CN109827452A - Low boiling point material condensation recovery heat exchanger - Google Patents
Low boiling point material condensation recovery heat exchanger Download PDFInfo
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- CN109827452A CN109827452A CN201910064898.1A CN201910064898A CN109827452A CN 109827452 A CN109827452 A CN 109827452A CN 201910064898 A CN201910064898 A CN 201910064898A CN 109827452 A CN109827452 A CN 109827452A
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Abstract
The invention relates to a traction bow, in particular to a low-boiling-point material condensation recovery heat exchanger which comprises a fixed underframe, a low-boiling-point material box, a condensation recovery pipe and a flow limiting assembly, wherein when the weight of low-boiling-point liquid in the box body is larger, the flow of a heat absorption liquid pipeline is reduced by the flow limiting assembly, and the heat absorption capacity of the heat absorption liquid is reduced; when the low boiling point liquid in the box body is vaporized and moved into the annular intermediate groove, the weight of the low boiling point liquid in the box body is reduced, the flow limiting assembly automatically increases the flow of the heat absorption liquid pipeline, increases the heat absorption capacity of the heat absorption liquid and automatically controls the flow of the heat absorption liquid pipeline. Low boiling point material case sliding connection is on fixed chassis, and condensation recovery tube fixed connection communicates between condensation recovery tube and the low boiling point material case in the upper end of fixed chassis, and current-limiting component fixed connection is on fixed chassis, and the current-limiting component sets up the one end at the condensation recovery tube.
Description
Technical field
The present invention relates to a kind of traction bows, are in particular a kind of low boiling material condensing recovery heat exchangers.
Background technique
Exactly by steam, cooling condenses into liquid to condensing recovery from gas, the nuisance suitable for recovered steam state
Matter.Especially it is used to recycle mass concentration in the organic solvent vapor of 1000mg/m3 or more.It theoretically can achieve very high
Degree of purification but expense also increases as.Equipment and operating condition needed for condensing recovery are fairly simple, recycle the purity ratio of substance
It is higher, frequently as the pre-treatment of the purification methods such as absorption, burning, load when these methods, such as chlorine industry are used to mitigate
In, common condensation method makes mercuryvapour become liquid mercury and be recycled.Furthermore high humility exhaust gas also keeps water vapour cold with condensation method
It coagulates, greatly reduces gas flow, be conducive to operate in next step.
Summary of the invention
The present invention provides a kind of low boiling material condensing recovery heat exchanger, and its advantages are memory box in the present invention
Low-boiling point liquid weight it is larger when, current limiting component can reduce the flow of heat absorption liquid pipeline, reduce the suction of heat absorption liquid
Heat；When the intracorporal low-boiling point liquid vaporization of case is moved between annular in slot, the intracorporal low-boiling point liquid weight of case reduces, this
When current limiting component increase the flow of heat absorption liquid pipeline automatically, increase the caloric receptivity of heat absorption liquid, automatically control heat absorption liquid pipe
The flow in road.
The present invention relates to a kind of traction bows, are in particular a kind of low boiling material condensing recovery heat exchangers, including
Fixed frame, low boilers hopper are condensed back to closed tube and current limiting component, existing low-boiling point liquid weight in raising middle flask body of the present invention
When larger, current limiting component can reduce the flow of heat absorption liquid pipeline, reduce the caloric receptivity of heat absorption liquid；When the intracorporal low boiling of case
When point liquid vaporization is moved between annular in slot, the intracorporal low-boiling point liquid weight of case reduces, and at this moment current limiting component increases automatically
The flow of heat absorption liquid pipeline increases the caloric receptivity of heat absorption liquid, automatically controls the flow of heat absorption liquid pipeline.
The low boilers hopper is slidably connected in fixed frame, is condensed back to closed tube and is fixedly connected on the upper of fixed frame
End, is condensed back between closed tube and low boilers hopper and is connected to, and current limiting component is fixedly connected in fixed frame, current limiting component setting
In the one end for being condensed back to closed tube.
