CN2392153Y - Machine for drying vegetables - Google Patents
Machine for drying vegetables Download PDFInfo
- Publication number
- CN2392153Y CN2392153Y CN 99229732 CN99229732U CN2392153Y CN 2392153 Y CN2392153 Y CN 2392153Y CN 99229732 CN99229732 CN 99229732 CN 99229732 U CN99229732 U CN 99229732U CN 2392153 Y CN2392153 Y CN 2392153Y
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- monoblock
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- distributor
- roller
- gas bag
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Abstract
The utility model relates to a machine for drying vegetables, which comprises at least a set of unit plants which comprise machine bodies, feeding devices, heating and drying devices and at least a set of humidity discharging device, wherein, the ends of the machine bodies of the unit plants on both sides are respectively provided with a charging device and a discharge port. The utility model has the advantages that the water content of vegetables dried by the machine for drying vegetables can be reduced within 5 percent from the original 90 percent, and the machine for drying vegetables solves the storing and preserving problems of seasonal and regional vegetables and has low energy consumption in the process of drying.
Description
The utility model relates to drying device field, particularly relates to a kind of drying machine that is applicable to provincialism and seasonal vegetable and some Chinese medicines, medicine materical crude slice.
Some provincialism and seasonal vegetable, as the water content of provincialism such as winter bamboo shoot, Chinese yam, garlic sheet, pumpkin, marine alga and seasonal vegetable class and some Chinese medicines, medicine materical crude slice up to 90%, to storage, fresh-keeping having difficulties, then can solve above-mentioned difficulties by oven dry, traditional drying unit ubiquity dehydration rate is not high, the shortcoming of storage and fresh-keeping difficulty and energy waste.
The purpose of this utility model is the vegetable dehydrator of a kind of good drying effect of design, energy savings.
The technical solution of the utility model is as follows: vegetable dehydrator, have at least one group of monoblock, monoblock has body, pay-off, heat drying device, at least one cover humidity-discharging device, body end in the monoblock of both sides is respectively arranged with feeder and discharging opening, the pay-off of monoblock have in body the feeding guipure and by the active live-roller of its coating and passive live-roller, the feeding guipure drives cycle operation by active live-roller and passive live-roller, and the motor that is arranged on the body top is connected with the active live-roller by chain or belt; The heat drying device has on circulating fan, heat exchanger, hot-air distributor, the hot blast gas bag under the gas bag and hot blast, the heat exchanger two ends communicate with circulating fan, hot-air distributor by pipeline respectively, hot-air distributor is the upper strata feeding guipure that transmits material between the gas bag under gas bag and the hot blast on the hot blast respectively by gas bag under gas bag and the hot blast on the pipeline connection hot blast under pipeline, the distributor on the distributor; Every group of humidity-discharging device has the hydrofuge airduct that communicates with internal body, and the hydrofuge airduct is connected with blast pipe by air-introduced machine; Adjacent monoblock is abutted against by body and is communicated; According to the material transmission direction, the active live-roller of preceding group of monoblock is in the passive live-roller top of back group monoblock.
In the aforementioned techniques scheme, can add following technical measures: gas bag has last plenum on the described hot blast, gas bag has following plenum under the hot blast, last plenum is relative with following plenum and be on the upper strata feeding guipure that transmits material, the below, on the distributor under pipeline and the distributor pipeline respectively along the two ends that extend plenum and following plenum, on plenum on the pipeline both sides under pipeline on the distributor and the distributor and following plenum, all be covered with the sealing wireway that is arranged in rows, on one end and the distributor under pipeline or the distributor pipeline communicate, on the bottom circumferential side wall of the above-mentioned relatively feeding guipure of sealing wireway, have gas port.
As adding further technical measures, aforesaid heat exchangers also is connected with air cleaner.
Aforementioned schemes of the present utility model also can remake following improvement: according to the material transmission direction, from first group of monoblock, have at least to be provided with brush net round brush between the monoblock at a place, before this brush net round brush is arranged on the active live-roller of group monoblock be in after organize between the feeding guipure of passive live-roller position of monoblock.
As aforesaid another technical measures: have at least two group monoblock, according to the material transmission direction, since second group of monoblock, have at least one group of monoblock also to be provided with heated air circulation device, heated air circulation device has the circulation airduct that communicates with internal body, and the circulation airduct connects with heat exchanger by circulating fan.
Be different from abovementioned technology, present technique measure: have one group of monoblock, feeder and discharging opening are separately positioned on this group monoblock body two ends, and have described pay-off, heat drying device and an at least one cover humidity-discharging device, also has heated air circulation device, heated air circulation device has the circulation airduct that communicates with internal body, and the circulation airduct connects with heat exchanger by circulating fan.
