CN104759141A - Diameter-varying tubular sand-rejecting and energy-saving apparatus used in heat exchanger - Google Patents
Diameter-varying tubular sand-rejecting and energy-saving apparatus used in heat exchanger Download PDFInfo
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- CN104759141A CN104759141A CN201510112859.6A CN201510112859A CN104759141A CN 104759141 A CN104759141 A CN 104759141A CN 201510112859 A CN201510112859 A CN 201510112859A CN 104759141 A CN104759141 A CN 104759141A
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Abstract
The invention discloses a diameter-varying tubular heat exchanger equipped with a sand-rejecting and energy-saving apparatus and belongs to the technical field of heat exchangers. The apparatus mainly includes: a front flange disk, a back flange disk, a front diameter-varying shell body, a back diameter-varying shell body, a screw joint, a blow-down valve, and a filtering and energy-saving assembly which is composed of a front filtering and energy-saving piece, a back filtering and blocking piece and a connecting fixed rod assembly. The front and the back flange disks are respectively welded to two small-diameter end openings of the front and the back diameter-varying shell bodies. The two large-diameter end openings of the front and the back diameter-varying shell bodies are butt-jointed to each other through a flange with bolt fastening. The filtering and energy-saving assembly is installed in a large-diameter chamber at the side of the front diameter-varying shell body, wherein a blow-down valve outlet is formed at a lower side wall of a large-diameter end of the front diameter-varying shell body. The blow-down valve is connected to the blow-down valve on the diameter-varying shell body through the screw joint. The apparatus not only can reduce failure rate of a heat pump unit, thereby reducing the maintenance cost of the unit and prolonging the service life of the heat pump unit, but also can effectively save the energy resources, thereby increasing the use-efficiency of primary energy resources.
Description
Technical field
The invention belongs to technical field of heat exchangers, particularly relate to a kind of reducing shell-tube type be equipped with for heat exchanger and remove sand that unload can the structural design of device.
Background technology
At present, in heat pump industry, often there will be heat exchanger internal heat exchange tubes leak or the dirty problem such as stifled, had a strong impact on the service life of source pump and the heat exchange efficiency of unit, and caused the problems such as too high maintenance cost expense.
Summary of the invention
The object of the invention is the weak point in order to overcome prior art, designing a kind of reducing shell-tube type for heat exchanger and removing sand that unload can device; One aspect of the present invention can reduce the fault rate of source pump, thus reduces the maintenance cost of unit, extends the service life of heat pump product; Effectively save the energy on the other hand, improve the service efficiency of primary energy.
A kind of reducing shell-tube type for heat exchanger that the present invention proposes removes sand and unloads energy device, it is characterized in that, comprise forward flange dish, rear stub, front reducing housing, rear reducing housing, to silk and blowoff valve, unload energy sheet by front filtration, rear filtration cut out tab unloads energy assembly with the filtration being connected and fixed bar assembly formation; Wherein, ring flange welds with two path ports of front and back reducing housing respectively, and the bigger diameter end mouth of front and back reducing housing is docked by flange, bolted; Filter and unload and can be arranged in the chamber, large footpath of front reducing case side by assembly, front reducing housing bigger diameter end lower wall has sewage draining exit, and blowoff valve is by being connected to the sewage draining exit place of reducing housing to silk.
Feature of the present invention and useful achievement:
For after using single hydrocyclone, also can there is the further filtration of the tiny grains of sand problem of part in the present invention, and can effectively reduce current and affect for the impact of heat exchanger internal heat exchange tubes in water quality.
This invention structure effectively can save the energy, improves the utilization ratio of primary energy, reduces the fault rate of source pump, thus reduces the maintenance cost of unit, extends the service life of heat pump product.
Accompanying drawing explanation
Fig. 1 is the general structure assembled view of structure of the present invention;
Fig. 2 is the general structure decomposition view of structure of the present invention;
Fig. 3 is that energy sheet view is unloaded in inside configuration of the present invention filtration;
Fig. 4 is the partial sectional view of structure of the present invention.
Detailed description of the invention
Below in conjunction with accompanying drawing and embodiment, the present invention will be described:
Structure of the present invention as shown in Figure 1, 2, comprises forward flange dish 1, rear stub 2, front reducing housing 3, rear reducing housing 4, and energy sheet 5 is unloaded in front filtration, and rear filtration cut out tab 6, is connected and fixed bar assembly 7, forms silk 8 and blowoff valve 9; Wherein, ring flange 1,2 welds with the both sides port of reducing housing 3,4 respectively, filtration unload can sheet 5 with filter cut out tab 6 be arranged on fixed connecting rod assembly 7 forms filtration unloads can assembly, this filtration is unloaded and can is arranged in the space, large footpath of long front reducing housing 3 by component integration, as shown in Figure 3, the bigger diameter end subordinate side of long reducing housing 3 has sewage draining exit, front reducing housing 3 is docked by flange with the bigger diameter end mouth of rear reducing housing 4, bolted, for convenience detach, blowoff valve 9 and reducing housing 3 are by being connected to the sewage draining exit place on the downside of reducing housing 3 end to silk 8.
The present invention is arranged on the water inlet port of heat exchanger unit, to after using single hydrocyclone, also can there is the further filtration of the tiny grains of sand problem of part in water quality, and can effectively reduce current and affect for the impact of heat exchanger internal heat exchange tubes.
Each parts specific embodiment in present device is respectively described below:
Ring flange 1, ring flange 2, and the mounting flange between two reducing housings is conventional specification product.Can select according to heat exchanger mouth of a river caliber adjustment coupling.
Front its miner diameter end of reducing housing 3 is according to heat exchanger water inlet match of pipe diameter, bigger diameter end caliber is according to the optional different tube diameters specification of concrete actual conditions, generally be not less than 1.5 times of path, the overall length dimension of reducing housing also can adjust according to actual requirement (being not less than 3 times of minor diameter), can better improve the effect of unloading and can remove sand.
The large footpath of rear reducing housing 4 and path and front reducing housing 3 measure-alike, its length is not less than 2 times of path.
This removes sand and unloads 5 times that energy device total length is path.
Filtration unloads energy sheet 5 for a circular filter mesh sheet is as shown in Fig. 3 (a), diameter is identical with the large footpath of reducing housing 3, it cuts a small gap (cut height is 1/10th of filter net sheet diameter) below, filtering cut out tab 6 is that a circular filter mesh sheet is as Fig. 3 (b), it is imperforate baffle below, imperforate baffle size and filtration unload can sheet 5 to cut small gap measure-alike, the dirt being deposited on bottom in front reducing housing 3 shell is blocked in its effect, and dirt is discharged from sewage draining exit.
Filtration is unloaded and can be filter net sheet with filtration cut out tab 6 by sheet 5, front filtration is unloaded and the screen distance of sheet can be greater than the screen distance of rear filtration cut out tab, different material specifications and filter screen order number can be selected according to the actual water quality in scene, between the two apart from being not less than 2 times of little electrical path length, the filtration of its deuterzooid structure is unloaded and the quantity of sheet also can be not limited to and select two, specifically can adjust according to actual field situation and select.
The conventional products matched all is selected to silk 8 and blowoff valve 9.
Embodiment:
The heat exchanger water inlet pipe latus rectum 100mm of application the present embodiment, ring flange 1,2 matches and selects, long front reducing housing 3 path latus rectum is 100mm, large footpath latus rectum is 150mm, reducing housing 3 total length is 300mm, the large footpath of short rear reducing housing 4 and path and reducing housing 3 measure-alike, reducing housing 4 total lengths >=200mm, it can sheet 5 external diameter be 100mm that filtration is unloaded, lower end cut height is positioned at 10mm place, filtration is unloaded and can be also positioned at 10mm place by sheet 6 imperforate baffle height, filters the spacing of unloading between energy sheet 5,6 and answers >=200mm.
This removes sand and unloads can device total length be 500mm.
The course of work of this heat exchanger is: during operation, when water route in pipe is along A to when entering in reducing housing 3, inner side caliber becomes large, water route flow velocity reduces, unload can manage interior water route flow velocity by further reduction of sheet 5 and 6 by filtering, wherein filter the pore size filter unloaded on energy sheet 6 and be less than the aperture of filtering and unloading energy sheet 5, in order to reach the effect of filtering more fine impurity.In the process by the change of caliber with filter that unload can the deceleration of sheet, grains of sand impurity in water quality precipitates, under the percussion of current, sediment is through filtering the otch 10 (as shown in Figure 4) unloading energy B place, sheet 5 lower end, then through filtering the imperforate baffle unloading energy sheet 6 lower end 11 place, lodged contamination is made not unload energy sheet 6 by filtering, and enable lodged contamination form deposition shape 12 at sewage draining exit place, reducing housing 3 lower end, as Fig. 4 (b), in the process that unit uses, only need regularly open blowoff valve 9, deposit is discharged.
Secondly structure of the present invention, filters and unloads and can realize dismounting by sheet, facilitate self-filtering to unload the cleaning of energy sheet.During installation, this invention structure should be arranged near heat exchanger water inlet as far as possible, thus is unloading the impact failure effectively protecting heat exchanger internal heat exchange tubes in energy process.
Claims (4)
1. the reducing shell-tube type for heat exchanger removes sand and unloads energy device, it is characterized in that, this reducing shell and tube exchanger comprises forward flange dish, rear stub, front reducing housing, rear reducing housing, to silk and blowoff valve, unload energy sheet by front filtration, rear filtration cut out tab unloads energy assembly with the filtration being connected and fixed bar assembly formation; Wherein, ring flange welds with two path ports of front and back reducing housing respectively, and the bigger diameter end mouth of front and back reducing housing is docked by flange, bolted; Filter and unload and can be arranged in the chamber, large footpath of front reducing case side by assembly, front reducing housing bigger diameter end lower wall has sewage draining exit, and blowoff valve is by being connected to the sewage draining exit place of reducing housing to silk.
2. the reducing shell-tube type for heat exchanger according to claim 1 removes sand and unloads energy device, be further characterized in that, described front and back reducing housing miner diameter end is according to heat exchanger mouth of a river match of pipe diameter, and bigger diameter end caliber is 1.5 times of path, and this removes sand and unloads 5 times that energy device total length is path.
3. reducing shell and tube exchanger according to claim 1, be further characterized in that, described front filtration is unloaded and sheet and rear filtration cut out tab can be filter net sheet, and front filtration is unloaded and the screen distance of sheet can be greater than the screen distance of rear filtration cut out tab, and the spacing between two filter net sheets is 2 times of path.
4. reducing shell and tube exchanger according to claim 1, is further characterized in that, filters and unload and can have breach in sheet lower end before described, and described rear filtration is unloaded and can be provided with imperforate baffle in sheet lower end.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201510112859.6A CN104759141A (en) | 2015-03-16 | 2015-03-16 | Diameter-varying tubular sand-rejecting and energy-saving apparatus used in heat exchanger |
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CN201510112859.6A CN104759141A (en) | 2015-03-16 | 2015-03-16 | Diameter-varying tubular sand-rejecting and energy-saving apparatus used in heat exchanger |
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CN201510112859.6A Pending CN104759141A (en) | 2015-03-16 | 2015-03-16 | Diameter-varying tubular sand-rejecting and energy-saving apparatus used in heat exchanger |
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105300135A (en) * | 2015-11-19 | 2016-02-03 | 苏州市金翔钛设备有限公司 | Self-filtering efficient titanium heat exchanger |
CN109959268A (en) * | 2017-12-26 | 2019-07-02 | 天水师范学院 | A kind of fluoroplastics tubular type liquid-liquid heat-exchange system |
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CN201120219Y (en) * | 2007-10-30 | 2008-09-24 | 广州有色金属研究院 | Filter |
CN202289667U (en) * | 2011-07-20 | 2012-07-04 | 恩曼自动化技术(上海)有限公司 | Straight-pipe type filtering device |
CN202342988U (en) * | 2011-12-01 | 2012-07-25 | 山东鲁能泰山铁塔有限公司 | Pipeline sewage filtering device |
CN203436917U (en) * | 2013-08-07 | 2014-02-19 | 长春黄金研究院 | Novel pipeline filter |
CN203886274U (en) * | 2014-04-21 | 2014-10-22 | 江苏赛宝龙石化有限公司 | Styrene multi-layer filter device |
CN204767807U (en) * | 2015-03-16 | 2015-11-18 | 北京中科华誉热泵设备制造有限公司 | A reducing shell and tube formula is removed sand and is unloaded ability device for heat exchanger |
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2015
- 2015-03-16 CN CN201510112859.6A patent/CN104759141A/en active Pending
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
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CN201120219Y (en) * | 2007-10-30 | 2008-09-24 | 广州有色金属研究院 | Filter |
CN202289667U (en) * | 2011-07-20 | 2012-07-04 | 恩曼自动化技术(上海)有限公司 | Straight-pipe type filtering device |
CN202342988U (en) * | 2011-12-01 | 2012-07-25 | 山东鲁能泰山铁塔有限公司 | Pipeline sewage filtering device |
CN203436917U (en) * | 2013-08-07 | 2014-02-19 | 长春黄金研究院 | Novel pipeline filter |
CN203886274U (en) * | 2014-04-21 | 2014-10-22 | 江苏赛宝龙石化有限公司 | Styrene multi-layer filter device |
CN204767807U (en) * | 2015-03-16 | 2015-11-18 | 北京中科华誉热泵设备制造有限公司 | A reducing shell and tube formula is removed sand and is unloaded ability device for heat exchanger |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105300135A (en) * | 2015-11-19 | 2016-02-03 | 苏州市金翔钛设备有限公司 | Self-filtering efficient titanium heat exchanger |
CN105300135B (en) * | 2015-11-19 | 2018-03-20 | 苏州市金翔钛设备有限公司 | The efficient Ti-heat exchanger of inherent filtration |
CN109959268A (en) * | 2017-12-26 | 2019-07-02 | 天水师范学院 | A kind of fluoroplastics tubular type liquid-liquid heat-exchange system |
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Application publication date: 20150708 |