KR200228816Y1 - Apparatus for treating and moving waste synthetically - Google Patents

Abstract

The present invention relates to a contaminant comprehensive treatment transporter, which includes a coarse contaminant secondary dewatering unit (B), a flow adjusting unit (E), a desorption liquid transfer unit (F), and a dewatering coarse contaminant in the first dehydrated manure. In the contaminant treatment device consisting of a storage tank, the coarse sediment primary dewatering unit (A) for firstly dewatering the coarse sediment in the manure, and transported through the crushed contaminant outlet (5ab) by crushing the secondary dehydration Crushed quantitative feed unit (C), pneumatic conveying unit (D) of crushed contaminants for conveying the crushed contaminants, and fine contaminant filtration unit for filtering the desorption liquid by vibrating screen (11) to discharge the desorption liquid and fine contaminants (G), the fine contaminant dehydration unit (H) for dewatering and discharging the fine condensate again by the screw press 14, and the air pressure of the fine condensate for conveying the introduced fine condensate through the contaminant discharge port 7b by air pressure. this It consists of a part (D ').

The present invention prevents coarse coarse matter from being caught on the outer circumferential surface of the drum screen, and allows the coarse matters of large chunks to be properly crushed to be transported to the waste transport vehicle smoothly by air pressure. It is possible to prevent odors and to smoothly deal with contaminants.

Description

Applicants for treating and moving waste synthetically}

The present invention relates to an integrated contaminant treatment transporter, and in particular, each unit device having a separate function is composed of a single device and a single device assembled to operate with a mutual organic relationship in a single frame, and various kinds of manure The present invention relates to a contaminant comprehensive treatment transporter configured to completely separate a contaminant and a wastewater which is a desorption liquid.

In general, the manure discharged from the human body is discharged to the sewage pipe from the flushing toilet, and then temporarily stored in the septic tank to be purified, and then the supernatant is discharged into the river, and the manure such as manure is collected and treated by the manure collection truck.

As an example of the conventionally used contaminant treatment device, the manure transported by the manure collection truck is put into a filter to filter, dehydrate and remove the contaminants contained in the manure primarily, and the rest is the storage tank, the aeration tank, and the digestion tank. Part of the manure waste digested in this treatment device is used as fertilizer and the rest is collected and landfilled. At this time, the digested water flows into the sewer and is discharged into the river.

Compared with developed countries, manure in Korea contains more contaminants and sediments, and the sediments in the contaminants flow into the storage tanks, aeration tanks, and digestion tanks to be settled and deposited. Of course, it is the cause of the closing of the discharge pipe.

Therefore, in order to remove the sediment deposited sand in the manure storage tank, the aeration tank, and the digestion tank, many difficulties are required to stop the operation of the treatment plant every few days and to remove the sand deposited in the underground tank by manpower. I'm experiencing it.

Another example of the contaminant treatment device used to improve the above problem is to filter the manure or animal manure coming into the feeder to filter the coarse contaminants with the rotary drum screen 20 (see Fig. 3), which is the primary dewatering device of the coarse contaminants. The moisture content of the coarse coarse is lowered with a screw press, which is a secondary dehydration device of coarse coarse, and the coarse is transported by a belt conveyor to a waste truck for processing. Also, the desorption liquid removed from the rotary drum screen is stored in a flow control tank. After the operation of the pump by the sensor is transferred to the cyclone, the desorption liquid transferred to the cyclone is treated by centrifugal dehydration of the heavy sand and fines by the cyclone and then sent out by processing fine contaminants with a screw conveyor, in case of emergency To store the overflowed liquid through the overflow pipe of the flow adjustment tank installed to The amount of desorption liquid temporarily stored in the flow adjustment tank is always constant, and the cyclone supernatant is sent to the storage tank, and the desorption liquid of the centrifugal dehydrator is also sent to the storage tank.

However, the conventional contaminant treatment device has the following problems.

That is, the belt conveyor is difficult to be installed in a narrow space because the belt must be continuously installed to the waste transport vehicle, when the inclination height of the belt exceeds 20 °, the contaminants do not rise, the belt Due to the transport of the contaminants by the trap, the debris was generated falling to the left and right sides of the belt and the fallen debris made the workplace dirty, the odor was generated in the debris, which deteriorated the surrounding environment, and the aversive substance was seen to the outside of the belt conveyor. There was a problem.

