CN109425222A - Burn reforming furnace in side - Google Patents

Burn reforming furnace in side Download PDF

Info

Publication number
CN109425222A
CN109425222A CN201710724346.XA CN201710724346A CN109425222A CN 109425222 A CN109425222 A CN 109425222A CN 201710724346 A CN201710724346 A CN 201710724346A CN 109425222 A CN109425222 A CN 109425222A
Authority
CN
China
Prior art keywords
burner hearth
wall
shaped
burner
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.)
Pending
Application number
CN201710724346.XA
Other languages
Chinese (zh)
Inventor
韩健
蔡建光
韩艳萍
王志民
张和香
孙毅
罗莹
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Sinopec Engineering Inc
Sinopec Engineering Group Co Ltd
Original Assignee
Sinopec Engineering Inc
Sinopec Engineering Group Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Sinopec Engineering Inc, Sinopec Engineering Group Co Ltd filed Critical Sinopec Engineering Inc
Priority to CN201710724346.XA priority Critical patent/CN109425222A/en
Publication of CN109425222A publication Critical patent/CN109425222A/en
Pending legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27FURNACES; KILNS; OVENS; RETORTS
    • F27BFURNACES, KILNS, OVENS, OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
    • F27B17/00Furnaces of a kind not covered by any preceding group
    • F27B17/0016Chamber type furnaces
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G11/00Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27FURNACES; KILNS; OVENS; RETORTS
    • F27DDETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS, OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
    • F27D1/00Casings; Linings; Walls; Roofs
    • F27D1/0043Floors, hearths
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27FURNACES; KILNS; OVENS; RETORTS
    • F27DDETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS, OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
    • F27D9/00Cooling of furnaces or of charges therein
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27FURNACES; KILNS; OVENS; RETORTS
    • F27DDETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS, OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
    • F27D99/00Subject matter not provided for in other groups of this subclass
    • F27D99/0001Heating elements or systems
    • F27D99/0033Heating elements or systems using burners
    • F27D99/0035Heating indirectly through a radiant surface
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27FURNACES; KILNS; OVENS; RETORTS
    • F27DDETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS, OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
    • F27D9/00Cooling of furnaces or of charges therein
    • F27D2009/0002Cooling of furnaces
    • F27D2009/0005Cooling of furnaces the cooling medium being a gas

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Combustion Of Fluid Fuel (AREA)

Abstract

The invention discloses a kind of sides to burn reforming furnace, radiant section and convection section including connection, wherein, radiant section includes at least one N-shaped burner hearth, multi-channel parallel N-shaped boiler tube is equipped in each N-shaped burner hearth, each N-shaped burner hearth includes symmetrically arranged entrance burner hearth and outlet burner hearth, the inlet tube row and outlet row of multi-channel parallel N-shaped boiler tube are respectively arranged in entrance burner hearth and outlet burner hearth, straight pipe on the side wall of entrance burner hearth and outlet burner hearth relative to N-shaped boiler tube is symmetrically equipped with wall-attached burner, forms double-side radiation side to straight pipe and burns heat supply.Reforming furnace is burnt in the side can be realized double-side radiation side burning heat-supplying mode, extends boiler tube long service life, and easy access and integral module design and batch production manufacture.

Description

Burn reforming furnace in side
Technical field
The present invention relates to field of petrochemical industrial, burn reforming furnace more particularly, to a kind of side.
Background technique
The reforming furnace generallyd use in the catalytic reforming unit of petrochemical industry at present generally includes radiant section and convection current Section.Wherein the radiating furnace tube in radiant section absorbs heat, provides heat for subsequent reactor, waste heat pot is usually arranged in convection section Furnace recycles high-temperature flue gas, and the thermic load of radiant section is supplied by heating equipment (i.e. burner) the consumption fuel in burner hearth.It is existing Reformer usually require multiple reactors, the corresponding heat absorption burner hearth of each reactor collectively forms series devices, wherein Multiple heat absorption burner hearths integrate the reforming furnace of an All-in-One.
According to the difference of use demand, the existing All-in-One reforming furnace type of furnace is broadly divided into the just U-shaped furnace (figure of All-in-One 1a and Fig. 1 b) and All-in-One inverted U furnace (Fig. 2 a and Fig. 2 b), heat-supplying mode, which is predominantly held, burns heat supply and bottom burning heat supply.
As illustrated in figs. 1A and ib, just U-shaped reformer includes radiation chamber and convection cell 5, and wherein radiation chamber is rectangle furnace 1, rectangle furnace 1 is divided into multiple radiation cells by the internal multiple midfeathers 3 of setting, and multichannel is arranged in each radiation chamber U-shaped coil pipe 2 in parallel, outlet, entrance and the radiation exhanst gas outlet of U-shaped coil pipe 2 are respectively positioned on radiating top, occupy headspace, End can only be equipped in the different height at U-shaped 2 middle part of coil pipe and combust burner 4, generate horizontal flame in end, U-shaped coil pipe 2 is carried out Burn heat supply in end.Its shortcoming is that the horizontal length of pipe row increases accordingly, the burner at both ends when U-shaped 2 number of coil pipe increases Flame not can guarantee enough cascade units, and uneven heating even property of the pipe row along horizontal length direction increases, every road medium heat absorption It measures inhomogeneities to increase, the tube wall temperature inhomogeneities that pipe arranges along horizontal length direction increases, therefore the coil pipe road of each burner hearth Number is limited, and total caloric receptivity is limited, and according to the difference of technical load and coil lengths etc., needs to design the burning of different load Device, specification and model are various.
As shown in Figure 2 a and 2 b, inverted U reformer includes radiation chamber and convection cell 10, and wherein radiation chamber is rectangle furnace 6, inside is arranged multiple midfeathers 8 and burner hearth is divided into multiple radiation cells, and multi-channel parallel inverted U disk is arranged in radiation chamber Pipe 7, the outlet of inverted U coil pipe 7, entrance are located at radiation chamber bottom, and radiation exhanst gas outlet is located at radiating top.This structure can be in square 6 bottom cloth bottom set of shape burner hearth combusts burner 9, when being distributed in the centre of multi-channel parallel inverted U coil pipe 7, can form bottom and burn single side spoke It penetrates, or is distributed in 7 straight pipe two sides of multi-channel parallel inverted U coil pipe, form asymmetrical bottom and burn double-side radiation.Its shortcoming is that When burning single side radiation the bottom of using, the circumferential heating inhomogeneities of boiler tube can be increased, it is uneven to increase boiler tube circumferential direction tube wall temperature Property, side towards the fire boiler tube tube wall temperature is much larger than the fiery face of back;When burner, which is distributed in boiler tube two sides, forms bottom burning double-side radiation, by It is needed in intermediate combustion device while being the heat supply of arranged on left and right sides straight pipe, leading to the thermic load of intermediate combustion device is two sides burner 2 times, thermic load difference causes intermediate combustion device flame height to be about 2 times of two sides burner, forms to boiler tube asymmetric Double-side radiation, equally also will increase the circumferential heating inhomogeneities of boiler tube, increase boiler tube circumferential direction tube wall temperature inhomogeneities, and Need to design the burner of different load, specification and model are more;Since straight pipe height is usually higher, bottom combusts burner and is formed Fire Radiation heat supply concentrate on burner hearth middle and lower part, uneven heat supply is generated along straight pipe short transverse to inverted U boiler tube, is increased Boiler tube radial direction tube wall temperature inhomogeneities, boiler tube lower half portion tube wall temperature is significantly greater than top half, and increases fire box temperature Unevenness vertically and degree.
In addition, no matter existing just U-shaped or inverted U reforming furnace, when need two-in-one, three-in-one or four-in-one When, it is necessary to midfeather is set, each single radiation chamber is completely cut off.The masonry of midfeather is complex, and midfeather exists heated The risk toppled over.Since the stability of midfeather is poor, it is difficult to keep stability in transit, therefore using integral module When changing design and batch production manufacture, it is difficult to accomplish that factory builds, site operation masonry can only be remained.
Therefore, it is necessary to develop a kind of heat supply uniformly, boiler tube long service life, easy access and integral moduleization design and The reforming furnace of batch production manufacture.
The information for being disclosed in background of invention part is merely intended to deepen the reason to general background technique of the invention Solution, and it is known to those skilled in the art existing to be not construed as recognizing or imply that the information is constituted in any form Technology.
Summary of the invention
The invention proposes a kind of sides to burn reforming furnace, can be realized double-side radiation side and burns heat-supplying mode.
The present invention provides a kind of sides to burn reforming furnace, radiant section and convection section including connection, wherein the radiation Section includes at least one N-shaped burner hearth, and multi-channel parallel N-shaped boiler tube is equipped in each N-shaped burner hearth, and each N-shaped burner hearth includes symmetrically setting The entrance burner hearth and outlet burner hearth set, the inlet tube row and outlet row of the multi-channel parallel N-shaped boiler tube are respectively arranged at described Straight tube in entrance burner hearth and outlet burner hearth, on the side wall of the entrance burner hearth and outlet burner hearth relative to the N-shaped boiler tube Section is symmetrically equipped with wall-attached burner, forms double-side radiation side to the straight pipe and burns heat supply.
Preferably, interval air wall is equipped between the entrance burner hearth and outlet burner hearth.
Preferably, the height of the straight pipe is H, and the height of the interval air wall is h, and h >=H.
Preferably, burner hearth air wall is equipped between adjacent N-shaped burner hearth.
Preferably, the width of the interval air wall and burner hearth air wall is all larger than 0.5m.
Preferably, multiple rows of attached wall is equipped at the different height on the side wall of the entrance burner hearth and outlet burner hearth to burn Device.
Preferably, the quantity, height, load for being set to the wall-attached burner on each side wall are all the same.
Preferably, the wall-attached burner forms wall-attached divergence form flame.
Preferably, the sidewall surfaces of the entrance burner hearth and outlet burner hearth are equipped with insulating lining.
Preferably, at least one described N-shaped burner hearth is connected with each other by crossbeam.
The advantages of heating furnace according to the present invention, is:
1. N-shaped burner hearth is arranged, wall-attached burner is symmetrical arranged on four side walls of N-shaped burner hearth, so that formation is absolutely right Heat-supplying mode is burnt in the double-side radiation side of title, realize homogeneous radiation heat supply to the straight pipe of N-shaped boiler tube and along inlet tube row and The homogeneous radiation heat supply in the horizontal length direction of outlet row.
2. being equipped with multiple rows of wall-attached burner at the different height on the side wall of entrance burner hearth and outlet burner hearth, and in entrance The sidewall surfaces of burner hearth and outlet burner hearth are equipped with insulating lining.Wall-attached burner can form the tubaeform flame of diverging, and flame is tight The insulating lining for pasting sidewall surfaces carries out heat radiation to insulating lining, so that insulating lining formation accumulation of heat is uniform, inner wall temperature Uniform radiation curtain heating source, it is uniform double so as to be carried out along the horizontal length direction of inlet tube row and outlet row Surface radiation heat supply, and the circumferential direction and the radial extremely uniform double-side radiation heat supply of progress of the straight pipe to N-shaped boiler tube, can either It avoids the end of typical just U-shaped furnace from burning caused by heat-supplying mode along the even property of uneven heating of pipe row's length direction, also can be avoided allusion quotation It burns pipe row caused by single side radiation or bottom burning Asymmetric two-sided radiant heating mode and is circumferentially heated with radial in the bottom of type inverted U furnace Inhomogeneities is conducive to the uniformity for increasing the distribution of boiler tube tube wall temperature, extends boiler tube service life, hence it is evident that improves fire box temperature Comprehensive uniformity.
3. the identical attached wall combustion of quantity, height, load is arranged on the four sides side wall of entrance burner hearth and outlet burner hearth Burner can simplify the load type of burner, and each N-shaped burner hearth only needs to design the burner of a kind of load and specification, thus Simplify design parameter, the complexity for reducing burner piping system, solve the problems, such as single burner load too high.
4. being equipped with interval air wall between entrance burner hearth and outlet burner hearth, burner hearth air is equipped between adjacent twin furnace Wall is conducive to improve hearth outer wall temperature, and maintenance, maintenance channel among formation heating furnace provide the peace of wall-attached burner Space is filled, in addition, also helping the burning line and furnace purge steam pipe line of arrangement burner, is conducive to increase side wall and sees fire Door, is monitored multi-channel parallel N-shaped boiler tube and burner operating status, is conducive to the heat dissipation of maintenance, maintenance channel.
5. cancelling the intermediate brick wall in existing heating furnace, the stability of heating furnace is improved, it is not necessary to carry out scene or factory applies Work is built, and in the case where traffic condition allows, is able to carry out integral module design and batch production manufacture.
Detailed description of the invention
Exemplary embodiment of the present is described in more detail in conjunction with the accompanying drawings, of the invention is above-mentioned and other Purpose, feature and advantage will be apparent, wherein in exemplary embodiments of the present invention, identical reference label is usual Represent same parts.
Burn the main view and top view of the heating furnace of heat supply in the just U-shaped end that Fig. 1 a and Fig. 1 b respectively illustrate the prior art.
Burn the main view and top view of the heating furnace of heat supply in the inverted U bottom that Fig. 2 a and Fig. 2 b respectively illustrate the prior art.
Burn the main view of reforming furnace in the side that Fig. 3 shows an exemplary embodiment according to the present invention.
Burn the top view of reforming furnace in the side that Fig. 4 shows an exemplary embodiment according to the present invention.
Description of symbols:
1, rectangle furnace;2, U-shaped coil pipe;3, midfeather;4, end combusts burner;5, convection section;6, rectangle furnace;7, it falls U-shaped coil pipe;8, midfeather;9, bottom combusts burner;10, convection cell;11, radiant section;12, convection section;13, N-shaped burner hearth;14, Entrance burner hearth;15, burner hearth is exported;16, it is spaced air wall;17, burner hearth air wall;18, N-shaped boiler tube;19, wall-attached burner;20, Inlet manifold;21, outlet header.
Specific embodiment
The present invention will be described in more detail below with reference to accompanying drawings.Although showing the preferred embodiment of the present invention in attached drawing, However, it is to be appreciated that may be realized in various forms the present invention and should not be limited by the embodiments set forth herein.On the contrary, providing These embodiments are of the invention more thorough and complete in order to make, and can will fully convey the scope of the invention to ability The technical staff in domain.
The radiant section and convection section that reforming furnace includes connection are burnt in the side of an exemplary embodiment of the present invention, In, radiant section includes at least one N-shaped burner hearth, is equipped with multi-channel parallel N-shaped boiler tube in each N-shaped burner hearth, each N-shaped burner hearth includes Symmetrically arranged entrance burner hearth and outlet burner hearth, multi-channel parallel N-shaped boiler tube inlet tube row and outlet row be respectively arranged at into In mouth burner hearth and outlet burner hearth, the straight pipe on the side wall of entrance burner hearth and outlet burner hearth relative to N-shaped boiler tube is symmetrically set There is wall-attached burner, double-side radiation side is formed to straight pipe and burns heat supply.
It includes at least one N-shaped burner hearth that reforming furnace is burnt in the side, and each N-shaped burner hearth includes entrance burner hearth and outlet furnace Thorax is provided with multi-channel parallel N-shaped boiler tube;Entrance burner hearth and outlet burner hearth provide four sides side wall altogether, burn for setting attached wall Device provides space, and the straight pipe on the side wall of entrance burner hearth and outlet burner hearth relative to N-shaped boiler tube is symmetrically arranged with attached wall combustion Burner, heat-supplying mode is burnt in the double-side radiation side for forming absolute symmetry, to realize uniform radiant heating.
In one example, interval air wall is equipped between entrance burner hearth and outlet burner hearth.
In one example, the height of straight pipe is H, is spaced the height of air wall as h, and h >=H.
In one example, burner hearth air wall is equipped between adjacent N-shaped burner hearth.
In one example, it is spaced air wall and the width of burner hearth air wall is all larger than 0.5m.
It is equipped with interval air wall between entrance burner hearth and outlet burner hearth, is equipped with burner hearth air wall between adjacent twin furnace, Be conducive to improve hearth outer wall temperature, maintenance, maintenance channel among formation heating furnace provide the installation sky of wall-attached burner Between, in addition, also helping the burning line and furnace purge steam pipe line of arrangement burner, be conducive to increase side wall observation door, Multi-channel parallel N-shaped boiler tube and burner operating status are monitored, the heat dissipation of maintenance, maintenance channel is conducive to.
In one example, can increase in interval air wall and burner hearth air wall two sides setting steel construction pillar and crossbeam Add the stability of N-shaped chamber structure.
In one example, multiple rows of attached wall is equipped at the different height on the side wall of entrance burner hearth and outlet burner hearth to burn Device, to improve uniformity of the fire box temperature along short transverse.For example, for including that reformation heating is burnt in the side of 4 N-shaped burner hearths 5 rows, 4 rows, 3 rows, 5 row's wall-attached burners can be respectively set on the side wall of first to fourth N-shaped burner hearth, pass through this side for furnace Formula forms the combination of the wall-attached burner of the N-shaped burner hearth and different load that meet different heat demands, forms All-in-One side and burns weight Whole heating furnace.
In one example, the quantity, height, load for being set to the wall-attached burner on each side wall are all the same.
The identical attached wall burning of quantity, height, load is set on the four sides side wall of entrance burner hearth and outlet burner hearth Device can simplify the load type of burner, and each N-shaped burner hearth only needs to design the burner of a kind of load and specification, thus simple Change design parameter, the complexity for reducing burner piping system, solve the problems, such as single burner load too high.
In one example, wall-attached burner forms wall-attached divergence form flame.
In one example, entrance burner hearth and outlet burner hearth sidewall surfaces be equipped with insulating lining, insulating lining can by brick, The materials such as castable or ceramic fibre are made.
Wall-attached burner can form the tubaeform flame of diverging, and flame is close to the insulating lining of sidewall surfaces, serve as a contrast to heat preservation In carry out heat radiation so that insulating lining is formed, accumulation of heat is uniform, inner wall temperature uniformly radiates curtain heating source, so as to Uniform double-side radiation heat supply, and the straight pipe to N-shaped boiler tube are carried out along the length direction of inlet tube row and outlet row Circumferential direction and it is radial carry out extremely uniform double-side radiation heat supply, the end of typical just U-shaped furnace can either be avoided to burn heat-supplying mode and led The even property of uneven heating along pipe row's length direction caused, single side radiation is burnt at the bottom that also can be avoided typical inverted U furnace or bottom burning is non- The circumferential and radial even property of uneven heating of pipe row caused by symmetrical double-side radiation heat-supplying mode, is conducive to increase boiler tube tube wall temperature The uniformity of distribution extends boiler tube service life, hence it is evident that improves the comprehensive uniformity of fire box temperature.
In one example, the top of N-shaped burner hearth is equipped with the exhanst gas outlet for being connected to convection section.
In one example, inlet tube row and outlet row are respectively communicated to be set to the entrance set of N-shaped burner hearth bottom Pipe and outlet header.
In one example, at least one N-shaped burner hearth is connected with each other by crossbeam.
When multiple N-shaped burner hearths are applied in combination, it is attached by crossbeam and is conducive to keep stable structure, form All-in-One Heating furnace.
Embodiment
Burn the main view of reforming furnace in the side that Fig. 3 and Fig. 4 respectively illustrates an exemplary embodiment according to the present invention Figure and top view.
As shown in Figures 3 and 4, the radiant section 11 and convection current that reforming furnace includes connection are burnt in side accoding to exemplary embodiment Section 12, wherein radiant section 11 includes 4 N-shaped burner hearths 13, is equipped with multi-channel parallel N-shaped boiler tube 18, each n in each N-shaped burner hearth 13 Type burner hearth 13 includes symmetrically arranged entrance burner hearth 14 and outlet burner hearth 15, and the inlet tube of multi-channel parallel N-shaped boiler tube 18 is arranged and gone out Mouthful pipe row is respectively arranged in entrance burner hearth 14 and outlet burner hearth 15, opposite on the side wall of entrance burner hearth 14 and outlet burner hearth 15 It is symmetrically equipped with wall-attached burner 19 in the straight pipe of N-shaped boiler tube, double-side radiation side is formed to straight pipe and burns heat supply.
Interval air wall 16 is equipped between entrance burner hearth 14 and outlet burner hearth 15, the height of interval air wall 16 is h, N-shaped The straight pipe height of boiler tube 18 is H, wherein h >=H.
Burner hearth air wall 17 is equipped between adjacent N-shaped burner hearth 13, in addition, interval air wall 16 and burner hearth air wall 17 Width is all larger than 0.5m, reserves inspection, maintenance channel, and N-shaped boiler tube 18 and wall-attached burner 19 are overhauled and monitored convenient for the work human world.
When multiple N-shaped burner hearths are applied in combination, it is connected with each other by crossbeam.
Wherein, the sidewall surfaces of entrance burner hearth and outlet burner hearth are equipped with insulating lining.
5 rows, 4 rows, 3 rows, the combustion of 5 row's attached walls are respectively set at the different height on the side wall of first to fourth N-shaped burner hearth Burner 19, wall-attached burner 19 are symmetrically set in the straight pipe two sides of N-shaped boiler tube 18, and the wall-attached burner 19 on each side wall Number of rows, height, single quantity and single load are all the same, form full symmetric double-side radiation side to N-shaped boiler tube and burn heat supply.
In addition, wall-attached burner can form the tubaeform flame of diverging, flame is close to the insulating lining of surrounding, serves as a contrast to heat preservation In carry out heat radiation.Multiple rows of wall-attached burner is set at the different height of side wall, can insulating lining to each side wall into The comprehensive heat radiation of row, formation accumulation of heat is uniform, inner wall temperature uniformly radiates curtain lining heating source on four sides, radiation curtain lining In heating source make N-shaped boiler tube 18 along inlet tube row and outlet row length direction, N-shaped boiler tube straight pipe circumferential direction and radial direction It is heated evenly, the uniformity of the tube wall temperature distribution of N-shaped boiler tube 18 can be improved, extend the service life of N-shaped boiler tube 18.This Outside, high-temperature flue gas can carry out radiant heating to the bend loss at top.
When work, processing medium enters from inlet manifold 20, distributes to the entrance straight tube of the N-shaped boiler tube 18 of multi-channel parallel Section into outlet straight pipe, then is collected to outlet header 21 by bend loss, high-temperature flue gas by N-shaped burner hearth 13 entrance furnace Wall-attached burner 19 on thorax and outlet burner hearth sidewall, which burns, to be generated, and high-temperature flue gas is collected to the top of each N-shaped burner hearth 13 upwards Portion outlet, is upwardly into convection section 12 by the top exit of multiple N-shaped burner hearths 13 again, carries out 12 coil pipe of convection section to spreading Heat.
The embodiment of the present invention is described above, above description is exemplary, and non-exclusive, and also not It is limited to disclosed embodiment.Without departing from the scope and spirit of illustrated each embodiment, this technology is led Many modifications and changes are obvious for the those of ordinary skill in domain.The selection of term used herein, it is intended to most The principle, practical application or the improvement to the technology in market of embodiment are explained well, or make the other general of the art Logical technical staff can understand embodiments disclosed herein.

Claims (10)

1. reforming furnace, radiant section and convection section including connection, wherein the radiant section includes at least one are burnt in a kind of side N-shaped burner hearth, is equipped with multi-channel parallel N-shaped boiler tube in each N-shaped burner hearth, each N-shaped burner hearth include symmetrically arranged entrance burner hearth and Burner hearth is exported, the inlet tube row and outlet row of the multi-channel parallel N-shaped boiler tube are respectively arranged at the entrance burner hearth and outlet In burner hearth, the straight pipe on the side wall of the entrance burner hearth and outlet burner hearth relative to the N-shaped boiler tube is symmetrically equipped with attached Wall burner forms double-side radiation side to the straight pipe and burns heat supply.
2. reforming furnace is burnt in side according to claim 1, wherein between being equipped between the entrance burner hearth and outlet burner hearth Every air wall.
3. reforming furnace is burnt in side according to claim 2, wherein the height of the straight pipe is H, the interval air The height of wall is h, and h >=H.
4. reforming furnace is burnt in side according to claim 2, wherein be equipped with burner hearth air wall between adjacent N-shaped burner hearth.
5. reforming furnace is burnt in side according to claim 4, wherein the width of the interval air wall and burner hearth air wall It is all larger than 0.5m.
6. reforming furnace is burnt in side according to claim 1, wherein on the side wall of the entrance burner hearth and outlet burner hearth Different height at be equipped with multiple rows of wall-attached burner.
7. reforming furnace is burnt in side according to claim 1, wherein be set to the number of the wall-attached burner on each side wall Amount, height, load are all the same.
8. reforming furnace is burnt in side according to claim 1, wherein the wall-attached burner forms wall-attached divergence form fire Flame.
9. reforming furnace is burnt in side according to claim 1, wherein the sidewall surfaces of the entrance burner hearth and outlet burner hearth Equipped with insulating lining.
10. reforming furnace is burnt in side according to claim 1, wherein at least one described N-shaped burner hearth is mutual by crossbeam Connection.
CN201710724346.XA 2017-08-22 2017-08-22 Burn reforming furnace in side Pending CN109425222A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201710724346.XA CN109425222A (en) 2017-08-22 2017-08-22 Burn reforming furnace in side

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201710724346.XA CN109425222A (en) 2017-08-22 2017-08-22 Burn reforming furnace in side

Publications (1)

Publication Number Publication Date
CN109425222A true CN109425222A (en) 2019-03-05

Family

ID=65498155

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201710724346.XA Pending CN109425222A (en) 2017-08-22 2017-08-22 Burn reforming furnace in side

Country Status (1)

Country Link
CN (1) CN109425222A (en)

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1036610A (en) * 1963-12-30 1966-07-20 Lummus Co Heater
JPS5778929A (en) * 1980-11-06 1982-05-17 Babcock Hitachi Kk Denitrification of waste gas from steam reforming furnace
CN201779983U (en) * 2010-08-30 2011-03-30 吴道洪 Heat accumulating-type combustion reformed heating furnace
CN103789002A (en) * 2012-10-30 2014-05-14 中国石油化工股份有限公司 Gas phase heating furnace and application of gas phase heating furnace in chemical field

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1036610A (en) * 1963-12-30 1966-07-20 Lummus Co Heater
JPS5778929A (en) * 1980-11-06 1982-05-17 Babcock Hitachi Kk Denitrification of waste gas from steam reforming furnace
CN201779983U (en) * 2010-08-30 2011-03-30 吴道洪 Heat accumulating-type combustion reformed heating furnace
CN103789002A (en) * 2012-10-30 2014-05-14 中国石油化工股份有限公司 Gas phase heating furnace and application of gas phase heating furnace in chemical field

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
蔡建光: "大型连续重整装置反应加热炉炉型比较", 《石油化工设备技术》 *

Similar Documents

Publication Publication Date Title
RU2643734C2 (en) Method and device for conducting endothermic reactions
JP2009001822A (en) Cracking furnace with more uniform heating
WO2011050573A1 (en) Ethylene cracking furnace with multipass radiant furnace tubes
JPH0313482B2 (en)
CN103992812B (en) Ethane cracking furnace
KR20110083195A (en) Condensing boiler
CN103992813A (en) Ethylene cracking furnace
CN109425222A (en) Burn reforming furnace in side
CN109425223A (en) Heating furnace
CN106398744B (en) Heating furnace
CN108240766B (en) Reforming furnace
CN101921607A (en) Delay coking heating furnace combining single-sided radiation and double-sided radiation
CN108458591A (en) Cylinder type tubular heater
CN210193772U (en) Heating furnace
EP3750974B1 (en) A delayed coking furnace for heating coker feedstock
CN208266119U (en) Heating furnace for hydrogenation plant
CN107011928A (en) Fast pyrogenation stove
CN110079356B (en) Heating furnace
CN102878807A (en) Flame heating furnace
CN208124886U (en) Standpipe square chest furnace
CN202379948U (en) Symmetric double-step tubular radiation furnace
CN107723019B (en) Ethylene cracking furnace
CN206624828U (en) A kind of petroleum cracking device
IT9047720A1 (en) APPARATUS FOR HIGH TEMPERATURE THERMAL PROCESSES, WITH INCANDESCENT HEAT SOURCE WITH RADIANT SURFACES AND COILS FOR PROCESS FLUID.
CN110835547A (en) Ethylene cracking furnace

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
RJ01 Rejection of invention patent application after publication

Application publication date: 20190305

RJ01 Rejection of invention patent application after publication