CN104949549A - External heat remover - Google Patents
External heat remover Download PDFInfo
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- CN104949549A CN104949549A CN201510320773.2A CN201510320773A CN104949549A CN 104949549 A CN104949549 A CN 104949549A CN 201510320773 A CN201510320773 A CN 201510320773A CN 104949549 A CN104949549 A CN 104949549A
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Abstract
The invention provides an external heat remover. The external heat remover is characterized by comprising a water or heat removing medium entering unit, a gas-water or heat removing medium discharging unit, a heat removing unit, a pipe plate, a water or heat removing medium entering pipe and a gas-water or heat removing medium heat exchanging casing pipe and the like. Partitions are arranged inside the water or heat removing medium entering unit and the gas-water or heat removing medium discharging unit, and correspond to an external water or heat removing medium inlet and a gas-water or heat removing medium outlet in a one-to-one mode. The heat removing unit is provided with a catalyst inlet, a fluidifying gas inlet and a sparger and the like. A catalyst carrying gas replacement unit can be arranged below a heat exchanging pipe. The problems that in an existing external heat remover, a heat exchanging pipe bundle is inconvenient to maintain and replace, the usage amount of a pipeline and a valve is large, and the operability is not high are solved.
Description
Technical field
The present invention relates to a kind of external warmer of technical field of heat exchange, be applicable to solid particle cooling heat transferring, be specially adapted to the external warmer taking out gas-solid fluidized bed superfluous heat in gas-solid fluidized bed course of reaction.
Background technology
In the exothermal reaction process such as catalytic cracked regenerated, fluid bed methanol-to-olefins, fluid bed Methanol aromatic hydrocarbons, need to take out partial heat or cool heat-obtaining to solid particles such as catalyst.Usual employing heat collector absorbs this part heat, ensures steadily carrying out of technological operation.Meanwhile, heat collector also utilizes this part superfluous heat generation steam or heats other media, becomes an important conservation measures in device.External warmer is because heat-obtaining amount is large, it is nimble to operate, and application is industrially very extensive.
Existing external warmer has multiple pattern, and domestic widely used a kind of heat exchanger tube external warmer, comprises a vertically disposed cylindrical shell, be vertically installed with many sleeve-type heat exchanging pipes in housing.Each root heat exchanger tube is enclosed construction, mainly contains water inlet pipe and steam water interface sleeve pipe composition.Every root heat exchanger tube is an independently heat transfer element, forms the heat exchange unit that has independently water-vapour loop.Need between these heat exchanger tube with steam traps to be connected with pipeline.An external warmer needs to arrange a large amount of heat exchanger tubes, also just needs a large amount of pipeline valve between external warmer and steam trap.Both added investment, heat also can run off, the external warmer that especially heat-obtaining amount is large, tube bank is many, will account for a large amount of spaces and arrange.
Reduce investment to simplify systematic pipeline, prior art, often the tube plate structure that heat exchange tube design becomes heat exchanger often to adopt, now only needs a pipeline between external warmer and steam trap.But because solid particle heat transfer intensity is high, non-uniform temperature, catalyst abrasion etc., heat exchanger tube is the parts the most easily occurring in heat exchanging process damaging.When water inlet pipe and steam water interface sleeve pipe, any one goes wrong, conventional tube-sheet type structure just causes whole equipment to come into operation.
Summary of the invention
The object of this invention is to provide a kind of external warmer, both retained the advantage of tube-sheet type design, can divide into groups again to control, even if occur that damage is restrained in local, also only impact local tube bank, external warmer still can use.
For solving the problem, the technical solution used in the present invention is:
A kind of external warmer, heat-obtaining unit is set in its underpart, the fluidizing gas inlet port that this unit is arranged by lower house, catalyst inlet port, low head and lower house bottom and distributor, the inner carbonated drink that arranges or heat-obtaining medium (also claiming heated medium) heat exchange sleeve, fixed guide are configured to; Carbonated drink or heat-obtaining medium outlet unit are set on heat-obtaining unit top, this unit is by the carbonated drink that upper shell and upper shell are arranged or heat-obtaining media outlet, and the water of inner setting or heat-obtaining medium enter pipe, carbonated drink or heat-obtaining media for heat exchange sleeve pipe tube sheet or claim lower perforated plate, heat-obtaining medium flow out subregion dividing plate or are called that lower clapboard is formed; Carbonated drink or heat-obtaining medium outlet unit top arranges water or heat-obtaining medium enters unit, the water that this unit is arranged by upper cover and upper cover top or sidepiece or heat-obtaining medium inlet, the inner water that arranges or heat-obtaining medium enter pipe, water or heat-obtaining medium and enter pipe tube sheet or deserve to be called tube sheet, water or heat-obtaining medium and enter subregion dividing plate or deserve to be called dividing plate formation.
