CN104654843A - Membrane-type multilayer vibrating transportation solid and fluid heat exchanger - Google Patents
Membrane-type multilayer vibrating transportation solid and fluid heat exchanger Download PDFInfo
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Abstract
The invention discloses a membrane-type multilayer vibrating transportation solid and fluid heat exchanger. The membrane-type multilayer vibrating transportation solid and fluid heat exchanger comprises a membrane-type wall transportation box body, an elastic connecting rod mechanism and a vibration exciting source, wherein a box body frame is fixedly arranged outside the membrane-type wall transportation box body; the elastic connecting rod mechanism with a bearing effect is hinged to the box body frame; the vibration exciting source is fixed to the box body frame; the membrane-type wall transportation box body comprises a top membrane-type wall, a left side membrane-type wall, a right side membrane-type wall and a bottom membrane-type wall which are connected with one another to form a fully-closed outer coating surface, and an inner membrane-type wall which is arranged in the membrane-type wall transportation box body. According to the membrane-type multilayer vibrating transportation solid and fluid heat exchanger, the effects of high power output, wide power output regulation ratio, small equipment size, low electric power consumption, low wear, long service life, full sealing, high temperature resistance, high pressure resistance, no blockage in operation and the like are achieved by adopting the technical measures of multi-layer vibrating transportation, a membrane-type wall heat exchange surface, sieving particles with different sizes to pass through different channels and the like.
Description
Technical field
The present invention relates to the wall-type heat exchange technical field of solid material and fluid, be specially solid and the fluid heat exchanger of the conveying of a kind of membrane type multi-layer vibration.
Background technology
Along with the fast development of modern industrial technology, what require solid material and fluid heat exchanger has larger exert oneself (conveying capacity and exchange capability of heat).The requirement single device of some chemical system is exerted oneself and is reached 50 ~ 100t/h, and also reaches 30t/h for the separate unit quantity of slag of the CFB boiler slag-cooling device of 300MW.
When using as material cooler, in order to obtain higher system effectiveness, needing to obtain higher heat carrier energy grade, namely making fluid reach higher outlet temperature and pressure.When using as heating material or drier, higher fluid side temperature, pressure ability to bear obviously also provides the wider scope of application.
In chemical system, some material can carry some inflammable and explosive or poisonous gases and enter solid material and fluid heat exchanger, if inflammable and explosive or toxic gas is inhaled into external leakage or air, may cause security incident.This just requires that solid material and fluid heat exchanger can ensure hermetically sealed conveying.
Modern industrial technology fast-developing makes that power system capacity is larger, parameter is higher, also requires that the arrangement space of equipment is more compact, equipment energy consumption is more saved on the other hand on the one hand.
The solid that current domestic application is more and fluid heat exchanger mainly drum type heat-exchanger, what be widely used in power system CFB boiler slag-cooling device has jacket type roller slag cooler and membrane type rotary drum slag, these two kinds of slag coolers are all adopt roller conveyor principle, material is only in bottom and metal heat-exchange surface contact, and therefore effective heating surface is little, equipment volume is huge; Due to conveying cylindrical shell is that rotation is turned, and therefore cooling water must be led in/out by swivel joint, and the operating pressure of equipment is by the restriction (withstand voltage be less than 4MPa, heatproof is lower than 200 DEG C) of swivel joint and encapsulant thereof; Owing to meter rotation must be established to turn the dynamic structure of sealing at conveying cylindrical shell input and output material end, therefore cannot guarantee air-tightness, wherein jacket type roller slag cooler is because reasons in structure bearing capacity is not as good as membrane type rotary drum slag and weight of equipment is heavier.Multiple pipe type cold slag device is also the one of drum type heat-exchanger, although than jacket type roller slag cooler and membrane type rotary drum slag more compact, exist and to exert oneself little, susceptible to plugging shortcoming.
