CN205361002U - A drying device for hydrocarbon mixture production - Google Patents
A drying device for hydrocarbon mixture production Download PDFInfo
- Publication number
- CN205361002U CN205361002U CN201620136361.3U CN201620136361U CN205361002U CN 205361002 U CN205361002 U CN 205361002U CN 201620136361 U CN201620136361 U CN 201620136361U CN 205361002 U CN205361002 U CN 205361002U
- Authority
- CN
- China
- Prior art keywords
- drying tower
- drying
- hydrocarbon mixture
- air inlet
- air outlet
- 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
Landscapes
- Drying Of Solid Materials (AREA)
Abstract
The utility model discloses a drying device for hydrocarbon mixture production, it includes the drying tower, be provided with the molecular sieve in the drying tower, the lower extreme of drying tower is provided with the drying tower air inlet, the first admission valve and feed gas tube coupling of drying tower air inlet department, the second admission valve is connected with the gas outlet of heater, and the third admission valve is connected with the subsidiary conduit, the upper end of drying tower is provided with the drying tower gas outlet, the first air outlet valve of drying tower gas outlet department is connected with feed gas exhaust pipe, and the second air outlet valve passes through the air inlet of pipe connection heat exchanger, and the third air outlet valve passes through the pipe connection extremely the air inlet of heater. The utility model discloses a drying device for hydrocarbon mixture production can carry out degree of depth dehydration to the feed gas to reach better drying effect, and drying efficiency is high, use cost is lower, and is convenient for maintain the maintenance.
Description
Technical field
This utility model relates to hydrocarbon mixture and produces equipment technical field, particularly relates to a kind of drying device produced for hydrocarbon mixture.
Background technology
Hydrocarbon mixture production process needs unstripped gas is dried dehydration, traditional handicraft all adopts simple thermal dehydration mode, this dewatering costs and poor dehydration results, it is extremely difficult to the deep dehydration of designing requirement, and dehydration equipment power consumption is higher, in turn result in use cost to increase, and be not easy to maintaining.
Utility model content
For this, the technical problems to be solved in the utility model is to overcome existing hydrocarbon mixture drying device above shortcomings, and then dehydrating effect is good, use cost is low to provide one, and is easy to the drying device produced for hydrocarbon mixture of maintaining.
For achieving the above object, this utility model is by the following technical solutions:
A kind of drying device produced for hydrocarbon mixture, it includes drying tower, it is provided with molecular sieve in described drying tower, the lower end of described drying tower is provided with drying tower air inlet, described drying tower air inlet place is provided with the first intake valve, the second intake valve, the 3rd intake valve, described first intake valve is connected with unstripped gas pipeline, and described second intake valve is connected with the gas outlet of heater, and described 3rd intake valve is connected with subsidiary conduit；The upper end of described drying tower is provided with drying tower gas outlet, described drying tower gas outlet place is provided with the first air outlet valve, the second air outlet valve, the 3rd air outlet valve, described first air outlet valve is connected with unstripped gas gas exhaust piping, described second air outlet valve connects the air inlet of heat exchanger by pipeline, and described 3rd air outlet valve is connected to the air inlet of described heater by pipeline.
Preferably, each described drying device produced for hydrocarbon mixture at least includes two described drying towers, and air inlet and the gas outlet of adjacent two described drying towers are connected in parallel by pipeline.
Preferably, described heater is electric heater.
Preferably, described molecular sieve is 4A molecular sieve.
The beneficial effects of the utility model:
Unstripped gas can be carried out deep dehydration by the drying device produced for hydrocarbon mixture of the present utility model, and to reach good drying effect, and drying efficiency is high, and use cost is relatively low, and is easy to maintaining.
Accompanying drawing explanation
In order to make content of the present utility model be more likely to be clearly understood, below in conjunction with accompanying drawing, this utility model is described in further detail, wherein:
Fig. 1 is the structural representation of the drying device produced for hydrocarbon mixture of the present utility model.