The fixed frame includes bottom plate, support plate, support column, fixed circular shaft, spring loop bar, condenser pipe support column, limit
Position pin, fixing slide carriage, perpendicular mobile column and sliding cylinder, the upper end of bottom plate are fixedly connected with support plate, and the upper end of support plate is fixed
It is connected with fixing slide carriage, perpendicular mobile column is slidably connected on fixing slide carriage, the lower end of perpendicular mobile column is fixedly connected with sliding cylinder, erects
The upper end of mobile column is fixedly connected with position-limitting pin, and position-limitting pin and sliding cylinder are located at the upper and lower ends of fixing slide carriage, bottom
The rear and front end of plate is fixedly connected to condenser pipe support column, and the upper end of bottom plate is fixedly connected with support column, the upper end of support column
It is fixedly connected with fixed circular shaft, the rear and front end of bottom plate right end is fixedly connected to spring loop bar, covers on two spring loop bars
It is connected to compressed spring in succession.
The low boiling material case includes cabinet, case lid, hot-fluid pipe, hose, sliding side seat, heat-conducting metal, slide opening and thick stick
Bar, the rear and front end of cabinet are fixedly connected to sliding side seat, and two sliding side seats are slidably connected at two spring loop bars respectively
On, the compressed spring on two spring loop bars is respectively positioned on the lower end of corresponding sliding side seat, and the upper end of cabinet is detachably connected
There is case lid, the lower end of cabinet is fixedly connected with heat-conducting metal, and hot-fluid pipe, the front and back two of hot-fluid pipe are fixedly connected on heat-conducting metal
End is fixedly connected to hose, is provided with slide opening on lever, and the right end of lever is hingedly connected to the left end of cabinet, fixed circular shaft and
Sliding cylinder is slidably connected on slide opening, and fixed circular shaft is located at the right end of sliding cylinder.
The closed tube that is condensed back to includes outer cylinder, heat absorption liquid pipeline, reflux bellows, steam bellows, outer sleeve, company
Slot between block, rubber tube, annular slab, inner cylinder and annular is connect, is coaxially disposed between outer cylinder and inner cylinder, outer cylinder and inner cylinder
Left and right ends between be fixedly connected to annular slab, between two annular slabs, outer cylinder and inner cylinders formed annular between slot, ring
The downside middle-end of slot is connected with steam bellows between shape, and the lower end of steam bellows is connected on case lid, and slot passes through steaming between annular
Vapour bellows is communicated with the box body, and the downside right end of outer cylinder is connected with reflux bellows, and the lower end for the bellows that flows back is connected to
The upper end of cabinet, annular between slot also pass through reflux bellows be communicated with the box body, heat absorption liquid pipe is plugged on the inside of inner cylinder
Road, the left end of heat absorption liquid pipeline are connected with rubber tube, and outer sleeve, the front and back two of outer sleeve are fixedly connected on the outside of outer cylinder
End is fixedly connected to link block, and two link blocks are respectively fixedly connected in the upper end of two condenser pipe support columns.
The outer cylinder and inner cylinder right low left high are obliquely installed.
The current limiting component includes fixed clamping column, mobile clamping column, circular orbit bar and L shape connecting rod, before fixing clamping column lower end
Both ends are fixedly connected to circular orbit bar afterwards, and two circular orbit bars are fixedly connected in the upper end of bottom plate, the front and back of mobile clamping column
Both ends are slidably connected at respectively in two mobile clamping columns, and the lower end of L shape connecting rod is fixedly connected on the upper end of perpendicular mobile column, and L shape connects
The upper end of bar is fixedly connected in mobile clamping column, and rubber tube is located between fixed clamping column and mobile clamping column.
A kind of low boiling material condensing recovery heat exchanger of the invention has the beneficial effect that
A kind of low boiling material condensing recovery heat exchanger of the present invention, existing low-boiling point liquid weight in raising middle flask body of the present invention
When measuring larger, current limiting component can reduce the flow of heat absorption liquid pipeline, reduce the caloric receptivity of heat absorption liquid；When case is intracorporal low
When boiling-point liquids vaporization is moved between annular in slot, the intracorporal low-boiling point liquid weight of case reduces, and at this moment current limiting component adds automatically
The flow of big heat absorption liquid pipeline, increases the caloric receptivity of heat absorption liquid, automatically controls the flow of heat absorption liquid pipeline.
Detailed description of the invention
The present invention will be further described in detail with specific implementation method with reference to the accompanying drawing.
Fig. 1 is a kind of overall structure diagram one of low boiling material condensing recovery heat exchanger of the present invention；
Fig. 2 is a kind of overall structure diagram two of low boiling material condensing recovery heat exchanger of the present invention；
Fig. 3 is the structural schematic diagram of fixed frame；
Fig. 4 is the structural schematic diagram one of low boilers hopper；
Fig. 5 is the structural schematic diagram two of low boilers hopper；
Fig. 6 is the structural schematic diagram for being condensed back to closed tube；
Fig. 7 is the half section schematic for being condensed back to closed tube；
Fig. 8 is the structural schematic diagram of current limiting component.
In figure: fixed frame 1；Bottom plate 1-1；Support plate 1-2；Support column 1-3；Fixed circular shaft 1-4；Spring loop bar 1-5；It is cold
Solidifying pipe support column 1-6；Position-limitting pin 1-7；Fixing slide carriage 1-8；Perpendicular mobile column 1-9；Sliding cylinder 1-10；Low boilers hopper 2；Case
Body 2-1；Case lid 2-2；Hot-fluid pipe 2-3；Hose 2-4；Slide side seat 2-5；Heat-conducting metal 2-6；Slide opening 2-7；Lever 2-8；Condensation
Recovery tube 3；Outer cylinder 3-1；Heat absorption liquid pipeline 3-2；Flow back bellows 3-3；Steam bellows 3-4；Outer sleeve 3-5；Connection
Block 3-6；Rubber tube 3-7；Annular slab 3-8；Inner cylinder 3-9；Slot 3-10 between annular；Current limiting component 4；Fixed clamping column 4-1；Mobile folder
Column 4-2；Circular orbit bar 4-3；L shape connecting rod 4-4.
Specific embodiment
In the description of the present invention, it is to be understood that, term " center ", " longitudinal direction ", " transverse direction ", "upper", "lower",
The orientation or positional relationship of the instructions such as "front", "rear", "left", "right", "vertical", "horizontal", "top", "bottom", "inner", "outside" is
It is based on the orientation or positional relationship shown in the drawings, is merely for convenience of description of the present invention and simplification of the description, rather than instruction or dark
Show that signified device or element must have a particular orientation, be constructed and operated in a specific orientation, therefore should not be understood as pair
Limitation of the invention.In addition, term " first ", " second " etc. are used for description purposes only, it is not understood to indicate or imply phase
To importance or implicitly indicate the quantity of indicated technical characteristic.The feature for defining " first ", " second " etc. as a result, can
To explicitly or implicitly include one or more of the features.In the description of the present invention, unless otherwise indicated, " multiple "
It is meant that two or more.
Specific embodiment 1:
Illustrate present embodiment below with reference to Fig. 1-8, the present invention relates to a kind of traction bows, are in particular a kind of low boilings
Point material condensing recovery heat exchanger, including fixed frame 1, low boilers hopper 2, it is condensed back to closed tube 3 and current limiting component 4, this
When existing low-boiling point liquid weight is larger in cabinet 2-1 in invention, current limiting component 4 can be by the flow of heat absorption liquid pipeline 3-2
Reduce, reduces the caloric receptivity of heat absorption liquid；When the low-boiling point liquid vaporization in cabinet 2-1 is moved between annular in slot 3-10,
Low-boiling point liquid weight in cabinet 2-1 reduces, and at this moment current limiting component 4 increases the flow of heat absorption liquid pipeline 3-2 automatically, increases
The caloric receptivity of heat absorption liquid automatically controls the flow of heat absorption liquid pipeline 3-2.
The low boilers hopper 2 is slidably connected in fixed frame 1, is condensed back to closed tube 3 and is fixedly connected on fixed frame 1
Upper end, be condensed back between closed tube 3 and low boilers hopper 2 and be connected to, current limiting component 4 is fixedly connected in fixed frame 1, current limliting
The one end for being condensed back to closed tube 3 is arranged in component 4.
Specific embodiment 2:
Illustrate that present embodiment, the fixed frame 1 include bottom plate 1-1, support plate 1-2, support column below with reference to Fig. 1-8
1-3, fixed circular shaft 1-4, spring loop bar 1-5, condenser pipe support column 1-6, position-limitting pin 1-7, fixing slide carriage 1-8, perpendicular mobile column
1-9 and sliding cylinder 1-10, the upper end of bottom plate 1-1 are fixedly connected with support plate 1-2, and the upper end of support plate 1-2 is fixedly connected with
Determine slide 1-8, perpendicular mobile column 1-9 is slidably connected on fixing slide carriage 1-8, the lower end of perpendicular mobile column 1-9 is fixedly connected with sliding circle
Column 1-10, the upper end of perpendicular mobile column 1-9 are fixedly connected with position-limitting pin 1-7, position-limitting pin 1-7 and sliding cylinder 1-10 and are located at
The upper and lower ends of fixing slide carriage 1-8, the rear and front end of bottom plate 1-1 are fixedly connected to condenser pipe support column 1-6, bottom plate 1-1's
Upper end is fixedly connected with support column 1-3, and the upper end of support column 1-3 is fixedly connected with fixed circular shaft 1-4, before bottom plate 1-1 right end
Both ends are fixedly connected to spring loop bar 1-5 afterwards, and socket is connected with compressed spring on two spring loop bar 1-5.Perpendicular mobile column
1-9 vertical sliding, position-limitting pin 1-7 and sliding cylinder 1-10 can be located at the upper of fixing slide carriage 1-8 on fixing slide carriage 1-8
Lower both ends prevent perpendicular mobile column 1-9 to be detached from fixing slide carriage 1-8.
Specific embodiment 3:
Illustrate present embodiment below with reference to Fig. 1-8, the low boilers hopper 2 includes cabinet 2-1, case lid 2-2, hot-fluid
Pipe 2-3, hose 2-4, sliding side seat 2-5, heat-conducting metal 2-6, slide opening 2-7 and lever 2-8, the rear and front end of cabinet 2-1 are solid
Surely it is connected with sliding side seat 2-5, two sliding side seat 2-5 are slidably connected at respectively on two spring loop bar 1-5, two spring pockets
Compressed spring on bar 1-5 is respectively positioned on the lower end of corresponding sliding side seat 2-5, and the upper end of cabinet 2-1 is removably connected with case
2-2 is covered, the lower end of cabinet 2-1 is fixedly connected with heat-conducting metal 2-6, hot-fluid pipe 2-3 is fixedly connected on heat-conducting metal 2-6, heat
The rear and front end of flow tube 2-3 is fixedly connected to hose 2-4, and slide opening 2-7 is provided on lever 2-8, and the right end of lever 2-8 is hinged
It is connected to the left end of cabinet 2-1, fixed circular shaft 1-4 and sliding cylinder 1-10 are slidably connected on slide opening 2-7, fixed circular shaft 1-4
Positioned at the right end of sliding cylinder 1-10.Two sliding side seat 2-5 respectively can on two spring loop bar 1-5 vertical sliding, two
Compressed spring on spring loop bar 1-5 gives two sliding side seat 2-5 elastic force moved up, so two sliding side seat 2-5
And cabinet 2-1 all has the trend moved up.It is used to place low boiling material in cabinet 2-1, the low boiling in cabinet 2-1
Point material can overcome the elastic force of two compressed springs to press cabinet 2-1 to move down when very much, the low boilers in cabinet 2-1
When material heat absorption vaporization, the upward elastic force of cabinet 2-1 returns to origin-location.Cabinet 2-1 can be driven perpendicular by lever 2-8 when moving down
Mobile column 1-9 upward sliding can drive perpendicular mobile column 1-9 slide downward by lever when cabinet 2-1 is moved up.Hot-fluid pipe 2-
It is used to be passed through exothermic liquid at 3, two hose 2-4 are used to connect the pipeline of exothermic liquid.Two hose 2-4 can be bent,
When low boilers 2 height change of hopper, the pipeline of exothermic liquid need not follow movement.