In addition, in the primary dewatering device of the coarse concave, as shown in FIG. 3, the hollow annular plate body 20a, which is a plurality of inner bilateral spaces, is provided in parallel by several through bolts 20c at regular intervals. A rotary drum screen (20) having a spacer (20b) assembled therein to maintain a constant gap between the hollow annular plate bodies (20a);

The circular plate body 21b is provided in the shaft 21a at regular intervals, and each circular plate body 21b is inserted between each said hollow annular plate body 20a, and the wiper screen which receives power by a motor ( 21), the coarse coarse particles are easily sandwiched between the hollow annular plates 20a of the rotary drum screen 20 being rotated, and the pinched coarse particles are each circular plate of the wiper screen 21. Since it is difficult to properly remove the sieve 21b, coarse contaminants are hardened in a state of being fitted into the space between the hollow annular plate bodies 20a, so that the filtration through the rotary drum screen 20 is smooth. There was a cumbersome problem that the cleaning is not made frequently, and between the circular plates 21b of the wiper screen 21 to remove the trapped contaminants. There is a problem of being able interrupted.

In the driving of the rotary drum screen 20, since the rotary drum screen 20 is installed in a chain driving manner, sagging or torsion occurs due to the overload of the chain during the first driving, and thus, the maintenance of the rotary drum screen 20 requires frequent maintenance. In the emergency, the flow rate of the overflow liquid flowing through the overflow pipe of the flow adjustment tank is directly transferred to the storage tank, or the gravity flow including sand that does not sink in the water during the process of transferring the overflow liquid to the storage tank through the overflow pipe. Fine contaminants are fine, but light contaminants such as sesame and fine paper and vinyl, which are floating on the water, are transferred to the storage tank, so that the light materials float in the storage tank and the light substance floats to the final effluent. There was a problem.

The present invention has been made to solve the above-mentioned problems, and each unit device has a mutual organic relationship in a single bed and a single frame so as not to occupy a large amount of space occupied by each unit device having a separate function. It consists of a single device that can be operated to occupy less space, and efficiently separates various contaminants in the manure and wastewater, which is sedimentation and desorption liquid, so that dehydrated contaminants can be treated in a state where no odor occurs. Its purpose is to provide a composite waste disposal transporter.

In order to achieve the above object, the integrated composite feed processing machine of the present invention is installed in the main body, and a drum screen for dewatering coarse coarse matter firstly during manure or livestock manure and a screw press for secondly dehydrating the coarse material dehydrated firstly. And a flow rate adjusting tank, a desorbing liquid transfer pump, and a storage tank comprising the above-mentioned unit devices, wherein the wedge wires having a triangular cross section of the drum screen face inwards. A coarse miscellaneous primary dewatering unit having a scraper installed to contact the outer circumferential surface of the drum screen; A crushing quantity transfer unit for transporting and discharging the coarse crushed material which is compressed and dehydrated and discharged through the screw press; A pneumatic conveying unit of the crushed contaminants for conveying the crushed contaminants discharged from the crushing fixed quantity to the waste transport vehicle through the contaminant discharge port and the conveying pipe by air pressure; A fine contaminant filtration unit having a vibrating screen for filtering fine contaminants including sand and the like contained in the desorption liquid and the monthly liquid; A fine contaminant dewatering unit by a screw press for dewatering and transporting the filtered fine contaminants; It consists of a pneumatic conveying portion of the fine contaminants for conveying to the waste transport vehicle by the air pressure of the dehydrated fine contaminants; Each unit device is characterized in that it consists of a single bed and a single device assembled in a single frame to operate in association.

1 is a longitudinal sectional view of a fine contaminant filtration unit is installed with a known vibration screen,

2 is a longitudinal sectional view of a pneumatic conveying unit of a known contaminant;

3 is a right side view showing a partial cross-section of a known coarse coarse matter primary dewatering part,

4 is a schematic front view of the contaminant comprehensive processing conveyor of the present invention;

5 is a schematic left side view;

6 is a schematic plan view;

7 is a right side view showing a partial cross-section of the coarse coarse matter primary dewatering part,

8 is a schematic cross-sectional view of a portion A-A of FIG.

