CN114278914A

CN114278914A - Steam generating equipment and heat exchange device thereof

Info

Publication number: CN114278914A
Application number: CN202110388096.3A
Authority: CN
Inventors: 岳俊
Original assignee: Anhui Hot Well Energy Saving Technology Co ltd
Current assignee: Anhui Hot Well Energy Saving Technology Co ltd
Priority date: 2021-04-10
Filing date: 2021-04-10
Publication date: 2022-04-05

Abstract

The invention discloses a quick steam generating device with energy saving, high efficiency and high reliability and a heat exchange device thereof, wherein the heat exchange device for the steam generating device comprises: a housing; a first coil unit and a second coil unit located within the housing; an inner space surrounded by the first coil unit is configured as a combustion chamber; the second coil unit surrounds the first coil unit; a spacing structure is arranged between the second coil unit and the first coil unit; a first flue gas flow channel is arranged between the first coil pipe unit and the spacing structure; a second flue gas channel is formed between the spacing structure and the shell; the second flue gas flow channel is communicated with the downstream of the first flue gas flow channel; the flow direction of the flue gas flowing into the second flue gas flow channel from the first flue gas flow channel is changed by more than 150 degrees; the first coil pipe unit is provided with a communicated flue gas channel which is used for communicating the first flue gas channel with the combustion chamber.

Description

Steam generating equipment and heat exchange device thereof

Technical Field

The invention relates to the field of steam generators, in particular to steam generating equipment and a heat exchange device thereof.

Background

The development of gas combustion equipment (gas water heating equipment/steam generating equipment) is accelerated to a fully premixed condensing technology with high efficiency and low emission. Especially, the rapid gas steam generating device has small water volume, has high steam generating speed compared with the traditional steam boiler, does not need regular annual inspection, is widely favored by the market, and is widely applied to national production and life, such as hotels, food, textile, chemical industry, feed and other industries. However, the existing rapid gas steam generation equipment in the market generally has the defects of poor reliability, high emission of nitrogen oxides, low efficiency, large size and the like.

For example: the steam generating apparatus disclosed in publication No. CN105402710A employs a split modular technique. The boiler flue gas has high nitrogen oxide emission, does not meet the low emission environmental protection requirement, has about 11 percent of flue gas oxygen content, has large surplus coefficient, takes away much heat by excessive air, and has low heat efficiency. The assembly of multiple components has a plurality of parts (such as gas valves, fans, burner groups, heat exchanger groups, wind pressure switches and the like), and the corresponding failure rate is high. In addition, the steam generating equipment adopts the three-layer fin type heat exchanger, after long-term combustion, due to uneven heating, water leakage is easy to occur at the deformed copper pipes and welding positions between the heat exchangers of different stages due to deformation, overheating and melting are easy to occur on the fins on the fire-facing side, and the heat exchangers are limited by volume and have small evaporation capacity.

The heat exchanger unit disclosed in publication No. CN109373302A adopts the integrated technology of thick and thin burning fire rows, solves the low nitrogen emission problem of equipment, but still has the high failure rate problem caused by the multi-component assembly and the multiple parts. Particularly, the heat exchanger unit adopts the stainless steel light pipe and the fin combined pipe as an evaporation section and a superheating section, and the copper fin type heat exchanger as a preheating section, so that when the burners are combusted in groups, the length direction of the heat exchanger is uneven in cooling and heating, and the problem of deformation and bending of the heat exchanger is easy to occur after long-term use.

Publication No. CN107781800A provides a circulating steam boiler which adopts a through-flow type full premixing technology, vertical multi-pipe parallel connection and upper and lower header welding. But the boiler has the defects of multiple welding spots, complex processing technology and poor reliability, and due to the adoption of a parallel structure, the uneven water flow distribution and the cracking of the heat exchange tube due to the overheating stress are easy to occur after the boiler is used for a long time. Meanwhile, the heat exchanger needs an additional water level detector to detect the liquid level height, and the heat exchange tube is prone to overheating if the height detection is inaccurate, so that the service life of the heat exchanger is influenced.

Publication No. CN112097234A provides a coil type steam generator which adopts the straight-flow type full premix technology and the three-layer stainless steel coil series connection mode, and this scheme has solved the problem that other schemes have many welding spots, and the diversion flow through 4 times of flue gas is utilized to increase the heat transfer, has improved the heat transfer ability simultaneously. However, the smoke in the scheme is always in a laminar flow state, the flow is not fully disturbed, and the heat exchange in the middle area of the fluid cannot be fully realized; and only utilize the heat transfer area of the inside and outside both sides of heat transfer coil pipe, the heat transfer area between the pipe is all failed to be used for the heat transfer, therefore effective heat transfer area is less, leads to the coil pipe overlength, and the water resistance is big, and is bulky, needs additionally to increase a large-scale energy-saving appliance to come the raising efficiency when the water volume is big, and the cost is very high.

Publication No. CN103512018B also provides a steam generator using a straight-flow full-premixing technique and a single coil in series, which solves the problem of many welding spots, but also has the problem of not utilizing the effective heat exchange area between the tubes, and the heat exchange efficiency is low. And only a round coil pipe is needed, the flue gas can not fully exchange heat, and in order to improve the heat exchange quantity, the coil pipe must be prolonged, so that the problem that the water capacity of the coil pipe is too large and the volume is too large is solved.

Disclosure of Invention

In view of the above problems in the prior art, an object of the present invention is to provide a fast steam generating device and a heat exchange device thereof, which are energy-saving, efficient and highly reliable.

In order to achieve the purpose, the invention adopts the following technical scheme:

a heat exchange device for a steam generating apparatus, comprising: a housing; a first coil unit and a second coil unit located within the housing;

an inner space surrounded by the first coil unit is configured as a combustion chamber;

the second coil unit surrounds the first coil unit; a spacing structure is arranged between the second coil unit and the first coil unit; a first flue gas flow channel is arranged between the first coil pipe unit and the spacing structure; a second flue gas channel is formed between the spacing structure and the shell; the second flue gas flow channel is communicated with the downstream of the first flue gas flow channel; the flow direction of the flue gas flowing into the second flue gas flow channel from the first flue gas flow channel is changed by more than 150 degrees; the first coil pipe unit is provided with a communicated flue gas channel which is used for communicating the first flue gas channel with the combustion chamber.

In a preferred embodiment, the extending directions of the first flue gas flow channel and the second flue gas flow channel are parallel; the flow direction of the flue gas in the first flue gas channel is opposite to that of the flue gas in the second flue gas channel.

In a preferred embodiment, the spacing structure surrounds the first coil unit and the second coil unit; the first flue gas flow channel extends along the inner wall surface of the spacing structure; the second flue gas flow channel extends along the outer wall surface of the spacing structure.

In a preferred embodiment, the spacer structure is a cylindrical spacer.

As a preferred embodiment, the combustion chamber extends in an axial direction; the spacing structure is cylindrical; the first flue gas flow channel is arranged between the spacing structure and the first coil pipe unit and extends along the axial direction; the second flue gas flow channel is arranged between the spacing structure and the shell and extends along the axial direction.

As a preferred embodiment, one end of the first flue gas flow channel in the axial direction is communicated with one end of the second flue gas flow channel; the other end of the second flue gas channel is communicated with the smoke exhaust structure.

In a preferred embodiment, the minimum effective flue gas flow area of the smoke evacuation structure is greater than or equal to half of the minimum effective flue gas flow area of the second flue gas flow channel.

As a preferred embodiment, the first coil unit comprises at least one inner heat exchange coil tube; wherein, the inner heat exchange coil pipe barrel positioned at the innermost side is formed by spirally extending the finless heat exchange pipe along the axial direction.

As a preferred embodiment, the first coil unit includes: two inner heat exchange coil pipes are sleeved with each other; each inner heat exchange coil pipe barrel is formed by spirally extending fin-free heat exchange pipes along the axial direction.

In a preferred embodiment, the innermost inner heat exchange coil tube communicates with the other inner heat exchange coil tubes upstream in the flow direction of the medium to be heated.

In a preferred embodiment, each of said inner heat exchange coil barrels comprises a plurality of axially stacked heat exchange tube rings; the communicating flue gas flow passage comprises: and the axial gap is positioned between two axially adjacent inner heat exchange coil rings.

As a preferred embodiment, the communicating flue gas flow passage further comprises: a gap between every two radially adjacent inner heat exchange coil tubes is formed between the two radially adjacent inner heat exchange coil tubes; the axial gaps of the two adjacent inner heat exchange coil pipe barrels are communicated through the inter-barrel gaps.

In a preferred embodiment, an axial spacer is disposed between two axially adjacent inner heat exchange coil rings.

In a preferred embodiment, the axial gaps of two adjacent inner heat exchange coil tubes are staggered.

In a preferred embodiment, the flow areas of the heated media of the inner heat exchange coils of at least two inner heat exchange coil barrels are different; the heated medium flow area of the inner heat exchange coil barrel positioned on the outer side is larger than that of the inner heat exchange coil barrel positioned on the inner side.

In a preferred embodiment, the second coil unit communicates upstream of the first coil unit in a flow direction of the heated medium.

In a preferred embodiment, the second coil unit comprises a helically axially extending finned coil or bellows located within the second flue gas flow path.

As a preferred embodiment, the extending direction of the combustion chamber is parallel to the vertical direction; the lower end of the shell is provided with a smoke exhaust structure; the upper end of the first flue gas channel is communicated with the upper end of the second flue gas channel, and the lower end of the second flue gas channel is communicated with the smoke exhaust structure.

As a preferred embodiment, the smoke exhausting structure comprises a smoke collecting cavity arranged at the lower end of the shell and a smoke exhaust port communicated with the smoke collecting cavity; a supporting part is arranged in the smoke collecting cavity; the support portion is supported between the top wall and the bottom wall of the smoke collection chamber.

In a preferred embodiment, the area of the smoke discharge port is 0.5 times or more the area of the smoke discharge port at the lower end of the second smoke flow path.

As a preferred embodiment, the shell is provided with a water inlet end close to or at the bottom of the shell; the water inlet end is communicated with the second coil unit.

As a preferred embodiment, the housing is provided with a steam outlet near or at the top of the housing; the steam output end is communicated with the first coil unit; and the top of the shell is also provided with a communicating pipe which is used for communicating the second coil unit with the first coil unit.

In a preferred embodiment, the heat exchange coil of the first coil unit is made of stainless steel; and the heat exchange coil of the second coil unit is a stainless steel finned tube.

As a preferred embodiment, the housing comprises a cylindrical main body and end covers fixedly covering two ends of the cylindrical main body; the inner side of the end cover is provided with a heat insulation plate; an air spacing layer is arranged between the heat insulation plate and the end cover.

In a preferred embodiment, a supporting structure for supporting the first coil unit is further provided in the housing.

As a preferred embodiment, a positioning box is further arranged on the inner side of the end cover; the first coil unit and the second coil unit are confined between an upper positioning box and a lower positioning box.

A steam generating apparatus comprising:

a can-shaped burner;

the heat exchange device for a steam generating apparatus according to any one of the above embodiments; the cylindrical combustor is positioned in a combustion chamber defined by the heat exchange device.

Has the advantages that:

according to the heat exchange device provided by the embodiment of the invention, the first flue gas flow channel, the second flue gas flow channel and the communicated flue gas flow channel are arranged, so that the contact area of flue gas and the heat exchange tubes of the first coil unit and the second coil unit is increased, the heat exchange efficiency is improved, the effects of energy conservation, high efficiency and high reliability are achieved, and the rapid generation of water vapor is realized.

In addition, the heat exchange device can also reduce the volume of the heat exchange device.

Specific embodiments of the present invention are disclosed in detail with reference to the following description and drawings, indicating the manner in which the principles of the invention may be employed. It should be understood that the embodiments of the invention are not so limited in scope.

Features that are described and/or illustrated with respect to one embodiment may be used in the same way or in a similar way in one or more other embodiments, in combination with or instead of the features of the other embodiments.

It should be emphasized that the term "comprises/comprising" when used herein, is taken to specify the presence of stated features, integers, steps or components but does not preclude the presence or addition of one or more other features, integers, steps or components.

Drawings

In order to more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the drawings used in the description of the embodiments or the prior art will be briefly described below, it is obvious that the drawings in the following description are only some embodiments of the present invention, and for those skilled in the art, other drawings can be obtained according to the drawings without inventive exercise.

FIG. 1 is a schematic cross-sectional view of a steam generating apparatus provided in accordance with an embodiment of the present invention;

FIG. 2 is a front view of the heat exchange unit of FIG. 1;

FIG. 3 is a side view of FIG. 2;

FIG. 4 is a perspective view of FIG. 2;

FIG. 5 is a sectional view A-A of FIG. 3;

FIG. 6 is a partial schematic view of FIG. 5;

FIG. 7 is a partial schematic view of FIG. 1;

FIG. 8 is a schematic cross-sectional view of the coil unit of FIG. 1;

FIG. 9 is a perspective view of the coil unit of FIG. 1;

FIG. 10 is a schematic view of the smoke evacuation arrangement of FIG. 1;

FIG. 11 is a side view of FIG. 1;

fig. 12 is a front view of fig. 10.

Description of reference numerals: 100. a housing; 101. an upper end cover; 102. a lower end cover; 110. a water inlet end; 120. a steam output end; 130. a fluid output; 140. a fluid input; 150. a communicating pipe; 180. an inner containing space; 190. an outer containment space; 200. a smoke evacuation structure; 201. a smoke outlet; 202. a smoke collection cavity; 203. a condensed water discharge port; 205. a bottom wall; 210. A support portion; 300. a supporting seat; 400. a burner; 500. a fan;

f1, axial; f2, radial;

1. a combustion chamber; 2. a first coil unit; 20. an inner heat exchange coil tube; 21. a first inner heat exchange coil tube; 22. a second inner heat exchange coil tube; 25. a heat exchange tube ring; 3. a second coil unit; 30. an outer heat exchange coil tube; 31. a finned heat exchange tube; 4. a spacer structure; 5. a first flue gas channel; 6. a second flue gas channel; 61. a smoke outlet; 7. a flue gas channel is communicated; 8. an upper positioning box; 81. an upper accommodating groove; 9. a heat insulation plate; 10. a lower positioning box; 1011. and a lower accommodating groove.

Detailed Description

In order to make those skilled in the art better understand the technical solution of the present invention, the technical solution in the embodiment of the present invention will be clearly and completely described below with reference to the drawings in the embodiment of the present invention, and it is obvious that the described embodiment is only a part of the embodiment of the present invention, and not all embodiments. All other embodiments, which can be obtained by a person skilled in the art without any inventive step based on the embodiments of the present invention, shall fall within the scope of the present invention.

It will be understood that when an element is referred to as being "disposed on" another element, it can be directly on the other element or intervening elements may also be present. When an element is referred to as being "connected" to another element, it can be directly connected to the other element or intervening elements may also be present. The terms "vertical," "horizontal," "left," "right," and the like as used herein are for illustrative purposes only and do not represent the only embodiments.

Unless defined otherwise, all technical and scientific terms used herein have the same meaning as commonly understood by one of ordinary skill in the art to which this invention belongs. The terminology used herein in the description of the invention is for the purpose of describing particular embodiments only and is not intended to be limiting of the invention. As used herein, the term "and/or" includes any and all combinations of one or more of the associated listed items.

Referring to fig. 1-12, one embodiment of the present invention provides a heat exchange device suitable for use in, but not limited to, a steam generating apparatus such as a steam boiler. The volume of the heat exchange device of the steam generating equipment is below 30L. This heat transfer device can be fast with by heating medium intensification 130 degrees centigrade more than, for example the temperature of input water is 20 degrees centigrade, and the steam temperature of output is 180 degrees, is 160 degrees centigrade through the heat transfer device temperature rise. Specifically, this heat transfer device includes: a housing 100; a first coil unit 2 and a second coil unit 3 located within the housing 100.

Specifically, the inner space surrounded by the first coil unit 2 is configured as a combustion chamber 1. The burner 400 is located in the combustion chamber 1 in the housing 100 for combustion to form high temperature flue gas. The second coil unit 3 surrounds the first coil unit 2. The first coil unit 2 and the second coil unit 3 heat the fluid inside to form steam through heat exchange with high-temperature flue gas.

A spacing structure 4 is provided between the second coil unit 3 and the first coil unit 2. The second coil unit 3 communicates upstream of the first coil unit 2 in the direction of the flow of the medium to be heated. The first coil unit 2 is closer to the burner 400 than the second coil unit 3, and correspondingly, the first coil unit 2 is located upstream of the second coil unit 3 in the flow direction of the flue gas.

As shown in FIG. 1, the combustor 400 is a fully premixed combustor 400. A fan 500 and a premixing device are connected to the upstream side of the combustor 400 (for example, to the upper side of the combustor 400). Air and gas are mixed in a desired ratio by a premixing device, and are sent to the combustor 400 by the fan 500 to be ignited in the combustion chamber 1 for combustion. The water in the first coil unit 2 is converted from liquid to steam, forming a steam-water mixing area, and outputting the steam. Water enters the second coil unit 3 for preheating, and then enters the first coil unit 2 for evaporation and overheating, so that water forms water vapor and the water vapor is output.

In this embodiment, a first flue gas flow channel 5 is provided between the first coil unit 2 and the spacer structure 4. A second flue gas flow channel 6 is formed between the spacer structure 4 and the housing 100. The second flue gas channel 6 is communicated with the downstream of the first flue gas channel 5. The first coil unit 2 is provided with a communicating flue gas channel 7 for communicating the first flue gas channel 5 with the combustion chamber 1. The high-temperature flue gas enters the first flue gas flow channel 5 through the communicating flue gas flow channel 7, flows in the first flue gas flow channel 5, enters the second flue gas flow channel 6, and is finally discharged.

The heat transfer device that this embodiment provided is through being equipped with first flue gas runner 5, second flue gas runner 6 and intercommunication flue gas runner 7, and then promotes the area of contact of flue gas and first coil unit 2 and second coil unit 3's heat exchange tube, promotes heat transfer efficiency, reaches energy-conserving high-efficient, the high effect of reliability, realizes the quick production of steam. Moreover, the heat exchange device can also reduce the volume of the heat exchange device.

In this embodiment, the interior cylindrical cavity of the housing 100. The spacing structure 4 is a cylindrical spacing plate, and can be a spacing cylinder. The spacing cylinder is of a cylindrical structure. The partition structure 4 partitions the inside of the case 100 to form an inner receiving space 180 and an outer receiving space 190. Wherein the first coil unit 2 and the burner 400 are located in the inner receiving space 180, and the second coil unit 3 is located in the outer receiving space 190. In outer accommodation space 190, the space in the outside of second coil unit 3 forms second flue gas runner 6, and the upper end of second flue gas runner 6 is the flue gas input end, and the lower extreme is the flue gas discharge end for the flue gas flows from the top down on the whole, carries out abundant heat transfer with second coil unit 3. The first coil unit 2 is located in the inner accommodating space 180, and an inter-tube gap L2 and an axial gap L1 are formed between the heat exchange tubes thereof, thereby increasing the contact heat exchange area with the flue gas and improving the heat exchange efficiency. The first coil unit 2 is spaced from the inner wall of the spacer cylinder by a certain distance to form a first flue gas flow channel 5.

In other embodiments, the spacer structure 4 may be a conical cylinder. The number of coil rings of the first coil unit 2 is gradually reduced from top to bottom, the longitudinal section of the first coil unit can be in an inverted cone structure, correspondingly, the number of coil rings of the second coil unit 3 is gradually increased from top to bottom, the longitudinal section of the second coil unit can be in a forward cone structure, the two ring sleeves form a roughly rectangular section shape, and correspondingly, the first flue gas flow channel 5 and the second flue gas flow channel 6 are parallel inner and outer inclined flow channels positioned on the inner side and the outer side of the cone cylinder.

In this embodiment, the second flue gas flow channel 6 is spaced around the first flue gas flow channel 5. One end of the second flue gas channel 6 along the whole flue gas flow direction is communicated with one end of the first flue gas channel 5, and the other end of the second flue gas channel 6 is a flue gas outlet 61 for outputting the flue gas after heat exchange outwards. Further, the flue gas direction of the first flue gas flow passage 5 and the second flue gas flow passage 6 is substantially parallel to the extending direction (length direction) of the combustion chamber 1.

The heat exchange device of this embodiment can promote the heat transfer area that first heat exchange coil participated in the heat transfer through being equipped with intercommunication flue gas runner 7. In this embodiment, combustion chamber 1 and first flue gas runner 5 are located the inside and outside both sides of first coil unit 2, guarantee that the inside and outside both sides of first coil unit 2 fully contact with the flue gas, guarantee heat exchange efficiency, intercommunication flue gas runner 7 is located the upper and lower (axial F1) both sides of the heat exchange tube of first heat exchange coil, make both sides can fully contact with the flue gas equally about the heat exchange tube of first coil unit 2, increase the heat transfer area of heat transfer device and flue gas, promote heat exchange efficiency, and then need not to increase coil length, be favorable to reducing heat transfer device's volume.

For reducing heat transfer device's volume and promoting the heat transfer effect, the flue gas certainly first flue gas runner 5 flows in the flow direction change more than 150 degrees of second flue gas runner 6, so reduce the flue gas velocity of flow, promote the heat transfer effect of flue gas and coil pipe unit. Preferably, the extending directions of the first flue gas channel 5 and the second flue gas channel 6 are parallel. The flow direction of the flue gas in the first flue gas flow channel 5 is opposite to the flow direction of the flue gas in the second flue gas flow channel 6. The spacing structure 4 is surrounding between the first coil unit 2 and the second coil unit 3. The first flue gas channel 5 extends along the inner wall surface of the spacer structure 4. The second flue gas channel 6 extends along the outer wall surface of the spacer structure 4.

In other embodiments, the first flue gas channel 5 and the second flue gas channel 6 may not be parallel. For example, one of the first flue gas flow passage 5 and the second flue gas flow passage 6 is a vertical flow passage, and the other is an oblique flow passage, or both are oblique flow passages. The flue gas directions of the first flue gas flow channel 5 and the second flue gas flow channel 6 form a certain included angle, and the communication position of the two is a flue gas turning position. The flue gas changes flow direction in first

flue gas runner

5 and 6 intercommunication departments of second flue gas runner, avoids the flue gas to flow at the excessive speed, promotes the heat transfer effect to, make 6 intervals of second flue gas runner encircle outside first flue gas runner 5, reduce heat transfer device's volume.

In this embodiment, the burner 400 of the heat exchanger may be a vertical burner 400, or may be a horizontal burner 400. In this embodiment, the burner 400 is a vertical burner 400, which facilitates the positioning and installation of the coil units (the first coil unit 2 and the second coil unit 3) in the housing 100 without the need for supporting and positioning the radial direction F2.

In the present embodiment, the combustion chamber 1 extends in an axial direction F1. The combustion chamber 1 extends in a direction parallel to the vertical direction. The vertical burner 400 is located in the combustion chamber 1 with the axial direction F1 likewise being vertical or parallel to the vertical direction. The spacer structure 4 is cylindrical. The spacer structure 4 may be a spacer cylinder fixed within the housing 100. The first flue gas flow channel 5 is arranged between the spacing structure 4 and the first coil unit 2 and extends along the axial direction F1. A first flue gas flow path 5 is located in the flow path of the straight tube structure between the spacer structure 4 and the first coil unit 2. The second flue gas flow channel 6 is arranged between the partition plate and the shell 100 and extends along the axial direction F1. The overall flue gas direction communicating with the flue gas channel 7 flows substantially in the radial direction F2. Preferably, the communicating flue gas flow passage 7 is perpendicular to the overall flue gas direction of the first axial direction F1 flue gas flow passage.

Specifically, the first coil unit 2 and the second coil unit 3 are formed by extending heat exchange tubes in a spiral manner. In order to bear the high pressure state of the vaporized water vapor and avoid the deformation of the heat exchange tube structure, the heat exchange tube is of a round tube structure and avoids the adoption of a flat tube structure which is easy to deform under the vapor pressure. Wherein the first coil unit 2 comprises at least one inner heat exchanging coil cylinder 20. The second coil unit 3 comprises at least one outer heat exchanging coil tube 30. The innermost inner heat exchange coil cylinder 20 communicates with the other inner heat exchange coil cylinders 20 upstream in the flow direction of the medium to be heated. Inside the shell 100, a plurality of inner heat exchange coil cylinders 20 are connected in series from inside to outside. The single inner heat exchange coil cartridge 20 may be formed by an uninterrupted spiral extension of a heat exchange tube from top to bottom. The inner heat exchange coil tube 20 is a cylindrical (or cylindrical) tube having the same outer diameter and inner diameter from top to bottom. First coil unit 2 may include one or two or three inner heat exchange coil barrels 20.

Further, each of the inner heat exchange coil cartridges 20 includes a plurality of rings of heat exchange tubes (spirals) stacked in the axial direction F1. The heat exchange tube ring 25 is not a closed ring, but a spiral structure formed by extending the heat exchange tube by 180 degrees in a spiral manner, and the projection of the spiral structure on a horizontal plane is a closed ring. Wherein, a plurality of heat exchange tube rings 25 are communicated in sequence from top to bottom to form a spiral structure.

Wherein, the communicating flue gas flow passage 7 comprises: an axial gap L1 between adjacent two of said inner heat exchange coil loops in axial direction F1 (in axial direction F1). The communicating flue gas flow passage 7 further comprises: and an inter-barrel gap L2 is formed between two adjacent inner heat exchange coil barrels 20 along the radial direction F2 (on the radial direction F2). The inter-barrel gap L2 communicates the axial gap L1 of two adjacent inner heat exchange coil barrels 20.

Further, the projection of the heat exchange tube ring 25, the inner heat exchange coil barrel 20 or the outer heat exchange coil barrel 30 in the horizontal plane is circular, and in other embodiments, the projection of the heat exchange tube ring 25, the inner heat exchange coil barrel 20 or the outer heat exchange coil barrel 30 in the horizontal plane may also be rectangular or in other shapes.

In the present embodiment, the heat exchange tube rings 25 of the first coil unit 2 have a spacing gap (axial gap L1) therebetween. The deformation space is provided for the deformation of the heat exchange tube through the interval gap, and the equipment is prevented from being damaged due to hard contact. Moreover, by arranging the interval gap, a communicated flue gas channel 7 which is approximately along the radial direction F2 can be formed, the heat exchange area between the first coil unit 2 and flue gas is increased, the heat exchange efficiency is improved, the volume of the coil unit is reduced, the volume of the steam generating equipment is maintained below a desired value, the capacity is not easy to exceed the standard, and the energy saver is not required for assistance. Wherein, the interval clearance (axial clearance L1) of first coil unit 2 is more than 2mm along the length of axial F1, so can avoid blocking up between the pipe, makes things convenient for the flue gas circulation, cooperatees with the fin heat exchange tube 31 of flue gas low reaches simultaneously, guarantees heat exchange efficiency.

In order to have better system reliability and ensure the service life of the equipment, the inner heat exchange surface of the first coil unit 2 surrounding the combustion chamber 1 is a finless heat exchange surface so as to bear the high temperature of high-temperature flue gas. Wherein, the innermost inner heat exchange coil tube is formed by spirally extending the finless heat exchange tubes along the axial direction F1.

Specifically, the fluid inside the first coil unit 2 is preheated by the second coil unit 3, so that the heat absorption capacity of the first coil unit is reduced, the temperature of the surface of the heat exchange tube is difficult to reduce, if the finned heat exchange tube 31 is easy to damage, and in order to ensure the service life of the equipment, the first coil unit 2 is formed by a finned heat exchange tube.

In the present embodiment, at least a part (length) of the heat exchange tubes in the first coil unit 2 are finless heat exchange tubes, and at least a part of the heat exchange tubes in the second coil unit 3 are finned heat exchange tubes 31, so as to improve heat exchange efficiency. Further, the heat exchange coil of the first coil unit 2 is made of stainless steel; and the heat exchange coil of the second coil unit 3 is a stainless steel finned tube.

The heat exchange device of this embodiment carries out the heat transfer with the high temperature flue gas before fin heat exchange tube 31 through no fin heat exchange tube, and then the flue gas has been cooled down when flowing to fin heat exchange tube 31, utilizes fin heat exchange tube 31 to carry out abundant heat transfer with flue gas and water, preheats water to avoid fin heat exchange tube 31 to be damaged by the high temperature flue gas, promoted equipment use reliability, guaranteed equipment life, extension maintenance cycle.

The finned heat exchange tube 31 is in contact with the outer wall of the spacer cylinder and the inner wall of the casing 100 in the outer accommodating space 190, and is communicated with the heat exchange tube up and down through gaps between the fins, so that smoke can pass through the heat exchange tube. The finned heat exchange tube 31 may not be in contact with the outer wall of the spacer and the inner wall of the casing 100. In order to reduce the volume of the heat exchange device, the clearance between the finned heat exchange tube 31 (the second coil unit 3) and the outer wall of the spacing cylinder and/or the inner wall of the shell 100 is within 5 mm.

To ensure the heat exchange efficiency, the second coil unit 3 includes a finned coil or a corrugated pipe which is located in the second flue gas flow passage 6 and spirally extends along the axial direction F1. In the present embodiment, the second coil unit 3 is formed by extending spirally a finned heat exchange tube 31.

In this embodiment, an axial spacer is disposed between two adjacent inner heat exchanging coil rings along the axial direction F1, and the uniformity of the axial gap L1 can be ensured by the axial spacer. Wherein, the axial spacing piece can be a spacing bar between two adjacent inner heat exchange coil rings. An axial clearance L1 which is spirally and uninterruptedly extended together with the heat exchange tube is arranged on the inner heat exchange coil tube. A plurality of spacer bars are provided in the axial gap L1. The spacing bars can be made of stainless steel materials, and deformation of the spacing bars under high-temperature smoke is avoided.

In order to improve the turbulent flow of the flue gas and enhance the heat exchange effect, at least partial (length or number) axial gaps L1 of the two adjacent inner heat exchange coil tubes are staggered. As shown in fig. 5, the arrow shows the flow direction of the flue gas in the communicating flue gas flow channel 7, the axial gap L1 at the upper part of the first inner heat exchange coil barrel 21 is opposite to the heat exchange tubes of the second inner heat exchange coil barrel 22 along the radial direction F2, the flue gas flowing out of the axial gap L1 of the first inner heat exchange coil barrel 21 collides with the inner side walls of the heat exchange tubes of the second inner heat exchange coil barrel 22 and flows upwards or downwards, then flows out of the axial gap L1 of the second inner heat exchange coil barrel 22 into the first flue gas flow channel 5 and flows upwards along the axial direction F1 along the inner wall of the spacer barrel.

Further, the heated medium flowing areas of the inner heat exchange coils of at least two inner heat exchange coil barrels are different. Wherein, the flow area of the heated medium is the internal cross-sectional area of the heat exchange tube. In this embodiment, in order to improve the operation stability of the apparatus, the heated medium flow area of the inner heat exchange coil tube located at the outer side is larger than that of the inner heat exchange coil tube located at the inner side. Compared with the inner heat exchange coil barrel on the inner side, the inner heat exchange coil barrel on the outer side has the advantages that the fluid inside the inner heat exchange coil barrel gradually begins to be vaporized to form water vapor, the volume of the fluid inside the inner heat exchange coil barrel is increased, the flow area of the heated medium of the inner heat exchange coil barrel on the outer side is larger, the volume change of the fluid can be adapted, the pipeline resistance is reduced, and the operation stability and the reliability of equipment are improved.

In the present embodiment, the first coil unit 2 includes: two inner heat exchange coil tubes are sleeved with each other. Wherein, each inner heat exchange coil pipe barrel is formed by spirally extending a finless heat exchange pipe along the axial direction F1. The finless heat exchange tube can be a light tube, or a corrugated tube. Preferably, the finned heat exchange tube is of a light pipe structure, so that the fins are prevented from being damaged by high temperature, and the service life of the equipment is influenced.

The two inner heat exchange coil barrels can be a first inner heat exchange coil barrel 21 and a second inner heat exchange coil barrel sleeved outside the first inner heat exchange coil barrel 21. The flow area of the heated medium of the second inner heat exchange tube cylinder (of the heat exchange tube) is larger than that of the heated medium of the first inner heat exchange tube cylinder (of the heat exchange tube). As can be seen in fig. 5 and 8, the pipe diameter of the second internal heat exchange tube is larger than that of the first internal heat exchange tube.

One end of the first flue gas channel 5 in the axial direction F1 is communicated with one end of the second flue gas channel 6. The other end of the second flue gas channel 6 is communicated with the smoke exhausting structure 200. As shown in fig. 1, the upper end of the first flue gas flow channel 5 is communicated with the upper end of the second flue gas flow channel 6. The lower end of the second flue gas channel 6 is communicated with the smoke exhausting structure 200. The second flue gas flow passage 6 or the flue gas outlet 61 at the lower end of the outer accommodating space 190 is annular and directly leads into the flue gas collecting cavity 202 below the second flue gas flow passage. Meanwhile, the smoke outlet 61 is also a condensed water discharge port 203 of the second smoke flow path 6.

The temperature of the fluid in the second coil unit 3 is low, and thus condensed water is easily formed in the outer receiving space 190. The fluid that first coil unit 2 flows in is the fluid after preheating through second coil unit 3 to the temperature rise is bigger, exceeds 100 degrees centigrade even, based on the higher temperature of the inside fluid of first coil unit 2, is difficult for forming the comdenstion water in accommodation space 180, and then can not set up the comdenstion water discharge structure including the lower end cover 102 of accommodation space 180 coverage.

In this embodiment, in order to ensure the heat exchange efficiency, ensure the smoke evacuation effect, and avoid the smoke from being too large to affect the steam generation, the minimum effective smoke flow area of the smoke evacuation structure 200 is greater than or equal to half of the minimum effective smoke flow area of the second smoke flow channel 6.

The lower end of the housing 100 is provided with a smoke evacuation structure 200. The lower end of the smoke evacuation structure 200 is further provided with a support base 400. The steam generating device is supported by the support base 400. The lower end of the second flue gas channel 6 is communicated with the smoke exhausting structure 200. Further, the smoke exhausting structure 200 can also be used as a condensed water discharging structure to collect condensed water in the second smoke flow channel 6 and discharge the condensed water to the outside. Of course, in other embodiments, the heat exchanger may additionally be provided with a condensed water discharging structure, which is communicated with the lower end of the second flue gas channel 6.

In this embodiment, the smoke exhausting structure 200 includes a smoke collecting cavity 202 disposed at the lower end of the casing 100, and a smoke exhausting port 201 connected to the smoke collecting cavity 202. A support portion 210 is disposed in the smoke collection chamber 202. The support 210 is supported between the top and bottom walls 205 of the smoke collection chamber 202. The smoke collection chamber 202 is an annular chamber surrounding the support portion. The area of the smoke exhaust port 201 is more than 0.5 times of the area of the smoke outlet 61 at the lower end of the second smoke flow channel 6. The bottom wall 205 of the smoke collection chamber 202 is a sloped bottom wall.

As shown in fig. 11, the bottom wall 205 of the smoke collection chamber 202 is gradually sloped downward toward the smoke exit 201. A condensed water outlet 203 is also arranged at the position of the bottom wall 205 of the smoke collection cavity 202 close to the smoke outlet 201. Preferably, condensate drain port 203 is located at the lowest position of bottom wall 205 of smoke collection chamber 202.

In this embodiment, the supporting portion 210 may be a supporting column located at a substantially central position of the smoke collection chamber 202. In other embodiments, the supporting portion 210 may also be supporting rods or other supporting structures dispersed at different positions in the smoke collecting cavity 202 to maintain the structural stability of the smoke exhausting structure 200, provide a higher smoke flowing area, facilitate the discharge of smoke from the heat exchanging device, and maintain the stable performance of efficient heat exchange inside the casing 100.

In this embodiment, the housing 100 includes a cylindrical body, and end caps (an upper end cap 101 and a lower end cap 102) fixedly covering both ends of the cylindrical body. The upper and

lower caps

101 and 102 may be fixedly coupled to upper and lower ends of the cylindrical body by flanges. And a heat insulation plate 9 is arranged on the inner side of the end cover. Further, in order to provide a better heat insulation effect, an air spacing layer is arranged between the heat insulation plate 9 and the end cover.

As shown in fig. 4, the housing 100 is provided with a water inlet end 110 near or at the bottom of the housing 100. The water inlet end 110 is communicated with the second coil unit 3. The lower end of the second coil unit 3 is a water inlet end 110. The water inlet end 110 may be a threaded or flanged connection. The housing 100 is provided with a steam output 120 near or at the top of the housing 100. The steam outlet 120 is in communication with the first coil unit 2. The top of the housing 100 is further provided with a communication pipe 150 for communicating the second coil unit 3 with the first coil unit 2. The communication pipe 150 is provided on the upper end cap 101 of the case 100.

The whole flow direction of the water (heated medium) in the second coil unit 3 is from bottom to top, the whole flue gas flow direction in the second flue gas flow channel 6 is from top to bottom, and the flow directions of the water and the flue gas are opposite, so that the preheating effect of the second coil unit 3 is improved. The upper end of the second coil unit 3 is a fluid output end 130, which is communicated with a fluid input end 140 at the upper end of the first coil unit 2 through a communicating pipe 150 outside the casing 100. The fluid input 140 at the upper end of the first coil unit 2 is the upper end of the innermost inner heat exchange coil cylinder. The heated medium in the innermost inner heat exchange coil tube (the first inner heat exchange coil tube 21) flows from top to bottom as a whole, and is communicated with the second inner heat exchange coil tube 22 at the bottom to flow into the second inner heat exchange coil tube 22. The second inner heat exchanging coil pipe 22 has a steam outlet 120 at an upper end thereof and extends from the upper end cap 101 to output steam outwardly.

In this embodiment, the inner side of the end cover is further provided with a positioning box (an upper positioning box 8 and a lower positioning box 10). The first coil unit 2 and the second coil unit 3 are confined between an upper positioning box 8 and a lower positioning box 10. The upper positioning box 8 and the lower positioning box 10 are fixedly arranged on the heat insulation plate 9. The positioning boxes (8, 10) are in annular U-shaped groove structures. The ends of the first coil unit 2 and the second coil unit 3 may protrude into the upper receiving groove 81 and the lower receiving groove 1011 of the positioning box.

In this embodiment, a holding structure for holding the first coil unit 2 is further disposed in the housing 100. The support structure may be a support plate provided on the lower positioning box 10. The supporting plate can be spirally extended (along with the heat exchange tube at the lowest position) to be arranged on the inner wall of the lower positioning box 10, so that the lowest heat exchange tube is supported, the phenomenon that the lowest heat exchange tube is suspended is avoided, and the coil tube unit deforms to influence the heat exchange effect is avoided. The lower end of the first coil unit 2 is seated in the lower positioning box 10, and the inner and outer sides of the lower end of the first coil unit 2 can be bonded to the inner wall of the lower positioning box 10, thereby restricting the first coil unit 2 in the radial direction F2.

Yet another embodiment of the present invention provides a steam generating apparatus including: a can-shaped burner 400; the heat exchanger for a steam generating apparatus according to any one of the above embodiments. The cylindrical burner 400 is positioned in the combustion chamber 1 defined by the heat exchange device.

Any numerical value recited herein includes all values from the lower value to the upper value, in increments of one unit, with at least two units of separation between any lower value and any higher value. For example, if it is stated that the number of a component or a value of a process variable (e.g., temperature, pressure, time, etc.) is from 1 to 90, preferably from 20 to 80, and more preferably from 30 to 70, it is intended that equivalents such as 15 to 85, 22 to 68, 43 to 51, 30 to 32 are also expressly enumerated in this specification. For values less than 1, one unit is suitably considered to be 0.0001, 0.001, 0.01, 0.1. These are only examples of what is intended to be explicitly recited, and all possible combinations of numerical values between the lowest value and the highest value may be considered to be explicitly recited in the specification in a similar manner.

Unless otherwise indicated, all ranges include the endpoints and all numbers between the endpoints. The use of "about" or "approximately" with a range applies to both endpoints of the range. Thus, "about 20 to 30" is intended to cover "about 20 to about 30", including at least the endpoints specified.

All articles and references disclosed, including patent applications and publications, are hereby incorporated by reference for all purposes. The term "consisting essentially of …" describing a combination shall include the identified element, ingredient, component or step as well as other elements, ingredients, components or steps that do not materially affect the basic novel characteristics of the combination. The use of the terms "comprising" or "including" to describe combinations of elements, components, or steps herein also contemplates embodiments that consist essentially of such elements, components, or steps. By using the term "may" herein, it is intended to indicate that any of the described attributes that "may" include are optional.

A plurality of elements, components, parts or steps can be provided by a single integrated element, component, part or step. Alternatively, a single integrated element, component, part or step may be divided into separate plural elements, components, parts or steps. The disclosure of "a" or "an" to describe an element, ingredient, component or step is not intended to foreclose other elements, ingredients, components or steps.

It is to be understood that the above description is intended to be illustrative, and not restrictive. Many embodiments and many applications other than the examples provided will be apparent to those of skill in the art upon reading the above description. The scope of the present teachings should, therefore, be determined not with reference to the above description, but should instead be determined with reference to the appended claims, along with the full scope of equivalents to which such claims are entitled. The disclosures of all articles and references, including patent applications and publications, are hereby incorporated by reference for all purposes. The omission in the foregoing claims of any aspect of subject matter that is disclosed herein is not intended to forego the subject matter and should not be construed as an admission that the inventors did not consider such subject matter to be part of the disclosed subject matter.

Claims

1. A heat exchange device for a steam generating apparatus, comprising: a housing; a first coil unit and a second coil unit located within the housing;

2. The heat exchange device of claim 1, wherein the extension directions of the first flue gas flow channel and the second flue gas flow channel are parallel; the flow direction of the flue gas in the first flue gas channel is opposite to that of the flue gas in the second flue gas channel.

3. The heat exchange device of claim 1, wherein the spacing structure surrounds the first coil unit and the second coil unit; the first flue gas flow channel extends along the inner wall surface of the spacing structure; the second flue gas flow channel extends along the outer wall surface of the spacing structure.

4. The heat exchange device of claim 1 wherein the spacing structure is a cylindrical spacer plate.

5. The heat exchange device of claim 1, wherein the combustion chamber extends in an axial direction; the spacing structure is cylindrical; the first flue gas flow channel is arranged between the spacing structure and the first coil pipe unit and extends along the axial direction; the second flue gas flow channel is arranged between the spacing structure and the shell and extends along the axial direction.

6. The heat exchange device according to claim 1, wherein one end of the first flue gas flow channel in the axial direction is communicated with one end of the second flue gas flow channel; the other end of the second flue gas channel is communicated with the smoke exhaust structure.

7. The heat exchange apparatus of claim 6 wherein the minimum effective flue gas flow area of the flue gas removal structure is greater than or equal to half the minimum effective flue gas flow area of the second flue gas flow path.

8. The heat exchange device of claim 1 wherein the first coil unit comprises at least one inner heat exchange coil tube; wherein, the inner heat exchange coil pipe barrel positioned at the innermost side is formed by spirally extending the finless heat exchange pipe along the axial direction.

9. The heat exchange device of claim 8, wherein the first coil unit comprises: two inner heat exchange coil pipes are sleeved with each other; each inner heat exchange coil pipe barrel is formed by spirally extending fin-free heat exchange pipes along the axial direction.

10. The heat exchange device of claim 8, wherein the innermost inner heat exchange coil tube communicates upstream of the other inner heat exchange coil tubes in the direction of flow of the medium being heated.

11. The heat exchange unit of claim 8 wherein each of said inner heat exchange coil barrels comprises a plurality of axially stacked heat exchange tube rings; the communicating flue gas flow passage comprises: and the axial gap is positioned between two axially adjacent inner heat exchange coil rings.

12. The heat exchange apparatus of claim 11 wherein the communicating flue gas flow path further comprises: a gap between every two radially adjacent inner heat exchange coil tubes is formed between the two radially adjacent inner heat exchange coil tubes; the axial gaps of the two adjacent inner heat exchange coil pipe barrels are communicated through the inter-barrel gaps.

13. The heat exchange unit of claim 11 wherein an axial spacer is disposed between axially adjacent ones of said inner heat exchange coil loops.

14. The heat exchange device of claim 11 wherein the axial gaps of adjacent two of the inner heat exchange coil tubes are staggered.

15. The heat exchange device according to claim 8, wherein the heated medium flow areas of the inner heat exchange coils of at least two of the inner heat exchange coil tubes are different; the heated medium flow area of the inner heat exchange coil barrel positioned at the outer side is larger than that of the inner heat exchange coil barrel positioned at the inner side.

16. The heat exchange device of claim 1, wherein the second coil unit communicates upstream of the first coil unit in a direction of flow of the heated medium.

17. The heat exchange unit of claim 1 wherein the second coil unit comprises an axially helically extending finned coil or bellows located within the second flue gas flow path.

18. The heat exchange device of claim 1, wherein the combustion chamber extends in a direction parallel to the vertical direction; the lower end of the shell is provided with a smoke exhaust structure; the upper end of the first flue gas channel is communicated with the upper end of the second flue gas channel, and the lower end of the second flue gas channel is communicated with the smoke exhaust structure.

19. The heat exchange device of claim 18, wherein the smoke evacuation structure comprises a smoke collection chamber disposed at the lower end of the shell, and a smoke exhaust port communicated with the smoke collection chamber; a supporting part is arranged in the smoke collecting cavity; the support portion is supported between the top and bottom walls of the smoke collection chamber.

20. The heat exchange apparatus of claim 19 wherein the area of the smoke exhaust is greater than 0.5 times the area of the smoke exhaust at the lower end of the second flue gas flow path.

21. The heat exchange device of claim 1 wherein the shell is provided with a water inlet end near or at the bottom of the shell; the water inlet end is communicated with the second coil unit.

22. The heat exchange device of claim 1 wherein the housing is provided with a steam outlet near or at the top of the housing; the steam output end is communicated with the first coil pipe unit; and the top of the shell is also provided with a communicating pipe for communicating the second coil unit with the first coil unit.

23. The heat exchange device of claim 1, wherein the heat exchange coil of the first coil unit is stainless steel; and the heat exchange coil of the second coil unit is a stainless steel finned tube.

24. The heat exchange device of claim 1, wherein the housing comprises a cylindrical body and end caps fixedly covering both ends of the cylindrical body; the inner side of the end cover is provided with a heat insulation plate; an air spacing layer is arranged between the heat insulation plate and the end cover.

25. The heat exchange device of claim 1 wherein a support structure is further provided within the housing to support the first coil unit.

26. The heat exchange device of claim 24, wherein a positioning box is further arranged inside the end cover; the first coil unit and the second coil unit are confined between an upper positioning box and a lower positioning box.

27. A steam generating apparatus, comprising:

a can-shaped burner;

the heat exchanging device for steam generating equipment as claimed in any one of claims 1 to 22; the cylindrical combustor is positioned in a combustion chamber defined by the heat exchange device.