CN201832437U - Submerged coiled tube condenser - Google Patents
Submerged coiled tube condenser Download PDFInfo
- Publication number
- CN201832437U CN201832437U CN2010205971945U CN201020597194U CN201832437U CN 201832437 U CN201832437 U CN 201832437U CN 2010205971945 U CN2010205971945 U CN 2010205971945U CN 201020597194 U CN201020597194 U CN 201020597194U CN 201832437 U CN201832437 U CN 201832437U
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- China
- Prior art keywords
- settling tank
- coiled tube
- settling
- submerged
- layer
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- 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
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Abstract
A submerged coiled tube condenser consists of three settling tanks, an upper-layer gas cooling coiled tube, a lower-layer liquid cooling coiled tube and a water pond. The three settling tanks, the upper-layer gas cooling coiled tube and the lower-layer liquid cooling coiled tube are fixedly mounted in the water pond, the first settling tank is connected with the second settling tank via upper and lower connecting pipes, the upper-layer gas cooling coiled tube and the lower-layer liquid cooling coiled tube are respectively connected to the upper portions and the lower portions of the second settling tank and the third settling tank, an oil gas inlet is disposed on the upper portion of the first settling tank, and a liquid oil outlet is arranged on the lower portion of the third settling tank. The submerged coiled tube condenser is simple in structure and convenient in manufacture, avoids problems that other condensing equipment is more complex in internal structure design, leakage cannot be found out easily and repair and cleaning are inconvenient, is fewer in bonding points, easy in manufacture and low in production cost, is large in area contacting with water due to submerged natural cooling, does not need any power during production, is convenient in maintenance and repair, is more sufficient in cooling compared with other types of condensers, is fast in speed, and is safe and reliable.
Description
Technical field
The utility model relates to a kind of condensing plant that is used for the oil plant chemical industry.
Background technology
Used condensing plant mostly is the shell and tube condensing plant greatly in producing at present, and these equipment exist production efficiency low mostly, and the manufacturing cost height cool off insufficiently, problem such as lacks service life.Because the insufficient part oil product that makes of cooling can not reclaim fully, cause output to reduce, and can produce unsafe factor.Manufacture view causes material and artificial input to strengthen cost up because structure is complicated.
Summary of the invention
The technical problems to be solved in the utility model is: it is simple to design a kind of technology, and cooling is abundant, and the immersion type coil condenser of low cost of manufacture is to overcome the problem that prior art exists.
The technical scheme that solution the utility model problem is taked is: it is made up of three settling tanks, top tank air cooling coil, lower floor's liquid cooling coil and pond, and three settling tanks, top tank air cooling coil, lower floor's liquid cooling coils all are fixed in the pond; First settling tank and second settling tank are connected by two tube connectors up and down, and top tank air cooling coil and lower floor's liquid cooling coil are connected to second settling tank and the 3rd settling tank upper and lower; The oil gas inlet is located at the first settling tank top, and the liquid oils outlet is located at the 3rd settling tank bottom.
Be convenient for maintaining and cleaning, the coil pipe two ends are connected with flange by U type elbow.
Good effect of the present utility model is: simple in structure, and convenient the manufacturing; Unlike other condensing plant internal structure design more complicated, leakage phenomenon is arranged, be difficult for also finding that maintenance of clean-up is also inconvenient; Binding site is less, and is easy to manufacture, and production cost is low; Since be that immersion type cools off naturally, big with the contact area of water, without any need for power, be convenient to maintenance and repair during production, and more abundant than the condenser cooling of other type, and speed is fast, and is safe and reliable.
Description of drawings
Accompanying drawing 1 is the utility model structural representation; Accompanying drawing 2 is the schematic top plan view of accompanying drawing 1.
The specific embodiment
Shown in accompanying drawing 1,2, it is made up of three settling tanks 1,4,5, top tank air cooling coil 2, lower floor's liquid cooling coil 3 and pond 6, and three settling tanks 1,4,5, top tank air cooling coil 2, lower floor's liquid cooling coils 3 are fixed in the pond 6; First settling tank 5 and second settling tank 4 are connected by two tube connectors 7,8 up and down, and top tank air cooling coil 2 and lower floor's liquid cooling coil 3 are connected to second settling tank 4 and the 3rd settling tank 1 upper and lower; Oil gas inlet 9 is located at first settling tank, 5 tops, and liquid oils outlet 10 is located at the 3rd settling tank 1 bottom.The two ends of pipe are connected with U type elbow 12 with flange 11 respectively, clear up with convenient for maintaining.
The operation principle of the present utility model and the course of work: at first with oil gas inlet 9 inputs of thermal cracking oil gas from first settling tank 5, the 5 buffering sedimentations of first settling tank make powdery ash fall and portion of hot cracked oil gas liquefaction in the oil gas; Oil gas enters second settling tank 4, and some dust and liquid secondary settlement enter top tank air cooling coil 2 by the oil gas behind the secondary settlement and carry out condensation liquefaction again, and the liquid oils after the liquefaction flows into the 3rd settling tank 1; Fluid after second settling tank, 4 bottom sedimentations this moment flows into lower floor's liquid cooling coil 3 and cools off, and cooled liquid oils flows into the 3rd settling tank 1, and complete cooled liquid oils flows into oil storage tank by the 3rd settling tank 1, and whole condensation process finishes.
Claims (2)
1. immersion type coil condenser, it is characterized in that: it is made up of three settling tanks, top tank air cooling coil, lower floor's liquid cooling coil and pond, and three settling tanks, top tank air cooling coil, lower floor's liquid cooling coils all are fixed in the pond; First settling tank and second settling tank are connected by two tube connectors up and down, and top tank air cooling coil and lower floor's liquid cooling coil are connected to second settling tank and the 3rd settling tank upper and lower; The oil gas inlet is located at the first settling tank top, and the liquid oils outlet is located at the 3rd settling tank bottom.
2. immersion type coil condenser according to claim 1 is characterized in that: the coil pipe two ends are connected with flange by U type elbow.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010205971945U CN201832437U (en) | 2010-11-02 | 2010-11-02 | Submerged coiled tube condenser |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010205971945U CN201832437U (en) | 2010-11-02 | 2010-11-02 | Submerged coiled tube condenser |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201832437U true CN201832437U (en) | 2011-05-18 |
Family
ID=44002534
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010205971945U Expired - Fee Related CN201832437U (en) | 2010-11-02 | 2010-11-02 | Submerged coiled tube condenser |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201832437U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20140377155A1 (en) * | 2013-06-21 | 2014-12-25 | Phillips 66 Company | Process for in-situ production of low dissolved hydrogen sulfide, degassed, sulfur from claus sulfur recovery |
-
2010
- 2010-11-02 CN CN2010205971945U patent/CN201832437U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20140377155A1 (en) * | 2013-06-21 | 2014-12-25 | Phillips 66 Company | Process for in-situ production of low dissolved hydrogen sulfide, degassed, sulfur from claus sulfur recovery |
| US9192887B2 (en) * | 2013-06-21 | 2015-11-24 | Phillips 66 Company | Process for in-situ production of low dissolved hydrogen sulfide, degassed, sulfur from claus sulfur recovery |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20110518 Termination date: 20111102 |