9 is a partial perspective view of the screen portion of the contaminant processing processor of the present invention,

10 is a partial right side view of the site where the scraper of the coarse contaminant primary dewatering part is installed;

Fig. 11 is a schematic front view showing a partial cross section of the crushing quantity transfer unit installed in the pneumatic conveying unit of the contaminant;

* Explanation of symbols for main parts of the drawings

1: Body 1c: Drum Screen

2: motor 2a: spur gear

3: scraper 3a: plate body

3c: Plate separation prevention piece 3c ': Adjusting bolt

4: screw press 4a: screw

5: Crushing quantity transfer device 5a: Cylindrical cylinder

5b: screw 5ba ': crushing protrusion

6 motor 7 transfer device by pneumatic pressure

8: flow rate adjusting tank 11: vibrating screen

14: screw press 15: desorption liquid transfer pump

A: Coarse sediment primary dehydration department B: Coarse miscellaneous secondary dehydration department

C: Crushed quantity transfer part D: Pneumatic transfer part of crushed contaminants

D ': Pneumatic conveying part of fine contaminants E: Flow adjusting part

F: Desorption liquid transfer part G: Fine contaminant filtration part

H: fine contaminant dewatering part

Hereinafter, an embodiment of the present invention will be described in detail with reference to the accompanying drawings.

As shown in FIGS. 4 to 11, the integrated composite feed processing machine of the present invention first filters and dehydrates the coarse coarse matter which is a foreign substance in the manure or livestock manure, and discharges the manure inlet 1a and the drum screen and the coarse miscellaneous material. A discharge port (1b) is formed, the coarse coarse matter primary dewatering portion (A) consisting of a motor (2) for transmitting power to the drum screen;

The coarse coarse matter inlet 4e is connected to the coarse coarse matter outlet 1b, and the screw 4a for compressing the coarse coarse material falling from the coarse coarse matter primary dewatering part and dewatered and transported secondly, and the screw 4a. ), The desorption liquid falls to the lower desorption liquid discharge port 4f, and the dehydrated coarse condensate is discharged to the coarse contaminant discharge port 4b, and the mesh-shaped hollow park cylindrical screen 4c and the screw 4a are energized. A coarse grain secondary dewatering part (B) by a screw press (4) made of a motor (4d) to transmit;

A water level detecting device (not shown) for automatically operating the desorption liquid transfer pump 15 is installed, and is installed below the coarse matter primary dewatering part, and is detached from the drum screen of the coarse matter primary dehydration part. After the incoming desorbing liquid is stored for a predetermined time, a desorption liquid discharge port 8b is formed which is discharged through the connecting pipe 9, and the overflow liquid discharge port 8c connected to one end of the decanter pipe 8a through which the overflow liquid is discharged is formed. A flow rate adjusting part E by the flow rate adjusting tank 8 formed;

Transfer the desorption liquid discharged through the connection pipe (9) connected to the desorbent discharge port (8b) of the flow rate adjustment tank (8) and the connection pipe (9) (10) connected to the desorbent discharge port (4f) of the screw press (4). In that it comprises a desorption liquid transfer part (F) by the desorption liquid transfer pump (15),

The coarse crushed substance discharge port through which the compressed and dehydrated coarse grains discharged through the coarse crushed substance discharge port 4b of the screw press 4 and the coarse crushed substance are crushed while the coarse crushed substance is injected. A plurality of crushing protrusions 5ba 'are provided in the cylindrical cylinder 5a in which 5ab is formed, and a screw 5b formed in the impeller 5ba and a motor 6 for transmitting power to the screw 5b. A crushing quantity transfer part C made by the crushing quantity transfer device 5 formed;

The crushed quantity discharged by a predetermined air pressure through the hopper 7a and a compressor (not shown) installed so that the crushed contaminants discharged to the crushed contaminant discharge port (5ab) while being crushed from the conveying unit (C) The air pressure of a known contaminant for conveying a contaminant is conveyed by the conveying apparatus 7 by the air pressure of the crushed contaminant, which is composed of a contaminant discharge outlet 7b and a conveying pipe 7c for conveying the discharged crushed contaminant to a waste transporter. Sending (D);

