CN211367381U

CN211367381U - Disc dryer

Info

Publication number: CN211367381U
Application number: CN201921873869.1U
Authority: CN
Inventors: 林国鑫; 章华熔; 张天兴; 杨文贞; 陈菲琳
Original assignee: Fujian Longking Co Ltd.
Current assignee: Fujian Longking Co Ltd.
Priority date: 2019-11-01
Filing date: 2019-11-01
Publication date: 2020-08-28
Anticipated expiration: 2029-11-01

Abstract

The utility model discloses a disc dryer, the shell of which comprises a sludge drying area and an electric dedusting area, when sludge is dried in the sludge drying area, evaporated gas enters the electric dedusting area from a gas channel for dedusting, flows out through a gas outlet of the shell and enters a subsequent process; for the sludge treatment system, a cyclone dust collector for dust removal, a spray tower for washing and a matched conveying device are not required to be arranged, namely, the gas outlet of the disc dryer of the utility model can be directly connected with the condensing tower, namely, the gas discharged by the disc dryer can directly enter the condensing process, thereby greatly simplifying the sludge treatment process flow, saving the cost and saving the arrangement space; and the conventional polar line vertical mode is broken through, the polar line is horizontally arranged, so that the method is further suitable for the environmental conditions of small space height above the sludge drying area and long, thin and narrow space of the conventional disc dryer, and the arrangement of the electric dust removal area is realized under the condition that the volume of the conventional disc dryer is not increased.

Description

Disc dryer

Technical Field

The utility model relates to a sludge treatment technical field, in particular to disc dryer.

Background

The disc dryer is a process equipment for sludge reduction treatment. The existing process route for sludge reduction treatment by adopting the equipment is as follows: after wet sludge with the water content of about 80 percent enters a disc dryer through a conveying system for drying treatment, the water content of the wet sludge is reduced to about 30 percent, and then harmless and resource treatment such as incineration and the like are carried out. The dust-containing gas generated in the drying process is dedusted by the cyclone dust collector and washed by the spray tower, then enters the condensing tower to be condensed, condensable gas and water vapor in the waste gas are sucked out, and the non-condensable gas is exhausted after being combusted by the deodorization device or the boiler. The sludge recovered by the cyclone dust collector and the dried sludge are treated together, and the sewage collected by the spray tower and the condensing tower is treated by the sewage treatment device and then recycled or discharged.

As can be seen from the above description, each process equipment has a single function, more equipment is used, and the process flow is longer.

In order to increase the function of a disc dryer in the prior art, a gas collecting hood is sometimes arranged on the dryer, a filter screen with 200 meshes is arranged in the dryer, the diameter of a steel wire is 0.11mm, and the theoretical diameter of the meshes is 0.017 mm. Although the filter screen can filter some granules in the gas, the screen cloth can not filter slight particulate matter, and dust collection efficiency is low, and here gaseous moist screen cloth is changeed the jam, adopts pressure differential to judge artifical manual deashing and is difficult to realize.

In view of this, how to simplify the process flow of the sludge treatment system, and achieve both the improvement of the dust removal efficiency and the space saving is an urgent problem to be solved by those skilled in the art.

SUMMERY OF THE UTILITY MODEL

The utility model aims at providing a disc dryer, under the condition that its occupation space is equal, it can compromise and improve dust collection efficiency, and difficult jam, can simplify sludge treatment system's process flow simultaneously greatly, reduces sludge treatment system's use cost.

In order to solve the technical problem, the utility model provides a disc dryer, which comprises a shell with a cavity; the cavity is provided with a sludge drying area, and the sludge drying area is provided with a drying part for drying sludge; the shell is provided with a feed inlet and a discharge outlet which are communicated with the sludge drying area, the cavity further comprises an electric dedusting area inside, the electric dedusting area is arranged above the sludge drying area, and a gas channel is arranged between the sludge drying area and the electric dedusting area; the shell is provided with a gas outlet communicated with the electric dust removing area; the electric dust removing area is provided with an electrode wire and a dust collecting plate, and the electrode wires are horizontally arranged.

Compared with the prior art, the utility model provides a disc dryer's casing is inside including sludge drying district and electric dust removal district, and mud flows through the sludge drying district and carries out the drying, and mud after the drying is discharged by the discharge gate. When sludge is dried in the sludge drying area, gas evaporated by the sludge enters the electric dedusting area through the gas channel, and in a high-voltage electrostatic field formed by the polar line and the dust collecting plate, when dusty gas passes through the electric field area, the dust is charged, the charged dust is drawn close to the dust collecting plate under the action of electric field force and is collected, and then the gas flows out through the gas outlet of the shell and enters the subsequent process.

