CN101446459B - Flexible fluid-directing double-spiral-sleeve type heat exchanger - Google Patents
Flexible fluid-directing double-spiral-sleeve type heat exchanger Download PDFInfo
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- CN101446459B CN101446459B CN2008100792306A CN200810079230A CN101446459B CN 101446459 B CN101446459 B CN 101446459B CN 2008100792306 A CN2008100792306 A CN 2008100792306A CN 200810079230 A CN200810079230 A CN 200810079230A CN 101446459 B CN101446459 B CN 101446459B
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- 239000012267 brine Substances 0.000 claims description 14
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical compound O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 claims description 14
- 239000007788 liquid Substances 0.000 claims description 8
- 238000005192 partition Methods 0.000 claims description 8
- 238000004891 communication Methods 0.000 claims description 4
- 239000003507 refrigerant Substances 0.000 abstract description 6
- 238000012546 transfer Methods 0.000 abstract description 6
- 239000012530 fluid Substances 0.000 abstract description 5
- 230000000694 effects Effects 0.000 abstract description 2
- 239000000463 material Substances 0.000 abstract description 2
- 239000000498 cooling water Substances 0.000 abstract 1
- 238000000605 extraction Methods 0.000 abstract 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical group [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 2
- 239000004677 Nylon Substances 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 230000008020 evaporation Effects 0.000 description 2
- 229920001778 nylon Polymers 0.000 description 2
- 239000007779 soft material Substances 0.000 description 2
- 230000004087 circulation Effects 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 230000008719 thickening Effects 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 230000003245 working effect Effects 0.000 description 1
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- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
Description
技术领域 technical field
本发明涉及一种套管式换热器,特别指小型、中型、大型水源热泵和水冷冷水机组均可使用的套管式换热器,具体为一种柔性导流双螺旋套管式换热器。The invention relates to a sleeve-type heat exchanger, in particular to a sleeve-type heat exchanger that can be used in small, medium and large-scale water source heat pumps and water-cooled chillers, specifically a flexible flow-guiding double-helix sleeve-type heat exchanger device.
背景技术 Background technique
现有的套管式换热器的结构包括压缩机,入口与压缩机相连通的螺旋状套管冷凝器,与压缩机相连通的、端部设有集气桶的螺旋状套管蒸发器,与螺旋状套管冷凝器的末端相连通的集流桶;集流桶通过分液器和螺旋状套管蒸发器相连通;螺旋状套管冷凝器和螺旋状套管蒸发器的结构均包括管套,以及穿套于管套中的数个细换热管。所谓套管式,就是指管套中穿套有数个细换热管,即管中套管。螺旋状套管冷凝器的入口通过连通管直接与压缩机相连通。集流桶直接设置于螺旋状套管冷凝器的末端。螺旋状套管蒸发器的集气桶通过汽液分离器与压缩机相连通。这种结构的套管式换热器只能适用于小型机组,在国标框架内的最优工作状态下的能效比(EER)≤4.6,性能系数(COP)≤4.05,传热系数(K)≤1100W/M2.℃,排热能力为1—180KW。而且,换热管耗材多。因此,无论从工作效果上,还是从节能减耗上讲,这种结构的套管式换热器还不能满足人们现在日益增长的节能、增效、减耗的要求。The structure of the existing casing heat exchanger includes a compressor, a spiral casing condenser whose inlet is connected with the compressor, and a spiral casing evaporator connected with the compressor and having a gas collecting bucket at the end. , the collecting barrel connected with the end of the spiral casing condenser; the collecting barrel is connected with the spiral casing evaporator through the liquid separator; the structures of the spiral casing condenser and the spiral casing evaporator are both It includes a pipe sleeve and several thin heat exchange tubes that are sheathed in the pipe sleeve. The so-called sleeve type means that there are several thin heat exchange tubes in the sleeve, that is, the sleeve in the tube. The inlet of the helical casing condenser is directly connected with the compressor through a communication pipe. The collecting bucket is directly set at the end of the spiral sleeve condenser. The gas collecting barrel of the spiral casing evaporator communicates with the compressor through a vapor-liquid separator. The casing heat exchanger of this structure can only be applied to small units, and the energy efficiency ratio (EER) ≤ 4.6, the coefficient of performance (COP) ≤ 4.05, and the heat transfer coefficient (K) under the optimal working condition within the framework of the national standard ≤1100W/M 2 .℃, heat removal capacity is 1-180KW. Moreover, there are many heat exchange tube consumables. Therefore, no matter in terms of working effect or energy saving and consumption reduction, the sleeve-pipe heat exchanger with this structure cannot meet people's increasing requirements for energy saving, efficiency increase and consumption reduction.
发明内容 Contents of the invention
为了解决现有的套管式换热器存在的上述缺陷,本发明提供了一种更加节能、增效、减耗的套管式换热器,即柔性导流双螺旋套管式换热器。In order to solve the above-mentioned defects of the existing sleeve-type heat exchanger, the present invention provides a sleeve-type heat exchanger that is more energy-saving, efficiency-enhancing, and consumption-reducing, that is, a flexible flow-guiding double-helix sleeve-type heat exchanger .
本发明采用了如下技术方案来实现上述目的:一种柔性导流双螺旋套管式换热器,包括压缩机,入口与压缩机相连通的螺旋状套管冷凝器,与压缩机相连通的、端部设有集气桶的螺旋状套管蒸发器,与螺旋状套管冷凝器的末端相连通的集流桶;集流桶通过分液器和螺旋状套管蒸发器相连通;螺旋状套管冷凝器和螺旋状套管蒸发器的结构均包括管套,以及穿套于管套中的数个细换热管;细换热管外壁间隔设置有柔性导流器,螺旋状套管冷凝器和螺旋状套管蒸发器均通过热交换器与压缩机连通;热交换器结构包括:外套桶,设于外套桶顶部的上排气口,设于外套桶底部的下排气口,设于外套桶底部的蒸发器连接口,设于外套桶侧壁的压缩机连接口,设于外套桶内部并与蒸发器连接口和压缩机连接口同时连通的内换热管;上排气口通过连通管与压缩机的排气口相连通,下排气口通过连通管与冷凝器的入口相连通,蒸发器连接口通过连通管与集气桶相连通,压缩机连接口通过连通管与压缩机的吸气口相连通。柔性导流器即采用硬质或软质材料制作成的圆环,如铜环,尼龙环等。The present invention adopts the following technical scheme to achieve the above object: a flexible diversion double helical casing heat exchanger, including a compressor, a spiral casing condenser whose inlet is connected to the compressor, and a spiral casing condenser connected to the compressor. , the spiral casing evaporator with a gas collecting barrel at the end, and the collecting barrel connected with the end of the spiral casing condenser; the collecting barrel is connected with the spiral casing evaporator through a liquid separator; The structures of both the tube-shaped condenser and the spiral-tube evaporator include tube sleeves and several thin heat exchange tubes that go through the tube sleeves; the outer walls of the thin heat exchange tubes are provided with flexible flow guides at intervals, Both the tube condenser and the helical casing evaporator communicate with the compressor through a heat exchanger; the structure of the heat exchanger includes: an outer casing, an upper exhaust port on the top of the outer casing, and a lower exhaust outlet on the bottom of the outer casing , the evaporator connection port at the bottom of the jacket drum, the compressor connection port on the side wall of the jacket drum, the inner heat exchange tubes located inside the jacket drum and connected to the evaporator connection port and the compressor connection port at the same time; the upper row The air port is connected with the exhaust port of the compressor through the connecting pipe, the lower exhaust port is connected with the inlet of the condenser through the connecting pipe, the connecting port of the evaporator is connected with the gas collecting barrel through the connecting pipe, and the connecting port of the compressor is connected through the connecting pipe. The pipe communicates with the suction port of the compressor. The flexible deflector is a ring made of hard or soft materials, such as copper rings, nylon rings, etc.
本发明突破了传统的技术瓶颈,使流经换热器的载冷剂和制冷剂呈反向螺旋形流动,此即为本发明所称双螺旋的含义。双螺旋流动,可以使制冷剂在管内和载冷剂在管外流动过程中形成多次环流从而产生离心力,该离心力可以破坏传热管内壁的阻力,绝对限制液膜增厚,提高了换热系数,而且扩大了换热面积,进一步提高了换热效率,柔性导流器的存在更强化了换热器的换热效率,而采用柔性一词,意在说明,由于该柔性导流器的存在,流经该柔性导流器的流体就象婀娜多姿的少女扭动着美丽的腰胯在舞动行进。本发明采用了热交换器替代了传统的气液分离器,不仅增加了进入压缩机的低压气体的过热度,提高了低压气体的干燥度,从而有效地防止了压缩机液击,而且降低了压缩机的吸气阻力,提高了蒸发温度,增大了制冷量。因此,本发明集流体动力学、传热学、热力学、美学与一身,并为这些学科的发展提供了非常有价值的应用范例。经应用检测,在国标框架内,本发明的能效比(EER)≥5.66,性能系数(COP)≥4.8,传热系数(K)≥2000W/M2.℃,排热能力1—400KW,制冷量比现有技术提高了30%左右,而换热管用材却降低了20%左右,节能降耗效果非常明显。因此达到了节能、增效、减耗的要求和目的。The present invention breaks through the traditional technical bottleneck, and makes the brine and refrigerant flowing through the heat exchanger flow in a reverse spiral shape, which is the meaning of the double helix in the present invention. The double helix flow can make the refrigerant flow in the tube and the brine flow outside the tube to form multiple circulations to generate centrifugal force, which can destroy the resistance of the inner wall of the heat transfer tube, absolutely limit the thickening of the liquid film, and improve heat transfer Coefficient, and expand the heat exchange area, further improve the heat exchange efficiency, the existence of the flexible flow deflector strengthens the heat exchange efficiency of the heat exchanger, and the word flexibility is used to explain that due to the Existence, the fluid flowing through the flexible deflector is like a graceful girl twisting her beautiful waist and hips and dancing. The invention adopts a heat exchanger to replace the traditional gas-liquid separator, which not only increases the superheat degree of the low-pressure gas entering the compressor, but also improves the dryness of the low-pressure gas, thus effectively preventing the compressor from liquid hammering and reducing the The suction resistance of the compressor increases the evaporation temperature and increases the cooling capacity. Therefore, the present invention integrates fluid dynamics, heat transfer, thermodynamics, and aesthetics, and provides a very valuable application example for the development of these subjects. After application testing, within the framework of the national standard, the energy efficiency ratio (EER) of the present invention is ≥ 5.66, the coefficient of performance (COP) is ≥ 4.8, the heat transfer coefficient (K) is ≥ 2000W/M 2 .℃, and the heat removal capacity is 1-400KW. Compared with the prior art, the energy consumption is increased by about 30%, while the materials used for the heat exchange tubes are reduced by about 20%, so the effect of energy saving and consumption reduction is very obvious. Therefore, the requirements and goals of energy saving, efficiency enhancement and consumption reduction are achieved.
附图说明 Description of drawings
图1为本发明结构示意图;Fig. 1 is a structural representation of the present invention;
图2为过冷器结构示意图;Fig. 2 is the schematic diagram of subcooler structure;
具体实施方式 Detailed ways
一种柔性导流双螺旋套管式换热器,包括压缩机1,入口16与压缩机1相连通的螺旋状套管冷凝器2,与压缩机1相连通的、端部设有集气桶3的螺旋状套管蒸发器4,与螺旋状套管冷凝器2的末端相连通的集流桶5;集流桶5通过分液器6和螺旋状套管蒸发器4相连通;螺旋状套管冷凝器2和螺旋状套管蒸发器4的结构均包括管套,以及穿套于管套中的数个细换热管7;细换热管7外壁间隔设置有柔性导流器8,螺旋状套管冷凝器2和螺旋状套管蒸发器4均通过热交换器与压缩机1连通;热交换器结构包括:外套桶9,设于外套桶9顶部的上排气口10,设于外套桶9底部的下排气口11,设于外套桶9底部的蒸发器连接口12,设于外套桶9侧壁的压缩机连接口13,设于外套桶9内部并与蒸发器连接口12和压缩机连接口13同时连通的内换热管14;上排气口10通过连通管15与压缩机1的排气口相连通,下排气口11通过连通管15与冷凝器的入口16相连通,蒸发器连接口12通过连通管15与集气桶3相连通,压缩机连接口13通过连通管15与压缩机1的吸气口相连通。柔性导流器即采用硬质或软质材料制作成的圆环,如铜环,尼龙环等。A flexible diversion double helix casing heat exchanger, including a compressor 1, a spiral casing condenser 2 with an
细换热管7在管套中呈曲线状分布,The thin heat exchange tubes 7 are distributed in a curved shape in the tube casing,
上述“呈曲线状分布”的曲线状是指除直线以外的任何能够使细换热管7内的流体呈非直线状行进的形态,如正弦(余弦)曲线、螺旋线等。The above-mentioned "distributed in a curved shape" refers to any form other than a straight line that can make the fluid in the thin heat exchange tube 7 travel non-linearly, such as a sine (cosine) curve, a helix, and the like.
细换热管7外壁间隔设置的柔性导流器8在空间上呈正弦(余弦)曲线或螺旋线分布。The flexible deflectors 8 arranged at intervals on the outer walls of the thin heat exchange tubes 7 are distributed in a sine (cosine) curve or a helix in space.
为了更进一步地提高本发明的换热效率,可在螺旋状套管冷凝器2的末端设置一过冷器,再在过冷器的另一端设置集流桶5,也就是说,集流桶5和螺旋状套管冷凝器2的末端通过一过冷器相连通,过冷器的结构包括上部右端设有载冷剂入管17、下部左端设有载冷剂出管18、下部右端设有集流桶连接口19的管桶,设于载冷剂入管17中的、中部设有圆孔的上隔板20,设于载冷剂出管18中的、中部设有圆孔的下隔板21,设于上隔板20的圆孔下方并与圆孔密封连通的上总管22,设于下隔板21的圆孔上方并与圆孔密封连通的下总管23,数个设于上总管22和下总管23间、并与上总管22和下总管23同时连通的、外壁设有螺纹的螺纹换热管24;集流桶连接口19处与集流桶5连通。载冷剂入管17与外部载冷剂供给管相通,载冷剂出管18与螺旋状套管冷凝器2的末端相通。In order to further improve the heat exchange efficiency of the present invention, a subcooler can be set at the end of the spiral sleeve condenser 2, and a collecting bucket 5 is set at the other end of the subcooler, that is to say, a collecting bucket 5 and the end of the spiral sleeve condenser 2 are connected through a subcooler. The structure of the subcooler includes a
上述螺纹换热管24的数量为3个。The number of the threaded
过冷器的存在使得本发明的换热效率更进一步提高了。The existence of the subcooler further improves the heat exchange efficiency of the present invention.
压缩机可以为柔性涡旋压缩机、螺杆压缩机、半封式活塞压缩机等。The compressor may be a flexible scroll compressor, a screw compressor, a semi-hermetic piston compressor, and the like.
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CN115031423B (en) * | 2022-06-10 | 2023-04-11 | 浙江青风环境股份有限公司 | Water chilling unit with vortex disc type micro-channel heat exchanger |
CN115371433B (en) * | 2022-10-26 | 2023-01-31 | 河南天利热工装备股份有限公司 | Quick cooling industrial furnace |
CN116538710B (en) * | 2023-07-06 | 2023-09-29 | 江苏达达节能科技有限公司 | Sleeve evaporation type condenser |
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JPH029439A (en) | 1988-03-21 | 1990-01-12 | Internatl Fuel Cells Corp | Heater for a catalyst tube for rerorming a fuel |
FR2801098A1 (en) * | 1999-11-12 | 2001-05-18 | Rubis Concept | Heat exchanger for pressed grapes has pipe section containing inner duct for heat exchange fluid, outer shell and insulating sleeve |
CN2449172Y (en) * | 2000-10-25 | 2001-09-19 | 于奎明 | Sleeve pipe type heat-exchanger for air conditioner set |
CN2510814Y (en) * | 2001-12-26 | 2002-09-11 | 台湾雷德斯减废科技有限公司 | Heat exchanger |
CN201297802Y (en) * | 2008-08-19 | 2009-08-26 | 郑引河 | Flexible diversion double spiral sleeve type heat exchanger |
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2008
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Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH029439A (en) | 1988-03-21 | 1990-01-12 | Internatl Fuel Cells Corp | Heater for a catalyst tube for rerorming a fuel |
FR2801098A1 (en) * | 1999-11-12 | 2001-05-18 | Rubis Concept | Heat exchanger for pressed grapes has pipe section containing inner duct for heat exchange fluid, outer shell and insulating sleeve |
CN2449172Y (en) * | 2000-10-25 | 2001-09-19 | 于奎明 | Sleeve pipe type heat-exchanger for air conditioner set |
CN2510814Y (en) * | 2001-12-26 | 2002-09-11 | 台湾雷德斯减废科技有限公司 | Heat exchanger |
CN201297802Y (en) * | 2008-08-19 | 2009-08-26 | 郑引河 | Flexible diversion double spiral sleeve type heat exchanger |
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Application publication date: 20090603 Assignee: Henan Baotianman air conditioning equipment Co. Assignor: Zheng Yinhe|Xing Qingxin Contract record no.: 2015990000322 Denomination of invention: Flexible fluid-directing double-spiral-sleeve type heat exchanger Granted publication date: 20120725 License type: Exclusive License Record date: 20150514 |
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