JP4350602B2 - Operation method of continuous conduction heat transfer dryer - Google Patents

Description

TECHNICAL FIELD The present invention relates to an apparatus suitable for drying materials such as mud, cake, and powder, especially for drying an object that is difficult to disperse inside the apparatus and easily adheres, such as sludge with high water content. Is related to the operation method of the continuous conduction heat transfer dryer which can be performed satisfactorily.

  In recent years, environmental conservation efforts have become popular, and companies, etc., can reduce waste and prevent spoilage by drying and concentrating general waste such as garbage and food processing residues and sewage sludge. Recycled and disposed of after planning.

  There is one continuous conduction heat transfer dryer 1 'which is one of the devices used for drying such sludge, and this device has a multi-tube heating in the main shell 10' as shown in FIG. 5 (a). A pipe 11 'is provided, and this multi-tubular heating pipe 11' is a device that causes heating steam to flow inside it and rotates it to bring the workpiece H into contact with the multi-tubular heating pipe 11 'to evaporate moisture. Yes (see Patent Document 1). Then, the workpiece H supplied into the main body shell 10 'from the inlet 101' is scraped up by the lifter 117 'and moves to the outlet 102' side as the drying progresses. FIG. As shown in FIG. 5A, the vehicle passes over the weir plate 108 'provided at the outlet 102' and is discharged to the outside via the chute 12 '.

In the continuous conduction heat transfer dryer 1 ', the product moisture content is adjusted mainly by adjusting the residence time of the workpiece H in the main body shell 10'. Adjustments have been made. That is, as the height of the weir plate 108 'increases, the lower limit of the outlet 102' increases, so the hold-up (retention height) increases, and the residence time of the workpiece H in the main body shell 10 'increases. On the contrary, when the height of the weir plate 108 ′ is decreased, the lower limit of the outlet 102 ′ is lowered, so that the hold-up (retention height) is lowered and the main body shell 10 of the workpiece H is reduced. The residence time in ′ decreases and the dryness decreases.
The outlet 102 'is formed at a height of the main body shell 10' in the continuous conduction heat transfer dryer 1 'so that a larger amount of the workpiece H contacts the tube bundle 116' serving as the heat transfer surface. This is because the heat transfer surface can be used more effectively, so that the higher the hold-up (retention height), the more efficient the drying.

In the continuous conduction heat transfer dryer 1 ′ as described above, there is room for improvement in the following points when handling an object to be treated H such as sludge having a high water content.
First, sludge with high moisture tends to adhere to the inside of the apparatus, and when it adheres to the tube bundle 116 'which is a heat transfer surface, the contact surface is not renewed, resulting in a decrease in drying capacity. Moreover, since sludge forms a lump and prevents inflow into tube bundle 116 ', the use efficiency of a heat-transfer surface falls and it causes the fall of drying capability.
In addition, when the workpiece H once adhered to the tube bundle 116 'and peeled off from the tube bundle 116', the hold-up (retention height) near the outlet 102 'increases all at once, and the undried substrate H The processed material H will flow out from the outlet 102 '.
Japanese Patent Application No. 2004-11680

The present invention is made from such a background, and even when the object to be processed such as sludge having a high moisture content is handled, the object to be processed is not discharged without being dried. the development of a method for operating a novel continuous conduction heat transfer dryer is obtained by a technical problem.

That is, in the operation method of the continuous conduction heat transfer dryer according to claim 1 , a multi-tube heating tube is provided in a main body shell provided on the machine frame, and the multi-tube heating tube is heated inside thereof. In a method of operating an apparatus for obtaining a dry product by flowing and rotating a steam and bringing the object to be processed put into the main body shell into contact with a multi-tube heating tube and evaporating the moisture, the operation is performed. method, the control discharge of intermittently by the be activated Rikomu treated a discharge device provided in outlet formed in the body shell, thereby, retention in the body shell of the object In order to obtain a desired dry state by adjusting the time, when the discharge device is intermittently started, the temperature of the object to be processed is monitored, and when this temperature exceeds a predetermined value, the discharge device The temperature is The discharge device is put into a non-discharge state when the value becomes a predetermined value or less. At this time, after a certain time has elapsed after the discharge device is put into the discharge state, the discharge device is put into a non-discharge state. It is characterized by this.
According to the present invention, even if sludge or the like adheres to the multi-tube heating tube and is then dried and peeled off, even if the hold-up (retention height) near the take-out rises at a stretch, it is discharged. By setting the apparatus to a non-discharge state, it is possible to prevent the undried workpiece from being discharged. In addition, by intentionally extending the residence time, it is possible to prevent the object to be processed from being discharged as an undried lump, so that a dry product having a small particle size can be obtained.
In addition, by grasping the temperature of the non-processed product corresponding to the predetermined product moisture in advance, it is possible to prevent the processed product from being discharged in an undried state.
Furthermore, it is possible to avoid the discharge of the workpiece that has been detected that the temperature is equal to or lower than the predetermined value, and it is possible to more reliably avoid the discharge of the undried product.

