CN110160377A - Vertical shell-and-tube heat exchanger - Google Patents
Vertical shell-and-tube heat exchanger Download PDFInfo
- Publication number
- CN110160377A CN110160377A CN201910576854.7A CN201910576854A CN110160377A CN 110160377 A CN110160377 A CN 110160377A CN 201910576854 A CN201910576854 A CN 201910576854A CN 110160377 A CN110160377 A CN 110160377A
- Authority
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- China
- Prior art keywords
- tube
- perforated plate
- shell
- heat exchanger
- central tube
- Prior art date
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- Pending
Links
- 238000000034 method Methods 0.000 claims abstract description 19
- 238000007789 sealing Methods 0.000 claims abstract description 11
- 238000009413 insulation Methods 0.000 claims description 14
- 230000008569 process Effects 0.000 claims description 12
- 230000008676 import Effects 0.000 claims description 11
- 238000012546 transfer Methods 0.000 claims description 8
- 239000000758 substrate Substances 0.000 claims description 4
- 230000003628 erosive effect Effects 0.000 claims 1
- 238000012856 packing Methods 0.000 abstract description 6
- 230000000694 effects Effects 0.000 abstract description 4
- 239000000463 material Substances 0.000 description 6
- 239000000126 substance Substances 0.000 description 6
- 239000012530 fluid Substances 0.000 description 5
- 230000006872 improvement Effects 0.000 description 5
- 238000006356 dehydrogenation reaction Methods 0.000 description 3
- 238000011161 development Methods 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 230000008646 thermal stress Effects 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- YNQLUTRBYVCPMQ-UHFFFAOYSA-N Ethylbenzene Chemical compound CCC1=CC=CC=C1 YNQLUTRBYVCPMQ-UHFFFAOYSA-N 0.000 description 2
- 150000004945 aromatic hydrocarbons Chemical class 0.000 description 2
- 238000013461 design Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000007667 floating Methods 0.000 description 2
- 238000005984 hydrogenation reaction Methods 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 239000003921 oil Substances 0.000 description 2
- 238000007670 refining Methods 0.000 description 2
- 230000035939 shock Effects 0.000 description 2
- 230000035882 stress Effects 0.000 description 2
- 229910000851 Alloy steel Inorganic materials 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 150000001336 alkenes Chemical class 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000001833 catalytic reforming Methods 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 239000003337 fertilizer Substances 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000003350 kerosene Substances 0.000 description 1
- 239000010687 lubricating oil Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000003345 natural gas Substances 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 238000010008 shearing Methods 0.000 description 1
- 238000004904 shortening Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
- F28D7/10—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged one within the other, e.g. concentrically
- F28D7/106—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged one within the other, e.g. concentrically consisting of two coaxial conduits or modules of two coaxial conduits
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F9/00—Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
- F28F9/02—Header boxes; End plates
- F28F9/0219—Arrangements for sealing end plates into casing or header box; Header box sub-elements
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F9/00—Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
- F28F9/22—Arrangements for directing heat-exchange media into successive compartments, e.g. arrangements of guide plates
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F9/00—Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
- F28F9/22—Arrangements for directing heat-exchange media into successive compartments, e.g. arrangements of guide plates
- F28F2009/222—Particular guide plates, baffles or deflectors, e.g. having particular orientation relative to an elongated casing or conduit
- F28F2009/224—Longitudinal partitions
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
The present invention relates to a kind of vertical shell-and-tube heat exchangers, including outer housing and the heat exchanger for being built in outer housing；The outer housing includes pressure hull, upper cover and lower head；The heat exchanger includes shell, upper perforated plate, lower perforated plate, tube bank, outer tube, deflector and central tube；The central tube lower end passes through the centre bore of upper cover, upper perforated plate to close to down tube Board position；The outer tube is socketed in central tube outer upper and forms exit passageway between the pipe outer wall of center, and the central tube is connected with upper cover, upper perforated plate sealing respectively by outer tube；The outer sleeve upper tube wall is connected by forming undergauge structure with the sealing of central tube upper end tube wall；Positioned at upper cover outer fix, the outer tube is exported equipped with thermal medium；The lower perforated plate is fixedly linked with shell, is connected between the upper perforated plate and shell by the way that packing box seal structure is arranged；The method can significantly improve the reliabilities of equipment, ensure that the economy of equipment, improve productivity effect.
Description
Technical field
The invention belongs to chemical industry and technical field of petrochemical industry, and it is swollen with sliding tube sheet and inside that the invention proposes one kind
The vertical shell-and-tube heat exchanger of swollen section, especially suitable for heating low temperature process material using high temperature super heated steam, in particular for
In the dehydrogenation reaction technique of aromatic hydrocarbons.
Background technique
In chemical industry and petrochemical industry, heat exchanger using very extensive, be that indispensable common technique is set
It is standby, in daily life and it is seen everywhere.According to statistics, heat exchanger accounts for the 40% of equipment sum in oil refining and chemical plant installations
Left and right, investment account for the 30-45% of gross investment.Recently as the development of power-saving technology, high temperature, Low Temperature Thermal are carried out using heat exchanger
The recycling of energy brings significant economic benefit.Currently, maximum usage amount is shell-and-tube heat exchanger in heat exchange equipment.With
The development of petroleum industry and chemical industry, the shell-and-tube heat exchanger that various harsh conditions use is more and more, such as is refining oil
Be hydrocracked, kerosene hydrogenation, gasoline, diesel add hydrogen and lube oil hydrogenation, catalytic reforming, hydrofinishing etc., the second in chemical industry
Alkene cracking, ethylbenzene dehydrogenation, high-pressure and low-pressure polymerization, ammonia synthesis, natural gas conversion in chemical fertilizer etc., heat exchanger needs to bear pressure
Power is from vacuum to 35MPa, temperature is up to 700 ~ 900 DEG C of harsh use environment.Since the 21th century, with device enlargement
High speed development, the use of large heat exchanger is more and more wide, more and more frequently, technical difficulty is more and more big, reliability of equipment
It is required that higher and higher.How to ensure heat transfer effect, improve the thermal efficiency, improves the reliability of equipment, have become highly important
Research topic, the various large heat exchanger technologies applied under the conditions of special process emerge one after another, too numerous to enumerate.
Most common two kinds of heat exchangers are fixed tube-sheet exchanger and movable tube sheets heat exchanger in shell-and-tube heat exchanger.Such as
Shown in attached drawing 1 and attached drawing 2, since heat exchanger tube pass and shell-side fluid exchange heat, temperature difference is certainly existed, when temperature difference arrives greatly
It, just must be using the engineering measure for eliminating expansion when the temperature stress that can be born more than material.Such as attached drawing 1, in fixed tube sheet
In heat exchanger, since both ends tube sheet is fixed, so expansion joint can only be arranged on shell, when elongation or contracting occur for tube bank
In short-term, it can be compensated by the elongation and shortening of expansion joint, not leaked between tube side and shell side to ensure, guarantee base
This heat transfer effect.If attached drawing 2 does not have expansion joint in movable tube sheets heat exchanger on shell, so tube side one end uses fixing pipe
Plate, the other end (are raised the nose above water to breathe) using sliding tube sheet, and tube bank freely can extend and shorten in shell, but this measure solves
It is the problem of expansion, inevitable by bringing another question, i.e., the Fluid Sealing problem between tube side and shell side.In order to solve
This problem, common method are that, due to using sealing structure, necessarily have leakage, so only using packing box seal structure
It can guarantee that the amount of leakage controls within the scope of acceptable, such as no more than the 5% of total flow.
