CN218421824U - Dust removal heat sink is used in bio-organic fertilizer production - Google Patents
Dust removal heat sink is used in bio-organic fertilizer production Download PDFInfo
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- CN218421824U CN218421824U CN202222034712.8U CN202222034712U CN218421824U CN 218421824 U CN218421824 U CN 218421824U CN 202222034712 U CN202222034712 U CN 202222034712U CN 218421824 U CN218421824 U CN 218421824U
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Abstract
The utility model belongs to the technical field of dust removal cooling equipment, specifically be a dust removal heat sink is used in bio-organic fertilizer production, include that the inertia force that connects gradually according to export access mouth order removes dust subassembly one, bag-type dust removal subassembly, sedimentation separation subassembly, inertia force remove dust subassembly two, the entry that pending dusty air current removed dust subassembly one from inertia force gets into, and export discharge from inertia force remove dust subassembly two after the drying of dust removal cooling. The utility model discloses can reach multistage dust removal, dust removal back air quality high, easy clean, semi-automatization, can guarantee exhaust air current's aridity, guarantee workshop drying environment when removing dust and cooling.
Description
Technical Field
The utility model belongs to the technical field of dust removal cooling equipment, specifically be a dust removal heat sink is used in bio-organic fertilizer production.
Background
In the production process of the bio-organic fertilizer, due to the diversification of processing steps, more dust is often generated at a processing part, and the dust floats in the air for a long time, so that the work of personnel is inconvenient, and the processing equipment is easy to break down. At present, most dust removal modes for organic fertilizer processing are mainly adsorption type, dust-containing gas is adsorbed and discharged, and fresh air is sent into the dust-containing gas. Although this dust removal method is simple, the dust in the gas is easily discharged to the outside, which causes environmental pollution. Therefore, the prepared biological organic fertilizer can remove the production dust in the processing process of the biological organic fertilizer, and the establishment of a production environment with high air quality is extremely important.
For example, the utility model with the authorization notice number of CN206778130U discloses a dust removal and temperature reduction device for the production of biological organic fertilizer. The dedusting and cooling device for the production of the biological organic fertilizer comprises a dedusting chamber and a water curtain spray deduster connected with the dedusting chamber, wherein the dedusting chamber comprises a cavity, and a slag cleaning door is arranged on the outer side wall of the dedusting chamber; the air inlet of clean room links to each other with an export of inhaling the wind pipeline, and the air outlet of clean room links to each other with the import of an air-out pipeline, the export of air-out pipeline with the air inlet that the water curtain sprayed the dust remover links to each other. This dust removal heat sink is used in bio-organic fertilizer production can effectively collect particulate matter and dust that produce in the workshop after the stoving operation. However, when the device is used, the sewage sprayed by the water curtain is difficult to clean, and although the device has a good dust removal effect, the cleaning capability of the device after use is poor.
SUMMERY OF THE UTILITY MODEL
In order to solve the technical problem, the utility model provides a can guarantee exhaust air flow's aridity, guarantee workshop drying environment's dust removal heat sink is used in bio-organic fertilizer production when multistage dust removal, dust removal back air quality are high, easy clean, semi-automatization, dust removal cooling.
The utility model particularly relates to a dust removal and cooling device for bio-organic fertilizer production, which comprises an inertia force dust removal component I, a bag type dust removal component, a sedimentation separation component and an inertia force dust removal component II which are connected in sequence, wherein dust-containing air flow to be treated enters from an inlet of the inertia force dust removal component I and is discharged from an outlet of the inertia force dust removal component II after dust removal, temperature reduction and drying;
the first inertial force dust removal assembly is composed of a first box body, a first partition plate vertically arranged at the middle position of the top end of the first box body, a first ash hopper arranged at the bottom of the first box body, and a first sewage discharge valve arranged at an opening of the first ash hopper;
the bag type dust removal assembly consists of a box body II, a filter bag vertically erected in the box body II through a support and an ash bucket II arranged at an outlet at the bottom end of the filter bag, and a spiral dust unloader is arranged at an opening of the ash bucket II;
the sedimentation separation assembly consists of a box body III, a water inlet pipe arranged at the top end of the box body III, an ash bucket III arranged at the bottom end of the box body III and a sewage discharge pipe arranged at three openings of the ash bucket;
the inertial force dust removal assembly II comprises a box body IV, a partition plate II arranged in the middle of the top end of the box body IV, an ash bucket IV arranged at the bottom of the box body IV and a sewage discharge valve II.
