CN204987735U - Directly spout hot -blast eiderdown drying -machine of formula - Google Patents
Directly spout hot -blast eiderdown drying -machine of formula Download PDFInfo
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- CN204987735U CN204987735U CN201520680064.0U CN201520680064U CN204987735U CN 204987735 U CN204987735 U CN 204987735U CN 201520680064 U CN201520680064 U CN 201520680064U CN 204987735 U CN204987735 U CN 204987735U
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- hot
- blast
- inner chamber
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- 238000001035 drying Methods 0.000 title claims abstract description 9
- 239000002912 waste gas Substances 0.000 claims abstract description 23
- 239000007789 gas Substances 0.000 claims abstract description 12
- 238000010438 heat treatment Methods 0.000 claims abstract description 6
- 238000001816 cooling Methods 0.000 claims abstract description 4
- 239000002028 Biomass Substances 0.000 claims description 41
- 238000002485 combustion reaction Methods 0.000 claims description 21
- 238000002347 injection Methods 0.000 claims description 14
- 239000007924 injection Substances 0.000 claims description 14
- 239000011229 interlayer Substances 0.000 claims description 9
- 239000000446 fuel Substances 0.000 claims description 8
- 238000009423 ventilation Methods 0.000 claims description 8
- 239000002699 waste material Substances 0.000 claims description 8
- 230000008676 import Effects 0.000 claims description 7
- 238000002156 mixing Methods 0.000 claims description 4
- 238000005452 bending Methods 0.000 claims description 3
- 230000001105 regulatory effect Effects 0.000 claims description 3
- 238000002955 isolation Methods 0.000 description 4
- 239000010902 straw Substances 0.000 description 4
- 238000003915 air pollution Methods 0.000 description 2
- 238000007664 blowing Methods 0.000 description 2
- 230000008878 coupling Effects 0.000 description 2
- 238000010168 coupling process Methods 0.000 description 2
- 238000005859 coupling reaction Methods 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
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- Drying Of Solid Materials (AREA)
Abstract
The utility model provides a directly spout hot -blast eiderdown drying -machine of formula, including interior cavity, set up in the drive device of inner chamber external portion and set up in the agitated vessel of the internal portion of inner chamber, the external portion of inner chamber cover is equipped with outer cavity, and interior cavity top is provided with the burr that adds that passes outer cavity, and inner chamber side face is provided with the hot -blast air inlet that passes outer cavity, outer cavity bottom is provided with used heat gas air inlet, and outer cavity top is provided with the air exit, the clean hot air exitus of outside living beings hot -blast furnace is connected to hot -blast air inlet, and the exhaust outlet of outside living beings hot -blast furnace connects used heat gas air inlet, and negative -pressure air fan is connected to the air exit, eiderdown through in the hot -blast internal cavity of clean hot air exitus exhaust of living beings hot -blast furnace carries out drying process, utilizes the exhaust outlet of living beings hot -blast furnace to send the waste gas of living beings hot -blast furnace into the intermediate layer between interior cavity and the outer cavity simultaneously, the heating of the internal cavity of externally, and the waste gas after the cooling is taken out through negative -pressure air fan through outer cavity top air exit. And energy is saved.
Description
Technical field
The utility model relates to a kind of hot drying plant, is specifically related to a kind of direct injection hot-air down drier.
Background technology
Existing direct injection hot-air down drier carries out heating, drying by connecting outside biomass thermal wind furnace, and while biomass thermal wind furnace combustion fuel, can produce waste gas, waste gas, also with a large amount of heats, is discharged in air, wastes energy greatly.And in eider down drying course, a large amount of moistures can be produced, directly extracted out by negative-pressure air fan, moisture exhausting difficulty, easily produce negative pressure, and centre can be mingled with eider down, easily blocks air channel.
Utility model content
For prior art Problems existing, the utility model provides a kind of direct injection hot-air down drier, by forming interlayer at the outside sheathed outer chamber of the inner chamber body of dryer, is directly passed into by the waste gas of biomass thermal wind furnace in this interlayer, to inner chamber from external heat, economize energy greatly.Simultaneously, left bank is utilized to wet valve triple valve and right hydrofuge valve triple valve, cooperatively interact adjustment, alternately discharged by moisture, greatly provide moisture exhausting efficiency from inner chamber body both sides, and by coordinating every suede sieve plate and airhood door, isolation eider down, when both sides replace hydrofuge gas, alternately can dry to every suede sieve plate back and forth, the script eider down be adsorbed on suede sieve plate is blown back in inner chamber body, ensures that eider down can not block every suede sieve plate.
The technical solution of the utility model is: a kind of direct injection hot-air down drier, comprises inner chamber body, is arranged at the driving arrangement of inner chamber body outside and is arranged at the mixing plant of inner chamber body inside; Described inner chamber body outer cover is provided with outer chamber, and what inner chamber body top was provided through outer chamber adds burr, and inner chamber body side is provided through the hot blast air inlet of outer chamber; Be provided with waste hot gas air inlet bottom outer chamber, outer chamber top is provided with exhaust outlet; Hot blast air inlet connects the clean hot-blast outlet of outside biomass thermal wind furnace, and the waste gas outlet of outside biomass thermal wind furnace connects waste hot gas air inlet, and exhaust outlet connects negative-pressure air fan; The hot blast of being discharged by the clean hot-blast outlet of biomass thermal wind furnace carries out drying and processing to the eider down in inner chamber body, utilize the waste gas outlet of biomass thermal wind furnace that the waste gas of biomass thermal wind furnace is sent into the interlayer between inner chamber body and outer chamber simultaneously, heat from outside inner chamber body, the waste gas after cooling is extracted out by negative-pressure air fan through outer chamber top exhaust outlet.
Further, comprise be arranged at the inner chamber body left and right sides first half every suede sieve plate, seal two the airhood doors of the left and right sides every suede sieve plate and extraneous air respectively, be communicated with the ventilation shaft of two airhood door inside, described ventilation shaft is provided with left bank to wet valve triple valve and right hydrofuge valve triple valve, be provided with a hydrofuge suction opeing in the middle of two hydrofuge valve triple valves, hydrofuge suction opeing connects negative-pressure air fan; By regulating the import and export of hydrofuge valve triple valve, moisture is alternately discharged from inner chamber body both sides.
Further, described biomass thermal wind furnace comprises biomass combustion furnace, air blast, airduct; Described biomass combustion furnace top is provided with waste gas outlet and clean hot-blast outlet; Described airduct one end connects air blast, and the other end penetrates the S-shaped bending clean hot-blast outlet extending to biomass thermal wind furnace below biomass combustion furnace; The gas-heated of being discharged by air blast by biomass combustion furnace inner fuel combustion heating is sent to clean hot-blast outlet.
Further, the fuel of described biomass combustion furnace is stalk.Can the agriculture comparatively developed regions of extensive use, namely can solve the problem of the too much Air-pollution From Combustion environment of agricultural crop straw, the heat that straw burning produces can be made full use of again, saved the energy greatly.
The beneficial effects of the utility model are: provide a kind of direct injection hot-air down drier, by forming interlayer at the outside sheathed outer chamber of the inner chamber body of dryer, the waste gas of biomass thermal wind furnace is directly passed in this interlayer, to inner chamber from external heat, economize energy greatly.
Simultaneously, left bank is utilized to wet valve triple valve and right hydrofuge valve triple valve, cooperatively interact adjustment, moisture is alternately discharged from inner chamber body both sides, moisture exhausting efficiency is provided greatly, when regulate left bank wet the import and export of valve triple valve be two ventilating openings be communicated with ventilation shaft time, then regulate the import and export of right hydrofuge valve triple valve to be one and be communicated with extraneous air, one is the ventilating opening away from hydrofuge suction opeing, after being bled by negative-pressure air fan, the ventilating opening air inlet of extraneous air is communicated with from right hydrofuge valve triple valve, after passing into inner chamber body, the moisture in inner chamber body is driven to be circulated to hydrofuge suction opeing to discharge from the left bank valve triple valve that wets, vice versa, and moisture is alternately discharged from inner chamber body both sides.
In addition, by coordinating every suede sieve plate and airhood door, isolation eider down, when both sides replace hydrofuge gas, can to every the alternately blowing back and forth of suede sieve plate, the eider down be adsorbed on suede sieve plate is originally blown back in inner chamber body, ensures that eider down can not block every suede sieve plate.
Accompanying drawing explanation
Fig. 1 is the structural representation of a kind of direct injection hot-air down drier of the utility model;
Fig. 2 is the side view of a kind of direct injection hot-air down drier of the utility model;
Fig. 3 is the structural representation of living beings hot-blast stove.
In figure: 1. left bank wets valve triple valve, and 2. hydrofuge suction opeing, 3. adds burr, 4. right hydrofuge valve triple valve, 5. every suede sieve plate, 6. airhood door, 7. goes out burr, 8. dryer inner chamber body, 9. dryer outer chamber, 10. shaft, 11. stirring vanes, 12. bearing blocks, 13. shaft couplings, 14. drive motors, 15. exhaust outlets, 16. hot blast air inlets, 17. isolation sieve plates, 18. waste hot gas air inlets, 19. waste gas outlets, 20. clean hot-blast outlets, 21. fuel, 22. air blasts, 23. airducts.