In these two types of heat exchangers, fixed tube-sheet exchanger and movable tube sheets heat exchanger, usually by dress pattern, there are two types of horizontal
Or it is vertical.Chinese patent CN200820151384.7 discloses a kind of horizontal shell with guided bearing and packing box seal
Formula heat exchanger；Chinese patent CN200710043304.6 discloses a kind of horizontal shell with guided bearing and inner expansion joint
Formula heat exchanger, it is intended to solve above as tube side, shell side thermal stress and expansion issues as caused by the temperature difference.In vertical floating head type
In heat exchanger, stuffing-box is able to maintain good stress, there is certain circumferential uniformity, can guarantee the amount control of leakage
Within the scope of acceptable.When case swells section is arranged in vertical heat exchanger, cutting when the unbearable earthquake of expansion joint occurs
Shear force, and when being designed to bear earthquake shearing power, and the expansion almost lost due to rigidity and intensity.But
Enlargement is that expansion joint is arranged on pressure hull, and reliability and device security are difficult to be guaranteed.
Summary of the invention
In order to overcome drawbacks described above, it is an object of the invention to propose a kind of novel vertical shell-and-tube heat exchanger, lead to
Setting built-in heat exchanger structure is crossed, the leakage of fluid between tube side and shell side is avoided, while guaranteeing that the tube side of heat exchanger can be with
Free expansion, to overcome thermal stress brought by the temperature difference of tube side and shell-side fluid, guarantees the reliability of heat exchanger.
To achieve the goals above, the technical solution of the present invention is as follows:
A kind of vertical shell-and-tube heat exchanger, including outer housing and the heat exchanger for being built in outer housing；The outer housing includes pressure resistance
The upper cover and lower head of shell and pressure hull both ends；The heat exchanger includes shell, be arranged in shell both ends upper perforated plate,
Lower perforated plate, tube bank, deflector and central tube；The upper perforated plate is equipped with centre bore；
The central tube lower end across upper cover, upper perforated plate centre bore to close to down tube Board position and lower perforated plate there are
Flow channels；Central tube upper end import is thermal medium import；
Equipped with outer tube, the outer tube is socketed in central tube outer upper and forms exit passageway between the pipe outer wall of center,
The central tube is connected with upper cover, upper perforated plate sealing respectively by outer tube；The exit passageway lower end is connected to heat transfer zone；
The outer sleeve upper tube wall is connected by forming undergauge structure with the sealing of central tube upper end tube wall；The position on the outside of upper cover
It sets, the outer tube is exported equipped with thermal medium；
The tube bank both ends are each passed through upper perforated plate, lower perforated plate and are fixedly connected respectively with upper perforated plate, lower perforated plate；It is described several to lead
Flowing plate is axially uniformly distributed in the heat transfer zone formed between central tube and shell；
The lower perforated plate is fixedly linked with shell, is connected between the upper perforated plate and shell by the way that packing box seal structure is arranged；
Equipped with cone of support section, the shell lower end is fixedly linked by cone of support section with lower head；Cone of support section lower end is set
There is process stream outlet, the pressure hull is equipped with process stream import.
As a further improvement of the present invention: corresponding upper cover and upper perforated plate section, the outer tube are equipped with expansion joint
Structure.It is further ensured that the tube side of heat exchanger be free to extend and shorten, effectively controls the leakage between shell journey
To a very small extent, guarantee the reliability of heat exchanger.
As a further improvement of the present invention: the reliability in order to further increase lower perforated plate, the lower perforated plate are equipped with
For protecting against shock and heat-insulated baffle.
As a further improvement of the present invention: in order to improve the uniformity of heat exchange and the stability of equipment, the pneumatic shell
Body, shell and central tube coaxial arrangement.
As a further improvement of the present invention: the reliability in order to guarantee central tube, the central tube tube wall inside are equipped with
Bubble top heat insulation barrel.
As a further improvement of the present invention: in order to guarantee bear high temperature shell lower end reliability, combine and set
Standby economy, inner walls end portion setting bubble top heat insulation barrel.
As the preferred embodiment of the present invention: the top heat insulation barrel is combined by bubble top plate, thermal insulation board and substrate.Its
In, it steeps top plate and thermal insulation board bears high temperature, substrate is used for pressure-bearing.
As the preferred embodiment of the present invention: be equipped with support skirt, for outer housing support and with outer housing lower head
It is fixedly connected.
