JP6308933B2 - Sludge dewatering method and sludge dewatering device - Google Patents

Description

  The present invention relates to a sludge dewatering method and a sludge dewatering device, and more particularly to a sludge dewatering method and a sludge dewatering device for sludge generated during the treatment of clean water, sewage and human waste, and sludge generated during the manufacture of industrial products.

  In order to dewater sludge, various types of sludge dewatering machines such as a screw press type, a belt press type, and a filter press type are used. Sludge treated with a sludge dehydrator includes not only sludge generated during the treatment of clean water, sewage, or human waste, but also sludge as industrial waste generated during the manufacture of industrial products such as food, cosmetics, and paper. included.

  When sludge is dewatered by the sludge dewatering machine of the above-described type, dewatered sludge (also referred to as dewatered cake) is discharged from the sludge dewatering machine. In general, the dewatered sludge discharged from the sludge dewatering machine is incinerated or discarded in a landfill.

  In order to incinerate the dewatered sludge, it is necessary to evaporate the water contained in the dewatered sludge. Therefore, when the moisture content of the dewatered sludge is high, the amount of auxiliary fuel used for the incineration process increases, so that the disposal cost increases and a lot of energy is consumed. Further, if the moisture content of the dewatered sludge is high, the volume of the dewatered sludge increases, so that the disposal cost becomes high and a large landfill site must be secured. Therefore, a technique for reducing the water content of dehydrated sludge and reducing the volume of dehydrated sludge is desired.

  In order to solve the above-mentioned problems, a method of heating and dewatering sludge and a method of heating and drying sludge in a vacuum state have been studied. If these methods of heating sludge are used, it is possible to reduce the moisture content of dewatered sludge. However, if the amount of energy required for heating the sludge exceeds the amount of energy required for evaporating the amount of water reduced by using these methods, the significance of heating the sludge is small. turn into.

JP 2003-88711 A

  The present invention has been made in view of the above circumstances, and sludge capable of significantly reducing the water content of dehydrated sludge and achieving volume reduction of dehydrated sludge even when the energy required for heating the sludge is small. An object is to provide a dewatering method and a sludge dewatering device.

In order to achieve the above-described object, according to one embodiment of the present invention, a heating and dehydration process is performed in which sludge is dehydrated while heating to form dehydrated sludge, and the dehydrated sludge formed in the heating and dehydration process is placed in a vacuum chamber. A vacuum evaporation step of evaporating moisture contained in the dewatered sludge in the vacuum chamber under vacuum, the heating dehydration step and the vacuum evaporation step are performed in a sludge dewatering device, and the vacuum The dewatered sludge outlet of the chamber is sealed with the dewatered sludge discharged from the vacuum chamber .

In a preferred aspect of the present invention, the dewatered sludge inlet of the vacuum chamber is sealed by the dewatered sludge transferred to the vacuum chamber .

In a preferred aspect of the present invention, the heating and dehydrating step is performed by a screw press type dehydrator incorporated in the sludge dewatering device.
In a preferred aspect of the present invention, a sludge concentration step for concentrating sludge is performed before the heating and dehydration step.

Another aspect of the present invention includes a heating dehydrator that forms dehydrated sludge by dewatering while heating the sludge, a vacuum chamber that is connected to the heating dehydrator and to which the dehydrated sludge is transferred, and the interior of the vacuum chamber A vacuum source for forming a vacuum, and a transport device connected to a dewatered sludge outlet of the vacuum chamber, the transport device compressing the dewatered sludge discharged from the vacuum chamber to A sludge dewatering apparatus is characterized in that a seal plug for sealing a dewatered sludge outlet is formed .

In a preferred aspect of the present invention, the heating dehydrator forms a seal plug that compresses the dewatered sludge and seals the dewatered sludge inlet of the vacuum chamber.
In a preferred aspect of the present invention, the heating dehydrator is a screw press dehydrator, and the screw press dehydrator includes a dewatered sludge passage pipe connected to a dehydrated sludge inlet of the vacuum chamber, and a vacuum chamber of the vacuum chamber. A back pressure plate disposed opposite to the dewatered sludge inlet, and a screw blade that forms a seal plug in the dewatered sludge passage pipe that seals the dewatered sludge inlet by pressing the dewatered sludge against the back pressure plate. to.

  According to the present invention, the sludge is first dehydrated while being heated. When sludge is heated, the viscosity of the sludge decreases and the filtrate is easily separated from the sludge, and the sludge is thermally denatured and the water retention capacity of the sludge decreases. Can be reduced. Furthermore, by dewatering while heating the sludge, water contained in the sludge is promptly separated from the sludge as filtrate before the heating of the sludge is completed. Therefore, it is possible to prevent excessive energy from being consumed for the separation of the filtrate. Furthermore, in the vacuum evaporation process, the water content of the dewatered sludge can be remarkably reduced because the evaporation of water from the dehydrated sludge is promoted by placing the dehydrated sludge heated in the heat dehydration process under vacuum. This vacuum evaporation process evaporates water from the sludge sufficiently dehydrated in the heating and dehydration process. Therefore, the energy (latent heat of vaporization) consumed in the evaporation process of moisture can be minimized. Moreover, in this invention, the heat | fever dehydration process which spin-dry | dehydrates sludge and the vacuum evaporation process performed after a heat | fever dehydration process are performed by one sludge dehydration apparatus. Therefore, the dewatered sludge having a significantly reduced moisture content can be generated with one sludge dewatering device. In particular, the dewatered sludge that has been subjected to the heat dehydration step while the sealed state of the vacuum chamber is maintained is sent into the vacuum chamber. According to such a method, dewatered sludge can be processed continuously.

  When the dewatered sludge is transported using the transport device while the temperature of the dewatered sludge heated in the heat dehydration process is high, the dewatered sludge is cooled in the transport device to generate condensed water, and this condensed water is corroded by the transport device. It may cause. Moreover, if high temperature dehydrated sludge is stored as it is, the dehydrated sludge may be fermented. According to the present invention, moisture in the dewatered sludge heated in the heat dehydration step is evaporated in the vacuum evaporation step, so that energy as latent heat of evaporation is taken away from the dewatered sludge, and the temperature of the dewatered sludge can be lowered. As a result, it is possible to further prevent corrosion of the conveying device and fermentation of dehydrated sludge.

It is the schematic of the sludge processing apparatus by which the sludge dehydration apparatus which concerns on one Embodiment of this invention is arrange | positioned. It is a mimetic diagram showing the sludge dehydration device concerning one embodiment of the present invention. It is the sectional view on the AA line of FIG. It is a figure explaining operation | movement of the sludge dehydration apparatus shown in FIG. It is a front view which shows the modification of a back pressure plate. Fig.6 (a) is a side view of the cutter shown in FIG. 5, FIG.6 (b) is a perspective view of the cutter shown in FIG. It is a schematic diagram which shows the modification of the sludge dehydration apparatus in which the water drive ejector apparatus was used as a vacuum source. It is a schematic diagram which shows the sludge dehydration apparatus which concerns on another embodiment.

  Embodiments of the present invention will be described below with reference to the drawings. FIG. 1 is a schematic view of a sludge treatment apparatus provided with a sludge dewatering apparatus according to an embodiment of the present invention. The sludge treated by the sludge treatment apparatus shown in FIG. 1 includes not only sludge generated during the treatment of clean water, sewage, or human waste, but also industrial waste generated during the manufacture of industrial products such as food, cosmetics, and paper. Sludge as a thing is also included.

  As shown in FIG. 1, in this sludge treatment apparatus, sludge is first supplied to a coagulation tank 30. A chemical such as a flocculant is charged into the coagulation tank 30, and the chemical and sludge are stirred by a stirring blade 31 that is rotated by a driving source 32 such as a motor. Aggregating flocs in which suspended substances in the sludge are gathered are formed by stirring the chemicals and sludge in the aggregating tank 30. Although the flocculation tank 30 shown in FIG. 1 has two stages, the flocculation tank 30 may be one stage or a plurality of stages of three or more stages.

  Next, the sludge on which the aggregated flocs are formed is supplied to the concentrating device 35. The concentration device 35 is a device that concentrates sludge by reducing the amount of water in the sludge. As the concentrating device 35, a known concentrating device such as a belt type concentrator can be used. The concentrating device 35 may be omitted.

  The sludge concentrated by the concentrating device 35 is conveyed to the sludge dewatering device 40. FIG. 2 is a schematic diagram showing a sludge dewatering device 40 according to an embodiment of the present invention. Hereinafter, the sludge dewatering device 40 will be described with reference to FIG.

  A sludge dewatering device 40 shown in FIG. 2 includes a screw press type dehydrator (heated dehydrator) 41 that dehydrates while heating sludge, and a vacuum chamber 42 into which the dewatered sludge formed by the screw press type dehydrator 41 is transferred. A vacuum source 44 connected to the vacuum chamber 42 via a pipe 45 and a screw-type transport conveyor (transport device) 20 for discharging dewatered sludge from the vacuum chamber 42 are provided. The vacuum source 44 is, for example, a vacuum pump. By driving the vacuum source 44, the air in the vacuum chamber 42 is exhausted, and a vacuum is formed in the vacuum chamber 42. The vacuum pressure in the vacuum chamber 42 achieved by the vacuum source 44 is, for example, −90 kPa. In the following, a screw press type dehydrator 41 will be described as a heating dehydrator. However, instead of the screw press dehydrator 41, a belt press dehydrator may be used as the heating dehydrator.

  As shown in FIG. 2, the screw press dehydrator 41 is fixed to a cylindrical screen casing (filter cylinder) 1, a screw shaft 3 concentrically arranged in the screen casing 1, and an outer surface of the screw shaft 3. The screw blade 4 is rotated, and the rotation mechanism 7 is configured to rotate the screw blade 4 and send the sludge toward the vacuum chamber 42. The screen casing 1 includes a cylindrical screen 1A that surrounds the screw blades 4, and a dewatered sludge passage pipe 1B that is connected to the downstream end of the cylindrical screen 1A. The cylindrical screen 1A is composed of a perforated plate such as punching metal, while the dewatered sludge passage tube 1B is composed of a plate without holes. The dewatered sludge passage pipe 1B is connected to the vacuum chamber 42, and the dewatered sludge passage pipe 1B is located between the cylindrical screen 1A and the vacuum chamber 42.

  The screw shaft 3 extends through the screen casing 1 (the cylindrical screen 1A and the dewatered sludge passage pipe 1B) and the vacuum chamber 42. The screw shaft 3 in the cylindrical screen 1A has a truncated cone shape whose diameter gradually increases toward the downstream side. The upstream end of the cylindrical screen 1 </ b> A is sealed by a blocking wall 8. The screw shaft 3 extends through the blocking wall 8, and the end of the screw shaft 3 is connected to the rotation mechanism 7. The rotation mechanism 7 includes a motor and a speed reduction mechanism. In addition, as the rotation mechanism 7, other drive sources such as a diesel engine may be used.

  A bearing 10 is installed on the closing wall 8 to rotatably support the screw shaft 3 and to have a sealing function. The other end of the screw shaft 3 is rotatably supported by a bearing 11 installed on the side wall 42 a of the vacuum chamber 42. This bearing 11 also has a sealing function, and the gap between the screw shaft 3 and the side wall 42 a is sealed by the bearing 11.

  The screw blade 4 is a single blade that spirally extends along the longitudinal direction of the screw shaft 3, and the axial length of the screw blade 4 is the same as the axial length of the cylindrical screen 1A made of a perforated plate. It is almost the same. A minute gap is formed between the inner surface of the cylindrical screen 1A and the screw blades 4, and the screw blades 4 can rotate without contacting the cylindrical screen 1A. A sludge inlet 2 is formed at the upstream end of the screen casing 1. The sludge thrown into the sludge inlet 2 is transferred to the dewatered sludge passage pipe 1B and the vacuum chamber 42 through the cylindrical screen 1A by the rotating screw blades 4.

  A space in which the sludge is transferred in the cylindrical screen 1 </ b> A is formed by the inner surface of the cylindrical screen 1 </ b> A, the screw blade 4, and the screw shaft 3. As shown in FIG. 2, the volume of the transfer space gradually decreases along the direction of sludge progression. Therefore, as this space is moved by the screw blades 4, the sludge is squeezed and dehydrated. The filtrate that has passed through the cylindrical screen 1A is collected by a filtrate receiver 14 disposed below the cylindrical screen 1A.

  The screw shaft 3 is configured to be hollow, and a supply pipe 3 a for supplying a heating medium such as steam, heated water, or heated oil to the internal space of the screw shaft 3 is connected to the downstream end of the screw shaft 3. Is done. Since the screw shaft 3 is heated by the heating medium supplied via the supply pipe 3a, the sludge in contact with the screw shaft 3 can be heated. The heating medium supplied to the internal space of the screw shaft 3 is discharged to the outside of the screw shaft 3 through a discharge pipe 3 b connected to the upstream end of the screw shaft 3.

  Instead of the discharge pipe 3b connected to the upstream end of the screw shaft 3, a discharge pipe 3c connected to the downstream end of the screw shaft 3 may be provided. In this case, the screw shaft 3 is provided with a double pipe structure including an outer flow path and an inner flow path communicating with each other on the upstream side of the screw shaft 3. The supply pipe 3a is connected to the outer flow path, while the discharge pipe 3c is connected to the inner flow path. The heating medium supplied to the outer flow path via the supply pipe 3 a passes through the inner flow path and is discharged to the outside of the screw shaft 3 from the discharge pipe 3 c connected to the downstream end of the screw shaft 3.

  The heating medium filling the internal space of the screw shaft 3 can indirectly heat the sludge in contact with the screw shaft 3 and evaporate the moisture contained in the sludge. In addition, when sludge is heated, the viscosity of the sludge decreases and the filtrate is easily separated from the sludge, and the sludge is thermally denatured and the water retention capacity of the sludge decreases, so the water content of the sludge is efficiently reduced. be able to. The sludge thrown into the cylindrical screen 1A is squeezed and dehydrated by the screw blades 4 while being heated by the heating medium through the screw shaft 3 to form dehydrated sludge.

  The cylindrical screen 1 </ b> A is connected to the dewatered sludge passage pipe 1 </ b> B, and the dehydrated sludge passage pipe 1 </ b> B is connected to the vacuum chamber 42. The dewatered sludge passage pipe 1B has a cylindrical shape, and the inner diameter of the dewatered sludge passage pipe 1B is equal to the inner diameter of the cylindrical screen 1A. The screw shaft 3 extends through the dewatered sludge passage pipe 1B, but the screw blade 4 is not provided in the dewatered sludge passage pipe 1B. The dewatered sludge passes through a space formed by the outer surface of the screw shaft 3 and the inner surface of the dewatered sludge passage pipe 1B and is transferred to the vacuum chamber 42.

  The downstream end of the dewatered sludge passage pipe 1B is connected to the dewatered sludge inlet 42c of the vacuum chamber 42. An annular back pressure plate 16 is disposed opposite to the dewatered sludge inlet 42c. The back pressure plate 16 is made of a metal such as stainless steel or brass, or a resin, and has a truncated cone shape having a tapered surface 16a for receiving dewatered sludge transferred through the dewatered sludge passage pipe 1B. . A through-hole through which the screw shaft 3 passes is formed at the center of the back pressure plate 16, and the back pressure plate 16 is disposed concentrically with the screw shaft 3. The back pressure plate 16 is not fixed to the screw shaft 3, and the back pressure plate 16 does not rotate.

  The back pressure plate 16 is connected to a back pressure plate driving device 18. The back pressure plate driving device 18 is configured to move the back pressure plate 16 in the axial direction of the screw shaft 3. Accordingly, the gap between the back pressure plate 16 and the dewatered sludge inlet 42 c of the vacuum chamber 42 is adjusted by the back pressure plate driving device 18. The back pressure plate driving device 18 is constituted by, for example, a hydraulic cylinder or an electric cylinder. The back pressure plate 16 is configured to move in the axial direction within a range that does not contact the screw blades 4. In the example shown in the figure, the outer diameter of the back pressure plate 16 is larger than the inner diameter of the screen casing 1 so that the back pressure plate 16 cannot enter the screen casing 1, but the present invention is not limited to this example. The back pressure plate 16 may be allowed to enter the screen casing 1 within a range that does not contact the screw blades 4.

  An aggregating device 49 is arranged between the vacuum source 44 and the vacuum chamber 42. The vacuum chamber 42 is connected to a vacuum source 44 via an aggregating device 49 disposed in the pipe 45. Cooling water flows through the aggregating device 49. This cooling water exchanges heat with the air exhausted from the vacuum source 44 and agglomerates the water vapor contained in the air to generate water. The generated water is discharged from the aggregating device 49 through the drain.

  The vacuum chamber 42 is connected to a screw-type transfer conveyor (transfer device) 20 for discharging dehydrated sludge from the vacuum chamber 42. More specifically, the dewatered sludge discharge pipe 21 of the screw type conveyor 20 is connected to the lower end of the vacuum chamber 42. The vacuum chamber 42 is disposed between the screw press type dehydrator 41 and the screw type conveyer 20. The dewatered sludge discharge pipe 21 is formed with a dewatered sludge inlet 22 into which dehydrated sludge is charged. The dewatered sludge inlet 22 is connected to a dewatered sludge outlet 42 d of the vacuum chamber 42. The dewatered sludge outlet 42 d is located at the lower end of the vacuum chamber 42. The dewatered sludge discharge pipe 21 of the present embodiment is disposed to be inclined with respect to the horizontal direction. Specifically, the dewatered sludge discharge pipe 21 has an upward gradient along the conveying direction of the dewatered sludge. The dewatered sludge discharge pipe 21 may be disposed horizontally.

  FIG. 3 is a cross-sectional view taken along line AA in FIG. As shown in FIG. 3, the dewatered sludge discharge pipe 21 has an elliptical cross section composed of a pair of parallel straight portions and a pair of arc portions that protrude outward and face each other. Two screw shafts 23 are arranged in the dewatered sludge discharge pipe 21, and screw blades 24 are fixed to the outer surface of each screw shaft 23. Similar to the dewatered sludge discharge pipe 21, the screw shaft 23 and the screw blade 24 have an upward gradient along the transport direction of the dewatered sludge. When the dewatered sludge discharge pipe 21 is disposed horizontally, the screw blades 24 extend in the horizontal direction in the same manner as the dewatered sludge discharge pipe 21.

  As shown in FIG. 2, the upstream end of the dewatered sludge discharge pipe 21 is sealed by a blocking wall 25. The screw shaft 23 extends through the blocking wall 25, and an end portion of the screw shaft 23 is connected to a rotation mechanism 27. The blocking wall 25 is provided with a bearing 26 that rotatably supports the screw shaft 23 and has a sealing function. The downstream end of the dewatered sludge discharge pipe 21 is sealed by a closing wall 28, and the other end of the screw shaft 23 is rotatably supported by a bearing 29 installed on the closing wall 28. The rotation mechanism 27 includes a motor and a speed reduction mechanism. Note that another driving source such as a diesel engine may be used as the rotation mechanism 27.

  The dewatered sludge discharge pipe 21 has an upstream portion 21a having a dewatered sludge inlet 22, a reduced portion 21b in which the cross-sectional area gradually decreases, and a downstream portion 21c having a cross-sectional area reduced in the reduced portion 21b. The vacuum chamber 42 is connected to the upstream part 21a, the upstream part 21a is connected to the reduction part 21b, and the reduction part 21b is connected to the downstream part 21c. The downstream portion 21c is provided with a dewatered sludge discharge port 21d through which dehydrated sludge is discharged. The screw shaft 23 extends through the upstream portion 21a, the reduced portion 21b, and the downstream portion 21c. The screw blades 24 are provided only in the upstream portion 21a, and are not provided in the reducing portion 21b and the downstream portion 21c.