Specifically, be that two tube sheets are set in the middle and upper part of existing external warmer, container be divided into three unit: top is that water or heat-obtaining medium enter unit, and middle part is carbonated drink or heat-obtaining medium outlet unit, and bottom is heat-obtaining unit.
Upper perforated plate to upper cover is that water or heat-obtaining medium enter unit, the upper cover inside entering unit at water or heat-obtaining medium arranges multiple upper spacer, water or heat-obtaining medium are entered unit and is divided into multiple district, at upper cover center, upper spacer fixed bar is set, upper spacer welds with upper spacer fixed bar, arrange multiple water or heat-obtaining medium inlet at upper cover top or sidepiece, water or the heat-obtaining medium inlet orientation between every two upper spacers, with each district one_to_one corresponding.So just be equivalent to multiple upper spacer water or heat-obtaining medium are entered water in unit or heat-obtaining medium and enter pipe and be divided into many groups, the often corresponding water of group or heat-obtaining medium inlet.
Be carbonated drink or heat-obtaining medium outlet unit between upper perforated plate and lower perforated plate, in the upper shell inside of carbonated drink or heat-obtaining medium outlet unit, the lower clapboard entering the quantity such as unit with water or heat-obtaining medium is set, carbonated drink or heat-obtaining medium outlet unit are divided into multiple district, at the center of upper lower perforated plate, lower clapboard fixed bar is set, lower clapboard welds with lower clapboard fixed bar, upper shell arranges multiple carbonated drink or heat-obtaining media outlet, carbonated drink or the orientation of heat-obtaining media outlet between every two lower clapboards, with each district one_to_one corresponding.So just be equivalent to multiple lower clapboard and carbonated drink or heat-obtaining medium outlet unit are divided into many groups, often the corresponding carbonated drink of group or heat-obtaining media outlet.Multiple district that carbonated drink or heat-obtaining medium outlet unit are divided into and water or heat-obtaining medium enter the upper and lower one_to_one corresponding in multiple districts that unit is divided into, and namely upper spacer is consistent with the orientation of lower clapboard, arranges branched heat exchanger tube in each district.
Be heat-obtaining unit below lower perforated plate, arrange the tube bank of some heat-obtainings in heat-obtaining unit housings, heat-obtaining tube bank is inner-outer sleeve tubular type, and outer tube is carbonated drink or heat-obtaining media for heat exchange sleeve pipe, and upper end is fixed on lower perforated plate; Interior Guan Weishui or heat-obtaining medium enter pipe, and upper end is fixed on upper perforated plate from heat-obtaining unit through after carbonated drink or heat-obtaining medium outlet unit.A catalyst inlet port is set on heat-obtaining unit top, bottom arranges fluidizing gas inlet port and distributor.Water or heat-obtaining medium enter unit and carbonated drink or heat-obtaining medium outlet unit and are separated by upper perforated plate, and carbonated drink or heat-obtaining medium outlet unit and heat-obtaining unit are separated by lower perforated plate, and are all set to detachable structure between each unit and tube sheet, optimum seeking method flange connection structure.
Catalyst is set in heat-obtaining unit bottom and carries gas displacement unit, in this permute unit housing, gas displacement element is set, replacement media entrance and replacement media distributor are set between gas displacement element and catalyst outlet.
