CN200968763Y - Seasoner pelletization drying apparatus - Google Patents
Seasoner pelletization drying apparatus Download PDFInfo
- Publication number
- CN200968763Y CN200968763Y CN 200620134277 CN200620134277U CN200968763Y CN 200968763 Y CN200968763 Y CN 200968763Y CN 200620134277 CN200620134277 CN 200620134277 CN 200620134277 U CN200620134277 U CN 200620134277U CN 200968763 Y CN200968763 Y CN 200968763Y
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- air
- foraminous conveyer
- heating clamber
- air channel
- flavoring
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Abstract
A flavoring palletizing drying equipment is provided. The feed end of the band dryer is provided with a mixer, a feed bin and a pelletizer, while the discharge end is provided with a sizing screen; the mentioned band dryer is provided with at least five drying rooms, and each drying room is provided with a separator air circulation system and a dehumidification system. The mentioned drying room has two kinds of heating room and cooling room. Wherein, the air circulation system in the heating room is a bottom to top or top to bottom circulation system, and the air circulation systems between two neighboring are not the same, that is to say two different circulation systems are positioned alternately. The utility model forms the flavoring production to be a process flows line, overcoming the cross pollution between people and products caused by interval producing of a single machine, adopts hot air crossing circulation, that means the heating air crosses the net belt with materiel from bottom to top and top to bottom, ensuring the wet materiel heated around evenly, gaining perfect drying effect.
Description
Technical field
The utility model relates to a kind of flavoring granulation drying equipment, the granulation drying of suitable especially chickens' extract.
Background technology
Exist the heat-sensitive substance of oil, salt, sugared stick nature in the raw material of chickens' extract, traditional production technique adopts the vibration of Vibratingfluidbeddrier to overcome problems such as bonding in drying process, crane span structure.Yet, Vibratingfluidbeddrier is with vibration mode wet feed to be pushed ahead, in advancing, carry out heat exchange, but because the vibration of drying machine causes the wet stock granularity broken greatly, fine powder material falls from the fluidized bed airflow hole and wastes with the hot-air that adds that penetrates the fluidisation plate.Simultaneously, the heating-up temperature of vibrated fluidized bed in dry run, whole process is consistent, causes the uneven phenomenon of finished product water content.Its drying chamber structure of traditional band drier is a channel-type, transmitting guipure moves in passage, material is laid on and transmits on the guipure, air communication is crossed the transmission guipure material is carried out drying, omnidistance heating-up temperature unanimity, energy resource consumption is bigger, and the heat that material is subjected on conveyer belt is inhomogeneous, cause the uneven phenomenon of finished product water content, influence the dry mass of material.
The utility model content
The purpose of this utility model is to propose that a kind of material is heated evenly and with the flavoring granulation drying equipment of streamline form processing.
For achieving the above object, the utility model has on the basis of band drier, is provided with mixer, feed bin and comminutor at the feed end of band drier, and discharge end is provided with classifying screen; The discharging opening of above-mentioned mixer is facing to the charging aperture of feed bin, and the discharging opening of feed bin is facing to the charging aperture of comminutor, and the discharging opening of comminutor is facing to the top of drying machine foraminous conveyer, and the end of foraminous conveyer is facing to the charging aperture of classifying screen; Foraminous conveyer is dragged by transmission device by motor; Described band drier is provided with at least 5 hothouses, the dividing plate of adjacent hothouse is provided with the opening that allows foraminous conveyer and shop material thereon to pass through, each hothouse is furnished with independently air circulation system and dehumidification system, above-mentioned hothouse is divided into two kinds of heating clamber and cooling chambers, the air circulation system of heating clamber or air circulation system or the from top to bottom circulatory system from the bottom to top, the air circulation system of adjacent heating clamber are that different i.e. two kinds of circulatory systems are to be provided with at interval.