By aforementioned each scheme or measure, aforesaid heat exchanger is made up of the heat exchanger fin that is arranged in rows.
If in aforementioned schemes or the measure, have two groups of above monoblock, then can go improvements again, the aforesaid transmission speed of afterwards organizing feeding guipure in the monoblock is lower than preceding group.
According to the technical solution of the utility model and or the vegetable dehydrator of measure after implementing, its advantage is: the vegetables after the vegetable dehydrator oven dry, water content can be reduced in 5% by original 90%, solved the storage of seasonality and provincialism vegetables, fresh-keeping problem, and energy consumption is lower in drying course; In addition, can be according to the height of vegetables water content, the unit number of selected cell unit.
Below in conjunction with accompanying drawing in detail embodiment of the present utility model is described in detail, embodiment is preferably three groups of monoblock.
Fig. 1 is a structural representation of the present utility model;
Fig. 2 is the vertical view of Fig. 1;
Fig. 3 is the component locations graph of a relation at second, third group monoblock top among Fig. 1;
Fig. 4 is an A-A schematic diagram among Fig. 3;
Fig. 5 be among Fig. 3 B to schematic diagram;
Fig. 6 is the schematic diagram of gas bag on the hot blast among Fig. 1;
Fig. 7 is the upward view of Fig. 6;
Fig. 8 is the connection diagram of gas bag on distributor duct and the hot blast among Fig. 1;
Fig. 9 is the schematic diagram of gas bag under the hot blast among Fig. 1;
Figure 10 is the vertical view of Fig. 9;
Figure 11 is the connection diagram of gas bag under distributor duct and the hot blast among Fig. 1;
Figure 12 is the sealing wireway schematic diagram of the relative feeding guipure of circumference end wall among Fig. 6 or Fig. 9;
Figure 13 is the schematic diagram of brush net round brush among Fig. 1;
Figure 14 is the schematic diagram of heat exchanger among Fig. 1;
Figure 15 is the side view of Figure 14;
Figure 16 is the schematic diagram of heat exchanger fin for the vertical view of Figure 14.
Mark is expressed as follows in the accompanying drawing: 1-body, 2-feeder, 3-discharging opening, 4-feeding guipure, 41-initiatively live-rollers, 42-passive live-roller, 43-motor, 44-chain, 45-brush net round brush, 51-circulating fan, 52-heat exchanger, 521-heat exchanger fin, 53-hot-air distributor, pipeline on 531-distributor, pipeline under 532-distributor, 533-sealing wireway, 5331-gas port, gas bag on 54-hot blast, gas bag under 55-hot blast, 56-air cleaner, 541-upward plenums, 551-following plenum, 61-hydrofuge airduct, 62-air-introduced machine, 63-blast pipe, 7-circulation airduct.
Vegetable dehydrator, have three groups of monoblock, every group of monoblock has body 1, pay-off, the heat drying device, at least one cover humidity-discharging device, wherein according to the transmission direction that needs dry material, first group of monoblock has two cover humidity-discharging devices, second and the 3rd group has a cover humidity-discharging device, the side of the body 1 of first group of monoblock is provided with feeder 2, the side of the body 1 of second group of monoblock is provided with and discharging opening 3, pay-off have in body 1 feeding guipure 4 and by the active live-roller 41 of its coating and passive live-roller 42, feeding guipure 4 drives cycle operation by active live-roller 41 and passive live-roller 42, and the motor 43 at body 1 top is connected with active live-roller 41 by chain 44; The heat drying device has on circulating fan 51, thermal converter 52, hot-air distributor 53, the hot blast gas bag 55 under the gas bag 54 and hot blast, heat exchanger 52 two ends communicate with circulating fan 51, hot-air distributor 53 by pipeline respectively, heat exchanger 52 also is connected with air cleaner 56, and heat exchanger 52 is made up of the heat exchanger fin 521 that is arranged in rows.Hot-air distributor 53 is the upper strata feeding guipure 4 that transmits material between the gas bag 55 under gas bag 54 and the hot blast on the hot blast respectively by gas bag 55 under gas bag 54 and the hot blast on the 532 connection hot blasts of pipeline under pipeline on the distributor 531, the distributor; Every group of humidity-discharging device has the hydrofuge airduct 61 that communicates with body 1 inside, and hydrofuge airduct 61 is connected with blast pipe 63 by air-introduced machine 62; First and second group, second is abutted against by body 1 with the 3rd group of monoblock and is communicated; The active live-roller 41 of first and second group monoblock is in passive live-roller 42 tops of second and the 3rd group of monoblock respectively.