Concrete scheme is: upper perforated plate arranges that the water of some or heat-obtaining medium enter pipe, lower perforated plate arranges carbonated drink or the heat-obtaining media for heat exchange sleeve pipe of some, water or heat-obtaining medium enter pipe with carbonated drink or heat-obtaining media for heat exchange sleeve pipe arrange quantity and orientation consistent, after upper lower perforated plate is installed by orientation, water or heat-obtaining medium enter pipe and put in carbonated drink or heat-obtaining media for heat exchange sleeve pipe, form the heat exchange unit of independent heat-obtaining medium loop one by one, carbonated drink or heat-obtaining media for heat exchange sleeve pipe then stretch to the heat-obtaining unit of bottom, heat exchange is carried out to catalyst, material is thus formed the divided into groups control formula heat exchanger tube of some.The catalyst of waste heat is had to enter the heat-obtaining unit of bottom by catalyst inlet port in regenerator or reactor; Simultaneously, 2 ~ 10 water that heat-obtaining medium is arranged by upper cover top or heat-obtaining medium inlet enter water or heat-obtaining medium enters in 2 ~ 10 inner corresponding subregions of unit, the water or the heat-obtaining medium that flow into upper perforated plate layout enter in pipe, then, in the carbonated drink entering bottom heat-obtaining unit or heat-obtaining media for heat exchange sleeve pipe, heat exchange is carried out with the catalyst of the waste heat entered by catalyst inlet port; After heat exchange, heat-obtaining medium enters in the carbonated drink at middle part or heat-obtaining medium outlet unit in corresponding 2 ~ 10 subregions, then is drawn by carbonated drink corresponding to each subregion or heat-obtaining media outlet.Like this, when the tube bank that certain is organized is broken down or machine utilization changes, only need close the heat exchanger tube of this group, equipment still can normally run, and is convenient to switch, workable.The cooling degree of fluidizing gas inlet port and the adjustable catalyst of distributor.
Can arrange solid particle outlet in heat-obtaining unit bottom, from then on cooled catalyst exports outflow.
Arrange catalyst and carry gas displacement unit below heat-obtaining unit heat exchanger tube and between solid particle outlet, inside arranges gas displacement element, and gas displacement element can be grid or veneer, arranges replacement media distributor below gas displacement element.
Invention effect
External warmer of the present invention compared with prior art, has following beneficial effect:
1, equipment self realizes heat exchanger tube grouping, and each group can independent operating, and having does not affect other groups heat exchange when heat exchanger tube damages use.
2, a large amount of steam inlet/outlet pipeline of existing external warmer and valve can be removed from, reduce steel waste, save space and arrange, reduce heat losses, improve income.
3, heat-obtaining media units respectively arranges but is not limited to 2 ~ 10 subregions, tube bank is divided into but is not limited to 2 ~ 10 groups, is convenient to switch, workable.
4, can prevent cooled catalyst from carrying oxygen or flue gas or other reaction mediums.
Accompanying drawing explanation
Fig. 1-Fig. 7 is external warmer structure, particularly:
Fig. 1 external warmer structural representation.
A-A sectional view in Fig. 2 Fig. 1.
B-B sectional view in Fig. 3 Fig. 1.
Fig. 4 carbonated drink or heat-obtaining media for heat exchange sleeve structure schematic diagram.
A kind of structure of C-C sectional view in Fig. 5 Fig. 4.
The another kind of structure of C-C sectional view in Fig. 6 Fig. 4.
Fig. 7 arranges the external warmer that catalyst carries gas displacement unit.
In figure: 1, water or heat-obtaining medium enter unit, 2, carbonated drink or heat-obtaining medium outlet unit, 3, heat-obtaining unit, 4, upper perforated plate, 5, lower perforated plate, 6, water or heat-obtaining medium enter pipe, 7, carbonated drink or heat-obtaining media for heat exchange sleeve pipe, 8, fixed guide frame, 11, upper cover, 12, water or heat-obtaining medium inlet, 13, upper spacer fixed bar, 14, upper spacer, 21, upper shell, 22, carbonated drink or heat-obtaining media outlet, 23, leakage fluid dram, 24, lower clapboard fixed bar, 25, lower clapboard, 31, lower house, 32, catalyst inlet port, 33, low head, 34, fluidizing gas inlet port, 35, distributor, 36, solid particle or catalyst outlet, 37, gas displacement element, 38, replacement media entrance, 39, replacement media distributor, 71, light pipe, 72, finned tube.