In figure, accompanying drawing labelling is expressed as:
1-drying tower；11-the first intake valve；12-the second intake valve；13-the 3rd intake valve；14-the first air outlet valve；15-the second air outlet valve；16-the 3rd air outlet valve；2-unstripped gas pipeline；3-heater；4-subsidiary conduit；5-unstripped gas gas exhaust piping；6-heat exchanger.
Detailed description of the invention
Referring to Fig. 1, a kind of drying device produced for hydrocarbon mixture, it includes drying tower 1, it is provided with molecular sieve in described drying tower 1, described molecular sieve is 4A molecular sieve, the lower end of described drying tower 1 is provided with drying tower air inlet, described drying tower air inlet place is provided with first intake valve the 11, second intake valve the 12, the 3rd intake valve 13, described first intake valve 11 is connected with unstripped gas pipeline 2, described second intake valve 12 is connected with the gas outlet of heater 3, described heater 3 is electric heater, and described 3rd intake valve 13 is connected with subsidiary conduit 4；The upper end of described drying tower 1 is provided with drying tower gas outlet, described drying tower gas outlet place is provided with first air outlet valve the 14, second air outlet valve the 15, the 3rd air outlet valve 16, described first air outlet valve 14 is connected with unstripped gas gas exhaust piping 5, described second air outlet valve 15 connects the air inlet of heat exchanger 6 by pipeline, and described 3rd air outlet valve 16 is connected to the air inlet of described heater 3 by pipeline.
Referring to Fig. 1, the drying device for hydrocarbon mixture production of the present embodiment includes three described drying towers 1, air inlet and the gas outlet of adjacent two described drying towers 1 are connected in parallel by pipeline, namely first intake valve the 11, second intake valve the 12, the 3rd intake valve the 13, first air outlet valve the 14, second air outlet valve the 15, the 3rd on each drying tower gives vent to anger 16 respectively through pipeline communication, in order to improve production efficiency.
Originally it is the chemical science and technology senior for the drying device employing of hydrocarbon mixture production of utility model, utilize saturated compression water in air molecule different from air molecule volume, the dedicated molecular sieve used filtration of gas purification is adopted to remove the moisture compressed in unstripped gas, can easily by Water Molecular Adsorption in sieve particle, recycling renovation process come redox molecule sieve.Having used 4A molecular sieve to do filler, unstripped gas can have been carried out deep dehydration to below 100ppm, after unstripped gas carries out deep dehydration, molecular sieve contains substantial amounts of moisture；Heat to 200 DEG C from drying tower cold dry gas out through electric heater, molecular sieve in drying tower is carried out regeneration dehydration, then with drying tower cold dry gas (about 15 DEG C) out, the molecular sieve after heating is cooled to room temperature, does absorbent drying after cooling again and use.Drying tower three state respectively cold blowings, absorption, regeneration, change once for every 12 hours.
Unstripped gas can be carried out deep dehydration by the drying device produced for hydrocarbon mixture of the present utility model, and to reach good drying effect, and drying efficiency is high, and use cost is relatively low, and is easy to maintaining.
The technical solution of the utility model is simply explained in detail by above-mentioned detailed description of the invention; this utility model is not only limited only to above-described embodiment; those skilled in the art should be understood that; every improvement according to above-mentioned principle and spirit on this utility model basis, replacement, all should within protection domain of the present utility model.
Claims (4)
1. the drying device produced for hydrocarbon mixture, it is characterized in that: include drying tower, it is provided with molecular sieve in described drying tower, the lower end of described drying tower is provided with drying tower air inlet, described drying tower air inlet place is provided with the first intake valve, the second intake valve, the 3rd intake valve, described first intake valve is connected with unstripped gas pipeline, and described second intake valve is connected with the gas outlet of heater, and described 3rd intake valve is connected with subsidiary conduit；The upper end of described drying tower is provided with drying tower gas outlet, described drying tower gas outlet place is provided with the first air outlet valve, the second air outlet valve, the 3rd air outlet valve, described first air outlet valve is connected with unstripped gas gas exhaust piping, described second air outlet valve connects the air inlet of heat exchanger by pipeline, and described 3rd air outlet valve is connected to the air inlet of described heater by pipeline.
2. the drying device produced for hydrocarbon mixture according to claim 1, it is characterized in that: each described drying device produced for hydrocarbon mixture at least includes two described drying towers, and air inlet and the gas outlet of adjacent two described drying towers are connected in parallel by pipeline.
3. the drying device produced for hydrocarbon mixture according to claim 1, it is characterised in that: described heater is electric heater.
4. the drying device produced for hydrocarbon mixture according to claim 1, it is characterised in that: described molecular sieve is 4A molecular sieve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620136361.3U CN205361002U (en) | 2016-02-23 | 2016-02-23 | A drying device for hydrocarbon mixture production |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620136361.3U CN205361002U (en) | 2016-02-23 | 2016-02-23 | A drying device for hydrocarbon mixture production |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205361002U true CN205361002U (en) | 2016-07-06 |
Family
ID=56272084
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620136361.3U Expired - Fee Related CN205361002U (en) | 2016-02-23 | 2016-02-23 | A drying device for hydrocarbon mixture production |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205361002U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN116440664A (en) * | 2023-06-20 | 2023-07-18 | 德州能奥石油科技有限公司 | Drying device for mixed hydrocarbon production |
-
2016
- 2016-02-23 CN CN201620136361.3U patent/CN205361002U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN116440664A (en) * | 2023-06-20 | 2023-07-18 | 德州能奥石油科技有限公司 | Drying device for mixed hydrocarbon production |
| CN116440664B (en) * | 2023-06-20 | 2023-08-22 | 德州能奥石油科技有限公司 | Drying device for mixed hydrocarbon production |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN205361002U (en) | A drying device for hydrocarbon mixture production | |
| CN204337980U (en) | A kind of carbon dioxide capture device | |
| CN204513433U (en) | A kind of boiler flue waste heat recycling system | |
| CN208504987U (en) | A kind of solar energy drying system | |
| CN106753633A (en) | A kind of natual gas dehydrate unit | |
| CN206256033U (en) | A kind of natual gas dehydrate unit of utilization new energy thermal regeneration | |
| CN203454882U (en) | Steam waste heat recovery system | |
| CN204678065U (en) | A kind of dehydration regeneration cooling system of natural gas pipe network pressure energy reclaiming system | |
| CN204311038U (en) | A kind of energy-saving natual gas dehydrate unit | |
| CN202682825U (en) | Acid mist recovery device of reaction kettle for producing polymeric aluminum | |
| CN206037312U (en) | Solution humidifying unit with heat pipe formula heat recovery device | |
| CN202482054U (en) | Hydrogen preparation device | |
| CN206881444U (en) | VOC purifying processing devices | |
| CN205748055U (en) | A kind of liquid nitrogen off gas energy recovery device | |
| CN205279853U (en) | Last circulation water heat exchanger of rectisol plant | |
| CN203530266U (en) | Drying device for preparing compressed biogas by using methane | |
| CN202648473U (en) | Tail gas heat exchanging device for nickel alloy production kiln | |
| CN203069002U (en) | Thermal converter | |
| CN202938378U (en) | Water heater for heating by waste heat of hearth | |
| CN205330773U (en) | High temperature tail gas recycle evaporation plant | |
| CN207545874U (en) | A kind of multitube demister | |
| CN208145727U (en) | A kind of dry purification devices of energy-efficient carbon dioxide | |
| CN202876626U (en) | Alkane dehydration device | |
| CN203525356U (en) | Solvent tail gas recycling device | |
| CN205313588U (en) | Pure dry process dust removal gas cooler of converter |
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 |
Granted publication date: 20160706 Termination date: 20210223 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |