CN219943537U - Large-block impurity removing device for calcium aluminate discharge end - Google Patents
Large-block impurity removing device for calcium aluminate discharge end Download PDFInfo
- Publication number
- CN219943537U CN219943537U CN202321715742.3U CN202321715742U CN219943537U CN 219943537 U CN219943537 U CN 219943537U CN 202321715742 U CN202321715742 U CN 202321715742U CN 219943537 U CN219943537 U CN 219943537U
- Authority
- CN
- China
- Prior art keywords
- sieve
- cooling cylinder
- discharge end
- calcium aluminate
- removing bulk
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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Links
- XFWJKVMFIVXPKK-UHFFFAOYSA-N calcium;oxido(oxo)alumane Chemical compound [Ca+2].[O-][Al]=O.[O-][Al]=O XFWJKVMFIVXPKK-UHFFFAOYSA-N 0.000 title claims abstract description 25
- 239000012535 impurity Substances 0.000 title claims abstract description 15
- 238000001816 cooling Methods 0.000 claims abstract description 37
- 238000007873 sieving Methods 0.000 claims description 4
- 230000001174 ascending effect Effects 0.000 claims description 3
- 239000000463 material Substances 0.000 abstract description 24
- 238000000034 method Methods 0.000 abstract description 11
- 238000012216 screening Methods 0.000 abstract description 4
- 238000012545 processing Methods 0.000 abstract description 3
- 239000000843 powder Substances 0.000 description 8
- 230000000694 effects Effects 0.000 description 6
- 238000004519 manufacturing process Methods 0.000 description 6
- 239000013590 bulk material Substances 0.000 description 3
- 230000015572 biosynthetic process Effects 0.000 description 2
- 125000004122 cyclic group Chemical group 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 238000003754 machining Methods 0.000 description 2
- 238000005096 rolling process Methods 0.000 description 2
- RNFJDJUURJAICM-UHFFFAOYSA-N 2,2,4,4,6,6-hexaphenoxy-1,3,5-triaza-2$l^{5},4$l^{5},6$l^{5}-triphosphacyclohexa-1,3,5-triene Chemical compound N=1P(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP=1(OC=1C=CC=CC=1)OC1=CC=CC=C1 RNFJDJUURJAICM-UHFFFAOYSA-N 0.000 description 1
- UXVMQQNJUSDDNG-UHFFFAOYSA-L Calcium chloride Chemical compound [Cl-].[Cl-].[Ca+2] UXVMQQNJUSDDNG-UHFFFAOYSA-L 0.000 description 1
- ANBBXQWFNXMHLD-UHFFFAOYSA-N aluminum;sodium;oxygen(2-) Chemical compound [O-2].[O-2].[Na+].[Al+3] ANBBXQWFNXMHLD-UHFFFAOYSA-N 0.000 description 1
- 230000004888 barrier function Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 239000001110 calcium chloride Substances 0.000 description 1
- 229910001628 calcium chloride Inorganic materials 0.000 description 1
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 description 1
- 239000000920 calcium hydroxide Substances 0.000 description 1
- 229910001861 calcium hydroxide Inorganic materials 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 239000003063 flame retardant Substances 0.000 description 1
- 229910017053 inorganic salt Inorganic materials 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000000123 paper Substances 0.000 description 1
- 230000003014 reinforcing effect Effects 0.000 description 1
- 239000005060 rubber Substances 0.000 description 1
- 229910001388 sodium aluminate Inorganic materials 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 229920003002 synthetic resin Polymers 0.000 description 1
- 239000000057 synthetic resin Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Landscapes
- Combined Means For Separation Of Solids (AREA)
Abstract
The utility model discloses a large-block impurity removing device for a discharge end of calcium aluminate, which comprises a cooling cylinder, wherein the cooling cylinder is connected with a driving device, the discharge end of the cooling cylinder is provided with a screening structure, the screening structure comprises a screen plate which is arranged on the outer wall of the cooling cylinder and extends towards the discharge direction, the side wall of the screen plate is provided with screen holes, and the screen plate can screen the mixed materials in the discharge process of the mixed materials at the discharge port of the cooling cylinder, so that the processing flow is simplified, and the processing efficiency is improved.
Description
Technical Field
The utility model relates to the technical field of calcium aluminate production, in particular to a device for removing massive impurities during cooling and discharging of calcium aluminate.
Background
The calcium aluminate is an inorganic salt which is prepared by the reaction of sodium aluminate, calcium chloride and calcium hydroxide and is used for manufacturing concrete accelerator, flame retardant of rubber, paper and synthetic resin, and the like.