Detailed description of the invention
Below in conjunction with the drawings and specific embodiments, the present invention is further detailed explanation, is intended to help reader understanding's feature of the present invention and essence, but the drawings and specific embodiments content do not limit of the present invention can practical range.
As shown in Figure 1, a kind of invention external warmer, it comprises heat-obtaining unit 3, the fluidizing gas inlet port 34 that this unit is arranged by lower house 31, catalyst inlet port 32, low head 33 and lower house 31 bottom and distributor 35, the inner carbonated drink that arranges or heat-obtaining media for heat exchange sleeve pipe 7, fixed guide frame 8 are formed; It also comprises the carbonated drink or heat-obtaining medium outlet unit 2 that are positioned at heat-obtaining unit 3 top, this unit is by the carbonated drink that upper shell 21 and upper shell 21 are arranged or heat-obtaining media outlet 22, and the water of inner setting or heat-obtaining medium enter pipe 6, carbonated drink or heat-obtaining media for heat exchange sleeve pipe tube sheet or claim lower perforated plate 5, heat-obtaining medium flow out subregion dividing plate or are called that lower clapboard 25 is formed; And also comprise the water that is positioned at carbonated drink or heat-obtaining medium outlet unit 2 top or heat-obtaining medium enters unit 1, the water that this unit is arranged by upper cover 11 and upper cover 11 top or heat-obtaining medium inlet 12, the inner water that arranges or heat-obtaining medium enter pipe 6, water or heat-obtaining medium and enter pipe tube sheet or deserve to be called tube sheet 4, water or heat-obtaining medium and enter subregion dividing plate or deserve to be called dividing plate 14 and form.
Water or heat-obtaining medium enter unit 1 and carbonated drink or heat-obtaining medium outlet unit 2 and are separated by upper perforated plate 4, carbonated drink or heat-obtaining medium outlet unit 2 and heat-obtaining unit 3 are separated by lower perforated plate 5, and be all set to detachable structure between each unit and tube sheet, optimum seeking method flange connection structure.Upper perforated plate 4 arranges that the water of some or heat-obtaining medium enter pipe 6, lower perforated plate 5 arranges carbonated drink or the heat-obtaining media for heat exchange sleeve pipe 7 of some, water or heat-obtaining medium enter pipe 6 and carbonated drink or heat-obtaining media for heat exchange sleeve pipe 7 arrange quantity and orientation consistent, after upper lower perforated plate is installed by orientation, water or heat-obtaining medium enter pipe 6 and put in carbonated drink or heat-obtaining media for heat exchange sleeve pipe 7, form the heat exchange unit of independent heat-obtaining medium loop one by one, carbonated drink or heat-obtaining media for heat exchange sleeve pipe 7 stretch to the heat-obtaining unit 3 of bottom, heat exchange is carried out to catalyst, material is thus formed the divided into groups control formula heat exchanger tube of some.
As shown in Figure 2, upper cover 11 inside entering unit 1 at water or heat-obtaining medium arranges 4 upper spacers 14, water or heat-obtaining medium are entered unit 1 be divided into but be not limited to 4 districts, at upper cover 11 center, upper spacer fixed bar 13 is set, upper spacer 14 welds with upper spacer fixed bar 13, arrange 4 water or heat-obtaining medium inlet 12 at upper cover 11 top, water or heat-obtaining medium inlet 12 orientation between every two upper spacers 14, with each district one_to_one corresponding.So just be equivalent to multiple upper spacer 14 water or heat-obtaining medium are entered water in unit 1 or heat-obtaining medium and enter pipe 6 and be divided into 4 groups, the often corresponding water of group or heat-obtaining medium inlet 12.In practical application according to equipment different with heat-obtaining amount need determine dividing plate 25 quantity, be not limited to the quantity of this figure.
