KR101665973B1 - Apparatus for drying sludges - Google Patents
Apparatus for drying sludges Download PDFInfo
- Publication number
- KR101665973B1 KR101665973B1 KR1020160025479A KR20160025479A KR101665973B1 KR 101665973 B1 KR101665973 B1 KR 101665973B1 KR 1020160025479 A KR1020160025479 A KR 1020160025479A KR 20160025479 A KR20160025479 A KR 20160025479A KR 101665973 B1 KR101665973 B1 KR 101665973B1
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- KR
- South Korea
- Prior art keywords
- conveyor belt
- sludge
- air
- horizontal conveying
- housing
- Prior art date
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
- C02F11/121—Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering
- C02F11/123—Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering using belt or band filters
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B17/00—Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement
- F26B17/02—Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement with movement performed by belts carrying the materials; with movement performed by belts or elements attached to endless belts or chains propelling the materials over stationary surfaces
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B21/00—Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B21/00—Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
- F26B21/004—Nozzle assemblies; Air knives; Air distributors; Blow boxes
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B25/00—Details of general application not covered by group F26B21/00 or F26B23/00
- F26B25/04—Agitating, stirring, or scraping devices
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B2200/00—Drying processes and machines for solid materials characterised by the specific requirements of the drying good
- F26B2200/18—Sludges, e.g. sewage, waste, industrial processes, cooling towers
Abstract
The drying apparatus of the present invention comprises: a housing having a sludge inlet and an air outlet formed at an upper end thereof and a sludge outlet and an air inlet formed at a lower end thereof; A blower disposed in the housing to allow air to flow from the air inlet to the air outlet; And a first conveyor belt and a second conveyor belt, wherein the first and second conveyor belts are configured such that sludge flowing from the sludge inlet is loaded and discharged to the sludge outlet and discharged from the air, Each having a plurality of horizontal transport sections extending horizontally perpendicular to the flow of air and arranged in parallel to one another in multiple stages from the top of the housing to the bottom.
Description
BACKGROUND OF THE
In the process of treating wastewater and wastewater, the sludge mixed with the solid phase and the liquid phase remains after the sedimentation process for separating the solid matter contained in the wastewater. These sludges have been buried in soil or treated by dumping them in the ocean. However, in recent years, pollution of the oceans and soil has become a problem, and landfilling of sludge or marine dumping is gradually being prohibited.
Therefore, the sludge must be incinerated or reformed to be composted. However, the incineration of the sludge containing a large amount of water consumes a considerable amount of fuel, and even when the reforming treatment is performed, a considerable amount of modifying agent is administered. It is necessary to minimize the amount of water contained in the sludge before the incineration or the reforming treatment in order to lower the cost by increasing the efficiency of composting by the sludge.
In order to reduce the moisture content of the sludge, the sludge produced in the precipitation process is dewatered to concentrate the sludge. However, since the concentrated sludge after dewatering also has a high water content for the purpose of incineration or reforming for composting, Modifiers are consumed.
By drying the concentrated sludge through dehydration treatment, the water content can be drastically reduced to lower the cost of incineration of the sludge or the cost of the reforming treatment for composting, as well as to lower the transportation cost by reducing the weight of the sludge.
Drying of such sludge has been proposed or proposed for drying by hot air, direct heating by a heater, drying by a microwave, and drying by contact with a high-temperature hot plate.
Hot air drying uses an infrared heater or the like as a heat source, heating the air, and passing the heated air through the sludge. In the hot air drying method, since the sludge is not heated directly, there is no danger of fire due to local heating, and there is no danger of fire, and the hot, high temperature air flows into the sludge and the moisture of the sludge is quickly transferred to the air.
A technique of using microwave drying and heating by a heater is disclosed in Patent Document 1033678 (Document 1).
The sludge rapid drying apparatus of
In the rapid drier of
Japanese Laid-Open Patent Application No. 1574596 (Document 2) discloses a drying device for heating and drying sludge by a hot plate. In the drying device of Document 2, an electric plate for heating sludge is arranged vertically, And the sludge is dropped by the lower drying plate. The sludge is conveyed in the electric plate by the screw, and is heated and dried.
