CN111998601A - Cooling device and method for circulating water - Google Patents
Cooling device and method for circulating water Download PDFInfo
- Publication number
- CN111998601A CN111998601A CN202010847801.7A CN202010847801A CN111998601A CN 111998601 A CN111998601 A CN 111998601A CN 202010847801 A CN202010847801 A CN 202010847801A CN 111998601 A CN111998601 A CN 111998601A
- Authority
- CN
- China
- Prior art keywords
- water
- cooling
- tower
- air
- circulating water
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 363
- 238000001816 cooling Methods 0.000 title claims abstract description 286
- 238000000034 method Methods 0.000 title claims abstract description 35
- 239000000498 cooling water Substances 0.000 claims abstract description 103
- 230000033228 biological regulation Effects 0.000 claims abstract description 3
- 230000008569 process Effects 0.000 claims description 22
- 239000007921 spray Substances 0.000 claims description 21
- 230000008859 change Effects 0.000 claims description 15
- 230000000903 blocking effect Effects 0.000 claims description 10
- 239000012530 fluid Substances 0.000 claims description 9
- 230000007423 decrease Effects 0.000 claims description 7
- 238000009826 distribution Methods 0.000 claims description 7
- 239000012528 membrane Substances 0.000 claims 1
- 230000000694 effects Effects 0.000 abstract description 22
- 238000005507 spraying Methods 0.000 abstract description 9
- 238000004519 manufacturing process Methods 0.000 abstract description 5
- 238000010276 construction Methods 0.000 abstract description 4
- 238000004064 recycling Methods 0.000 abstract description 3
- 239000008235 industrial water Substances 0.000 abstract description 2
- 230000001105 regulatory effect Effects 0.000 abstract 2
- 230000001276 controlling effect Effects 0.000 abstract 1
- 238000001704 evaporation Methods 0.000 description 15
- 230000008020 evaporation Effects 0.000 description 15
- 230000002093 peripheral effect Effects 0.000 description 12
- 238000009423 ventilation Methods 0.000 description 10
- 230000008901 benefit Effects 0.000 description 5
- 238000010586 diagram Methods 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- 238000010521 absorption reaction Methods 0.000 description 3
- 230000005611 electricity Effects 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 238000012546 transfer Methods 0.000 description 3
- 230000005494 condensation Effects 0.000 description 2
- 238000009833 condensation Methods 0.000 description 2
- 239000002826 coolant Substances 0.000 description 2
- 230000007797 corrosion Effects 0.000 description 2
- 238000005260 corrosion Methods 0.000 description 2
- 230000005855 radiation Effects 0.000 description 2
- 230000000630 rising effect Effects 0.000 description 2
- 238000004544 sputter deposition Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000000295 complement effect Effects 0.000 description 1
- 230000002596 correlated effect Effects 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 230000007257 malfunction Effects 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 238000005272 metallurgy Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000009418 renovation Methods 0.000 description 1
- 238000012827 research and development Methods 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
Images
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25D—REFRIGERATORS; COLD ROOMS; ICE-BOXES; COOLING OR FREEZING APPARATUS NOT OTHERWISE PROVIDED FOR
- F25D17/00—Arrangements for circulating cooling fluids; Arrangements for circulating gas, e.g. air, within refrigerated spaces
- F25D17/02—Arrangements for circulating cooling fluids; Arrangements for circulating gas, e.g. air, within refrigerated spaces for circulating liquids, e.g. brine
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28C—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA COME INTO DIRECT CONTACT WITHOUT CHEMICAL INTERACTION
- F28C1/00—Direct-contact trickle coolers, e.g. cooling towers
- F28C1/14—Direct-contact trickle coolers, e.g. cooling towers comprising also a non-direct contact heat exchange
-
- 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
- F28D1/00—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators
- F28D1/02—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid
- F28D1/04—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits
- F28D1/053—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits the conduits being straight
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F1/00—Tubular elements; Assemblies of tubular elements
- F28F1/10—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses
- F28F1/12—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element
- F28F1/24—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element and extending transversely
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28C—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA COME INTO DIRECT CONTACT WITHOUT CHEMICAL INTERACTION
- F28C1/00—Direct-contact trickle coolers, e.g. cooling towers
- F28C2001/006—Systems comprising cooling towers, e.g. for recooling a cooling medium
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Thermal Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Geometry (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
Description
技术领域technical field
本发明涉工业过程中冷却用的循环水升温后的降温的循环水的冷却装置与方法,特别是对工业过程中的循环冷却水的降温和蒸汽的冷凝,利用空气间接冷却和凉水塔的空气直接冷却串联克服传统凉水塔消耗水量大而空气间接冷却换热能力低的问题,保证循环水降温循环利用和蒸汽冷凝的效果,又达到减少装置规模、节省装置投资和运行费用的目的,属于工业水循环、工业冷却和空气冷却节水领域。The invention relates to a cooling device and method for cooling circulating water after the circulating water used for cooling in industrial processes is heated, especially for the cooling of circulating cooling water and the condensation of steam in industrial processes, indirect cooling by air and the use of air in cooling water towers Direct cooling in series overcomes the problem of large water consumption in traditional cooling towers and low heat exchange capacity for indirect air cooling, ensures the effect of circulating water cooling and recycling and steam condensation, and achieves the purpose of reducing device scale, saving device investment and operating costs, and belongs to the industry. Water circulation, industrial cooling and air cooling water saving fields.
背景技术Background technique
在电力、冶金、化工等很多工业生产过程中,大量的水作为冷却介质对生产设备和产品进行冷却。作为冷却介质的冷却水在工艺冷却过程中自身升温后必须降低温度才能循环再使用。循环水的降温常采用在凉水塔中循环水与空气直接接触降温的凉水塔方式,也有采用闭路循环间接冷却的方法,间接冷却要通过管外喷水或空气冷却。凉水塔式的直接冷却和喷水降温的间接冷却均是通过水蒸发吸热实现,并且还有水滴被空气夹带损失,所以,需要消耗大量的水。采用翅片管的空气间接冷却可节省大量工业用水,但由于空气的传热系数远小于水蒸发的传热系数,所以,冷却设备庞大,会导致设备投资过大。通常凉水塔方式冷却的耗水量与循环水的降温幅度呈正相关,降温幅度减少耗水也会减少;空气间接冷却的空冷器的降温能力是管内流动的水温与大气温度差的正函数,降温过程中循环水温度高的流体段的传热推动力温差大,冷却能力强,反之亦然。另外,夏季大气温度高的情况下,凉水塔能够较好满足冷却要求,而翅片管空气间接冷却却很难满足冷却要求,而在春秋冬季大气温度降低后,翅片管的冷却能力大幅升高,而凉水塔的耗水降低却很少。即单独使用凉水塔冷却在低温时段也同样耗水多,单独使用翅片管冷却在高温时段由于冷却能力不足不能满足要求且投资费用高。上世纪八十年代德国科技工作者也曾经探索和试行过翅片管空气间接冷却和凉水塔空气直接冷却的串联使用的技术和应用,但未能成为普及应用的技术推广实施。其原因是多方面的,但最基本的原因还在于工艺构成和设施结构的深度研究和开发不足,系统不尽合理,未能充分发挥两者的互补优势,导致设备投资较大,投资性价比不高,以及适应工业应用实际工况的能力不足。因此,探索一种夏季利用凉水塔冷却确保冷却效果,春秋冬利用空冷器冷却减少冷却耗水,即达到适度减少水耗,又能适度抑制设备投资费用的技术路线、配套系统及装置对于电力、冶金化工等行业的节水增效,特别是对已有的凉水塔冷却系统的改造就显得尤为重要。In many industrial production processes such as electric power, metallurgy, and chemical industry, a large amount of water is used as a cooling medium to cool production equipment and products. The cooling water used as the cooling medium must be reduced in temperature before it can be recycled and reused after heating itself up in the process cooling process. The cooling of circulating water often adopts the cooling tower method in which the circulating water and the air are directly contacted to cool down in the cooling water tower, and there are also closed-circuit indirect cooling methods. The direct cooling of the cooling tower type and the indirect cooling of the water spray cooling are realized by the heat absorption of water evaporation, and the water droplets are also entrained and lost by the air, so a large amount of water needs to be consumed. Air indirect cooling with finned tubes can save a lot of industrial water, but since the heat transfer coefficient of air is much smaller than that of water evaporation, the large cooling equipment will lead to excessive equipment investment. Usually, the water consumption of cooling tower cooling is positively correlated with the cooling rate of circulating water, and the reduction of cooling rate will also reduce water consumption; The heat transfer driving force temperature difference of the fluid section with high circulating water temperature is large, and the cooling capacity is strong, and vice versa. In addition, when the atmospheric temperature is high in summer, the cooling tower can better meet the cooling requirements, while the indirect cooling of the finned tube air is difficult to meet the cooling requirements. After the atmospheric temperature decreases in the spring, autumn and winter, the cooling capacity of the finned tube increases significantly. high, and the water consumption of the cooling tower is reduced very little. Even if the cooling tower is used alone, it also consumes a lot of water in the low temperature period. The finned tube cooling alone cannot meet the requirements and the investment cost is high due to the insufficient cooling capacity in the high temperature period. In the 1980s, German scientific and technological workers also explored and tried the technology and application of the tandem use of finned tube air indirect cooling and cooling water tower air direct cooling, but it failed to become a popularized and applied technology. There are many reasons for this, but the most basic reason is that the in-depth research and development of process composition and facility structure is insufficient, the system is not reasonable, and the complementary advantages of the two cannot be fully utilized, resulting in large equipment investment and poor investment cost performance. high, and the ability to adapt to the actual working conditions of industrial applications is insufficient. Therefore, explore a technical route, supporting systems and devices that use cooling water tower cooling in summer to ensure the cooling effect, and use air cooler cooling to reduce cooling water consumption in spring, autumn and winter, which can moderately reduce water consumption and moderate equipment investment costs. It is particularly important to save water and increase efficiency in metallurgical and chemical industries, especially the transformation of the existing cooling tower cooling system.
发明内容SUMMARY OF THE INVENTION
本发明的目的在于提供一种可大幅降低投资费用,保障循环水冷却效果又节水的装置和方法。通过高效有机地结合翅片管和凉水塔冷却的特点,构建翅片管与凉水塔串联系统,并将凉水塔喷淋区域在其横截面的投影面上分成能够单独调控的区域,根据大气温度进行喷水调节,并通过翅片管后循环水进入凉水塔水量的调控实现保证冷却要求条件下的最大化的节水;通过翅片管在凉水塔下部进风口位置的设置,并与通风通道的调节能够节省吸风塔的建造费用;通过将空冷器置于面朝北的阴面最大限度地利用大气风力和避免太阳直射,进一步提高了空冷器的效果;翅片管在吸风塔的进风口设置成可移动式避免了吸风塔吸力不够的问题;翅片管翅片间距扩大后风阻降低,确保了吸风塔的吸力的同时也能达到较好的空冷效果。本发明为确保循环水的冷却效果,降低投资费用并达到节水的目的提供了工艺系统、运行模式及装备保障。The purpose of the present invention is to provide a device and method that can greatly reduce investment costs, ensure the cooling effect of circulating water and save water. By efficiently and organically combining the cooling characteristics of finned tubes and cooling water towers, a series system of finned tubes and cooling water towers is constructed, and the spraying area of cooling water towers is divided into areas that can be individually adjusted on the projection plane of its cross-section, according to the atmospheric temperature. The water spray is adjusted, and the maximum water saving under the cooling requirements is guaranteed by the adjustment of the amount of water circulating in the cooling tower after the finned tube. The adjustment can save the construction cost of the suction tower; by placing the air cooler on the shady side facing north to maximize the use of atmospheric wind and avoid direct sunlight, the effect of the air cooler is further improved; The tuyere is set to be movable to avoid the problem of insufficient suction of the suction tower; after the fin spacing of the finned tube is enlarged, the wind resistance is reduced, which ensures the suction of the suction tower and also achieves a better air cooling effect. The invention provides a process system, an operation mode and equipment guarantee for ensuring the cooling effect of the circulating water, reducing the investment cost and achieving the purpose of saving water.
本发明的技术采用如下方案实现:The technology of the present invention adopts the following scheme to realize:
循环水的冷却装置,其特征是所述装置至少包括实现循环水的间接空气冷却过程的空冷器、及实现循环水的直接空气冷却过程的凉水塔;空冷器至少包括由被冷却流体在其内部流通的流体管和与该流体管外侧相连接的间隔设置的片状薄板构成的翅片所组成的翅片管,翅片及流体管外壁与流通的空气接触;凉水塔至少包括吸风塔和吸风塔上部设置的循环水喷淋器,吸风塔下部设置进风口,顶部为出风口;空冷器的循环水入口与需要冷却的循环水热水相连接,空冷器的循环水出口与凉水塔的循环水喷淋器入口相连接,凉水塔的循环水出口与循环水用户需水侧相连接;The cooling device for circulating water is characterized in that the device at least includes an air cooler for realizing the indirect air cooling process of the circulating water, and a cooling water tower for realizing the direct air cooling process of the circulating water; A finned tube composed of a circulating fluid pipe and fins formed by spaced sheet-like thin plates connected to the outside of the fluid pipe, the fins and the outer wall of the fluid pipe are in contact with the circulating air; the cooling water tower at least includes a suction tower and The circulating water sprayer is set on the upper part of the suction tower, the air inlet is set on the lower part of the suction tower, and the air outlet is on the top; The circulating water sprinkler inlet of the tower is connected, and the circulating water outlet of the cooling water tower is connected with the water demand side of the circulating water user;
循环水的流动调节采用如下方法进行:The flow regulation of circulating water is carried out as follows:
(1)经过空冷器冷却后的循环水分两部分流动,其中一部分进入凉水塔进一步冷却,其另一部分不经凉水塔冷却,而是与凉水塔冷却后的循环水混合,作为循环水冷水返回工艺系统循环使用,进入凉水塔冷却的水量比例根据大气温度变化通过阀门调节,(1) The circulating water cooled by the air cooler flows in two parts, one part of which enters the cooling water tower for further cooling, and the other part is not cooled by the cooling water tower, but is mixed with the circulating water cooled by the cooling water tower, and returned to the process as circulating water cold water The system is recycled, and the proportion of water entering the cooling tower for cooling is adjusted by the valve according to the change of atmospheric temperature.
或(2)凉水塔上部的循环水喷淋器在吸风塔横截面的投影面上分成两个以上喷水区域,各个喷水区域能够独自控制进水,随大气温度升高喷水区域喷水个数增加,随大气温度降低喷水区域喷水个数减少,Or (2) the circulating water sprinkler on the upper part of the cooling water tower is divided into two or more water spray areas on the projection surface of the cross section of the suction tower. The number of water increases, and as the atmospheric temperature decreases, the number of water sprays in the water spray area decreases.
或所述(1)和(2)同时采用。Or the above (1) and (2) can be used simultaneously.
所述装置,其特征是所述空冷器的翅片管设置在吸风塔下部的进风口,空气穿过空冷器翅片空间后从进风口进入吸风塔并向上流动最后从出风口排出。The device is characterized in that the finned tube of the air cooler is arranged at the air inlet at the lower part of the suction tower, and the air enters the suction tower from the air inlet after passing through the fin space of the air cooler, flows upward and finally is discharged from the air outlet.
所述装置,其特征是所述吸风塔底部的空冷器的翅片管出风口侧相距一定距离处设置有挡水帘,挡水帘由丝网或板构成,挡水帘垂直于水平面设置或与水平面倾斜设置。The device is characterized in that a water blocking curtain is arranged at a certain distance from the air outlet side of the finned tube of the air cooler at the bottom of the suction tower. Or set inclined to the horizontal plane.
所述装置,其特征是所述在吸风塔下部的进风口设置的空冷器为可移动式结构,在需要的工况下将其设置在进风口,空气穿过空冷器翅片间的空间,在不需要的工况下,可将空冷器移动离开进风口位置。The device is characterized in that the air cooler arranged at the air inlet at the lower part of the suction tower is a movable structure, and is arranged at the air inlet under required working conditions, and the air passes through the space between the fins of the air cooler. , In unneeded conditions, the air cooler can be moved away from the air inlet position.
所述装置,其特征是所述空冷器与凉水塔相邻设置,空冷器设置在空冷塔内,在空冷塔顶部设置有引风机,由引风机吸引空气穿过空冷器翅片空间,之后从其顶部排出。The device is characterized in that the air cooler is arranged adjacent to the cooling water tower, the air cooler is arranged in the air cooling tower, and an induced draft fan is arranged on the top of the air cooling tower, and the induced draft fan attracts air through the fin space of the air cooler, and then flows from the air cooler. Its top is discharged.
所述装置,其特征是所述空冷器在所述空冷塔下部设置,与凉水塔的吸风塔下部的进风口设置通过位置移动进行切换。The device is characterized in that the air cooler is arranged at the lower part of the air cooling tower, and is switched with the setting of the air inlet at the lower part of the suction tower of the cooling water tower through position movement.
所述装置,其特征在于所述装置至少包括实现循环水的间接空气冷却过程的空冷器、实现循环水间接冷却的直立冷却管及实现循环水的直接空气冷却过程的凉水塔;空冷器循环水入口与需要冷却的循环水热水相连接,空冷器循环水出口与直立冷却管循环水入口相连接,直立冷却管循环水出口与凉水塔循环水喷淋器入口相连接,凉水塔循环水出口与循环水用户需水侧相连接;直立冷却管设置于凉水塔底部,直立冷却管顶部设置有布水器,通过布水器形成沿直立冷却管外壁向下流动的水膜,布水器的布水能够根据大气温度变化调节开启。The device is characterized in that the device includes at least an air cooler for realizing the indirect air cooling process of circulating water, a vertical cooling pipe for realizing the indirect cooling of circulating water, and a cooling water tower for realizing the direct air cooling process of circulating water; The inlet is connected to the circulating water and hot water to be cooled, the circulating water outlet of the air cooler is connected to the circulating water inlet of the vertical cooling pipe, the circulating water outlet of the vertical cooling pipe is connected to the inlet of the circulating water sprayer of the cooling water tower, and the circulating water outlet of the cooling water tower is connected. It is connected with the water demand side of circulating water users; the vertical cooling pipe is arranged at the bottom of the cooling water tower, and the top of the vertical cooling pipe is provided with a water distributor, through which a water film flowing down along the outer wall of the vertical cooling pipe is formed. The water distribution can be adjusted and opened according to the change of atmospheric temperature.
所述装置,其特征是所述空冷器的翅片间距离在4~8mm之间。The device is characterized in that the distance between the fins of the air cooler is between 4 and 8 mm.
应用所述循环水的冷却装置的方法,其特征是在吸风塔下部进风口分为两部分进风区间,一部分为设置空冷器的空冷器进风区间,另一部分为没有设置空冷器的通道进风区间;通道进风区间为可调节开闭度的结构,随大气温度的变化实施开闭度的调节。The method of applying the cooling device for circulating water is characterized in that the air inlet at the lower part of the suction tower is divided into two parts of the air inlet section, one part is the air inlet section of the air cooler with the air cooler, and the other part is the channel without the air cooler. Air inlet section; the air inlet section of the channel is a structure that can adjust the opening and closing degree, and the opening and closing degree can be adjusted with the change of atmospheric temperature.
应用所述循环水的冷却装置的方法,其特征是在吸风塔下部进风口的面朝北的背阴面设置空冷器,面朝南的向阳面为没有设置空冷器的通道进风区间;通道进风区间采用可调节开闭度的结构,随大气温度的变化实施开闭度的调节。The method of applying the cooling device for circulating water is characterized in that an air cooler is arranged on the shady side facing north of the air inlet at the lower part of the suction tower, and the sunny side facing south is a passage air inlet section without an air cooler; The air inlet section adopts a structure that can adjust the opening and closing degree, and the opening and closing degree is adjusted with the change of the atmospheric temperature.
具体说明如下:The specific instructions are as follows:
实现循环水的冷却是通过空气间接冷却的空冷器与空气直接冷却的凉水塔串联的方式进行。循环水热水从空冷器流体管循环水入口进入,经过空冷器与空气的间接冷却换热带走热量,使管内流通的循环水降温,后从空冷器流体管循环水出口排出,再从凉水塔的循环水淋水器入口进入凉水塔并淋水而下与上升的空气直接接触换热,被进一步冷却的循环水落到凉水塔底部,作为循环水冷水返回用户循环水用。循环水在高温度段由空气间接冷却传热推动力大,换热效率高,降低了进入凉水塔的循环水的温度,降低了凉水塔的冷却负荷,使其蒸发量减少;同时,在夏季大气温度高的时段,单靠间接冷却的空冷器不能满足冷却要求的情况下,通过凉水塔的空气直接冷却能够比较容易地达到循环水的冷却要求。由于大气温度变化较大,对循环水的冷却能力也波动很大,通过空冷器冷却后的水的温度也波动较大,在大气温度低的时段通过进入凉水塔的阀门调节可以少量送入凉水塔,进一步冷却后与只通过空冷器冷却的循环水混合作为循环水冷水返回用户循环使用,由此减少了凉水塔中水的损耗。随着大气温度的变化,通过调节送往凉水塔的水量实现保证循环水冷水温度的条件下最大限度地减少凉水塔的水蒸发损耗,达到节水的目的。在严冬极低温时,还可以关闭进入凉水塔的阀门,只通过空冷器实现冷却。另外,由于循环水热水通过空冷器的冷却温度降低后在凉水塔中需要的冷却强度降低,采用在凉水塔中横截面投影面上分区域的控制喷淋可以根据进入水量的多少及温度高低,确定喷淋面积,进水温度低水量少的情况下,缩小喷淋面积,减少喷淋水与空气的接触面积可以降低蒸发量和夹带量,减少水的损耗。通过根据大气温度调节进入凉水塔的水量和喷淋面积技术手段的单独使用或联合使用,能够最大限度的减少水的损耗。The cooling of circulating water is realized by connecting an air cooler with indirect air cooling and a cooling water tower with direct air cooling in series. The circulating water and hot water enter from the circulating water inlet of the fluid pipe of the air cooler, and the heat is removed by the indirect cooling and exchanging heat between the air cooler and the air, so as to cool the circulating water circulating in the pipe, and then discharged from the circulating water outlet of the fluid pipe of the air cooler, and then from the cold water. The inlet of the circulating water shower of the tower enters the cooling water tower and sprays water down and directly contacts with the rising air to exchange heat. The further cooled circulating water falls to the bottom of the cooling water tower and returns to the user as circulating water cold water for circulating water. In the high temperature section, the circulating water is indirectly cooled by the air, and the heat transfer has a large driving force and high heat exchange efficiency, which reduces the temperature of the circulating water entering the cooling water tower, reduces the cooling load of the cooling water tower, and reduces the evaporation; at the same time, in summer When the atmospheric temperature is high, when the indirect cooling air cooler alone cannot meet the cooling requirements, the direct cooling of the air through the cooling water tower can easily meet the cooling requirements of the circulating water. Due to the large change in atmospheric temperature, the cooling capacity of the circulating water also fluctuates greatly, and the temperature of the water cooled by the air cooler also fluctuates greatly. During the period of low atmospheric temperature, a small amount of cold water can be fed by adjusting the valve entering the cooling water tower. The tower, after further cooling, is mixed with the circulating water cooled only by the air cooler and returned to the user as circulating water cold water for recycling, thereby reducing the loss of water in the cooling tower. With the change of atmospheric temperature, the water evaporation loss of the cooling tower can be minimized under the condition of ensuring the cold water temperature of the circulating water by adjusting the amount of water sent to the cooling tower, so as to achieve the purpose of water saving. In severe winter and extremely low temperature, the valve entering the cooling tower can also be closed, and cooling is only achieved through the air cooler. In addition, since the cooling intensity of the circulating water and hot water in the cooling tower decreases after the cooling temperature of the circulating water and hot water passes through the air cooler, the use of sub-regional control spray on the cross-sectional projection surface of the cooling water tower can be based on the amount of water entering and the temperature. , Determine the spray area, when the inlet water temperature is low and the water volume is low, reducing the spray area and reducing the contact area between the spray water and the air can reduce the amount of evaporation and entrainment, and reduce the loss of water. By adjusting the amount of water entering the cooling tower and the technical means of spraying area alone or in combination according to the atmospheric temperature, the loss of water can be minimized.