The vertical dividing plate and the lateral partitions that are equipped with in all heating clambers are divided into two spaces with heating clamber top, and wherein a space is the dry place that foraminous conveyer is set, and the upper and lower double-layer separate of foraminous conveyer is in lateral partitions both sides up and down, and another space is the air channel; Middle part, air channel at heating clamber is provided with the heater that cuts off the air channel, the dehumidification tube that the corresponding position, top of heating clamber is provided with air-introduced machine, additional mouthful of new wind and is connected with outside hydrofuge house steward, the part of corresponding blower fan discharge pipe is the orifice plate that is communicated with discharge pipe and top, air channel on the vertical dividing plate, vertically on the dividing plate between the upper strata of corresponding foraminous conveyer and the lateral partitions part in space be the orifice plate that is communicated with this space and bottom, air channel.
In the described heating clamber and the inlet side that is in heater is provided with drawable type and keeps off grey filter screen.
The air circulation system from the bottom to top that described heating clamber adopts, then the air inlet of its air-introduced machine is in the dry place, and new wind replenishes mouth and communicates with top, air channel, and dehumidification tube communicates with dry place, and air circulation is passed the upper strata of foraminous conveyer from the bottom to top; The air circulation system from top to bottom that described heating clamber adopts, then the air inlet of its air-introduced machine is arranged in the top, air channel, and new wind replenishes mouth and communicates with dry place, and dehumidification tube communicates with the bottom, air channel, and air circulation is passed the upper strata of foraminous conveyer from top to bottom.
The vertical dividing plate and the lateral partitions that are provided with in the described cooling chamber are divided into two spaces with cooling chamber top, and wherein a space is the dry place that foraminous conveyer is set, and another space is the air channel; The upper and lower double-layer separate of foraminous conveyer is in lateral partitions both sides up and down, the corresponding position, top of cooling chamber is provided with air-introduced machine and new wind replenishes mouth, humid air is discharged by the air-introduced machine of this chamber, on the vertical dividing plate between the upper strata of corresponding foraminous conveyer and the lateral partitions part in space for being communicated with the orifice plate of this space and bottom, air channel.
The air inlet of the air-introduced machine of described cooling chamber is arranged in the dry place, and new wind replenishes mouth and communicates with the air channel, and air circulation is passed the upper strata of foraminous conveyer from the bottom to top.
At least one end is provided with deashing device in the beginning of described drying machine foraminous conveyer, the last two ends, and described deashing device is an electric rolling formula brush.
The utlity model has following characteristics:
1, the utility model raw material that flavoring is produced mixes, and granulates, and drying and sizing screening technology are formed the technological process production line, and production line is in the state work down of sealing, overcomes traditional unit Batch Process and people's logistics cross pollution of producing.
2, the utility model is used the dynamic dry technology of continuous motion, adopt the circulation of hot blast percolation, promptly add hot-air from the bottom to top and from top to bottom percolation in the guipure that is loaded with material, make wet stock in continuous motion, realize heat exchange with the hot-air that adds of percolation in guipure, wet stock up and down around thermally equivalent, the material surface curing fast owing to rapid draing, avoid phenomenons such as material bonding, crane span structure to take place, and because wet stock is in and is in metastable state on the foraminous conveyer, particle is cracky not.The utility model all has certain guarantee on product quality and yield rate.
3, each hothouse of drying machine of the present utility model is furnished with independently air circulation system, sets the temperature of each hothouse according to arts demand, so economize energy.
4, the utility model in the drying machine heating clamber and the inlet side that is in heater be provided with drawable type and keep off grey filter screen, help the cleaning of heater, drawable type keeps off grey filter screen can take out cleaning from drying machine, for the drying machine cleaning is provided convenience.
