollow shaft body. Is supplied into the hollow shaft body from one end side of the hollow shaft body located on the opening side of the rotating body, and is introduced into the rotating body from the other end side of the hollow shaft body,
The separation unit receives the agitated material discharged from the opening of the rotating body, puts water separated from the agitated material into the storage tank, and collects residue other than water. Processing equipment.   The stirring piece which protrudes toward a hollow shaft body is attached to the inner wall of the rotary body in the spiral space partitioned by the spiral blade provided in the rotary body. Remaining processing unit.   3. The remaining-con processing apparatus according to claim 2, wherein the stirring pieces are attached to the hollow shaft body at an angular interval of 180 degrees.   4. The remaining-con processing apparatus according to claim 1, further comprising a rotation driving unit that rotationally drives the hollow shaft body or the rotating body.   It is connected to one end of the hollow shaft body and the additive supply side, and can move up and down by ejecting the remaining container and additive through the hollow shaft body from the outlet formed on the other end side of the hollow shaft body into the rotating body. 5. The residual content processing apparatus according to claim 1, further comprising an additional residual content / additive adding unit.   The remaining container of the hollow shaft body is connected to the one end of the hollow shaft body and the additive supply side, and the remaining container can be moved up and down through the hollow shaft body from the jet port formed on the other end side of the hollow shaft body. 2. The apparatus according to claim 1, further comprising: a charging portion; and an additive charging portion that causes the additive to be ejected through the hollow shaft from the other end of the hollow shaft into the rotating body. 2. The remaining-con processing apparatus according to claim 3, 3 or 4.   Until the water in the storage tank is neutralized, the water in the storage tank is circulated to the residual condenser / additive charging section or the additive charging section. The residual control apparatus according to claim 5 or 6, wherein a neutralizing agent is supplied into the rotating body.   After the water in the storage tank is neutralized, the neutralized water in the storage tank is circulated to the residual condenser / additive charging section or the additive charging section, and from the charging section, 8. The residual content processing apparatus according to claim 7, wherein a flocculant as an additive is supplied into the rotating body.   The separation unit includes a hopper disposed to receive the agitated material discharged from the opening of the rotating body before the neutralization, and an inclined channel disposed on the storage tank. , One end is connected to the lower opening of the hopper, and the other end is attached with a filtration bag for storing the residue, so that water can flow down to the storage tank while the agitated material flows in a portion located on the storage tank. 8. The remaining-con processing apparatus according to claim 7, wherein the remaining-con processing apparatus has a plurality of minute holes.   The separation unit includes a flow path for flowing agglomerates discharged from the opening of the rotating body after the neutralization, and a treatment water tank disposed corresponding to the flow path, and the flow path has one end of the hopper. A filtration bag is connected to the lower port, and a filtration bag for storing a residue other than water from the aggregate after neutralization is attached to the other end, and the filtered water from the filtration bag is stored in a treated water tank. Item 10 or claim 9, the remaining-con processing apparatus.   The separation unit is configured to flow the agitated material discharged from the opening of the rotating body to the inclined channel before the neutralization among the inclined channel and the agglomerate channel connected to the hopper. 11. The remaining-con processing apparatus according to claim 10, further comprising a switching valve that is controlled so that the aggregate discharged from the opening of the rotating body flows through the flow path after the neutralization.   The said remaining container processing apparatus is constructed | assembled in the container mounted so that attachment or detachment to a transport vehicle, or on the movable trolley | bogie is characterized by the above-mentioned. The remaining-con processing apparatus according to claim 4, claim 5, claim 6, claim 7, claim 8, claim 9, claim 10, or claim 11. A hollow shaft body that is rotatably supported, a cylindrical rotary body that is inserted into the hollow shaft body and is rotatable around the hollow shaft body, one end is open and the other end is closed, and the hollow shaft body The outer wall of the rotating body and the inner wall of the rotating body are used, and a stirring unit provided with a spiral blade that conveys the stirring object from the closed side of the rotating body to the opening side according to the rotation direction of the hollow shaft body,
The remaining condenser and washing water are supplied from one end side of the hollow shaft body located on the opening side of the rotating body of the stirring unit to the hollow shaft body, and the remaining condenser and washing water are rotated from the other end side of the hollow shaft body. While being introduced into the body and stirring the remaining container and washing water by the rotation of the rotating body, the stirring material is conveyed from the closed side of the rotating body to the opening side by the spiral blade, and the stirring material discharged from the opening of the rotating body is And a washing process for separating the residue other than water,
The water and neutralizing agent separated in the washing step are introduced into the rotating body from the hollow shaft body in the same manner as described above, and the stirring material is stirred by the spiral blade while stirring the water and the neutralizing agent by rotating the rotating body. A neutralization step of repeating until the water is neutralized, transporting from the closed side to the open side, and separating the stirred product discharged from the opening of the rotating body into water and a residue other than water,
The water and the flocculant separated in the neutralization step are introduced from the hollow shaft body into the rotating body in the same manner as described above, and the agglomerates are blocked by the spiral blade while stirring the water and the flocculant by the rotation of the rotating body. A coagulation step for conveying the aggregate from the side to the opening side and separating the aggregate discharged from the opening of the rotating body into water and a residue other than water;
A remaining-con processing method comprising:

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