Specific embodiment 4:
Illustrate present embodiment below with reference to Fig. 1-8, the closed tube 3 that is condensed back to includes outer cylinder 3-1, heat absorption liquid pipeline
3-2, reflux bellows 3-3, steam bellows 3-4, outer sleeve 3-5, link block 3-6, rubber tube 3-7, annular slab 3-8, inner circle
Slot 3-10 between cylinder 3-9 and annular, is coaxially disposed, a left side of outer cylinder 3-1 and inner cylinder 3-9 between outer cylinder 3-1 and inner cylinder 3-9
It is fixedly connected to annular slab 3-8 between right both ends, forms ring between two annular slab 3-8, outer cylinder 3-1 and inner cylinder 3-9
Slot 3-10 between shape, the downside middle-end of slot 3-10 is connected with steam bellows 3-4 between annular, the lower end connection of steam bellows 3-4
On case lid 2-2, slot 3-10 is connected by steam bellows 3-4 with cabinet 2-1 between annular, the downside right end of outer cylinder 3-1
It is connected with reflux bellows 3-3, the lower end of reflux bellows 3-3 is connected to the upper end of cabinet 2-1, and slot 3-10 also passes through between annular
Reflux bellows 3-3 is connected with cabinet 2-1, and heat absorption liquid pipeline 3-2, heat absorption liquid pipe are plugged on the inside of inner cylinder 3-9
The left end of road 3-2 is connected with rubber tube 3-7, and outer sleeve 3-5, the front and back of outer sleeve 3-5 are fixedly connected on the outside of outer cylinder 3-1
Both ends are fixedly connected to link block 3-6, and two link block 3-6 are respectively fixedly connected in the upper of two condenser pipe support column 1-6
End.Entered between annular in slot 3-10 when low boiling material vaporization in cabinet 2-1 by steam bellows 3-4, heat absorption liquid pipe
It is used to pass through the liquid into needs heat absorption at road 3-2, the liquid that the needs in heat absorption liquid pipeline 3-2 absorb heat siphons away heat
Afterwards, it liquefies again into the low boiling material between annular in slot 3-10, cabinet 2-1 is then back to by the bellows 3-3 that flows back
It is interior.The bellows 3-3 and steam bellows 3-4 that flows back is the structure that can be stretched, to adapt to low boilers hopper 2 and cold
The variation of the distance between solidifying recovery tube 3.
Specific embodiment 5:
Illustrate that present embodiment, the outer cylinder 3-1 and inner cylinder 3-9 right low left high are obliquely installed below with reference to Fig. 1-8.
The right end of slot 3-10 between annular is flowed to convenient for liquefied low boiling material again, is then back to from reflux bellows 3-3
In cabinet 2-1.
Specific embodiment 6:
Illustrate present embodiment below with reference to Fig. 1-8, the current limiting component 4 include fixed clamping column 4-1, mobile clamping column 4-2,
Circular orbit bar 4-3 and L shape connecting rod 4-4, the rear and front end of the fixed lower end clamping column 4-1 are fixedly connected to circular orbit bar 4-3, and two
Circular orbit bar 4-3 is fixedly connected in the upper end of bottom plate 1-1, and the rear and front end of mobile clamping column 4-2 is slidably connected at two respectively
On mobile clamping column 4-2, the lower end of L shape connecting rod 4-4 is fixedly connected on the upper end of perpendicular mobile column 1-9, and the upper end of L shape connecting rod 4-4 is solid
Surely it is connected on mobile clamping column 4-2, rubber tube 3-7 is located between fixed clamping column 4-1 and mobile clamping column 4-2.Perpendicular mobile column 1-9 liter
Mobile clamping column 4-2 can be driven to increase or reduce by L shape connecting rod 4-4 when high or reduction, hot-fluid pipe 2-3 thermal discharge is smaller
When, low boiling material vaporization in cabinet 2-1 it is less, at this moment cabinet 2-1 weight is larger, and cabinet 2-1 is moved down, and at this moment erects
Mobile column 1-9 is moved up, and when fixing clamping column 4-1 and mobile clamping column 4-2 Distance Shortened, rubber tube 3-7 is pinched, heat absorption is reduced
The flow of heat absorption liquid in fluid pipeline 3-2 makes hot liquid pipeline 3-2 that must absorb heat and slows；Similarly, hot-fluid pipe 2-3 heat release
When measuring larger, cabinet 2-1 weight saving, cabinet 2-1 is moved up, and is at this moment erected mobile column 1-9 and is moved down, fixed clamping column 4-1
Increase with mobile clamping column 4-2 Distance Shortened, expands the flow of heat absorption liquid in heat absorption liquid pipeline 3-2, make hot liquid pipeline 3-2
The speed that must absorb heat becomes faster.