Furthermore, in the operation method of the continuous conduction heat transfer dryer according to claim 2 , a multi-tube heating pipe is provided in a main body shell provided on the machine frame, and the multi-tube heating pipe is provided therein. In a method of operating a device that obtains a dry product by flowing and rotating heated steam, bringing the object to be processed put in the main body shell into contact with the multi-tube heating tube and evaporating the water, and obtaining a dry product, this method is said to control the discharge of intermittently by the be activated Rikomu treated a discharge device provided in outlet formed in the body shell, thereby, in the body shell of the object In order to obtain a desired dry state by adjusting the residence time, when the discharge device is started intermittently, the residence height of the object to be processed in the main body shell is monitored, and this residence height is a predetermined value. When the above becomes the discharge device Thereafter, when the staying height becomes equal to or less than a predetermined value, the discharge device is set to a non-discharge state. At this time, when a certain time has elapsed after the discharge device is set to the discharge state, the discharge device Is characterized in that it is in a non-discharged state .
According to the present invention, even if sludge or the like adheres to the multi-tube heating tube and is then dried and peeled off, the hold-up (retention height) in the vicinity of the outlet may be increased at a stretch. By setting the apparatus to a non-discharge state, it is possible to prevent the undried workpiece from being discharged. In addition, by intentionally extending the residence time, it is possible to prevent the object to be processed from being discharged as an undried lump, so that a dry product having a small particle size can be obtained.
In addition, by grasping the staying height corresponding to a predetermined product moisture in advance, it is possible to prevent the object to be processed from being discharged in an undried state.
Furthermore, it is possible to avoid discharge of the object to be processed in which it has been detected that the staying height is equal to or less than a predetermined value, and it is possible to more reliably avoid discharge of the undried product.
The above problems can be solved by using the configuration of the invention described in each of the claims as a means.

  According to the present invention, even when a processing object such as sludge having a high moisture content is handled, the processing object is not discharged in an undried state, and a good dry product can be obtained.

The best mode of the operation method of the continuous conduction heat transfer dryer of the present invention is as shown in the following examples, but these examples are appropriately modified within the scope of the technical idea of the present invention. It is also possible.

Hereinafter, after first explaining the configuration of the continuous conduction heat transfer dryer 1 to which the present invention is applied, the operation method of the present invention will be described.
The continuous conduction heat transfer dryer 1 is provided as a main component of a direct pressure heat pump type processing apparatus S as shown in FIG. 1 as an example.
The direct pressurization type heat pump type processing apparatus S comprises a continuous conduction heat transfer dryer 1, a charging device 2, a bag filter 3, and a pressurization device 5 as constituent elements. Will be described in detail.
First, the continuous conduction heat transfer dryer 1 will be described. As shown in FIGS. 2 and 3, the continuous conduction heat transfer dryer 1 is provided with a multi-tube heating tube 11 in a main body shell 10 provided on a machine frame F. The multi-tube heating tube 11 is dried by flowing a steam (hereinafter referred to as heating steam) through the multi-tube heating tube 11 and rotating the multi-tube heating tube 11 to contact the outer periphery of the multi-tube heating tube 11. Machine.

As shown in FIG. 3, the main body shell 10 is a hollow member having an elliptical cross section as an example, and has an inlet 101, an outlet 102, a carrier gas port 103, and an exhaust port 104. Here, as shown in FIG. 2, the charging port 101 is formed near the end of the main body shell 10, and an exhaust port 104 is formed near the charging port 101. Further, the second inlet 101 is formed in a portion of the main body shell 10 closer to the center than the exhaust outlet 104. In this embodiment, the inlet 101 is formed in two places with the exhaust outlet 104 in between. I did it. Of course, you may make it form the inlet 101 further in several places along the longitudinal direction of the multi-tube type heating tube 11 mentioned later.
Further, the main body shell 10 and the multi-tube heating tube 11 are installed in the machine frame F so as to be horizontal or inclined so that the inlet 101 side is somewhat higher than the outlet 102 side.
Furthermore, the main body shell 10 has a double jacket structure, and a configuration is adopted in which a steam passage path from the steam supply port 105 to the drain port 106 is formed so that the temperature inside the main body shell 10 can be raised. However, it is also possible to install a trace pipe in place of such a double jacket structure.