Summary of the invention
The object of the present invention is to provide one to exert oneself greatly for the problems referred to above, equipment volume is little, the solid of the membrane type multi-layer vibration conveying that hermetically sealed, high-temperature resistant is withstand voltage and fluid heat exchanger, and concrete technical scheme is as follows:
The solid of membrane type multi-layer vibration conveying and a fluid heat exchanger, comprise membrane wall conveying casing, elastic linkage mechanism and exciting source; Described membrane wall conveying box is external is fixedly installed box frame, and elastic linkage mechanism and the box frame with load-bearing effect are hinged, and exciting source is fixed on box frame; Described membrane wall conveying casing comprises the top membrane wall, right side membrane wall, left side membrane wall and the bottom membrane wall that are interconnected to constitute totally-enclosed outsourcing clad can, and is arranged on the internal membrane wall of membrane wall conveying box house; Described membrane wall conveying casing is also provided with charging aperture and discharging opening.
Further, described elastic linkage mechanism with suspend in midair force way be articulated with described box frame top or to support the below that force way is articulated with box frame.
Further, described elastic linkage mechanism comprise elastic spacing connecting rod for limiting vibrating body amplitude with for limiting the swing connecting bar of vibrating body movement locus, swing connecting bar is articulated with described membrane wall conveying tank ends, and elastic spacing rod hinge connection is in the middle part of described membrane wall conveying casing.
Further, described internal membrane wall comprises inner upper membrane wall and interior subordinate's membrane wall, and on inside, membrane wall carries casing to be separated into three, upper, middle and lower material conveying passage by membrane wall and interior subordinate's membrane wall.
Further, on described inside, membrane wall is the sieve texture only allowing the particle being less than screen size to pass through near one end of charging aperture, and it is horizontal screen or inclined screen.
Further, in described membrane wall conveying casing, the arrival end top of three material conveying passages in upper, middle and lower is respectively equipped with adjustable for height limit for height baffle plate.
Further, described top membrane wall and bottom membrane wall are two independently tube panels, and its one end is connected by the first header, and the other end is connected by the second header; Membrane wall one end, described right side is provided with the 3rd header, and the other end is provided with the 5th header, and membrane wall one end, left side is provided with the 4th header, and the other end is provided with the 6th header; On described inside, the heat pipe of membrane wall and interior subordinate's membrane wall is U-shaped structure, on inside membrane wall heat pipe influent stream mouth with go out head piece be connected respectively in establish the shunting section of the 7th header of dividing plate and the section of confluxing, the influent stream mouth of interior subordinate's membrane wall heat pipe and go out head piece be connected respectively in establish shunting section and the section of confluxing of the 8th header of dividing plate; Described first header connects the portal metal flexible pipe entered for fluid, second header connects the 3rd header and the 4th header respectively by tube connector, 5th header connects the shunting section of the 7th header by tube connector, 6th header connects the shunting section of the 8th header by tube connector, the common connection outlet metal hose of the section of confluxing of the 7th header and the 8th header.
Further, described top membrane wall and bottom membrane wall are bent by an overall tube panel and form, and membrane wall end, bottom is provided with the first header, and membrane wall end, top is provided with the second header; The heat pipe of right side membrane wall and left side membrane wall is U-shaped structure, the influent stream mouth of right side membrane wall heat pipe and go out head piece be connected respectively in establish shunting section and the section of confluxing of the 3rd header of dividing plate, the influent stream mouth of left side membrane wall heat pipe with go out head piece be connected respectively in establish shunting section and the section of confluxing of the 4th header of dividing plate; Interior subordinate's membrane wall one end is provided with the 5th header, and the other end is provided with the 6th header, and on inside, membrane wall one end is provided with the 7th header, and the other end is provided with the 8th header; Described first header connects the portal metal flexible pipe entered for fluid, second header connects the shunting section of the 3rd header and the 4th header respectively by tube connector, the section of confluxing of the 3rd header and the 4th header is connected to the 5th header by tube connector, 6th header is connected to the 7th header by tube connector, the 8th header connection outlet metal hose.
Further, described charging aperture and discharging opening are plane bend pipe membrane wall open-celled structure or space bent pipe membrane wall open-celled structure.
Further, described membrane wall conveying casing is also provided with steam drain.
The invention has the beneficial effects as follows: the present invention adopts multi-layer vibration conveying, membrane wall heat-transfer surface, screening sized particles subchannel to pass through, control the technical measures such as material conveying layer height, achieve exert oneself (conveying capacity and exchange capability of heat) large, wide adjustment ratio of exerting oneself, equipment volume is little, electrical power consumed is little, the low life-span of wearing and tearing is long, hermetically sealed, high-temperature resistant is withstand voltage, runs effects such as not blocking; Can be used as solid material cooler or Exposure degree equipment use, also can be used as solid material heater or drying equipment use.
