CN216144129U - Rotary flash dryer - Google Patents

Rotary flash dryer Download PDF

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Publication number
CN216144129U
CN216144129U CN202121949301.0U CN202121949301U CN216144129U CN 216144129 U CN216144129 U CN 216144129U CN 202121949301 U CN202121949301 U CN 202121949301U CN 216144129 U CN216144129 U CN 216144129U
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CN
China
Prior art keywords
dust remover
cyclone separator
flash dryer
cyclone
spin flash
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CN202121949301.0U
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Chinese (zh)
Inventor
夏树安
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Jiangsu Anzhili Environmental Protection Technology Co ltd
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Jiangsu Anzhili Environmental Protection Technology Co ltd
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Priority to CN202121949301.0U priority Critical patent/CN216144129U/en
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Abstract

The utility model discloses a spin flash dryer, which comprises a cyclone separator (6) and a dust remover (9), wherein the cyclone separator (6) is arranged in the dust remover (9), the cyclone separator (6) is positioned at the inner lower part of the dust remover (9), a feed pipe of the cyclone separator (6) penetrates through the outer wall of the lower part of the dust remover (9), and a bottom leakage opening (7) of the cyclone separator (6) is positioned above a bottom outlet of the dust remover (9). The rotary flash evaporation dryer has high drying and discharging efficiency and has more energy-saving and environment-friendly benefits.

Description

Rotary flash dryer
Technical Field
The utility model relates to a rotary flash evaporation dryer which can be used for drying pasty, cake-shaped and thixotropic or heat-sensitive powder materials and belongs to the technical field of drying equipment.
Background
At present, the rotary flash dryer can be used for quickly drying powdery or granular materials in various fields such as chemical industry, food, medicine and the like. The structure of a conventional spin flash dryer is generally shown in Chinese patent CN201020619698.2 "a spin flash dryer", the air supply of an air feeder is heated by a heater, after hot air enters the bottom of the dryer tangentially, a powerful rotary wind field is formed under the drive of a stirrer and enters the dryer; meanwhile, the materials to be dried are fed into the dryer through a spiral feeder, under the strong action of a high-speed rotating stirring paddle, the materials are dispersed under the action of impact, friction and shearing force, and the massive materials are quickly crushed and are merged into hot air entering the dryer to be fully contacted, heated and dried; the dehydrated dry materials rise along with hot air flow, the classifier intercepts large particles (the materials are not dried completely or the large materials are thrown to the wall of the separator under the action of centrifugal force and fall to the bottom again to be crushed and dried), the small particles are discharged out of the drier from the center of the classifier, and the processed materials are recovered from a star-shaped discharger after the cyclone separator and are bagged.
However, the spin flash dryer in the above form has a problem in use, 95% of the material is discharged after passing through the cyclone separator, but about 5% of the material inevitably enters the bag-type dust collector, and in order to avoid waste, the 5% of the material needs to be collected again and mixed with the discharged material of the cyclone separator again, and then is bagged, so the operation flow is more lengthy, the production efficiency is affected, and the energy-saving effect is poor. For this reason, it is required to improve it to solve the above-mentioned problems.
Disclosure of Invention
The utility model aims to overcome the defects and provide the rotary flash evaporation dryer with high drying and discharging efficiency, so that the rotary flash evaporation dryer has more energy-saving and environment-friendly benefits.
The purpose of the utility model is realized as follows:
the utility model provides a spin flash dryer, includes cyclone and dust remover, cyclone sets up in the dust remover, and cyclone is located the dust remover lower part, cyclone's inlet pipe passes the lower part outer wall of dust remover, cyclone's bottom leakage mouth is located the top of the bottom export of dust remover.
Furthermore, a blanking gap is formed between the outer wall of the cyclone separator and the inner wall of the dust remover.
Furthermore, the dust remover is a bag type dust remover, and a dust removing bag positioned in the dust remover is positioned above the cyclone separator.
Furthermore, a vibration mechanism is installed on the dust remover.
Furthermore, the dust remover is provided with a pulse type oscillating mechanism to form a pulse bag type dust remover.
Furthermore, the cyclone separator passes through a feeding pipe on the outer wall of the dust remover and is communicated to a discharge hole of the classifier, the classifier and the stirrer are respectively arranged at the upper part and the lower part of the dryer, and the stirrer is communicated with the air feeder through a heater and a hot air inlet at the lower part.
Furthermore, a pipeline connected with an upper air suction opening of the dust remover is communicated to the silencer through a draught fan.
Compared with the prior art, the utility model has the beneficial effects that:
the cyclone separator is integrated in the dust remover, so that the discharging of the cyclone separator and the discharging of the dust remover are concentrated at one position, and in the whole working process, the cyclone separator and the dust remover continuously discharge materials continuously, namely, material mixing is carried out synchronously, so that the whole equipment structure is more compact, the required occupied area is smaller, the working efficiency is effectively improved, the working process is simplified, the materials can be discharged from the same outlet and bagged at the same time in hundreds of percent, the production of production enterprises is greatly facilitated, the energy consumption of the operation is reduced, the market competitiveness of the products of the enterprises is improved, and the energy-saving and environment-friendly positive benefits are achieved.
Drawings
Fig. 1 is a schematic structural diagram of a spin flash dryer according to the present invention.
Wherein:
the device comprises a blower 1, a heater 2, a stirrer 3, a dryer 4, a classifier 5, a cyclone separator 6, a discharge port 7, a vibration mechanism (pulse) 8, a dust collector (cloth bag) 9, a silencer 10 and an induced draft fan 11.
Detailed Description
Referring to fig. 1, the spin flash dryer according to the present invention includes a blower 1, a heater 2, a stirrer 3, a dryer 4, a classifier 5, a cyclone separator 6, a leakage port 7, a vibration mechanism (pulse) 8, a dust collector (cloth bag) 9, a silencer 10, and a draught fan 11;
the air outlet of the air feeder 1 is communicated to the air inlet of the heater 2, the hot air outlet of the heater 2 is communicated to the side wall air inlet of the stirring machine 3, the bottom of the dryer 4 of the vertically arranged cylindrical structure is communicated with the stirring machine 3, the top of the stirring machine 3 is communicated with the classifier 5, the side wall of the stirring machine 3 is provided with a material feeding hole for guiding materials to be ground and dried, the side wall discharging hole of the classifier 5 is communicated to the side wall feeding hole of the cyclone separator 6 through a pipeline penetrating through the side wall of the dust remover 9, the cyclone separator 6 is located below the inner portion of the dust remover 9, the bottom discharging hole 7 of the cyclone separator 6 is located above the bottom discharging hole of the dust remover 9, and the pipeline on the side wall of the top of the dust remover 9 is communicated to the silencer 10 through the induced draft fan 11.
When the device is used, the air feeder 1 sends high-temperature hot air heated by the heater 2 into the stirrer 3, the high-temperature hot air enters the dryer 4 upwards to collide with materials in a cyclone formed by the stirrer 3, the materials are smashed and dried, then large-particle materials after drying are blocked by the classifier 5 and fall off, the large-particle materials are smashed again by the stirrer 3 to meet the requirements, small-particle materials meeting the requirements on particle size enter the cyclone separator 6 arranged in the dust remover 9 after passing through the classifier 5, the materials fall off through the discharge hole 7 downwards in the cyclone separator 6 and are discharged through the discharge hole at the bottom of the dust remover 9 again; meanwhile, partial materials are blocked by the dust remover 9 with the bag-type structure through external negative pressure suction, and meanwhile, the materials blocked by the dust remover 9 fall downwards under the action of the pulse-type oscillation mechanism 8 and are discharged and bagged through a bottom discharge hole of the dust remover 9. Therefore, the discharging of the two materials is positioned at the same position, 100% of the materials can be discharged at one time, the production efficiency is greatly improved, the operation flow and the process are greatly simplified, the efficiency is further improved, the energy consumption is reduced, and the energy-saving and emission-reducing benefits are remarkable.
In addition: it should be noted that the above-mentioned embodiment is only a preferred embodiment of the present patent, and any modification or improvement made by those skilled in the art based on the above-mentioned conception is within the protection scope of the present patent.