  The screw blade 24 is a single blade that extends spirally along the longitudinal direction of the screw shaft 23. A minute gap is formed between the inner surface of the dewatered sludge discharge pipe 21 and the screw blade 24, and the screw blade 24 can rotate without contacting the dewatered sludge discharge pipe 21.

  The upstream portion of the screw shaft 23 is hollow. That is, the upstream part of the screw shaft 23 located in the upstream part 21a of the dewatered sludge discharge pipe 21 is formed hollow. As shown in FIG. 2, a supply pipe 37 for supplying a heating medium such as steam, heated water, or heated oil and fat, and the heating medium are discharged into the internal space in the upstream portion of the screw shaft 23. A discharge pipe 38 is connected.

  Next, the heat dehydration process and the vacuum evaporation process of sludge will be described. FIG. 4 is a diagram for explaining the operation of the sludge dewatering device 40 shown in FIG. Sludge is introduced into the cylindrical screen 1A of the screen casing 1 from the sludge inlet 2. The sludge is transported through the cylindrical screen 1A toward the dehydrated sludge passage pipe 1B by the rotating screw blades 4 while being heated by the heating medium flowing in the screen shaft 3. The sludge is squeezed and dehydrated as it moves through the cylindrical screen 1A. The filtrate that has passed through the cylindrical screen 1A is collected by a filtrate receiver 14 disposed below the cylindrical screen 1A. The sludge is heated and dehydrated in the cylindrical screen 1A to form dehydrated sludge (heating and dehydrating step).

  The dewatered sludge that has moved through the cylindrical screen 1A reaches the dewatered sludge passage pipe 1B in which the screw blades 4 are not provided. In the dewatered sludge passage pipe 1B, the dewatered sludge is moved in the dewatered sludge passage pipe 1B by the subsequent dewatered sludge transferred by the screw blades 4 and further pressed against the back pressure plate 16. The dewatered sludge is compressed by being prevented from moving by the back pressure plate 16. The compressed dewatered sludge forms a seal plug for sealing the dewatered sludge inlet 42c of the vacuum chamber 42 in the dewatered sludge passage pipe 1B. Since the dewatered sludge existing in the dewatered sludge passage pipe 1B is in contact with the outer peripheral surface of the screw shaft 3, it is heated by the heating medium flowing in the screw shaft 3.

  When the vacuum source 44 is driven, a vacuum is formed in the vacuum chamber 42. The dewatered sludge inlet 42c of the vacuum chamber 42 is sealed by the dewatered sludge in the dewatered sludge passage pipe 1B pressed against the back pressure plate 16. The dehydrated sludge is introduced into the vacuum chamber 42 through a gap between the back pressure plate 16 and the dehydrated sludge inlet 42c while forming a seal plug in the dehydrated sludge passage pipe 1B. The dewatered sludge in the vacuum chamber 42 is placed under vacuum, and the water contained in the dewatered sludge evaporates (vacuum evaporation process).

  The dehydrated sludge is input to the dehydrated sludge discharge pipe 21 of the screw type conveyor 20 through the dehydrated sludge inlet 22. The dewatered sludge is transported through the dewatered sludge discharge pipe 21 toward the discharge port 21d by the rotating screw blades 24. The heating medium is supplied into the upstream portion of the screw shaft 23 through the supply pipe 37 and heats the dewatered sludge in contact with the screw shaft 23. The heating medium supplied into the screw shaft 23 is discharged outside the screw shaft 23 through a discharge pipe 38 connected to the screw shaft 23.

  The cross-sectional area of the space where the dewatered sludge is transferred in the dewatered sludge discharge pipe 21 is gradually reduced by the reduction portion 21b. Therefore, in the reduced portion 21b, the resistance acting on the dewatered sludge increases. In the reduced portion 21b, the dewatered sludge is compressed by the subsequent dewatered sludge transferred by the screw blades 24 to form a seal plug in the downstream portion 21c. When the vacuum source 44 is operated, the dewatered sludge outlet 42d of the vacuum chamber 42 is sealed by the dewatered sludge that becomes the seal plug. The dehydrated sludge is pushed by the subsequent dehydrated sludge and discharged from the discharge port 21d little by little while forming a seal plug in the screw type conveyor 20. As described above, the dewatered sludge inlet 42c and the dewatered sludge outlet 42d of the vacuum chamber 42 are continuously sealed by the dewatered sludge, so that the dewatered sludge is continuously supplied to the vacuum chamber 42 while maintaining the sealed state of the vacuum chamber 42. It can be transferred and continuously discharged from the vacuum chamber 42.

  By placing the dewatered sludge heated in the heat dehydration step under vacuum in the vacuum chamber 42, evaporation of water from the dewatered sludge is promoted. Further, moisture evaporates from the dewatered sludge in the upstream portion 21 a of the dewatered sludge discharge pipe 21 communicating with the vacuum chamber 42. The evaporated water is exhausted by the vacuum source 44. As a result, the moisture content of the dewatered sludge can be greatly reduced.

  Instead of the screw-type transport conveyor 20 shown in FIG. 4, a positive displacement pump such as a single screw pump or a piston pump may be used as the transport device. The dewatered sludge supplied to such a positive displacement pump is compressed and conveyed while maintaining the compacted state of the dewatered sludge that the seal plug formed by the screw press dehydrator 41 has. Therefore, even if these positive displacement pumps are used, a seal plug for sealing the dewatered sludge outlet 42d of the vacuum chamber 42 can be formed.

  In the present embodiment, sludge is first dehydrated while being heated by the screw press dehydrator 41 (heating dehydration step). When sludge is heated, the viscosity of the sludge decreases and the filtrate is easily separated from the sludge, and the sludge is thermally denatured and the water retention capacity of the sludge decreases. Can be reduced. Further, when the sludge is dehydrated while being heated, the water contained in the sludge is promptly separated from the sludge as filtrate before the heating of the sludge is completed. Therefore, it is possible to prevent excessive energy from being consumed for the separation of the filtrate. Further, in the vacuum chamber 42, a vacuum evaporation step is performed in which the moisture of the dewatered sludge formed by the screw press dehydrator 41 is evaporated under vacuum. In the vacuum evaporation step, the water content from the dewatered sludge is promoted by placing the dehydrated sludge heated in the heat dehydration step under vacuum, so that the water content of the dewatered sludge can be significantly reduced. This vacuum evaporation process evaporates water from the sludge sufficiently dehydrated in the heating and dehydration process. Therefore, the energy (latent heat of vaporization) consumed in the evaporation process of moisture can be minimized. Moreover, the vacuum which implements the vacuum evaporation process which evaporates the water | moisture content of the dewatering sludge formed with the screw press-type dehydrator 41 and the screw press-type dehydrator 41 which performs the heat | fever dehydration process which dehydrates, heating sludge A chamber 42 is provided in one sludge dewatering device 40. In particular, the dewatered sludge is continuously transferred into the vacuum chamber 42 while the dewatered sludge inlet 42c and the dewatered sludge outlet 42d of the vacuum chamber 42 are continuously sealed by the dewatered sludge. Therefore, dehydrated sludge having a reduced water content can be produced by continuous treatment.