Accompanying drawing explanation
Fig. 1 is the structural representation that elastic linkage mechanism of the present invention adopts supporting force way hinged.
Fig. 2 is the structural representation that elastic linkage mechanism of the present invention adopts suspention force way hinged.
Fig. 3 is that on inside of the present invention, membrane wall end is the membrane wall conveying box body structure schematic diagram of horizontal screen.
Fig. 4 is that on inside of the present invention, membrane wall end is the membrane wall conveying box body structure schematic diagram of inclined screen.
Fig. 5 is the fluid flow schematic diagram of the membrane wall conveying casing that Fig. 3, Fig. 4 of the present invention are corresponding.
Fig. 6 is the membrane wall conveying box body structure schematic diagram of the another kind of membrane wall structure of the present invention.
Fig. 7 is the fluid flow schematic diagram of the membrane wall conveying casing that Fig. 6 of the present invention is corresponding.
Fig. 8 is the membrane wall heat-transfer surface sectional drawing of pipe of the present invention and the direct welding fabrication of band steel.
Fig. 9 is the shaping membrane wall heat-transfer surface sectional drawings of the present invention's many extended surface tube assembly weldings.
Figure 10 is that the present invention welds extended surface tube sectional drawing.
Figure 11 is the extended surface tube sectional drawing of steel straight forming of the present invention.
Figure 12 is the sieve aperture membrane wall structure schematic diagram of single-ended header tube panel of the present invention.
Figure 13 is the sieve aperture membrane wall structure schematic diagram of both-end header tube panel of the present invention.
Figure 14 is a kind of plane bend pipe of the present invention membrane wall open-celled structure schematic diagram.
Figure 15 is a kind of space bent pipe membrane wall of the present invention open-celled structure schematic diagram.
In figure: 1-membrane wall conveying casing; 2-box frame; 3-elastic linkage mechanism; 4-exciting source; 5-elastic spacing connecting rod; 6-swing connecting bar; 7-top membrane wall; Membrane wall on the right side of 8-; Membrane wall on 9-inside; Subordinate's membrane wall in 10-; Membrane wall bottom 11-; Membrane wall on the left of 12-; 13-first header; 14-second header; 15-the 3rd header; 16-the 4th header; 17-the 5th header; 18-the 6th header; 19-the 7th header; 20-the 8th header; 21,22,23-limit for height baffle plate; 24-charging aperture; 25-discharging opening; 26-steam drain; 27-portal metal flexible pipe; 28-tube connector; 29-exports metal hose.
Detailed description of the invention
Below in conjunction with the drawings and specific embodiments, the present invention will be further described: a kind of solid of membrane type multi-layer vibration conveying and fluid heat exchanger, comprises membrane wall conveying casing 1, elastic linkage mechanism 3 and exciting source 4.Described membrane wall conveying casing 1 extenal fixation is provided with box frame 2, for transmitting exciting force and strengthening membrane wall conveying casing 1 rigidity; Exciting source 4 is fixed on box frame 2, for generation of periodic exciting force; Elastic linkage mechanism 3 is hinged with box frame 2, carry with membrane wall the elastic link vibrating mechanism that the common structure of casing 1, box frame 2 and exciting source 4 is complete, while and bear the weight of three.
Elastic linkage mechanism 3 can be hinged in Equipment Foundations in one end, the other end to support the below that force way is articulated with box frame 2, as shown in Figure 1; Also can be hinged on spandrel girder in one end, the other end to suspend the top that force way is articulated with described box frame 2 in midair, as shown in Figure 2.
Elastic linkage mechanism 3 comprise elastic spacing connecting rod 5 for limiting vibrating body amplitude with for limiting the swing connecting bar 6 of vibrating body movement locus, swing connecting bar 6 is articulated with described membrane wall conveying casing 1 two ends, and elastic spacing connecting rod 5 is articulated with in the middle part of described membrane wall conveying casing 1.Elastic spacing connecting rod 5 can design on demand with the quantity of swing connecting bar 6, and the length of the length of elastic spacing connecting rod 5, spring rate, swing connecting bar 6 can be fixing or adjustable.
