CN208091116U - A kind of sodium benzoate production drying system - Google Patents
A kind of sodium benzoate production drying system Download PDFInfo
- Publication number
- CN208091116U CN208091116U CN201820200781.2U CN201820200781U CN208091116U CN 208091116 U CN208091116 U CN 208091116U CN 201820200781 U CN201820200781 U CN 201820200781U CN 208091116 U CN208091116 U CN 208091116U
- Authority
- CN
- China
- Prior art keywords
- drying drum
- drainpipe
- heating boiler
- sodium benzoate
- drying system
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
Landscapes
- Drying Of Solid Materials (AREA)
- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
Abstract
The utility model discloses a kind of sodium benzoates to produce drying system, including drying drum and heating boiler, drying drum inner space are connect with heating boiler by air inlet pipe, and the vapor in heating boiler is entered by air inlet pipe inside drying drum;Drainpipe is additionally provided in the drying drum, the drainpipe is connect by heat-exchanger pump with the heating boiler.A kind of sodium benzoate of the utility model produces drying system, by the way that drainpipe is arranged in drying drum, the distilled water generated in drying drum is imported by heat-exchanger pump in heating boiler, distilled water ebuillition of heated is generated vapor by heating boiler, enter drying drum by air inlet pipe, vapor enters in drying drum to generate draught head and be also beneficial to distilled water to be discharged by drainpipe, to realize the cycle of water, avoids water resource waste and environmental pollution caused by being arranged outside distilled water.A kind of sodium benzoate production drying system of the utility model has environment protecting good, the high advantage of water utilization rate.
Description
Technical field
It is good more particularly, to a kind of environment protecting the utility model is related to a kind of sodium benzoate production equipment, water resource profit
Drying system is produced with the high sodium benzoate of rate.
Background technology
When the sodium benzoate production of the prior art, sodium benzoate drying makes its surface using using the heating of drums inside steam
Reach certain temperature, roller rotation affixes material in hopper makes its moisture evaporation reach dried material after leaving fluid feed slot
Purpose.However, steam carries out heat exchange in drums inside generates certain distilled water, drums inside can keep certain liquid level,
Superfluous water is discharged, and causes water resource waste to be also easy pollution environment with unexpected bat.
Therefore, it is necessary to propose a kind of improve to overcome the defect of traditional technology.
Utility model content
It is good that the technical problem to be solved by the utility model is to provide a kind of environment protectings, the high benzene first of water utilization rate
Sour sodium produces drying system.
To achieve the goals above, a kind of sodium benzoate production drying system of the utility model uses following technical scheme:
A kind of sodium benzoate production drying system, including drying drum and heating boiler, the drying drum inner space
It is connect by air inlet pipe with the heating boiler, the vapor in the heating boiler enters the drying by the air inlet pipe
Drums inside;Wherein:Drainpipe is additionally provided in the drying drum, the drainpipe passes through heat-exchanger pump and the heating boiler
Connection.
As a kind of perferred technical scheme, the drainpipe includes fixing end and free end;The fixing end with it is described
The axis of rolling of drying drum is arranged in parallel, and the free end is freely positioned over inside the drying drum.
As a kind of further preferred technical solution, the drainpipe is hose.
As a kind of technical solution still more preferably, the free end of the drainpipe is provided with clump weight.
As another further preferred technical solution, the drainpipe fixing end is connected by pipeline and the heat-exchanger pump
It connects.
As a kind of technical solution still more preferably, the heating boiler includes hot water storgae, the heat-exchanger pump and institute
Hot water storgae is stated to connect also by pipeline.
A kind of sodium benzoate production drying system of the utility model will be done by the way that drainpipe is arranged in drying drum
The distilled water generated in dry roller is imported by heat-exchanger pump in heating boiler, and distilled water ebuillition of heated is generated water and steamed by heating boiler
Gas enters drying drum by air inlet pipe, and vapor, which enters in drying drum to generate draught head and be also beneficial to distilled water, passes through row
Water pipe is discharged, and to realize the cycle of water, avoids water resource waste and environmental pollution caused by being arranged outside distilled water.The utility model
A kind of sodium benzoate production drying system have environment protecting it is good, the high advantage of water utilization rate.