Such conventional drying apparatuses use a direct heating method using hot air, microwaves, a heating plate, a heating lamp or the like as means for heating the sludge. Any heating means generates heat that can evaporate moisture from the sludge, Is common in that it transfers heat to the sludge, that is, it provides the heat of evaporation necessary for the water to evaporate in the sludge.
Therefore, such a drying apparatus of the prior art tries to reduce the consumption of energy and resources required for the incineration or modification treatment of the concentrated sludge by drying the precipitated and dehydrated sludge, but rather consumes a considerable amount of energy for drying the sludge, It is impossible to expect an improvement in the efficiency of energy use in sludge treatment or an effect of improving the efficiency by drying is insignificant.
In consideration of the problems of the above-described conventional sludge drying apparatus, the present invention provides a sludge drying apparatus that uses a small amount of energy for drying concentrated sludge after sedimentation and dehydration, but also has a low moisture content suitable for incineration or reforming treatment And to provide a drying device that can provide the desired results.
In connection with this problem, the inventors of the present invention have considered using the principle of natural drying in the drying of the slurry.
Moisture drying is optimal for low humidity, high temperature, and sufficient air movement. The prior art only contemplates only increasing the temperature of the sludge by means of a microwave or a heating lamp considering only the condition of 'high temperature' among these three conditions.
The inventor of the present invention has considered a construction in which the sludge is dried by applying sufficient air flow around the sludge as in natural drying without applying high temperature heat to the sludge.
However, drying of the slurry under natural drying conditions can take a considerable time and requires a very large area of drying equipment which can spread the sludge widely to increase the contact area between the sludge and the air.
Therefore, the inventor of the present invention intends to provide a drying apparatus capable of providing a sufficient air flow to the sludge, while allowing the sludge to contact with air in a large area with a small occupied space.
The above-described object of the present invention is achieved by a drying apparatus for sludge according to the present invention,
A housing having a sludge inlet and an air outlet formed at an upper end thereof and a sludge outlet and an air inlet formed at a lower end thereof; A blower disposed in the housing to allow air to flow from the air inlet to the air outlet; And first and second conveyor belts configured such that the sludge introduced from the sludge inlet is loaded and discharged to the sludge outlet and is formed of a material through which air is permeated,
The first conveyor belt and the second conveyor belt each have a plurality of horizontal conveyance sections extending horizontally perpendicularly to the flow of air and arranged in parallel to each other in multiple stages from the top to the bottom of the housing,
The horizontal conveyance section of the first conveyor belt and the horizontal conveyance section of the second conveyor belt are alternately arranged so that the sludge falling at the end of one horizontal conveyance section of the first conveyor belt is conveyed to the horizontal conveyance section And the sludge falling at the end of one horizontal conveying section of the second conveyor belt is conveyed in the horizontal conveying section of the first conveyor belt under the first conveying belt, Conveyed in a horizontal conveying section of the conveyor belt,
The sludge is introduced from the sludge inlet into the uppermost horizontal conveying section of the horizontal conveying section of the first conveyor belt and the second conveyor belt, falls to the sludge outlet at the end of the lowermost conveying section, And dried by air passing through the first conveyor belt and the second conveyor belt during conveyance on the conveyor belt.
In the sludge drying apparatus of the present invention, air flows in from the air inlet at the lower end to the air outlet at the upper end, thereby forming a vertical air flow from the lower end to the upper end of the housing.
In the housing, two conveyor belts carry the slurry, and the conveyor belts are made of air-permeable material having a horizontal horizontal conveying section orthogonal to the vertical air flow, so that the conveyor belts are conveyed on a conveyor belt The sludge is dried by the air flowing upward from the lower side of the conveyor belt.
The horizontal conveying sections of the conveyor belt are arranged such that the horizontal conveying section of the first conveyor belt and the horizontal conveying section of the second conveyor belt are alternately stacked so that the sludge conveyed in one horizontal conveying section falls down And the drying is carried out while being loaded on the horizontal conveying sections in a sequential manner so as to be conveyed to other horizontal conveying sections arranged in the horizontal conveying sections.
