CN205940072U - Pressure drying -machine - Google Patents
Pressure drying -machine Download PDFInfo
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- CN205940072U CN205940072U CN201620876199.9U CN201620876199U CN205940072U CN 205940072 U CN205940072 U CN 205940072U CN 201620876199 U CN201620876199 U CN 201620876199U CN 205940072 U CN205940072 U CN 205940072U
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- cylinder body
- pipe
- heat exchanger
- pressure dehydrator
- air inlet
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Abstract
The utility model relates to a pressure drying -machine. This pressure drying -machine is through disposing hygrometer and controller for the pressure drying -machine main part to the controller is connected with hygrometer and governing valve electricity respectively. When the yarn is dried in the hot -blast cylinder body of high pressure, utilize the humidity of hygrometer monitoring cylinder body exit gas and send humidity monitoring value to controller, steam flow that the controller got into first heat exchanger according to the matching condition regulation and control of the humidity value of monitoring and humidity default realizes the automatic control that the yarn was dried, convenient operation, drying degree that can control yarn directly perceived and accurate.
Description
Technical field
This utility model is related to textile industry weaving field, more particularly to a kind of pressure dehydrator.
Background technology
At present, in textile industry, yarn generally utilizes drying machine drying.Conventional drying plant is pressure dehydrator.Pressure
Power dehydrator is dried to yarn by high pressure and hot blast.
Existing judgement pressure dehydrator is that only detection enters pressure dehydrator cylinder body to the method for drying yarn degree
Hot air temperature T1, damp-heat air temperature T of outflow pressure dehydrator cylinder body2Temperature T with the cold air after cooler cooling3,
Work as T1-T2And T2-T3When being respectively maintained at corresponding setting value within a certain period of time, then judge that yarn is dried.But actual raw
During product, the yarn amount that carries of pressure dehydrator is different, judges that by detection temperature drying degree is easy to overbaking
Or the not enough situation of the degree of drying, wherein overbaking can produce extra energy resource consumption, dry deficiency and can produce potential quality
Problem.
Utility model content
Based on this it is necessary to provide a kind of pressure dehydrator that can intuitively and accurately control drying yarn degree.
A kind of pressure dehydrator, including pressure dehydrator main body, detection means and controller；
Described pressure dehydrator main body includes cylinder body, admission line, outlet pipe and First Heat Exchanger；Described cylinder body has
Air inlet and gas outlet；Described cylinder body is connected with described admission line by described air inlet；Described cylinder body pass through described go out
QI KOU is connected with described outlet pipe；
Described First Heat Exchanger is on described admission line；Described First Heat Exchanger has steam and enters pipe；Described steaming
Vapour enters pipe and is provided with regulating valve；
Described detection means includes drimeter；Described drimeter at the described gas outlet in described cylinder body or described go out
In feed channel；
Described controller is electrically connected with described regulating valve and described drimeter respectively.
Wherein in an embodiment, described pressure dehydrator main body also includes blower fan；
Described admission line includes the first air inlet pipe and the second air inlet pipe；Described blower fan passes through institute with described First Heat Exchanger
State the first air inlet pipe to be connected, described cylinder body is connected by described second air inlet pipe with described First Heat Exchanger.
Wherein in an embodiment, described pressure dehydrator main body also includes the second heat exchanger；
Described outlet pipe includes the first escape pipe and the second escape pipe；Described second heat exchanger and described cylinder body pass through institute
State the first escape pipe to be connected, described blower fan is connected by described second escape pipe with described second heat exchanger；
Described drimeter is on the first escape pipe described in described cylinder body or on the second escape pipe.
Wherein in an embodiment, described detection means also includes the first thermometer, second temperature meter and the 3rd temperature
Meter；
Described first thermometer is in described second air inlet pipe；Described second temperature meter is located at described first escape pipe
On；Described 3rd thermometer is on described second escape pipe.
Wherein in an embodiment, described controller respectively with described first thermometer, described second temperature meter and institute
State the 3rd thermometer electrical connection.
Wherein in an embodiment, described hygroscopic range is 0～100RH.
Above-mentioned pressure dehydrator is by being configured with drimeter for pressure dehydrator main body and being electrically connected with drimeter and regulating valve
The controller connecing, when yarn is dried in the cylinder body of high-pressure hot wind, monitors, using drimeter, the high temperature flowing out in cylinder body
The humidity of hot blast simultaneously sends humidity value to controller, and controller is according to its match condition regulation and control entrance with humidity preset value the
The steam flow of one heat exchanger realizes automatically controlling of drying yarn, easy to operate, can intuitively and accurately control the baking of yarn
Dry degree.
Brief description
Fig. 1 is the pressure dehydrator schematic diagram of an embodiment.
Specific embodiment
For the ease of understanding this utility model, below with reference to relevant drawings, this utility model is more fully retouched
State.Preferred embodiment of the present utility model is given in accompanying drawing.But, this utility model can come real in many different forms
Existing however it is not limited to embodiment described herein.On the contrary, providing the purpose of these embodiments to be to make to public affairs of the present utility model
The understanding opening content is more thoroughly comprehensive.
It should be noted that when element is referred to as " being fixed on " another element, it can be directly on another element
Or can also there is element placed in the middle.When an element is considered as " connection " another element, it can be directly connected to
To another element or may be simultaneously present centering elements.
Unless otherwise defined, all of technology used herein and scientific terminology are led with belonging to technology of the present utility model
The implication that the technical staff in domain is generally understood that is identical.In term used in the description of the present utility model it is simply herein
The purpose of description specific embodiment is it is not intended that in limiting this utility model.Term as used herein " and/or " include
The arbitrary and all of combination of one or more related Listed Items.
Incorporated by reference to Fig. 1, the pressure dehydrator 10 of an embodiment, including pressure dehydrator main body, detection means and controller
300.
Pressure dehydrator main body includes cylinder body 110, First Heat Exchanger 120, admission line and outlet pipe.
Cylinder body 110 has air inlet and gas outlet.Cylinder body 110 is connected with admission line by air inlet, and cylinder body 110 leads to
Cross gas outlet to be connected with outlet pipe.The air that First Heat Exchanger 120 is used for being fed in feed channel on admission line adds
Heat makes it become hot blast, and hot blast enters in cylinder body 110 and yarn is dried.First Heat Exchanger 120 has steam and enters pipe
Road (in figure does not mark), steam enters pipeline and is provided with regulating valve 161 to regulate and control to enter the steam flow of First Heat Exchanger 120.
Detection means includes drimeter 200.Drimeter 200 gas or outlet pipe at the gas outlet in cylinder body 110
On.
Controller 300 is electrically connected with regulating valve 161 and drimeter 200 respectively.
Specifically, in the present embodiment, pressure dehydrator main body also includes blower fan 130 and the second heat exchanger 140.
Admission line includes the first air inlet pipe 151 and the second air inlet pipe 152.First Heat Exchanger 120 and blower fan 130 pass through the
One air inlet pipe phase 151 is connected.First Heat Exchanger 120 is connected by the second air inlet pipe 152 with cylinder body 110.
Specifically, in the present embodiment, outlet pipe is divided into the first escape pipe 153 and the second escape pipe 154.Second heat exchange
Device 140 is connected by the first escape pipe 153 with cylinder body 110.Blower fan 130 and the second heat exchanger 140 pass through the second escape pipe 154
It is connected.Second heat exchanger 140 is cooled down to the hot blast flowing out in cylinder body 110 by cooling water.
When pressure dehydrator 10 runs, air is entered in the first air inlet pipe 151 by blower fan 130 and enters First Heat Exchanger
It is heated by steam formation high-temperature hot-air, high-temperature hot-air enters into cylinder body 110 internal circulation flow by the second air inlet pipe 152 in 120
And take away the moisture in yarn.High-temperature hot-air temperature after cylinder body 110 interior circulation reduces, and humidity increases, and is changed into high humidity hot blast,
High humidity hot blast enters the second heat exchanger 140 by the first escape pipe 153 and cools down, and after cooling, the water in high humidity hot blast condenses out
Discharged by drain valve afterwards, high humidity hot blast is changed into low temperature hot blast, continue through wind from the second heat exchanger 140 low temperature hot blast out
Machine 130 delivers into First Heat Exchanger 120, carries out circulation next time, with further save energy consumption, recycles.
In the present embodiment, drimeter 200 is on the first escape pipe 153 of cylinder body 110.In other embodiments, wet
Degree meter 200 can also be on the gas outlet in cylinder body 100 or the second escape pipe 154, for monitoring from cylinder body 110
The humidity of the steam flowing out.Drimeter 200 can work in 0-150 DEG C of environment and have the humidity range of 0-100RH.
In the present embodiment, controller 300 electrically connects the analogue signal for monitoring humidity meter 200 with drimeter 200
Output valve.Controller 300 is electrically connected with regulating valve 161 to adjust steam flow.Controller 300 presets humidity value, then
The degree of opening to regulate and control regulating valve 161 for the match condition of the monitor value of monitoring humidity meter 200 and default humidity value.Work as drimeter
200 monitor value and when matching of default humidity value, drying yarn, controller 300 regulates and controls the first regulating valve 161 and cuts out, section
Save energy resource consumption, and drying degree that is directly perceived and controlling yarn exactly, produce the extra energy during effectively solving overbaking and disappear
Consumption and drying produce potential quality problems when not enough.
Further, pressure dehydrator main body also includes the first thermometer, second temperature meter and the 3rd thermometer.First temperature
Degree meter is located at the gas access of cylinder body 110 or in the second air inlet pipe 152.The gas that second temperature meter is located in cylinder body 110
On exit or the first escape pipe 153.3rd thermometer is located on the second escape pipe 154.
Controller 300 is corresponding for monitoring with the electrical connection of the first thermometer, second temperature meter and the 3rd thermometer respectively
The monitor value of thermometer, for carrying out Collaborative Control to drying yarn degree.
Above-mentioned pressure dehydrator by pressure dehydrator main body configuration drimeter 200 and with drimeter 200 and adjust
The controller 300 of valve 161 electrical connection.When yarn is dried in the cylinder body 110 of high-pressure hot wind, supervised using drimeter 200
The humidity surveying cylinder body 110 exit gas simultaneously sends humidity detection value to controller 300, controller 300 according to moisture signal with
Humidity preset value regulates and controls to enter First Heat Exchanger steam flow after matching realizes automatically controlling of drying yarn, operation side
Just, can intuitively and effective control yarn drying degree.
Each technical characteristic of embodiment described above can arbitrarily be combined, for making description succinct, not to above-mentioned reality
The all possible combination of each technical characteristic applied in example is all described, as long as however, the combination of these technical characteristics is not deposited
In contradiction, all it is considered to be the scope of this specification record.
Embodiment described above only have expressed several embodiments of the present utility model, and its description is more concrete and detailed,
But therefore can not be interpreted as the restriction to utility model patent scope.It should be pointed out that the common skill for this area
For art personnel, without departing from the concept of the premise utility, some deformation can also be made and improve, these broadly fall into
Protection domain of the present utility model.Therefore, the protection domain of this utility model patent should be defined by claims.
Claims (6)
1. a kind of pressure dehydrator is it is characterised in that include pressure dehydrator main body, detection means and controller；
Described pressure dehydrator main body includes cylinder body, admission line, outlet pipe and First Heat Exchanger；Described cylinder body has air inlet
Mouth and gas outlet；Described cylinder body is connected with described admission line by described air inlet；Described cylinder body passes through described gas outlet
It is connected with described outlet pipe；
Described First Heat Exchanger is on described admission line；Described First Heat Exchanger has steam and enters pipe；Described steam enters
Enter pipe and be provided with regulating valve；
Described detection means includes drimeter；Described drimeter is at the described gas outlet in described cylinder body or described escape pipe
On road；
Described controller is electrically connected with described regulating valve and described drimeter respectively.
2. pressure dehydrator as claimed in claim 1 is it is characterised in that described pressure dehydrator main body also includes blower fan；
Described admission line includes the first air inlet pipe and the second air inlet pipe；Described blower fan and described First Heat Exchanger pass through described the
One air inlet pipe is connected, and described cylinder body is connected by described second air inlet pipe with described First Heat Exchanger.
3. pressure dehydrator as claimed in claim 2 is it is characterised in that described pressure dehydrator main body also includes the second heat exchange
Device；
Described outlet pipe includes the first escape pipe and the second escape pipe；Described second heat exchanger and described cylinder body pass through described the
One escape pipe is connected, and described blower fan is connected by described second escape pipe with described second heat exchanger；
Described drimeter is on the first escape pipe described in described cylinder body or on the second escape pipe.
4. pressure dehydrator as described in any of claims 3 is it is characterised in that described detection means also includes the first temperature
Degree meter, second temperature meter and the 3rd thermometer；
Described first thermometer is in described second air inlet pipe；Described second temperature meter is on described first escape pipe；Institute
State the 3rd thermometer on described second escape pipe.
5. pressure dehydrator as claimed in claim 4 it is characterised in that described controller respectively with described first thermometer,
Described second temperature meter and described 3rd thermometer electrical connection.
6. as described pressure dehydrator arbitrary in claim 1 to 5 it is characterised in that described hygroscopic range be 0～
100RH.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620876199.9U CN205940072U (en) | 2016-08-12 | 2016-08-12 | Pressure drying -machine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620876199.9U CN205940072U (en) | 2016-08-12 | 2016-08-12 | Pressure drying -machine |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205940072U true CN205940072U (en) | 2017-02-08 |
Family
ID=57920076
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620876199.9U Active CN205940072U (en) | 2016-08-12 | 2016-08-12 | Pressure drying -machine |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205940072U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109028933A (en) * | 2018-06-15 | 2018-12-18 | 安徽森米诺农业科技有限公司 | Intelligent foodstuff drying device |
-
2016
- 2016-08-12 CN CN201620876199.9U patent/CN205940072U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109028933A (en) * | 2018-06-15 | 2018-12-18 | 安徽森米诺农业科技有限公司 | Intelligent foodstuff drying device |
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| GR01 | Patent grant |