CN104654843B - 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, specially a kind of membrane type multi-layer vibration is defeated
The solid sending and fluid heat exchanger.
Background technology
Fast development with modern industrial technology it is desirable to solid material and fluid heat exchanger have bigger exert oneself (defeated
The amount of sending and exchange capability of heat).The requirement single device of some chemical systems is exerted oneself and is reached 50 ~ 100t/h, and is used for the cfb of 300mw
The separate unit quantity of slag of boiler slag-cooling device also reaches 30t/h.
When using as material cooler, in order to obtain higher system effectiveness, need to obtain higher heat carrier energy
Grade, that is, make fluid reach higher outlet temperature and pressure.When using as material heating or drier, higher stream
Side temperature pressure tolerance obviously also provides the broader scope of application.
In chemical system, some materials can carry some inflammable and explosive or poisonous gas entrance solid material and fluids
Heat exchanger, if inflammable and explosive or toxic gas leaks out or air is inhaled into, may cause security incident.This will
Solid material and fluid heat exchanger is asked to can guarantee that hermetically sealed conveying.
On the one hand the fast-developing of modern industrial technology make that power system capacity is bigger, parameter is higher, on the other hand also requires that
The arrangement space of equipment is more compact, equipment energy consumption is more saved.
The more solid of domestic application and fluid heat exchanger are mainly drum type heat-exchanger at present, are widely used in power train
System cfb boiler slag-cooling device have jacket type roller slag cooler and membrane type rotary drum slag, both slag coolers are all to adopt cylinder
Conveyer principle, material is only contacted with metal heat-exchange surface in bottom, and therefore effective heating surface is little, equipment volume is huge；Due to
Conveying cylinder is swivel, and therefore cooling water must be led in/out by swivel joint, and the operating pressure of equipment is connect by rotation
The restriction (pressure less than 4mpa, heatproof is less than 200 DEG C) of head and its encapsulant；Due to must set at conveying cylinder input and output material end
Meter turns the dynamic structure of sealing, therefore cannot guarantee air-tightness, wherein jacket type roller slag cooler is due to reasons in structure bearing capacity
Not as good as membrane type rotary drum slag and weight of equipment is heavier.Multiple pipe type cold slag device is also one kind of drum type heat-exchanger although ratio presss from both sides
Shell type roller slag cooler and membrane type rotary drum slag are more compact, but there is little, susceptible to plugging shortcoming of exerting oneself.
Content of the invention
For the problems referred to above it is an object of the invention to provide one kind is exerted oneself greatly, equipment volume is little, and hermetically sealed, high-temperature resistant is resistance to
The solid of membrane type multi-layer vibration conveying of pressure and fluid heat exchanger, concrete technical scheme is as follows:
A kind of solid of membrane type multi-layer vibration conveying and fluid heat exchanger, including membrane wall conveying casing, elastic link machine
Structure and exciting source；Described membrane wall conveying box is fixedly installed box frame in vitro, has the elastic linkage mechanism of load-bearing effect
Hinged with box frame, exciting source is fixed on box frame；Described membrane wall conveying casing includes being interconnected to constitute full envelope
Close top membrane wall, right side membrane wall, left side membrane wall and the bottom membrane wall of outsourcing clad can, and be arranged on membrane wall conveying
The internal membrane wall of box house；It is additionally provided with charging aperture and discharging opening on described membrane wall conveying casing.
Further, described elastic linkage mechanism is articulated with the top of described box frame or to prop up to suspend force way in midair
Support force way is articulated with the lower section of box frame.
Further, described elastic linkage mechanism include for the elastic spacing connecting rod limiting vibrating body amplitude be used for
Limit the swing connecting bar of vibrating body movement locus, swing connecting bar is articulated with described membrane wall conveying tank ends, and elastic spacing is even
Bar is articulated with the middle part of described membrane wall conveying casing.
Further, described internal membrane wall includes membrane wall and internal lower membrane wall, membrane wall on inside on inside
With membrane wall under inside, membrane wall conveying casing is separated into upper, middle and lower three material conveying passage.
Further, on described inside, membrane wall is the particle only allowing less than screen size near one end of charging aperture
The sieve texture passing through, it is horizontal screen or inclined screen.
Further, in described membrane wall conveying box body, the arrival end top of three material conveying passages in upper, middle and lower is divided
It is not provided with adjustable for height limit for height baffle plate.
