CN210287125U - Sludge dewatering system - Google Patents

Sludge dewatering system Download PDF

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Publication number
CN210287125U
CN210287125U CN201921219676.4U CN201921219676U CN210287125U CN 210287125 U CN210287125 U CN 210287125U CN 201921219676 U CN201921219676 U CN 201921219676U CN 210287125 U CN210287125 U CN 210287125U
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China
Prior art keywords
heating chamber
conveying
dewatering system
guide plate
sludge dewatering
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CN201921219676.4U
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Chinese (zh)
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石颂恒
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Shanghai Concrete Leading Construction Technology Co Ltd
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Shanghai Concrete Leading Construction Technology Co Ltd
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Abstract

The utility model relates to a silt dewatering system, it includes the heating chamber and sets up the frame in the heating chamber, the top of heating chamber is provided with feed hopper, the bottom of heating chamber is provided with ejection of compact funnel, from the top down interval is provided with the multilayer transport mechanism with silt from top to bottom transmission in the frame, be provided with a plurality of far infrared heating pipes in the heating chamber, the far infrared heating pipe is located each transport mechanism's top, the surface of heating chamber is provided with graphite alkene layer. The utility model discloses have and add the transfer distance of slurry waste silt in the heating chamber, utilize solar energy and far infrared to get rid of the effect of moisture in the slurry waste silt.