In the prior art, a single-cylinder cooler is adopted to cool the calcium aluminate, so that the calcium aluminate is one of important equipment in a rotary kiln production system, clinker coming out of the rotary kiln is driven to fully exchange heat with air through the rotation of a cylinder body, so that the material is cooled, the quality and grindability of the clinker are improved, in the cooling process, the powder calcium aluminate and massive calcium aluminate are mixed, the sieved massive material is required to be sieved by a sieving device, the sieved massive material is required to be crushed again, the sieving process is increased, the production space and the production time are occupied, the steps are complex, and the technical improvement is made.
Disclosure of Invention
The utility model aims to overcome the defects that the powder and the bulk materials need to be screened again after the calcium aluminate is cooled to occupy the production space and influence the efficiency in the prior art, and provides a device for removing bulk impurities at the discharge end of the calcium aluminate.
The utility model is realized by the following technical scheme: the utility model provides a calcium aluminate discharge end large-scale impurity removing device, includes the cooling cylinder, the cooling cylinder is connected with drive arrangement, the discharge end of cooling cylinder is provided with the screen structure that removes, the screen structure is including setting up at the cooling cylinder outer wall and to the sieve of ejection of compact direction extension, be provided with the sieve mesh on the lateral wall of sieve.
Further, the sieve plate is cylindrical, the sieve holes are uniformly formed in the sieve plate, and an extension plate is arranged at the outer edge of the sieve holes from the outer edge of the sieve plate.
Further, the width of the extension plate is 10-30cm.
Further, an upward annular baffle is arranged at the joint of the extension plate and the sieve holes.
Further, a receiving plate is arranged on the outer side of the screen plate, and a space is reserved between the receiving plate and the screen plate.
Further, the cooling cylinder is obliquely arranged through the support, and the inclination angle of the cooling cylinder is 5 degrees.
Further, the driving device comprises a driving gear arranged on the outer side of the cooling cylinder, and the driving gear is connected with a driving motor.
The utility model has the beneficial effects that: the discharge end of cooling cylinder is provided with at cooling cylinder outer wall and to the sieve of ejection of compact direction extension, the sieve is cylindric, the sieve mesh evenly sets up on the sieve, the outward flange of sieve mesh is provided with the extension board apart from the outward flange of sieve, the junction of extension board and sieve mesh is provided with ascending cyclic annular baffle, use cyclic annular baffle to block the mixed material in sieve mesh portion, reduce the outflow of powder from the discharge gate, the bulk material has the part to pile up in baffle department at pivoted in-process, but can not block the sieve mesh formation, simultaneously the bulk material is striking at rolling in-process, shake the calcium aluminate powder of piling up on the sieve mesh, the reinforcing ejection of compact effect, set up the sieve at the discharge gate of cooling cylinder and just can sieve it at the in-process of mixed material ejection of compact, the processing flow has been simplified, machining efficiency has been improved.
Drawings
FIG. 1 is a schematic diagram of the overall structure of the present utility model;
FIG. 2 is a schematic illustration of the screening structure of the present utility model;
wherein: 1. a cooling cylinder; 101. a driving motor; 2. a sieve plate; 201. an extension plate; 202. a baffle; 203. a collecting bin; 3. and a material receiving plate.
Detailed Description
In the description of the present utility model, it should also be noted that, unless explicitly specified and limited otherwise, the terms "disposed," "mounted," "connected," and "connected" are to be construed broadly, and may be, for example, fixedly connected, detachably connected, or integrally connected; can be mechanically or electrically connected; can be directly connected or indirectly connected through an intermediate medium, and can be communication between two elements. The specific meaning of the above terms in the present utility model will be understood in specific cases by those of ordinary skill in the art.
The following description of the embodiments of the present utility model will be made clearly and fully with reference to the accompanying drawings, in which it is evident that the embodiments described are only some, but not all embodiments of the utility model. All other embodiments, which can be made by those skilled in the art based on the embodiments of the utility model without making any inventive effort, are intended to be within the scope of the utility model.
Examples
As shown in fig. 1-2: the utility model provides a calcium aluminate discharge end large scale impurity removing devices, including cooling cylinder 1, cooling cylinder 1 is connected with drive arrangement, cooling cylinder 1 passes through the support slope setting, cooling cylinder 1 inclination is 5 degrees, drive arrangement is including setting up the drive gear in cooling cylinder 1 outside, drive gear is connected with driving motor 101, the material of mixing gets into from cooling cylinder 1's feed inlet when using, driving motor 101's drive cooling cylinder 1 takes place to rotate, the mixture cools off the material when taking place to rotate, the material can be along cooling cylinder 1 to the discharge gate motion under the effect of gravity, the material can take place friction collision when rotating, the screening effect of increase material.
The discharge end of cooling cylinder 1 is provided with the screen structure, screen structure is including setting up at cooling cylinder 1 outer wall and to the screen plate 2 of ejection of compact direction extension, screen plate 2 is cylindric, be provided with the sieve mesh on the lateral wall of screen plate 2, the sieve mesh evenly sets up on screen plate 2, the outside edge of sieve mesh is provided with extension board 201 apart from the outside edge of screen plate 2, the width of extension board 201 is 10-30cm, cooling cylinder 1 can spill the calcium aluminate powder in the material of process from the sieve mesh when rotating, collect the powder with collection storehouse 203 of below, bulk material and impurity continue to roll forward under the effect of gravity and separate the unloading from the discharge gate, carry out the next step through the deflector to it.
The extension board 201 is provided with ascending annular baffle 202 with the junction of sieve mesh, uses annular baffle 202 to block the mixed material in the sieve mesh part, reduces the outflow of powder from the discharge gate, and baffle 202 highly is 3-5cm, and the massive material has the part to pile up in baffle 202 department at pivoted in-process, but can not block the sieve mesh formation, and massive material is striking sieve 2 at rolling in-process simultaneously, shakes down the calcium aluminate powder of piling up on the sieve mesh, strengthens the ejection of compact effect, sets up sieve 2 at the discharge gate of cooling cylinder 1 and just can sieve it at the in-process of mixed material ejection of compact, has simplified the process flow, has improved machining efficiency.
The outside at sieve 2 is provided with receives flitch 3, and receive flitch 3's cross section is the arc, leaves the interval between receipts flitch 3 and the sieve 2, and powdery calcium aluminate material can lift up along with the rotation of sieve 2 when using, causes the waste of material, uses receipts flitch 3 to form the barrier to the powdery material that lifts up to collect collection storehouse 203 inside with the material after blocking from the bottom, reduce the pollution of environment, improve the collection effect of material.
Finally, it should be noted that: the foregoing description of the preferred embodiments of the present utility model is not intended to be limiting, but rather, it will be apparent to those skilled in the art that the foregoing description of the preferred embodiments of the present utility model can be modified or equivalents can be substituted for some of the features thereof, and any modification, equivalent substitution, improvement or the like that is within the spirit and principles of the present utility model should be included in the scope of the present utility model.
Claims (7)
1. The utility model provides a calcium aluminate discharge end large-scale impurity removing devices, includes the cooling cylinder, the cooling cylinder is connected with drive arrangement, its characterized in that: the discharge end of cooling cylinder is provided with the structure of sieving, the structure of sieving is including setting up at the cooling cylinder outer wall and to the sieve of ejection of compact direction extension, be provided with the sieve mesh on the lateral wall of sieve.
2. The device for removing bulk impurities at a discharge end of calcium aluminate according to claim 1, wherein: the sieve is cylindric, the sieve mesh evenly sets up on the sieve, the outward flange of sieve mesh is provided with the extension board apart from the outward flange of sieve.
3. The apparatus for removing bulk impurities at a discharge end of calcium aluminate according to claim 2, wherein: the width of the extension plate is 10-30cm.
4. The apparatus for removing bulk impurities at a discharge end of calcium aluminate according to claim 2, wherein: the junction of extension board and sieve mesh is provided with ascending annular baffle.
5. The device for removing bulk impurities at a discharge end of calcium aluminate according to claim 1, wherein: the outside of sieve is provided with the receipts flitch, leave the interval between receipts flitch and the sieve.
6. The device for removing bulk impurities at a discharge end of calcium aluminate according to claim 1, wherein: the cooling cylinder is obliquely arranged through the support, and the inclination angle of the cooling cylinder is 5 degrees.
7. The device for removing bulk impurities at a discharge end of calcium aluminate according to claim 1, wherein: the driving device comprises a driving gear arranged on the outer side of the cooling cylinder, and the driving gear is connected with a driving motor.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202321715742.3U CN219943537U (en) | 2023-06-30 | 2023-06-30 | Large-block impurity removing device for calcium aluminate discharge end |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202321715742.3U CN219943537U (en) | 2023-06-30 | 2023-06-30 | Large-block impurity removing device for calcium aluminate discharge end |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN219943537U true CN219943537U (en) | 2023-11-03 |
Family
ID=88541856
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202321715742.3U Active CN219943537U (en) | 2023-06-30 | 2023-06-30 | Large-block impurity removing device for calcium aluminate discharge end |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN219943537U (en) |
-
2023
- 2023-06-30 CN CN202321715742.3U patent/CN219943537U/en active Active
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