Description of drawings
For the easier quilt of content of the present utility model is clearly understood, below the specific embodiment and in conjunction with the accompanying drawings of basis, the present invention is further detailed explanation, wherein
Fig. 1 is the utility model configuration diagram;
Fig. 2 promptly adopts the heating clamber configuration diagram of air circulation system from the bottom to top for the A-A cutaway view of Fig. 1;
Fig. 3 promptly adopts the heating clamber configuration diagram of air circulation system from top to bottom for the B-B cutaway view of Fig. 1;
Fig. 4 is the cooling chamber configuration diagram for the C-C cutaway view of Fig. 1.
The specific embodiment
Present embodiment shown in the accompanying drawing 1～3 has band drier, mixer 2, feed bin 3 and comminutor 4, and discharge end is provided with classifying screen 5; The discharging opening of above-mentioned mixer 2 is facing to the charging aperture of feed bin 3; the discharging opening of feed bin 3 is facing to the charging aperture of comminutor 4; the discharging opening of comminutor 4 is facing to the top of drying machine foraminous conveyer 5; the end of foraminous conveyer 5 is facing to the charging aperture of classifying screen 5; in addition, the discharging opening of classifying screen 5 is provided with perfume sprayer 8.At least one end is provided with deashing device 7 in the beginning of drying machine foraminous conveyer 5, the last two ends.Comminutor 4 adopts swing wet granulator, by changing granulator granulation mesh screen, can reach the granularity diameter of required different size.Deashing device is an electric rolling formula brush, and the setting of deashing device is to influence the circulation of air so that influence drying effect because of the obstruction of foraminous conveyer in order to prevent.Mixer 2, comminutor 4 and classifying screen 5 all are machines commonly used.Foraminous conveyer 5 is dragged by transmission device 10 by motor.
Described band drier is provided with at least 5 hothouses, the dividing plate of adjacent hothouse is provided with the opening that allows foraminous conveyer and shop material thereon to pass through, each hothouse is furnished with independently air circulation system and dehumidification system, and each hothouse is provided with cleaning door 17.Above-mentioned hothouse is divided into heating clamber 1A and cooling chamber 1B, and wherein heating clamber is set at prebake, oven dry respectively according to the needs of technology, recovery and capable and experienced 5 class heating clambers.Described prebake, oven dry, recovery, capable and experienced heating clamber and cooling chamber need the time of stop therein according to the speed and the wet stock of guipure, determine all kinds of hothouses 105 ℃ of-30 ℃ of different heating-up temperatures and quantity.For example the prebake heating clamber, the oven dry heating clamber, recovery heating clamber, capable and experienced heating clamber and cooling chamber respectively are 2.The air circulation system of heating clamber divides or the circulatory system or the from top to bottom circulatory system from the bottom to top, and the circulatory system of adjacent heating clamber is that different i.e. two kinds of circulatory systems are to be provided with at interval.
See Fig. 2 and Fig. 3, the vertical dividing plate 11 and the lateral partitions 12 that are equipped with in all heating clamber 1A are divided into two spaces with heating clamber top, wherein a space is the dry place E that foraminous conveyer is set, upper and lower two-layer 5-1, the 5-2 branch of foraminous conveyer 5 is in lateral partitions, and about in the of 12 both sides, and another space is air channel F.Be provided with the heater 14 that cuts off air channel F at the air channel of heating clamber F middle part, heater 14 is a steam heater, has steam inlet 15 and condensation-water drain 16.In the heating clamber 1A and the inlet side that is in heater 14 is provided with drawable type and keeps off grey filter screen 13.The dehumidification tube 1A-2 that the corresponding position, top of heating clamber 1A is provided with air-introduced machine 18-1, the additional mouthful 1A-1 of new wind and is connected with outside hydrofuge house steward 9, the part of corresponding blower fan 18-1 discharge pipe is the orifice plate 11-1 that is communicated with discharge pipe and top, air channel on the vertical dividing plate 11, vertically on the dividing plate 11 between the upper strata of corresponding foraminous conveyer 5 and the lateral partitions 12 part in space be the orifice plate 11-2 that is communicated with this space and bottom, air channel.
