CN204100587U - Biomass heat-conduction oil oven bootstrap system - Google Patents
Biomass heat-conduction oil oven bootstrap system Download PDFInfo
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- CN204100587U CN204100587U CN201420558585.4U CN201420558585U CN204100587U CN 204100587 U CN204100587 U CN 204100587U CN 201420558585 U CN201420558585 U CN 201420558585U CN 204100587 U CN204100587 U CN 204100587U
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- heat
- radiator
- conduction oil
- biomass
- oil oven
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Abstract
Biomass heat-conduction oil oven bootstrap system, comprise biomass heat-conduction oil oven, radiator and deduster, the left and right sides of radiator is communicated with deduster with biomass heat-conduction oil oven respectively by pipeline, the rear side of radiator is provided with fan, the front side of radiator is connected with heat-condutive oil heat exchanger by airtight breather line, and heat-condutive oil heat exchanger is connected with pneumatic drier by the UTILIZATION OF VESIDUAL HEAT IN pipeline closed; The centre of radiator is provided with the gas channel be communicated with heat-condutive oil heat exchanger; Heat-condutive oil heat exchanger is provided with flowline, biomass heat-conduction oil oven is provided with waste heat oil-in, the utility model effectively make use of the waste heat of biomass heat-conduction oil oven, avoid waste, adopt fan, radiator and heat exchanger simultaneously, by airtight vent line, waste heat is delivered in the desiccant pneumatic conveyer dryer of straw-like materials.
Description
Technical field
The present invention relates to biomass heat-conduction oil oven, especially relate to the waste heat utilization equipment of hot oil furnace.
Background technology
The fuel for combustion of biomass heat-conduction oil oven is living beings, if rice husk, wheat bran, the dregs of a decoction, corncob, straw heat transfer medium are conduction oil.Discarded living beings can be utilized to generate heat, supply whole plant area and use.But the outlet temperature of heat-conducting oil furnace is still higher, if directly discharge can cause the waste of heat energy.Utilizing the factory of stalk, because the water content of stalk is comparatively large, the weak effect directly pulverized, easily block pulverizer, delay man-hour, labor intensive removes maintenance maintenance again, increases cost of labor, also reduces production efficiency.
Summary of the invention
The object of the present invention is to provide a kind of biomass heat-conduction oil oven bootstrap system, make full use of the waste heat that biomass heat-conduction oil oven produces and carry out drying to straw-like materials, avoid energy dissipation, the temperature of waste heat also can meet the requirement of stalk drying.
Technical scheme of the present invention is:
Biomass heat-conduction oil oven bootstrap system, comprise biomass heat-conduction oil oven, radiator and deduster, the left and right sides of radiator is communicated with deduster with biomass heat-conduction oil oven respectively by pipeline, the rear side of radiator is provided with fan, the front side of radiator is connected with heat-condutive oil heat exchanger by airtight breather line, and heat-condutive oil heat exchanger is connected with pneumatic drier by the UTILIZATION OF VESIDUAL HEAT IN pipeline closed; The centre of radiator is provided with the gas channel be communicated with heat-condutive oil heat exchanger; Heat-condutive oil heat exchanger is provided with flowline, and biomass heat-conduction oil oven is provided with waste heat oil-in, and heat-condutive oil heat exchanger is communicated with the waste heat oil-in of biomass heat-conduction oil oven by flowline.
Radiator is gilled radiator.
Deduster comprises the multi-tube dust cleaner and high temperature cloth bag dust collector that connect successively, and the outlet of high temperature cloth bag dust collector is connected with chimney.
Heat-insulation layer is enclosed with outside UTILIZATION OF VESIDUAL HEAT IN pipeline.
Fan is tube-axial fan.
The airflow direction that bearing of trend and the fan of gas channel blow is identical.
The present invention effectively make use of the waste heat of biomass heat-conduction oil oven, avoids waste, adopts fan, radiator and heat exchanger simultaneously, is delivered in the desiccant pneumatic conveyer dryer of straw-like materials by waste heat by airtight vent line.Hot stream temperature after heat-condutive oil heat exchanger heat exchange meets the dry requirement of stalk combustible material just, save the energy, effectively utilize waste heat, specially for the desiccant pneumatic drier of stalk provides hot-air to originate, the problem in drying source source need not be solved.
Accompanying drawing explanation
Fig. 1 is structural representation of the present invention.
Detailed description of the invention
As shown in Figure 1, biomass heat-conduction oil oven bootstrap system of the present invention, comprises biomass heat-conduction oil oven 1, radiator 2 and deduster.Deduster comprises the multi-tube dust cleaner 3 and high temperature cloth bag dust collector 4 that connect successively, and the outlet of high temperature cloth bag dust collector 4 is connected with chimney 6.Radiator 2 is gilled radiator.Fan 5 is tube-axial fan.
The left and right sides of radiator 2 is communicated with multi-tube dust cleaner 3 with biomass heat-conduction oil oven 1 respectively by pipeline, the rear side of radiator 2 is provided with fan 5, the front side of radiator 2 is connected with heat-condutive oil heat exchanger 8 by airtight breather line 7, heat-condutive oil heat exchanger 8 is connected with pneumatic drier 9 by airtight UTILIZATION OF VESIDUAL HEAT IN pipeline 10, be enclosed with heat-insulation layer outside UTILIZATION OF VESIDUAL HEAT IN pipeline 10, corresponding factory building can be passed as required.