Membrane wall conveying casing 1 is also provided with charging aperture 24, discharging opening 25 and steam drain 26, and steam drain 26 is as the use of discharging the steam that material is separated out during dried material.
Membrane wall conveying casing 1 comprises the top membrane wall 7, right side membrane wall 8, left side membrane wall 12 and the bottom membrane wall 11 that are interconnected to constitute totally-enclosed outsourcing clad can, and this totally-enclosed outsourcing clad can by material and external environs; Also comprise the internal membrane wall being horizontally installed on membrane wall conveying casing 1 inside.According to the different needs of conveying capacity size, can increase or reduce the quantity of internal membrane wall, the upper surface of internal membrane wall can weld the expansion heat transfer element of longitudinal fin or other shapes for strengthening exchange capability of heat.
As a specific embodiment of the present invention: arranging two internal membrane walls can, be specially inner upper membrane wall 9 and interior subordinate's membrane wall 10, on inside, membrane wall carries casing 1 to be separated into three, upper, middle and lower material conveying passage by membrane wall 9 and interior subordinate's membrane wall 10.On inside, membrane wall 9 is positioned at casing upper strata, its one end near charging aperture 24 is the sieve texture (as shown in Figure 12 and Figure 13) only allowing the particle being less than screen size to pass through, this sieve texture by layering conveying after material screening, can avoid the blocking of lower channel.Enough height space are left between membrane wall 9 and top membrane wall 7 in inside, can guarantee that the lump material of maximum particle diameter passes through, when membrane wall heat exchanger tube inside has fluid to cool, on inside, this sieve pore structure of membrane wall 9 sieves high-temperature material.This section of sieve texture part can be set to horizontal screen (as shown in Figure 3), also can be set to inclined screen (as shown in Figure 4), and the structure of inclination can make material more easily enter transfer passage by means of the effect of gravity, avoids the blocking of material.
In membrane wall conveying casing 1, the arrival end top of three material conveying passages in upper, middle and lower is respectively equipped with adjustable for height limit for height baffle plate 21,22,23, for limiting each layer material thickness, avoids that material is blocked up causes blocking.Can by limit for height baffle plate 21,22,23 are designed to limit material thickness fixes or adjustable structure, to guarantee reasonable thickness of feed layer required by vibrating transportation and to control the conveying capacity of material.
The vibration force that the present invention utilizes exciting source 4 to produce, membrane wall is forced to carry casing 1 to make periodic vibration under elastic linkage mechanism 3 limits, in casing, the solid material (graininess or powdery) of multilayer film type wall upper surface is jumped by periodically forward upward throwing and moves ahead, and this mode of movement equipment attrition little life-span is long; Fluid then consists of the membrane wall heat exchanger tube of membrane wall conveying casing 1 successively these, carry out septate heat transfer by tube wall, fin or fin and solid material.Whole membrane wall conveying casing 1 can be arranged to complete level, also can along mass transport direction horizontal by necessarily inclination angle up or down.Fluid can be the media such as water, conduction oil, water vapour, air, and fluid inlet and outlet adopts metal hose directly to connect, and its fluid side is withstand voltage reaches 10MPa, and heatproof can reach 400 DEG C.
A specific embodiment of above-mentioned membrane wall conveying casing 1 structure that two internal membrane walls (on inside membrane wall 9 and interior subordinate's membrane wall 10) are set: membrane wall conveying casing 1 structure corresponding to this embodiment as shown in Figure 3 and Figure 4, the concrete structure of each several part membrane wall is as follows: top membrane wall 7 and bottom membrane wall 11 are two independently tube panels, its one end is connected by the first header 13, and the other end is connected by the second header 14; Membrane wall 8 one end, described right side is provided with the 3rd header 15, and the other end is provided with the 5th header 17, and left side membrane wall 12 one end is provided with the 4th header 16, and the other end is provided with the 6th header 18; On described inside, the heat pipe of membrane wall 9 and interior subordinate's membrane wall 10 is U-shaped structure (now the sieve pore structure of inner upper membrane wall 9 end as shown in figure 12), on inside membrane wall 9 heat pipe influent stream mouth with go out head piece be connected respectively in establish the shunting section of the 7th header 19 of dividing plate and the section of confluxing, the influent stream mouth of interior subordinate's membrane wall 10 heat pipe and go out head piece be connected respectively in establish shunting section and the section of confluxing of the 8th header 20 of dividing plate; Described first header 13 connects the portal metal flexible pipe 27 entered for fluid, second header 14 connects the 3rd header 15 and the 4th header 16 respectively by tube connector 28,5th header 17 connects the shunting section of the 7th header 19 by tube connector 28,6th header 18 connects the shunting section of the 8th header 20 by tube connector 28, the common connection outlet metal hose 29 of the section of confluxing of the 7th header 19 and the 8th header 20.