在循环水的冷却设备和工程中,依靠自然抽风的吸风塔的高度一般达到100m以上,依靠风机抽风的凉水塔的塔高度虽然不高但需要配置风机,其设备费都比较高,因此降低吸风设备的投资,特别是现有凉水塔的改造,增设空冷器的情况下,抑制设备投资费用,提高投资效益就成为技术方案和项目可行与否的重要因素。本发明通过将空冷器的翅片管设置在吸风塔下部的进风口,空气穿过空冷器翅片空间后从进风口进入吸风塔并向上流动最后从出风口排出的设备构成,可以充分利用吸风塔的吸风作用达到空冷器的通风冷却,大幅降低设备投资。但是,由于空冷器设置在吸风塔的空气进口处,会增加吸风塔的阻力,如果设置不当会影响吸风塔的吸风能力。因此,本发明采用了空冷器翅片管移动式设置方式,即在大气温度高主要靠凉水塔冷却时,同时大气温度升高导致抽吸力降低的情况下,可以将从吸风塔进风口移开,只依靠凉水塔冷却;当大气温度降低后,吸风塔吸风能力提高后将翅片管在移至吸风塔进风口,进行空冷器冷却,既保证了吸风能力,又能发挥空冷器冷却与凉水塔冷却的优势组合,保证了运行的可靠性。In the cooling equipment and engineering of circulating water, the height of the suction tower that relies on natural ventilation generally reaches more than 100m. Although the height of the cooling tower that relies on fan ventilation is not high, it needs to be equipped with a fan, and its equipment costs are relatively high, so it is reduced. The investment in air suction equipment, especially the renovation of existing cooling towers and the addition of air coolers, reduces equipment investment costs and improves investment returns. It has become an important factor for the feasibility of technical solutions and projects. In the present invention, the finned tube of the air cooler is arranged at the air inlet at the lower part of the suction tower, and the air passes through the fin space of the air cooler and enters the suction tower from the air inlet, flows upward and finally is discharged from the air outlet. The ventilation and cooling of the air cooler is achieved by the suction effect of the suction tower, which greatly reduces the equipment investment. However, since the air cooler is set at the air inlet of the suction tower, it will increase the resistance of the suction tower. If it is not set properly, it will affect the suction capacity of the suction tower. Therefore, the present invention adopts the movable arrangement mode of the finned tubes of the air cooler, that is, when the atmospheric temperature is high and the cooling water tower is mainly used for cooling, and the suction force is reduced due to the increase of the atmospheric temperature, the air inlet of the suction tower can be used. Move it away, and only rely on the cooling water tower for cooling; when the atmospheric temperature is lowered, the suction capacity of the suction tower is improved, and the finned tube is moved to the air inlet of the suction tower for cooling by the air cooler, which not only ensures the suction capacity, but also The combination of the advantages of air cooler cooling and cooling water tower cooling ensures the reliability of operation.
空冷器的翅片管设置在吸风塔底部进风口,会被吸风塔上部喷淋落下的水滴溅射沾水,造成翅片管的腐蚀,在大气温度很低的情况下还有可能结冰,造成设备运行故障。通过在凉水塔底部的翅片管出风侧设置挡水帘,能够很好地解决水滴溅射造成的翅片管沾水。挡水帘与翅片管相隔一定距离既可以阻挡水滴飞溅到翅片管,又不影响翅片管的出风流动。同时,挡水帘与水平面倾斜设置或将挡水帘的上部制成向外倾斜的结构既可以扩大挡水帘与翅片管之间的距离保证其不影响翅片管出风流动,又能最大限度地拦截上部的落水。挡水帘可以是丝网材料构成也可以是板状材料构成,丝网材料要求丝网孔径小于1mm以下,即能够阻挡水滴溅射到翅片管。The finned tube of the air cooler is set at the air inlet at the bottom of the suction tower, and will be splashed and stained by the water droplets sprayed from the upper part of the suction tower, causing corrosion of the finned tube. ice, causing equipment malfunction. By setting a water blocking curtain on the air outlet side of the finned tube at the bottom of the cooling water tower, the finned tube caused by water drop sputtering can be well solved. A certain distance between the water blocking curtain and the finned tube can not only prevent water droplets from splashing on the finned tube, but also does not affect the air flow of the finned tube. At the same time, the water curtain is inclined to the horizontal plane or the upper part of the water curtain is made into an outwardly inclined structure, which can not only expand the distance between the water curtain and the finned tube, but also ensure that it does not affect the air flow of the finned tube. Maximum interception of falling water from the upper part. The water curtain can be made of a wire mesh material or a plate-shaped material. The wire mesh material requires that the aperture of the wire mesh is less than 1 mm, that is, it can prevent water droplets from sputtering to the finned tube.
实现循环水的间接空气冷却过程的空冷器为实现循环水间接冷却的直立冷却管及翅片管串联使用的设备,循环水热水先翅片管初步冷却后再进入直立冷却管,经过直立冷却管冷却后送入凉水塔循环水喷淋器入口,再通过凉水塔冷却后作为循环水冷水送往用户使用。直立冷却管设置于凉水塔底部,直立冷却管顶部设置有布水圈,通过布水圈形成沿直立冷却管外壁向下流动的水膜,布水圈的布水能够根据大气温度变化调节开启。直立冷却管作为可以进行水膜蒸发冷却也可通过不布水直接由空气热传导冷却。还可在大气温度低的时段,单靠翅片管冷却能力不足,用凉水塔冷却又耗水,还要往位置很高的喷淋器送水消耗动力,这种情况下利用翅片管与直立冷却管的水膜蒸发冷却可以实现节水节电的冷却和运行。The air cooler that realizes the indirect air cooling process of the circulating water is a device used in series with the vertical cooling tube and the finned tube to realize the indirect cooling of the circulating water. The circulating water and hot water are initially cooled by the finned tube before entering the vertical cooling tube. After cooling, it is sent to the inlet of the circulating water sprayer of the cooling water tower, and then cooled by the cooling water tower and sent to the user as circulating water cold water. The upright cooling pipe is arranged at the bottom of the cooling water tower, and the top of the upright cooling pipe is provided with a water distribution ring, through which a water film flowing down along the outer wall of the upright cooling pipe is formed. The vertical cooling pipe can be used for water film evaporative cooling or direct air heat conduction cooling without water distribution. In the period of low atmospheric temperature, the cooling capacity of the finned tube alone is insufficient, and the cooling of the cooling tower consumes water, and the power is consumed by sending water to the sprinkler at a high position. In this case, the finned tube and the vertical The water film evaporative cooling of the cooling pipe can realize the cooling and operation of saving water and electricity.
另外,在自然吸风的凉水塔内,抽吸的空气量主要受气温的影响,通常空气量的变化不很大,而当水的喷淋量大幅减少后,吸湿的空气相对于水量的比例会大幅增加,对单位喷淋水量而言其耗水量会显著增加。这种情况下,直立冷却管冷却的水膜蒸发则与空气的接触面积相对少很多,接触时间也短且不飞散,耗水就会少很多,而冷却能力却比较大,避免了大量空气的吸湿与夹带耗水。而直立冷却管相对于翅片管的设备成本又低的比较多,投资对冷却效果的性价比比较高,特别是气温低,寒冷天时间长的地域其效果就更为明显,对于规模大的循环冷却系统而言优势和必要性就更显突出。In addition, in the cooling water tower with natural suction, the amount of air sucked is mainly affected by the temperature, and the change of the amount of air is usually not large. When the spray amount of water is greatly reduced, the ratio of hygroscopic air to water will increase significantly, and the water consumption per unit of spray water will increase significantly. In this case, the evaporation of the water film cooled by the vertical cooling pipe has a relatively small contact area with the air, the contact time is also short and does not scatter, the water consumption will be much less, but the cooling capacity is relatively large, avoiding a large amount of air. Hygroscopic and entrained water consumption. Compared with the finned tube, the equipment cost of the vertical cooling tube is much lower, and the cost-effectiveness of the investment on the cooling effect is relatively high, especially in areas with low temperature and long cold days, the effect is more obvious. The advantages and necessity of the cooling system are even more prominent.