The top end of the first box body is of a plane structure, and an air inlet and an air outlet of the first inertia force dust removal assembly are respectively arranged on the side wall of the first box body on two sides of the first partition plate.
The top end and the bottom end of the filter bag are erected inside the second box body through the upper layer support and the lower layer support respectively, the air inlet of the bag type dust removal assembly is arranged on the two side walls of the second box body above the upper layer support, and the air outlet of the bag type dust removal assembly is arranged on the two side walls of the second box body between the upper layer support and the lower layer support.
The third box body is filled with water; the dusty airflow entering the sedimentation separation assembly enters the box body from the three side walls through the air guide pipes and is inserted into water, and the air outlet of the sedimentation separation assembly is arranged on the three side walls of the box body; the water inlet pipe is provided with a water inlet ball valve and a Y-shaped filter, and the drain pipe is provided with a drain ball valve.
The three internal parts of the box body are respectively provided with a liquid level sensor and a turbidity sensor, a PLC electrical control box is arranged outside the three box bodies, and the PLC electrical control box is respectively connected with the turbidity sensor, the liquid level sensor, the water inlet ball valve and the water discharge ball valve.
The top of the box body IV is provided with a symmetrically arranged convex arc structure, and the second partition plate is vertically arranged at the symmetrical axis of the convex arc structure; an air inlet and an air outlet of the second inertial force dust removal component are respectively arranged on two sides of the second partition plate; and granular carbon is filled in the box body IV.
The utility model has the advantages that the whole dust removal and cooling device comprises a four-stage dust removal component, thereby ensuring the dust removal efficiency; the first inertial force dust removal component is matched with the first box body through the first partition plate, after dust-containing air flows into the first box body, the flow velocity of the cross section is reduced, solid with large particles colliding with the first partition plate is settled first, and small particles enter the bag type dust removal component; in the bag type dust removal component, the dust removal effect is further achieved by arranging the filter bag; in the sedimentation separation assembly, water is contained in the box body III, airflow entering the box body III directly flushes into the water, dust is dissolved into the water, the airflow is insoluble in water and is discharged through the air outlet, and the purpose of finally filtering the dust is achieved; in addition, the process uses electricity to achieve semi-automatic control, water is automatically drained and fed when the water is turbid, operators do not need to drain and feed the water again after the work is finished, and labor is saved; and granular carbon is placed in the inertial force dust removal component II and is used for drying gas after the sedimentation separation component.
The utility model discloses can reach multistage dust removal, dust removal back air quality high, easy clean, semi-automatization, can guarantee exhaust air current's aridity, guarantee workshop drying environment when removing dust and cooling.
Drawings
Fig. 1 is an overall view of the dust-removing and cooling device for the production of the bio-organic fertilizer.
Fig. 2 is the utility model discloses a bio-organic fertilizer production is with bag collector subassembly sketch map of dust removal heat sink.
Fig. 3 is the utility model discloses a bio-organic fertilizer production is with dust removal heat sink's sedimentation separation subassembly sketch map.
Fig. 4 is the utility model discloses a bio-organic fertilizer production is with electric module connection schematic diagram of sedimentation separation subassembly among dust removal heat sink.
Description of the drawings: 1: inertial force dust removal assembly I, 11: first box body, 12: a first partition plate, 13: ash bucket I, 14: a first sewage discharge valve, 2: bag house dust removal assembly, 21: case two, 22: a filter bag, 23: ash buckets II and 24: spiral dust discharging machine, 25: upper layer support, 26: lower layer support, 3: sedimentation separation module, 31: case three, 32: inlet tube, 33: ash bucket three, 34: blow off pipe, 35: water inlet ball valve, 36: y-filter, 37: drain ball valve, 38: liquid level sensor, 39: turbidity sensor, 310: PLC electrical control box, 4: inertial force dust removal assemblies two, 41: case four, 42: second partition plate, 43: ash bucket four, 44: a second sewage discharge valve and 45: particulate carbon.
Detailed Description
To further understand the objects, technical solutions and advantages of the present invention, the present invention will be further described with reference to the accompanying drawings and embodiments, and it is obvious that the described embodiments are only some embodiments of the present invention, not all embodiments. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative efforts belong to the protection scope of the present invention.
Examples
As shown in fig. 1-4, the utility model relates to a dust removal and cooling device for bio-organic fertilizer production, which comprises an inertia force dust removal component 1, a bag type dust removal component 2, a sedimentation separation component 3 and an inertia force dust removal component two 4 which are sequentially connected according to the sequence of an outlet and an inlet, wherein the dust-containing air flow to be treated enters from the inlet of the inertia force dust removal component 1 and is discharged from the outlet of the inertia force dust removal component two 4 after dust removal, cooling and drying;
the inertial force dust removal assembly I1 is composed of a box body I11, a partition plate I12 vertically arranged in the middle of the top end of the box body I11, an ash bucket I13 arranged at the bottom of the box body I11, and a sewage discharge valve I14 arranged at an opening of the ash bucket I13;
the bag type dust removal assembly 2 consists of a second box body 21, a filter bag 22 vertically erected in the second box body 21 through a support, and a second ash hopper 23 arranged at an outlet at the bottom end of the filter bag 22, wherein a spiral dust discharging machine 24 is arranged at an opening of the second ash hopper 23;
the sedimentation separation component 3 consists of a box body III 31, a water inlet pipe 32 arranged at the top end of the box body III 31, an ash bucket III 33 arranged at the bottom end of the box body III 31 and a sewage discharge pipe 34 arranged at the opening of the ash bucket III 33;
the inertial force dust removal assembly II 4 is composed of a box body IV 41, a partition plate II 42 arranged in the middle of the top end of the box body IV 41, an ash bucket IV 43 arranged at the bottom of the box body IV 41 and a sewage discharge valve II 44.
The top end of the first box body 11 is of a plane structure, and an air inlet and an air outlet of the first inertial force dust removal assembly 1 are respectively formed in the side walls of the first box body 11 on the two sides of the first partition plate 12.
The top end and the bottom end of the filter bag 22 are erected inside the second box body 21 through an upper layer support 25 and a lower layer support 26 respectively, the air inlet of the bag type dust removal assembly 2 is formed in the side wall of the second box body 21 above the upper layer support 25, and the air outlet of the bag type dust removal assembly 2 is formed in the side wall of the second box body 21 between the upper layer support 25 and the lower layer support 26.
The third box body 31 is filled with water; the dusty airflow entering the sedimentation separation assembly 3 enters the water from the side wall of the box body III 31 through the air guide pipe and is inserted into the water, and the air outlet of the sedimentation separation assembly 3 is arranged on the side wall of the box body III 31; the water inlet pipe 32 is provided with a water inlet ball valve 35 and a Y-shaped filter 36, and the sewage discharge pipe 34 is provided with a water discharge ball valve 37.
A liquid level sensor 38 and a turbidity sensor 39 are respectively installed in the third box body 31, a PLC (programmable logic controller) electrical control box 310 is arranged outside the third box body 31, and the PLC electrical control box 310 is respectively connected with the turbidity sensor 39, the liquid level sensor 38, the water inlet ball valve 35 and the water discharge ball valve 37.
The top of the box body IV 41 is a symmetrically arranged convex arc structure, and the second partition plate 42 is vertically arranged at the symmetrical axis of the convex arc structure; the air inlet and the air outlet of the second inertia force dust removal assembly 4 are respectively arranged at two sides of the second partition plate 42; the box body four 41 is internally provided with granular carbon 45.
