CN2485535Y - Thermal conducting oil-gas fluid drier - Google Patents
Thermal conducting oil-gas fluid drier Download PDFInfo
- Publication number
- CN2485535Y CN2485535Y CN 01224425 CN01224425U CN2485535Y CN 2485535 Y CN2485535 Y CN 2485535Y CN 01224425 CN01224425 CN 01224425 CN 01224425 U CN01224425 U CN 01224425U CN 2485535 Y CN2485535 Y CN 2485535Y
- Authority
- CN
- China
- Prior art keywords
- oil
- heat
- pipeline
- heat exchanger
- oven dry
- 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.)
- Expired - Fee Related
Links
Landscapes
- Drying Of Solid Materials (AREA)
Abstract
The utility model relates to a thermal conducting oil-gas fluid drier which comprises a thermal conducting oil furnace, a heat exchanger, an exalted expanding groove, a circular oil pump, a filter, oil-gas segregator and a pipeline. An oil outlet which is arranged on the top of the thermal conducting oil furnace is connected with an oil inlet of the heat exchanger by the pipeline, the oil outlet is orderly connected with the oil-gas segregator, the filter, the circular oil pump and an oil retuning port which is arranged under the thermal conducting oil furnace by the pipeline. After the conducting oil undertakes a thermal exchange, the temperature descends by about 20 DEG C, the conducting oil can return to the oil furnace and be circularly used. The utility model has simple structure, not only saves the energy, but also reduces the investment. The conducting oil has good safety when running in the normal pressure.
Description
The utility model relates to a kind of drying plant, and particularly a kind of conduction oil airflow dryer is mainly used in food processing.
Drying plant commonly used at present all is to be the steam boiler of heat carrier with steam.This drying plant need be equipped with demineralizing plant and facilities such as water storage, water supply, its complex structure, investment height; Under high pressure work, poor stability; The waste heat of steam can not utilize, and heat is imitated low.
The purpose of this utility model just provides the conduction oil airflow dryer that a kind of structure is simple, cost is low, efficient is high, security is good.
The technical solution of the utility model is: comprise heat supply unit and drying unit, this heat supply unit comprises: heat-conducting oil furnace, heat exchanger, the high-order swollen groove that rises, oil circulating pump, filter, oil gas divide tooth device, pipeline, the oil-out on heat-conducting oil furnace top is connected to the heat exchanger oil-in by pipeline, its oil-out connects the oil return opening of gs-oil separator, filter, oil circulating pump and heat-conducting oil furnace bottom successively by pipeline, top at gs-oil separator connects the high-order swollen groove that rises by expanding pipe, on its top opening port is arranged; Described drying unit comprises oven dry blower fan and oven dry assembly, and the oven dry blower fan is connected with the air channel and the oven dry group body of heat exchanger.Also can connect a filling pump and oil storage tank by pipeline on the top of the swollen groove that rises of a described high position.Described heat-conducting oil furnace is a coal-burning boiler, its burner hearth around and top be the heat conduction oil pocket, at the body of heater skin one preheating cavity is arranged, the outlet of this cavity is connected to the air intake vent of heat exchanger.Described oven dry assembly is the starch drying plant, comprise starch conveyer, drying tower, separator, the starch conveyer is connected on the air channel of hot-blast outlet of heat exchanger, the other end in this air channel is connected with the inlet of dryer, its outlet is connected with the drying tower lower end, and this drying tower other end connects separator.
The utility model has the advantages that: conduction oil is after heat exchange, and temperature descends about 20 ℃, can return in the oil oven to recycle, and has improved the thermal efficiency; Compare with steam boiler, it is simple in structure, has reduced investment; Conduction oil moves under normal pressure, and security is good.
Down in that the utility model is described in further detail with implementing side in conjunction with the accompanying drawings.
Fig. 1 is a formation schematic diagram of the present utility model;
Fig. 2 is an example structure schematic diagram of the present utility model.