The working principle of the invention: perpendicular mobile column 1-9 can on fixing slide carriage 1-8 vertical sliding, position-limitting pin 1-7 and
Sliding cylinder 1-10 is located at the upper and lower ends of fixing slide carriage 1-8, and perpendicular mobile column 1-9 is prevented to be detached from fixing slide carriage 1-8.Two cunnings
Dynamic side seat 2-5 vertical sliding, the compressed spring on two spring loop bar 1-5 can give on two spring loop bar 1-5 respectively
Two elastic force for moving up of sliding side seat 2-5, so two sliding side seat 2-5 and cabinet 2-1 all have and move up
Trend.It is used to place low boiling material in cabinet 2-1, two compressions can be overcome when there are many low boiling material in cabinet 2-1
The elastic force of spring presses cabinet 2-1 and moves down, and when the low boiling material in cabinet 2-1 absorbs heat vaporization, cabinet 2-1 upsprings
Power returns to origin-location.Cabinet 2-1 can drive perpendicular mobile column 1-9 upward sliding, cabinet 2-1 when moving down by lever 2-8
Perpendicular mobile column 1-9 slide downward can be driven when moving up by lever.It is used to be passed through exothermic liquid at hot-fluid pipe 2-3, two
A hose 2-4 is used to connect the pipeline of exothermic liquid.Two hose 2-4 can be bent, when low boilers 2 height change of hopper,
The pipeline of exothermic liquid need not follow movement.Ring is entered by steam bellows 3-4 when low boiling material in cabinet 2-1 vaporizes
It is used to pass through the liquid into needs heat absorption, the need in heat absorption liquid pipeline 3-2 between shape in slot 3-10, at heat absorption liquid pipeline 3-2
It after the liquid to be absorbed heat siphons away heat, liquefies again into the low boiling material between annular in slot 3-10, then passes through reflux
Bellows 3-3 is back in cabinet 2-1.The bellows 3-3 and steam bellows 3-4 that flows back is the structure that can be stretched, thus
It has adapted to low boilers hopper 2 and has been condensed back to the variation of the distance between closed tube 3.It is flowed to convenient for liquefied low boiling material again
Then the right end of slot 3-10 between annular is back in cabinet 2-1 from reflux bellows 3-3.Perpendicular mobile column 1-9 is increased or drop
Mobile clamping column 4-2 can be driven to increase or reduce by L shape connecting rod 4-4 when low, when hot-fluid pipe 2-3 thermal discharge is smaller, cabinet
In 2-1 low boiling material vaporization it is less, at this moment cabinet 2-1 weight is larger, and cabinet 2-1 is moved down, at this moment erect mobile column
1-9 is moved up, and when fixing clamping column 4-1 and mobile clamping column 4-2 Distance Shortened, rubber tube 3-7 is pinched, heat absorption liquid pipe is reduced
The flow of heat absorption liquid in road 3-2 makes hot liquid pipeline 3-2 that must absorb heat and slows；Similarly, hot-fluid pipe 2-3 thermal discharge is larger
When, cabinet 2-1 weight saving, cabinet 2-1 is moved up, and it at this moment erects mobile column 1-9 and moves down, fixed clamping column 4-1 and movement
Clamping column 4-2 Distance Shortened increases, and expands the flow of heat absorption liquid in heat absorption liquid pipeline 3-2, makes hot liquid pipeline 3-2 that must absorb heat
Speed becomes faster.
Certainly, above description is not limitation of the present invention, and the present invention is also not limited to the example above, the art
The variations, modifications, additions or substitutions that those of ordinary skill is made within the essential scope of the present invention also belong to guarantor of the invention
Protect range.
Claims (6)
1. a kind of low boiling material condensing recovery heat exchanger, including fixed frame (1), low boilers hopper (2), condensing recovery
Manage (3) and current limiting component (4), it is characterised in that: the low boilers hopper (2) is slidably connected on fixed frame (1), condensation
Recovery tube (3) is fixedly connected on the upper end of fixed frame (1), is condensed back between closed tube (3) and low boilers hopper (2) and is connected to,
Current limiting component (4) is fixedly connected on fixed frame (1), and current limiting component (4) is arranged in the one end for being condensed back to closed tube (3).