Further, described top membrane wall and bottom membrane wall are two independent tube panels, and its one end passes through first
Header connects, and the other end passes through the second header and connects；Described right side membrane wall one end is provided with the 3rd header, and the other end is provided with
5th header, left side membrane wall one end is provided with the 4th header, and the other end is provided with the 6th header；On described inside membrane wall and
The heat pipe of internal lower membrane wall is u-shaped structure, on inside the flow inlet of membrane wall heat pipe with go out head piece connect respectively in set
The shunting section of the 7th header of dividing plate and conflux section, the flow inlet of internal lower membrane wall heat pipe and go out head piece connect respectively in set
The shunting section of the 8th header of dividing plate and section of confluxing；The portal metal flexible pipe that described first header connection enters for fluid, second
Header connects the 3rd header and the 4th header by connecting tube respectively, and the 5th header connects the shunting of the 7th header by connecting tube
Section, the 6th header connects the shunting section of the 8th header by connecting tube, and the section of confluxing of the 7th header and the 8th header connects jointly
Outlet metal hose.
Further, described top membrane wall and bottom membrane wall are formed by an overall tube panel bending, bottom membrane wall
End is provided with the first header, and top membrane wall end is provided with the second header；Right side membrane wall and the heat conduction of left side membrane wall
Manage as u-shaped structure, the flow inlet of right side membrane wall heat pipe and go out head piece connect respectively in set dividing plate the 3rd header shunting
Section and conflux section, the flow inlet of left side membrane wall heat pipe and go out head piece connect respectively in set dividing plate the 4th header shunting section
With section of confluxing；Internal lower 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
It is provided with the 7th header, the other end is provided with the 8th header；Described first header connects the portal metal flexible pipe entering for fluid,
Second header connects the shunting section of the 3rd header and the 4th header respectively by connecting tube, the confluxing of the 3rd header and the 4th header
Section is connected to the 5th header by connecting tube, and the 6th header is connected to the 7th header by connecting tube, 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 additionally provided with steam drain.
The invention has the beneficial effects as follows: the present invention is divided using multi-layer vibration conveying, membrane wall heat-transfer surface, screening sized particles
Passage passes through, controls the conveying technical measures such as bed depth it is achieved that regulation of exerting oneself that (conveying capacity and exchange capability of heat) big, width is exerted oneself
Than, equipment volume is little, electrical power consumed is little, low life-span length of wearing and tearing, hermetically sealed, high-temperature resistant is pressure, run and do not block and other effects；Can conduct
Solid material cooler or Exposure degree equipment are using it is also possible to make solid material heater or drying equipment use.
Brief description
Fig. 1 is the elastic linkage mechanism of the present invention using the hinged structural representation of supporting force way.
Fig. 2 is the elastic linkage mechanism of the present invention using the hinged structural representation of suspention force way.
Fig. 3 is the membrane wall conveying casing structural representation that on the inside of the present invention, membrane wall end is horizontal screen.
Fig. 4 is the membrane wall conveying casing structural representation that on the inside of the present invention, membrane wall end is inclined screen.
Fig. 5 is the fluid flow schematic diagram that the corresponding membrane wall of Fig. 3, Fig. 4 of the present invention conveys casing.
Fig. 6 is the membrane wall conveying casing structural representation of present invention another kind membrane wall structure.
Fig. 7 is the fluid flow schematic diagram that the corresponding membrane wall of Fig. 6 of the present invention conveys casing.
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 membrane wall heat-transfer surface sectional drawing that many extended surface tube groups of the present invention are welded into type.
Figure 10 is present invention welding 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 the single-ended header tube panel of the present invention.
Figure 13 is the sieve aperture membrane wall structure schematic diagram of the both-end header tube panel of the present invention.
Figure 14 is a kind of present invention plane bend pipe membrane wall open-celled structure schematic diagram.
Figure 15 is a kind of present invention space bent pipe membrane wall 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 is even
Bar；6- swing connecting bar；7- top membrane wall；Membrane wall on the right side of 8-；Membrane wall on 9- inside；Lower membrane wall inside 10-；11- bottom
Portion's membrane wall；Membrane wall on the left of 12-；13- first header；14- second header；15- the 3rd header；16- the 4th header；17-
Five headers；18- the 6th header；19- the 7th header；20- the 8th header；21,22,23- limit for height baffle plates；24- charging aperture；25- goes out
Material mouth；26- steam drain；27- portal metal flexible pipe；28- connecting tube；29- exports metal hose.
