CN205245751U - Gardenia is drying system for extract product - Google Patents
Gardenia is drying system for extract product Download PDFInfo
- Publication number
- CN205245751U CN205245751U CN201520900570.6U CN201520900570U CN205245751U CN 205245751 U CN205245751 U CN 205245751U CN 201520900570 U CN201520900570 U CN 201520900570U CN 205245751 U CN205245751 U CN 205245751U
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- China
- Prior art keywords
- hot
- flue
- heat exchanger
- exchanger tube
- drying system
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- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
The utility model discloses a gardenia is drying system for extract product aims at providing the gardenia is drying system for extract product that energy -conservation is effectual. It includes hot -blast furnace, spray drier, chimney, flue fan and air inlet machine, the hot air exitus of hot -blast furnace and spray drier's hot -blast entry linkage, the air intake of hot -blast furnace is connected with preheating device through the intake stack, just the air inlet machine sets up on the intake stack, the outlet flue of hot -blast furnace passes through the flue to be connected with the chimney, just the flue fan sets up on the flue, preheating device includes the heat exchange tube, and holds the sealed box of heat exchange tube, the intake stack is connected with the air outlet of heat exchange tube, the air intake of heat exchange tube stretches out sealed box and the tip is provided with air cleaner, sealed box sets up on the flue, just lies in between flue fan and the hot -blast furnace, and the flue gas of messenger's hot -blast furnace is flowed through and is sealed up box and the exchange of heat exchange tube formation heat. The utility model discloses heat utilization efficiency is high.
Description
Technical field
The utility model relates to drying equipment technical field, especially relates to a kind of capejasmine extract drying system.
Background technology
The thermal source adopting in the dry production process of traditional capejasmine extract spraying comprises: steam, conduction oil, electrical heating, hot-blast stove etc., the effect of various thermals source is the hot blast that heat drying is used, and energy consumption is the important factor in order of the efficient operation of whole drying system and production cost. In large-scale drying system, hot-blast stove heating system is a kind of mode generally adopting, and this system thermal utilization rate is limited, and thermal losses is large. How reducing energy consumption, reduce operating cost, is the common problem of paying close attention to of equipment manufacturer and user, is also the trend of the times under country's " energy-saving and emission-reduction " policy.
In addition, traditional technological improvement is all to go to consider from hot-blast stove body, and room for promotion is limited, and transformation difficulty is large.
Utility model content
The utility model has overcome shortcoming of the prior art, provides a kind of efficiency of utilization high, the capejasmine extract drying system of good energy-conserving effect.
In order to solve the problems of the technologies described above, the utility model is achieved through the following technical solutions:
A kind of capejasmine extract drying system, comprises hot-blast stove, spray dryer, chimney, flue blower fan and air inlet fan; The hot-blast outlet of described hot-blast stove is connected with the hot-wind inlet of spray dryer, and the air inlet of described hot-blast stove is connected with preheating device by intake stack, and described air inlet fan is arranged on intake stack; The outlet flue of described hot-blast stove is connected with chimney by flue, and described flue blower fan is arranged on flue; Described preheating device comprises heat exchanger tube, and holds the seal case of described heat exchanger tube; Described intake stack is connected with the air outlet of heat exchanger tube, and the air inlet of described heat exchanger tube stretches out seal case and end is provided with air cleaner; Described seal case is arranged on flue and between flue blower fan and hot-blast stove, makes the smoke gas flow of hot-blast stove form heat exchange through seal case and heat exchanger tube.
Preferably, described air cleaner adopts just medium effeciency filter of nonwoven.
Preferably, described heat exchanger tube adopts fin heat exchange pipe.
Preferably, the first medium effeciency filter of described nonwoven and heat exchanger tube are with bolts.
Preferably, described seal case adopts insulation material to make.
Compared with prior art, the utlity model has following advantage:
The utility model adopts high-temperature flue gas that hot-blast stove flue discharges to carry out preheating to dry with air intake, has increased the temperature of air intake, reduces the heat demand of hot-blast stove; Reduce the temperature of flue gas, reduced hot-blast stove thermal loss; Comprehensively can reduce the caloric value of hot-blast stove, reduce the use amount of primary energy, energy-saving and emission-reduction, disposable little cost drops into, and energy economy & environment is benefited for a long time. Can well be applied to capejasmine extract sprays in dry and other similar production processes.
Brief description of the drawings
In order to be illustrated more clearly in the utility model embodiment or technical scheme of the prior art, to the accompanying drawing of required use in embodiment or description of the Prior Art be briefly described below, apparently, accompanying drawing in the following describes is only embodiment more of the present utility model, for those of ordinary skill in the art, do not paying under the prerequisite of creative work, can also obtain according to these accompanying drawings other accompanying drawing.
Fig. 1 is schematic diagram of the present utility model.
Detailed description of the invention
Below in conjunction with the accompanying drawing in the utility model embodiment, the technical scheme in the utility model embodiment is clearly and completely described, obviously, described embodiment is only the utility model part embodiment, instead of whole embodiment. Based on the embodiment in the utility model, those of ordinary skill in the art are not paying the every other embodiment obtaining under creative work prerequisite, all belong to the scope of the utility model protection.
Capejasmine extract drying system shown in Fig. 1, comprises hot-blast stove 1, spray dryer 2, chimney 3, flue blower fan 4 and air inlet fan 5; The hot-blast outlet of described hot-blast stove 1 is connected with the hot-wind inlet of spray dryer 2, and the air inlet of described hot-blast stove 1 is connected with preheating device 7 by intake stack 6, and described air inlet fan 5 is arranged on intake stack 6; The outlet flue of described hot-blast stove 1 is connected with chimney 3 by flue 8, and described flue blower fan 4 is arranged on flue 8; Described preheating device 7 comprises heat exchanger tube 71, and holds the seal case 72 of described heat exchanger tube 71; Described intake stack 6 is connected with the air outlet of heat exchanger tube 71, and the air inlet of described heat exchanger tube 71 stretches out seal case 72 and end is provided with air cleaner 9; Described seal case 72 is arranged on flue 8 and between flue blower fan 4 and hot-blast stove 1, makes the smoke gas flow of hot-blast stove 1 form heat exchange through seal case 72 and heat exchanger tube 71.
Wherein, described air cleaner 9 preferably adopts just medium effeciency filter of nonwoven. Described heat exchanger tube 71 preferably adopts the high fin heat exchange pipe 71 of heat exchange efficiency. The first medium effeciency filter of described nonwoven and heat exchanger tube 71 are preferably with bolts, are convenient to dismounting. Described seal case 72 adopts insulation material to make, and reduces heat radiation loss.
The utility model adopts high-temperature flue gas that hot-blast stove flue discharges to carry out preheating to dry with air intake, has increased the temperature of air intake, reduces the heat demand of hot-blast stove; Reduce the temperature of flue gas, reduced hot-blast stove thermal loss; Comprehensively can reduce the caloric value of hot-blast stove, reduce the use amount of primary energy, energy-saving and emission-reduction, disposable little cost drops into, and energy economy & environment is benefited for a long time. Can well be applied to capejasmine extract sprays in dry and other similar production processes.
The foregoing is only preferred embodiment of the present utility model; not in order to limit the utility model; all within spirit of the present utility model and principle, any amendment of doing, be equal to replacement, improvement etc., within all should being included in protection domain of the present utility model.
Claims (5)
1. a capejasmine extract drying system, comprises hot-blast stove, spray dryer, chimney, flue blower fan and air inlet fan; It is characterized in that: the hot-blast outlet of described hot-blast stove is connected with the hot-wind inlet of spray dryer, and the air inlet of described hot-blast stove is connected with preheating device by intake stack, and described air inlet fan is arranged on intake stack; The outlet flue of described hot-blast stove is connected with chimney by flue, and described flue blower fan is arranged on flue; Described preheating device comprises heat exchanger tube, and holds the seal case of described heat exchanger tube; Described intake stack is connected with the air outlet of heat exchanger tube, and the air inlet of described heat exchanger tube stretches out seal case and end is provided with air cleaner; Described seal case is arranged on flue and between flue blower fan and hot-blast stove, makes the smoke gas flow of hot-blast stove form heat exchange through seal case and heat exchanger tube.
2. capejasmine extract drying system according to claim 1, is characterized in that: described air cleaner adopts just medium effeciency filter of nonwoven.
3. capejasmine extract drying system according to claim 1 and 2, is characterized in that: described heat exchanger tube adopts fin heat exchange pipe.
4. capejasmine extract drying system according to claim 2, is characterized in that: the first medium effeciency filter of described nonwoven and heat exchanger tube are with bolts.
5. according to the capejasmine extract drying system described in claim 1,2 or 4, it is characterized in that: described seal case adopts insulation material to make.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520900570.6U CN205245751U (en) | 2015-11-12 | 2015-11-12 | Gardenia is drying system for extract product |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520900570.6U CN205245751U (en) | 2015-11-12 | 2015-11-12 | Gardenia is drying system for extract product |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205245751U true CN205245751U (en) | 2016-05-18 |
Family
ID=55944821
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520900570.6U Expired - Fee Related CN205245751U (en) | 2015-11-12 | 2015-11-12 | Gardenia is drying system for extract product |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205245751U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107687747A (en) * | 2017-10-09 | 2018-02-13 | 志圣科技（广州）有限公司 | Etc. speed heating and cooling baking oven |
-
2015
- 2015-11-12 CN CN201520900570.6U patent/CN205245751U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107687747A (en) * | 2017-10-09 | 2018-02-13 | 志圣科技（广州）有限公司 | Etc. speed heating and cooling baking oven |
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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 | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160518 Termination date: 20171112 |