See Fig. 2, the air circulation system from the bottom to top that described heating clamber 1A adopts, then the air inlet of its air-introduced machine 18-1 is in the dry place E, new wind replenishes a mouthful 1A-1 and communicates with F top, air channel, dehumidification tube 1A-2 communicates with dry place E, drawable type keeps off the top that grey filter screen 13 is arranged on heater 14, air pass from the bottom to top foraminous conveyer 5 upper strata 5-1, through air-introduced machine 18-1, the orifice plate 11-1, the drawable type that pass vertical dividing plate 11 tops keep off the orifice plate 11-2 of grey filter screen 13, heater 14, vertical dividing plate 11 bottoms, the upper strata of passing foraminous conveyer 5 again circulates.
See Fig. 3, the air circulation system from top to bottom that described heating clamber 1A adopts, then the air inlet of its air-introduced machine 18-1 is arranged in the top, air channel, new wind replenishes a mouthful 1A-1 and communicates with dry place E, dehumidification tube 1A-2 communicates with the bottom, air channel, drawable type keeps off the below that grey filter screen 13 is arranged on heater 14, and air circulation is passed the upper strata 5-1 of foraminous conveyer 5 from top to bottom.
See Fig. 4, the vertical dividing plate 11 and the lateral partitions 12 that are provided with in the described cooling chamber 1B are divided into two spaces with cooling chamber top, and wherein a space is the dry place E that foraminous conveyer is set, and another space is air channel F; Upper and lower two-layer 5-1, the 5-2 branch of foraminous conveyer 5 is in lateral partitions, and about in the of 12 both sides, the corresponding position, top of cooling chamber 1B is provided with air-introduced machine 18-2 and new wind replenishes a mouthful 1A-1, humid air is discharged by the air-introduced machine 18-2 of this chamber, on the vertical dividing plate 11 between the upper strata of corresponding foraminous conveyer 5 and the lateral partitions 12 part in space be the orifice plate 11-2 that is communicated with this space and F-2 bottom, air channel.The air inlet of the air-introduced machine 18-2 of cooling chamber 1B is arranged in the dry place E, and new wind replenishes a mouthful 1A-1 and communicates with air channel F, and air circulation is passed the upper strata 5-1 of foraminous conveyer 5 from the bottom to top.
Wet stock mixes the laggard feed bin of going into by mixer, enters the comminutor granulation again, sends into the drying machine people then and transmits on the guipure; successively by prebake, oven dry; recovery, capable and experienced heating clamber and cooling chamber, classified again sieve screening becomes product after spraying an amount of spices.
Claims (7)
1, a kind of flavoring granulation drying equipment has band drier (1), it is characterized in that: the feed end of band drier (1) is provided with mixer (2), feed bin (3) and comminutor (4), and discharge end is provided with classifying screen (6); The discharging opening of above-mentioned mixer (2) is facing to the charging aperture of feed bin (3), the discharging opening of feed bin (3) is facing to the charging aperture of comminutor (4), the discharging opening of comminutor (4) is facing to the top of drying machine foraminous conveyer (5), and the end of foraminous conveyer (5) is facing to the charging aperture of classifying screen (6); Foraminous conveyer (5) is dragged by transmission device (10) by motor; Described band drier is provided with at least 5 hothouses, the dividing plate of adjacent hothouse is provided with the opening that allows foraminous conveyer and shop material thereon to pass through, each hothouse is furnished with independently air circulation system and dehumidification system, above-mentioned hothouse is divided into two kinds of heating clamber (1A) and cooling chambers (1B), the air circulation system of heating clamber or air circulation system or the from top to bottom circulatory system from the bottom to top, the air circulation system of adjacent heating clamber are that different i.e. two kinds of circulatory systems are to be provided with at interval.
2, flavoring granulation drying equipment according to claim 1, it is characterized in that: the vertical dividing plate (11) and the lateral partitions (12) that are equipped with in all heating clambers (1A) are divided into two spaces with heating clamber top, wherein a space is the dry place (E) that foraminous conveyer (6) are set, upper and lower two-layer (5-1,5-2) branch of foraminous conveyer (5) is in lateral partitions (12) both sides up and down, and another space is air channel (F); Be provided with the heater (14) that cuts off air channel (F) at middle part, the air channel of heating clamber (F), the dehumidification tube (1A-2) that the corresponding position, top of heating clamber (1A) is provided with air-introduced machine (18-1), new wind additional mouthful (1A-1) and is connected with outside hydrofuge house steward (9), the part that vertical dividing plate (11) is gone up corresponding blower fan (18-1) discharge pipe is the orifice plate (11-1) that is communicated with discharge pipe and top, air channel, vertical dividing plate (11) upward between upper strata and the lateral partitions (12) of corresponding foraminous conveyer (5) part in space be the orifice plate (11-2) that is communicated with this space and bottom, air channel.
3, flavoring granulation drying equipment according to claim 2 is characterized in that: in the described heating clamber (1A) and the inlet side that is in heater (14) is provided with drawable type and keeps off grey filter screen (13).
4, flavoring granulation drying equipment according to claim 3, it is characterized in that: the air circulation system from the bottom to top that described heating clamber (1A) adopts, then the air inlet of its air-introduced machine (18-1) is in the dry place (E), new wind replenishes mouthful (1A-1) and communicates with top, air channel (F), dehumidification tube (1A-2) communicates with dry place (E), and air circulation is passed the upper strata (5-1) of foraminous conveyer (5) from the bottom to top; The air circulation system from top to bottom that described heating clamber (1A) adopts, then the air inlet of its air-introduced machine (18-1) is arranged in the top, air channel (F), new wind replenishes mouthful (1A-1) and communicates with dry place (E), dehumidification tube (1A-2) communicates with the bottom, air channel, and air circulation is passed the upper strata (5-1) of foraminous conveyer (5) from top to bottom.
5, flavoring granulation drying equipment according to claim 1, it is characterized in that: the vertical dividing plate (11) and the lateral partitions (12) that are provided with in the described cooling chamber (1B) are divided into two spaces with cooling chamber top, wherein a space is the dry place (E) that foraminous conveyer is set, and another space is air channel (F); Upper and lower two-layer (5-1,5-2) branch of foraminous conveyer (5) is in lateral partitions (12) both sides up and down, the corresponding position, top of cooling chamber (1B) is provided with air-introduced machine (18-2) and new wind replenishes mouthful (1B-1), humid air is discharged by the air-introduced machine (18-2) of this chamber, and the part in space is the orifice plate (11-2) that is communicated with this space and bottom, air channel between the upper strata that vertical dividing plate (11) is gone up corresponding foraminous conveyer (5) and the lateral partitions (12).
6, flavoring granulation drying equipment according to claim 5, it is characterized in that: the air inlet of the air-introduced machine (18-2) of described cooling chamber (1B) is arranged in the dry place (E), new wind replenishes mouthful (1A-1) and communicates with air channel (F), and air circulation is passed the upper strata (5-1) of foraminous conveyer (5) from the bottom to top.
7, flavoring granulation drying equipment according to claim 1, it is characterized in that: at least one end is provided with deashing device (7) in the beginning of described drying machine foraminous conveyer (5), the last two ends, and described deashing device is an electric rolling formula brush.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200620134277 CN200968763Y (en) | 2006-11-06 | 2006-11-06 | Seasoner pelletization drying apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200620134277 CN200968763Y (en) | 2006-11-06 | 2006-11-06 | Seasoner pelletization drying apparatus |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN200968763Y true CN200968763Y (en) | 2007-10-31 |
Family
ID=38968334
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 200620134277 Expired - Fee Related CN200968763Y (en) | 2006-11-06 | 2006-11-06 | Seasoner pelletization drying apparatus |
Country Status (1)
| Country | Link |
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| CN (1) | CN200968763Y (en) |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102538421A (en) * | 2012-02-29 | 2012-07-04 | 兰州奇正粉体装备技术有限公司 | Method and device for drying by heating and dehydrating |
| CN103851888A (en) * | 2014-03-06 | 2014-06-11 | 江苏海狮机械集团有限公司 | Bedding drying device |
| CN103868335A (en) * | 2012-12-11 | 2014-06-18 | 蒋小华 | Three-section paper tube drying machine |
| CN105627713A (en) * | 2016-02-17 | 2016-06-01 | 常州市一红干燥设备有限公司 | Belt type drier |
| CN106839730A (en) * | 2017-03-07 | 2017-06-13 | 江苏牧羊控股有限公司 | A kind of belt drying cooler |
| CN110513993A (en) * | 2018-05-22 | 2019-11-29 | 云南卓一食品有限公司 | A kind of bacterium bone fresh seasoning production system |
| CN110663969A (en) * | 2019-10-09 | 2020-01-10 | 山东天力能源股份有限公司 | Drying device and drying method |
| CN116020576A (en) * | 2021-10-27 | 2023-04-28 | 中国石油化工股份有限公司 | Inorganic oxide forming and drying integrated equipment and preparation method of inorganic oxide spherical particles |
-
2006
- 2006-11-06 CN CN 200620134277 patent/CN200968763Y/en not_active Expired - Fee Related
Cited By (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102538421A (en) * | 2012-02-29 | 2012-07-04 | 兰州奇正粉体装备技术有限公司 | Method and device for drying by heating and dehydrating |
| CN102538421B (en) * | 2012-02-29 | 2014-05-14 | 兰州奇正粉体装备技术有限公司 | Method and device for drying by heating and dehydrating |
| CN103868335A (en) * | 2012-12-11 | 2014-06-18 | 蒋小华 | Three-section paper tube drying machine |
| CN103868335B (en) * | 2012-12-11 | 2015-09-09 | 蒋小华 | A kind of syllogic Paper tube drier machine |
| CN103851888A (en) * | 2014-03-06 | 2014-06-11 | 江苏海狮机械集团有限公司 | Bedding drying device |
| CN103851888B (en) * | 2014-03-06 | 2016-04-06 | 江苏海狮机械集团有限公司 | Bed clothes drying unit |
| CN105627713A (en) * | 2016-02-17 | 2016-06-01 | 常州市一红干燥设备有限公司 | Belt type drier |
| CN105627713B (en) * | 2016-02-17 | 2018-12-04 | 江苏太阳臣干燥科技有限公司 | A kind of band drier |
| CN106839730A (en) * | 2017-03-07 | 2017-06-13 | 江苏牧羊控股有限公司 | A kind of belt drying cooler |
| CN106839730B (en) * | 2017-03-07 | 2019-07-26 | 江苏牧羊控股有限公司 | A kind of belt drying cooler |
| CN110513993A (en) * | 2018-05-22 | 2019-11-29 | 云南卓一食品有限公司 | A kind of bacterium bone fresh seasoning production system |
| CN110513993B (en) * | 2018-05-22 | 2020-08-28 | 云南卓一食品有限公司 | Fresh fungus bone seasoning production system |
| CN110663969A (en) * | 2019-10-09 | 2020-01-10 | 山东天力能源股份有限公司 | Drying device and drying method |
| CN116020576A (en) * | 2021-10-27 | 2023-04-28 | 中国石油化工股份有限公司 | Inorganic oxide forming and drying integrated equipment and preparation method of inorganic oxide spherical particles |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| EE01 | Entry into force of recordation of patent licensing contract |
Assignee: Changzhou Xianfeng drying equipment Co., Ltd. Assignor: Xie Hongqing Contract record no.: 2010320000286 Denomination of utility model: Seasoner pelletization drying apparatus Granted publication date: 20071031 License type: Exclusive License Record date: 20100323 |
|
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20071031 Termination date: 20121106 |