The present invention avoids and expansion joint structure is arranged on pressure hull by the design of built-in heat exchanger；Pass through simultaneously
By design of heat exchanger at a kind of shell-and-tube heat exchanger with sliding tube sheet and inner expansion joint, tube side can be reliably avoided
The leakage of fluid between shell side, while guaranteeing that the tube side of heat exchanger be free to expand, to overcome tube side and shell side stream
Thermal stress brought by the temperature difference of body guarantees the reliability of heat exchanger, low especially suitable for being heated using high temperature super heated steam
Warm process stream.
Detailed description of the invention
Attached drawing 1 is fixed tube-sheet exchanger of the shell with expansion joint in background；
Attached drawing 2 is stuffing box type floating head heat exchanger in background；
Attached drawing 3 is vertical shell-and-tube heat exchanger of the invention.
Attached drawing 4 is packing box seal structural schematic diagram in the present invention.
Attached drawing 5 is bubble top heat insulation barrel structural schematic diagram in the present invention.
Specific embodiment
In order to deepen the understanding of the present invention, the present invention is done below in conjunction with drawings and examples and is further retouched in detail
It states.
Embodiment, as shown in Figure 3: the present embodiment is related to a kind of vertical shell-and-tube heat exchanger, including outer housing and is built in
The heat exchanger of outer housing.Wherein, outer housing includes the upper cover 12 and lower head 13 at pressure hull 11 and pressure hull both ends；It changes
Hot device includes shell 21, is arranged in upper perforated plate 22, the lower perforated plate 23 at shell both ends, tube bank 25, deflector 26, central tube 24, outer
Casing 27 and cone of support section 29；The pressure hull 11, shell 21 and central tube 24 are coaxially disposed.Heat exchanger upper end passes through housing
Pipe 24 is connected with the sealing of the upper cover 12 of outer housing, and the lower end of heat exchanger passes through 13 phase of lower head of cone of support section 29 and outer housing
Even；There are circular passages between pressure hull 11 and heat exchanger shell 21；Upper perforated plate 22 is equipped with centre bore.
As shown in Figure 3: in heat exchanger, 24 lower end of central tube passes through the centre bore of upper cover 12, upper perforated plate 22 under
23 position of tube sheet and there are flow channels between lower perforated plate 23；24 upper end import of central tube is thermal medium import；Outer tube
27 are socketed in 24 outer upper of central tube and form exit passageway between 24 outer wall of central tube, and 27 lower end of outer tube passes through upper envelope
First 12, upper perforated plate 22 and therewith sealing be connected, exit passageway lower end is connected to heat transfer zone.It is as shown in Figure 3: 27 upper pipes of outer tube
Wall is connected by undergauge mode with the sealing of 24 upper end tube wall of central tube；Positioned at 12 outer fix of upper cover, on the outer tube 27
Equipped with thermal medium outlet 271.29 lower end of cone of support section is exported equipped with process stream, and the pressure hull 11 is equipped with technique object
Expect import 111.
As shown in Figure 3: 25 both ends of tube bank are each passed through upper perforated plate 22, lower perforated plate 23 and solid with upper perforated plate, lower perforated plate respectively
Fixed connection.Several axial are uniformly distributed between central tube 24 and shell 21, upper perforated plate 22 and lower perforated plate 23 of deflector 26 are formed
Heat transfer zone in, and mutually stagger, from bottom, first deflector is that material is flowed from center toward radially distant end, second
Piece deflector makes material from radially distant end toward center flow.
As shown in Figure 3 and Figure 4: lower perforated plate 23 is fixedly linked with shell 21, passes through setting between upper perforated plate 22 and shell 21
Close 211 seal structure of stuffing-box is connected.Corresponding upper cover 12 and 22 section of upper perforated plate, outer tube 27 are equipped with 28 structure of expansion joint.
It is as shown in Figure 3 and Figure 5: if thermal medium reaches very high temperature, such as 900 DEG C when, in order to guarantee bear high temperature and
The reliability of equipment, 24 tube wall of central tube inside are equipped with bubble top heat insulation barrel；From bottom, second between deflector and lower perforated plate
Inner walls on setting bubble top heat insulation barrel.Lower perforated plate 23, which is equipped with, is used for protecting against shock and heat-insulated baffle 30,30 realities of baffle
Example is applied to be made of high temperature alloy Steel material.Top heat insulation barrel is combined by bubble top plate 51, thermal insulation board 52 and substrate 53.
As shown in Figure 3: built-in heat exchanger is supported on lower head 23 by cone of support section 29, and entire heat exchanger includes shell
Body 11 is by supporting skirt 3 to be supported on other equipment or ground.
The basic principle of the present embodiment are as follows: the process-stream PS1 of low temperature is entered in pressure hull by process stream import, and
The circular passage being made up of pressure hull and shell is flowed from bottom to top, arrived by pressure hull, upper cover, upper perforated plate and
After the upper tube box that outer tube is constituted, process-stream turns around to flow downward into tube bank heat exchange, by the high temperature heating medium of shell side
After being heated to assigned temperature, into the lower tube box being made of lower perforated plate, cone of support section, left finally by process stream outlet
This equipment.High temperature thermal medium SS1 flows downward after being entered by central tube import, into the shell side of heat exchanger, counts from bottom
It is horizontal from inside to outside to skim over tube bank heat exchange in the first water conservancy diversion spacing that first piece of several deflectors and lower perforated plate are constituted, in pipe
Low temperature process logistics heating, and pass sequentially through second, third, n-th water conservancy diversion plate spacing heat back and forth, until reaching last one
It is from bottom to top flowed after a deflector by the exit passageway that outer tube and central tube are constituted, until being exported by thermal medium
Equipment is flowed out, while thermal medium is cooled to low temperature by high temperature.
In the present embodiment, it is provided with packing box seal structure between shell and upper perforated plate, connects upper cover and upper perforated plate
Outer tube on be provided with expansion joint, both having solved vertical heat exchanger in this way, free wxpansion is asked when high temperature difference between shell journey
Topic, also avoids that expansion joint is arranged on heat exchanger pressure hull, it is ensured that the reliability and safety of equipment.
The present embodiment especially suitable between low temperature process material and high temperature thermal medium heat exchange and other leakage shadows
Ring serious occasion.The reliability of equipment is significantly improved, the economy of equipment is ensure that, improves productivity effect.It is especially suitable
It shares in the dehydrogenation reaction technique of aromatic hydrocarbons.
The above is only used to illustrate the technical scheme of the present invention and not limits, and those of ordinary skill in the art are to this
The other modifications or equivalent replacement that the technical solution of invention is made, without departing from the spirit and scope of the technical program,
It is intended to be within the scope of the claims of the invention.
Claims (8)
1. a kind of vertical shell-and-tube heat exchanger, it is characterised in that: including outer housing and the heat exchanger for being built in outer housing；It is described outer
Shell includes the upper cover and lower head at pressure hull and pressure hull both ends；The heat exchanger includes shell, is arranged in shell
Upper perforated plate, the lower perforated plate at both ends, tube bank, deflector and central tube；The upper perforated plate is equipped with centre bore；The central tube lower end
Across upper cover, upper perforated plate centre bore to close to down tube Board position and there are flow channels lower perforated plate；The center
The import of pipe upper end is thermal medium import；Equipped with outer tube, the outer tube is socketed in central tube outer upper and and central tube
Exit passageway is formed between outer wall, the central tube is connected with upper cover, upper perforated plate sealing respectively by outer tube；The outlet
Channel lower end is connected to heat transfer zone；The outer sleeve upper tube wall seals phase with central tube upper end tube wall by forming undergauge structure
Even；Positioned at upper cover outer fix, the outer tube is exported equipped with thermal medium；The tube bank both ends are each passed through upper tube
It plate, lower perforated plate and is fixedly connected respectively with upper perforated plate, lower perforated plate；Several deflectors are axially uniformly distributed in central tube and shell
In the heat transfer zone formed between body；The lower perforated plate is fixedly linked with shell, is filled out between the upper perforated plate and shell by setting
Expect that letter sealing structure is connected；Equipped with cone of support section, the shell lower end is fixedly linked by cone of support section with lower head；The branch
Support cone section lower end is exported equipped with process stream, and the pressure hull is equipped with process stream import.