空冷器的翅片管还可以与凉水塔相邻设置,空冷器设置在空冷塔内,在空冷塔顶部设置有引风机,由引风机吸引空气穿过空冷器翅片空间,之后从其顶部排出。这样翅片管可以独立运行,对于规模小的冷却系统,更为简便。也可以空冷器在空冷塔下部设置,与凉水塔的吸风塔下部的进风口设置通过位置移动进行切换。这样在大气温度低的时段可以停止空冷塔顶部抽风机的运行,做到节省电力,降低运行成本。The finned tubes of the air cooler can also be arranged adjacent to the cooling water tower. The air cooler is arranged in the air cooling tower, and an induced draft fan is arranged at the top of the air cooling tower. The induced draft fan attracts air through the fin space of the air cooler and then discharges from the top . In this way, the finned tubes can operate independently, which is more convenient for small-scale cooling systems. It is also possible to set the air cooler at the lower part of the air cooling tower, and switch with the setting of the air inlet at the lower part of the suction tower of the cooling water tower by moving the position. In this way, the operation of the exhaust fan at the top of the air cooling tower can be stopped during the period of low atmospheric temperature, so as to save electricity and reduce operating costs.
由于翅片管设置在吸风塔底部的进风口会增加吸风塔阻力,设置不当会影响吸风塔运行,通过将空冷器的翅片间距离由通常采用的3.2mm扩大到4~8mm之间,会显著降低其空气阻力,而翅片的冷却能力降低又不多,能够很好地解决吸风塔吸力和翅片管阻力不匹配的矛盾。Since the air inlet of the finned tube at the bottom of the suction tower will increase the resistance of the suction tower, improper setting will affect the operation of the suction tower. It will significantly reduce its air resistance, and the cooling capacity of the fins will not be reduced much, which can well solve the contradiction between the suction tower suction and the resistance of the finned tubes.
在大型的自然吸风塔系统中,进风口面积比较大,随大气温度的变化吸风能力和冷却能力变化也大。进风口全部设置翅片管则投资成本增加较多,而只在进风口的一部分设置,则会造成阻力系数不同通过翅片管的空气严重不足,严重影响其冷却效果。将吸风塔下部进风口分为两部分进风区间,一部分为设置空冷器的空冷器进风区间,另一部分为没有设置空冷器的通道进风区间;通道进风区间为可调节开闭度的结构,随大气温度的变化实施开闭度的调节的技术方案能够通过通道进风区间为可调节开闭度调节进风阻力,实现流过翅片管的空气量的调节和保障,保障翅片管冷却能力的发挥。同时,开闭度调节机构设备简单成本也低,采用工业上常规使用的简单设备即可。In a large-scale natural suction tower system, the area of the air inlet is relatively large, and the suction capacity and cooling capacity vary greatly with the change of atmospheric temperature. If all the air inlets are equipped with finned tubes, the investment cost will increase greatly, but if only a part of the air inlets are installed, the air passing through the finned tubes with different resistance coefficients will be seriously insufficient, which will seriously affect the cooling effect. The air inlet at the lower part of the suction tower is divided into two parts, one part is the air inlet area of the air cooler with the air cooler, and the other part is the air inlet area of the channel without the air cooler; the air inlet area of the channel is adjustable opening and closing. The technical scheme of adjusting the opening and closing degree with the change of the atmospheric temperature can adjust the air inlet resistance for the adjustable opening and closing degree through the air inlet section of the channel, realize the adjustment and protection of the air volume flowing through the finned tube, and ensure the fins The cooling capacity of the sheet tube is exerted. At the same time, the opening and closing degree adjusting mechanism is simple in equipment and low in cost, and simple equipment commonly used in the industry can be used.
对于如电厂等的大型循环水冷却凉水塔的直径都很大,自然吸风塔的朝阳面和朝北面所受的风力冲击及受太阳辐射吸热都有明显的差别,特别是我国北方以西北风为主导风向的情况下,在吸风塔下部进风口的面朝北的背阴面设置空冷器,面朝南的向阳面为没有设置空冷器的通道进风区间;通道进风区间为可调节开闭度的结构,随大气温度的变化实施开闭度的调节设置,能够有效地利用西北风的风力进风优势和减少辐射的特点,提高翅片管的冷却效果和作用,以少量的投资得到较大的冷却效果。For large-scale circulating water cooling towers such as power plants, the diameters of the cooling towers are very large, and there are obvious differences in the wind impact and solar radiation heat absorption between the sunny side and the north side of the natural suction tower, especially in the northwest of northern my country. When the wind is the dominant wind direction, an air cooler is installed on the shady side facing north of the air inlet at the lower part of the suction tower, and the sunny side facing south is the air inlet section of the channel without an air cooler; the air inlet section of the channel is adjustable. The structure of the opening and closing degree, the adjustment and setting of the opening and closing degree are implemented with the change of the atmospheric temperature, which can effectively take advantage of the wind inlet advantage of the northwest wind and the characteristics of reducing radiation, improve the cooling effect and function of the finned tube, with a small investment. Get a greater cooling effect.
本发明的有益效果是通过高效有机地结合翅片管空冷器和凉水塔冷却的特点,构建空冷器与凉水塔串联系统,将凉水塔喷淋区域在其横截面的投影面上分成能够单独调控的区域,根据大气温度进行喷水调节,并通过空冷器后循环水进入凉水塔水量的调控实现保证冷却要求条件下的最大化的节水;通过空冷器在凉水塔下部进风口位置的设置,并与通风通道的调节能够节省吸风塔的建造费用而又能实现利用空气冷却的节水;通过在吸风塔底部的翅片管出风口侧相距一定距离处设置挡水帘,既可以阻挡水滴飞溅到翅片管,又不影响翅片管的出风流动;通过间接空气冷却的空冷器、间接冷却的直立冷却管及直接空气冷却凉水塔串联可在大气温度低的时段,克服单靠翅片管冷却能力不足,用凉水塔冷却又耗水,还要往位置很高的喷淋器送水消耗动力,利用翅片管与直立冷却管的水膜蒸发冷却实现节水节电的冷却和运行;通过将空冷器置于面朝北的阴面最大限度地利用大气风力和避免太阳直射,进一步提高了空冷器的效果;空冷器在吸风塔的进风口设置成可移动式避免了吸风塔吸力不够的问题;空冷器翅片间距扩大后风阻降低,确保了吸风塔的吸力的同时也能达到较好的空冷效果。本发明为确保循环水的冷却效果,降低投资费用并达到节水的目的提供了工艺系统、运行模式及装备保障。The beneficial effect of the invention is that by efficiently and organically combining the characteristics of the finned tube air cooler and the cooling water tower, a series system of the air cooler and the cooling water tower is constructed, and the spraying area of the cooling water tower is divided on the projection plane of its cross section into separate controllable In the area, the water spray is adjusted according to the atmospheric temperature, and the water volume of the circulating water entering the cooling tower after the air cooler is adjusted to ensure maximum water saving under the cooling requirements; And the adjustment of the ventilation channel can save the construction cost of the suction tower and realize water saving by using air cooling; by setting a water curtain at a certain distance from the air outlet side of the fin tube at the bottom of the suction tower, it can not only block The water droplets splash on the finned tubes without affecting the air flow of the finned tubes; through the indirect air cooling air cooler, the indirect cooling vertical cooling tube and the direct air cooling cooling tower in series, it can overcome the The cooling capacity of the finned tube is insufficient, and the cooling of the cooling tower consumes water, and the power is consumed by sending water to the sprinkler at a high position. The water film evaporative cooling of the finned tube and the vertical cooling tube is used to realize the cooling and energy saving of water and electricity. Operation; by placing the air cooler on the shady side facing north to maximize the use of atmospheric wind and avoid direct sunlight, the effect of the air cooler is further improved; the air cooler is set to be movable at the air inlet of the suction tower to avoid suction The problem of insufficient tower suction; the air resistance is reduced after the fin spacing of the air cooler is enlarged, which ensures the suction of the suction tower and also achieves a better air cooling effect. The invention provides a process system, an operation mode and equipment guarantee for ensuring the cooling effect of the circulating water, reducing the investment cost and achieving the purpose of saving water.
附图说明Description of drawings
图1:自然吸风通道进风区间调节翅片管与凉水塔串联冷却示意图;Figure 1: Schematic diagram of series cooling between the finned tube and the cooling tower in the air inlet section of the natural suction channel;
图2:自然吸风翅片管移动设置示意图;Figure 2: Schematic diagram of the movement setting of the natural suction finned tube;
图3:翅片管与水膜蒸发直立冷却管及凉水塔串联冷却示意图;Figure 3: Schematic diagram of series cooling between finned tubes and water film evaporation vertical cooling tubes and cooling water towers;
图4:引风机吸风翅片管与引风机吸风凉水塔串联冷却示意图;Figure 4: Schematic diagram of series cooling between the suction fin tube of the induced draft fan and the suction cooling water tower of the induced draft fan;
其中:1-循环水热水,2-翅片管,3-翅片,4-自然吸风塔,5-凉水塔淋水器,6-凉水塔底部水池,7-循环水加压泵,8-循环水冷水,9-凉水塔喷淋器中心区进水控制阀门,10-凉水塔喷淋器外周区进水控制阀门,11-翅片管出水直接回水阀门,12-吸风塔下部通道进风调节窗,13-从凉水塔进风口移出的翅片管,14-翅片管引风机吸风罩,15-翅片管引风机,16-引风机吸风凉水塔,17-凉水塔引风机,18-引风机吸风凉水塔空气进口,19-引风机吸风凉水塔内填料,20-自然吸风塔进风口处翅片管移动方向,21-凉水塔底部回水阀门,22-流向翅片管的空气,23-凉水塔出风口,24-挡水帘,25-直立冷却管,26-直立冷却管布水器,27-环形缝隙布水流路,28-水膜。Among them: 1- circulating water hot water, 2- finned tube, 3- fin, 4- natural suction tower, 5- cooling water tower shower, 6- cooling water tower bottom pool, 7- circulating water pressurized pump, 8- circulating water cold water, 9- water inlet control valve in the central area of the cooling tower sprinkler, 10- water inlet control valve in the outer peripheral area of the cooling tower sprinkler, 11- finned tube outlet water direct return valve, 12- suction tower Lower channel air inlet adjustment window, 13-finned tube removed from the air inlet of the cooling tower, 14-finned tube induced draft fan suction hood, 15-finned tube induced draft fan, 16-induced draft fan suction cooling tower, 17-cooling water Tower induced draft fan, 18- induced draft fan suction cooling tower air inlet, 19- induced draft fan suction cooling water tower packing, 20- natural suction tower fin tube moving direction at the air inlet, 21- cooling water tower bottom return valve, 22- The air flowing to the finned tube, 23-cooling tower air outlet, 24-water curtain, 25-vertical cooling pipe, 26-vertical cooling pipe water distributor, 27-annular gap water distribution flow path, 28-water film.
具体实施方式Detailed ways
实施例1Example 1
本实施例是发电厂自然吸风通道通风区间调节翅片管与凉水塔串联冷却工艺的应用例,如图1所示。从发电厂乏汽冷凝器送来的循环水热水1进入在自然吸风塔4的下部进风口设置的翅片管2,与在吸风塔抽吸作用下穿过翅片3间空间的空气22换热降温后,流出翅片管一部分被送往凉水塔淋水器5从上流下与向上流动的空气接触,水蒸发吸热被冷却后落到凉水塔底部水池6,另一部分水从翅片管流出后直接进入循环水加压泵7的入口与凉水塔底部水池6排出的水混合后送往发电厂乏汽冷凝器进行循环冷却。与翅片管的翅片换热后温度升高的空气进一步与在凉水塔内上升过程中,与淋下的水直接接触并与蒸发的水蒸气一同从凉水塔出风口23排出,进入大气。This embodiment is an application example of the cooling process of adjusting the finned tube and the cooling water tower in series in the ventilation area of the natural suction channel of the power plant, as shown in FIG. 1 . The circulating water and hot water 1 sent from the exhausted steam condenser of the power plant enters the
在大气温度高的时段,关闭翅片管出水直接回水阀门11,经过翅片冷却的循环水全部进入凉水塔,凉水塔喷淋器中心区进水控制阀门9和凉水塔喷淋器外周区进水控制阀门10全开,并全开凉水塔底部回水阀门21,最大能力地冷却循环水;大气温度下降后,部分开启翅片管出水直接回水阀门11和凉水塔底部回水阀门21,一部分循环水直接进入循环水加压泵7的入口与凉水塔底部水池排出的水混合后送往发电厂乏汽冷凝器进行循环冷却,同时关闭凉水塔喷淋器中心区进水控制阀门9,循环水只通过凉水塔喷淋器外周区进水控制阀门10进入凉水塔淋水器外周区进行淋水(或关闭凉水塔喷淋器外周区进水控制阀门10,循环水只通过凉水塔喷淋器中心区进水控制阀门9进入凉水塔淋水器外周区进行淋水),由此,由于进入凉水塔的水量减少,且水温也比循环水热水温度低,减少了循环水的蒸发和夹带损失;当大气温度进一步降低后,全部开启翅片管出水直接回水阀门11,循环水直接进入循环水加压泵7的入口送往发电厂乏汽冷凝器进行循环冷却,同时关闭凉水塔喷淋器中心区进水控制阀门9和凉水塔喷淋器外周区进水控制阀门10及凉水塔底部回水阀门21,停止凉水塔冷却,避免了水在凉水塔中的蒸发和夹带损失,最大限度的节水。During the period of high atmospheric temperature, close the direct return valve 11 of the finned tube outlet water, all the circulating water cooled by the fins enters the cooling water tower, the water inlet control valve 9 in the central area of the cooling tower sprayer and the outer peripheral area of the cooling water tower sprayer The water inlet control valve 10 is fully opened, and the return water valve 21 at the bottom of the cooling tower is fully opened to cool the circulating water to the maximum; , a part of the circulating water directly enters the inlet of the circulating water booster pump 7 and is mixed with the water discharged from the pool at the bottom of the cooling water tower, and then sent to the exhaust steam condenser of the power plant for circulating cooling, and the water inlet control valve 9 in the central area of the cooling water tower sprayer is closed , the circulating water only enters the peripheral area of the cooling tower sprinkler through the water inlet control valve 10 in the outer peripheral area of the cooling tower sprinkler for water spraying (or close the water inlet control valve 10 in the outer peripheral area of the cooling tower sprinkler, and the circulating water only passes through the cooling tower The water inlet control valve 9 in the central area of the shower enters the outer peripheral area of the cooling tower shower for watering), thus, because the amount of water entering the cooling tower is reduced, and the water temperature is also lower than the temperature of the circulating water and the hot water, the circulation water is reduced. Evaporation and entrainment losses; when the atmospheric temperature is further reduced, all open the
在凉水塔空气入口处设置的翅片管的上部设置了通道通风区间,由吸风塔下部通道通风调节窗12调节通道通风区间开闭度,随大气温度的变化实施开闭度的调节,大气温度高时开启吸风塔下部通道进风调节窗12,大量的空气进入凉水塔,大气温度很低时关闭吸风塔下部通道通风调节窗12,空气完全从翅片管穿过,进行循环水的间接冷却。翅片管的翅片间距离为4.2mm,与传统的翅片管将距离3.2mm相比,空气流通阻力显著降低,保证了凉水塔的自然吸风塔在夏天的吸力,能够克服翅片管带来的阻力,保证了冷却系统的正常进行。A passage ventilation section is set on the upper part of the finned tube set at the air inlet of the cooling tower, and the opening and closing degree of the passage ventilation section is adjusted by the passage
在凉水塔底部设置有挡水帘24,挡水帘由丝网构成,挡水帘向外倾斜于水平面,由此阻挡了凉水塔落下的水向翅片管的飞溅,避免了翅片管的腐蚀和结冰,同时还不影响穿过翅片管的空气的流通。A
通过翅片管空气间接冷却与凉水塔空气直接冷却的串联冷却,实现了既保证循环水的冷却效果,又能达到节水的目的;将凉水塔淋水区域在其横截面的投影面上分成能够单独调控的区域,根据大气温度进行喷水调节,并通过翅片管后循环水进入凉水塔水量的调控实现保证冷却要求条件下的最大化的节水;通过翅片管在凉水塔下部进风口位置的设置,并与通风通道的调节能够利用自然吸风式凉水塔,节省翅片管吸风塔的建造费用;通过在吸风塔底部的翅片管出风口侧设置挡水帘,既可以阻挡水滴飞溅到翅片管,又不影响翅片管的出风流动。在北方寒冷地区可以实现以完全翅片管空气冷却投资的15%达到与凉水塔方式耗水相比节水30%以上的效果。Through the series cooling of the finned tube air indirect cooling and the cooling water tower air direct cooling, the cooling effect of the circulating water can be ensured, and the purpose of water saving can be achieved; In the area that can be adjusted separately, the water spray is adjusted according to the atmospheric temperature, and the water volume of the circulating water entering the cooling tower after the finned tube is adjusted to ensure maximum water saving under the cooling requirements; the finned tube enters the lower part of the cooling tower The setting of the position of the air outlet and the adjustment of the ventilation channel can use the natural suction cooling tower to save the construction cost of the finned tube suction tower; It can prevent water droplets from splashing to the finned tube without affecting the air flow of the finned tube. In the northern cold region, it can achieve the effect of saving more than 30% of water compared with the water consumption of the cooling tower method with 15% of the investment in complete finned tube air cooling.
实施例2Example 2
本实施例与实施例1基本相同,所不同的是在自然吸风塔空气入口处不设通道进风区间调节,而是如图2所示,在盛夏温度很高的时段,将可移动翅片管25,从自然吸风塔空气入口处沿吸风塔进风口处翅片管移动方向20移开,成为不通水的离开凉水塔进风口的翅片管13,自然吸风塔空气入口如同传统的自然吸风凉水塔进风,保证了凉水塔的吸力。在大气温度降低,空气冷却能力上升,吸风塔吸风能力也提高后,再将翅片管沿吸风塔进风口处翅片管移动方向20移回到自然吸风塔空气入口处,对翅片管内通水,实施空气对循环水热水的间接冷却,并与凉水塔串联进行循环水的冷却,达到节水目的。在应用移动式翅片管冷却的方式下,可以将翅片管的翅片间距离按通常设计的3.2mm制作。挡水帘由板状材料构成,挡水帘垂直于水平面于水平面设置(图中未标示)。This embodiment is basically the same as Embodiment 1, the difference is that there is no channel air inlet interval adjustment at the air inlet of the natural suction tower, but as shown in Figure 2, when the temperature is very high in midsummer, the movable fins are The
应用移动式翅片管冷却的方式对于在温度不太冷的地区可以实现以完全翅片管空气冷却投资的18%达到与凉水塔方式耗水相比节水25%以上的效果。The application of mobile finned tube cooling can achieve 18% of the investment in complete finned tube air cooling to save more than 25% of water compared with the cooling tower method in areas where the temperature is not too cold.
实施例3Example 3
本实施例与实施例1基本相同,所不同的是在自然吸风塔空气入口的圆周上的北部半面安装翅片管,在自然吸风塔空气入口的圆周上的南部半面安装处设置通道进风区间调节。翅片管的翅片间距离为8mm,与传统的翅片管将距离3.2mm相比,空气流通阻力极大地降低,保证了凉水塔的自然吸风塔在夏天的吸力,能够克服翅片管带来的阻力,保证了冷却系统的正常进行。This embodiment is basically the same as Embodiment 1, the difference is that the finned tube is installed on the northern half of the circumference of the air inlet of the natural suction tower, and the channel inlet is installed on the southern half of the circumference of the air inlet of the natural suction tower. Wind range adjustment. The distance between the fins of the finned tube is 8mm. Compared with the traditional finned tube with a distance of 3.2mm, the air circulation resistance is greatly reduced, which ensures the suction of the natural suction tower of the cooling water tower in summer and can overcome the finned tube. The resistance brought by it ensures the normal operation of the cooling system.
实施例4Example 4
本实施例与实施例1基本相同,所不同的是在自然吸风塔内设置了实现循环水间接冷却的直立冷却管,如图3所示。循环水热水1进入翅片管2被通过翅片3的空气冷却后流出,再进入直立冷却管25经过间接冷却,流出直立冷却管的一部分循环水被送往凉水塔淋水器5从上流下与向上流动的空气接触,水蒸发吸热被冷却后落到凉水塔底部水池6,另一部分水从直立冷却管流出后直接进入循环水加压泵7的入口与凉水塔底部水池的水混合后送往发电厂乏汽冷凝器进行循环冷却。直立冷却管上部设置有直立冷却管布水器26,形状为倒锥形外壳,布水用水从布水器与直立冷却管之间形成的环形缝隙布水流路27流出,并从顶部溢出沿直立冷却管外壁向下流动形成水膜28。供应布水器26的水可以是凉水塔上部淋水也可以是可控进水。当上部淋水量大时,利用凉水塔上部淋水即可,当凉水塔停止淋水,而大气温度还不很低,仅靠翅片管冷却不能满足循环水回水要求的情况下,开启直立冷却管布水器的可控进水入口(图中未标示)流入用于布水;当大气温度很低时,停止水膜直立冷却管的可控进水布水,由空气冷却。倒锥形圈的外壁与水平面的夹角在60°~80°之间。在翅片管出口增设水膜蒸发直立冷却管,通过直立冷却管的水膜蒸发冷却进一步使循环水得到冷却,由于水膜蒸发的冷却效果远大于空气间接冷却,在大气温度比较低的深秋和初春季节,通过翅片管冷却和水膜蒸发直立冷却管冷却就能达到循环水回水的温度要求,避免了使用凉水塔直接冷却,实现循环水的闭路冷却和循环。且由于直立冷却管的制作成本比翅片管低的较多,所以投资费用降低。This embodiment is basically the same as Embodiment 1, the difference is that a vertical cooling pipe for indirect cooling of circulating water is arranged in the natural suction tower, as shown in FIG. 3 . The circulating water hot water 1 enters the
实施例5Example 5
本实施例是冶金企业翅片管空气冷却与凉水塔串联冷却工艺的应用例,如图4所示。从工艺冷却装置送来的循环水热水1进入在翅片管引风机吸风罩14下设置的翅片管2,与在引风机抽吸作用下穿过翅片3间空间的空气22换热降温后,流出翅片管的一部分循环水被送往引风机吸风凉水塔16内的凉水塔淋水器5从上流下,在引风机吸风凉水塔内填料19的表面与由凉水塔引风机17抽吸向上流动的空气接触换热,水蒸发吸热被冷却后落到凉水塔底部水池6,吸热后的空气由引风机17吸引排入大气;另一部分循环水从翅片管流出后直接进入循环水加压泵7的入口与凉水塔底部水池6排出的水混合后送往工艺冷却装置进行循环冷却。与翅片管的翅片换热后温度升高的空气在翅片管引风机15的抽吸下上升排出进入大气。This embodiment is an application example of the finned tube air cooling and cooling water tower series cooling process in a metallurgical enterprise, as shown in FIG. 4 . The circulating water hot water 1 sent from the process cooling device enters the
在大气温度高的时段,关闭翅片管出水直接回水阀门11,经过翅片冷却的循环水全部进入凉水塔,凉水塔喷淋器中心区进水控制阀门9和凉水塔喷淋器外周区进水控制阀门10全开,并全开凉水塔底部回水阀门21,最大能力地冷却循环水;大气温度下降后,部分开启翅片管出水直接回水阀门11和凉水塔底部回水阀门21,一部分循环水直接进入循环水加压泵7的入口与凉水塔底部水池排出的水混合后送往工艺冷却装置进行循环冷却,同时关闭凉水塔喷淋器外周区进水控制阀门10,循环水只通过凉水塔喷淋器中心区进水控制阀门9进入凉水塔淋水器外周区进行淋水(或关闭凉水塔喷淋器中心区进水控制阀门9,循环水只通过凉水塔喷淋器外周区进水控制阀门10进入凉水塔淋水器外周区进行淋水),由此,由于进入凉水塔的水量减少,且水温也比循环水热水温度低,减少了循环水的蒸发和夹带损失;当大气温度进一步降低后,全部开启翅片管出水直接回水阀门11,循环水直接进入循环水加压泵7的入口送往发电厂乏汽冷凝器进行循环冷却,同时关闭凉水塔喷淋器中心区进水控制阀门9和凉水塔喷淋器外周区进水控制阀门10及凉水塔底部回水阀门21,停止凉水塔冷却,避免了水在凉水塔中的蒸发和夹带损失,最大限度的节水。During the period of high atmospheric temperature, close the
通过翅片管空气间接冷却与风机吸风凉水塔空气直接冷却的串联冷却,实现了既保证循环水的冷却效果,又能达到节水的目的;将凉水塔淋水区域在其横截面的投影面上分成能够单独调控的区域,根据大气温度进行喷水调节,并通过翅片管后循环水进入凉水塔水量的调控实现保证冷却要求条件下的最大化的节水。Through the series cooling of finned tube air indirect cooling and fan suction cooling tower air direct cooling, both the cooling effect of circulating water can be ensured, and the purpose of water saving can be achieved; It is divided into areas that can be independently adjusted, and the water spray is adjusted according to the atmospheric temperature, and the maximum water saving under the cooling requirements is guaranteed by the adjustment of the amount of circulating water entering the cooling tower after the finned tube.
Claims (10)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202010847801.7A CN111998601A (en) | 2020-08-21 | 2020-08-21 | Cooling device and method for circulating water |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202010847801.7A CN111998601A (en) | 2020-08-21 | 2020-08-21 | Cooling device and method for circulating water |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN111998601A true CN111998601A (en) | 2020-11-27 |
Family
ID=73473488
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202010847801.7A Pending CN111998601A (en) | 2020-08-21 | 2020-08-21 | Cooling device and method for circulating water |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN111998601A (en) |
Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2011163682A (en) * | 2010-02-10 | 2011-08-25 | Asahi Kogyosha Co Ltd | Indirect evaporation cooling type outdoor air conditioner system |
| CN105403068A (en) * | 2015-11-20 | 2016-03-16 | 华北电力大学 | Dry-wet unified cooling tower adopting natural ventilation and composite running mode and application of dry-wet unified cooling tower |
| US20170097198A1 (en) * | 2015-10-01 | 2017-04-06 | Pacific Airwell Corp. | Water recovery from cooling tower exhaust |
| CN108050871A (en) * | 2017-11-23 | 2018-05-18 | 黄德夫 | A kind of combined heat pipe-type indirect air cooling method of dry and wet |
| CN108253814A (en) * | 2017-12-29 | 2018-07-06 | 中国电建集团河北省电力勘测设计研究院有限公司 | The combination cooling system and cooling means of a kind of electric power plant circulating water |
| CN209763788U (en) * | 2019-04-17 | 2019-12-10 | 福建龙净环保股份有限公司 | cooling tower |
| CN211012543U (en) * | 2019-11-21 | 2020-07-14 | 贾珊珊 | Cooling tower with good water-saving effect and strong fog dispersal capability |
| CN111457758A (en) * | 2020-03-31 | 2020-07-28 | 天津大学 | Cooling device and method for industrial hot fluid |
-
2020
- 2020-08-21 CN CN202010847801.7A patent/CN111998601A/en active Pending
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2011163682A (en) * | 2010-02-10 | 2011-08-25 | Asahi Kogyosha Co Ltd | Indirect evaporation cooling type outdoor air conditioner system |
| US20170097198A1 (en) * | 2015-10-01 | 2017-04-06 | Pacific Airwell Corp. | Water recovery from cooling tower exhaust |
| CN105403068A (en) * | 2015-11-20 | 2016-03-16 | 华北电力大学 | Dry-wet unified cooling tower adopting natural ventilation and composite running mode and application of dry-wet unified cooling tower |
| CN108050871A (en) * | 2017-11-23 | 2018-05-18 | 黄德夫 | A kind of combined heat pipe-type indirect air cooling method of dry and wet |
| CN108253814A (en) * | 2017-12-29 | 2018-07-06 | 中国电建集团河北省电力勘测设计研究院有限公司 | The combination cooling system and cooling means of a kind of electric power plant circulating water |
| CN209763788U (en) * | 2019-04-17 | 2019-12-10 | 福建龙净环保股份有限公司 | cooling tower |
| CN211012543U (en) * | 2019-11-21 | 2020-07-14 | 贾珊珊 | Cooling tower with good water-saving effect and strong fog dispersal capability |
| CN111457758A (en) * | 2020-03-31 | 2020-07-28 | 天津大学 | Cooling device and method for industrial hot fluid |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US10436482B2 (en) | All-weather solar water source heat pump air conditioning system | |
| CN109000491B (en) | Coupling heat exchanger and heat exchange system for cooling flowable high-temperature medium | |
| CN107155280B (en) | A kind of integration ventilating and cooling heat reclamation device | |
| CN206919708U (en) | Oblique top formula dry and wet combines closed cooling tower | |
| WO2018000773A1 (en) | Air-cooled heat-sink open/close switchable hybrid air-cooled/cold-water cooling tower and manner of operation thereof | |
| CN105004198A (en) | Water type circulating water-air cooling system and method | |
| CN202092479U (en) | Closed air cooling system for auxiliary machine circulating cooling water | |
| CN105021058A (en) | Energy-saving, water-saving and environment-friendly type technological adiabatic air cooler | |
| CN115143805A (en) | Combined air cooling tower with flexible combination of evaporation tube bundle and dry tube bundle and its control method | |
| CN105258528A (en) | Efficient composite steam condensation system | |
| CN211012543U (en) | Cooling tower with good water-saving effect and strong fog dispersal capability | |
| CN207132498U (en) | Passive evaporative cooling ventilation and air conditioning system | |
| WO2018000774A1 (en) | Opening and closing switchable air-cooled cool water-type machine cooling tower for air-cooled radiator and operating mode of same | |
| CN104930619A (en) | Evaporative cooling-absorption heat pump combined air conditioning system for power plant | |
| CN211876793U (en) | Cross flow type fog dissipation water-saving cooling tower | |
| CN206638053U (en) | Water saving recirculated water composite cooling tower | |
| CN111998601A (en) | Cooling device and method for circulating water | |
| CN201133773Y (en) | Direct air cooling units air cooling island cooling apparatus | |
| CN203881170U (en) | ALFAC energy-saving closed type secondary circulating water cooling system for chemical engineering industry | |
| CN115574627B (en) | A natural ventilation air cooling tower with windbreaks and air inlet spray and its working method | |
| CN207501733U (en) | A kind of mechanical-draft cooling tower with cold coagulation liquid fog dispersal | |
| CN110186293A (en) | A kind of central air-conditioning solar energy cooling tower and cooling means | |
| CN211739938U (en) | Closed cooling tower with heat absorption function | |
| CN104197747A (en) | Glass steel closed cooling tower | |
| CN204787919U (en) | Adiabatic air cooler of energy -conserving festival water environmental protection molding die skill |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20201127 |