Specific embodiment
The present invention will be further described with specific embodiment below in conjunction with the accompanying drawings: what a kind of membrane type multi-layer vibration conveyed consolidates
Body and fluid heat exchanger, convey casing 1, elastic linkage mechanism 3 and exciting source 4 including membrane wall.Described membrane wall conveys casing 1
It is fixedly installed outward box frame 2, for transmitting exciting force and strengthening membrane wall conveying casing 1 rigidity；Exciting source 4 is fixed on case
On body framework 2, for producing periodic exciting force；Elastic linkage mechanism 3 is hinged with box frame 2, with membrane wall conveying box
Body 1, box frame 2 and the complete elastic link vibrating mechanism of the common structure of exciting source 4, simultaneously and bear the weight of three.
Elastic linkage mechanism 3 can be hinged in Equipment Foundations with one end, and the other end is articulated with casing to support force way
The lower section of framework 2, as shown in Figure 1；Can also be hinged on spandrel girder one end, the other end with suspend in midair force way be articulated with described
The top of box frame 2, as shown in Figure 2.
Elastic linkage mechanism 3 includes transporting with for limiting vibrating body for the elastic spacing connecting rod 5 limiting vibrating body amplitude
The swing connecting bar 6 of dynamic rail mark, 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 be designed on demand with the quantity of swing connecting bar 6, elastic spacing
The length of connecting rod 5, spring rate, the length of swing connecting bar 6 can be fixing or adjustable.
It is additionally provided with charging aperture 24, discharging opening 25 and steam drain 26, steam drain 26 is as dried object on membrane wall conveying casing 1
The steam discharging material precipitation during material is used.
Membrane wall conveys top membrane wall 7, the right side membrane wall that casing 1 includes being interconnected to constitute totally-enclosed outsourcing clad can
8th, left side membrane wall 12 and bottom membrane wall 11, this totally-enclosed outsourcing clad can be by material and external environs；Also include horizontal stroke
Convey the internal membrane wall within casing 1 to being arranged on membrane wall.According to the different needs of conveying capacity size, can increase and add deduct
The quantity of few internal membrane wall, the extension heat transfer unit of longitudinal fin or other shapes can be welded in the upper surface of internal membrane wall
Part is used for strengthening exchange capability of heat.
A specific embodiment as the present invention: two internal membrane walls of setting can, specially internal upper membrane wall 9 He
Internal lower membrane wall 10, on inside, membrane wall is conveyed casing 1 and is separated into upper, middle and lower three by membrane wall 9 and internal lower membrane wall 10
Individual material conveying passage.On inside, membrane wall 9 is located at casing upper strata, and it is only to allow to be less than sieve aperture near one end of charging aperture 24
The sieve texture (as shown in Figure 12 and Figure 13) that the particle of size passes through, layering after material screening can be conveyed by this sieve texture,
Avoid the blocking of lower channel.Leave enough height space between membrane wall 9 and top membrane wall 7 on inside, can ensure that
The lump material of maximum particle diameter passes through, when having fluid cooling inside membrane wall heat exchanger tube, this sieve aperture of membrane wall 9 on inside
Structure is sieved to high-temperature material.This section of sieve texture part could be arranged to horizontal screen (as shown in Figure 3) it is also possible to arrange
For inclined screen (as shown in Figure 4), the structure of inclination can make material be easier to enter transfer passage by means of the effect of gravity, it is to avoid
The blocking of material.
The arrival end top that membrane wall conveys three material conveying passages in upper, middle and lower in casing 1 is respectively equipped with height adjustable
Limit for height baffle plate 21,22,23, for limiting each layer material thickness, it is to avoid material is blocked up to cause blocking.Can be 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 processed.
The present invention utilizes the vibration force that exciting source 4 produces, and forces membrane wall conveying casing 1 to limit in elastic linkage mechanism 3
Under make periodic vibration, in casing, the solid material (graininess or powdery) of multilayer film type wall upper surface is periodically gone up forward
Square throwing and jump and move ahead, this little life-span length of mode of movement equipment attrition；Fluid then passes sequentially through these and constitutes membrane wall conveying
The membrane wall heat exchanger tube of casing 1, carries out septate heat transfer by tube wall, fin or fin and solid material.Whole membrane wall conveying
Casing 1 can be arranged to fully horizontally it is also possible to along material conveying 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 is directly connected to using metal hose, its fluid side
Pressure up to 10mpa, heatproof is up to 400 DEG C.
The membrane wall conveying casing of above-mentioned two internal membrane walls of setting (membrane wall 9 and internal lower membrane wall 10 on inside)
One specific embodiment of 1 structure: the corresponding membrane wall of this embodiment conveys casing 1 structure as shown in Figure 3 and Figure 4, each several part
The concrete structure of membrane wall is as follows: top membrane wall 7 and bottom membrane wall 11 are two independent tube panels, and its one end passes through first
Header 13 connects, and the other end is connected by the second header 14；Described right side membrane wall 8 one end is provided with the 3rd header 15, another
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；Institute
The heat pipe stating membrane wall 9 and internal lower membrane wall 10 on inside is the u-shaped structure (sieve aperture of now internal upper membrane wall 9 end
Structure is as shown in figure 12), on inside the flow inlet of membrane wall 9 heat pipe and go out head piece connect respectively in set the 7th header of dividing plate
19 shunting section and conflux section, the flow inlet of internal lower membrane wall 10 heat pipe and go out head piece connect respectively in set the 8th of dividing plate
The shunting section of header 20 and section of confluxing；Described first header 13 connects the portal metal flexible pipe 27 entering for fluid, the second header
14 connect the 3rd header 15 and the 4th header 16 by connecting tube 28 respectively, and the 5th header 17 connects the 7th collection by connecting tube 28
The shunting section of case 19, the 6th header 18 connects the shunting section of the 8th header 20, the 7th header 19 and the 8th collection by connecting tube 28
Section of the confluxing common connection outlet metal hose 29 of case 20.
This membrane wall conveys the fluid flow schematic diagram of casing 1 structure as shown in figure 5, fluid passes through portal metal flexible pipe 27
Enter the first header 13, a point two-way comes together in the second header 14, then after separately flowing into top membrane wall 7 and bottom membrane wall 11
Divide two-way again, a road flows successively through the 3rd header 15, right side membrane wall 8, the 5th header 17,19 points of the 7th header through connecting tube 28
Stream section, membrane wall 9 on inside, the 7th header 19 are confluxed section, finally flow out from exporting metal hose 29；Another road is through connecting tube 28
Flow successively through the 4th header 16, left side membrane wall 12, the 6th header 18, the 8th header 20 shunting section, internal lower membrane wall 10, the
Eight headers 20 are confluxed section, finally also flow out from outlet metal hose 29.
The membrane wall conveying casing of above-mentioned two internal membrane walls of setting (membrane wall 9 and internal lower membrane wall 10 on inside)
One specific embodiment of 1 structure: this embodiment corresponding membrane wall conveying casing 1 structure is as shown in fig. 6, each several part membrane wall
Concrete structure as follows: described top membrane wall 7 and bottom membrane wall 11 are formed by an overall tube panel bending, bottom membrane wall 11
End is provided with the first header 13, and top membrane wall 7 end is provided with the second header 14；Right side membrane wall 8 and left side membrane wall
12 heat pipe is u-shaped structure, the flow inlet of right side membrane wall 8 heat pipe and go out head piece connect respectively in set the 3rd collection of dividing plate
The shunting section of case 15 and conflux section, the flow inlet of left side membrane wall 12 heat pipe and go out head piece connect respectively in set the 4th of dividing plate
The shunting section of header 16 and section of confluxing；Internal lower membrane wall 10 one end is provided with the 5th header 17, and the other end is provided with the 6th collection
Case 18, 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, now internal upper membrane type
The sieve pore structure of wall 9 end is as shown in figure 15；The portal metal flexible pipe 27 that described first header 13 connection enters for fluid, second
Header 14 connects shunting section, the 3rd header 15 and the 4th header of the 3rd header 15 and the 4th header 16 respectively by connecting tube 28
16 section of confluxing is connected to the 5th header 17 by connecting tube 28, and the 6th header 18 is connected to the 7th header by connecting tube 28
19, the 8th header 20 connection outlet metal hose 29.
The fluid flow schematic diagram that this membrane wall conveys casing 1 structure is as shown in Figure 7: fluid passes through portal metal flexible pipe 27
Flow successively through the first header 13, bottom membrane wall 11, top membrane wall 7, the second header 14, then divide two-way, the company of leading up to
Section that adapter 28 flows successively through the 3rd header 15 shunting section, right side membrane wall 8, the 3rd header 15 are confluxed；Separately lead up to connecting tube
Section that 28 flow successively through the 4th header 16 shunting section, left side membrane wall 12, the 4th header 16 are confluxed；Then two-way fluid comes together in
Five headers 17, then flow successively through membrane wall 10 under inside, the 6th header 18, the 7th header 19, membrane wall 9, the 8th collection on inside
Case 20, finally flows out from outlet metal hose 29.
Wherein, the heat exchanger tube of membrane wall can be the structure being directly welded by pipe and band steel, as shown in Figure 8；?
Can be the structure being welded with many extended surface tubes, as shown in Figure 9.Wherein, extended surface tube can be pipe with band steel weld and
The extended surface tube becoming, as shown in Figure 10；The extended surface tube of straight forming can also be made, as shown in figure 11.This structure allows in material temperature
Spending relatively low position adopts steel plate (non-membrane wall) to construct.This heat exchanger can be used as solid material cooler or Exposure degree equipment
Using it is also possible to make solid material heater or drying equipment use, solid material when using as solid material cooler
Inlet temperature is up to more than 1000 DEG C.When this heat exchanger uses as material cooler, near discharging opening 25 near zone
When material and fluid temperature (F.T.) are all very low, the membrane wall cladding face in these low-temperature regions that membrane wall conveys casing 1 can be with letter
Single steel plate structure replaces.In the same manner, when using as material heater or drier, near the thing of charging aperture 24 near zone
When material and fluid temperature (F.T.) are all very low, the membrane wall cladding face in these low-temperature regions that membrane wall conveys casing 1 can also be with letter
Single steel plate structure replaces.
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；Can also be space bent pipe membrane wall open-celled structure, as shown in figure 15.This structure can make material enter and
During discharging membrane wall conveying casing 1, also can carry out heat exchange, increased thermal interface, strengthen exchange capability of heat.
The present invention can be by the frequency of regulation exciting source 4, membrane wall conveying casing 1 inclination angle, swing connecting bar 6 angle,
The spring rate of elastic spacing connecting rod 5, the height of limit for height baffle plate 21,22,23 of three material conveying passages, fluid flow are to going out
Power is adjusted.
Claims (9)
1. a kind of solid of membrane type multi-layer vibration conveying and fluid heat exchanger are it is characterised in that include membrane wall conveying casing
(1), elastic linkage mechanism (3) and exciting source (4)；It is fixedly installed box frame (2) outside described membrane wall conveying casing (1),
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 conveys casing (1) and includes being interconnected to constitute top membrane wall (7), the right side membrane wall of totally-enclosed outsourcing clad can
(8), left side membrane wall (12) and bottom membrane wall (11), and it is arranged on the internal membrane that membrane wall conveys casing (1) inside
Wall；It is additionally provided with charging aperture (24) and discharging opening (25) on described membrane wall conveying casing (1)；Described elastic linkage mechanism (3) bag
Include for the elastic spacing connecting rod (5) limiting vibrating body amplitude with for limiting the swing connecting bar (6) of vibrating body movement locus, put
Dynamic connecting rod (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
In the middle part of casing (1).
2. a kind of solid of membrane type multi-layer vibration conveying according to claim 1 with fluid heat exchanger it is characterised in that
Described elastic linkage mechanism (3) is articulated with the top of described box frame (2) or to support force way to suspend force way in midair
It is articulated with the lower section of box frame (2).
3. a kind of solid of membrane type multi-layer vibration conveying according to claim 1 with fluid heat exchanger it is characterised in that institute
State internal membrane wall and include membrane wall on inside (9) and internal lower membrane wall (10), membrane wall (9) and internal lower membrane type on inside
Membrane wall is conveyed casing (1) and is separated into upper, middle and lower three material conveying passage by wall (10).
4. a kind of solid of membrane type multi-layer vibration conveying according to claim 3 with fluid heat exchanger it is characterised in that institute
Stating membrane wall on inside (9) is the sieve-like knot only allowing to pass through less than the particle of screen size near one end of charging aperture (24)
Structure, it is horizontal screen or inclined screen.
5. a kind of solid of membrane type multi-layer vibration conveying according to claim 3 with fluid heat exchanger it is characterised in that institute
The arrival end top stating three material conveying passages in membrane wall conveying casing (1) interior upper, middle and lower is respectively equipped with adjustable for height limit
High baffle plate (21,22,23).
6. the solid of a kind of membrane type multi-layer vibration conveying according to any one of claim 3-5 and fluid heat exchanger, it is special
Levy and be, described top membrane wall (7) and bottom membrane wall (11) are two independent tube panels, its one end passes through the first header
(13) connect, the other end passes through the second header (14) and connects；Described right side membrane wall (8) one end is provided with the 3rd header (15),
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
Six headers (18)；On described inside, the heat pipe of membrane wall (9) and internal lower membrane wall (10) is u-shaped structure, membrane type on inside
The flow inlet of wall (9) heat pipe and go out head piece connect respectively in set the shunting section of the 7th header (19) of dividing plate and conflux section, interior
The flow inlet of subordinate's membrane wall (10) heat pipe and go out head piece connect respectively in set dividing plate the shunting section of the 8th header (20) and
Conflux section；Described first header (13) connects the portal metal flexible pipe (27) entering for fluid, and the second header (14) is passed through respectively
Connecting tube (28) connects the 3rd header (15) and the 4th header (16), and the 5th header (17) connects the 7th collection by connecting tube (28)
The shunting section of case (19), the 6th header (18) connects the shunting section of the 8th header (20), the 7th header by connecting tube (28)
(19) and the 8th header (20) section of confluxing common connection outlet metal hose (29).
7. the solid of a kind of membrane type multi-layer vibration conveying according to any one of claim 3-5 and fluid heat exchanger, it is special
Levy and be, described top membrane wall (7) and bottom membrane wall (11) are formed by an overall tube panel bending, and bottom membrane wall (11) is held
Portion is provided with the first header (13), and top membrane wall (7) end is provided with the second header (14)；Right side membrane wall (8) and left side
The heat pipe of membrane wall (12) be u-shaped structure, the flow inlet of right side membrane wall (8) heat pipe and go out head piece connect respectively in set every
The shunting section of the 3rd header (15) of plate and conflux section, the flow inlet of left side membrane wall (12) heat pipe and go out head piece and connect respectively
Inside set the shunting section of the 4th header (16) of dividing plate and section of confluxing；Internal lower membrane wall (10) one end is provided with the 5th header
(17), 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 sets
It is equipped with the 8th header (20)；Described first header (13) connects the portal metal flexible pipe (27) entering for fluid, the second header
(14) connect the shunting section of the 3rd header (15) and the 4th header (16) respectively by connecting tube (28), the 3rd header (15) and the
The section of confluxing of four headers (16) is connected to the 5th header (17) by connecting tube (28), and the 6th header (18) passes through connecting tube (28)
It is connected to the 7th header, the 8th header (20) connection outlet metal hose (29).
8. the solid of a kind of membrane type multi-layer vibration conveying according to any one of claim 1-5 and fluid heat exchanger, it is special
Levy and be, described charging aperture (24) and discharging opening (25) are plane bend pipe membrane wall open-celled structure or space bent pipe membrane wall perforate
Structure.
9. the solid of a kind of membrane type multi-layer vibration conveying according to any one of claim 1-5 and fluid heat exchanger, it is special
Levy and be, described membrane wall conveying casing (1) is additionally provided with steam drain (26).
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| Application Number | Priority Date | Filing Date | Title |
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| CN201510075325.0A CN104654843B (en) | 2015-02-12 | 2015-02-12 | Membrane-type multilayer vibrating transportation solid and fluid heat exchanger |
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| CN201510075325.0A CN104654843B (en) | 2015-02-12 | 2015-02-12 | Membrane-type multilayer vibrating transportation solid and fluid heat exchanger |
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| CN104654843B true CN104654843B (en) | 2017-01-18 |
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| US5056587A (en) * | 1990-09-07 | 1991-10-15 | Halliburton Company | Method for deslagging a boiler |
| 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 |
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2015
- 2015-02-12 CN CN201510075325.0A patent/CN104654843B/en active Active
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| CN104654843A (en) | 2015-05-27 |
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Address after: Floor 1, no.139-20, Tianjiu North Lane, hi tech Zone, Chengdu, Sichuan 610000 Patentee after: Sichuan Longlin Energy Conservation and Environmental Protection Technology Co.,Ltd. Address before: No. 1 and 2, Floor 5, Unit 2, Building 8, No. 46, Shuxi Road, Jinniu Hi tech Industrial Park, Chengdu, Sichuan 610037 Patentee before: SICHUAN LONGLIN KECHUANG ENERGY SAVING AND ENVIRONMENTAL PROTECTION TECHNOLOGY CO.,LTD. |
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