The fluid flow schematic diagram of this membrane wall conveying casing 1 structure as shown in Figure 5, fluid enters the first header 13 by portal metal flexible pipe 27, the second header 14 is come together in after dividing two-way to flow into top membrane wall 7 and bottom membrane wall 11 respectively, and then point two-way, membrane wall 9, the 7th header 19 section of confluxing on the 3rd header 15, right side membrane wall 8, the 5th header 17, the 7th header 19 shunting section, inside are flow through successively through tube connector 28 in one tunnel, finally flow out from outlet metal hose 29; The 4th header 16, left side membrane wall 12, the 6th header 18, the 8th header 20 shunting section, interior subordinate's membrane wall 10, the 8th header 20 section of confluxing are flow through successively through tube connector 28 in another road, finally also flow out from outlet metal hose 29.
A specific embodiment of above-mentioned membrane wall conveying casing 1 structure that two internal membrane walls (on inside membrane wall 9 and interior subordinate's membrane wall 10) are set: membrane wall conveying casing 1 structure corresponding to this embodiment as shown in Figure 6, the concrete structure of each several part membrane wall is as follows: described top membrane wall 7 and bottom membrane wall 11 are bent by an overall tube panel and form, membrane wall 11 end, bottom is provided with the first header 13, and top membrane wall 7 end is provided with the second header 14; The heat pipe of right side membrane wall 8 and left side membrane wall 12 is U-shaped structure, the influent stream mouth of right side membrane wall 8 heat pipe and go out head piece be connected respectively in establish shunting section and the section of confluxing of the 3rd header 15 of dividing plate, the influent stream mouth of left side membrane wall 12 heat pipe with go out head piece be connected respectively in establish shunting section and the section of confluxing of the 4th header 16 of dividing plate; Interior subordinate's membrane wall 10 one end is provided with the 5th header 17, and the other end is provided with the 6th header 18, and on inside, membrane wall 9 one end is provided with the 7th header 19, and the other end is provided with the 8th header 20, and now the sieve pore structure of inner upper membrane wall 9 end as shown in figure 15; Described first header 13 connects the portal metal flexible pipe 27 entered for fluid, second header 14 connects the shunting section of the 3rd header 15 and the 4th header 16 respectively by tube connector 28, the section of confluxing of the 3rd header 15 and the 4th header 16 is connected to the 5th header 17 by tube connector 28,6th header 18 is connected to the 7th header the 19, eight header 20 connection outlet metal hose 29 by tube connector 28.
This membrane wall carries the fluid flow schematic diagram of casing 1 structure as shown in Figure 7: fluid flows through the first header 13, bottom membrane wall 11, top membrane wall 7, second header 14 successively by portal metal flexible pipe 27, then divide two-way, tube connector 28 of leading up to flows through the 3rd header 15 shunting section, right side membrane wall 8, the 3rd header 15 section of confluxing successively; Tube connector 28 of separately leading up to flows through the 4th header 16 shunting section, left side membrane wall 12, the 4th header 16 section of confluxing successively; Then two-way fluid collection is in the 5th header 17, then flows through membrane wall 9, the 8th header 20 on interior subordinate's membrane wall 10, the 6th header 18, the 7th header 19, inside successively, finally flows out from outlet metal hose 29.
Wherein, the heat exchanger tube of membrane wall can be the structure be directly welded by pipe and band steel, as shown in Figure 8; Also can be the structure be welded with many extended surface tubes, as shown in Figure 9.Wherein, extended surface tube can be the extended surface tube that pipe and band steel are welded, as shown in Figure 10; Also the extended surface tube of straight forming can be made, as shown in figure 11.This structure allows to adopt steel plate (non-membrane wall) structure at the position that temperature of charge is lower.This heat exchanger can be used as solid material cooler or Exposure degree equipment use, and also can be used as solid material heater or drying equipment use, when using as solid material cooler, the inlet temperature of solid material can reach more than 1000 DEG C.When this heat exchanger uses as material cooler, near the material of discharging opening 25 near zone and fluid temperature (F.T.) all very low time, can replacing with simple steel plate structure coated of the membrane wall of these low-temperature regions of membrane wall conveying casing 1.In like manner, when using as material heater or drier, near the material of charging aperture 24 near zone and fluid temperature (F.T.) all very low time, also can replacing with simple steel plate structure in the coated face of the membrane wall of these low-temperature regions of membrane wall conveying casing 1.
Another embodiment of the present invention, charging aperture 24 and discharging opening 25 can be plane bend pipe membrane wall open-celled structure, as shown in figure 14; Also can be space bent pipe membrane wall open-celled structure, as shown in figure 15.This structure can make, in the process of material inlet and outlet membrane wall conveying casing 1, also can carry out heat exchange, add thermal interface, strengthen exchange capability of heat.
The present invention can by regulating the frequency of exciting source 4, and membrane wall conveying casing 1 inclination angle, swing connecting bar 6 angle, height, the fluid flow of the limit for height baffle plate 21,22,23 of the spring rate of elastic spacing connecting rod 5, three material conveying passages regulate exerting oneself.
Claims (10)
1. the solid of membrane type multi-layer vibration conveying and a fluid heat exchanger, is characterized in that, comprise membrane wall conveying casing (1), elastic linkage mechanism (3) and exciting source (4); Described membrane wall conveying casing (1) extenal fixation is provided with box frame (2), and the elastic linkage mechanism (3) with load-bearing effect is hinged with box frame (2), and exciting source (4) is fixed on box frame (2); Described membrane wall conveying casing (1) comprises the top membrane wall (7), right side membrane wall (8), left side membrane wall (12) and the bottom membrane wall (11) that are interconnected to constitute totally-enclosed outsourcing clad can, and is arranged on the inner internal membrane wall of membrane wall conveying casing (1); Described membrane wall conveying casing (1) is also provided with charging aperture (24) and discharging opening (25).
2. the solid of a kind of membrane type multi-layer vibration conveying according to claim 1 and fluid heat exchanger, it is characterized in that, described elastic linkage mechanism (3) with suspend in midair force way be articulated with described box frame (2) top or to support the below that force way is articulated with box frame (2).
3. the solid of a kind of membrane type multi-layer vibration conveying according to claim 1 and fluid heat exchanger, it is characterized in that, described elastic linkage mechanism (3) comprise elastic spacing connecting rod (5) for limiting vibrating body amplitude with for limiting the swing connecting bar (6) of vibrating body movement locus, swing connecting bar (6) is articulated with described membrane wall conveying casing (1) two ends, and elastic spacing connecting rod (5) is articulated with described membrane wall conveying casing (1) middle part.
4. the solid of a kind of membrane type multi-layer vibration conveying according to claim 1 and fluid heat exchanger, it is characterized in that, described internal membrane wall comprises inner upper membrane wall (9) and interior subordinate's membrane wall (10), and on inside, membrane wall carries casing (1) to be separated into three, upper, middle and lower material conveying passage by membrane wall (9) and interior subordinate's membrane wall (10).
5. the solid of a kind of membrane type multi-layer vibration conveying according to claim 4 and fluid heat exchanger, it is characterized in that, on described inside, membrane wall (9) is the sieve texture only allowing the particle being less than screen size to pass through near one end of charging aperture (24), and it is horizontal screen or inclined screen.
6. the solid of a kind of membrane type multi-layer vibration conveying according to claim 4 and fluid heat exchanger, it is characterized in that, the arrival end top of three material conveying passages in described membrane wall conveying casing (1) interior upper, middle and lower is respectively equipped with adjustable for height limit for height baffle plate (21,22,23).
7. the solid of a kind of membrane type multi-layer vibration conveying according to any one of claim 4-6 and fluid heat exchanger, it is characterized in that, described top membrane wall (7) and bottom membrane wall (11) are two independently tube panels, its one end is connected by the first header (13), and the other end is connected by the second header (14); Membrane wall (8) one end, described right side is provided with the 3rd header (15), and the other end is provided with the 5th header (17), and left side membrane wall (12) one end is provided with the 4th header (16), and the other end is provided with the 6th header (18); On described inside, the heat pipe of membrane wall (9) and interior subordinate's membrane wall (10) is U-shaped structure, on inside membrane wall (9) heat pipe influent stream mouth with go out head piece be connected respectively in establish the shunting section of the 7th header (19) of dividing plate and the section of confluxing, the influent stream mouth of interior subordinate's membrane wall (10) heat pipe and go out head piece be connected respectively in establish shunting section and the section of confluxing of the 8th header (20) of dividing plate; Described first header (13) connects the portal metal flexible pipe (27) entered for fluid, second header (14) connects the 3rd header (15) and the 4th header (16) respectively by tube connector (28), 5th header (17) connects the shunting section of the 7th header (19) by tube connector (28), 6th header (18) connects the shunting section of the 8th header (20) by tube connector (28), the common connection outlet metal hose (29) of the section of confluxing of the 7th header (19) and the 8th header (20).
8. the solid of a kind of membrane type multi-layer vibration conveying according to any one of claim 4-6 and fluid heat exchanger, it is characterized in that, described top membrane wall (7) and bottom membrane wall (11) are bent by an overall tube panel and form, membrane wall (11) end, bottom is provided with the first header (13), and top membrane wall (7) end is provided with the second header (14); The heat pipe of right side membrane wall (8) and left side membrane wall (12) is U-shaped structure, the influent stream mouth of right side membrane wall (8) heat pipe and go out head piece be connected respectively in establish the shunting section of the 3rd header (15) of dividing plate and the section of confluxing, the influent stream mouth of left side membrane wall (12) heat pipe with go out head piece be connected respectively in establish shunting section and the section of confluxing of the 4th header (16) of dividing plate; Interior subordinate's membrane wall (10) one end is provided with the 5th header (17), and the other end is provided with the 6th header (18), and on inside, membrane wall (9) one end is provided with the 7th header (19), and the other end is provided with the 8th header (20); Described first header (13) connects the portal metal flexible pipe (27) entered for fluid, second header (14) connects the shunting section of the 3rd header (15) and the 4th header (16) respectively by tube connector (28), the section of confluxing of the 3rd header (15) and the 4th header (16) is connected to the 5th header (17) by tube connector (28), 6th header (18) is connected to the 7th header by tube connector (28), the 8th header (20) connection outlet metal hose (29).
9. the solid of a kind of membrane type multi-layer vibration conveying according to any one of claim 1-6 and fluid heat exchanger, it is characterized in that, described charging aperture (24) and discharging opening (25) are plane bend pipe membrane wall open-celled structure or space bent pipe membrane wall open-celled structure.
10. the solid of a kind of membrane type multi-layer vibration conveying according to any one of claim 1-6 and fluid heat exchanger, is characterized in that, described membrane wall conveying casing (1) is also provided with steam drain (26).
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN107014221A (en) * | 2017-05-18 | 2017-08-04 | 华北理工大学 | A kind of oscillatory type multilayer variable cross-section membrane wall turbulent flow particle heat-exchanger rig |
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| CN2191974Y (en) * | 1994-05-12 | 1995-03-15 | 崔炳玮 | Herringbone film type sieve tray fluidized bed residue cooler |
| CN2562083Y (en) * | 2002-05-24 | 2003-07-23 | 王建海 | Water cooling vibrating apparatus for cooling slags |
| CN1400424A (en) * | 2002-08-08 | 2003-03-05 | 李玉清 | Rocking type slag-cooling machine |
| CN2847071Y (en) * | 2005-08-31 | 2006-12-13 | 盛健刚 | Vibration type air and water cooling slag tapping machine |
| CN204665992U (en) * | 2015-02-12 | 2015-09-23 | 四川龙麟锅炉设备有限责任公司 | A kind of solid of membrane type multi-layer vibration conveying and fluid heat exchanger |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107014221A (en) * | 2017-05-18 | 2017-08-04 | 华北理工大学 | A kind of oscillatory type multilayer variable cross-section membrane wall turbulent flow particle heat-exchanger rig |
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| CN104654843B (en) | 2017-01-18 |
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