CN103791616B - The dry air intake generation device of dryer - Google Patents
The dry air intake generation device of dryer Download PDFInfo
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- CN103791616B CN103791616B CN201410041534.9A CN201410041534A CN103791616B CN 103791616 B CN103791616 B CN 103791616B CN 201410041534 A CN201410041534 A CN 201410041534A CN 103791616 B CN103791616 B CN 103791616B
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- condenser
- evaporimeter
- dryer
- intake stack
- pipeline
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Abstract
The present invention relates to a kind of dry air intake generation device of dryer, this device comprises compressor, intake stack and the evaporimeter be successively set on along chimneying direction in intake stack and condenser, heat absorbing sheet is provided with outside described intake stack, described heat absorbing sheet, between evaporimeter and condenser, is provided with blower fan near described heat absorbing sheet; Described intake stack forms air outlet near one end of condenser and is communicated with dryer air inlet; Described compressor respectively with the refrigerant exit of evaporimeter and the refrigerant inlet communication of condenser, the refrigerant import of described evaporimeter is communicated with the refrigerant exit of condenser, is provided with expansion valve between the refrigerant import of described evaporimeter and the refrigerant exit of condenser; Be provided with water leg immediately below described evaporimeter, in described water leg, be provided with draining pump.This installation cost is low, efficiency is high and environmental pollution impact is less.
Description
Technical field
The present invention relates to a kind of dry air intake generation device of dryer, belong to dryer technical field.
Background technology
Dryer is also drying equipment or drying machine, and surrounding air is heated to proper temperature by hot-blast stove by existing dryer usually, and the air after heating is transported to drying chamber, carries out dehumidification treatments to needing dry article (as grain etc.).
But in high temperature damp-heat area (such as Hainan etc.), the humidity of surrounding air is very large, surrounding air is delivered directly to the poor effect that drying chamber dehumidifies to article, and hot-blast stove often adopts fuel oil, firewood or other combustible materials etc. to produce power, the energy consumed is more, not only add the production cost of dryer, and pollute environment.In addition, the life-span of hot-blast stove only has 2 ~ 3 years, but selling price remains high always, therefore also needs cheap replacement scheme badly.
Summary of the invention
The technical problem to be solved in the present invention is: propose a kind of can improve the drying efficiency of dryer and cost is lower, energy-conserving and environment-protective produce the device of dry wind for dryer.
The present invention is the technical scheme solving the problems of the technologies described above proposition: a kind of dry air intake generation device of dryer, comprise compressor, intake stack and be successively set on evaporimeter in intake stack and condenser along intake stack airflow direction, described compressor respectively with the refrigerant exit of evaporimeter and the refrigerant inlet communication of condenser, the refrigerant import of described evaporimeter is communicated with the refrigerant exit of condenser, is provided with expansion valve between the refrigerant import of described evaporimeter and the refrigerant exit of condenser; Described intake stack forms air outlet near one end of condenser and is communicated with dryer air inlet; Described intake stack forms near the other end of evaporimeter the air inlet being communicated with surrounding air; Intake stack lateral wall between described evaporimeter and condenser is glued with heat absorbing sheet, and also including can by natural wind or the hot blast drainage blower fan through heat absorbing sheet.
The dry air intake generation device of dryer of the present invention will create a condition in fact exactly, allows the air of the low relative humidity with proper temperature flow through article to be dried, and to take away moisture fast, its course of work is as follows:
1) under the main air blower effect of dryer, surrounding air enters intake stack, absorbs heat cooling, the portion of water condensation in air is separated out the air obtaining low temperature low relative humidity by evaporimeter;
2) air of the low relative humidity of low temperature recovers room temperature under the effect of heat absorbing sheet and blower fan, obtains the low relative humidity air of room temperature;
3) compressor exchange heat that evaporimeter is absorbed is to condenser, and the low relative humidity air of room temperature heats under the effect of condenser, becomes dry high temperature air and is transported in dryer.
The beneficial effect that the present invention brings is:
1) the present invention utilizes evaporimeter, condenser and compressor to carry out heat exchange, not only can by surrounding air cool-down dehumidification, and dehumidification rate is very high, compares the energy consumption that additive method considerably reduces dehumidifying; In addition, the heat utilizing condenser to be obtained by cool-down dehumidification fully utilizes, and is not only conducive to the drying efficiency improving dryer, and reduces the energy consumption needed for atmosphere temperature rising, heat environmental protection more relative to hot-blast stove, be particularly suitable for the area of high-temperature high-humidity.
2) surrounding air after cool-down dehumidification is creatively returned to room temperature rapidly by heat absorbing sheet and blower fan by the present invention, thus utilize the high heat exchanger effectiveness of compressor to obtain the low humidity air of high temperature, and required energy consumption is only the power consumption driving compressor and blower fan.If the present invention saves heat absorbing sheet and blower fan, then only can obtain the low humidity air of room temperature.In addition, with traditional hot-blast stove heat only can obtain high temperature surrounding air compared with, the present invention can not only obtain dry high temperature air, and Energy Efficiency Ratio improves greatly.
In order to prevent the moisture by condensation from surrounding air is separated out to be brought in dryer under the effect of air-flow, the present invention arranges water leg immediately below evaporimeter.In addition, under the effect of air-flow, can form negative pressuren zone in water leg, therefore the present invention arranges the air inversion at the water leg discharge outlet place that draining pump can prevent negative pressure from causing in water leg.
In order to prevent the moisture by condensation from surrounding air is separated out to be brought in dryer under the effect of air-flow further, the present invention can adopt one of following three kinds of technical schemes:
(1) described intake stack is vertically arranged, and described evaporimeter is positioned at immediately below condenser, and the air inlet of described intake stack is arranged on the side of intake stack.
(2) described intake stack is horizontally disposed with, and is provided with ventilative water bar in the intake stack between described evaporimeter and heat absorbing sheet, and described baffle plate is evaporated in air for preventing from the moisture in water leg to be taken in condenser heating again.
Preferably, described water bar is positioned at water leg directly over the cell wall of condenser side.
(3) described intake stack is divided into three sections, and be respectively the first pipeline, second pipe and the 3rd pipeline, wherein the first pipeline is vertically arranged, and described evaporimeter is placed in the first pipeline; Second pipe is horizontally disposed with, and described condenser and heat absorbing sheet are arranged on the inner side and outer side of second pipe respectively; 3rd pipeline is positioned at the below of second pipe, the 3rd pipeline respectively with the outlet of the first pipeline and the inlet communication of second pipe, described water leg is positioned at the inside bottom of the 3rd pipeline.As improving further, the air outlet of described first pipeline is lower than the bottom of second pipe.
In order to strengthen the heating effect of heat absorbing sheet to Cryogenic air further, the present invention can also increase exhaust duct, one end of described exhaust duct is communicated with the exhaust outlet of described dryer, the hot blast drainage that the exhaust outlet of dryer is discharged by the other end of described exhaust duct through heat absorbing sheet, the wind direction that described exhaust duct produces and the wind direction that blower fan produces basically identical.
The weather seasoned oneself to cold better to make the present invention, arranges the hot-blast stove being used for air in auxiliary heating intake stack between described condenser and the air outlet of intake stack.Compared with traditional only use hot-blast stove mode of heating, the present invention is economize energy more, and what obtain is the air that the air of high temperature drying instead of humidity are larger.
Accompanying drawing explanation
Be described further below in conjunction with the dry air intake generation device of accompanying drawing to dryer of the present invention.
Fig. 1 is the principle schematic of the embodiment of the present invention one.
Fig. 2 is the principle schematic of the embodiment of the present invention two.
Fig. 3 is the principle schematic of the embodiment of the present invention three.
Detailed description of the invention
Embodiment one
The dry air intake generation device of the dryer of the present embodiment as shown in Figure 1, comprise compressor 1, intake stack 2 and be successively set on evaporimeter 3 in intake stack 2 and condenser 4 along intake stack 2 airflow direction, intake stack 2 lateral wall between evaporimeter 3 and condenser 4 is glued with heat absorbing sheet 5, be provided with blower fan 6 near heat absorbing sheet 5, blower fan 6 can by natural wind (surrounding air) drainage through heat absorbing sheet 5; Intake stack 2 forms air outlet near one end of condenser 4 and is communicated with the air inlet of dryer 7; Compressor 1 respectively with the refrigerant exit of evaporimeter 3 and the refrigerant inlet communication of condenser 4, the refrigerant import of evaporimeter 3 is communicated with the refrigerant exit of condenser 4, is provided with expansion valve 9 between the refrigerant import of evaporimeter 3 and the refrigerant exit of condenser 4.
Surrounding air is carried out cool-down dehumidification through evaporator 3, carries out recovery room temperature, after condenser 4 heats up through heat absorbing sheet 5 by the dry air intake generation device of the dryer of the present embodiment successively, obtain the air carrying wet very capable high temperature drying, then the air of high temperature drying enters dryer, uniformly across article to be dried, effusion being taken away by air-flow rapidly after the heat energy in the air of high temperature drying of the moisture absorption in article to be dried.
The present embodiment can also do following improvement: be provided with water leg 10 immediately below evaporimeter 3, is provided with draining pump 8 in water leg 10.Like this, the moisture by condensation from surrounding air is separated out can be prevented to be brought in dryer under the effect of air-flow.
The present embodiment can also be improved further: intake stack 2 is horizontally disposed with, be provided with ventilative water bar (not shown in figure 1) in intake stack 2 between evaporimeter 3 and heat absorbing sheet 5, this water bar is evaporated in air for preventing the moisture in water leg 10 from being brought in condenser 4 to heat by air-flow again.
Preferably, in the present embodiment, water bar is positioned at water leg 10 directly over the cell wall of condenser 4 side.In the present embodiment, water bar is the non-woven fabrics of one or more layers waterproof and breathable be fixed on inside intake stack 2.
In order to strengthen the heating effect of heat absorbing sheet to Cryogenic air further, the present embodiment can also arrange exhaust duct (not shown) at the exhaust outlet of dryer, the exhaust outlet of dryer is communicated with one end of exhaust duct, the hot blast drainage that the exhaust outlet of dryer is discharged by the other end of exhaust duct through heat absorbing sheet, and the hot blast wind direction that the exhaust outlet of dryer is discharged by exhaust duct and the wind direction that blower fan produces basically identical.Like this, the waste heat of the gas that dryer gives off can be made full use of.
In order to the weather seasoned oneself to cold better, the present embodiment can also arrange the hot-blast stove (not shown) being used for air in auxiliary heating intake stack 2 between condenser 4 and the air outlet of intake stack 2.Compared with traditional only use hot-blast stove mode of heating, the air of high temperature drying that what the present embodiment obtained is instead of the larger air of humidity, and the mode of heating of the present embodiment more economize energy.
Embodiment two
The present embodiment is with the difference implementing: as shown in Figure 2, in the present embodiment, intake stack 2 is vertically arranged, and evaporimeter 3 is positioned at immediately below condenser 4, and the air inlet of intake stack 2 is arranged on the side of intake stack 2.Like this, even if do not use baffle plate, the moisture that in air, condensation is separated out is deposited under gravity in the water leg 10 of below and is discharged by draining pump 8, air-flow enters continuation after intake stack 2 and upwards flows from the side of intake stack 2, therefore the moisture in water leg 10 can not to be taken in condenser to heating evaporation in air again.
Certainly, the baffle plate of the waterproof and breathable described in embodiment one can also be increased in the intake stack 2 between the evaporimeter 3 of the present embodiment and heat absorbing sheet 5.
Embodiment three
The present embodiment is the improvement on enforcement one basis, the difference of itself and embodiment one is: in the present embodiment, the air inlet of intake stack 2 is biased, as shown in Figure 3, intake stack 2 in the present embodiment is divided into three sections, be respectively the first pipeline, second pipe and the 3rd pipeline, wherein the first pipeline is vertically arranged, and evaporimeter 3 is placed in the first pipeline; Second pipe is horizontally disposed with, and condenser 4 and heat absorbing sheet 5 are arranged on the inner side and outer side of second pipe respectively; 3rd pipeline is positioned at the below of second pipe, the 3rd pipeline respectively with the outlet of the first pipeline and the inlet communication of second pipe, water leg 10 is positioned at the inside bottom of the 3rd pipeline.
Like this, after biased to the air inlet of intake stack 2, balanced windage, therefore also can not to take to the moisture in water leg 10 in condenser in heating evaporation air again.
The present invention is not limited to above-described embodiment, and all employings are equal to the technical scheme of replacing and being formed, and all drop on the protection domain of application claims.
Claims (6)
1. the dry air intake generation device of a dryer, comprise compressor, intake stack and be successively set on evaporimeter in intake stack and condenser along intake stack airflow direction, described compressor respectively with the refrigerant exit of evaporimeter and the refrigerant inlet communication of condenser, the refrigerant import of described evaporimeter is communicated with the refrigerant exit of condenser, is provided with expansion valve between the refrigerant import of described evaporimeter and the refrigerant exit of condenser; Described intake stack forms air outlet near one end of condenser and is communicated with dryer air inlet; Described intake stack forms near the other end of evaporimeter the air inlet being communicated with surrounding air; It is characterized in that: the intake stack lateral wall between described evaporimeter and condenser is glued with heat absorbing sheet, also including can by natural wind or the hot blast drainage blower fan through heat absorbing sheet; Be provided with water leg immediately below described evaporimeter, in described water leg, be provided with draining pump; Described intake stack is horizontally disposed with, and is provided with ventilative water bar in the intake stack between described evaporimeter and heat absorbing sheet.
2. the dry air intake generation device of dryer according to claim 1, is characterized in that: described water bar is positioned at water leg directly over the cell wall of condenser side.
3. the dry air intake generation device of dryer according to claim 1, it is characterized in that: described intake stack is divided into three sections, be respectively the first pipeline, second pipe and the 3rd pipeline, wherein the first pipeline is vertically arranged, and described evaporimeter is placed in the first pipeline; Second pipe is horizontally disposed with, and described condenser and heat absorbing sheet are arranged on the inner side and outer side of second pipe respectively; 3rd pipeline is positioned at the below of second pipe, the 3rd pipeline respectively with the outlet of the first pipeline and the inlet communication of second pipe, described water leg is positioned at the inside bottom of the 3rd pipeline.
4. the dry air intake generation device of dryer according to claim 3, is characterized in that: the air outlet of described first pipeline is lower than the bottom of second pipe.
5. according to the dry air intake generation device of the arbitrary described dryer of Claims 1 to 4, it is characterized in that: also comprise exhaust duct, one end of described exhaust duct is communicated with the exhaust outlet of described dryer, the hot blast drainage that the exhaust outlet of dryer is discharged by the other end of described exhaust duct through heat absorbing sheet, the wind direction that described exhaust duct produces and the wind direction that blower fan produces basically identical.
6., according to the dry air intake generation device of the arbitrary described dryer of Claims 1 to 4, it is characterized in that: between described condenser and the air outlet of intake stack, be provided with the hot-blast stove for air in auxiliary heating intake stack.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410041534.9A CN103791616B (en) | 2014-01-28 | 2014-01-28 | The dry air intake generation device of dryer |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410041534.9A CN103791616B (en) | 2014-01-28 | 2014-01-28 | The dry air intake generation device of dryer |
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| CN103791616A CN103791616A (en) | 2014-05-14 |
| CN103791616B true CN103791616B (en) | 2016-03-09 |
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| CN201410041534.9A Active CN103791616B (en) | 2014-01-28 | 2014-01-28 | The dry air intake generation device of dryer |
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Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN105887453B (en) * | 2016-05-31 | 2019-07-19 | 无锡小天鹅股份有限公司 | Dryer |
| CN114111294B (en) * | 2021-11-26 | 2022-10-11 | 成都洁能干燥设备有限责任公司 | Box section expansion type dryer and process |
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|---|---|---|---|---|
| JP2007017107A (en) * | 2005-07-08 | 2007-01-25 | Green Seiju:Kk | Drying system |
| CN202350444U (en) * | 2011-11-25 | 2012-07-25 | 天津市国民制药机械有限公司 | Novel superconducting heat pump drying box |
| CN202511591U (en) * | 2012-03-26 | 2012-10-31 | 东南大学 | Heat pump drying device |
| CN102803882A (en) * | 2009-06-04 | 2012-11-28 | 松下电器产业株式会社 | Drying device |
| CN103398566A (en) * | 2013-08-21 | 2013-11-20 | 湖南科技大学 | Spiral-flow type heat pump dryer |
| CN203771688U (en) * | 2014-01-28 | 2014-08-13 | 滁州奥岚格机械有限公司 | Dry inlet air generation device of dryer |
-
2014
- 2014-01-28 CN CN201410041534.9A patent/CN103791616B/en active Active
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2007017107A (en) * | 2005-07-08 | 2007-01-25 | Green Seiju:Kk | Drying system |
| CN102803882A (en) * | 2009-06-04 | 2012-11-28 | 松下电器产业株式会社 | Drying device |
| CN202350444U (en) * | 2011-11-25 | 2012-07-25 | 天津市国民制药机械有限公司 | Novel superconducting heat pump drying box |
| CN202511591U (en) * | 2012-03-26 | 2012-10-31 | 东南大学 | Heat pump drying device |
| CN103398566A (en) * | 2013-08-21 | 2013-11-20 | 湖南科技大学 | Spiral-flow type heat pump dryer |
| CN203771688U (en) * | 2014-01-28 | 2014-08-13 | 滁州奥岚格机械有限公司 | Dry inlet air generation device of dryer |
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Denomination of invention: Dry inlet air generating device of dryer Effective date of registration: 20171027 Granted publication date: 20160309 Pledgee: Quanjiao enterprise financing Company limited by guarantee Pledgor: CHUZHOU OULANGO MACHINERY CO., LTD.|Wang Zhishui Registration number: 2017340000314 |