Description of the drawings
Fig. 1 is the structural schematic diagram that a kind of sodium benzoate of the utility model produces drying system specific implementation mode.
Fig. 2 is the middle dry rolling that a kind of sodium benzoate of the utility model shown in Fig. 1 produces drying system specific implementation mode
Cylinder internal structure schematic diagram.
Specific implementation mode
Below in conjunction with the accompanying drawings, a kind of concrete structure of sodium benzoate production drying system of the utility model is described in detail.
As shown in Figures 1 and 2, the utility model a kind of sodium benzoate produce drying system, including drying drum 1 and add
The inner space of heat boiler 2, drying drum 1 is connected to heating boiler 2 by air inlet pipe 3, and the vapor in heating boiler 2 passes through
Air inlet pipe 3 enters inside drying drum, and drainpipe 4 is additionally provided in drying drum 1, and drainpipe 4 passes through heat-exchanger pump 5 and heating
Boiler 2 connects.The distilled water in drying drum 1 can be discharged for drainpipe 4, heated into heating boiler 2 and generate vapor, real
Existing water cycle, avoids water resource waste and environmental pollution caused by distilled water discharge.
As shown in Figures 1 and 2, drainpipe 4 includes fixing end 4a and free end 4b, the rolling of fixing end 4a and drying drum 1
Moving axis is arranged in parallel, and free end 4b is freely positioned over inside drying drum 1, and by gravity, the free end 4b of drainpipe 4 is always
Positioned at the lower position of drying drum 1, it is ensured that distilled water is discharged.
Preferably, drainpipe 4 is hose, and when drying drum 1 rolls, free end 4b is always positioned at drying drum
Lower position in 1.For the weight of enlarged free end 4b, as shown in Figures 1 and 2, the free end 4b of drainpipe 4 is additionally provided with
Clump weight 6.
As shown in Figure 1, the fixing end 4a of drainpipe 4 is connected to by pipeline 7 with heat-exchanger pump 5.
Preferably, heating boiler can be provided with hot water storgae, and heat-exchanger pump is connect with hot water storgae by pipeline, will be steamed
Distilled water imports in hot water storgae, is entered inside heating boiler by hot water storgae.
A kind of sodium benzoate production drying system of the utility model will be done by the way that drainpipe is arranged in drying drum
The distilled water generated in dry roller is imported by heat-exchanger pump in heating boiler, and distilled water ebuillition of heated is generated water and steamed by heating boiler
Gas enters drying drum by air inlet pipe, and vapor, which enters in drying drum to generate draught head and be also beneficial to distilled water, passes through row
Water pipe is discharged, and to realize the cycle of water, avoids water resource waste and environmental pollution caused by being arranged outside distilled water.The utility model
A kind of sodium benzoate production drying system have environment protecting it is good, the high advantage of water utilization rate.
It these are only the utility model case study on implementation, be not intended to limit the utility model, as long as this field is common
Technical staff should all be included in described in claims according to equivalent modification or variation made by the utility model disclosure
Protection domain in.
Claims (6)
1. a kind of sodium benzoate produces drying system, including drying drum and heating boiler, the drying drum inner space with
The heating boiler is connected by air inlet pipe, and the vapor in the heating boiler enters the dry rolling by the air inlet pipe
Cylinder is internal;It is characterized in that:Drainpipe is additionally provided in the drying drum, the drainpipe passes through heat-exchanger pump and the heating
Boiler connects.
2. a kind of sodium benzoate according to claim 1 produces drying system, it is characterised in that:The drainpipe includes solid
Fixed end and free end;The fixing end and the axis of rolling of the drying drum are arranged in parallel, and the free end is freely positioned over institute
It states inside drying drum.
3. a kind of sodium benzoate according to claim 2 produces drying system, it is characterised in that:The drainpipe is soft
Pipe.
4. a kind of sodium benzoate according to claim 3 produces drying system, it is characterised in that:The freedom of the drainpipe
End is provided with clump weight.
5. a kind of sodium benzoate according to claim 2 produces drying system, it is characterised in that:The drainpipe fixing end
It is connect with the heat-exchanger pump by pipeline.
6. a kind of sodium benzoate according to claim 5 produces drying system, it is characterised in that:The heating boiler includes
Hot water storgae, the heat-exchanger pump are connect with the hot water storgae also by pipeline.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201820200781.2U CN208091116U (en) | 2018-02-06 | 2018-02-06 | A kind of sodium benzoate production drying system |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201820200781.2U CN208091116U (en) | 2018-02-06 | 2018-02-06 | A kind of sodium benzoate production drying system |
Publications (1)
Publication Number | Publication Date |
---|---|
CN208091116U true CN208091116U (en) | 2018-11-13 |
Family
ID=64063578
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201820200781.2U Active CN208091116U (en) | 2018-02-06 | 2018-02-06 | A kind of sodium benzoate production drying system |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN208091116U (en) |
-
2018
- 2018-02-06 CN CN201820200781.2U patent/CN208091116U/en active Active
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN202809328U (en) | Heat pump clothes dryer | |
CN205747818U (en) | Nonwoven production drying plant | |
CN201774913U (en) | High-efficiency energy-saving water-removing machine | |
CN207180179U (en) | One kind weaving dryer | |
CN102797064A (en) | Drying and adjusting process and device for viscose fibers | |
CN207035870U (en) | A kind of rotary kiln waste-heat recovery device | |
CN106017060A (en) | Intelligent textile dryer capable of recycling waste heat | |
CN206043233U (en) | A kind of waste-heat recovery device and Fryer | |
CN208091116U (en) | A kind of sodium benzoate production drying system | |
CN101564200B (en) | Tobacco redrying energy-saving technique and energy-saving device of redrying machine thereof | |
CN105444535A (en) | Drying room | |
CN202547286U (en) | Static drying oven for thermal sensitive materials | |
CN106839749A (en) | One kind is used for Reuse of Condensate from Drying Cylinder apparatus for reusing residual heat | |
CN206428486U (en) | A kind of industrial drying machine | |
CN206714039U (en) | A kind of heat energy recovery apparatus for Feed Manufacturing | |
CN206247749U (en) | A kind of medicinal material drying room | |
CN204881054U (en) | Pine formula drying -machine waste gas utilizes device | |
CN207035781U (en) | A kind of jeans drying production line that function is used with hot air circulation | |
CN203704613U (en) | Equipment for drying materials through air energy | |
CN202786549U (en) | Oven-drying and adjusting device for viscose fibers | |
CN207849918U (en) | Yarn air flow dryer | |
CN207180419U (en) | Heat exchanger for pneumatic conveying drying heat recovery | |
CN105806057A (en) | Drum drying device for bentonite | |
CN204806880U (en) | Dry tail gas waste heat recovery device of fibre | |
CN204401334U (en) | A kind of energy-saving clothes dryer |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
GR01 | Patent grant | ||
GR01 | Patent grant | ||
CP03 | Change of name, title or address |
Address after: 277212 No.1, Yinshan Industrial Park, economic development zone, Shanting District, Zaozhuang City, Shandong Province Patentee after: Shandong tongtaiweirun Food Technology Co., Ltd Address before: 277212 East waterlogged village, Cheng tou Town, Shan Ting District, Zaozhuang, Shandong Patentee before: SHANDONG TONGTAIWEIRUN FOOD SCIENCE TECH Co.,Ltd. |
|
CP03 | Change of name, title or address |