The connecting pipes 9 and 10 connected to the desorbing liquid discharge ports 8b and 4f of the flow rate adjusting tank 8 and the screw press 4, respectively, and the connecting pipe 18 connected to the desorbing liquid conveying unit F are connected to each other. The flow-through liquid inlet (11a ') through which the light liquid flows in through the flow-through desorbing liquid inlet (11a) and the overflow pipe (8a) connected to the overflow liquid outlet (8c) of the flow rate adjustment tank (8); The desorption solution, which is again moisture by filtering the excess liquid and the monthly liquid, is installed to a well-known storage tank (not shown) through the desorption outlet 11c, and the fine contaminants including sand containing some water are discharged through the fine contaminant outlet 11b. A lake drive 12 having a vibration screen 11 and a chain 12a having a brush 12a 'formed at predetermined intervals while receiving a driving force of the motor 16 on an upper portion of the vibration screen 11; The nozzle is configured to spray water to the vibrating screen (11) Member 13, and a fine impurities of known consisting of a motor 17 for transmitting power to the vibrating screen 11, the filtration unit (G) and;

The fine contaminant inlet 14a is connected to the fine contaminant discharge port 11b of the fine contaminant filtration unit G, and the fine contaminant discharge port 14c is formed to discharge the compressed and dehydrated fine contaminant. Compresses and dehydrates and transports the mesh-shaped hollow tube cylindrical screen 14d discharged to the storage tank and the fine condensate containing some of the water injected from the fine-collar filter portion G to dehydrate and transfer the inside. A well-known fine condensate dewatering part (H) by a screw press (14) comprising a screw (14b) provided and a motor (14e) for transmitting power to the screw (14b);

Hopper (7a) is installed so that the fine condensate discharged into the fine contaminant discharge port (14c) of the screw press 14, and the fine contaminant discharge port (7b) discharged by a predetermined air pressure through a compressor (not shown) And a pneumatic conveying unit (D ′) of a known contaminant for conveying the contaminant by the conveying device (7) by the air pressure of the micro-concave of the conduit (7c) for transporting the fine contaminant to the waste transport vehicle;

The coarse clamp primary dewatering part (A) is formed with a plurality of insertion recesses (1ca ″) at regular intervals on each support (1ca ') arranged at regular intervals, respectively, an annular wedge having a triangular cross section A triangular pointed portion of the wedge wire 1ca '' 'is inserted into each insertion recess 1ca' 'of each support 1ca' so that the pointed portion of the wire 1ca '' 'faces inward. A drum screen 1c formed of a screen portion 1ca which is welded;

An upper end of the plate body 3a is formed with an inclined surface 3a 'so as to be in contact with the drum screen 1c, and is assembled with bolts while being inserted between the inner and outer fixing bars 3aa and 3ab. Adjusting piece 3c '' to which the adjusting bolt 3c '' 'is inserted into which the fixing table 3aa is inserted to reciprocate the long hole 1d' formed in the front and rear wall 1d of the main body 1. The plate departure prevention piece 3c, which is welded to the support 3b at which both ends thereof are fixed to each other, and to which the adjustment bolt 3c 'is coupled to prevent the plate 3a from being separated outward, And a scraper 3 fixed to the rear wall 1d;

Both ends of each support 1ca 'are coupled to the disc front and rear plate body 1cc of the drum screen 1c. In addition, the unit devices are composed of a single bed 19 and a single device 19 assembled in a single frame 19 'to operate in association. In the figure, reference numeral 7e denotes an air passage, 7f denotes a closed holding portion, and 7g denotes a hemispherical valve.

In the first dehydration process of the coarse coarse matter, the fine screen filter unit G provided with the transfer part D (D ′) and the screw press 14 by the air pressure of the crushed fine or fine coarse matter is present. Utility Model Registration No. 182417 (Driving device of drum screen for sludge), Utility Model Registration No. 156098 (Drying sludge conveying apparatus using air pressure), Utility Model Registration Application No. 2000-118670 (with screw press) Dehydration device), so the description of the description will not be specifically provided herein, but will be briefly described.

That is, the drum screen 1c is installed such that the spur gear 1cb of the drum and the spur gear 2a of the motor 2 are directly engaged, as in the driving device of the sludge drum screen of Utility Model Registration No. 182417. The transfer unit (D) (D ') by the air pressure of the contaminant is, as in the dry sludge conveying apparatus using the air pressure of Utility Model Registration No. 156098, a valve having a closed holding portion at the bottom of the hopper (7a) around the And an air inlet 7e for injecting air pressure in a direction toward the wall surface of the clutter storage part 7d at a predetermined portion of the clutter storage part 7d, and the lower part of the clutter storage part 7d. The venturi portion narrowing the conveying path is formed in the crushed fine or fine contaminant discharge port 7b, and the transfer pipe 7c is configured to be connected to the venturi portion to the outside.

In addition, as in the dehydration apparatus in which the screw press of Utility Model Registration Application No. 2000-11867 is installed, the fine condensate contained in the incoming desorbing liquid is filtered through the vibrating screen 11 and then discharged through the fine contaminant outlet 11b. It enters the inside of the mesh-shaped hollow tube cylindrical screen 14d through the fine contaminant injection hole 14a of the screw press 14, and is forcibly compressed by the screw 14b, and is transported while dewatering the hollow tube cylindrical screen 14d. Moisture of the fine contaminants are separated through the desorbed liquid is introduced into the storage tank (not shown).

Referring to the operation of the composite contaminant processing transporter of the present invention configured as described above are as follows.

The complex processing feed machine of the present invention first turns on the main switch of the control panel, and then each unit device (A) (B) (C) (D) (D ') (E) (F) (G) (H ) And then manure or livestock manure is introduced into the manure inlet 1a of the drum screen 1c, which is the primary dehydration part A of the coarse sewage, and the manure is rotated by the drum screen 1c. Water from the coarse coarse water is separated from the coarse coarse particles, and the coarse coarse water, which is solids filtered by the scraper 3, is introduced into the coarse coarse material secondary dewatering unit (B). do.

That is, as shown in FIGS. 4 to 11, when the motor 2 of the driving unit rotates, the spur gear 2a integral to the motor 2 rotates, and the spur gear 2a rotates. The drum screen 1c is rotated by the drum screen 1c which is rotated while the spur gear 1cb installed on the shaft of the drum screen 1c directly engaged with the spur gear 2a rotates. The manure or livestock manure that has flowed into the screen portion 1ca, which is the outer circumferential surface thereof, also rotates, and the water passes through the space portion, which is a gap portion between each wedge wire 1ca '' 'and the wedge wire 1ca' '' of the screen portion 1ca. The desorbed and desorbed water flows into the flow regulating tank (8), and the coarse coarse matter, which is being rotated while being dehydrated and filtered by the scraper (3), is installed to contact the outer circumferential surface of the screen portion (1ca). Screw presses (4) being restrained from continuing to rotate Through a coarse impurities inlet (4e) is injected into the screw press (4).

The dewatering coarse debris injected by the scraper 3 is compressed and transported by the screw press 4, which is a secondary dehydration device, to be dehydrated again. When the driving motor 4d is driven, the chain gear 4d ' ) And the coarse grains injected through the coarse grain inlet 4e by the screw 4a which is rotated by rotating the chain gear 4a 'fixed to the screw shaft while being connected to the chain 4g. Moisture contained in the coarse contaminant while being transported in a stable state is quickly discharged through the dehydration filtration hole of the hollow park cylindrical screen 4c, and the dehydrated coarse coarse matter is injected into the coarse coarse matter inlet 5aa of the crushing quantity transfer device 5. do.

The coarse coarse matter injected into the coarse coarse matter inlet 5aa is finely crushed and finely crushed by a plurality of crushing protrusions 5ba 'formed on the rotating screw 5b of the crushing quantity transfer device 5. Is passed through the hopper 7a into the conveying apparatus 7 by the air pressure of the crushed contaminants, and the crushed contaminants conveyed into the conveying apparatus 7 by the air pressure of the crushed contaminants are transferred to a compressor (not shown). The air pressure generated by the air is transferred to the waste transport vehicle through the lower venturi portion and the transport pipe 7c.

On the other hand, the overflowed liquid flowed through the overflow liquid inlet (11a ') through the overflow pipe (8a) of the flow adjusting tank 8 is installed in preparation for emergencies among the desorption liquid detached by the drum screen (1c). The desorption liquid flowing into the screen 11 and stored in the flow adjusting tank 8 and the desorption liquid discharged from the screw press 4 are connected to the tube 9 and the desorption liquid by a sensor not shown. By the operation of 15) is introduced into the vibrating screen 11 of the fine contaminant filtration unit (G) through the desorption fluid inlet (11a).

The overflow liquid and the desorption liquid pass through the vibrating screen 11 that separates the fine condensate and the desorption liquid, and the desorption liquid flows into the storage tank, and the fine condensate dehydrated is transferred to the screw press 14.

The fine condensate is introduced into the hollow-cylindrical cylindrical screen 14d through the micro-concrete inlet 14a of the screw press 14 while being compressed by the screw 14b which is rotated by the driving of the driving motor 14e. When the drive motor 14e is driven, the chain gear 14e 'is connected to the chain 14f, and the chain gear 14g fixed to the screw shaft is rotated to rotate the screw 14b. As the fine contaminants injected through the fine contaminant inlet 14a are forcibly conveyed in a compressed state, the water contained in the microconcave is quickly discharged through the dewatering hole of the hollow-cylindrical cylindrical screen 14d and again dehydrated. Is transferred into the conveying device 7 by the air pressure of the fine condensate through the hopper (7a), the fine condensate introduced into the conveying device (7) by the air pressure of the fine contaminants Presser (not shown) of waste handling equipment is transported away through the bottom of the venturi portion and the transfer tube (7c) by the air pressure generated by the.

As described above, the present invention is installed so that the pointed portion of the wedge wire (1ca '' ') of the drum screen (1c) is directed inwards, so that the moisture rides on the inclined surface of the wedge wire (1ca' ''). Desorption is easily performed, and the flat portion of the wedge wire 1ca '' 'is the outer circumferential surface of the screen portion 1ca, so that the coarse grains are not caught in the gap and the scraper 3 is disposed on the outer circumferential surface of the drum screen 1c. Since the plate body (3a) of the c) is installed to be in contact with each other, the coarse coarse matter is smoothly injected into the coarse coarse matter inlet 4e of the screw press 4 without fear of the coarse coarse matter being caught in the scraper 3. In addition, since the crushing quantity is properly crushed by the plural crushing protrusions 5ba 'formed on the impeller 5ba of the screw 5b of the conveying device 5, the large lumps of contaminants are smoothly removed by the air pressure. Can be transferred.

In addition, the crushed quantity transfer unit (C) and the fine contaminant dehydration unit (H) in each of the unit devices (A) (B) (C) (D) (D ') (E) (F) (G) (H). Each unit device (A) (B) (C) (D) (D ') including additionally installing a fine contaminant filtration unit (G) and a pneumatic conveying unit (D) (D') of crushed contaminants or fine contaminants. Since (E) (F) (G) (H) is composed of a single device that is assembled to operate with mutually organic relationship, it occupies less space and transfer device by pneumatic pressure of contaminants (7) Since the transport pipe (7c) of the transport to the waste truck, the coarse grains and fine contaminants of the aversive substance is not visible to the outside to prevent odors and smoothly process the contaminants.

Claims (6)

Coarse coarse matter secondary dewatering unit (B), which is installed in the coarse coarse matter discharge outlet 1b in the firstly dehydrated manure, dewatered secondly by a screw press 4 and discharged through the coarse coarse matter discharge outlet 4b. )Wow; A flow rate adjusting part (E) installed at a lower side of the coarse coarse matter primary dewatering part and temporarily storing the desorption liquid, and discharging the temporarily desorbed liquid and the overflowed liquid over the desorption outlet (8b) and the overflow pipe (8a); The desorption liquid which is connected to the connection pipes 9 and 10 respectively connected to the desorption liquid discharge ports 4f and 8b of the screw press 4 and the flow rate adjustment tank 8 and flows through the connection pipe 18 is introduced into the desorbing liquid. Sending (F); In the contaminant treatment device consisting of a storage tank, Coarse coarse primary dehydration unit (A) for dewatering coarse coarse matter first during manure; A crushing quantity transfer unit (C) installed at the coarse filthy water outlet (4b) of the screw press (4) and crushing the coarse filth dehydrated secondly and then conveyed through the crushed fine material discharge port (5ab); A pneumatic conveying unit (D) of known crushed contaminants for conveying the crushed contaminants which are installed and injected into the crushed contaminant discharge ports (5ab) of the conveying unit (C) through the contaminant discharge ports (7b) by air pressure; The connecting pipe 18 connected to the desorption liquid conveying unit F is connected to the desorption liquid, which is introduced and filtered by the vibrating screen 11, through which the desorption liquid and the fine condensate are respectively discharged through the desorption liquid discharge port 11c and the fine contaminant discharge port 11b. Known fine contaminant filtration unit (G) to discharge; Known fine contaminant dewatering part to be discharged through the fine concave discharge outlet 14c by dehydrating again the fine contaminant injected and installed in the fine contaminant discharge port (11b) of the fine contaminant filtration unit (G) by the screw press 14 (H); Including a pneumatic conveying unit (D ') of the known fine contaminants of the fine contaminant discharge port (14c) installed in the fine contaminant discharge port (14c) of the fine contaminant dehydration unit (H) to transfer the fine contaminants introduced through the contaminant discharge port (7b) Comprehensive processing feeder, characterized in that made. The coarse coarse matter primary dewatering portion (A) is formed with a plurality of insertion recesses (1ca ″) at regular intervals on each support (1ca ') arranged at regular intervals, the cross section is A triangular shape of the wedge wire 1ca '' 'is provided at each insertion recess 1ca' 'of the support 1ca' so that a sharp portion of the triangular annular wedge wire 1ca '' 'faces inward. A drum screen 1c including a screen portion 1ca to which a sharp portion is inserted and welded; And a scraper (3) installed on the outer circumferential surface of the drum screen (1c). The crushing quantity transfer part (C) is a screw (5b) provided with a plurality of crushing protrusions (5ba ') in the impeller (5ba) while being provided in the hollow-cylindrical cylindrical cylinder (5a), and said screw (5b). Comprehensive contaminants processing transport, characterized in that consisting of a motor (6) for transmitting power to. 2. The other end of the overflow pipe (8a) having one end connected to the overflow liquid discharge port (8c) of the flow rate adjustment tank (8) is connected to the overflow liquid inlet (11a ') of the fine contaminant filter portion (G). A composite contaminant processing feeder, characterized in that. According to claim 1, wherein the coarse grains primary dewatering unit (A), the coarse grains secondary dewatering unit (B), the crushed fixed quantity transfer unit (C), a pneumatic conveying unit of the complex (D) ) (D '), flow rate adjusting part (E), desorption liquid conveying part (F), fine contaminant filtration part (G), fine contaminant dewatering part (H) is mutually organic in the single bed (19) and single frame (20) A composite material processing transporter, characterized in that it consists of a single unit grouped to operate with an association. 3. The scraper (3) according to claim 2, wherein the scraper (3) has a top of which is formed with an inclined surface (3a '), and is fixed to a plate body (3a) assembled with bolts in a state inserted between the inner and outer fixing bars (3aa) (3ab). (Adjustment piece 3c '' in which an adjustment bolt 3c '' 'is inserted to allow (3aa) to reciprocate the long hole 1d' formed in the front and rear side walls 1d of the main body 1. The plate removal prevention piece 3c, which is welded to the support 3b at which both ends are fixed to each other, and the adjustment bolt 3c 'is coupled so that the plate 3a is not separated outward, is transferred to the body 1. And a scraper 3 fixed to the rear wall 1d; Both ends of each support (1ca ') is a composite material processing transfer machine that is bolted to the front and rear plate body (1cc) of the disk screen of the drum screen (1c).