CN204325246U - A kind of 5-2-2 type radiating furnace tube of ethane cracking furnace elliptic cross-section - Google Patents
A kind of 5-2-2 type radiating furnace tube of ethane cracking furnace elliptic cross-section Download PDFInfo
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- CN204325246U CN204325246U CN201420770153.XU CN201420770153U CN204325246U CN 204325246 U CN204325246 U CN 204325246U CN 201420770153 U CN201420770153 U CN 201420770153U CN 204325246 U CN204325246 U CN 204325246U
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Abstract
The utility model provides a kind of 5-2-2 type radiating furnace tube of ethane cracking furnace elliptic cross-section, belongs to pyrolyzer field.This device comprises the first journey boiler tube, the second journey boiler tube and the 3rd journey boiler tube; Described first journey boiler tube comprises five boiler tubes, and the second journey boiler tube and the 3rd journey boiler tube include two boiler tubes; Five boiler tubes of described first journey boiler tube are oval boiler tube, and the second journey boiler tube and the 3rd journey boiler tube are circular boiler tube; One end of every root boiler tube of described first journey boiler tube is connected with the inlet end of oval-circle transition fitting, described ellipse-the exit end of circle transition fitting is connected with one end of U-tube, the other end of U-tube is connected with one end of the second journey boiler tube, the other end of every root boiler tube of the second journey boiler tube is connected with an one end across pipe, and two the other ends across pipe are connected with one end of two boiler tubes of the 3rd journey boiler tube respectively.
Description
Technical field
The utility model belongs to field, is specifically related to a kind of 5-2-2 type radiating furnace tube of ethane cracking furnace elliptic cross-section.
Background technology
The radiant coil that in petrochemical complex ethylene unit, ethane cracking furnace extensively adopts is configured as two journey boiler tubes and quadruple pass boiler tube, and three journey pipes also do not have application in ethane cracking furnace.
As depicted in figs. 1 and 2, the two journey 2-1 types (comprising the first journey boiler tube 1 ' and the second journey boiler tube 2) of stone-Robert Webster company exploitation and quadruple pass 2-1-1-1 type boiler tube (comprising the first journey boiler tube 1 ', second journey boiler tube 2, the 3rd journey boiler tube 3 and quadruple pass boiler tube 4 and transition conduit 5 and Y-piece part 6 ') for typically regardless of branch adapter bonnet, the caliber of these two kinds of boiler tubes is by Cheng Fang great, but the pipe number of every journey is all 1, and the residence time is about 0.15s-0.3s.Two journey 2-1 type boiler tube length are short compared with quadruple pass 2-1-1-1 type boiler tube, and the residence time is also shorter, and pressure drop is also less; Comparatively two journey 2-1 type boiler tubes are long for quadruple pass 2-1-1-1 type boiler tube, and the residence time is also slightly long, and pressure drop is also larger, but throughput is large compared with two journey 2-1 type boiler tubes.
At present, no matter be that two journey 2-1 types and quadruple pass 2-1-1-1 type boiler tube are arranged, radiating furnace tube entrance and exit is all at pyrolyzer radiation furnace roof, be arranged in the small space of furnace roof across pipe, furnace tube spring hanger system and waste heat boiler, their rational, collisionless layouts are the difficult points of engineering design always.
Two journey boiler tubes of the patent business design of all ethane cracking furnaces all adopt circular boiler tube.
The initial of pyrolyzer reaction is thermo-negative reaction, needs to absorb a large amount of heats to reach scission reaction temperature.So usually all pipe with small pipe diameter will be selected for the first journey pipe two journey boiler tubes, to obtain high surface area, reach the effect be rapidly heated of absorbing heat in a large number.
In general, pipe with small pipe diameter boiler tube is comparatively responsive to coking, especially boiler tube arrangement is now more and more intensive, cover more and more serious between adjacent boiler tube, this just causes same boiler tube high by counter-fire surface temperature during double-side radiation heat transfer, and being masked between adjacent boiler tube, it is lower to affect temperature, actual effective heat exchange area is caused to reduce, boiler tube is heated uneven, and result is the easy coking in high-temperature zone, the flexible distortion of boiler tube.
Utility model content
The purpose of this utility model is to solve the difficult problem existed in above-mentioned prior art, a kind of 5-2-2 type radiating furnace tube of ethane cracking furnace elliptic cross-section is provided, it has the feature of two journey 2-1 type boiler tubes compared with short residence time(SRT) and low pressure drop, there is again the feature that quadruple pass 2-1-1-1 type boiler tube throughput is larger, three journey 5-2-2 type radiating furnace tube material bottom in and top out or upper entering and lower leavings; First journey pipe adopts oval boiler tube, can improve cracking technology performance, can obtain good mechanical properties simultaneously.
The utility model is achieved through the following technical solutions:
A 5-2-2 type radiating furnace tube for ethane cracking furnace elliptic cross-section, comprises the first journey boiler tube, the second journey boiler tube and the 3rd journey boiler tube;
Described first journey boiler tube comprises five boiler tubes, and the second journey boiler tube and the 3rd journey boiler tube include two boiler tubes;
Five boiler tubes of described first journey boiler tube are oval boiler tube, and the second journey boiler tube and the 3rd journey boiler tube are circular boiler tube;
One end of every root boiler tube of described first journey boiler tube is connected with the inlet end of oval-circle transition fitting, described ellipse-the exit end of circle transition fitting is connected with one end of U-tube, the other end of U-tube is connected with one end of the second journey boiler tube, the other end of every root boiler tube of the second journey boiler tube is connected with an one end across pipe, and two the other ends across pipe are connected with one end of two boiler tubes of the 3rd journey boiler tube respectively;
The opening end of described first journey boiler tube is positioned at the top, and the opening end of described 3rd journey boiler tube is positioned at bottom;
Or the opening end of described first journey boiler tube is positioned at bottom, the opening end of described 3rd journey boiler tube is positioned at the top.
The inwall of every root boiler tube of described first journey boiler tube is equipped with two with the projection of its axis being parallel;
The cross section of two described projections is arc;
On the cross section of every root boiler tube of the first journey boiler tube, two projections lay respectively at the two ends of oval major axis.
A Venturi tube is equipped with in every root boiler tube of described second journey boiler tube.
Described ellipse-circle transition fitting comprises five inlet ends and two exit end of connection;
The cross section of each described inlet end is ellipse, the cross section of each boiler tube of its size and the first journey boiler tube measure-alike; Five boiler tubes of described first journey boiler tube are connected with five inlet ends of oval-circle transition fitting respectively;
The cross section of exit end is circular, the cross section of its size and U-tube measure-alike, and each exit end connects a U-tube.
Described first journey boiler tube, the second journey boiler tube are hung with the 3rd journey boiler tube is all vertical, and perpendicular to the center line of radiant heat zone.
Compared with prior art, the beneficial effects of the utility model are:
1, the utility model has the feature of two journey 2-1 type boiler tubes compared with short residence time(SRT) and low pressure drop, has again the feature that quadruple pass 2-1-1-1 type boiler tube throughput is larger, improves processing performance to a certain extent; The mode that three journey 5-2-2 type radiating furnace tubes can be taked material furnace bottom to enter furnace roof to go out, make to be arranged in the spring hanger system layout of furnace bottom, waste heat boiler and part boiler tube at furnace roof across pipe, add the handiness of furnace roof spatial arrangement, bring facility to engineering construction;
2, the first journey boiler tube is oval boiler tube, and more circular boiler tube increases surface-area, is conducive to the carrying out of scission reaction;
3, the first journey boiler tube is oval boiler tube, more circular boiler tube reduces the bridging effect between adjacent boiler tube, farthest reduce cold-zone area (S2 < S1), ensure the uniformity of temperature profile in the circumferential surface of boiler tube footpath, alleviate the degree of coking, and then extend the cycle of operation of pyrolyzer;
4, there are two arc convex in oval boiler tube cross section at major axis two ends, can play the effect reducing tube fluid frictional belt, increase heat-transfer effect.
Accompanying drawing explanation
Two journey 2-1 type boiler tube configurations of Fig. 1 prior art
The quadruple pass 2-1-1-1 type boiler tube configuration of Fig. 2 prior art
Fig. 3 the utility model three journey 5-2-2 type boiler tube configuration
Fig. 4 prior art boiler tube sectional view
Fig. 5 boiler tube sectional view 1 of the present utility model
Fig. 6 boiler tube sectional view 2 of the present utility model
1-first journey boiler tube (oval boiler tube); 1 '-the first journey boiler tube (circular boiler tube); 2-second journey boiler tube; 3-the 3rd journey boiler tube; 4-quadruple pass boiler tube; 5-transition conduit; Oval-round transition fitting of 6-; 6 '-Y-piece part; Cold-zone signal between 7-prior art circular boiler tube; Cold-zone signal between 8-oval boiler tube of the present utility model; Cold-zone scope between the circular boiler tube of S1-; Cold-zone scope between the oval boiler tube of S2-; 9-arc convex; 10-Venturi tube; 20-radiation section center line.
Embodiment
Below in conjunction with accompanying drawing, the utility model is described in further detail:
The utility model 5-2-2 type radiating furnace tube is three journey boiler tubes, and the first journey boiler tube 1 is five boiler tubes, and the second journey pipe 2 and the 3rd journey boiler tube 3 are two boiler tubes, and the first journey boiler tube 1 is oval boiler tube, and the second journey boiler tube 2 and the 3rd journey boiler tube 3 are circular boiler tube.
Particularly, in order to overcome the shortcoming of existing two journey 2-1 boiler tubes and quadruple pass 2-1-1-1 boiler tube, the utility model adopts three journey 5-2-2 type radiating furnace tubes, and radiating furnace tube material bottom in and top out, improves processing performance to a certain extent; First journey pipe is designed to oval boiler tube, and the second journey and the 3rd journey pipe are circular boiler tubes.Increase the first journey pipe heat transfer sheet area, reduce the bridging effect of adjacent boiler tube, thus reduce cold-zone area, improve effective heat exchange area, make radiative transfer more even.
As shown in Figure 3, an embodiment is as follows: radiating furnace tube is three journey boiler tube 5-2-2 type boiler tubes, and the first journey boiler tube is five boiler tubes, and the second journey boiler tube and the 3rd journey boiler tube are two boiler tubes, and the first journey boiler tube is oval boiler tube, the second journey and the 3rd journey boiler tube are circular boiler tube.
Five described first journey pipes are transitioned into two second journey pipes through oval-circle transition fitting 6, and under the effect of the second journey pipe Venturi tube 10, are evenly distributed to two the second journey pipes.
First journey boiler tube is oval boiler tube, and the cross section of oval boiler tube is respectively arranged with arc convex 9 at major axis two ends, as shown in Figure 6.Radiating furnace tube is vertical hanging, and perpendicular to the center line 20 of radiant heat zone.There are two arc convex in oval boiler tube cross section at major axis two ends, can play the effect reducing tube fluid frictional belt, increase heat-transfer effect.
Be the arrangement of many group boiler tubes in Figure 4 and 5, many group arrangements have less shielding to embody arrangement between oval boiler tube.(S2＜S1)。Specifically, Fig. 4 is the first journey pipe is circular boiler tube arrangement, and wherein, between circular boiler tube, cold-zone is illustrated as 7, and the cold-zone scope between circular boiler tube is S1; Fig. 5 is the first journey pipe is oval boiler tube arrangement, wherein, between oval boiler tube, cold-zone is illustrated as 8, cold-zone scope between oval boiler tube is S2, and the first journey boiler tube is oval boiler tube, and more circular boiler tube reduces the bridging effect between adjacent boiler tube, farthest reduce cold-zone area (S2 < S1), ensure the uniformity of temperature profile in the circumferential surface of boiler tube footpath, alleviate the degree of coking, and then extend the cycle of operation of pyrolyzer.
The utility model provides a kind of 5-2-2 type radiating furnace tube of ethane cracking furnace elliptic cross-section, it has the feature of two journey 2-1 type boiler tubes compared with short residence time(SRT) and low pressure drop, there is again the feature that quadruple pass 2-1-1-1 type boiler tube throughput is larger, improve processing performance to a certain extent; (material is from the first journey to the 3rd journey boiler tube to the three journey 5-2-2 type radiating furnace tubes mode that material furnace bottom can be taked to enter furnace roof go out forever, first journey pipe may at topmost, the 3rd journey pipe at foot, also can be the first journey pipe at foot, the 3rd journey pipe at topmost), make to be arranged in the spring hanger system layout of furnace bottom, waste heat boiler and part boiler tube at furnace roof across pipe, add the handiness of furnace roof spatial arrangement, bring facility to engineering construction; First journey pipe is designed to oval boiler tube, and the second journey pipe is circular boiler tube, increases the first journey pipe heat transfer sheet area, reduces the bridging effect of adjacent boiler tube, thus reduce cold-zone area, improve effective heat exchange area, make radiative transfer more even.
Technique scheme is several the most typical embodiment of the present utility model, for those skilled in the art, on the basis that the utility model discloses application method and principle, be easy to make various types of improvement or distortion, and the method be not limited only to described by the above-mentioned embodiment of the utility model, therefore previously described mode is just preferred, and does not have restrictive meaning.The utility model radiant coil can be used for newly-built pyrolyzer or carries out capacity expansion revamping to pyrolyzer.
Claims (6)
1. a 5-2-2 type radiating furnace tube for ethane cracking furnace elliptic cross-section, is characterized in that: the 5-2-2 type radiating furnace tube of described ethane cracking furnace elliptic cross-section, comprises the first journey boiler tube, the second journey boiler tube and the 3rd journey boiler tube;
Described first journey boiler tube comprises five boiler tubes, and the second journey boiler tube and the 3rd journey boiler tube include two boiler tubes;
Five boiler tubes of described first journey boiler tube are oval boiler tube, and the second journey boiler tube and the 3rd journey boiler tube are circular boiler tube;
One end of every root boiler tube of described first journey boiler tube is connected with the inlet end of oval-circle transition fitting, described ellipse-the exit end of circle transition fitting is connected with one end of U-tube, the other end of U-tube is connected with one end of the second journey boiler tube, the other end of every root boiler tube of the second journey boiler tube is connected with an one end across pipe, and two the other ends across pipe are connected with one end of two boiler tubes of the 3rd journey boiler tube respectively.
2. the 5-2-2 type radiating furnace tube of ethane cracking furnace elliptic cross-section according to claim 1, is characterized in that: the opening end of described first journey boiler tube is positioned at the top, and the opening end of described 3rd journey boiler tube is positioned at bottom;
Or the opening end of described first journey boiler tube is positioned at bottom, the opening end of described 3rd journey boiler tube is positioned at the top.
3. the 5-2-2 type radiating furnace tube of ethane cracking furnace elliptic cross-section according to claim 2, is characterized in that: be equipped with on the inwall of every root boiler tube of described first journey boiler tube two with the projection of its axis being parallel;
The cross section of two described projections is arc;
On the cross section of every root boiler tube of the first journey boiler tube, two projections lay respectively at the two ends of oval major axis.
4. the 5-2-2 type radiating furnace tube of ethane cracking furnace elliptic cross-section according to claim 3, is characterized in that: in every root boiler tube of described second journey boiler tube, be equipped with a Venturi tube.
5. the 5-2-2 type radiating furnace tube of ethane cracking furnace elliptic cross-section according to claim 4, is characterized in that: described ellipse-circle transition fitting comprises five inlet ends and two exit end of connection;
The cross section of each described inlet end is ellipse, the cross section of each boiler tube of its size and the first journey boiler tube measure-alike; Five boiler tubes of described first journey boiler tube are connected with five inlet ends of oval-circle transition fitting respectively;
The cross section of exit end is circular, the cross section of its size and U-tube measure-alike, and each exit end connects a U-tube.
6., according to the 5-2-2 type radiating furnace tube of the arbitrary described ethane cracking furnace elliptic cross-section of claim 1 to 5, it is characterized in that: described first journey boiler tube, the second journey boiler tube are hung with the 3rd journey boiler tube is all vertical, and perpendicular to the center line of radiant heat zone.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420770153.XU CN204325246U (en) | 2014-12-09 | 2014-12-09 | A kind of 5-2-2 type radiating furnace tube of ethane cracking furnace elliptic cross-section |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420770153.XU CN204325246U (en) | 2014-12-09 | 2014-12-09 | A kind of 5-2-2 type radiating furnace tube of ethane cracking furnace elliptic cross-section |
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| Publication Number | Publication Date |
|---|---|
| CN204325246U true CN204325246U (en) | 2015-05-13 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420770153.XU Expired - Fee Related CN204325246U (en) | 2014-12-09 | 2014-12-09 | A kind of 5-2-2 type radiating furnace tube of ethane cracking furnace elliptic cross-section |
Country Status (1)
| Country | Link |
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| CN (1) | CN204325246U (en) |
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2014
- 2014-12-09 CN CN201420770153.XU patent/CN204325246U/en not_active Expired - Fee Related
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| 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: 20150513 Termination date: 20151209 |
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| EXPY | Termination of patent right or utility model |