Detailed description of the invention
Below in conjunction with accompanying drawing, the utility model is described further.
As shown in Figure 1, 2, a kind of direct injection hot-air down drier, comprise inner chamber body 8, be arranged at the driving arrangement of inner chamber body outside and be arranged at the mixing plant of inner chamber body inside, described driving arrangement comprises bearing block 12, shaft coupling 13, drive motors 14, and described mixing plant comprises shaft 10, stirring vane 11.Described inner chamber body 8 outer cover is provided with outer chamber 9, and what inner chamber body 8 top was provided through outer chamber 9 adds burr 3, and inner chamber body 8 side is provided through the hot blast air inlet 16 of outer chamber 9; Be provided with waste hot gas air inlet 18 bottom outer chamber 9, outer chamber 9 top is provided with exhaust outlet 15; Hot blast air inlet 16 connects the clean hot-blast outlet 20 of outside biomass thermal wind furnace, and the waste gas outlet 19 of outside biomass thermal wind furnace connects waste hot gas air inlet 18, and exhaust outlet 15 connects negative-pressure air fan; The hot blast of being discharged by the clean hot-blast outlet 20 of biomass thermal wind furnace carries out drying and processing to the eider down in inner chamber body 8, utilize the waste gas outlet 19 of biomass thermal wind furnace that the waste gas of biomass thermal wind furnace is sent into the interlayer between inner chamber body 8 and outer chamber 9 simultaneously, heat from outside to inner chamber body 8, the waste gas after cooling is extracted out by negative-pressure air fan through outer chamber 9 top exhaust outlet 15.By forming interlayer at the outside sheathed outer chamber of the inner chamber body of dryer, the waste gas of biomass thermal wind furnace is directly passed in this interlayer, to inner chamber from external heat, economize energy greatly.
As preferred embodiment, direct injection hot-air down drier comprise be arranged at inner chamber body 8 left and right sides first half every suede sieve plate 5, seal two the airhood doors 6 of the left and right sides every suede sieve plate and extraneous air respectively, be communicated with the ventilation shaft of two airhood door 6 inside, described ventilation shaft is provided with left bank to wet valve triple valve 1 and right hydrofuge valve triple valve 4, be provided with a hydrofuge suction opeing 2 in the middle of two hydrofuge valve triple valves, hydrofuge suction opeing 2 connects negative-pressure air fan; By regulating the import and export of hydrofuge valve triple valve, moisture is alternately discharged from inner chamber body both sides.Left bank is utilized to wet valve triple valve and right hydrofuge valve triple valve, cooperatively interact adjustment, moisture is alternately discharged from inner chamber body both sides, moisture exhausting efficiency is provided greatly, when regulate left bank wet the import and export of valve triple valve be two ventilating openings be communicated with ventilation shaft time, then regulate the import and export of right hydrofuge valve triple valve to be one and be communicated with extraneous air, one is the ventilating opening away from hydrofuge suction opeing, after being bled by negative-pressure air fan, the ventilating opening air inlet of extraneous air is communicated with from right hydrofuge valve triple valve, after passing into inner chamber body, the moisture in inner chamber body is driven to be circulated to hydrofuge suction opeing to discharge from the left bank valve triple valve that wets, vice versa, and moisture is alternately discharged from inner chamber body both sides.In addition, by coordinating every suede sieve plate and airhood door, isolation eider down, when both sides replace hydrofuge gas, can to every the alternately blowing back and forth of suede sieve plate, the eider down be adsorbed on suede sieve plate is originally blown back in inner chamber body, ensures that eider down can not block every suede sieve plate.
The wind furnace of biomass thermal described in the present embodiment comprises biomass combustion furnace, air blast 22, airduct 23; Described biomass combustion furnace top is provided with waste gas outlet 19 and clean hot-blast outlet 20; Described airduct 23 one end connects air blast 22, and the other end penetrates the S-shaped bending clean hot-blast outlet 20 extending to biomass thermal wind furnace below biomass combustion furnace; The gas-heated of being discharged by air blast by biomass combustion furnace inner fuel combustion heating is sent to clean hot-blast outlet.The fuel of biomass combustion furnace is stalk.Can the agriculture comparatively developed regions of extensive use, namely can solve the problem of the too much Air-pollution From Combustion environment of agricultural crop straw, the heat that straw burning produces can be made full use of again, saved the energy greatly.
The above is only preferred embodiment of the present utility model; be noted that for those skilled in the art; under the prerequisite not departing from the utility model principle; can also make some improvements and modifications, these improvements and modifications also should be considered as protection domain of the present utility model.
Claims (4)
1. a direct injection hot-air down drier, comprises inner chamber body (8), is arranged at the driving arrangement of inner chamber body outside and is arranged at the mixing plant of inner chamber body inside; It is characterized in that: described inner chamber body (8) outer cover is provided with outer chamber (9), what inner chamber body (8) top was provided through outer chamber (9) adds burr (3), and inner chamber body (8) side is provided through the hot blast air inlet (16) of outer chamber (9); Outer chamber (9) bottom is provided with waste hot gas air inlet (18), and outer chamber (9) top is provided with exhaust outlet (15); Hot blast air inlet (16) connects the clean hot-blast outlet (20) of outside biomass thermal wind furnace, the waste gas outlet (19) of outside biomass thermal wind furnace connects waste hot gas air inlet (18), and exhaust outlet (15) connects negative-pressure air fan; The hot blast of being discharged by the clean hot-blast outlet (20) of biomass thermal wind furnace carries out drying and processing to the eider down in inner chamber body (8), utilize the waste gas outlet (19) of biomass thermal wind furnace that the waste gas of biomass thermal wind furnace is sent into the interlayer between inner chamber body (8) and outer chamber (9) simultaneously, from outside to inner chamber body (8) heating, the waste gas after cooling is extracted out by negative-pressure air fan through outer chamber (9) top exhaust outlet (15).
2. a kind of direct injection hot-air down drier according to claim 1, it is characterized in that: comprise be arranged at inner chamber body (8) left and right sides first half every suede sieve plate (5), seal two the airhood doors (6) of the left and right sides every suede sieve plate and extraneous air respectively, be communicated with the ventilation shaft that two airhood doors (6) are inner, described ventilation shaft is provided with left bank to wet valve triple valve (1) and right hydrofuge valve triple valve (4), a hydrofuge suction opeing (2) is provided with in the middle of two hydrofuge valve triple valves, hydrofuge suction opeing (2) connects negative-pressure air fan, by regulating the import and export of hydrofuge valve triple valve, moisture is alternately discharged from inner chamber body both sides.
3. a kind of direct injection hot-air down drier according to claim 1, is characterized in that: described biomass thermal wind furnace comprises biomass combustion furnace, air blast (22), airduct (23); Described biomass combustion furnace top is provided with waste gas outlet (19) and clean hot-blast outlet (20); Described airduct (23) one end connects air blast (22), and the other end penetrates the S-shaped bending clean hot-blast outlet (20) extending to biomass thermal wind furnace below biomass combustion furnace; The gas-heated of being discharged by air blast by biomass combustion furnace inner fuel combustion heating is sent to clean hot-blast outlet.
4. a kind of direct injection hot-air down drier according to claim 3, is characterized in that: the fuel (21) of described biomass combustion furnace is stalk.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520680064.0U CN204987735U (en) | 2015-09-02 | 2015-09-02 | Directly spout hot -blast eiderdown drying -machine of formula |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520680064.0U CN204987735U (en) | 2015-09-02 | 2015-09-02 | Directly spout hot -blast eiderdown drying -machine of formula |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204987735U true CN204987735U (en) | 2016-01-20 |
Family
ID=55122096
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520680064.0U Expired - Fee Related CN204987735U (en) | 2015-09-02 | 2015-09-02 | Directly spout hot -blast eiderdown drying -machine of formula |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204987735U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105091528A (en) * | 2015-09-02 | 2015-11-25 | 徐州腾宇羽绒制品设备有限公司 | Direct injection type hot-wind down feather dryer |
| CN107478023A (en) * | 2017-07-31 | 2017-12-15 | 泉州科维嘉电力有限公司 | A kind of feed mixing machine device people with functions/drying |
-
2015
- 2015-09-02 CN CN201520680064.0U patent/CN204987735U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105091528A (en) * | 2015-09-02 | 2015-11-25 | 徐州腾宇羽绒制品设备有限公司 | Direct injection type hot-wind down feather dryer |
| CN105091528B (en) * | 2015-09-02 | 2017-07-21 | 徐州腾宇羽绒制品设备有限公司 | A kind of direct injection hot-air down drier |
| CN107478023A (en) * | 2017-07-31 | 2017-12-15 | 泉州科维嘉电力有限公司 | A kind of feed mixing machine device people with functions/drying |
| CN107478023B (en) * | 2017-07-31 | 2019-11-15 | 杨晨晖 | A feed mixing robot with drying function |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160120 Termination date: 20190902 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |