CN101579597B - Efficient energy-saving saturation dehumidifier and application method thereof - Google Patents
Efficient energy-saving saturation dehumidifier and application method thereof Download PDFInfo
- Publication number
- CN101579597B CN101579597B CN2008100375666A CN200810037566A CN101579597B CN 101579597 B CN101579597 B CN 101579597B CN 2008100375666 A CN2008100375666 A CN 2008100375666A CN 200810037566 A CN200810037566 A CN 200810037566A CN 101579597 B CN101579597 B CN 101579597B
- Authority
- CN
- China
- Prior art keywords
- moisture separator
- thermally insulated
- insulated container
- saturation
- efficient energy
- 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
Images
Landscapes
- Drying Of Gases (AREA)
Abstract
The invention relates to an efficient energy-saving saturation dehumidifier which comprises a thermally insulated container body, a throttle valve and a moisture separator, wherein the moisture separator is arranged in the thermally insulated container body and is connected with the throttle valve, a compressed air inlet pipe of the moisture separator is connected to the outside of the thermally insulated container body, and a condensed water outlet pipe of the moisture separator is connected to the outside of the thermally insulated container body. Compared with the prior art, the invention has the advantages of low operation cost, high efficiency and energy saving, high safety, simple structure and the like.
Description
Technical field
The present invention relates to saturation dehumidifier, particularly efficient energy-saving saturation dehumidifier and application process thereof.
Background technology
In a lot of fields, all need to use dry air at present.Adopt silica gel, molecular sieve adsorption or freezing to reach the purpose of air dewetting now mostly, the method of silica gel, molecular sieve adsorption at first needs air pressure increased to a certain degree just can carry out, and silica gel, molecular sieve adsorption need carry out " regeneration " to silica gel, molecular sieve, causes the waste of resource.Freezing is generally used for the bigger situation of dry air use amount.And in the practical application, do not need aridity very high and measure very large air sometimes, and only need reach a certain lower dry standard or very little consumption gets final product, in this case, original technology just seems has too wasted.
Summary of the invention
Purpose of the present invention is exactly to provide a kind of simple and practical efficient energy-saving saturation dehumidifier and application process thereof for the defective that overcomes above-mentioned prior art existence.
Purpose of the present invention can be achieved through the following technical solutions: efficient energy-saving saturation dehumidifier, it is characterized in that, this device comprises thermally insulated container body, choke valve, moisture separator, described moisture separator is located in the thermally insulated container body, described moisture separator is connected with choke valve, the compressed air inlet pipe of described moisture separator is connected to the thermally insulated container external body, and the condensating water outlet tube of described moisture separator is connected to the thermally insulated container external body.
Also comprise refrigeration module, this refrigeration module is located on the compressed air inlet pipe outer wall.
Described choke valve is located at thermally insulated container body inner top.
Described moisture separator is located in the thermally insulated container body.
Described compressed air inlet pipe is located at moisture separator side top.
Described condensating water outlet tube is located at the moisture separator bottom.
Below, described thermally insulated container side is provided with product gas outlet.
The application process of efficient energy-saving saturation dehumidifier is characterized in that, this method may further comprise the steps:
(1) compresses cooled air through air compressor and enter moisture separator;
(2) moisture content that surpasses saturation moisture content in the compressed air is condensed to the bottom of moisture separator, and flows out by condensating water outlet tube;
(3) compressed air through dehumidifying enters in the diffusion chamber of thermally insulated container body by choke valve;
(4) the compressed air volumetric expansion becomes big, and pressure reduces, and absorbs heat, makes moisture separator lower the temperature;
(5) the moisture separator temperature reduces, and reduces compressed-air actuated saturation moisture content in the moisture separator;
(6) outside the output of the product gas after the step-down jar.
Described refrigeration module is used for auxiliary temperature-reducing.
Compared with prior art, the present invention has the following advantages:
(1) operating cost is low;
(2) energy-efficient;
(3) safe;
(4) simple in structure.
Description of drawings
Fig. 1 is the structural representation of efficient energy-saving saturation dehumidifier of the present invention.
The specific embodiment
As shown in Figure 1, efficient energy-saving saturation dehumidifier of the present invention, this device comprises thermally insulated container body 1, choke valve 2, moisture separator 3, described moisture separator 3 is located in the thermally insulated container body 1, described moisture separator 3 is connected with choke valve 2, the compressed air inlet pipe 5 of described moisture separator 3 is connected to thermally insulated container body 1 outside, and the condensating water outlet tube 7 of described moisture separator 3 is connected to thermally insulated container body 1 outside.Described thermally insulated container body 1 wall is provided with refrigeration module 4.
The application process of efficient energy-saving saturation dehumidifier, this method may further comprise the steps: will reach near the air after the environment temperature through air compressor compression cooling and charge into moisture separator, this moment, this compressed air was 30 ℃, 0.4MPa, and saturation moisture content is 6.66g/m
3The moisture content that surpasses saturation moisture content in the compressed air is condensed to the bottom of moisture separator, and flows out by condensating water outlet tube; Compressed air through dehumidifying enters in the diffusion chamber of thermally insulated container body by choke valve; Compressed air pressure reduces, and absorbs heat, makes moisture separator be cooled to 25 ℃, when temperature does not reach when requiring, can utilize the compensation of refrigeration module refrigeration, reaches necessary requirement; The moisture separator temperature reduces, and makes that compressed-air actuated saturation moisture content is reduced to 5.88g/m in the moisture separator
3At last, be depressured to outside product gas (dew point under the atmospheric pressure is approximately-16 ℃) the output jar of 0.01MPa.
Claims (7)
1. efficient energy-saving saturation dehumidifier, it is characterized in that, this device comprises thermally insulated container body, choke valve, moisture separator, described moisture separator is located in the thermally insulated container body, described moisture separator is connected with choke valve, the compressed air inlet pipe of described moisture separator is connected to the thermally insulated container external body, and the condensating water outlet tube of described moisture separator is connected to the thermally insulated container external body.
2. efficient energy-saving saturation dehumidifier according to claim 1 is characterized in that, also comprises refrigeration module, and this refrigeration module is located on the compressed air inlet pipe outer wall.
3. efficient energy-saving saturation dehumidifier according to claim 1 is characterized in that, described choke valve is located at thermally insulated container body inner top.
4. efficient energy-saving saturation dehumidifier according to claim 1 is characterized in that, described compressed air inlet pipe is located at moisture separator side top.
5. efficient energy-saving saturation dehumidifier according to claim 1 is characterized in that, described condensating water outlet tube is located at the moisture separator bottom.
6. efficient energy-saving saturation dehumidifier according to claim 1 is characterized in that, below, described thermally insulated container side is provided with product gas outlet.
7. the application process of an efficient energy-saving saturation dehumidifier as claimed in claim 1 is characterized in that, this method may further comprise the steps:
(1) compresses cooled air through air compressor and enter moisture separator;
(2) moisture content that surpasses saturation moisture content in the compressed air is condensed to the bottom of moisture separator, and flows out by condensating water outlet tube;
(3) compressed air through dehumidifying enters in the diffusion chamber of thermally insulated container body by choke valve;
(4) the compressed air volumetric expansion becomes big, and pressure reduces, and absorbs heat, makes moisture separator lower the temperature;
(5) the moisture separator temperature reduces, and reduces compressed-air actuated saturation moisture content in the moisture separator;
(6) outside the product gas output device after the step-down.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2008100375666A CN101579597B (en) | 2008-05-16 | 2008-05-16 | Efficient energy-saving saturation dehumidifier and application method thereof |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2008100375666A CN101579597B (en) | 2008-05-16 | 2008-05-16 | Efficient energy-saving saturation dehumidifier and application method thereof |
Publications (2)
Publication Number | Publication Date |
---|---|
CN101579597A CN101579597A (en) | 2009-11-18 |
CN101579597B true CN101579597B (en) | 2011-08-24 |
Family
ID=41361996
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN2008100375666A Expired - Fee Related CN101579597B (en) | 2008-05-16 | 2008-05-16 | Efficient energy-saving saturation dehumidifier and application method thereof |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN101579597B (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103053991A (en) * | 2013-01-04 | 2013-04-24 | 菱花集团有限公司 | Energy-saving cooling method and energy-saving cooling device of compressed air for aerobic microbial fermentation system |
CN112058033A (en) * | 2020-09-08 | 2020-12-11 | 浙江中控技术股份有限公司 | Compressed air dehumidifying device |
-
2008
- 2008-05-16 CN CN2008100375666A patent/CN101579597B/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
CN101579597A (en) | 2009-11-18 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN105420750A (en) | System and method for recycling compression heat of hydrogen gas produced by water electrolysis | |
CN101899341A (en) | Adsorption type high pressure natural gas dehydration process and device | |
CN210495768U (en) | Device for recycling dichloromethane of diaphragm of lithium battery by wet process through compression condensation membrane separation technology | |
CN101906800A (en) | Vacuum dehumidification membrane based device and method for recovering liquid state water from air | |
CN108870878A (en) | Direct heat pump integrates transformation drying system and method | |
CN201493042U (en) | Residual heat type combined low-dew point dryer | |
CN101579597B (en) | Efficient energy-saving saturation dehumidifier and application method thereof | |
CN213556279U (en) | Carbon dioxide ammonia method capturing and low-temperature liquefying system of coal-fired power plant | |
CN104163404B (en) | Recoverying and utilizing method and the device of dirty oxide gas is regenerated in nitrogen purification process | |
CN202109725U (en) | Cooling and dehumidifying device of small-sized space division precooling system | |
CN211198605U (en) | Efficient energy-saving oxygen generator | |
CN202756905U (en) | Evaporated-gas recovery device for carbon dioxide storage tank | |
CN201205486Y (en) | Efficient energy saving type saturation dehydrating device | |
CN102229427B (en) | Carbon dioxide purifying device | |
CN214512791U (en) | Energy-saving neon gas purification device | |
CN202778223U (en) | Composite dehumidifier | |
CN201404762Y (en) | Adsorption high-pressure natural gas dehydration unit | |
CN206362002U (en) | Freezing type drier | |
CN201768479U (en) | Zero-air rate low-dew point waste heat recyclable adsorption type drier | |
CN101601959A (en) | A kind of Zero gas consumption low dew point compression heat regeneration absorption compressed air drying method and device thereof | |
CN203829869U (en) | Zero-gas-consumption compression heat regeneration adsorption type drying machine | |
CN2873282Y (en) | Organic waste gas condensation method recovery device | |
CN206778157U (en) | A kind of waste heat regeneration air drying device | |
CN208651072U (en) | It is a kind of can high-temp resisting high-humidity resisting vacuum pump system | |
CN101000206B (en) | Compression gas afterheat regeneration drying process without gas consumption |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
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: 20110824 Termination date: 20170516 |
|
CF01 | Termination of patent right due to non-payment of annual fee |