Description

Sludge dewatering system
Technical Field
The utility model belongs to the technical field of waste material, useless thick liquid recycle's technique and specifically relates to a silt dewatering system is related to.
Background
At present, a certain amount of waste slurry is generated in the process of building engineering construction, for example, the waste slurry is poured out from the interior of a pipe pile after the centrifugal process, and the turbid liquid contains cement, sand powder, water and a water reducing agent. The waste slurry is generally directly dumped, and the directly discharged waste slurry causes environmental pollution.
The existing Chinese patent with publication number CN206716714U discloses a concrete mixing plant waste material and waste slurry recycling device, which comprises a slope pool, a sewage pool and a clean water pool which are sequentially arranged, wherein an outlet of the slope pool is connected with one end of a first water guide pipe, the other end of the first water guide pipe is connected with an inlet of the sewage pool, an outlet of the sewage pool is connected with one end of a second water guide pipe, the other end of the second water guide pipe is connected with an inlet of the clean water pool, an outlet of the sewage pool and an outlet of the clean water pool are both connected with one end of a third water guide pipe, the other end of the third water guide pipe is connected with a mixer, the mixer comprises a mixer body, a mixing shaft is rotatably arranged in the mixer body, a plurality of blades are welded on the mixing shaft, a discharge port communicated with the interior of the mixer body is arranged at the bottom of the mixer body, and a sliding chute matched with the discharge port is, one end of the chute, which is far away from the stirrer, is connected with a spiral belt device, and one end of the spiral belt device, which is far away from the chute, is connected with a separating device.
The above prior art solutions have the following drawbacks: the process of recycling the sludge and the waste slurry needs the cooperation of various devices to remove the water in the sludge and the waste slurry, so that the energy consumption is high and the cost is high.
SUMMERY OF THE UTILITY MODEL
The utility model aims at providing a silt dewatering system has the conveying distance that increases useless thick liquid silt in the heating chamber, utilizes solar energy and far infrared to get rid of the effect of the interior moisture of useless thick liquid silt.
The above utility model discloses an above-mentioned utility model purpose can realize through following technical scheme:
the utility model provides a silt dewatering system, includes the heating chamber and sets up the frame in the heating chamber, the top of heating chamber is provided with feed hopper, the bottom of heating chamber is provided with ejection of compact funnel, from the top down the interval is provided with the multilayer transport mechanism of transmitting silt from top to bottom in the frame, be provided with a plurality of far infrared heating pipes in the heating chamber, the far infrared heating pipe is located each transport mechanism's top, the surface of heating chamber is provided with graphite alkene layer.
Through adopting above-mentioned technical scheme, multilayer transport mechanism's setting, the distance of useless thick liquid silt conveying in the heating chamber has effectively been increased, because the surface of heating chamber is provided with graphite alkene layer, graphite alkene layer is used for realizing efficient light and heat conversion, through the energy of absorption solar energy, with the leading-in heating chamber of heat under the effect of graphite alkene, be provided with the far infrared heating pipe in the heating chamber, the far infrared heating pipe can improve the absorptive capacity of heated material to the radiation ray, make the moisture in the useless thick liquid silt evaporated under the effect of graphite alkene layer and far infrared heating pipe, drying effect is obvious, reduce the energy consumption.
The utility model discloses further set up to: the heating chamber is internally provided with a plurality of guide plates, the conveying mechanism comprises a driving wheel, a driven wheel, a conveyor belt sleeved between the driving wheel and the driven wheel and a motor driving the driving wheel, the guide plates are arranged between adjacent conveying mechanisms, the upper ends of the guide plates correspond to the tail ends of the conveying mechanisms above, and the lower ends of the guide plates correspond to the head ends of the conveying mechanisms below.
Through adopting above-mentioned technical scheme, transport mechanism's setting has realized the conveying of waste slurry silt in the heating chamber, and the setting of guide plate plays fine water conservancy diversion effect.
The utility model discloses further set up to: the vertical section of the guide plate is V-shaped.
Through adopting above-mentioned technical scheme, the effect that the V font of guide plate set up and play the water conservancy diversion is more obvious, ensures that the useless thick liquid silt can be under the water conservancy diversion effect of guide plate, and more complete falls to the conveyer belt and conveys.
The utility model discloses further set up to: the conveying direction of the conveying mechanism is arranged in an upward inclined mode towards the direction close to the guide plate.
Through adopting above-mentioned technical scheme, transport mechanism's direction of transfer upwards inclines to set up towards the direction that is close to the guide plate for the separation of solid and liquid in the waste slurry silt on the conveyer belt plays better drying effect.
The utility model discloses further set up to: the conveying directions of the adjacent conveying mechanisms are opposite.
Through adopting above-mentioned technical scheme, adjacent transport mechanism's direction of transfer is opposite, has increased the time of useless thick liquid silt conveying in the heating chamber, because there is the heat absorption of far infrared heating pipe and graphite alkene in the heating chamber, the evaporation of water effect that plays to the useless thick liquid silt of longer time in the heating chamber is better.
The utility model discloses further set up to: be equipped with a plurality of baffle on the conveyer belt, the perpendicular cross-section of baffle is the arc, the opening of baffle is towards conveyer belt direction of transfer, the equidistant distribution of baffle is on the conveyer belt, the baffle is porous infiltration structure.
Through adopting above-mentioned technical scheme, the baffle is porous and curved opening towards the direction of transfer for moisture in the waste slurry silt is at the in-process of conveying, because the effect of gravity, better realization solid-liquid separation, the getting rid of moisture in the waste slurry silt with higher speed.