2. a kind of low boiling material condensing recovery heat exchanger according to claim 1, it is characterised in that: the fixed bottom
Frame (1) includes bottom plate (1-1), support plate (1-2), support column (1-3), fixed circular shaft (1-4), spring loop bar (1-5), condenser pipe
Support column (1-6), position-limitting pin (1-7), fixing slide carriage (1-8), perpendicular mobile column (1-9) and sliding cylinder (1-10), bottom plate (1-1)
Upper end be fixedly connected with support plate (1-2), the upper end of support plate (1-2) is fixedly connected with fixing slide carriage (1-8), fixing slide carriage
Perpendicular mobile column (1-9) is slidably connected on (1-8), the lower end of perpendicular mobile column (1-9) is fixedly connected with sliding cylinder (1-10), vertical shift
The upper end of dynamic column (1-9) is fixedly connected with position-limitting pin (1-7), and position-limitting pin (1-7) and sliding cylinder (1-10) are located at admittedly
Determine the upper and lower ends of slide (1-8), the rear and front end of bottom plate (1-1) is fixedly connected to condenser pipe support column (1-6), bottom plate
The upper end of (1-1) is fixedly connected with support column (1-3), and the upper end of support column (1-3) is fixedly connected with fixed circular shaft (1-4), bottom
The rear and front end of plate (1-1) right end is fixedly connected to spring loop bar (1-5), socket connection on two spring loop bars (1-5)
There is compressed spring.
3. a kind of low boiling material condensing recovery heat exchanger according to claim 2, it is characterised in that: the low boiling point
Body feed tank (2) includes cabinet (2-1), case lid (2-2), hot-fluid pipe (2-3), hose (2-4), sliding side seat (2-5), heat-conducting metal
(2-6), slide opening (2-7) and lever (2-8), the rear and front end of cabinet (2-1), which is fixedly connected to, slides side seat (2-5), and two
Sliding side seat (2-5) is slidably connected at respectively on two spring loop bars (1-5), the compressed spring on two spring loop bars (1-5)
It is respectively positioned on the lower end of corresponding sliding side seat (2-5), the upper end of cabinet (2-1) is removably connected with case lid (2-2), cabinet
The lower end of (2-1) is fixedly connected with heat-conducting metal (2-6), and hot-fluid pipe (2-3), hot-fluid are fixedly connected on heat-conducting metal (2-6)
The rear and front end of pipe (2-3) is fixedly connected to hose (2-4), is provided on lever (2-8) slide opening (2-7), lever (2-8)
Right end is hingedly connected to the left end of cabinet (2-1), and fixed circular shaft (1-4) and sliding cylinder (1-10) is slidably connected at slide opening (2-
7) on, fixed circular shaft (1-4) is located at the right end of sliding cylinder (1-10).
4. a kind of low boiling material condensing recovery heat exchanger according to claim 3, it is characterised in that: described to be condensed back to
Closed tube (3) includes outer cylinder (3-1), heat absorption liquid pipeline (3-2), reflux bellows (3-3), steam bellows (3-4), outer cylinder
Slot (3-10) between set (3-5), link block (3-6), rubber tube (3-7), annular slab (3-8), inner cylinder (3-9) and annular, outer circle
It is coaxially disposed between cylinder (3-1) and inner cylinder (3-9), it is fixed between outer cylinder (3-1) and the left and right ends of inner cylinder (3-9)
It is connected with annular slab (3-8), forms slot (3- between annular between two annular slabs (3-8), outer cylinder (3-1) and inner cylinder (3-9)
10), the downside middle-end of slot (3-10) is connected with steam bellows (3-4) between annular, and the lower end of steam bellows (3-4) is connected to
On case lid (2-2), slot (3-10) is connected by steam bellows (3-4) with cabinet (2-1) between annular, outer cylinder (3-1)
Downside right end is connected with reflux bellows (3-3), and the lower end of reflux bellows (3-3) is connected to the upper end of cabinet (2-1), annular
Between slot (3-10) also by flow back bellows (3-3) be connected with cabinet (2-1), be plugged with heat absorption on the inside of inner cylinder (3-9)
Fluid pipeline (3-2), the left end of heat absorption liquid pipeline (3-2) are connected with rubber tube (3-7), and the outside of outer cylinder (3-1) is fixed
It is connected with outer sleeve (3-5), the rear and front end of outer sleeve (3-5) is fixedly connected to link block (3-6), two link block (3-
6) it is respectively fixedly connected in the upper end of two condenser pipe support columns (1-6).
5. a kind of low boiling material condensing recovery heat exchanger according to claim 4, it is characterised in that: the outer cylinder
(3-1) and inner cylinder (3-9) right low left high is obliquely installed.
6. a kind of low boiling material condensing recovery heat exchanger according to claim 5, it is characterised in that: the current limliting group
Part (4) includes fixed clamping column (4-1), mobile clamping column (4-2), circular orbit bar (4-3) and L shape connecting rod (4-4), fixed clamping column (4-
1) rear and front end of lower end is fixedly connected to circular orbit bar (4-3), and two circular orbit bars (4-3) are fixedly connected in bottom plate
The rear and front end of the upper end of (1-1), mobile clamping column (4-2) is slidably connected at respectively on two mobile clamping columns (4-2), L shape connecting rod
The lower end of (4-4) is fixedly connected on the upper end of perpendicular mobile column (1-9), and the upper end of L shape connecting rod (4-4) is fixedly connected on mobile clamping column
On (4-2), rubber tube (3-7) is located between fixed clamping column (4-1) and mobile clamping column (4-2).
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Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3598178A (en) * | 1969-05-26 | 1971-08-10 | Gen Electric | Heat pipe |
| US4955361A (en) * | 1986-10-31 | 1990-09-11 | The Furukawa Electric Co., Ltd. | Hot plate |
| CN103471194A (en) * | 2013-09-24 | 2013-12-25 | 中国航天空气动力技术研究院 | Separating type heat pipe heat exchanging system for reducing infrared radiation of high-temperature hole body |
| CN107356142A (en) * | 2017-08-28 | 2017-11-17 | 张洪延 | Self-priming heat transfer unit (HTU) |
| CN107388859A (en) * | 2017-09-07 | 2017-11-24 | 华中科技大学 | Heat exchanger assembly and flow self-regulating heat exchanger |
| CN107462095A (en) * | 2017-08-31 | 2017-12-12 | 南昌大学 | A kind of thermal siphon of variable heat conduction |
| CN107869727A (en) * | 2016-09-27 | 2018-04-03 | 湖南中集竹木业发展有限公司 | A kind of heat exchanger and heat-exchange method |
| CN108027227A (en) * | 2015-07-14 | 2018-05-11 | 香港科技大学 | Passive type thermal diode |
-
2019
- 2019-01-23 CN CN201910064898.1A patent/CN109827452B/en active Active
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3598178A (en) * | 1969-05-26 | 1971-08-10 | Gen Electric | Heat pipe |
| US4955361A (en) * | 1986-10-31 | 1990-09-11 | The Furukawa Electric Co., Ltd. | Hot plate |
| CN103471194A (en) * | 2013-09-24 | 2013-12-25 | 中国航天空气动力技术研究院 | Separating type heat pipe heat exchanging system for reducing infrared radiation of high-temperature hole body |
| CN108027227A (en) * | 2015-07-14 | 2018-05-11 | 香港科技大学 | Passive type thermal diode |
| CN107869727A (en) * | 2016-09-27 | 2018-04-03 | 湖南中集竹木业发展有限公司 | A kind of heat exchanger and heat-exchange method |
| CN107356142A (en) * | 2017-08-28 | 2017-11-17 | 张洪延 | Self-priming heat transfer unit (HTU) |
| CN107462095A (en) * | 2017-08-31 | 2017-12-12 | 南昌大学 | A kind of thermal siphon of variable heat conduction |
| CN107388859A (en) * | 2017-09-07 | 2017-11-24 | 华中科技大学 | Heat exchanger assembly and flow self-regulating heat exchanger |
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| CN109827452B (en) | 2020-05-12 |
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Effective date of registration: 20220510 Address after: 841000 multimodal transport industrial logistics park, Heshuo County, Bayingolin Mongolian Autonomous Prefecture, Xinjiang Uygur Autonomous Region Patentee after: Heshuo Nanhua Chemical Co.,Ltd. Address before: 325024 No. 3, Jianhai Road, Tianhe Town, Longwan District, Wenzhou City, Zhejiang Province Patentee before: Cheng Qinghai |