Claims (7)

1. A spin flash dryer comprising a cyclone separator (6) and a dust separator (9), characterized in that: cyclone (6) sets up in dust remover (9), and cyclone (6) are located dust remover (9) lower part, the inlet pipe of cyclone (6) passes the lower part outer wall of dust remover (9), bottom leakage mouth (7) of cyclone (6) are located the top of the bottom export of dust remover (9).
2. A spin flash dryer as claimed in claim 1, wherein: a blanking gap is formed between the outer wall of the cyclone separator (6) and the inner wall of the dust remover (9).
3. A spin flash dryer as claimed in claim 1, wherein: the dust remover (9) is a bag type dust remover, and a dust removing bag positioned in the dust remover (9) is positioned above the cyclone separator (6).
4. A spin flash dryer according to claim 1 or 3, wherein: and a vibration mechanism (8) is arranged on the dust remover (9).
5. A spin flash dryer according to claim 4, wherein: the dust remover (9) is provided with a pulse type vibration mechanism (8) to form a pulse bag type dust remover.
6. A spin flash dryer according to claim 1 or 3, wherein: the cyclone separator (6) penetrates through a feeding pipe on the outer wall of the dust remover (9) and is communicated to a discharge hole of the classifier (5), the classifier (5) and the stirrer (3) are respectively arranged at the upper part and the lower part of the dryer (4), and the stirrer (3) is communicated with the air feeder (1) through a heater (2) through a hot air inlet at the lower part.
7. A spin flash dryer as claimed in claim 6, wherein: and a pipeline connected with an upper air suction opening of the dust remover (9) is communicated to the silencer (10) through a draught fan (11).
CN202121949301.0U 2021-08-19 2021-08-19 Rotary flash dryer Active CN216144129U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202121949301.0U CN216144129U (en) 2021-08-19 2021-08-19 Rotary flash dryer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202121949301.0U CN216144129U (en) 2021-08-19 2021-08-19 Rotary flash dryer

Publications (1)

Publication Number Publication Date
CN216144129U true CN216144129U (en) 2022-03-29

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN202121949301.0U Active CN216144129U (en) 2021-08-19 2021-08-19 Rotary flash dryer

Country Status (1)

Country Link
CN (1) CN216144129U (en)

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