Thus, the utility model provides a disc dryer can accomplish the dust removal to the mud evaporates gas, to sludge treatment system, need not to set up cyclone and remove dust, spray column washing and supporting conveying equipment, that is to say, the utility model provides a disc dryer's gas outlet can the lug connection condensing tower, and the disc dryer combustion gas can directly get into condensation process promptly, has simplified sludge treatment process flow greatly, saves the cost and arranges the space.

And, the utility model discloses the polar line level in well electric dust removal district arranges, breaks the vertical mode of conventional polar line promptly here, sets up polar line level, and the sludge drying district top space height who further adapts to current disc dryer like this is little, and the long and thin little ambient condition in space realizes the setting in electric dust removal district under the condition that does not increase current disc dryer volume.

Optionally, the number of the polar lines is at least two, the polar lines are parallel to the length direction of the disc dryer, the plate surface of each dust collecting plate is vertically arranged, and the plate surface is parallel to the polar lines.

Optionally, each of the pole wires is integrally mounted on the same mounting frame, and the mounting frame is suspended in the housing through a support insulator in an insulating manner.

Optionally, the dust collector further comprises a plurality of guide plates for guiding the airflow to one end of the dust collecting plate far away from the gas outlet; the gas channels are formed between adjacent baffles.

Optionally, the feed inlet is arranged at the top of the shell, and the gas outlet is also arranged at the top of the shell and close to one side of the feed inlet; the end part of the electric dust removing area, which is close to the feed inlet, is provided with a partition plate for isolating the feed inlet from the electric dust removing area; and the lower end of the baffle plate extends to the sludge drying area.

Optionally, each dust collecting plate is suspended from the top wall of the housing by a suspension bracket, and at least three suspension points are located between the same dust collecting plate and the housing, and all suspension points are arranged along the length direction; the dust collecting device is characterized by further comprising a limiting plate group fixed on the shell, the limiting plate group comprises two limiting plates arranged in parallel, and the lower end part of the dust collecting plate is limited between the two limiting plates.

Optionally, the limiting plate group further includes supporting members arranged at intervals in the transverse direction, two ends of each supporting member are fixed to the inner wall of the corresponding side of the housing, the limiting plate groups corresponding to the dust collecting plates one to one are arranged on the supporting members, and the predetermined gap is formed between the dust collecting plates and the supporting members.

Optionally, a bin wall vibrator is further installed on the outer wall of the housing, and is used for vibrating the dust collecting plate and the guide plate to remove ash.

Optionally, the drying part includes a hollow shaft rotatably supported on the housing, and a plurality of hollow discs communicated with the hollow shaft are further disposed on the hollow shaft along the axial direction, and a predetermined space is provided between adjacent hollow discs.

Optionally, at least the middle dust collecting plate of each dust collecting plate is provided with a plurality of through holes.

Drawings

Fig. 1 is a schematic structural diagram of a disc dryer according to an embodiment of the present invention;

FIG. 2 is a cross-sectional view A-A of the disc dryer of FIG. 1;

fig. 3 is an enlarged view of fig. 2 at B.

Wherein, the correspondence between the reference numbers and the component names in fig. 1 to 3 is:

1-1 drying zone; 1-2 electric dust removing areas; 3, a shell; 31 a lower shell; 32 an upper shell; 4, a disc; 5 a hollow disc; 6, a mud scraper; 7, a propeller; 9 hanging point; 10, mounting a frame; 11 a flow guide plate; 12 a dust collecting plate; 13, an anode vibrator; 15 limiting plate assembly; 151 support member; 152 a limiting plate; 16 insulators; 18 polar lines; 19 high voltage wire inlet device; 21 a deflector vibrator; 22 a hollow shaft; 23 an air inlet; 24 water outlet; 25 steam-water separator; 28 a speed reduction device; 29 partition plate.

Detailed Description

In order to make those skilled in the art better understand the technical solution of the present invention, the present invention will be further described in detail with reference to the accompanying drawings and specific embodiments.

Referring to fig. 1, 2 and 3, fig. 1 is a schematic structural diagram of a disc dryer according to an embodiment of the present invention; FIG. 2 is a cross-sectional view A-A of the disc dryer of FIG. 1; fig. 3 is an enlarged view of fig. 2 at B.