As shown in Figure 3, in upper shell 21 inside of carbonated drink or heat-obtaining medium outlet unit 2, the lower clapboard 25 entering the quantity such as unit 1 with water or heat-obtaining medium is set, carbonated drink or heat-obtaining medium outlet unit 2 are divided into 4 districts, at the center of upper lower perforated plate, lower clapboard fixed bar 24 is set, lower clapboard 25 welds with lower clapboard fixed bar 24, upper shell 21 arranges 4 carbonated drinks or heat-obtaining media outlet 22, and carbonated drink or the orientation of heat-obtaining media outlet 22 between every two lower clapboards 25, with each district one_to_one corresponding.So just be equivalent to 4 lower clapboards 25 and carbonated drink or heat-obtaining medium outlet unit 2 are divided into 4 groups, often the corresponding carbonated drink of group or heat-obtaining media outlet 22.4 districts that carbonated drink or heat-obtaining medium outlet unit 2 are divided into and water or heat-obtaining medium enter 4 upper and lower one_to_one corresponding in district that unit 1 is divided into, and namely upper spacer 14 is consistent with the orientation of lower clapboard 25, arranges branched heat exchanger tube in each district.In practical application according to equipment different with heat-obtaining amount need determine dividing plate 25 quantity, be not limited to the quantity of this figure.
The catalyst of waste heat is had to enter the heat-obtaining unit 3 of bottom by catalyst inlet port 32 in regenerator or reactor; Simultaneously, heat-obtaining medium by upper cover 11 top arrange but be not limited to 2 ~ 10 water or heat-obtaining medium inlet 12 and enter water or heat-obtaining medium and enter in the corresponding subregion that the inner upper spacer of unit 1 14 is divided into, the water or the heat-obtaining medium that flow into upper perforated plate 4 layout enter in pipe 6, then, in the carbonated drink entering bottom heat-obtaining unit 3 or heat-obtaining media for heat exchange sleeve pipe 7, heat exchange is carried out by heat exchange sleeve 7 and the catalyst of the waste heat entered by catalyst inlet port 32; After heat exchange, heat-obtaining medium enters in the carbonated drink at middle part or heat-obtaining medium outlet unit 2 in the corresponding subregion that is divided into of lower clapboard 25, then is drawn by carbonated drink corresponding to each subregion or heat-obtaining media outlet 22.Like this, when the tube bank of certain group break down or equipment meet change time, only need close the heat exchanger tube of this group, equipment still can normally run, and is convenient to switching, workable.The cooling degree of fluidizing gas inlet port 34 and the adjustable catalyst of distributor 35.
As shown in Figure 7, can arrange solid particle outlet 36 in heat-obtaining unit 3 bottom, from then on cooled catalyst exports outflow.
As shown in Figure 4,5, 6, a kind of carbonated drink of invention external warmer or heat-obtaining media for heat exchange sleeve pipe 7, can be set to light pipe 71, also can be set to finned tube 72, specifically determined by apparatus arrangement and heat-obtaining amount.
As shown in Figure 7, a kind of external warmer, arrange gas displacement element 37 in heat-obtaining unit 3 bottom, gas displacement element 37 has function of steam stripping, for displacing the gas that catalyst carries, replacement media entrance 38 and replacement media distributor 39 are set in gas displacement element 37 bottom.
External warmer of the present invention, is mainly used in the catalytic cracking unit of PETROLEUM PROCESSING industry, and the fluid bed gas-solid reaction device similar with its technical process, such as MTO(preparing olefin by conversion of methanol) device, fluid bed MTA device; Also can be applicable to other heat trnasfer place with requirement of similarity.
Heat-obtaining medium of the present invention can be gas, can be also liquid, as reaction raw materials.
Claims (9)
1. an external warmer, it comprises heat-obtaining unit (3), the fluidizing gas inlet port (34) that this unit is arranged by lower house (31), solid particle or catalyst inlet port (32), low head (33) and lower house (31) bottom and distributor (35), the carbonated drink of inner setting or heat-obtaining media for heat exchange sleeve pipe (7), fixed guide frame (8) formation; It also comprises the carbonated drink or heat-obtaining medium outlet unit (2) that are positioned at heat-obtaining unit (3) top, the carbonated drink that this unit is above arranged by upper shell (21) and upper shell (21) or heat-obtaining media outlet (22), the water of inner setting or heat-obtaining medium enter pipe (6), carbonated drink or heat-obtaining media for heat exchange sleeve pipe tube sheet or claim lower perforated plate (5), heat-obtaining medium outflow subregion dividing plate or be called that lower clapboard (25) is formed; And also comprise the water that is positioned at carbonated drink or heat-obtaining medium outlet unit (2) top or heat-obtaining medium enters unit (1), the water that this unit is arranged by upper cover (11) and upper cover (11) top or sidepiece or heat-obtaining medium inlet (12), the inner water that arranges or heat-obtaining medium enter pipe (6), water or heat-obtaining medium and enter pipe tube sheet or deserve to be called tube sheet (4), water or heat-obtaining medium and enter subregion dividing plate or deserve to be called dividing plate (14) formation.
2. external warmer as claimed in claim 1, it is characterized in that, upper cover (11) inside entering unit (1) at water or heat-obtaining medium arranges upper spacer (14), water or heat-obtaining medium is entered unit (1) and is divided into multiple district; Arrange on upper cover (11) top and be divided into the identical water of district's number or heat-obtaining medium inlet (12) by upper spacer, water or heat-obtaining medium inlet (12) are positioned at the orientation between every two upper spacers (14), with each district one_to_one corresponding; Lower clapboard (25) is set in upper shell (21) inside of carbonated drink or heat-obtaining medium outlet unit (2), carbonated drink or heat-obtaining medium outlet unit (2) are divided into multiple district; At the multiple carbonated drink of upper shell (21) outer setting or heat-obtaining media outlet (22), carbonated drink or heat-obtaining media outlet (22) are positioned at the orientation between every two lower clapboards (25), with each district one_to_one corresponding; The Qu Yushui that carbonated drink or heat-obtaining medium outlet unit (2) are divided into or heat-obtaining medium enter the upper and lower one_to_one corresponding in district that unit (1) is divided into, and namely upper spacer (14) is consistent with the orientation of lower clapboard (25).
3. external warmer as claimed in claim 1, it is characterized in that, water or heat-obtaining medium enter unit (1) and carbonated drink or heat-obtaining medium outlet unit (2) and are separated by upper perforated plate (4), carbonated drink or heat-obtaining medium outlet unit (2) and heat-obtaining unit (3) are separated by lower perforated plate (5), and be all set to detachable between each unit and tube sheet, preferred flange method.
4. the external warmer as described in claim 1 or 3, it is characterized in that, upper perforated plate (4) arranges the water of some or heat-obtaining medium enters pipe (6), lower perforated plate (5) arranges carbonated drink or the heat-obtaining media for heat exchange sleeve pipe (7) of some, and it is all consistent that water or heat-obtaining medium enter pipe (6) and carbonated drink or heat-obtaining media for heat exchange sleeve pipe (7) magnitude setting and orientation; After upper lower perforated plate is installed by orientation, water or heat-obtaining medium enter pipe (6) and put in carbonated drink or heat-obtaining media for heat exchange sleeve pipe (7), form the heat exchange unit of independent heat-obtaining medium loop one by one, carbonated drink or heat-obtaining media for heat exchange sleeve pipe (7) then stretch to the heat-obtaining unit (3) of bottom, carry out heat exchange to catalyst.
5. external warmer as claimed in claim 1 or 2, it is characterized in that, upper cover (11) center entering unit (1) at water or heat-obtaining medium arranges upper spacer fixed bar (13), and upper spacer (14) welds with upper spacer fixed bar (13); Arrange lower clapboard fixed bar (24) at upper shell (21) center of carbonated drink or heat-obtaining medium outlet unit (2), lower clapboard (25) welds with lower clapboard fixed bar (24).
6. the external warmer as described in claim 1 or 4, is characterized in that, carbonated drink or heat-obtaining media for heat exchange sleeve pipe (7) can be set to light pipe (71), also can be set to finned tube (72).
7. external warmer as claimed in claim 1, it is characterized in that, can arrange solid particle or catalyst outlet (36) in heat-obtaining unit (3) bottom, from then on cooled catalyst exports outflow.
8. the external warmer as described in claim 1 or 7, is characterized in that, arranges gas displacement element (37) in heat-obtaining unit (3) bottom, arranges replacement media entrance (38) and replacement media distributor (39) in gas displacement element (37) bottom.
9. external warmer as claimed in claim 1 or 2, it is characterized in that, upper spacer and lower clapboard can be designed as flat board or arc respectively.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510320773.2A CN104949549B (en) | 2015-06-12 | 2015-06-12 | A kind of external warmer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510320773.2A CN104949549B (en) | 2015-06-12 | 2015-06-12 | A kind of external warmer |
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| Publication Number | Publication Date |
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| CN104949549A true CN104949549A (en) | 2015-09-30 |
| CN104949549B CN104949549B (en) | 2017-11-03 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510320773.2A Active CN104949549B (en) | 2015-06-12 | 2015-06-12 | A kind of external warmer |
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| CN (1) | CN104949549B (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106642044A (en) * | 2016-10-17 | 2017-05-10 | 天津亚泰昊德科技有限公司 | Novel waste heat boiler |
| CN109282679A (en) * | 2018-10-30 | 2019-01-29 | 中国石油大学(北京) | A kind of fluidized bed external warmer that baffle plate is strengthened |
Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB1475674A (en) * | 1974-08-16 | 1977-06-01 | Babcock & Wilcox Ltd | Thermal stress reducing arrangements |
| CN200962014Y (en) * | 2006-09-20 | 2007-10-17 | 沈志康 | Highly efficient heat exchanger |
| CN101216268A (en) * | 2008-01-10 | 2008-07-09 | 北京亚都空气污染治理技术有限公司 | Adsorption type runner dehumidifier dehumidifying runner and method of manufacture |
| CN101216264A (en) * | 2008-01-08 | 2008-07-09 | 哈尔滨工程大学 | Needle fin tube and plain tube mixedly arranged self-supporting type heat exchanger |
| CN201628498U (en) * | 2010-04-16 | 2010-11-10 | 北京广厦环能科技有限公司 | Multi-shell-side and tube side multi-media mixed heat exchanger |
| CN204142061U (en) * | 2014-10-08 | 2015-02-04 | 青岛京润石化工程有限公司 | A kind of catalyst external warmer |
| CN204220127U (en) * | 2014-10-08 | 2015-03-25 | 青岛京润石化工程有限公司 | A kind of tube-sheet type external warmer |
| CN204987960U (en) * | 2015-06-12 | 2016-01-20 | 青岛京润石化工程有限公司 | External heat collector |
-
2015
- 2015-06-12 CN CN201510320773.2A patent/CN104949549B/en active Active
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB1475674A (en) * | 1974-08-16 | 1977-06-01 | Babcock & Wilcox Ltd | Thermal stress reducing arrangements |
| CN200962014Y (en) * | 2006-09-20 | 2007-10-17 | 沈志康 | Highly efficient heat exchanger |
| CN101216264A (en) * | 2008-01-08 | 2008-07-09 | 哈尔滨工程大学 | Needle fin tube and plain tube mixedly arranged self-supporting type heat exchanger |
| CN101216268A (en) * | 2008-01-10 | 2008-07-09 | 北京亚都空气污染治理技术有限公司 | Adsorption type runner dehumidifier dehumidifying runner and method of manufacture |
| CN201628498U (en) * | 2010-04-16 | 2010-11-10 | 北京广厦环能科技有限公司 | Multi-shell-side and tube side multi-media mixed heat exchanger |
| CN204142061U (en) * | 2014-10-08 | 2015-02-04 | 青岛京润石化工程有限公司 | A kind of catalyst external warmer |
| CN204220127U (en) * | 2014-10-08 | 2015-03-25 | 青岛京润石化工程有限公司 | A kind of tube-sheet type external warmer |
| CN204987960U (en) * | 2015-06-12 | 2016-01-20 | 青岛京润石化工程有限公司 | External heat collector |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106642044A (en) * | 2016-10-17 | 2017-05-10 | 天津亚泰昊德科技有限公司 | Novel waste heat boiler |
| CN109282679A (en) * | 2018-10-30 | 2019-01-29 | 中国石油大学(北京) | A kind of fluidized bed external warmer that baffle plate is strengthened |
| CN109282679B (en) * | 2018-10-30 | 2023-12-29 | 中国石油大学(北京) | Fluidized bed external heat collector reinforced by baffle plate |
Also Published As
| Publication number | Publication date |
|---|---|
| CN104949549B (en) | 2017-11-03 |
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