The outlet 102 is formed on the side surface of the main body shell 10 near the end opposite to the inlet 101, and a damper 13, which is an example of a discharge device, is provided outside the outlet 102. Provided.
The damper 13 is a device for enabling intermittent discharge of the dried product, and has a mechanism for moving the lid 13a close to and away from the outlet 102 and closing the outlet 102 by the lid 13a. Provided.
Further, a chute 12 is provided outside the outlet 102 and the damper 13, and a rotary valve 122 is provided at a product discharge port 121 formed in the chute 12. Instead of the rotary valve 122, a double damper type discharging device may be provided.

Moreover, as shown in FIG.4 (c), the screw conveyor 14 may be used as the said discharge apparatus, In this case, since the discharge port of the screw conveyor 14 becomes the product discharge port 14a, the said chute | shoot 12 is unnecessary. Become.
Further, when the screw conveyor 14 is used, the outlet 102 can be formed near the bottom of the main body shell 10 as shown in FIG.

The multi-tube heating tube 11 includes end plates 112 on both sides of a tube bundle 116 formed by arranging a plurality of tubes in a cylindrical shape, and includes a shaft body 113 at the center of the end plate 112. The shaft body 113 is rotatably supported by a bearing block 114 provided in the machine frame F. A motor M is provided on the machine frame F as a power source for rotating the multi-tube heating tube 11.
A rotary joint 115 is attached to both ends of the shaft body 113 and connected to the tube bundle 116. In addition, a seal mechanism is provided between the shaft body 113 and the main body shell 10 to block off from the outside air.
The tube bundle 116 has a plurality of angles 111 (12 in this embodiment) to which a plurality of lifters 117 and feeding blades 118 having appropriate angles are attached. The workpiece H is scraped up and comes into contact with each tube of the tube bundle 116 and advances from the inlet 101 side to the outlet 102 side.

Next, the charging device 2 will be described. As an example, a monopump having a hopper 20 is applied to this charging device 2, and its discharge port is connected to the charging port 101 in the continuous conduction heat transfer dryer 1 with an appropriate pipe. Connected by road.
The hopper 20 has a structure capable of vacuum degassing, and prevents air from entering the main body shell 10 in the continuous conduction heat transfer dryer 1.

  Next, the bag filter 3 will be described. In this embodiment, a shaking type bag filter is adopted as an example, and is connected to the exhaust port 104 in the main body shell 10. The filter element 30 can be vibrated by an appropriate swing mechanism to remove clogged dust and the like. In addition, various types such as a backwash type can be used as the bag filter 3.

Next, the pressurizing device 5 will be described. The pressurizing device 5 is configured by providing various devices in the main pipe line 50 connecting the exhaust part of the bag filter 3 and the rotary joint 115 in the multi-tube heating pipe 11. The compressor 51 is provided.
As the compressor 51, a Roots blower or another structure is adopted, and this compressor can be provided in a plurality of stages of two or more stages according to specifications. That is, in the direct pressurization type heat pump type processing apparatus S, the size of the apparatus is almost inversely proportional to the temperature difference between the heated steam S1 and the workpiece H. Therefore, when the compressor is provided in a plurality of stages, On the other hand, when the compressor is provided alone, the initial cost can be reduced.

  Further, the exhaust side of the compressor 51 in the main pipeline 50 is configured to supply cooling water as an example, and a cooling water pipeline 53 is connected to the main pipeline 50. The cooling water pipe 53 is provided with a valve V1 so that the amount of cooling water supplied from an appropriate water supply source can be adjusted.

  Although not shown, the direct pressure heat pump type processing apparatus S is provided with a steam generator, and appropriate apparatuses such as a U-shape, a straight pipe shape, and a helical coil shape are applied. A pipe line is connected from the steam generator to the rotary joint 115, the carrier gas port 103 and the steam supply port 105 in the continuous conduction heat transfer dryer 1.

The continuous conduction heat transfer dryer 1 to which the present invention is applied and the direct pressure heat pump type processing apparatus S to which the apparatus is applied are configured as described above as an example. The operation method of the present invention will be described together with embodiments.
(1) Preparation of dryer Prior to the introduction of the workpiece H, the multi-tube heating tube 11 and the main body shell 10 in the continuous conduction heat transfer dryer 1 are heated, and the motor M is turned on. Auxiliary steam (0.5 MPa (about 160 ° C. as an example)) is supplied to the rotary joint 115, the carrier gas port 103, and the steam supply port 105 with the multi-tube heating tube 11 rotated. The auxiliary steam supplied to the rotary joint 115 raises the temperature of the multi-tube heating pipe 11 while passing through the tube bundle 116, and eventually becomes a drain D and is discharged to the outside from the rotary joint 115 on the other end side. Further, the auxiliary steam supplied to the steam supply port 105 raises the temperature of the main body shell 10 and eventually becomes a drain D and is discharged from the drain port 106 to the outside.

(2) Deaeration process Next, the to-be-processed object H (organic sludge as an example) supplied to the hopper 20 in the injection apparatus 2 is deaerated.

(3) Drying of the object to be processed Next, the object to be processed H is input from the input device 2 to the input port 101, which is moved from the input port 101 side to the outlet 102 side by the action of the feed blade 118, Further, it is scraped up by the lifter 117 and comes into contact with the tube bundle 116 or the like. At this time, it receives heat and the drying proceeds. At this time, since the inlets 101 are formed at a plurality of locations along the longitudinal direction of the multi-tube heating tube 11, the heat conduction surface of the multi-tube heating tube 11 as a condenser can be used effectively, and drying is performed. Efficiency is increased.
And as shown to Fig.4 (a), the to-be-processed object H will be in the state raised in the rotation direction by the effect | action of the multi-tubular heating tube 11, and the temperature of the to-be-processed object H in the vicinity of the outlet 102 is shown. Alternatively, either one or both of the hold-up (residence height) is monitored by an appropriate sensor.

(4) Vapor Exhaust Vapor S0 generated from the organic sludge as a result of such a series of drying processes is exhausted from the exhaust port 104 to the outside of the main body shell 10, and the exhaust port 104 is connected to the main body shell 10. Since it is formed in the vicinity of the inlet 101 with the largest amount of steam S0, the steam S0 with a small content of fine powder generated when the organic sludge is dried can be exhausted.
Furthermore, since a small amount of fine powder contained in the steam S0 discharged from the exhaust port 104 is separated from the steam S0 in the bag filter 3, only the steam S0 can be supplied to the pressurizing device 5. When the clogging of the bag filter 3 has progressed, the shaking mechanism is operated as appropriate to remove the fine powder, and the fine powder can be removed without using backwash air. 3 increase in pressure loss can be avoided.

(5) Generation of heated steam The steam S0 (temperature 60 to 100 ° C., pressure 20 to 101 kPa-abs) that reaches the compressor 51 through the main pipe 50 is compressed and heated (temperature 80 to 120). C., pressure 47 to 199 kPa-abs) and heated steam S1 is supplied to the rotary joint 115.
At this time, when the heating degree of the heating steam S1 is too high, the valve V1 is opened as appropriate to supply cooling water from the cooling water pipe 53 to the main pipe 50, and the heating degree of the heating steam S1 discharged from the compressor 51. Can be controlled to prevent heat exchange in a gaseous state (superheated steam) with a small heat conduction coefficient, and to conduct condensation heat conduction with a large heat conduction coefficient by saturated steam.
The auxiliary steam supplied to the rotary joint 115 is additionally added as appropriate according to the moisture concentration of the workpiece H, the input amount, the amount and temperature of the heating steam S1.

(6) Discharge of the dried product And, when the temperature of the workpiece H near the outlet 102 becomes a predetermined value or more, the discharge device is put into a discharge state, as shown in FIG. The lid 13 a of the damper 13 is separated from the outlet 102 to be in a discharged state, and the dried product is discharged from the outlet 102. When the screw conveyor 14 is used as the discharging device, the screw is rotated in the discharging direction.
Thereafter, when the temperature of the workpiece H in the vicinity of the outlet 102 becomes equal to or lower than a predetermined value, the discharging device is brought into a non-discharge state, and the outlet 102 is blocked by the lid 13a of the damper 13. The non-discharge state is set, and the outflow of the workpiece H from the outlet 102 is stopped. When the screw conveyor 14 is used as the discharging device, the screw is stopped or reversed.
In performing such an operation, it is possible to prevent the workpiece H from being discharged in an undried state by grasping the temperature of the workpiece H corresponding to a predetermined product moisture in advance. It can be done.
In addition, after the discharge device is set in the discharge state, the non-discharge state after a predetermined time has elapsed, and thus the workpiece H whose temperature is detected to be lower than a predetermined value is discharged. Can be avoided, and the discharge of the undried product can be avoided more reliably.
As described above, the discharge of the workpiece H is controlled by intermittently starting the discharge device. As a result, the hold-up (retention height) and retention of the workpiece H in the main body shell 10 are controlled. It is possible to obtain a desired dry state by adjusting the time. Further, when the discharge device is in a non-discharge state, the hold-up (retention height) is increased, the moisture in the main body shell 10 is lowered, the dispersibility of the workpiece H is improved, and the drying is performed satisfactorily. .