The utility model relates to a method for using a dust removal and temperature reduction device for a bio-organic fertilizer and the steps are as follows.
The first step. The dust-containing airflow enters the inertial force dust removal assembly I1 from the air inlet, the first partition plate 12 is arranged in the middle of the top of the first box body 11, after the dust-containing airflow enters the first box body 11, the radius of the cross section of the airflow is increased, the flow speed is reduced, heavy dust carried in the airflow falls into the first dust hopper 13, and when excessive dust is accumulated in the first dust hopper 13, the first pollution discharge valve 14 is manually opened to remove the dust; the lighter dust flows out of the air outlet along with the air flow and enters the bag-type dust removal component 2.
And a second step. The airflow reaching the bag-type dust removal assembly 2 enters the upper part of the upper layer bracket 25 and enters the filter bag 22, the airflow passes through the small Kong Lvchen on the filter bag 22, and the further purified airflow is discharged from the air outlet and enters the sedimentation separation assembly 3; the relatively heavy dust is discharged from the second dust hopper 23 at the bottom of the filter bag 22, and the purpose of arranging the spiral dust discharging machine 24 at the bottom of the second dust hopper 23 is to prevent a large amount of airflow from directly discharging from below.
And thirdly, performing the step of. The airflow entering the sedimentation separation component 3 is inserted into water through an air guide pipe to further filter dust, and the airflow after dust filtration by water flow is discharged from an air outlet in the side wall of the box body III 31; when the water in the third box body 31 is turbid, the turbidity sensor 39 monitors that the turbidity of the water is too high, a signal is sent to the PLC electrical control box 310, and the PLC electrical control box 310 controls the drainage ball valve 37 to be opened to drain dirty water; after the dirty water is completely discharged, the liquid level sensor 38 detects and feeds back the dirty water to the PLC electrical control box 310, the PLC electrical control box 310 controls the water inlet ball valve 35 to be opened, and water is fed into the box body III 31; when the water amount reaches the threshold value, the liquid level sensor 38 feeds back a signal, and the PLC electrical control box 310 controls the water inlet ball valve 35 to be closed. A third ash hopper 33 is arranged at the bottom of the third box body 31 to help sediment in the turbid water to be gathered at an outlet of the third ash hopper 33, so that the third box body 31 is cleaned; the inlet pipe 32 is provided with a Y-shaped filter 36 for purifying the inlet water.
And fourthly, performing the step of. The airflow after passing through the settling separation assembly 3 enters the second inertia force dust removal assembly 4, and is adsorbed by the carbon particles 45 contained in the fourth box body 41, and then is discharged through the air outlet.
It should be noted that the water inlet ball valve 35 and the water discharge ball valve 37 in this embodiment are Q911F electric internal thread ball valves; the liquid level sensor 38 is a separate photoelectric liquid level sensor; the turbidity sensor 39 is a DTS-600 digital turbidity sensor; the first sewage draining valve 14 and the second sewage draining valve 44 are manual gate valves; the liquid level sensor 38 is arranged at the top end of the inner side wall of the box body III, and the turbidity sensor 39 is arranged at least 20cm away from the bottom in the box body III and is submerged; in the device, the spiral dust remover 24 is of a windmill structure, and the central shaft position of the spiral dust remover 24 is arranged at the outlet of the second ash bucket 23 through a rotating shaft by using a bracket.
It is noted that, in this document, relational terms such as "a," "an," "two," and the like may be used solely to separate one entity or action from another entity or action without necessarily requiring or implying any actual such relationship or order between such entities or actions. The above description is only the preferred embodiment of the present invention, but the protection scope of the present invention is not limited thereto, and any person skilled in the art is in the technical scope of the present invention, and the technical solution and the utility model concept of the present invention should be covered by the protection scope of the present invention.
Claims (6)
1. The utility model provides a bio-organic fertilizer production is with dust removal heat sink which characterized in that: the device comprises a first inertial force dust removal component, a bag type dust removal component, a sedimentation separation component and a second inertial force dust removal component which are sequentially connected, wherein a to-be-treated dusty airflow enters from an inlet of the first inertial force dust removal component, and is discharged from an outlet of the second inertial force dust removal component after dust removal, temperature reduction and drying;
the first inertial force dust removal assembly is composed of a first box body, a first partition plate vertically arranged at the middle position of the top end of the first box body, a first ash hopper arranged at the bottom of the first box body, and a first sewage discharge valve arranged at an opening of the first ash hopper;
the bag type dust removal assembly consists of a box body II, a filter bag vertically erected in the box body II through a support and an ash bucket II arranged at an outlet at the bottom end of the filter bag, wherein a spiral dust discharging machine is arranged at an opening of the ash bucket II;
the sedimentation separation assembly consists of a box body III, a water inlet pipe arranged at the top end of the box body III, an ash bucket III arranged at the bottom end of the box body III and a sewage discharge pipe arranged at three openings of the ash bucket;
the inertia force dust removal assembly II is composed of a box body IV, a partition plate II arranged in the middle of the top end of the box body IV, an ash hopper IV arranged at the bottom of the box body IV and a sewage discharge valve II.
2. The dedusting and cooling device for bio-organic fertilizer production according to claim 1 is characterized in that: the top end of the first box body is of a plane structure, and an air inlet and an air outlet of the first inertia force dust removal assembly are respectively arranged on the side wall of the first box body on two sides of the first partition plate.
3. The dust removal and temperature reduction device for the production of the bio-organic fertilizer, according to claim 2, is characterized in that: the top end and the bottom end of the filter bag are erected inside the second box body through the upper layer support and the lower layer support respectively, the air inlet of the bag type dust removal assembly is arranged on the two side walls of the second box body above the upper layer support, and the air outlet of the bag type dust removal assembly is arranged on the two side walls of the second box body between the upper layer support and the lower layer support.
4. The dust removal and temperature reduction device for the production of the bio-organic fertilizer, according to claim 3, is characterized in that: the third box body is filled with water; the dusty airflow entering the sedimentation separation assembly enters the box body from the three side walls through the air guide pipe and is inserted into water, and the air outlet of the sedimentation separation assembly is arranged on the three side walls of the box body; the water inlet pipe is provided with a water inlet ball valve and a Y-shaped filter, and the drain pipe is provided with a drain ball valve.
5. The dedusting and cooling device for bio-organic fertilizer production according to claim 4, wherein a liquid level sensor and a turbidity sensor are respectively installed in the third box body, a PLC electrical control box is arranged outside the third box body, and the PLC electrical control box is respectively connected with the turbidity sensor, the liquid level sensor, the water inlet ball valve and the water discharge ball valve.
6. The dust removal and temperature reduction device for the production of the bio-organic fertilizer, according to claim 5, is characterized in that: the top of the box body IV is provided with a symmetrically arranged convex arc structure, and the second partition plate is vertically arranged at the symmetrical axis of the convex arc structure; an air inlet and an air outlet of the inertial force dust removal assembly II are respectively arranged on two sides of the partition plate II; and granular carbon is filled in the box body IV.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202222034712.8U CN218421824U (en) | 2022-08-03 | 2022-08-03 | Dust removal heat sink is used in bio-organic fertilizer production |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202222034712.8U CN218421824U (en) | 2022-08-03 | 2022-08-03 | Dust removal heat sink is used in bio-organic fertilizer production |
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| Publication Number | Publication Date |
|---|---|
| CN218421824U true CN218421824U (en) | 2023-02-03 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202222034712.8U Active CN218421824U (en) | 2022-08-03 | 2022-08-03 | Dust removal heat sink is used in bio-organic fertilizer production |
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| Country | Link |
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| CN (1) | CN218421824U (en) |
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- 2022-08-03 CN CN202222034712.8U patent/CN218421824U/en active Active
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