2. vertical shell-and-tube heat exchanger according to claim 1, it is characterised in that: corresponding upper cover and upper perforated plate section,
The outer tube is equipped with expansion joint structure.
3. vertical shell-and-tube heat exchanger according to claim 1, it is characterised in that: the lower perforated plate, which is equipped with, is used for erosion control
It hits and heat-insulated baffle.
4. vertical shell-and-tube heat exchanger according to claim 1 or 2, it is characterised in that: the pressure hull, shell and in
The coaxial arrangement of heart pipe.
5. vertical shell-and-tube heat exchanger according to claim 1, it is characterised in that: be equipped with bubble on the inside of the central tube tube wall
Push up heat insulation barrel.
6. vertical shell-and-tube heat exchanger according to claim 1, it is characterised in that: the inner walls end portion setting
Bubble top heat insulation barrel.
7. vertical shell-and-tube heat exchanger according to claim 5 or 6, it is characterised in that: the top heat insulation barrel by bubble top plate,
Thermal insulation board and substrate are combined.
8. vertical shell-and-tube heat exchanger according to claim 1, it is characterised in that: be equipped with support skirt, be used for outer housing
Support and be fixedly connected with outer housing lower head.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910576854.7A CN110160377A (en) | 2019-06-28 | 2019-06-28 | Vertical shell-and-tube heat exchanger |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910576854.7A CN110160377A (en) | 2019-06-28 | 2019-06-28 | Vertical shell-and-tube heat exchanger |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN110160377A true CN110160377A (en) | 2019-08-23 |
Family
ID=67637426
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201910576854.7A Pending CN110160377A (en) | 2019-06-28 | 2019-06-28 | Vertical shell-and-tube heat exchanger |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN110160377A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112902710A (en) * | 2021-01-27 | 2021-06-04 | 上海蓝滨石化设备有限责任公司 | Cold wall jacket type high-temperature gas-gas heat exchanger |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB1340123A (en) * | 1970-02-04 | 1973-12-12 | Foster Wheeler Corp | Liquid metal heat exchanger |
| CN2903882Y (en) * | 2006-04-11 | 2007-05-23 | 刘金成 | Shell-and-tube heat exchanger |
| CN201251387Y (en) * | 2008-07-29 | 2009-06-03 | 徐志刚 | Shell-and-tube heat exchanger with sliding guided support and stuffing box |
| CN105091634A (en) * | 2014-05-21 | 2015-11-25 | 航天长征化学工程股份有限公司 | Baffle rod type heat exchanger with built-in expansion joint |
| CN210441706U (en) * | 2019-06-28 | 2020-05-01 | 常州瑞凯化工装备有限公司 | Vertical shell-and-tube heat exchanger |
-
2019
- 2019-06-28 CN CN201910576854.7A patent/CN110160377A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB1340123A (en) * | 1970-02-04 | 1973-12-12 | Foster Wheeler Corp | Liquid metal heat exchanger |
| CN2903882Y (en) * | 2006-04-11 | 2007-05-23 | 刘金成 | Shell-and-tube heat exchanger |
| CN201251387Y (en) * | 2008-07-29 | 2009-06-03 | 徐志刚 | Shell-and-tube heat exchanger with sliding guided support and stuffing box |
| CN105091634A (en) * | 2014-05-21 | 2015-11-25 | 航天长征化学工程股份有限公司 | Baffle rod type heat exchanger with built-in expansion joint |
| CN210441706U (en) * | 2019-06-28 | 2020-05-01 | 常州瑞凯化工装备有限公司 | Vertical shell-and-tube heat exchanger |
Non-Patent Citations (1)
| Title |
|---|
| 中国石化北京设计院编, 北京：中国石化出版社: "《石油炼厂设备》", 30 June 2001, pages: 224 * |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112902710A (en) * | 2021-01-27 | 2021-06-04 | 上海蓝滨石化设备有限责任公司 | Cold wall jacket type high-temperature gas-gas heat exchanger |
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