Be provided with brush net round brush 45 between first group and second group of monoblock, this brush net round brush 45 is arranged on the active live-roller 41 of first group of monoblock and is in 4 of the feeding guipures of passive live-roller 42 positions of second group of monoblock.The effect of brush net round brush 45 is and will be delivered on the feeding guipure of second group of monoblock down by the material brush that easily is bonded on the feeding guipure 4 owing to also have suitable moisture content after first group of drying.
Second group and the 3rd group of monoblock, also respectively be provided with heated air circulation device, heated air circulation device has the circulation airduct 7 that communicates with body 1 inside, and circulation airduct 7 connects with heat exchanger 52 by circulating fan 51.
The transmission speed of each motor 43 in first, second and third group monoblock reduces successively, thereby the transmission speed of feeding guipure 4 also reduces successively.
During work, start first group of monoblock earlier, the pay-off running, heat exchanger heats, circulating fan is carried hot-air, and hot blast is distributed to the upper and lower gas bag of hot blast by hot-air distributor, the upper and lower pipeline of distributor, add the material that needs drying from feeder, hot blast in the upper and lower gas bag of hot blast is laid the feeding guipure of material through the gas port directive of sealing wireway, hot-air and material carry out heat exchange in transmission, material water evaporates, damp-heat air by air-introduced machine through the air draught of hydrofuge airduct, from the blast pipe hydrofuge.Open second, third group monoblock in succession, dry running continuously.Because material is through first group of bake drying, most of moisture content evaporates, therefore the heating-up temperature that enters second and third group can suitably be turned down, all the other hot-airs are behind hydrofuge, the remaining air that has heat can be delivered to the upper and lower gas bag of hot blast by circulating fan, heat exchanger, hot-air distributor through the circulation airduct and utilize, to reach energy-saving effect, improve the thermal efficiency.The transfer rate of the feeding guipure of these three groups of monoblock reduces with multiple, the transfer rate ratio that is first, second and third group is 4: 2: 1, therefore the material thickness on second group of feeding guipure is first group 2 times, and the 3rd group material thickness is 4 times of first group, has embodied the production capacity of this drying machine thus.Material after the drying is from the 3rd group the distolateral discharge hole for discharge of body, and the water content of drying material this moment is reducing in 5% more than 90% from charge door.
It more than is most preferred embodiment of the present utility model.Certainly, the utility model also can be provided with embodiment according to the concrete water content of initial material, as the water content extra-high-speed, then can increase monoblock quantity; When hanging down as water content, can reduce monoblock quantity until one group, only need on this element unit, to be provided with simultaneously feeder and discharging opening this moment, and look concrete condition and on body, set up heated air circulation device, as the airduct that circulates is beneficial to make full use of the hot-air heat, enough humidity-discharging devices is set simultaneously to guarantee abundant hydrofuge.
Claims (8)
1, vegetable dehydrator, have at least one group of monoblock, monoblock has body, pay-off, heat drying device, at least one cover humidity-discharging device, body end in the monoblock of both sides is respectively arranged with feeder and discharging opening, it is characterized in that: the pay-off of monoblock have in body the feeding guipure and by the active live-roller of its coating and passive live-roller, the feeding guipure drives cycle operation by active live-roller and passive live-roller, and the motor that is arranged on the body top is connected with the active live-roller by chain or belt; The heat drying device has on circulating fan, heat exchanger, hot-air distributor, the hot blast gas bag under the gas bag and hot blast, the heat exchanger two ends communicate with circulating fan, hot-air distributor by pipeline respectively, hot-air distributor is the upper strata feeding guipure that transmits material between the gas bag under gas bag and the hot blast on the hot blast respectively by gas bag under gas bag and the hot blast on the pipeline connection hot blast under pipeline, the distributor on the distributor; Every group of humidity-discharging device has the hydrofuge airduct that communicates with internal body, and the hydrofuge airduct is connected with blast pipe by air-introduced machine; Adjacent monoblock is abutted against by body and is communicated; According to the material transmission direction, the active live-roller of preceding group of monoblock is in the passive live-roller top of back group monoblock.
2, vegetable dehydrator according to claim 1, it is characterized in that: gas bag has last plenum on the described hot blast, gas bag has following plenum under the hot blast, last plenum is relative with following plenum and be on the upper strata feeding guipure that transmits material, the below, on the distributor under pipeline and the distributor pipeline respectively along the two ends that extend plenum and following plenum, on plenum on the pipeline both sides under pipeline on the distributor and the distributor and following plenum, all be covered with the sealing wireway that is arranged in rows, on one end and the distributor under pipeline or the distributor pipeline communicate, on the bottom circumferential side wall of the above-mentioned relatively feeding guipure of sealing wireway, have gas port.