The utility model discloses further set up to: and a drainage groove is formed in the middle of the conveying belt.
Through adopting above-mentioned technical scheme, the setting up of drainage groove makes the moisture in the waste slurry silt discharge through the drainage groove, effectively improves the effect that moisture was got rid of.
The utility model discloses further set up to: the feeding hopper is positioned right above the driving wheel of the uppermost conveying mechanism, and the discharging hopper is positioned right below the driven wheel of the lowermost conveying mechanism.
Through adopting above-mentioned technical scheme, the position setting of feed hopper and ejection of compact funnel effectively reduces the emergence of the extravagant phenomenon of waste slurry silt at whole recycle's in-process material.
To sum up, the utility model discloses a beneficial technological effect does:
1. the arrangement of the multilayer conveying mechanism effectively increases the conveying distance of the waste slurry sludge in the heating chamber, and as the graphene layer is arranged on the outer surface of the heating chamber and is used for realizing efficient photo-thermal conversion, the graphene layer can guide heat into the heating chamber under the action of graphene by absorbing solar energy, and the far infrared heating pipe is arranged in the heating chamber and can improve the absorption capacity of a heated material on radiation rays, so that moisture in the waste slurry sludge is evaporated under the action of the graphene layer and the far infrared heating pipe, the drying effect is obvious, and the energy consumption is reduced;
2. the V-shaped arrangement of the guide plate has more obvious flow guide effect, and ensures that the waste slurry and sludge can more completely fall onto the conveying belt for conveying under the flow guide effect of the guide plate;
3. the baffle is porous and curved opening towards direction of transfer for moisture in the waste slurry silt is at the in-process of conveying, because the effect of gravity, better realization solid-liquid separation, the getting rid of moisture in the waste slurry silt with higher speed.
Drawings
Fig. 1 is a schematic view of the overall structure of the present invention.
Fig. 2 is a schematic sectional structure view of fig. 1.
Fig. 3 is a schematic view of the overall internal structure of the present invention.
In the figure, 1, a heating chamber; 11. a feed hopper; 12. a discharging hopper; 13. a far infrared heating pipe; 14. a baffle; 2. a frame; 3. a transport mechanism; 31. an upper conveying mechanism; 311. a driving wheel; 312. a driven wheel; 313. a conveyor belt; 314. a motor; 315. a baffle plate; 316. a drainage groove; 32. a lower transport mechanism.
Detailed Description
The present invention will be described in further detail with reference to the accompanying drawings.
As shown in fig. 1 and 2, for the utility model discloses a sludge dewatering system, including heating chamber 1 and frame 2, frame 2 sets up in heating chamber 1, be provided with two sets of transport mechanism 3 in the frame 2, be respectively last transport mechanism 31 and lower transport mechanism 32, the top of heating chamber 1 is provided with feed hopper 11, the bottom of heating chamber 1 is provided with discharge hopper 12, the surface of heating chamber 1 is provided with graphite alkene layer, the material of heating chamber 1 is toughened glass, be provided with a plurality of far infrared heating pipes 13 and a plurality of guide plate 14 in the heating chamber 1, far infrared heating pipe 13 is located each transport mechanism 3's top.
As shown in fig. 3, the two sets of transmission mechanisms 3 have the same structure and are respectively an upper transmission mechanism 31 and a lower transmission mechanism 32, the upper transmission mechanism 31 is located below the lower transmission mechanism 32, the transmission mechanism 3 includes a driving wheel 311, a driven wheel 312, a transmission belt 313 and a motor 314, the driving wheel 311 and the driven wheel 312 are both arranged on the frame 2, the transmission belt 313 is sleeved between the driving wheel 311 and the driven wheel 312, and an output shaft of the motor 314 is fixedly connected with the driving wheel 311; the guide plate 14 is arranged between the adjacent conveying mechanisms 3, the upper end of the guide plate 14 is correspondingly positioned at the tail end of the upper conveying mechanism 3, the lower end of the guide plate 14 is correspondingly positioned at the head end of the lower conveying mechanism 3, and the vertical section of the guide plate 14 is V-shaped. The driving wheel 311 is arranged at one end of the frame 2 far away from the guide plate 14, the driven wheel 312 is arranged at one end of the frame 2 near the guide plate 14, the feeding hopper 11 is positioned right above the driving wheel 311 of the uppermost conveying mechanism 3, and the discharging hopper 12 is positioned right below the driven wheel 312 of the lowermost conveying mechanism 3.
As shown in fig. 2 and 3, the conveying directions of the upper conveying mechanism 31 and the lower conveying mechanism 32 are opposite, and the conveying direction of the conveying mechanism 3 is inclined upward toward the direction close to the baffle 14. The conveyor belt 313 is provided with a plurality of baffles 315, the vertical sections of the baffles 315 are arc-shaped, the openings of the baffles 315 face the conveying direction of the conveyor belt 313, the baffles 315 are distributed on the conveyor belt 313 at equal intervals, the baffles 315 are porous water permeable structures, and the middle of the conveyor belt 313 is provided with a drainage groove 316.
The implementation principle of the embodiment is as follows: the waste slurry and sludge enter the conveying belt 313 of the upper conveying mechanism 31 through the feeding hopper 11, when the conveying belt 313 is conveyed to a blanking position, the waste slurry and sludge fall to the lower conveying mechanism 32 under the action of the guide plate 14, and when the waste slurry and sludge are conveyed to the blanking position of the lower conveying mechanism 32, the waste slurry and sludge fall to the discharging hopper 12 under the action of the guide plate 14; whole transfer process sets up the state that far infrared heating pipe 13 in heating chamber 1 is in the heating, and heating chamber 1 is toughened glass moreover, and heating chamber 1's surface scribbles graphite alkene layer, turns into light energy heat energy through absorbing solar energy, increases the temperature in the heating chamber 1 and reaches the effect that evaporates the moisture in the useless thick liquid silt.
The embodiment of this specific implementation mode is the preferred embodiment of the present invention, not limit according to this the utility model discloses a protection scope, so: all equivalent changes made according to the structure, shape and principle of the utility model are covered within the protection scope of the utility model.

Claims (8)

1. The utility model provides a silt dewatering system, includes heating chamber (1) and frame (2) of setting in heating chamber (1), the top of heating chamber (1) is provided with feed hopper (11), the bottom of heating chamber (1) is provided with ejection of compact funnel (12), its characterized in that: the sludge drying machine is characterized in that a plurality of layers of conveying mechanisms (3) for conveying sludge from top to bottom are arranged on the rack (2) at intervals from top to bottom, a plurality of far infrared heating pipes (13) are arranged in the heating chamber (1), the far infrared heating pipes (13) are located above the conveying mechanisms (3), and graphene layers are arranged on the outer surface of the heating chamber (1).
2. A sludge dewatering system according to claim 1, wherein: be provided with a plurality of guide plates (14) in heating chamber (1), transport mechanism (3) include action wheel (311), follow driving wheel (312), cover and establish conveyer belt (313) between action wheel (311) and follow driving wheel (312) and motor (314) of drive action wheel (311), guide plate (14) set up between adjacent transport mechanism (3), the upper end correspondence of guide plate (14) is located the end of top transport mechanism (3), the lower extreme correspondence of guide plate (14) the head end of below transport mechanism (3).
3. A sludge dewatering system according to claim 2, wherein: the vertical section of the guide plate (14) is V-shaped.
4. A sludge dewatering system according to claim 3, wherein: the conveying direction of the conveying mechanism (3) is arranged to incline upwards towards the direction close to the guide plate (14).
5. A sludge dewatering system according to claim 4, wherein: the conveying directions of the adjacent conveying mechanisms (3) are opposite.
6. A sludge dewatering system according to claim 5, wherein: be equipped with a plurality of baffle (315) on conveyer belt (313), the perpendicular cross-section of baffle (315) is the arc, the opening of baffle (315) is towards conveyer belt (313) direction of transfer, baffle (315) equidistant distribution is on conveyer belt (313), baffle (315) are porous water permeable structure.
7. A sludge dewatering system according to claim 6, wherein: and a drainage groove (316) is arranged in the middle of the conveyor belt (313).
8. The sludge dewatering system of claim 7, wherein: the feeding hopper (11) is positioned right above a driving wheel (311) of the uppermost conveying mechanism (3), and the discharging hopper (12) is positioned right below a driven wheel (312) of the lowermost conveying mechanism (3).
CN201921219676.4U 2019-07-29 2019-07-29 Sludge dewatering system Active CN210287125U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201921219676.4U CN210287125U (en) 2019-07-29 2019-07-29 Sludge dewatering system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201921219676.4U CN210287125U (en) 2019-07-29 2019-07-29 Sludge dewatering system

Publications (1)

Publication Number Publication Date
CN210287125U true CN210287125U (en) 2020-04-10

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Application Number Title Priority Date Filing Date
CN201921219676.4U Active CN210287125U (en) 2019-07-29 2019-07-29 Sludge dewatering system

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112209590A (en) * 2020-10-30 2021-01-12 芜湖海创环保科技有限责任公司 Continuous rotation pyrolysis desorption system

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112209590A (en) * 2020-10-30 2021-01-12 芜湖海创环保科技有限责任公司 Continuous rotation pyrolysis desorption system

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