Referring to Fig. 1, the utility model comprises heat supply unit and drying unit, this heat supply unit comprises: heat-conducting oil furnace 1, heat exchanger 2, the high-order swollen groove 3 that rises, oil circulating pump 4, filter 5, gs-oil separator 6, pipeline 7, the oil-out on heat-conducting oil furnace 1 top is connected to the oil-in of heat exchanger 2 by pipeline 7, and its oil-out connects the oil return opening of gs-oil separator 6, filter 5, oil circulating pump 4 and heat-conducting oil furnace bottom successively by pipeline 7.The top of gs-oil separator 6 connects the high-order swollen groove 3 that rises by expanding pipe 15, on its top opening port 26 is arranged; Described drying unit comprises oven dry blower fan 8 and oven dry assembly 9, and oven dry blower fan 8 is connected with the air channel and the oven dry assembly 9 of heat exchanger 2.Also can connect a filling pump 12 and oil storage tank 11 on the top of the swollen groove 3 that rises of a described high position by pipeline 10 as required.
Referring to Fig. 2, be an embodiment of the present utility model, described heat-conducting oil furnace 1 is a coal-burning boiler, its burner hearth around and top be the heat conduction oil pocket, at the body of heater skin one preheating cavity is arranged, the outlet 14 of this cavity is connected to the air intake vent of heat exchanger 2 by air channel 13.Described oven dry assembly is the starch drying plant, comprise starch conveyer 20, drying tower 21, separator 22, starch conveyer 20 is connected on the air channel of hot-blast outlet of heat exchanger 2, the other end in this air channel is connected with the inlet of dryer 8, its outlet is connected with drying tower 21 lower ends, and its other end connects separator 22.
On the top of hot oil furnace 1 chimney 25 is arranged, bimetallic thermometer 16 is arranged, be used for measuring oil temperature, also have the air inlet 17 of preheating cavity, can connect air filter at this mouthful in upper of furnace body in the upper of furnace body side.Be provided with draining valve 18 in the bottom of body of heater, at the series connected valve 19 on the pipeline 7 of oil circulating pump 4.
Claims (4)
1, a kind of conduction oil airflow dryer, it is characterized in that: comprise heat supply unit and drying unit, this heat supply unit comprises: heat-conducting oil furnace (1), heat exchanger (2), the high-order swollen groove that rises (3), oil circulating pump (4), filter (5), gs-oil separator (6), pipeline (7), the oil-out on heat-conducting oil furnace (1) top is connected to the oil-in of heat exchanger (2) by pipeline (7), its oil-out connects gs-oil separator (6) successively by pipeline (7), filter (5), the oil return opening of oil circulating pump (4) and heat-conducting oil furnace (1) bottom, the top of gs-oil separator (6) connects the high-order swollen groove that rises (3) by expanding pipe (15), and opening port (26) is arranged on its top; Described drying unit comprises oven dry blower fan (8) and oven dry assembly (9), and oven dry blower fan (8) is connected with the air channel and the oven dry assembly (9) of heat exchanger (2).
2, conduction oil airflow dryer according to claim 1 is characterized in that: the top at the swollen groove that rises of a described high position (3) connects a filling pump (12) and oil storage tank (11) by pipeline (10).
3, conduction oil airflow dryer according to claim 1, it is characterized in that: described heat-conducting oil furnace (1) is a coal-burning boiler, its burner hearth around and top be the heat conduction oil pocket, at the body of heater skin one preheating cavity is arranged, the outlet of this cavity (14) is connected to the air intake vent of heat exchanger (2) by wind channel tube (13).
4, conduction oil airflow dryer according to claim 1, it is characterized in that: described oven dry assembly is the starch drying plant, comprise starch conveyer (20), drying tower (21), separator (22), starch conveyer (20) is connected on the air channel of hot-blast outlet of heat exchanger (2), the other end in this air channel is connected with the inlet of oven dry blower fan (8), its outlet is connected with drying tower (21) lower end, and the other end of this drying tower (21) connects separator (22).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 01224425 CN2485535Y (en) | 2001-05-23 | 2001-05-23 | Thermal conducting oil-gas fluid drier |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 01224425 CN2485535Y (en) | 2001-05-23 | 2001-05-23 | Thermal conducting oil-gas fluid drier |
Publications (1)
Publication Number | Publication Date |
---|---|
CN2485535Y true CN2485535Y (en) | 2002-04-10 |
Family
ID=33640733
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN 01224425 Expired - Fee Related CN2485535Y (en) | 2001-05-23 | 2001-05-23 | Thermal conducting oil-gas fluid drier |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN2485535Y (en) |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN100365354C (en) * | 2006-01-20 | 2008-01-30 | 劳关明 | protective device of heat-conducting oil furnace |
CN102185537A (en) * | 2011-04-09 | 2011-09-14 | 王海波 | System and method for realizing cogeneration by using heat-conducting oil furnace and semiconductor power generation device |
CN102692117A (en) * | 2012-06-17 | 2012-09-26 | 甘肃省机械科学研究院 | Corn seed and cluster drying device |
CN103609630A (en) * | 2013-12-12 | 2014-03-05 | 竹山县沛丰粮油工贸有限责任公司 | Noodle baking room |
CN104019649A (en) * | 2014-06-25 | 2014-09-03 | 苏州创维晟自动化科技有限公司 | Electromagnetic heat conduction oil type granular powder material environment-friendly drying machine |
CN104482736A (en) * | 2014-12-23 | 2015-04-01 | 开封市四达农产品设备有限公司 | High-humidity material drying device |
CN105043055A (en) * | 2015-08-25 | 2015-11-11 | 付锦帆 | Mixed steam drying device and method |
-
2001
- 2001-05-23 CN CN 01224425 patent/CN2485535Y/en not_active Expired - Fee Related
Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN100365354C (en) * | 2006-01-20 | 2008-01-30 | 劳关明 | protective device of heat-conducting oil furnace |
CN102185537A (en) * | 2011-04-09 | 2011-09-14 | 王海波 | System and method for realizing cogeneration by using heat-conducting oil furnace and semiconductor power generation device |
CN102185537B (en) * | 2011-04-09 | 2013-04-17 | 王海波 | System and method for realizing cogeneration by using heat-conducting oil furnace and semiconductor power generation device |
CN102692117A (en) * | 2012-06-17 | 2012-09-26 | 甘肃省机械科学研究院 | Corn seed and cluster drying device |
CN102692117B (en) * | 2012-06-17 | 2014-07-09 | 甘肃省机械科学研究院 | Corn seed and cluster drying device |
CN103609630A (en) * | 2013-12-12 | 2014-03-05 | 竹山县沛丰粮油工贸有限责任公司 | Noodle baking room |
CN103609630B (en) * | 2013-12-12 | 2016-07-06 | 湖北沛丰粮油股份有限公司 | Noodle drying room |
CN104019649A (en) * | 2014-06-25 | 2014-09-03 | 苏州创维晟自动化科技有限公司 | Electromagnetic heat conduction oil type granular powder material environment-friendly drying machine |
CN104482736A (en) * | 2014-12-23 | 2015-04-01 | 开封市四达农产品设备有限公司 | High-humidity material drying device |
CN105043055A (en) * | 2015-08-25 | 2015-11-11 | 付锦帆 | Mixed steam drying device and method |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN101900347B (en) | System for high-grade recycling waste heat of smoke discharged from boiler of power station | |
CN2485535Y (en) | Thermal conducting oil-gas fluid drier | |
CN202791972U (en) | Boiler tail flue gas waste heat utilization system | |
CN102788493A (en) | Heat pump drier driven by gas engine | |
CN206101556U (en) | Air ability and solar energy tobacco flue -curing bulk curer | |
CN201779684U (en) | High-grade recycling system for exhaust heat of power station boiler | |
CN107869846A (en) | Condensing gas heating stove | |
CN2211577Y (en) | Air heater | |
CN2599475Y (en) | Hot water and hot air integrated device | |
CN2704789Y (en) | Energy saver of condensing gas boiler | |
CN201103958Y (en) | Forced heat exchange radiator | |
CN2041415U (en) | Combined type heat pipe heat exchanger | |
CN2504551Y (en) | Energy saving multipurpose boiler | |
CN2406192Y (en) | Energy-saving hot-air stove | |
CN2449138Y (en) | Oil and gas combustion heating blower fan | |
CN2758677Y (en) | Soybean drier using steam as heat source | |
CN2222314Y (en) | Indoor warming device | |
CN201731634U (en) | Energy-conserving boiler preheating boiler feed water by heat pump | |
CN206919405U (en) | Household warming boiler | |
CN2251704Y (en) | Reversing circulating hot-air kiln for drying timber | |
CN2420576Y (en) | Temperature lifting furnace for greenhouse | |
CN207317257U (en) | A kind of bio oil hot-blast stove residual heat using device | |
CN2736652Y (en) | Environment protection energy-conserving full-automatic steam boiler | |
CN205537291U (en) | Surplus heat energy -saving of intelligence phase transition heat transfer utilizes device | |
CN2125079U (en) | Waste heat recoverer for kitchen range |
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 |