CN204987969U - Gaseous effluent cooler - Google Patents
Gaseous effluent cooler Download PDFInfo
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- CN204987969U CN204987969U CN201520774705.9U CN201520774705U CN204987969U CN 204987969 U CN204987969 U CN 204987969U CN 201520774705 U CN201520774705 U CN 201520774705U CN 204987969 U CN204987969 U CN 204987969U
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- gaseous effluent
- cooler casing
- perforated plate
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- heat
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Abstract
The application discloses gaseous effluent cooler, including waste gas or cooling agent at the heat exchanger tube bundles who wherein flows, every root canal among this heat exchanger tube bundles is respectively including the fluorescent lamp and the screwed pipe that set up from top to bottom, the inner wall of screwed pipe is formed with protruding threads. The utility model discloses a receive the hot side to take the enhanced heat transfer means to gaseous effluent cooler to and use low resistance efficient soda water conservancy diversion structure, obtain a high efficiency safe more, energy -concerving and environment -protective waste gas cooling device.
Description
Technical field
The application relates to a kind of gaseous effluent, is applied to Coal Chemical Industry and petrochemical industry technology waste gas heat recovery flow process.
Background technology
The low-carbon alkene such as ethene, propylene is important basic chemical raw materials, and along with the demand of development to low-carbon alkene of the development of Chinese national economy, particularly modern chemical industry day by day rises, imbalance between supply and demand also will become increasingly conspicuous.The MTO technique of Methanol ethene, propylene and the MTP technique of preparing propylene from methanol are Chemical Engineering Technologies important at present.This technology is with the methyl alcohol of coal or natural gas synthesis for raw material, and producing low-carbon alkene, is the core technology that development non-oil resource produces the product such as ethene, propylene.
The high-temp waste gas produced in MTO technology process reclaims waste heat for generating steam by gas cooler usually, due to, MTO technology bag mostly is foreign corporation and provides, the version that gas cooler structure all adopts technique package vendor to recommend, there are certain technology barriers, and equipment volume is comparatively large, economy is poor, along with the trend of larger-scale unit, these drawbacks will highlight more.There is certain defect in part-structure in addition, in use goes wrong, and as high temperature tube sheet local overheating is forced to change more high-grade material etc., both added the difficulty of manufacture, raised cost, had a strong impact on again equipment safety operation.
Utility model content
The purpose of this utility model is to provide a kind of gaseous effluent, by taking augmentation of heat transfer means to gaseous effluent heating surface, and the carbonated drink flow-guiding structure of application high-efficiency low-resistance, obtain one more safe and efficient, the exhaust gas cooling device of energy-conserving and environment-protective.
For achieving the above object, the utility model provides following technical scheme:
The embodiment of the present application discloses a kind of gaseous effluent, and comprise the heat-exchanging tube bundle that waste gas or cooling agent flow wherein, the every root pipe in this heat-exchanging tube bundle comprises light pipe setting up and down and screwed pipe respectively, and the inwall of described screwed pipe is formed with thread protrusion.
Preferably, in above-mentioned gaseous effluent, the length of described screwed pipe is 1/3 ~ 1/2 of whole pipe.
Preferably, in above-mentioned gaseous effluent, described gaseous effluent also comprises entrance bobbin carriage assembly, outlet box assembly and cooler casing, described inlet tube box assembly and outlet box assembly are connected to the two ends of described cooler casing, described cooler casing surrounds a cooling agent flowing space, described heat-exchanging tube bundle is arranged in this flowing space, and the two ends of described heat-exchanging tube bundle are communicated with outlet box assembly with described inlet tube box assembly respectively.
Preferably, in above-mentioned gaseous effluent, described inlet tube box assembly comprises upper perforated plate and entrance bobbin carriage, described upper perforated plate adopts flexible flat tube plate structure, described upper perforated plate comprises plate part and cylindrical portions, by circular sliding slopes between the plate part of described upper perforated plate and the bottom of cylindrical portions, with the thermal expansion curve between absorption heat-exchange tube bank and cooler casing.
Preferably, in above-mentioned gaseous effluent, refractory material is laid in the exhaust gas contact face of described entrance bobbin carriage and upper perforated plate.
Preferably, in above-mentioned gaseous effluent, in described cooler casing, upper perforated plate place is provided with vapour-liquid guiding device, this vapour-liquid guiding device cylindrically, between heat-exchanging tube bundle and cooler casing, seal between described vapour-liquid guiding device lower end and cooler casing, between upper end and upper perforated plate, ensure certain gap, force cooling agent liquid-vapor mixture evenly to wash away upper perforated plate with certain speed before going out cooler casing.
Preferably, in above-mentioned gaseous effluent, described outlet box assembly comprises lower perforated plate and outlet bobbin carriage, described lower perforated plate adopts flexible flat tube plate structure, described lower perforated plate comprises plate part and cylindrical portions, by circular sliding slopes between the plate part of described lower perforated plate and cylindrical portions, with the thermal expansion curve between absorption heat-exchange tube bank and cooler casing.
Preferably, in above-mentioned gaseous effluent, be provided with deflection plate in described cooler casing, this deflection plate comprises the disc and donut and disk deflection plate that arrange alternatively up and down, and described disk deflection plate has certain overlapping with annulus baffling in vertical direction view field.
Preferably, in above-mentioned gaseous effluent, the bottom of described cooler casing is communicated with the liquid inlet distributing pipe of import annular header and circle distribution, and described liquid inlet distributing pipe is communicated between described import annular header and cooler casing; The top of described cooler casing is communicated with the liquid-vapor mixture conduit of outlet annular header and circle distribution, and described liquid-vapor mixture conduit is communicated between described outlet annular header and cooler casing.
Compared with prior art, the utility model has the advantage of: the utility model is provided with vapour-liquid guiding device near upper perforated plate place in housing, guiding device cylindrically, between tube bank and housing, seal between guide shell lower end and cylindrical shell, cylinder inwall and tube bank outer rim and all ensure specific gap between cylinder upper end and upper perforated plate, force liquid-vapor mixture evenly to wash away upper perforated plate with certain speed before going out housing, make it to be in safe and reliable operation atmosphere all the time.
Accompanying drawing explanation
In order to be illustrated more clearly in the embodiment of the present application or technical scheme of the prior art, be briefly described to the accompanying drawing used required in embodiment or description of the prior art below, apparently, the accompanying drawing that the following describes is only some embodiments recorded in the application, for those of ordinary skill in the art, under the prerequisite not paying creative work, other accompanying drawing can also be obtained according to these accompanying drawings.
Figure 1 shows that the sectional view of gaseous effluent in the utility model specific embodiment.
Detailed description of the invention
Below in conjunction with the accompanying drawing in the utility model embodiment, be described in detail the technical scheme in the utility model embodiment, obviously, described embodiment is only the utility model part embodiment, instead of whole embodiments.Based on the embodiment in the utility model, the every other embodiment that those of ordinary skill in the art obtain under the prerequisite not making creative work, all belongs to the scope of the utility model protection.
As shown in Figure 1, gaseous effluent is that vertical structure is arranged, tube side medium is waste gas, and shell side medium is steam water interface.High-temp waste gas is introduced into entrance bobbin carriage 1, then carries out heat exchange by cooler bundle 12, and waste gas is reduced to after suitable temperature through heat exchange and discharges cooler by outlet bobbin carriage 15 through waste gas outlet 9.
Cooler casing 5 two ends are welded to connect with upper perforated plate 4 and lower perforated plate 8 respectively, and by upper perforated plate 4, lower perforated plate 8 respectively with entrance bobbin carriage 1 with export bobbin carriage 15 and be welded to connect, cooler bundle 12 is built in housing 5, and tube bank two ends are connected with upper and lower Tube-sheet Welding respectively.Entrance bobbin carriage 1 inwall and upper perforated plate 4 exhaust gas contact side are laid refractory liner 10 and are carried out thermal insulation.
Upper perforated plate 4 and lower perforated plate 8 all adopt flexible flat tube plate structure, namely between the plate part of tube sheet and cylindrical portions by circular sliding slopes, tube plate thickness is not more than 30mm, in order to the thermal expansion curve between absorption heat-exchange tube bank 12 and housing 5.
Cooler bundle adopts light pipe and screwed pipe combining form, adopt the whole steel pipe combination without splicing to form, top is light pipe portion 121, is in high exhaust temperatures section, bottom is threaded pipe section 122, account for the 1/3-1/2 of whole tube length, be in waste gas low-temperature zone, threaded pipe section 122 is by roll-in helix outside pipe, be corresponding spiral salient at tube wall, impel flow perturbation in pipe, reach strengthening low-temperature zone heat-transfer effect, reduce heat exchange area.Shell-side cylinder adopts reducing in two end portions.
Outside feedwater is introduced into import annular header 6, then enters cooler casing by the liquid inlet distributing pipe 7 between annular header and housing 5, more evenly enters heat-exchanging tube bundle 12 through feedwater distribution guide shell 14.Tube bank 12 is built in housing 5, in cooler casing 5, shell side medium washes away outside tube bank 12 by a kind of deflection plate 13 of disk-and-doughnut combining form successively, absorb the vaporization of waste gas liberated heat, annulus 131 and disk 132 are alternately fixed in tube bank 12 with certain spacing, shell side medium is forced along certain flow process by tube bank 12 by the stop of deflection plate, this baffle arrangement makes carbonated drink wash away heat-exchanging tube bundle more evenly fully, effectively can reduce and wash away dead band, reduce " waste stream ", heat-transfer effect is good, and resistance is little.
Shell side steam water interface forces carbonated drink to wash away even upper perforated plate 4 with specific flow velocity by carbonated drink guide shell 11, avoids upper perforated plate local overheating after arriving cooler upper end.After steam water interface has been heated, import outlet annular header 2 by the liquid-vapor mixture conduit 3 being distributed in housing 5 upper end, and then by completing whole water circulation in pipeline connecting system drum, output needs the steam of quality.
Effectively can be fallen the steel consumption of gaseous effluent equipment by the enforcement of above-mentioned means, reduce costs, whole circulation process resistance drop is less simultaneously, and security is high, namely improves the security reliability of system cloud gray model.
It should be noted that, in this article, the such as relational terms of first and second grades and so on is only used for an entity or operation to separate with another entity or operating space, and not necessarily requires or imply the relation that there is any this reality between these entities or operation or sequentially.And, term " comprises ", " comprising " or its any other variant are intended to contain comprising of nonexcludability, thus make to comprise the process of a series of key element, method, article or equipment and not only comprise those key elements, but also comprise other key elements clearly do not listed, or also comprise by the intrinsic key element of this process, method, article or equipment.When not more restrictions, the key element limited by statement " comprising ... ", and be not precluded within process, method, article or the equipment comprising described key element and also there is other identical element.
The above is only the detailed description of the invention of the application; it should be pointed out that for those skilled in the art, under the prerequisite not departing from the application's principle; can also make some improvements and modifications, these improvements and modifications also should be considered as the protection domain of the application.
Claims (9)
1. a gaseous effluent, is characterized in that, comprise the heat-exchanging tube bundle that waste gas or cooling agent flow wherein, the every root pipe in this heat-exchanging tube bundle comprises light pipe setting up and down and screwed pipe respectively, and the inwall of described screwed pipe is formed with thread protrusion.
2. gaseous effluent according to claim 1, is characterized in that: the length of described screwed pipe is 1/3 ~ 1/2 of whole pipe.
3. gaseous effluent according to claim 1, it is characterized in that: described gaseous effluent also comprises entrance bobbin carriage assembly, outlet box assembly and cooler casing, described inlet tube box assembly and outlet box assembly are connected to the two ends of described cooler casing, described cooler casing surrounds a cooling agent flowing space, described heat-exchanging tube bundle is arranged in this flowing space, and the two ends of described heat-exchanging tube bundle are communicated with outlet box assembly with described inlet tube box assembly respectively.
4. gaseous effluent according to claim 3, it is characterized in that: described inlet tube box assembly comprises upper perforated plate and entrance bobbin carriage, described upper perforated plate adopts flexible flat tube plate structure, described upper perforated plate comprises plate part and cylindrical portions, by circular sliding slopes between the plate part of described upper perforated plate and the bottom of cylindrical portions, with the thermal expansion curve between absorption heat-exchange tube bank and cooler casing.
5. gaseous effluent according to claim 4, is characterized in that: refractory material is laid in the exhaust gas contact face of described entrance bobbin carriage and upper perforated plate.
6. gaseous effluent according to claim 4, it is characterized in that: in described cooler casing, upper perforated plate place is provided with vapour-liquid guiding device, this vapour-liquid guiding device cylindrically, between heat-exchanging tube bundle and cooler casing, seal between described vapour-liquid guiding device lower end and cooler casing, ensure certain gap between upper end and upper perforated plate, force cooling agent liquid-vapor mixture evenly to wash away upper perforated plate with certain speed before going out cooler casing.
7. gaseous effluent according to claim 3, it is characterized in that: described outlet box assembly comprises lower perforated plate and outlet bobbin carriage, described lower perforated plate adopts flexible flat tube plate structure, described lower perforated plate comprises plate part and cylindrical portions, by circular sliding slopes between the plate part of described lower perforated plate and cylindrical portions, with the thermal expansion curve between absorption heat-exchange tube bank and cooler casing.
8. gaseous effluent according to claim 3, it is characterized in that: in described cooler casing, be provided with deflection plate, this deflection plate comprises the disc and donut and disk deflection plate that arrange alternatively up and down, and described disk deflection plate has certain overlapping with annulus baffling in vertical direction view field.
9. gaseous effluent according to claim 3, it is characterized in that: the bottom of described cooler casing is communicated with the liquid inlet distributing pipe of import annular header and circle distribution, described liquid inlet distributing pipe is communicated between described import annular header and cooler casing; The top of described cooler casing is communicated with the liquid-vapor mixture conduit of outlet annular header and circle distribution, and described liquid-vapor mixture conduit is communicated between described outlet annular header and cooler casing.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520774705.9U CN204987969U (en) | 2015-10-08 | 2015-10-08 | Gaseous effluent cooler |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520774705.9U CN204987969U (en) | 2015-10-08 | 2015-10-08 | Gaseous effluent cooler |
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| Publication Number | Publication Date |
|---|---|
| CN204987969U true CN204987969U (en) | 2016-01-20 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201520774705.9U Active CN204987969U (en) | 2015-10-08 | 2015-10-08 | Gaseous effluent cooler |
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| CN (1) | CN204987969U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105135916A (en) * | 2015-10-08 | 2015-12-09 | 张家港市江南锅炉压力容器有限公司 | Waste gas cooler |
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2015
- 2015-10-08 CN CN201520774705.9U patent/CN204987969U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105135916A (en) * | 2015-10-08 | 2015-12-09 | 张家港市江南锅炉压力容器有限公司 | Waste gas cooler |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CP01 | Change in the name or title of a patent holder | ||
| CP01 | Change in the name or title of a patent holder |
Address after: Zhangjiagang Jiangnan Boiler and Pressure Vessel Co., Ltd., No. 139 Gangfeng Road, Yangzijiang International Chemical Park, Zhangjiagang City, Suzhou City, Jiangsu Province, 215635 Patentee after: Jiangsu Jiangguo Intelligent Equipment Co.,Ltd. Address before: Zhangjiagang Jiangnan Boiler and Pressure Vessel Co., Ltd., No. 139 Gangfeng Road, Yangzijiang International Chemical Park, Zhangjiagang City, Suzhou City, Jiangsu Province, 215635 Patentee before: Jiangnan Boilers & Pressure Vessels (Zhangjiagang) Co.,Ltd. |