CN203635042U - Gas dryer - Google Patents
Gas dryer Download PDFInfo
- Publication number
- CN203635042U CN203635042U CN201320837001.2U CN201320837001U CN203635042U CN 203635042 U CN203635042 U CN 203635042U CN 201320837001 U CN201320837001 U CN 201320837001U CN 203635042 U CN203635042 U CN 203635042U
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- gas
- inner core
- distributor
- drier
- inner barrel
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Abstract
The utility model relates to the field of dryers, in particular to a gas dryer. The gas dryer comprises a tank body which comprises an outer barrel and an inner barrel, wherein a gas inlet and a gas outlet are formed on the inner barrel, a cooling coiled pipe is arranged between the outer barrel and the inner barrel, sieve plates are arranged in the inner barrel, a drying agent, namely a molecular sieve desiccant or aluminum oxide, is arranged between the sieve plates, and a gas distributor is arranged in the gas outlet of the inner barrel. With the adoption of the technical scheme, the gas dryer has the beneficial effects that the drying effect is good, and as the temperature of a drying agent bed layer can be kept in an appropriate range during drying, the adsorbing capacity of the drying agent bed layer can be ensured, and the qualified content of water in gas entering the next link is ensured.
Description
Technical field
the utility model relates to drier field, especially a kind of gas-drying apparatus.
Background technology
in working order, mist is entered by air inlet traditional drier, has the moisture in the drying machine absorption mist in urceolus.Because the molecular sieve of loading or aluminium oxide can produce heat of adsorption when adsorption moisture at normal temperatures, impel the drier adsorbent bed temperature qualification in the outer cylinder body of drier, moving rising, cause the adsorbed water capacity of the drier such as molecular sieve or aluminium oxide obviously to reduce, and adsorption deeply variation.
Because molecular sieve is to adsorb at normal temperatures, and the higher adsorption deeply of adsorption bed temperature is poorer, and adsorption capacity is less.When drier is in lower time in regeneration stage, regeneration gas is through the built-in heater of inner barrel, and after heating, thermal current reaches molecular sieve or alumina desiccant bed, after the temperature of molecular sieve or aluminium oxide raises, the moisture of absorption is resolved out, is reproduced gas and brings to outdoor.After drier regeneration heating, enter cooling stage, tightly utilize regeneration gas to carry out cooling down to drier bed in traditional structure, the effect of cooling is undesirable and temperature fall time is long, need to consume a large amount of regeneration gas.
Utility model content
the technical problems to be solved in the utility model is: overcome in prior art in drier the temperature of drier bed high, the little technical deficiency of adsorbance while adsorbing work, provides the gas-drying apparatus that a kind of drier bed adsorbance is large, temperature maintains optimum range.
For solving the problems of the technologies described above, the technical solution adopted in the utility model is as follows:
A kind of gas-drying apparatus, comprise tank body, described tank body comprises urceolus and inner core, inner core is provided with gas feed and gas vent, between described urceolus and inner core, be provided with cooling coil, in inner core, be provided with sieve plate, between sieve plate, be provided with drier, described drier is the one in molecular sieve desiccant or aluminium oxide, and described inner core gas vent is provided with gas distributor.
Further, the spiral inner core periphery that is distributed in of described cooling coil, has cooling water inlet and coolant outlet on described urceolus, and described cooling water inlet and coolant outlet are connected respectively at the two-port of described cooling coil.
Further, described gas distributor comprises 3 flaring hollow distributor pipes, and described distributor pipe is socketed mutually, has common gas outlet.
Further, in described gas distributor, there is molecular sieve drying layer.
Adopt the beneficial effect of the technical solution of the utility model to be: gas-drying apparatus drying effect of the present utility model is good, and the temperature of drier bed can maintain in a suitable scope in dry run, thereby guarantee the adsorbance of drier bed, the measurement of moisture content of gas of guaranteeing to enter next link is qualified.
Accompanying drawing explanation
Fig. 1 is the structural representation of gas-drying apparatus of the present utility model.
In figure, 1 is gas feed, and 2 is gas vent, and 3 is coolant outlet, and 4 is cooling water inlet, and 5 is cooling coil, and 6 is gas distributor, and 7 is urceolus, and 8 is inner core, and 9 is sieve plate, and 10 is drier, and 11 is molecular sieve drying layer.
The specific embodiment
Below in conjunction with the drawings and specific embodiments, the utility model is described further.
As shown in Fig. 1, gas-drying apparatus of the present utility model comprises tank body, described tank body comprises urceolus 7 and inner core 8, inner core 8 is provided with gas feed 1 and gas vent 2, between described urceolus 7 and inner core 8, is provided with cooling coil 5, is provided with sieve plate 9 in inner core 8, between sieve plate 9, be provided with drier 10, described drier 10 is the one in molecular sieve desiccant or aluminium oxide, and the drying effect of molecular sieve desiccant and aluminium oxide is good, and described inner core 8 gas vents 2 are provided with gas distributor 6.
Further, in order to ensure not generating heat after drier bed adsorption moisture, guarantee adsorption deeply and adsorbance, spiral inner core 8 peripheries that are distributed in of described cooling coil 5, on described urceolus 7, have cooling water inlet 4 and coolant outlet 3, described cooling water inlet 4 and coolant outlet 3 are connected respectively at the two-port of described cooling coil 5.
Further, in order to distribute air-flow and guarantee to enter moisture-free in the gas of next link, described gas distributor 6 comprises 3 flaring hollow distributor pipes, and described distributor pipe is socketed mutually, has common gas outlet.
Further, in order to ensure entering moisture-free in the gas of next link, in described gas distributor 6, there is molecular sieve drying layer 11.
Claims (4)
1. a gas-drying apparatus, comprise tank body, described tank body comprises urceolus and inner core, inner core is provided with gas feed and gas vent, it is characterized in that: between described urceolus and inner core, be provided with cooling coil, in inner core, be provided with sieve plate, between sieve plate, be provided with drier, described drier is the one in molecular sieve desiccant or aluminium oxide, and described inner core gas vent is provided with gas distributor.
2. a kind of gas-drying apparatus according to claim 1, it is characterized in that: the spiral inner core periphery that is distributed in of described cooling coil, on described urceolus, have cooling water inlet and coolant outlet, described cooling water inlet and coolant outlet are connected respectively at the two-port of described cooling coil.
3. a kind of gas-drying apparatus according to claim 1, is characterized in that: described gas distributor comprises 3 flaring hollow distributor pipes, and described distributor pipe is socketed mutually, has common gas outlet.
4. a kind of gas-drying apparatus according to claim 3, is characterized in that: in described gas distributor, have molecular sieve drying layer.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320837001.2U CN203635042U (en) | 2013-12-18 | 2013-12-18 | Gas dryer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320837001.2U CN203635042U (en) | 2013-12-18 | 2013-12-18 | Gas dryer |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203635042U true CN203635042U (en) | 2014-06-11 |
Family
ID=50866326
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320837001.2U Expired - Fee Related CN203635042U (en) | 2013-12-18 | 2013-12-18 | Gas dryer |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203635042U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105688673A (en) * | 2014-11-26 | 2016-06-22 | 安徽智新生化有限公司 | Dehydrating device |
-
2013
- 2013-12-18 CN CN201320837001.2U patent/CN203635042U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105688673A (en) * | 2014-11-26 | 2016-06-22 | 安徽智新生化有限公司 | Dehydrating device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| ASS | Succession or assignment of patent right |
Owner name: HENAN HUANYU PETROCHEMICAL EQUIPMENT TECHNOLOGY CO Free format text: FORMER OWNER: DING QI Effective date: 20150814 |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20150814 Address after: Xiuwu County, Henan province 454350 industrial agglomeration area in Jiaozuo City, the middle of the road on the south side of Yunxiang Patentee after: HENAN HUANYU PETROCHEMICAL EQUIPMENT TECHNOLOGY Co.,Ltd. Address before: 225500, 8, five Zhuang village, Jiangyan Town, Jiangyan City, Jiangsu, Taizhou Patentee before: Ding Qi |
|
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20140611 Termination date: 20211218 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |