CN203264537U - Micro-heat absorption drier with energy saving device - Google Patents
Micro-heat absorption drier with energy saving device Download PDFInfo
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- CN203264537U CN203264537U CN 201320270365 CN201320270365U CN203264537U CN 203264537 U CN203264537 U CN 203264537U CN 201320270365 CN201320270365 CN 201320270365 CN 201320270365 U CN201320270365 U CN 201320270365U CN 203264537 U CN203264537 U CN 203264537U
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- absorption tower
- adsorption tower
- drier
- absorption
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Abstract
The utility model discloses a micro-heat absorption drier with an energy saving device. The micro-heat absorption drier comprises a base, a first absorption tower and a second absorption tower, wherein the first absorption tower and the second absorption tower are arranged on the base. A control box is arranged between the first absorption tower and the second absorption tower, the upper parts of the first absorption tower and the second absorption tower are connected with an upper valve system, and the lower parts of the first absorption tower and the second absorption tower are connected with a lower valve system. When a drying agent regenerates, hot air of 150 DEG C is utilized for desorption from bottom to top one layer by one layer. The 1/4 position of each absorption tower is provided with an energy saving device, and the front part of each energy saving device is provided with a temperature sensing rod for control, so that heating can be finished early, and the heating energy consumption is saved. As cooling and heating are on the same direction, the drying agent which does not finish desorption can utilize waste heat brought by the cooling process to carry out final desorption. The micro-heat absorption drier utilizes the waste heat to cause the heating to be finished early, and 20 percent (minus 40 DEG C) of energy can be saved.
Description
Technical field
The utility model relates to a kind of compressed air treatment device, particularly a kind of low-grade fever absorption drier that is provided with energy saver.
Background technology
The compressed air purifying industry is progressively rise and develop industry faster in China in recent years, under the situation of global available resources growing tension, utilize compressed air as power source general be applied in all trades and professions, but along with being growing more intense of market competition, also more and more higher to the requirement of product quality and manufacturing cost.Therefore need to purify compressed air, the dry processing.Existing drying machine mainly comprises low-grade fever formula absorption drier and freezing type drier.Low-grade fever formula absorption drier is better with its drying effect, can reach-70 above pressure leak sources of degree and enjoys and have the industry of requirements at the higher level to favor to compressed air quality.The absorption drier of existing low-grade fever formula mainly comprises the first adsorption tower, the second adsorption tower, absorption direction bottom in and top out, compressed air from lower to upper, thereby cause: 1. the upper strata drier easily produces fluidisation, drier thereby generation collision, easily there is dust to produce, causes the loss of drier and filter relatively to increase.2. the drier that adsorbs from lower to upper, the replacing engineering of drier can't segmentation be carried out, therefore can't effectively save the drier renewal cost after first being polluted by oil content in the bottom.3. air-flow from lower to upper, the end drier can't be fixed in a down-to-earth manner, aqueous vapor easily diffuses to outlet, affects drying effect.
The utility model content
In order to solve the deficiencies in the prior art, the purpose of this utility model is to provide a kind of low-grade fever absorption drier that is provided with energy saver.
the purpose of this utility model is achieved by the following technical solution: the utility model comprises base, be located at the first adsorption tower and the second adsorption tower on base, be provided with control cabinet between the first adsorption tower and the second adsorption tower, being connected with valve on the top of the first adsorption tower and the second adsorption tower is, described upper valve is to comprise pneumatic operated valve, upper tube connector and compressed air inlet, being connected with lower valve in the bottom of the first adsorption tower and the second adsorption tower is, described lower valve is to comprise non-return valve, lower tube connector and compressed air outlet, an energy saver is installed respectively in 1/4 position above described the first adsorption tower and the second adsorption tower.
As a kind of improvement of the present utility model, described energy saver its front portion is provided with a sensing rod for temperature.
The beneficial effect that the utility model is obtained: the absorption direction of low-grade fever absorption drier described in the utility model is upper entering and lower leaving, and approximately an energy saver is respectively installed in 1/4 position above the first adsorption tower and the second adsorption tower, its front portion is provided with a sensing rod for temperature temperature is controlled, and can allow heat time heating time and finish in advance to save the heating power consumption; 2, the cooling and heating design direction of low-grade fever absorption drier described in the utility model is in the same way, therefore desorption drier completely not can utilize the used heat of taking out of in cooling process to carry out last desorption, and reach energy-conservation purpose.
Description of drawings
Fig. 1 is structural representation of the present utility model.
Fig. 2 is that the utility model energy saver is arranged on the structural representation on adsorption tower.
The specific embodiment
Below in conjunction with accompanying drawing, the utility model is further elaborated explanation:
shown in figure, the low-grade fever absorption drier that is provided with energy saver described in the utility model, comprise base 1, be located at the first adsorption tower 5 and the second adsorption tower 9 on base 1, be provided with control cabinet 10 between the first adsorption tower 5 and the second adsorption tower 9, being connected with valve on the top of the first adsorption tower 5 and the second adsorption tower 9 is, described upper valve is to comprise tube connector 8 and compressed air inlet 7 on pneumatic operated valve 6, being connected with lower valve in the bottom of the first adsorption tower 5 and the second adsorption tower 9 is, described lower valve is to comprise non-return valve 3, lower tube connector 4 and compressed air outlet 2, an energy saver 12 is installed respectively in 1/4 position above the first adsorption tower 5 and the second adsorption tower 9, the front portion of described energy saver 12 is provided with a sensing rod for temperature 11.
Described a kind of absorption direction that is provided with the low-grade fever absorption drier of energy saver is upper entering and lower leaving, utilizing approximately during desiccant regeneration, the hot gas of 150 ℃ in layer carries out desorption from lower to upper, and above in the first adsorption tower 5 and the second adsorption tower 9 approximately 1/4 position one energy saver 12 respectively is installed, the front of energy saver 12 is provided with 11 pairs of temperature of sensing rod for temperature and controls, and can allow heat time heating time and finish in advance to save the heating power consumption.Because of cooling and heating design direction in the same way, therefore desorption drier completely not can utilize the used heat of taking out of in cooling process to carry out last desorption, and reach energy-conservation purpose.
The above is only the preferred embodiment of utility model; be not limited in above utility model; it is identical with the above-mentioned principle of describing in principle; for all any modifications of doing within spirit of the present utility model and principle, be equal to and replace and improvement etc., all should be included in protection domain of the present utility model.
Claims (2)
1. low-grade fever absorption drier that is provided with energy saver, comprise base, be located at the first adsorption tower and the second adsorption tower on base, be provided with control cabinet between the first adsorption tower and the second adsorption tower, being connected with valve on the top of the first adsorption tower and the second adsorption tower is, described upper valve is to comprise pneumatic operated valve, upper tube connector and compressed air inlet, being connected with lower valve in the bottom of the first adsorption tower and the second adsorption tower is, described lower valve is to comprise non-return valve, lower tube connector and compressed air outlet, it is characterized in that: an energy saver is installed respectively in 1/4 position above described the first adsorption tower and the second adsorption tower.
2. a kind of low-grade fever absorption drier that is provided with energy saver as claimed in claim 1 is characterized in that: described energy saver its front portion is provided with a sensing rod for temperature.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320270365 CN203264537U (en) | 2013-05-17 | 2013-05-17 | Micro-heat absorption drier with energy saving device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320270365 CN203264537U (en) | 2013-05-17 | 2013-05-17 | Micro-heat absorption drier with energy saving device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203264537U true CN203264537U (en) | 2013-11-06 |
Family
ID=49495032
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201320270365 Expired - Fee Related CN203264537U (en) | 2013-05-17 | 2013-05-17 | Micro-heat absorption drier with energy saving device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203264537U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104275079A (en) * | 2014-09-26 | 2015-01-14 | 吴江市欧诚包装材料制品有限公司 | Adsorption type air dryer |
-
2013
- 2013-05-17 CN CN 201320270365 patent/CN203264537U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104275079A (en) * | 2014-09-26 | 2015-01-14 | 吴江市欧诚包装材料制品有限公司 | Adsorption type air dryer |
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Legal Events
| 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 | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20131106 Termination date: 20200517 |