Accordingly, in the drying apparatus of the present invention, the sludge can be dried while being moved along a long path including horizontal conveying sections of the conveyor belt while being exposed to the flow of air, and the drying apparatus forms a long path for drying the sludge It is configured to occupy only a narrow area.
delete
The first conveyor belt and the second conveyor belt are wound around a plurality of large-diameter pulleys and large-diameter pulleys disposed in the upper and lower positions, respectively, and a plurality of small- Diameter pulley and a small-diameter pulley so as to form the horizontal conveying section at a portion which is advanced from the large-diameter pulley to the small-diameter pulley,
The small diameter pulleys of the first conveyor belt are each horizontally adjacent to the large diameter pulley of the second conveyor belt and the small diameter pulleys of the second conveyor belt are each horizontally adjacent to the large diameter pulley of the first conveyor belt So that the horizontal conveying sections of the first conveyor belt and the second conveyor belt are arranged alternately up and down.
According to this configuration, two conveyor belts are arranged in one drying apparatus, but these conveyor belts are arranged in parallel with each other and are arranged to cross each other in the same space without occupying each space, It is transferred sequentially in the receiving mode.
Thus, the drying apparatus occupies a small area and a small space, and can form a long conveyance path for drying the sludge.
As one embodiment of the present invention, in the drying apparatus of the present invention, at least one horizontal conveying section of the horizontal conveying sections of the first conveyor belt and the second conveyor belt is conveyed to the first conveyor belt or the second conveyor belt, A stirrer can be installed.
The agitator includes a panel disposed in a direction perpendicular to the moving direction of the first conveyor belt or the second conveyor belt, and a panel extending and protruding in a direction perpendicular to the longitudinal direction of the panel and being loaded on the first conveyor belt or the second conveyor belt, And a plurality of projections contacting the sludge.
According to the structure of the agitator, the sludge conveyed by the conveyor belt collides with the projections of the agitator during transportation, and the agglomerated sludge is crushed or mixed with each other to promote the movement of water in the sludge, The drying of the sludge is promoted.
1 is a front view showing the overall structure of a drying apparatus for a sludge according to an embodiment of the present invention.
2 is a longitudinal sectional view showing the arrangement of a conveyor belt in a drying apparatus of one embodiment of the present invention.
3 is a plan view showing the arrangement of the agitator in the drying apparatus of one embodiment of the present invention.
4 is a cross-sectional view showing the arrangement of the electromagnetic wave generator in the drying apparatus of one embodiment of the present invention.
5 is a plan view and a longitudinal sectional view showing a pulverizer of a sludge in a drying apparatus of one embodiment of the present invention.
Hereinafter, the construction and operation of a drying apparatus for sludge according to one embodiment of the present invention will be described with reference to the accompanying drawings.
FIG. 1 is a view showing the overall structure of the drying apparatus of the present embodiment. In FIG. 1, a part of the
1, a
The upper end of the
The
A
5 (a) is a cross-sectional view of a
The
The sludge to be discharged is loaded on the
In FIG. 2, for the sake of convenience of illustration and explanation, some of the constituent elements necessary for driving the
The drying
Since the
The
The
In this way, the
2, the
The
2, the
On the other hand, the small diameter pulleys 42 of the first conveyor belt are each disposed horizontally adjacent to the
The point at which the
The horizontal conveying sections of the
In addition, the horizontal transfer sections of the first and
3, the
Particularly, the
As shown in FIG. 2, in the present embodiment, two
Referring again to Figure 1, Figure 1 shows the entire arrangement for driving the
A
Above the
A
Similarly, the
Since the
The sludge introduced into the
The loaded sludge is conveyed while passing between the horizontal conveying sections of the
At the lower end of the
According to this configuration, the air introduced from each
This vertical airflow collides with the
In the present embodiment, the
Referring to FIG. 1, three first electromagnetic wave generators 81 are disposed on both sides of the housing, and a second electromagnetic wave generator 82 is disposed on each of the
The first and second electromagnetic wave generators 81 and 82 generate an electromagnetic wave having a frequency of 30 to 50 kHz belonging to a long wave region by applying an alternating current having a frequency of 20,000 V and 30 to 50 kHz.
The first electromagnetic wave generator 81 is formed to extend vertically between the
The electromagnetic waves generated from the electromagnetic wave generators 81 and 82 are loaded on the
Moisture on the surface of the sludge is evaporated by the air flowing around the sludge conveyed by the first and second conveyor belts (40, 50), and moisture on the inside of the sludge moves to the surface as the surface sludge is dried. The movement of such moisture is promoted by the electromagnetic waves applied by the electromagnetic wave generators 81 and 82, and drying of the inside of the sludge is promoted.
On the other hand, in the present embodiment, the electromagnetic wave generated from the electromagnetic wave generator has a frequency of 30 to 50 kHz. If the frequency of the electromagnetic wave is less than 30 kHz, the activation effect of excitation and movement of moisture by electromagnetic waves is lowered, The drying is very slow. When the frequency is higher than 50 kHz, the electromagnetic wave becomes high frequency, and the heating effect of the sludge by the electromagnetic wave becomes high, and the energy consumption becomes excessive.
Also, in this embodiment, the voltage of the current for generating the electromagnetic wave is 20,000 V, and the higher the voltage, the higher the effect of exciting the moisture.
The
The
These electric fields are alternated by alternating currents, so that alternating electric fields excite the air moving in the housing and the moisture contained in the sludge and sludge. By the excitation of air, sludge and moisture, the flow of air and the movement of moisture are activated and promoted, thereby promoting the drying of the sludge.
The embodiments of the present invention have been described above, but the present invention is not limited to these embodiments, and various changes and modifications may be made within the scope of the claims.
10: screw conveyor 20: housing
30: crusher 40: first conveyor belt
50: second conveyor belt 60: stirrer
70: blower 81, 82: electromagnetic wave generator
90: Electromagnet
Claims (6)
A housing having a sludge inlet and an air outlet formed at an upper end thereof and a sludge outlet and an air inlet formed at a lower end thereof; A blower disposed in the housing to allow air to flow from the air inlet to the air outlet; And first and second conveyor belts configured such that the sludge introduced from the sludge inlet is loaded and discharged to the sludge outlet and is formed of a material through which air is permeated,
The first conveyor belt and the second conveyor belt each have a plurality of horizontal conveying sections extending horizontally perpendicularly to the flow of air and arranged in parallel to each other in a multistage manner from the top to the bottom of the housing, Diameter pulleys and large-diameter pulleys, which are wound in a plurality of small-diameter pulleys arranged horizontally opposite to each other and arranged on top of each other, and are alternately wound on large-diameter pulleys and small-diameter pulleys, To form the horizontal transport section,
The small diameter pulleys of the first conveyor belt are each horizontally adjacent to the large diameter pulley of the second conveyor belt and the small diameter pulleys of the second conveyor belt are each horizontally adjacent to the large diameter pulley of the first conveyor belt Whereby the horizontal conveying sections of the first conveyor belt and the second conveyor belt are arranged alternately up and down,
The sludge falling at the end of one horizontal conveying belt of the first conveyor belt is carried and conveyed in the horizontal conveying section of the second conveyor belt lying below the horizontal conveying section of the first conveyor belt, The sludge falling at the end of the horizontal conveying section of the second conveyor belt is loaded and transported in the horizontal conveying section of the first conveyor belt lying below the horizontal conveying section of the second conveyor belt,
The sludge is introduced from the sludge inlet into the uppermost horizontal conveying section of the horizontal conveying section of the first conveyor belt and the second conveyor belt, falls to the sludge outlet at the end of the lowermost conveying section, And is dried by air passing through the first conveyor belt and the second conveyor belt during conveyance on the conveyor belt.
Wherein the first conveyor belt and the second conveyor belt are made of filter cloth.
A stirrer for stirring the sludge to be loaded on the first conveyor belt or the second conveyor belt is installed in at least one horizontal conveying section of the horizontal conveying sections of the first conveyor belt and the second conveyor belt,
The agitator includes a panel disposed in a direction perpendicular to the moving direction of the first conveyor belt or the second conveyor belt, and a panel extending and protruding in a direction perpendicular to the longitudinal direction of the panel and being loaded on the first conveyor belt or the second conveyor belt, And a plurality of projections in contact with the sludge.
Further comprising an electromagnetic wave generator for applying an electromagnetic wave having a frequency of 30 to 50 kHz to the sludge moving along the conveyor belt, wherein movement of moisture in the sludge conveyed by the electromagnetic wave from the electromagnetic wave generator and carried on the conveyor belt The drying device being activated.
Wherein at least one of an inlet and an outlet of the air is provided with an electromagnet to which an alternating current having a frequency of 30 to 50 kHz is applied to form an electric field in the sludge and air circulated in the housing,
Priority Applications (1)
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KR1020160025479A KR101665973B1 (en) | 2016-03-03 | 2016-03-03 | Apparatus for drying sludges |
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KR1020160025479A KR101665973B1 (en) | 2016-03-03 | 2016-03-03 | Apparatus for drying sludges |
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR20190042364A (en) | 2017-10-16 | 2019-04-24 | 한국전기연구원 | Belt type sludge dryer with air fluid control functions |
KR102151062B1 (en) * | 2020-01-23 | 2020-09-02 | 거림환경 주식회사 | Dewatering sludge dryer |
CN112479546A (en) * | 2019-09-12 | 2021-03-12 | 广州新致晟环保科技有限公司 | Sludge drying device and operation method |
Citations (5)
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KR20000005940A (en) * | 1998-06-05 | 2000-01-25 | 오또꿈뿌 오와이제이 | Method for making drying more effective |
KR101033678B1 (en) | 2011-01-05 | 2011-05-12 | (주)제이디이엔지 | Apparatus for electro-penetrative dehydrating and rapid drying sludge |
KR20120136004A (en) * | 2011-06-08 | 2012-12-18 | 강용수 | Apperatus for treatmenting sludge of sewage |
KR20130126167A (en) * | 2012-05-11 | 2013-11-20 | 대구염색산업단지관리공단 | Device for manufacturing slice chips of sludge, apparatus for drying waste water sludge including the same and method thereof |
KR101574596B1 (en) | 2014-10-15 | 2015-12-04 | (주)지우이노베이션 | Apparatus for drying sludge |
-
2016
- 2016-03-03 KR KR1020160025479A patent/KR101665973B1/en active IP Right Grant
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR20000005940A (en) * | 1998-06-05 | 2000-01-25 | 오또꿈뿌 오와이제이 | Method for making drying more effective |
KR101033678B1 (en) | 2011-01-05 | 2011-05-12 | (주)제이디이엔지 | Apparatus for electro-penetrative dehydrating and rapid drying sludge |
KR20120136004A (en) * | 2011-06-08 | 2012-12-18 | 강용수 | Apperatus for treatmenting sludge of sewage |
KR20130126167A (en) * | 2012-05-11 | 2013-11-20 | 대구염색산업단지관리공단 | Device for manufacturing slice chips of sludge, apparatus for drying waste water sludge including the same and method thereof |
KR101574596B1 (en) | 2014-10-15 | 2015-12-04 | (주)지우이노베이션 | Apparatus for drying sludge |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR20190042364A (en) | 2017-10-16 | 2019-04-24 | 한국전기연구원 | Belt type sludge dryer with air fluid control functions |
KR102372159B1 (en) * | 2017-10-16 | 2022-03-07 | 한국전기연구원 | Belt type sludge drying device with matching air flow path for sludge transfer section |
CN112479546A (en) * | 2019-09-12 | 2021-03-12 | 广州新致晟环保科技有限公司 | Sludge drying device and operation method |
KR102151062B1 (en) * | 2020-01-23 | 2020-09-02 | 거림환경 주식회사 | Dewatering sludge dryer |
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