The centre of radiator 2 is provided with the gas channel be communicated with heat-condutive oil heat exchanger 8; Heat-condutive oil heat exchanger 8 is provided with flowline 11, and biomass heat-conduction oil oven 1 is provided with waste heat oil-in 12, and heat-condutive oil heat exchanger 8 is communicated with the waste heat oil-in 12 of biomass heat-conduction oil oven 1 by flowline 11.
During use, biomass heat-conduction oil oven 1 starts heating, then tube-axial fan 5 is started, be blown into air to radiator 2, the thermal current that biomass heat-conduction oil oven 1 produces, thermal current flows in the process of multi-tube dust cleaner 3 through radiator 2, the gas channel of level is provided with in radiator 2, blown to heat-condutive oil heat exchanger 8 by fan 5 inner, the hot-air after heat exchange delivers to pneumatic drier 9 along UTILIZATION OF VESIDUAL HEAT IN pipeline 10, carries out drying to the stalk in pneumatic drier 9.And the heat that the conduction oil in heat-condutive oil heat exchanger 8 absorbs is delivered in biomass heat-conduction oil oven 1 through flowline 11 again, supply as thermal source.Directly utilize the dry stalk of biomass heat-conduction oil oven 1 waste heat, waste heat supply temperature is too high, and can ignite stalk, so through exhaust-heat absorption again, blowing by fan, waste heat supply temperature now just meets the requirement of stalk drying.
Claims (6)
1. biomass heat-conduction oil oven bootstrap system, it is characterized in that: comprise biomass heat-conduction oil oven, radiator and deduster, the left and right sides of radiator is communicated with deduster with biomass heat-conduction oil oven respectively by pipeline, the rear side of radiator is provided with fan, the front side of radiator is connected with heat-condutive oil heat exchanger by airtight breather line, and heat-condutive oil heat exchanger is connected with pneumatic drier by the UTILIZATION OF VESIDUAL HEAT IN pipeline closed; The centre of radiator is provided with the gas channel be communicated with heat-condutive oil heat exchanger; Heat-condutive oil heat exchanger is provided with flowline, and biomass heat-conduction oil oven is provided with waste heat oil-in, and heat-condutive oil heat exchanger is communicated with the waste heat oil-in of biomass heat-conduction oil oven by flowline.
2. biomass heat-conduction oil oven bootstrap system according to claim 1, is characterized in that: radiator is gilled radiator.
3. biomass heat-conduction oil oven bootstrap system according to claim 1 and 2, is characterized in that: deduster comprises the multi-tube dust cleaner and high temperature cloth bag dust collector that connect successively, and the outlet of high temperature cloth bag dust collector is connected with chimney.
4. biomass heat-conduction oil oven bootstrap system according to claim 1 and 2, is characterized in that: be enclosed with heat-insulation layer outside UTILIZATION OF VESIDUAL HEAT IN pipeline.
5. biomass heat-conduction oil oven bootstrap system according to claim 1 and 2, is characterized in that: fan is tube-axial fan.
6. biomass heat-conduction oil oven bootstrap system according to claim 1 and 2, is characterized in that: the airflow direction that bearing of trend and the fan of gas channel blow is identical.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201420558585.4U CN204100587U (en) | 2014-09-26 | 2014-09-26 | Biomass heat-conduction oil oven bootstrap system |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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CN201420558585.4U CN204100587U (en) | 2014-09-26 | 2014-09-26 | Biomass heat-conduction oil oven bootstrap system |
Publications (1)
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CN204100587U true CN204100587U (en) | 2015-01-14 |
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Family Applications (1)
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CN201420558585.4U Withdrawn - After Issue CN204100587U (en) | 2014-09-26 | 2014-09-26 | Biomass heat-conduction oil oven bootstrap system |
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104279757A (en) * | 2014-09-26 | 2015-01-14 | 河南鑫企实业有限公司 | Waste heat utilization system for biomass heat-transfer oil furnace |
CN104930840A (en) * | 2015-06-06 | 2015-09-23 | 何小平 | Biomass heat conducting oil furnace tail gas utilization treatment device |
-
2014
- 2014-09-26 CN CN201420558585.4U patent/CN204100587U/en not_active Withdrawn - After Issue
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104279757A (en) * | 2014-09-26 | 2015-01-14 | 河南鑫企实业有限公司 | Waste heat utilization system for biomass heat-transfer oil furnace |
CN104279757B (en) * | 2014-09-26 | 2017-08-08 | 河南鑫企实业有限公司 | Biomass heat-conduction oil oven afterheat utilizing system |
CN104930840A (en) * | 2015-06-06 | 2015-09-23 | 何小平 | Biomass heat conducting oil furnace tail gas utilization treatment device |
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Legal Events
Date | Code | Title | Description |
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C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
AV01 | Patent right actively abandoned |
Granted publication date: 20150114 Effective date of abandoning: 20170808 |
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AV01 | Patent right actively abandoned |