  When the dewatered sludge is transported using a transport device (for example, the screw-type transport conveyor 20) while the temperature of the dewatered sludge heated in the heat dehydration process is high, the dewatered sludge is cooled in the transport device to generate dew condensation water. The condensed water may cause corrosion of the transport device. Moreover, if high temperature dehydrated sludge is stored as it is, the dehydrated sludge may be fermented. According to the present invention, moisture in the dewatered sludge heated in the heat dehydration step is evaporated in the vacuum evaporation step, so that energy as latent heat of evaporation is taken away from the dewatered sludge, and the temperature of the dewatered sludge can be lowered. As a result, low-temperature dehydrated sludge is generated, and corrosion of the transfer device and fermentation of the dehydrated sludge can be prevented.

  A comparative experiment of sludge dewatering methods was conducted using surplus sludge generated at a human waste treatment plant. In the experiment, dehydrated sludge was generated in the heating and dehydration process that dehydrates while heating the sludge, and then the vacuum evaporation process was performed on the dehydrated sludge, and the moisture content of the dewatered sludge after the vacuum evaporation process was measured (experiment). 1: Sludge dewatering method of this embodiment). The vacuum pressure in the vacuum evaporation step in Experiment 1 was −97 kPa. Furthermore, when the dewatered sludge dehydrated without heating the sludge is not vacuum evaporated (Comparative Example 1), the water content of the dewatered sludge and the dewatered sludge subjected to the heat dewatering process of dewatering while heating the sludge are vacuum evaporated. The moisture content of the dewatered sludge when the process was not performed (Comparative Example 2) was measured. The dewatered sludge of Experiment 1, Comparative Example 1, and Comparative Example 2 was generated using a screw press dehydrator 41 and a vacuum chamber 42 as shown in FIG. The sludge solid matter dry matter weight (processed solid matter amount) is 7 kg-DS / h, and the sludge is concentrated to 10% with a concentrator before the sludge is put into the screw press dehydrator 41. In addition, a polymer and an inorganic flocculant (polyiron) are added to the concentrated sludge.

  The water content of the dewatered sludge of Comparative Example 1 was 80%, and the water content of the dewatered sludge of Comparative Example 2 was 73%. From the results of Comparative Examples 1 and 2, it can be seen that when the sludge is dehydrated while heating, the water content of the dehydrated sludge can be significantly reduced.

  The water content of the dewatered sludge in Experiment 1 was 71%. From the results of Experiment 1 and Comparative Example 2, it can be seen that the moisture content of the dewatered sludge that has been subjected to the vacuum evaporation step after the heat dehydration step can be further reduced.

  Thus, when the sludge is heated and dehydrated by dehydrating to form dehydrated sludge, and after the heated and dehydrated step, the vacuum evaporation step of evaporating the moisture contained in the dehydrated sludge is performed. The water content of can be significantly reduced. However, if the amount of energy required for the sludge dewatering method for obtaining a low water content dewatered sludge is large, the sludge dewatering method is disadvantageous from the viewpoint of energy saving. Therefore, based on the moisture content of the dewatered sludge obtained by the sludge dewatering method of the present embodiment that performs the heating dewatering step and the vacuum evaporation step, the thermal energy required by this sludge dewatering method and the following comparative sludge dewatering method Compare the thermal energy required by

  The comparative sludge dewatering method 1 is a sludge dewatering method in which the water contained in the dewatered sludge is vacuum evaporated while the dewatered sludge is heated after dewatering without heating the sludge. The comparative sludge dewatering method 2 is a sludge dewatering method in which after sludge is heated to a desired temperature, the sludge is dehydrated to generate dehydrated sludge, and the dewatered sludge is vacuum evaporated.

  First, the thermal energy necessary for the sludge dewatering method of the present embodiment is examined. Assume sludge having a dry matter weight (processed solid amount) of 50 kg-DS / h and a sludge concentration of 2.5%. In this case, the amount of sludge to be treated is 4000 kg / h. When dewatering 4000 kg / h sludge while heating from 20 ° C. to 60 ° C. with the screw press type dehydrator 41, the required thermal energy is 503 MJ / h. The amount of heat required to dehydrate while heating 4000 kg / h sludge is about 50% of the amount of heat required to heat the entire amount of 4000 kg / h sludge. It is assumed that the ratio of thermal energy consumed by heat radiation is 50%. When the sludge is dehydrated with the screw press dehydrator 41 without heating the sludge, the water content of the dehydrated sludge is 80%. When the sludge is heated to 60 ° C. and the sludge is dehydrated with the screw press dehydrator 41 The water content of the dewatered sludge is 72%. The amount of water that can be reduced by dehydrating the sludge while heating is 142.9 kg / h. Furthermore, dehydrated sludge heated to 60 ° C. is placed under a vacuum of −97 kPa. Assuming that the temperature of the dewatered sludge decreases to 30 ° C., which is the saturation temperature of water of −97 kPa, the amount of heat deprived from the dewatered sludge is 44.89 MJ / h. The latent heat of vaporization was 2.35 MJ / kg. The amount of water that can be evaporated by this amount of heat is 19.1 kg / h. Therefore, the water content of dewatered sludge can be reduced from 72% to 70.4% by carrying out the vacuum evaporation step. Further, as described above, the thermal energy required in the sludge dewatering method of the present embodiment is 503 MJ / h.

  Next, after dewatering without heating the sludge, a comparative sludge dewatering method 1 in which moisture contained in the dewatered sludge is vacuum evaporated while the dewatered sludge is heated will be examined. When the sludge is dehydrated by the screw press dehydrator 41 without heating the sludge, the water content of the dehydrated sludge is 80%. In order to reduce the water content of the dewatered sludge from 80% to 70.4%, it is necessary to evaporate a water content of 162 kg / h. In order to evaporate the moisture contained in the dewatered sludge by vacuum evaporation while heating the dewatered sludge, the heat energy of 585.5 MJ / h is required. As the thermal efficiency, 0.65 which is a general value of an indirect steam dryer was used. Therefore, the thermal energy required for the comparative sludge dewatering method 1 is 585.5 MJ / h.

  Next, a comparative sludge dewatering method 2 in which the sludge is heated to 60 ° C. and then dehydrated to produce dehydrated sludge, and the dewatered sludge is evaporated in vacuum will be examined. In the case of this comparative sludge dewatering method 2, it is necessary to heat a total amount of 4000 kg / h sludge to 60 ° C. The amount of heat required to raise the temperature of 4000 kg / h sludge to 60 ° C. is 1006 MJ / h. It is assumed that the ratio of thermal energy consumed by heat radiation is 50%. When this heated sludge is dehydrated using the screw press type dehydrator 41, the water content of the dehydrated sludge obtained is 72%. When this dewatered sludge is placed under a vacuum of -97 kPa, the water content of the dewatered sludge can be reduced from 72% to 70.4%. Therefore, the heat energy required in the comparative sludge dewatering method 2 is 1006 MJ / h.

  The heat energy (503 MJ / h) required in the sludge dewatering method of the present embodiment is required in the heat energy (585.5 MJ / h) required in the comparative sludge dewatering method 1 and the comparative sludge dewatering method 2. Compared with the heat energy (1006 MJ / h) to be used, the heat energy required in the sludge dewatering method of this embodiment is the smallest. Therefore, it turns out that the sludge dehydration method of this embodiment is the most effective from a viewpoint of energy saving. Thus, in the sludge dewatering method of this embodiment, moisture is evaporated in the vacuum evaporation step from the sludge sufficiently dehydrated in the heat dehydration step. Therefore, the energy (latent heat of vaporization) consumed in the evaporation process of moisture can be minimized.

  As shown in FIGS. 2 and 4, a heating jacket 46 that covers the outer surface of the dewatered sludge passage pipe 1 </ b> B may be provided. The heating jacket 46 includes a supply pipe 47 for supplying a heating medium such as steam, heated water, or heated oil and fat to the heating jacket 46, and a discharge pipe 48 for discharging the heating medium from the heating jacket 46. And connected to. The heating medium is supplied into the heating jacket 46 through the supply pipe 47, fills the heating jacket 46, and is discharged from the heating jacket 46 through the discharge pipe 48. The heating medium passing through the inside of the heating jacket 46 can give thermal energy to the dewatered sludge before being introduced into the vacuum chamber 42.

  As shown in FIG. 2, the back pressure plate 16 may be configured to be hollow. The internal space of the back pressure plate 16 includes a supply pipe 17a for supplying a heating medium such as steam, heated water, or heated oil and fat to the back pressure plate 16, and a discharge pipe 17b for discharging the heating medium from the back pressure plate 16. And connected to. The heating medium is supplied into the back pressure plate 16 through the supply pipe 17a, fills the internal space of the back pressure plate 16, and is discharged from the back pressure plate 16 through the discharge pipe 17b. The heating medium passing through the back pressure plate 16 can give thermal energy to the dewatered sludge in contact with the back pressure plate 16.

  Thermal energy given to the dewatered sludge from the heating medium via the screw shaft 3, the heating jacket 46, and the back pressure plate 16 is used to evaporate water in the dewatered sludge transferred into the vacuum chamber 42. As a result, dehydrated sludge having a very low moisture content can be generated. When water evaporates from the dewatered sludge, heat energy is taken away from the dehydrated sludge as latent heat of vaporization, so that dehydrated sludge having a reduced temperature is formed in the vacuum chamber 42.

  The dewatered sludge conveyed through the dewatered sludge discharge pipe 21 forms a seal plug in the downstream portion 21 c of the dewatered sludge discharge pipe 21. Therefore, a vacuum is formed in the upstream portion 21 a of the dewatered sludge discharge pipe 21 communicating with the vacuum chamber 42. The heating medium supplied to the upstream portion of the screw shaft 23 gives thermal energy to the dewatered sludge that contacts the upstream portion of the screw shaft 23. This thermal energy is used to evaporate the water in the dewatered sludge transported in the upstream portion 21a of the dewatered sludge discharge pipe 21. Since the heat energy given to the dewatered sludge in the dewatered sludge discharge pipe 21 is deprived from the dehydrated sludge as latent heat of evaporation, the temperature of the dewatered sludge in the dewatered sludge discharge pipe 21 hardly rises. Therefore, low-temperature dehydrated sludge can be discharged from the screw type conveyor 20.

  As a heating medium supplied to the inside of the screw shaft 3, the heating jacket 46, the back pressure plate 16, and the screw shaft 23, steam or hot water generated from a combustion furnace that burns digestion gas taken out from the digestion tank may be used. it can. Further, waste heat steam or hot water generated from a generator that generates power using digestion gas may be used. This digester is a facility for fermenting sludge. As the heating medium, steam generated from an incinerator that incinerates the dewatered sludge discharged from the sludge dewatering device 40 may be used.

  FIG. 5 is a front view showing a modified example of the back pressure plate 16. As shown in FIG. 5, a plurality of cutters 19 are provided on the tapered surface 16 a of the back pressure plate 16. These cutters 19 are arranged at equal intervals along the circumferential direction of the annular back pressure plate 16 and extend in the radial direction of the back pressure plate 16.

  6A is a side view of the cutter 19 shown in FIG. 5, and FIG. 6B is a perspective view of the cutter 19 shown in FIG. As shown in FIG. 6A and FIG. 6B, the cutter 19 of the present embodiment has a triangular prism shape, and is one of three square surfaces (side surfaces of the triangular prism) constituting the triangular prism. The square surface 19 a is fixed to the tapered surface 16 a of the back pressure plate 16. The other two square surfaces 19b and 19c are in contact with each other at a side 19d, and these square surfaces 19b and 19c constitute a blade surface. The side 19 d extends in the radial direction of the back pressure plate 16. Two triangular surfaces (the top surface and the bottom surface of the triangular prism) 19e and 19f constituting the triangular prism are connected perpendicularly to the side 19d. Since the tapered surface 16a of the back pressure plate 16 is inclined with respect to the horizontal direction, the quadrangles 19b and 19c are trapezoidal.

  The dewatered sludge pressed against the back pressure plate 16 is finely divided by these cutters 19. As a result, the water in the dewatered sludge becomes more likely to approach the vacuum pressure, and the amount of water evaporated from the dewatered sludge can be increased. Sixteen cutters 19 according to this embodiment are provided (see FIG. 5). However, the number of cutters 19 may be less than 16, or more than 16.

  FIG. 7 is a schematic view showing a modification of the sludge dewatering device 40 in which a water-driven ejector device is used as the vacuum source 44 for evacuating the vacuum chamber 42. As shown in FIG. 7, the ejector device used as the vacuum source 44 includes an ejector 50, a drive water tank 51 that stores water as drive fluid of the ejector 50 (hereinafter referred to as drive water), and drive water. And a drive pump 52 for boosting the pressure. The ejector 50 is connected to the vacuum chamber 42 via an aggregating device 49 disposed in the pipe 45. The drive water in the drive water tank 51 is boosted by the drive pump 52 and supplied to the ejector 50. In the process in which the high-pressure driving water passes through the ejector 50, the air in the vacuum chamber 42 is sucked. The driving water discharged from the ejector 50 and the air in the vacuum chamber 42 are returned to the driving water tank 51 and separated into water and air by the driving water tank 51. The separated air is exhausted from the driving water tank 51, and the separated water is stored in the driving water tank 51 and used again as driving water.

  In the present embodiment, the sludge is dehydrated while being heated by the screw press dehydrator 41. When sludge is heated, volatile odor components increase. When a water-driven ejector device is used as the vacuum source 44 for depressurizing the vacuum chamber 42, volatile odor components contained in the air exhausted from the vacuum chamber 42 can be dissolved in the driving water. As a result, since the odor component contained in the air exhausted from the drive water tank 51 can be reduced, the load on the deodorizing device for processing the odor component generated from the sludge is reduced. The odor component dissolved in the driving water is processed in a wastewater treatment facility to which used driving water is transferred.

  FIG. 8 is a schematic diagram showing a sludge dewatering device 40 according to another embodiment. In the sludge dewatering device 40 shown in FIG. 8, the vacuum source 44 communicates with the dewatered sludge passage pipe 1B and depressurizes the dewatered sludge passage pipe 1B. In the present embodiment, instead of the vacuum chamber 42 shown in FIG. 2 connected to the screw press dehydrator 41, a communication chamber 60 that communicates the screw press dehydrator 41 and the screw conveyor 20 is provided. The above-described bearing 11 is installed on the side wall 60 a of the communication chamber 60, and the end of the screw shaft 3 is rotatably supported by the bearing 11. The dehydrated sludge passage pipe 1B described above is connected to the dehydrated sludge inlet 60c of the communication chamber 60. Further, the dewatered sludge inlet 22 of the screw type conveyor 20 is connected to the dehydrated sludge outlet 60 d of the communication chamber 60. The dehydrated sludge is supplied from the dehydrated sludge passage pipe 1B to the communication chamber 60 through the dehydrated sludge inlet 60c. The dewatered sludge supplied to the communication chamber 60 is supplied to the screw-type transport conveyor 20 from the dehydrated sludge inlet 22 through the dehydrated sludge outlet 60d. Since the vacuum source 44 is not connected to the communication chamber 60, the pressure in the communication chamber 60 is atmospheric pressure. Moreover, unlike the above-mentioned embodiment, the cross-sectional area of the dewatered sludge discharge pipe 21 of the screw type conveyance conveyor 20 is constant. The other configuration is the same as the sludge dewatering device 40 shown in FIG.

  An annular vacuum chamber 55 is provided on the outer surface of the dewatered sludge passage pipe 1B. The vacuum chamber 55 is connected to one end of the pipe 45, and the vacuum source 44 is connected to the other end of the pipe 45. An aggregating device 49 is disposed in the pipe 45. A large number of openings (not shown) communicating with the vacuum chamber 55 are provided on the outer surface of the dewatered sludge passage pipe 1B. When the vacuum source 44 is operated, a vacuum is formed in the vacuum chamber 55, and the inside of the dewatered sludge passage pipe 1B communicating with the vacuum chamber 55 is evacuated. A vacuum pump may be used as the vacuum source 44, or an ejector device shown in FIG.

  As described above, the dewatered sludge that has become a seal plug is present inside the dewatered sludge passage pipe 1B. Therefore, the internal space of the dewatered sludge passage pipe 1B is sealed by the dewatered sludge existing on the upstream side and the downstream side of the vacuum chamber 55, and a vacuum can be formed in the dewatered sludge passage pipe 1B.

  By placing the dewatered sludge heated in the heat dehydration step under vacuum, evaporation of water from the dewatered sludge is promoted. The evaporated water is exhausted by the vacuum source 44. As a result, the moisture content of the dewatered sludge can be further reduced, and a dehydrated sludge having a significantly reduced moisture content can be obtained. Further, in the present embodiment, the heating and dehydrating process for dewatering while heating the sludge and the vacuum evaporating process for evaporating the moisture of the dewatered sludge are continuously performed in the screen casing 1 of the screw press type dehydrator 41. Therefore, dehydrated sludge having a significantly reduced moisture content can be produced by continuous treatment.

  In the embodiment shown in FIG. 8, the dewatered sludge passage pipe 1 </ b> B is heated by a heating jacket 46 to which a heating medium such as steam, heated water or heated oil is supplied. The warming jacket 46 includes an upstream warming jacket 46 a disposed on the upstream side of the vacuum chamber 55 and a downstream warming jacket 46 b disposed on the downstream side of the vacuum chamber 55. A heating medium is supplied to 46a and the downstream heating jacket 46b.

  In the embodiment shown in FIG. 1 described above, the sludge is concentrated by the concentrating device 35 before the sludge is dehydrated by the sludge dewatering device 40. Since the amount of water contained in the sludge is reduced by concentrating the sludge, the amount of sludge heated by the heating dehydrator 41 included in the sludge dewatering device 40 can be reduced. Therefore, the heat energy consumed by the heat dehydrator 41 can be reduced. On the other hand, a sludge drying method that heats sludge as it is using an indirect steam dryer and evaporates moisture in the sludge has been conventionally known. Below, the thermal energy consumed by the sludge drying method using an indirect steam dryer and the thermal energy consumed by heating the sludge not concentrated and the sludge concentrated by the concentrator 35 with the heating dehydrator 41 And compare.

  First, consider unconcentrated sludge. A sludge having a dry matter weight (amount of treated solid matter) of 100 kg-DS / h is assumed. In the case of general sewage digested sludge, the sludge concentration is 2%. In this case, the amount of sludge to be treated is 5000 kg / h. When dewatering 5000 kg / h sludge while heating from 20 ° C. to 80 ° C. with the sludge dewatering device 40, the required thermal energy is 943 MJ / h. The amount of heat required to dehydrate while heating 5000 kg / h sludge is about 50% of the amount of heat required to heat the entire amount of 5000 kg / h sludge. It is assumed that the ratio of thermal energy consumed by heat radiation is 50%. The moisture content of the dewatered sludge when the sludge is dehydrated by the heating dehydrator 41 without heating the sludge is 80%, and the water content of the dewatered sludge when the sludge is heated to 80 ° C. and the sludge is dehydrated by the heat dehydrator 41 The rate is 70%. The amount of water that can be reduced by dewatering the sludge while heating is 166.7 kg / h. On the other hand, when the moisture content of 166.7 kg / h is evaporated by an indirect steam dryer, the thermal energy required for drying is 579.5 MJ / h. As the thermal efficiency, 0.65 which is a general value of an indirect steam dryer was used. Comparing these heat energies, less heat energy is consumed when the sludge is dried with an indirect steam dryer. Therefore, it can be seen that the indirect steam dryer is superior from the viewpoint of energy saving.

  When the sludge concentration is concentrated to 6% with the concentrator 35, the amount of sludge to be treated is 1667 kg / h. When the 1667 kg / h sludge is dehydrated while being heated from 20 ° C. to 80 ° C. by the heating dehydrator 41, the necessary heat energy is 314 MJ / h. The amount of heat required to dehydrate while heating 1667 kg / h sludge is about 50% of the amount of heat required to heat the entire amount of 1667 kg / h sludge. The moisture content of the dewatered sludge when the sludge is dehydrated by the heating dehydrator 41 without heating the sludge is 80%, and the water content of the dewatered sludge when the sludge is heated to 80 ° C. and the sludge is dehydrated by the heat dehydrator 41 The rate is 70%. The amount of water that can be reduced by dewatering the sludge while heating is 166.7 kg / h. On the other hand, when the moisture content of 166.7 kg / h is evaporated by an indirect steam dryer, the thermal energy required for drying is 579.5 MJ / h. As the thermal efficiency, 0.65 which is a general value of an indirect steam dryer was used. When these heat energies are compared, less heat energy is consumed when the sludge concentrated to 6% by the concentrating device 35 is dehydrated while being heated by the sludge dewatering device 40. Therefore, it can be seen that, from the viewpoint of energy saving, it is more advantageous to dehydrate sludge concentrated to 6% by the concentrator 35 while heating with the heating dehydrator 41.

  When the sludge concentration is concentrated to 8% by the concentrator 35, the amount of sludge to be treated is 1250 kg / h. When dewatering 1250 kg / h of sludge while heating from 20 ° C. to 80 ° C. with the heating dehydrator 41, the required thermal energy is 236 MJ / h. The amount of heat required to dehydrate while heating 1250 kg / h sludge is about 50% of the amount of heat required to heat the entire amount of 1250 kg / h sludge. The moisture content of the dewatered sludge when the sludge is dehydrated by the heating dehydrator 41 without heating the sludge is 80%, and the water content of the dewatered sludge when the sludge is heated to 80 ° C. and the sludge is dehydrated by the heat dehydrator 41 The rate is 70%. The amount of water that can be reduced by dewatering the sludge while heating is 166.7 kg / h. On the other hand, when the moisture content of 166.7 kg / h is evaporated by an indirect steam dryer, the thermal energy required for drying is 579.5 MJ / h. As the thermal efficiency, 0.65 which is a general value of an indirect steam dryer was used. When these heat energies are compared, less heat energy is consumed when the sludge concentrated to 8% by the concentrator 35 is dehydrated while being heated by the heating dehydrator 41. Therefore, it can be seen that, from the viewpoint of energy saving, it is more advantageous to dehydrate sludge concentrated to 8% by the concentrator 35 while heating with the heating dehydrator 41.

  From the above results, it can be seen that the sludge dehydrated while being heated by the sludge dewatering device 40 is preferably concentrated to 6% or more by the concentrating device 35. A more preferable concentration of the sludge concentrated by the concentrator 35 is 8 to 14%.

  Although the embodiments of the present invention have been described above, the present invention is not limited to the above-described embodiments, and various modifications can be made within the scope of the technical idea described in the claims.

1 Screen casing (filter cylinder)
DESCRIPTION OF SYMBOLS 1A Cylindrical screen 1B Dewatered sludge passage pipe 2 Sludge inlet 3 Screw shaft 3a Supply piping 3b Discharge piping 3c Discharge piping 4 Screw blade 7 Rotating mechanism 10 Bearing 11 Bearing 14 Filtlet receiver 16 Back pressure plate 16a Tapered surface 18 Back pressure plate moving device 17a Supply piping 17b Discharge piping 19 Cutter 20 Screw-type conveyor 21 Dehydrated sludge discharge pipe 21a Upstream portion 21b Reduced portion 21c Downstream portion 22 Dehydrated sludge inlet 23 Screw shaft 24 Screw blade 25 Blocking wall 26 Bearing 27 Rotating mechanism 28 Blocking wall 29 Bearing DESCRIPTION OF SYMBOLS 30 Coagulation tank 31 Stirring blade 32 Motor 35 Concentrator 37 Supply pipe 38 Drain pipe 40 Sludge dehydrator 41 Heating dehydrator (screw press type dehydrator)
42 Vacuum chamber 42a Side wall 42c Dehydrated sludge inlet 42d Dehydrated sludge outlet 44 Vacuum source 45 Piping 46 Heating jacket 46a Upstream heating jacket 46b Downstream heating jacket 47 Supply piping 48 Discharge piping 49 Condensing device 50 Ejector 51 Drive water tank 52 Drive pump 55 Vacuum chamber 60 Communication chamber 60a Side wall 60c Dehydrated sludge inlet 60d Dehydrated sludge outlet

Claims (7)

A heating and dehydration process is performed to form dehydrated sludge by dewatering while heating the sludge.
Transferring the dewatered sludge formed in the heating and dehydrating step into a vacuum chamber;
Performing a vacuum evaporation step of evaporating moisture contained in the dewatered sludge in the vacuum chamber under vacuum;
The heating dehydration step and the vacuum evaporation step are performed in a sludge dewatering device ,
The dewatered sludge outlet of the vacuum chamber is sealed with the dewatered sludge discharged from the vacuum chamber .   The sludge dewatering method according to claim 1, wherein the dewatered sludge inlet of the vacuum chamber is sealed by the dewatered sludge transferred to the vacuum chamber. The sludge dewatering method according to claim 1 or 2, wherein the heating and dewatering step is performed by a screw press type dehydrator incorporated in the sludge dewatering device. The sludge dewatering method according to any one of claims 1 to 3 , wherein a sludge concentration step of concentrating sludge is performed before the heating and dehydration step. A heating dehydrator that forms dehydrated sludge by dewatering while heating the sludge;
A vacuum chamber connected to the heating dehydrator and into which the dewatered sludge is transferred;
A vacuum source for forming a vacuum in the vacuum chamber;
A transport device connected to the dewatered sludge outlet of the vacuum chamber ,
2. The sludge dewatering apparatus according to claim 1, wherein the transfer device forms a seal plug that compresses the dewatered sludge discharged from the vacuum chamber and seals the dewatered sludge outlet of the vacuum chamber . 6. The sludge dewatering apparatus according to claim 5 , wherein the heat dehydrator forms a seal plug that compresses the dewatered sludge and seals the dewatered sludge inlet of the vacuum chamber. The heating dehydrator is a screw press type dehydrator,
The screw press type dehydrator includes a dewatered sludge passage pipe connected to a dewatered sludge inlet of the vacuum chamber, a back pressure plate disposed opposite to the dehydrated sludge inlet of the vacuum chamber, and the dehydrated sludge to the back pressure plate. The sludge dewatering device according to claim 6 , further comprising: a screw blade that forms a seal plug in the dewatered sludge passage pipe to be pressed against the dewatered sludge inlet.

Images