3, vegetable dehydrator according to claim 1 and 2 is characterized in that: described heat exchanger also is connected with air cleaner.
4, according to claim 1 or 2 or 3 described vegetable dehydrators, it is characterized in that: according to the material transmission direction, from first group of monoblock, have at least to be provided with brush net round brush between the monoblock at a place, before this brush net round brush is arranged on the active live-roller of group monoblock be in after organize between the feeding guipure of passive live-roller position of monoblock.
5, according to each described vegetable dehydrator in the claim 1～4, it is characterized in that: have at least two group monoblock, according to the material transmission direction, since second group of monoblock, have at least one group of monoblock also to be provided with heated air circulation device, heated air circulation device has the circulation airduct that communicates with internal body, and the circulation airduct connects with heat exchanger by circulating fan.
6, according to each described vegetable dehydrator in the claim 1～3, it is characterized in that: have one group of monoblock, feeder and discharging opening are separately positioned on this group monoblock body two ends, and have described pay-off, heat drying device and an at least one cover humidity-discharging device, also has heated air circulation device, heated air circulation device has the circulation airduct that communicates with internal body, and the circulation airduct connects with heat exchanger by circulating fan.
7, according to the described vegetable dehydrator of aforementioned each claim, it is characterized in that: described heat exchanger is made up of the heat exchanger fin that is arranged in rows.
8, require 6 described each described vegetable dehydrators according to the aforementioned right of removing, it is characterized in that: the transmission speed of feeding guipure is lower than preceding group in the group monoblock of described back.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 99229732 CN2392153Y (en) | 1999-10-23 | 1999-10-23 | Machine for drying vegetables |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 99229732 CN2392153Y (en) | 1999-10-23 | 1999-10-23 | Machine for drying vegetables |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2392153Y true CN2392153Y (en) | 2000-08-16 |
Family
ID=34018931
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 99229732 Expired - Fee Related CN2392153Y (en) | 1999-10-23 | 1999-10-23 | Machine for drying vegetables |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2392153Y (en) |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101878943A (en) * | 2010-06-11 | 2010-11-10 | 新疆农业科学院农业机械化研究所 | Continuous dehydrating machine |
| CN101907382A (en) * | 2010-08-20 | 2010-12-08 | 昆明理工大学 | Natural rubber drying system |
| CN101690607B (en) * | 2009-09-03 | 2011-05-18 | 陆文光 | Dehydrated vegetables continuous dryer |
| CN102183130A (en) * | 2010-12-20 | 2011-09-14 | 福建来康家食品发展有限公司 | Energy-saving dryer and drying method thereof |
| CN104990384A (en) * | 2015-07-24 | 2015-10-21 | 丽江心联欣粮油贸易有限公司 | Belt type drying machine special for moringa oleifera |
| CN105145794A (en) * | 2015-09-10 | 2015-12-16 | 安徽省葛根生产力促进中心有限公司 | Fruit drying machine using secondary liquid medium to transmit heat energy |
| CN105783471A (en) * | 2016-05-11 | 2016-07-20 | 江西省鑫纬业环保设备制造有限公司 | Electromagnetic heating tunnel type steel belt fluid bed dryer |
| CN106288722A (en) * | 2016-09-14 | 2017-01-04 | 江苏沙家浜医药化工装备股份有限公司 | Pneumatic drying device |
-
1999
- 1999-10-23 CN CN 99229732 patent/CN2392153Y/en not_active Expired - Fee Related
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101690607B (en) * | 2009-09-03 | 2011-05-18 | 陆文光 | Dehydrated vegetables continuous dryer |
| CN101878943A (en) * | 2010-06-11 | 2010-11-10 | 新疆农业科学院农业机械化研究所 | Continuous dehydrating machine |
| CN101907382A (en) * | 2010-08-20 | 2010-12-08 | 昆明理工大学 | Natural rubber drying system |
| CN102183130A (en) * | 2010-12-20 | 2011-09-14 | 福建来康家食品发展有限公司 | Energy-saving dryer and drying method thereof |
| CN104990384A (en) * | 2015-07-24 | 2015-10-21 | 丽江心联欣粮油贸易有限公司 | Belt type drying machine special for moringa oleifera |
| CN105145794A (en) * | 2015-09-10 | 2015-12-16 | 安徽省葛根生产力促进中心有限公司 | Fruit drying machine using secondary liquid medium to transmit heat energy |
| CN105783471A (en) * | 2016-05-11 | 2016-07-20 | 江西省鑫纬业环保设备制造有限公司 | Electromagnetic heating tunnel type steel belt fluid bed dryer |
| CN106288722A (en) * | 2016-09-14 | 2017-01-04 | 江苏沙家浜医药化工装备股份有限公司 | Pneumatic drying device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |