CN88210298U - High temp. air preheating apparatus - Google Patents
High temp. air preheating apparatus Download PDFInfo
- Publication number
- CN88210298U CN88210298U CN 88210298 CN88210298U CN88210298U CN 88210298 U CN88210298 U CN 88210298U CN 88210298 CN88210298 CN 88210298 CN 88210298 U CN88210298 U CN 88210298U CN 88210298 U CN88210298 U CN 88210298U
- Authority
- CN
- China
- Prior art keywords
- air
- taken over
- heat
- tube bundle
- housing
- 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
Links
- 239000000779 smoke Substances 0.000 claims abstract description 13
- 238000004519 manufacturing process Methods 0.000 claims abstract description 6
- 239000000463 material Substances 0.000 claims abstract description 5
- 239000011449 brick Substances 0.000 claims description 3
- 238000000034 method Methods 0.000 claims description 3
- 238000003466 welding Methods 0.000 claims description 3
- 229910000831 Steel Inorganic materials 0.000 claims description 2
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims description 2
- 229910001220 stainless steel Inorganic materials 0.000 claims description 2
- 239000010935 stainless steel Substances 0.000 claims description 2
- 239000010959 steel Substances 0.000 claims description 2
- 239000006229 carbon black Substances 0.000 abstract description 9
- 238000006243 chemical reaction Methods 0.000 abstract description 2
- 238000012423 maintenance Methods 0.000 abstract description 2
- 229910000975 Carbon steel Inorganic materials 0.000 abstract 1
- 239000010962 carbon steel Substances 0.000 abstract 1
- 230000008642 heat stress Effects 0.000 abstract 1
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 8
- 239000007789 gas Substances 0.000 description 8
- 239000003546 flue gas Substances 0.000 description 7
- 239000012774 insulation material Substances 0.000 description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 239000010425 asbestos Substances 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 229910052895 riebeckite Inorganic materials 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 230000008646 thermal stress Effects 0.000 description 1
- 230000003245 working effect Effects 0.000 description 1
Images
Landscapes
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
- Air Supply (AREA)
Abstract
The utility model discloses a high temperature air preheater for preheating air required by carbon black reaction in the production process of furnace carbon black, comprising a housing (5), a heat exchange tube bundle (6), an air inlet and an air outlet connection tubes (11), (8), a smoke gas inlet and a smoke gas outlet connection tubes (2), (12), and a base (15). The high temperature air preheater adopts a U-shaped heat exchange tube bundle, air runs in a tube side, and smoke gas runs in a shell side, so that the heat stress of the heat exchange tube bundle (6) while running can be reduced, and the phenomenon of rupture can be eliminated; air temperature can also be preheated to 450 DEG C by using common carbon steel materials. Compared with the existing shell and tube air preheaters, the utility model has the advantages of simple structure, convenient maintenance, low cost and long service life.
Description
A kind of novel high-temperature air preheater is suitable for preheated air in the furnace treated black Production Flow Chart.In manufacturing technologies of carbon black, utilize the sooty high-temperature flue gas in air preheater, to carry out heat exchange, thereby preheated air reach the purpose that improves carbon black mass and yield with generation carbon black reaction required air.
At present, the domestic shell and tube air preheater that adopts more, air is walked shell side, flue gas is walked between the last lower tubesheet that the tube side heat-exchanging tube bundle is fixed on preheater, because the inhomogeneous temperature of respectively managing of flue gas flow between each pipe is unequal, the thermal expansion of each pipe is not waited, inequality between pipe and the shell expands in addition, cause the work-ing life of air preheater very short, after general 2-3 month, advance flue gas end tube plate deformation, the welding seam breaking of tube sheet and pipe causes air leaks, cause partial combustion, air preheater is damaged, and can't overhaul; In order to address this problem, taked complicated single tube equalising means abroad, complex structure involves great expense.
In order to overcome above-mentioned deficiency, the utility model has adopted the medium flow process opposite way of the air preheater of using with existing production of carbon black, its major technique feature is: air is walked tube side, carbon black smoke is walked shell side, structurally adopt single backhaul U type heat-exchanging tube bundle (6), be weldingly fixed on upper end tube sheet (7), upper end tube sheet (7) is connected with bolt with flange (4) on the housing (5), the lower end does not have tube sheet, tube bank (7) retractable.Fixedly the baffling rod (3) of heat transfer tube places between pipe, makes carbon black smoke become turbulence state to flow enhance heat transfer speed; Housing (5) inner lining as thermal insulation material (13), thus solved between the thermal stress issues and tube and tube that interchanger exists, inequality thermal expansion problem between pipe and shell, and it is also less that heat-exchanging tube bundle is stopped the influence of stove rapid heat cycle simultaneously; Owing to adopt new texture, also can make preheating of air to 450 ℃ with the heat-exchanging tube bundle of plain carbon stool material; Equipment has low cost, the advantage of long service life.
The present invention is achieved in that
Housing (5) is the square metal cylindrical shell, divide four sections, every intersegmentally connect with bolt by flange (4), seal with asbestos plate, housing (5) inner lining as thermal insulation material (13), heat-exchanging tube bundle (6) adopts U type list backhaul form, the upper end is welded on the upper end tube sheet (7), fixing between tube and tube with baffling rod (3), gas inlet takes over (11) and air is taken over (8) and plenum chamber (9) welding, and the centre separates with dividing plate (10), and dividing plate is welded on the upper end tube sheet (7), smoke inlet takes over (2) and exhanst gas outlet is taken over (12) liner refractory concrete backing layer (1), establishes hand-hole (14) and base (15) in the equipment bottom
Concrete structure of the present invention is provided by embodiment and accompanying drawing:
Fig. 1: new type high temperature air preheater structure iron
(1) refractory concrete backing layer, (2) smoke inlet is taken over, (3) baffling rod (4) flange, (5) housing, (6) heat-exchanging tube bundle, (7) upper end tube sheet, (8) air is taken over, (9) air plenum chamber, (10) dividing plate, (11) gas inlet is taken over, (12) exhanst gas outlet is taken over, (13) lagging material lining, (14) hand-hole, (15) base.
Describe details and the working condition of the concrete device that proposes according to the present invention in detail below in conjunction with accompanying drawing:
High-temperature air preheater is when operation, high-temperature flue gas is taken over (2) from smoke inlet and is entered shell side, making flue gas form turbulent flow through baffling rod (3) upwards flows, carry out heat exchange with the air in the heat-exchanging tube bundle (6), taking over (12) from exhanst gas outlet then flows out, air is taken over (11) from air intake and is entered plenum chamber (9), evenly distribute and enter heat-exchanging tube bundle (6), air in pipe, flow with manage outside flue gas carry out heat exchange, realize the purpose of preheated air, take over (8) from air outlet slit then and flow out.
Embodiment:
Housing (5) is 1200 * 1200mm square metal housing, wall thickness 8mm is divided into four sections, except that one section of base is the 3100mm, its excess-three section is each section of 2000mm has flange (4) to connect with bolt, the asbestos plate sealing, housing (5) inner lining as thermal insulation material lining (13), lagging material lining (13) is built by laying bricks or stones for light weeight alumina brick, thick 160mm; Heat-exchanging tube bundle (6) in the housing (5) is 55 in φ 57 * 3.5mm weldless steel tube, and pipe range 12000mm is processed into the U type, is welded on the upper end tube sheet (7), and its tube spacing is 75mm, arranged in squares; Place between pipe the fixing baffling rod (3) of heat transfer tube to adopt the stainless steel tube of φ 90 * 4.5 and φ 16 * 1.5, length is 800mm, and two ends are welded on the heat-exchanging tube bundle (6), the layout of baffling rod (3), every interlamellar spacing is 400mm, and adjacent two layers is crossed as 90 °; It is 1600mm that tube bank (6) lower end and smoke inlet are taken over (2) width between centers, makes flue gas evenly flow through heat-exchanging tube bundle (6); The plenum chamber on top (9) is of a size of 1200 * 1200 * 400mm, gas inlet takes over (11) and air is taken over (8) employing bi-directional symmetrical layout, central dividing plate (10) separates, dividing plate (10) is welded on the upper end tube sheet (7), it is two Dg300 pipes that gas inlet is taken over (11), and it is two Dg350 pipes that air is taken over (8); Smoke inlet is taken over (2) and is of a size of φ 650mm, and exhanst gas outlet is taken over (12) and is of a size of φ 600, the thick refractory concrete backing layer of liner 100~120mm (1).
The present invention is owing to adopted novel structural shape, so that production of carbon black ruptures with air preheater no heat exchanger tube in the middle of operation and clogging takes place, this equipment is reliable, long service life is convenient to maintenance, compare with existing shell and tube air preheater, have the advantages such as cost simple in structure is low.
Claims (5)
1, the high temperature air that is used for the furnace treated black technological process of production gives hot device, by shell (5), joint flange (4), heat-exchanging tube bundle (6), upper end tube sheet (7), smoke inlet is taken over (2), and exhanst gas outlet is taken over (12), gas inlet is taken over (11), air is taken over (8), hand-hole (14), and base (15) constitutes.Feature of the present utility model is: the heat-exchanging tube bundle (6) in the housing (5) adopts U type list return structures, and two nose ends are weldingly fixed on the upper end tube sheet (7), and upper end tube sheet (7) is connected with bolt with flange (4) on the housing (5); Fixing between tube and tube with baffling rod (3); Housing (5) thickness of inner lining is the lightweight high alumina insulating brick material (13) of 160mm; The smoke inlet of housing (5) lower end is taken over the exhanst gas outlet on (2) and top and is taken over the thick refractory concrete lining (1) of (12) liner 100-120mm; Air intlet takes over (11) and air is taken over (8) and plenum chamber (9) welding, and the centre separates with dividing plate (10), and dividing plate (10) is welded on the upper end tube sheet (7).
2, according to claim 1ly give hot device and it is characterized in that: heat-exchanging tube bundle (6) is 55 single backhaul U type weldless steel tubes, and the pipe specification is φ 57 * 3.5, and tube spacing is 75mm, arranged in squares.
3, according to claim 1ly give hot device, it is characterized in that: it is 1600mm that heat-exchanging tube bundle (6) lower end and smoke inlet are taken over (2) width between centers.
4, according to claim 1ly give hot device, it is characterized in that: baffling rod (3) is φ 90 * 4.5 and φ 16 * 1.5 stainless steel tubes, and length is 800mm, and its two ends are welded on the heat-exchanging tube bundle (6).
5, describedly give hot device according to claim 1 or 4, it is characterized in that: the every interlamellar spacing of layout of baffling rod (3) is 400mm, and adjacent two layers is crossed as 90 °.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 88210298 CN88210298U (en) | 1988-03-16 | 1988-03-16 | High temp. air preheating apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 88210298 CN88210298U (en) | 1988-03-16 | 1988-03-16 | High temp. air preheating apparatus |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN88210298U true CN88210298U (en) | 1988-12-21 |
Family
ID=4843801
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 88210298 Pending CN88210298U (en) | 1988-03-16 | 1988-03-16 | High temp. air preheating apparatus |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN88210298U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102563891A (en) * | 2010-12-28 | 2012-07-11 | 新奥科技发展有限公司 | Capillary tube radiation cooling type photovoltaic electricity and heat combined using device |
| CN102840771A (en) * | 2012-09-26 | 2012-12-26 | 洛阳隆华传热科技股份有限公司 | Vertical type air cooling cooler |
| CN101910778B (en) * | 2008-01-07 | 2013-07-17 | 阿尔斯托姆科技有限公司 | Flexible assembly of recuperator for combustion turbine exhaust |
| CN106957541A (en) * | 2017-03-24 | 2017-07-18 | 中昊黑元化工研究设计院有限公司 | The carbon black energy-saving production method and device of a kind of outer pre-heating technique air of line |
-
1988
- 1988-03-16 CN CN 88210298 patent/CN88210298U/en active Pending
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101910778B (en) * | 2008-01-07 | 2013-07-17 | 阿尔斯托姆科技有限公司 | Flexible assembly of recuperator for combustion turbine exhaust |
| CN102563891A (en) * | 2010-12-28 | 2012-07-11 | 新奥科技发展有限公司 | Capillary tube radiation cooling type photovoltaic electricity and heat combined using device |
| CN102840771A (en) * | 2012-09-26 | 2012-12-26 | 洛阳隆华传热科技股份有限公司 | Vertical type air cooling cooler |
| CN106957541A (en) * | 2017-03-24 | 2017-07-18 | 中昊黑元化工研究设计院有限公司 | The carbon black energy-saving production method and device of a kind of outer pre-heating technique air of line |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN101457304B (en) | Central reverse flame interior heat storing type energy-saving high efficiency furnace and tank integrated reducing furnace system | |
| CN102042609B (en) | Rotary high-temperature air preheater | |
| US4346753A (en) | Regenerator checkerwork brick | |
| CN102251094A (en) | Regenerative soaking furnace burning low calorific value gas | |
| CN110514037A (en) | A lower tube-sheet cooling structure of a shell-and-tube high-temperature air preheater | |
| CN102676849A (en) | Reduction tank and magnesium reduction furnace | |
| CN88210298U (en) | High temp. air preheating apparatus | |
| CN201945175U (en) | Multiple-effect integrated pipe type heating furnace | |
| CN2079616U (en) | High temp. air preheater for producing carbon black | |
| CN102978317B (en) | Hot-blast stove double-preheating device | |
| CN203550637U (en) | Plate-type preheating device for aluminum-fusing shaft furnace | |
| CN111238247A (en) | Ascending pipe for recovering waste heat of coke oven crude gas and method for utilizing waste heat of ascending pipe | |
| CN2506641Y (en) | Dry quenched coke oven body | |
| CN102080933A (en) | Rotary high-temperature air preheater | |
| EP0152967B1 (en) | A recuperative heat exchanger | |
| CN108387119B (en) | All ceramic heat exchanger, heat exchange baffle mold and preparation method of heat exchange baffle | |
| CN101922868B (en) | High temperature heat exchanger | |
| CN2203424Y (en) | Vertical air heating furnace by ribbed tube heat-exchange | |
| RU237033U1 (en) | Recuperative heat exchanger of radial-spiral type | |
| CN206724722U (en) | Rotary hearth furnace fume afterheat gradient utilization system | |
| CN2173903Y (en) | Separated spiral groove pipe heat-exchanging furnace | |
| CN217875922U (en) | High-temperature energy-saving plate preheater | |
| CN2290005Y (en) | Vertical pearlite expansion furnace | |
| CN206425543U (en) | A kind of big bag roaster | |
| CN2138282Y (en) | Spray-pipe air preheater |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C20 | Patent right or utility model deemed to be abandoned or is abandoned | ||
| WD01 | Invention patent application deemed withdrawn after publication |