(6 ′) Discharge of the dried product In order to intermittently start the discharge device, the discharge device is set to the discharge state when the retention height of the workpiece H near the outlet 102 becomes a predetermined value or more. On the other hand, the discharge device may be put into a non-discharge state when the staying height becomes a predetermined value or less. In this case, it is possible to prevent the workpiece H from being discharged in an undried state by grasping the staying height corresponding to the predetermined product moisture in advance.

It is a block diagram which shows the direct pressurization type heat pump type processing apparatus to which the continuous conduction heat transfer dryer which is the application object of this invention is applied . It is a side view which shows a continuous conduction heat transfer dryer which is an application object of the present invention, partially broken. It is the front view and rear view which show a partial see-through | perspective view and show the continuous conduction heat-transfer dryer which is the application object of this invention. It is a cross-sectional view showing the vicinity of the outlet in the main body shell. It is the side view and cross-sectional view which show the existing continuous conduction heat transfer dryer.

Explanation of symbols

DESCRIPTION OF SYMBOLS S Direct pressurization type heat pump type processing apparatus 1 Continuous conduction heat transfer dryer 10 Main body shell 101 Input port 102 Outlet 103 Carrier gas port 104 Exhaust port 105 Steam supply port 106 Drain port 11 Multi-tube heating tube 111 Angle 112 End plate 113 Shaft body 114 Bearing block 115 Rotary joint 116 Tube bundle 117 Lifter 118 Feed vane 12 Chute 121 Product discharge port 122 Rotary valve 13 Damper 13a Lid 14 Screw conveyor 14a Product discharge port 2 Loading device 20 Hopper 3 Bag filter 30 Filter element 5 Addition Pressure device 50 Main pipeline 51 Compressor D Drain F Machine frame H Processed object M Motor S0 Steam S1 Heated steam V1 Valve

Claims (2)

A multi-tube heating tube is provided in a main body shell provided on the machine frame, and the multi-tube heating tube is rotated while flowing a heating steam therein, and the object to be processed put in the main body shell In a device for obtaining a dry product by contacting a multi-tube heating tube and evaporating the water to obtain a dry product, the method comprising: a discharge device provided at an outlet formed in the main body shell the controlled discharge of Rikomu treated by the bringing intermittently activated, thereby, is intended to obtain the desired dry by adjusting the residence time in the body shell of the object, the discharge device When intermittently starting up, the temperature of the object to be processed is monitored, and when the temperature exceeds a predetermined value, the discharge device is put into a discharge state, and then the temperature becomes a predetermined value or less. In addition, the discharge device should , And the this time, after the discharge device and the discharge state, when a predetermined time has elapsed, the method operating a continuous conduction heat transfer drier, characterized in that the discharge device and the non-discharge state. A multi-tube heating tube is provided in a main body shell provided on the machine frame, and the multi-tube heating tube is rotated while flowing a heating steam therein, and the object to be processed put in the main body shell In a device for obtaining a dry product by contacting a multi-tube heating tube and evaporating the water to obtain a dry product, the method comprising: a discharge device provided at an outlet formed in the main body shell the controlled discharge of Rikomu treated by the bringing intermittently activated, thereby, is intended to obtain the desired dry by adjusting the residence time in the body shell of the object, the discharge device Is intermittently started, the staying height of the object to be processed in the main body shell is monitored, and when the staying height becomes a predetermined value or more, the discharge device is put into a discharge state, and then the staying height is When the value falls below the specified value, The is intended to be non-discharged state, this time, after the discharge device and the discharge state, when a predetermined time has elapsed, a continuous conduction heat transfer drier, characterized in that the discharge device and the non-discharge state Driving method.

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