The utility model provides a disc dryer, it is including the casing 3 that is formed with the cavity, including sludge drying district 1-1 in the cavity, sludge drying district 1-1 is provided with dry part for dry sludge. In a preferred manner, the drying unit of the present invention may include a hollow shaft 22 and hollow discs 5, wherein the hollow discs 5 are spaced apart from each other in the axial direction of the hollow shaft 22, i.e., a predetermined distance is provided between adjacent hollow discs 5. The hollow shaft 22 is rotatably supported by the housing 3, and the hollow shaft 22 may be rotatably supported by the housing 3 via a bearing or the like capable of relative rotation.

The hollow disc 5 is generally a hollow structure formed by two disc sheets 4, and the hollow cavity of the hollow disc 5 is communicated with the inner cavity of the hollow shaft 22. The hollow shaft 22 is provided with a steam inlet 23 and a water outlet 24, pressure steam or other heating media are allowed to enter the hollow disc 5, heat is transferred to wet sludge through the disc surface, the sludge is dried, and condensed water of the hollow disc 5 flows back to the inner cavity of the hollow shaft 22 and is discharged through a steam-water separator 25.

The quill 22 may be provided with stub shafts at both ends, supported by rolling bearings. The hollow shaft 22 may be rotated at a low speed by the reduction gear 28. A mud scraper 6 can be arranged between the hollow discs 5, so that the influence of slime on heat transfer efficiency is avoided. The propeller 7 of the hollow disc 5 stirs to push the sludge to the outlet, the propeller angle is adjusted, the propelling speed of the sludge can be changed, the sludge is dried in the propelling process, the expected moisture content is achieved, and continuous operation is achieved.

Of course, the above description is only a description of one preferred embodiment of the drying means, and the arrangement of the drying means is not limited to the above description, and other structures are also possible. Other configurations of the drying section are not described in detail herein with reference to the prior art.

For the inlet and discharge of sludge, the housing 3 of the disc dryer is necessarily provided with a feed inlet and a discharge outlet which are communicated with the sludge drying zone 1-1. The structure and shape of the feed inlet and the discharge outlet are not limited herein.

The utility model provides a 3 inside still further including electric dust removal district 1-2 of casing of disc dryer's cavity, electric dust removal district 1-2 is in the top of sludge drying district 1-1 to be provided with gas passage between sludge drying district 1-1 and the electric dust removal district 1-2, like this sludge drying district 1-1 when carrying out sludge drying, gas such as vapor that is evaporated out in the mud can get into electric dust removal district 1-2 from gas passage.

Meanwhile, the shell 3 is provided with a gas outlet communicated with the electric dust removing area 1-2, and gas can flow to the outside of the disc dryer from the gas outlet after passing through the electric dust removing area 1-2 and is directly discharged or enters a downstream process flow.

The electric dust removing area 1-2 is provided with a polar line 18 and a dust collecting plate 12, and in normal work, the polar line 18 is connected with the negative pole of a power supply through a high-voltage wire inlet device 19 to form a cathode line 18; the dust collecting plate 12 is connected to the positive electrode of the power supply to become an anode plate.

The dust collection plates 12 are generally parallel to each other, and a plurality of parallel pole lines 18 are disposed between adjacent dust collection plates 12. The anode plate can be formed by a metal flat plate or a metal flat plate with a rigid crease.

The utility model provides an extreme line 18 level sets up, that is to say, the utility model provides an extreme line 18 is on a parallel with the horizontal plane. The technical solution is described herein by taking the disc dryer horizontally placed with the axis of the hollow shaft 22 horizontally disposed as an example. I.e. the plane in which the pole line 18 lies is parallel to the axis of the quill 22.

Compared with the prior art, the utility model provides a disc dryer's 3 insides include sludge drying district 1-1 and electric dust removal district 1-2, and mud flows through sludge drying district 1-1 and dries, and the mud after the drying is discharged by the discharge gate. When sludge is dried in the sludge drying area 1-1, gas evaporated from the sludge enters the electric dust removing area 1-2 through a gas channel, in a high-voltage electrostatic field formed by the polar line 18 and the dust collecting plate 12, when dust-containing gas passes through the electric field area, dust is charged, the charged dust is drawn to the dust collecting plate 12 under the action of electric field force and is collected, and then the gas flows out through a gas outlet of the shell 3 and enters a subsequent process.

And, the utility model discloses the polar line 18 horizontal arrangement in well electric dust removal district 1-2, this text breaks the vertical mode of conventional polar line 18 promptly, with the setting of polar line 18 level, further adapts to the sludge drying district 1-1 top space height of current disc dryer like this little, the long and thin narrow little ambient condition in space, under the condition that does not increase current disc dryer volume, realizes the setting in electric dust removal district 1-2.

In a specific embodiment, the number of the polar lines 18 is at least two, each polar line 18 is parallel to the length direction of the disc dryer, i.e. the axial direction of the hollow shaft 22, i.e. the polar lines 18 are arranged parallel to the hollow shaft 22. The plate surface of each dust collecting plate 12 is arranged vertically and the plate surface is parallel to the pole line 18.

In the above embodiment, the pole wire 18 can be a long pole wire, and of course, the pole wire 18 can be divided into multiple segments along the axial direction. The electric dust removing area 1-2 may be formed by one electric field or may be formed by a plurality of electric fields.

In the above embodiments, the pole wires 18 are integrally mounted on the same mounting block 10, and the mounting block 10 is suspended in the housing 3 through the supporting insulator 16. The connection of the support insulator 16 to the housing 3 is not described and reference is made to the prior art.

The pole wires 18 are mounted to the same mounting block 10, which facilitates the mounting of the pole wires 18.

The disc dryer in the above embodiments may further include a plurality of guide plates 11 for guiding the airflow to the end of the dust collecting plate 12 away from the gas outlet; therefore, the gas from the sludge drying area 1-1 flows to the electric field far away from one end of the gas outlet along the guide plate 11, and reaches the gas outlet after flowing through a far path in the electric field, so that the dust removal effect is further improved. And a gas channel is formed between the adjacent guide plates 11, and the uniform arrangement of gas can be realized by controlling the shapes and the intervals between the guide plates 11.

In a specific embodiment, the feeding hole is arranged at the top of the shell 3, and the gas outlet is also arranged at the top of the shell 3 and close to one side of the feeding hole; the end part of the electric dust removing area 1-2 close to the feeding hole is provided with a clapboard 29 for separating the feeding hole from the electric dust removing area 1-2; the lower end of the partition 29 extends to the sludge drying zone 1-1. The partition 29 is vertically disposed at the left side of the electric dust removing area 1-2 as shown in the drawing.

The partition plate 29 can isolate the wet sludge from the electric dust removing area 1-2 on one hand, prevent the wet sludge from contacting with the polar line 18 and the dust collecting plate 12 of the electric dust removing area 1-2 and ensure the normal operation of each component in the electric dust removing area 1-2; in addition, wet sludge can flow to the sludge drying area 1-1 along the partition plate to play a role in guiding flow.

Each dust collecting plate 12 is suspended on the top wall of the shell 3 through a suspension bracket, and the suspension points 9 between the two are at least three; that is, there are at least three suspension points 9 between the same dust collecting plate 12 and the housing 3, and all the suspension points are arranged along the length direction.

The disc dryer also comprises a limiting plate group fixed on the shell 3, the limiting plate group comprises two limiting plates arranged in parallel, and the lower end part of the dust collecting plate 12 is limited between the two limiting plates. The number of the limiting plate assemblies 15 may be one or two or more.

In the embodiment, the position of the dust collection plate 12 is limited by the upper suspension points 6 and the lower limit, so that the dust collection plate 12 is reliably mounted.

Specifically, the set of limiting plates may include supporting members 151 arranged laterally at intervals, both ends of the supporting members 151 are fixed to the inner walls of the respective sides of the housing 3, the supporting members 151 are provided with the set of limiting plates corresponding to the dust collecting plates 12 one by one, and the predetermined gap is provided between the dust collecting plates 12 and the supporting members 151. The dust collecting plate 12 and the supporting member 151 have a predetermined gap therebetween to satisfy the requirement of expansion and contraction of the dust collecting plate 12.

In the above embodiments, the outer wall of the housing 3 is further provided with a bin wall vibrator for vibrating the dust collecting plate 12 and the flow guide plate 11 to clean ash. Specifically, the bin wall vibrator can be set to a timing vibration dust cleaning mode, so that the dust collecting plate 12 and the guide plate 11 are kept clean, and dust accumulation is avoided. The bin wall vibrator comprises an anode vibrator 13 and a guide plate vibrator 21 which respectively vibrate the dust collecting plate 12 and the guide plate 11 to remove ash.

The width of the housing 3 is usually more than two meters, the number of the flue gas dust removal channels formed by the dust collecting plates 12 is usually several, and the figure shows the specific embodiment that four integrated plates are arranged to form three flue gas dust removal channels. The remaining flue gas dust removal passages may not be aligned with the flue gas outlets, except for the middle passage which is aligned with the housing 3 gas outlets. Therefore, for the normal discharge of the flue gas in the electric dust removing area 1-2, the following arrangement is also provided.

In consideration of installation and maintenance, the housing 3 may further include an upper housing 32 and a lower housing 31, and the upper housing 32 and the lower housing 31 enclose a cavity.

In the above embodiments, at least the middle dust collecting plate of the dust collecting plates is provided with a plurality of through holes. Therefore, the gas in each channel can flow to different channels formed by the dust collecting plates, so that dead zones are avoided, all the dust collecting plates can participate in dust collection, and the dust collection efficiency is improved. And the through holes on the dust collecting plate have the function of uniformly distributing air flow, so that the system resistance is reduced, and the dust removal efficiency is further improved.

The above is to the utility model provides a disc dryer introduces in detail. The principles and embodiments of the present invention have been explained herein using specific examples, and the above descriptions of the embodiments are only used to help understand the method and its core ideas of the present invention. It should be noted that, for those skilled in the art, without departing from the principle of the present invention, the present invention can be further modified and modified, and such modifications and modifications also fall within the protection scope of the appended claims.

Claims

1. A disc dryer comprises a housing (3) formed with a cavity; the cavity is provided with a sludge drying area (1-1), and the sludge drying area (1-1) is provided with a drying component for drying sludge; the shell (3) is provided with a feeding hole and a discharging hole which are communicated with the sludge drying area (1-1), and is characterized in that the cavity further comprises an electric dedusting area (1-2), the electric dedusting area (1-2) is arranged above the sludge drying area (1-1), and a gas channel is arranged between the sludge drying area (1-1) and the electric dedusting area (1-2); the shell (3) is provided with a gas outlet communicated with the electric dedusting area (1-2); the electric dusting area (1-2) is provided with pole wires (18) and a dust collecting plate (12), and each of the pole wires (18) is arranged horizontally.

2. Disc dryer according to claim 1, characterized in that the number of pole lines (18) is at least two, that the pole lines (18) are parallel to the length direction of the disc dryer, that the plate surfaces of the dust collecting plates (12) are arranged vertically and that the plate surfaces are parallel to the pole lines (18).

3. Disc dryer according to claim 2, characterized in that the pole wires (18) are mounted integrally on the same mounting block (10), the mounting block (10) being suspended insulated from the housing (3) by means of support insulators (16).

4. A disc dryer according to claim 2, further comprising a plurality of flow deflectors (11) for directing a flow of air to the end of the dust collection plate (12) remote from the gas outlet; the gas channels are formed between adjacent baffles (11).

5. Disc dryer according to claim 4, characterized in that the inlet opening is arranged at the top of the housing (3), and the gas outlet is also open at the top of the housing (3) and close to the inlet opening side; a partition plate is arranged at the end part, close to the feeding hole, of the electric dust removing area (1-2) and used for isolating the feeding hole from the electric dust removing area (1-2); and the lower end of the baffle plate extends to the sludge drying area (1-1).

6. The disc dryer according to claim 4, characterized in that each dust collecting plate (12) is suspended from the top wall of the housing (3) by suspension brackets, and that there are at least three suspension points between the same dust collecting plate (12) and the housing (3), all suspension points being arranged in the length direction; the dust collecting device is characterized by further comprising a limiting plate group fixed on the shell (3), wherein the limiting plate group (15) comprises two limiting plates (152) arranged in parallel, and the lower end part of the dust collecting plate (12) is limited between the two limiting plates (152).

7. The disc dryer according to claim 6, wherein the set of position-limiting plates (15) further comprises supporting members (151) arranged laterally at intervals, both ends of the supporting members (151) are fixed to the inner walls of the respective sides of the housing (3), the supporting members (151) are provided with the set of position-limiting plates corresponding to the dust-collecting plates (12) one by one, and a predetermined gap is provided between the dust-collecting plates (12) and the supporting members (151).

8. The disc dryer according to claim 4, characterized in that the outer wall of the housing (3) is further provided with a bin wall vibrator for vibrating and cleaning the dust collecting plate (12) and the flow guide plate (11).

9. Disc dryer according to claim 1, characterized in that said drying means comprise a hollow shaft rotatably supported on said casing (3), said hollow shaft being further provided with a plurality of hollow discs (5) communicating with said hollow shaft in an axial direction, adjacent hollow discs (5) having a predetermined spacing therebetween.

10. The disc dryer according to any of the claims 1 to 9, characterized in that at least the middle dust collecting plate (12) of the dust collecting plates (12) is provided with a plurality of through holes.