CN205095431U - Utilize drying device of new forms of energy - Google Patents
Utilize drying device of new forms of energy Download PDFInfo
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- CN205095431U CN205095431U CN201520898227.2U CN201520898227U CN205095431U CN 205095431 U CN205095431 U CN 205095431U CN 201520898227 U CN201520898227 U CN 201520898227U CN 205095431 U CN205095431 U CN 205095431U
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- tank body
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- dry tank
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- heat source
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Abstract
The utility model discloses an utilize drying device of new forms of energy, including a drying tank body, steam outlet and feed inlet, discharge gate, material distributor, vacuum pipe, filling device, heater, the heater includes the heat source runner pipe, heat source entry, heat source export, the heat source is the vapours, the heat source entry is connected with catch water through the air pump, still includes the hot water heating device who is connected through temperature control valve and catch water, hot water heating device adopts solar vacuum heat collection tube to restraint and wind -force stirring pyrogenicity device heats. This drying device utilizes solar energy, wind energy to unite simultaneously and does the steam heat source together, further heats to required pressure temperature steam through the heating chamber again, further improves the heating efficiency of steam, and solar energy, wind energy have been overcome owing to influenced by geographical environment, weather conditions to lead to the fact the unbalanced defect of energy to both combinations, greatly reduced drying cost, and realize new energy utilization maximize to further energy saving.
Description
Technical field
The utility model relates to a kind of drying device utilizing new forms of energy.
Background technology
Epoxidized soybean oil (ESO) belongs to epoxy plasticiser, that a kind of widely used polyvinyl chloride (PVC) plasticizer is held concurrently stabilizing agent, there is good light and heat stabilization, there is resistance to extraction compared with ester plasticizer, resistance to migration, resistance to volatilization, the advantages such as the good and degradable of intermiscibility, it is the epoxy plasticiser that uniquely can be used for packaging material for food, it is as the favorable substitutes of phthalic ester plasticizer, meet European Union RoHS environmental protection instruction and U.S. FDA food additives rule completely, cause showing great attention to of increasing Plastics Processing Industry and plasticizer production enterprise, current, the annual production of China's phthalic ester plasticizer and consumption figure all account for more than 80% of plasticizer total amount, epoxidized soybean oil (ESO) is less than 10%, and in the U.S., its consumption figure is only second to phthalic acid ester and fatty group dibasic acid plasticizer, occupy the 3rd.Along with the aggravation of the energy and environmental crisis, the exploitation of renewable resource become study hotspot, and therefore, exploitation epoxidized soybean oil (ESO) has vast potential for future development.
The existing drying device being applied to epoxidized soybean oil easily produces coking, generally, within 2 ~ 4 months, just need stopping production coke cleaning, make to need in the inside the plan stopping production overhaul life to carry out stopping production coke cleaning unplanned for several times, not only increase the maintaining cost of equipment, and directly cause huge production suspension induced losses and add a large amount of coke cleaning sewage, energy consumption is higher, product yield is low and quality is unstable, and cost is high; And pollute with waste comparatively serious at present, the regenerative resources such as solar energy are not utilized well, cause the waste of resource.
Utility model content
In order to solve above-mentioned the deficiencies in the prior art, the utility model provides a kind of drying device utilizing new forms of energy, which solve material coking, blocking filler, cause equipment can not the problem of continuous service, decrease equipment maintenance cost, enhance productivity significantly, stabilized product quality and save energy; Utilize solar energy, wind energy to combine simultaneously and do steam source together, through heating clamber, required pressure and temp is heated to further to steam again, the efficiency of heating surface of further raising steam, both combine and overcome solar energy, wind energy owing to affecting cause the unbalanced defect of energy by geographical environment, meteorological condition, greatly reduce drying cost, and realize utilization of new energy resources maximization, with further economize energy.
Technical problem to be solved in the utility model is achieved by the following technical programs:
A kind of drying device utilizing new forms of energy, be applied to the drying of epoxidized soybean oil, comprise a dry tank body, be arranged on the steam (vapor) outlet above described dry tank body and charging aperture, be arranged on the discharging opening below described dry tank body, be arranged on epimere in described dry tank body and the material distributor be connected with charging aperture, the vacuum pipe being used for material being carried out to negative pressure dehydration is connected with described steam (vapor) outlet, be arranged on stage casing in described dry tank body and the sizer be connected with described material distributor, be arranged on hypomere in described dry tank body, be positioned at the heater below described sizer, described heater comprises the heat source stream siphunculus be distributed on described dry tank body hypomere tube wall, the top of described dry tank body hypomere is provided with the thermal source inlet be connected with described heat source stream siphunculus, and the bottom of described dry tank body hypomere is provided with the thermal source outlet be connected with described heat source stream siphunculus, described thermal source is vapours, described thermal source inlet is connected with steam-water separator by air pump, also comprises the hot-water heating system be connected with steam-water separator by temperature control valve, and described hot-water heating system adopts solar vacuum heat-collecting pipe bundle and wind stirring heating device to heat.
Preferably, described dry tank body hypomere is provided with temperature sensor.
Preferably, described dry tank base is provided with agitating device.
The utility model has following beneficial effect:
The material distributor of material through epimere is distributed on the sizer of interruption by this drying device uniformly, increase the specific area of material to greatest extent, reduce wall stream, improve boil-off rate, accelerate moisture evaporation, the further heated material of hypomere is to improve vaporization rate, solve material coking, blocking filler, cause equipment can not the problem of continuous service, decrease equipment maintenance cost, enhance productivity significantly, stabilized product quality and save energy; Utilize solar energy, wind energy to combine and do steam source together, through heating clamber, required pressure and temp is heated to further to steam again, the efficiency of heating surface of further raising steam, both combine and overcome solar energy, wind energy owing to affecting cause the unbalanced defect of energy by geographical environment, meteorological condition, greatly reduce drying cost, and realize utilization of new energy resources maximization, with further economize energy.
Accompanying drawing explanation
Fig. 1 is the structural representation of the utility model drying device.
Detailed description of the invention
Below in conjunction with drawings and Examples, the utility model is described in detail.
Please refer to Fig. 1, which show a kind of drying device utilizing new forms of energy, this drying device comprises dry tank body 1 and is arranged on steam (vapor) outlet 2, charging aperture 3, discharging opening 4, material distributor 5, vacuum pipe, sizer 6 and the heater 7 on dry tank body 1; Wherein, described steam (vapor) outlet 2 is arranged on the top of described dry tank body 1, is preferably top center, so that the moisture etc. in dry run in material evaporates away; Described charging aperture 3 is arranged on described dry tank body 1 side surface upper part, to carry material to be dried; Described discharging opening 4 is arranged on the bottom of described dry tank body 1, is preferably bottom centre, and the material after convenient and dry is discharged collection and entered next process; Described material distributor 5 is arranged on the inner upper portion of described dry tank body 1, and be positioned at the below of described charging aperture 3, described material distributor 5 is provided with multiple riser 51 of passing through for belows steam and several cloth sieve apertures 52, it is for being evenly distributed to described sizer 6 by material; Described vacuum pipe is arranged on described steam (vapor) outlet 2, for carrying out negative pressure dehydration to material; Described sizer 6 is arranged on described dry tank body 1 inner stage casing part, to be positioned at below described material distributor 5 and to be attached thereto, for receiving the material after being uniformly distributed by described material distributor 5, further dispersed material, increase the specific area of material, accelerate moisture evaporation; Described heater 7 is arranged on the inner hypomere part of described dry tank body 1, is positioned at below described sizer 6, to receive the material after flowing through described sizer 6, carries out heat drying more further, to improve vaporization rate, avoid material coking to material.Described heater 7 comprises the heat source stream siphunculus 71 be evenly distributed on described dry tank body 1 hypomere tube wall, the top of described dry tank body 1 hypomere is provided with the thermal source inlet 72 be connected with described heat source stream siphunculus 71, the bottom of described dry tank body 1 hypomere is provided with the thermal source outlet 73 be connected with described heat source stream siphunculus 71, and described thermal source inlet 72 and thermal source outlet 73 are positioned at the relative both sides of described dry tank body 1.Described heat source stream siphunculus 71 is provided with resistive heater.
Described thermal source is vapours; Described thermal source inlet 72 is connected with steam-water separator 8 by air pump, also comprise the hot-water heating system be connected with steam-water separator 8 by temperature control valve 9, described hot-water heating system adopts solar vacuum heat-collecting pipe bundle 10 and wind stirring heating device 11 to heat.Solar vacuum heat-collecting pipe bundle 10 super-absorbent, thermal effect are high, quick heating, under same illumination condition, can go out the hot water of more, higher water temperature than common tube; And wind stirring heating device 11, rotated by wind wheel and change wind energy into mechanical energy, pass to rotating shaft 12 and drive the blade rotation of the stirring rotator 13 stretched in water pot 17 to do eddy motion by stirring water, and constantly shock, friction, mechanical energy is all converted into heat energy, makes water heat temperature raising.
Water injects solar vacuum heat-collecting pipe bundle 10 and wind stirring heating device 11 heats, and carries out pressure thermal cycle, make two kinds of thermal source equilibriums by hot water circulating pump 14 pairs of heating processes, improves pyrogenicity speed; Hot water heating temperature is controlled by temperature control valve 9, and after temperature reaches the boiling point of water, temperature control valve 9 is opened, and the steam of generation enters steam-water separator 8 and is separated; Vapours after separation enters described thermal source inlet as thermal source; And the aqueous water after being separated turns back to solar vacuum heat-collecting pipe bundle 10 by drain valve 15 and wind stirring heating device 11 continues heat temperature raising.In wind stirring heating device 11, the liquid level of water pot 17 is controlled by LLCV 16, and after hot water temperature reaches the boiling point of water, temperature control valve 9 is opened, the liquid level of water pot 17 declines, LLCV 16 is opened, and cold water injects water pot 17 and heats, and continues next circulating-heating process.
Preferably, described cloth hole shape is generally circle, certainly also can arrange triangular form, quadrangle or other profiled holes as required, the shape being distributed in the cloth sieve aperture on described material distributor 5 can be identical, also can be used through multi-form arrangement by difform through hole.Described sizer 6 preferably but be not defined as ripple silk net sizer.Described dry tank body 1 hypomere is provided with the temperature sensor 74 for detecting heater heating state.
During specific implementation, be also provided with agitating device 18 bottom described dry tank body 1, preferably but be not defined as magnetic force or motor stirrer, make material can better uniformly transfer heat, material be heated evenly, and reduces the possibility of material coking further.
During specific implementation, described charging aperture 3 can arrange a control valve, to control the uninterrupted of material.Conveniently see drying the drying regime of the material in tank body 1, can arrange a pair visor between dry tank body 1 stage casing and hypomere.
Before this dry plant running, first start vacuum plant, with the absolute pressure≤8Kpa in guarantee equipment, enter after drying device hypomere until material, start magnetic stirring apparatus; The control valve at unlatching thermal source inlet place, injects solar vacuum heat-collecting pipe bundle by water and wind stirring heating device heats, and after temperature reaches the boiling point of water, temperature control valve is opened, and the steam of generation enters steam-water separator and is separated; Steam after separation enters heat source stream by air pump through thermal source inlet and threads a pipe, and in conjunction with resistance wire by heating material to technological temperature (105 ~ 115 DEG C), this drying device can regulate and control output preferably in actual production, the quality of product can not be affected in 2 tons to 5 tphs range of flows, and further heated material is to improve vaporization rate, solve material coking, blocking filler, cause equipment can not the problem of continuous service, decrease equipment maintenance cost, enhance productivity significantly, stabilized product quality and use new forms of energy to save energy.
The above embodiment only have expressed embodiment of the present utility model; it describes comparatively concrete and detailed; but therefore can not be interpreted as the restriction to the utility model the scope of the claims; in every case the technical scheme adopting the form of equivalent replacement or equivalent transformation to obtain, all should drop within protection domain of the present utility model.
Claims (3)
1. one kind utilizes the drying device of new forms of energy, be applied to the drying of epoxidized soybean oil, it is characterized in that, comprise a dry tank body, be arranged on the steam (vapor) outlet above described dry tank body and charging aperture, be arranged on the discharging opening below described dry tank body, be arranged on epimere in described dry tank body and the material distributor be connected with charging aperture, the vacuum pipe being used for material being carried out to negative pressure dehydration is connected with described steam (vapor) outlet, be arranged on stage casing in described dry tank body and the sizer be connected with described material distributor, be arranged on hypomere in described dry tank body, be positioned at the heater below described sizer, described heater comprises the heat source stream siphunculus be distributed on described dry tank body hypomere tube wall, the top of described dry tank body hypomere is provided with the thermal source inlet be connected with described heat source stream siphunculus, and the bottom of described dry tank body hypomere is provided with the thermal source outlet be connected with described heat source stream siphunculus, described thermal source is vapours, described thermal source inlet is connected with steam-water separator by air pump, also comprises the hot-water heating system be connected with steam-water separator by temperature control valve, and described hot-water heating system adopts solar vacuum heat-collecting pipe bundle and wind stirring heating device to heat.
2. the drying device utilizing new forms of energy according to claim 1, is characterized in that, described dry tank body hypomere is provided with temperature sensor.
3. the drying device utilizing new forms of energy according to claim 1, is characterized in that, described dry tank base is provided with agitating device.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520898227.2U CN205095431U (en) | 2015-11-12 | 2015-11-12 | Utilize drying device of new forms of energy |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520898227.2U CN205095431U (en) | 2015-11-12 | 2015-11-12 | Utilize drying device of new forms of energy |
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| Publication Number | Publication Date |
|---|---|
| CN205095431U true CN205095431U (en) | 2016-03-23 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520898227.2U Expired - Fee Related CN205095431U (en) | 2015-11-12 | 2015-11-12 | Utilize drying device of new forms of energy |
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| Country | Link |
|---|---|
| CN (1) | CN205095431U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108046565A (en) * | 2018-01-02 | 2018-05-18 | 李卫军 | A kind of sludge drying mechanism |
-
2015
- 2015-11-12 CN CN201520898227.2U patent/CN205095431U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108046565A (en) * | 2018-01-02 | 2018-05-18 | 李卫军 | A kind of sludge drying mechanism |
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| 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: 20160323 Termination date: 20201112 |
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| CF01 | Termination of patent right due to non-payment of annual fee |