CN202432507U - Energy-saving recovery device for condensed water - Google Patents
Energy-saving recovery device for condensed water Download PDFInfo
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- CN202432507U CN202432507U CN2011205508695U CN201120550869U CN202432507U CN 202432507 U CN202432507 U CN 202432507U CN 2011205508695 U CN2011205508695 U CN 2011205508695U CN 201120550869 U CN201120550869 U CN 201120550869U CN 202432507 U CN202432507 U CN 202432507U
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 167
- 238000011084 recovery Methods 0.000 title claims abstract description 24
- 239000007921 spray Substances 0.000 claims description 10
- 238000005507 spraying Methods 0.000 abstract description 4
- 230000000694 effects Effects 0.000 abstract description 3
- 238000000034 method Methods 0.000 description 5
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 239000002253 acid Substances 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 230000017525 heat dissipation Effects 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 239000007769 metal material Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
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- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
Description
技术领域 technical field
本实用新型涉及一种水处理装置,特别是涉及一种冷凝水的回收装置。 The utility model relates to a water treatment device, in particular to a recovery device for condensed water. the
背景技术 Background technique
蒸汽锅炉水循环系统中的冷凝水中所含的蒸汽热量占总热量的百分之二十到百分之三十,而且冷凝水的品质优良,具有较高的温度,其所含热量是相当可观的余热资源,回收冷凝水是良好的节水节能措施。 The steam heat contained in the condensed water in the steam boiler water circulation system accounts for 20% to 30% of the total heat, and the condensed water is of good quality and has a relatively high temperature, and the heat contained in it is considerable Recycling condensed water is a good water-saving and energy-saving measure. the
传统的冷凝水回收采用开式方法,其集水罐是开口形式的,就是把冷凝水回收到锅炉的集水罐(给水箱)中。在传统的冷凝水的回收和利用过程中,冷凝水的集水罐敞开于大气,与大气相通,由于冷凝水进入集水罐时压力突然降低,在压力瞬间降低时,冷凝水的水温高于该压力对应的沸点,由此将产生大量二次闪蒸汽,而剩余的冷凝水温度大约是100℃,且二次蒸汽直接排入大气将产生热污染,有时还对水泵产生严重的气蚀。 The traditional condensate recovery adopts an open method, and the water collection tank is in the form of an opening, which is to recycle the condensed water into the water collection tank (water supply tank) of the boiler. In the process of traditional recovery and utilization of condensed water, the condensed water collection tank is open to the atmosphere and communicated with the atmosphere. Since the pressure suddenly drops when the condensed water enters the water collection tank, the temperature of the condensed water is higher than that when the pressure drops instantly. The boiling point corresponding to this pressure will generate a large amount of secondary flash steam, and the temperature of the remaining condensed water is about 100°C, and the secondary steam directly discharged into the atmosphere will cause thermal pollution and sometimes cause serious cavitation to the pump. the
实际上,由于闪蒸散热或有时为了防止输送水泵汽蚀而会在冷凝水中兑入冷水,此时回收水温仅在70℃左右,使得冷凝水的能源利用率不足60%。加之开式回收方式会有空气进入冷凝水回收管道,由于凝结水与空气的接触,将使得冷凝水再次遭到空气中杂质的污染。同时,空气中的氧气和二氧化碳会溶入冷凝水导致水pH值降低,管路系统金属材料遭受酸腐蚀,缩短了设备和管道的使用寿命,降低凝结水的品质,甚至使其达不到锅炉给水水质标准,丧失了原本可直接作为锅炉给水的洁净蒸汽凝结水的品质,而不得不浪费掉或是重新进水处理,从而增加了水处理设备和费用。 In fact, due to flash heat dissipation or sometimes cold water is added to the condensed water to prevent cavitation of the delivery pump, the temperature of the recovered water is only about 70°C at this time, making the energy utilization rate of the condensed water less than 60%. In addition, in the open recovery method, air will enter the condensed water recovery pipeline. Due to the contact between the condensed water and the air, the condensed water will be polluted by impurities in the air again. At the same time, the oxygen and carbon dioxide in the air will dissolve into the condensed water, causing the pH value of the water to decrease, and the metal materials of the piping system will be corroded by acid, which will shorten the service life of equipment and pipelines, reduce the quality of condensed water, and even make it unable to reach the boiler. The quality standard of feed water loses the quality of clean steam condensate that could have been directly used as boiler feed water, and has to be wasted or re-introduced for water treatment, thereby increasing water treatment equipment and costs. the
实用新型内容 Utility model content
为解决上述问题,本实用新型提供一种可有效提高回收水质的冷凝水节能回收装置。 In order to solve the above problems, the utility model provides an energy-saving recovery device for condensed water that can effectively improve the quality of recovered water. the
本实用新型解决其技术问题所采用的技术方案是: The technical scheme that the utility model solves its technical problem adopts is:
一种冷凝水节能回收装置,包括通过管道联接的集水罐和加压罐,加压罐内设有用于向加压罐内高速喷射冷凝水的射流头,射流头的出水口设有喷淋装置,与射流头的进水口相连设有高温水泵,高温水泵的进水口联接于加压罐的下方,与高温水泵的出水口相连设有出水管。 An energy-saving recovery device for condensed water, comprising a water collection tank and a pressurized tank connected by pipelines, the pressurized tank is provided with a jet head for spraying condensed water into the pressurized tank at high speed, and the water outlet of the jet head is provided with a spray The device is connected with the water inlet of the jet head and provided with a high-temperature water pump, the water inlet of the high-temperature water pump is connected with the lower part of the pressurized tank, and is connected with the water outlet of the high-temperature water pump with a water outlet pipe.
进一步作为本实用新型技术方案的改进,与射流头的入水口相连设有深入集水罐内的集水罐吸管。 Further as an improvement of the technical solution of the utility model, a water collecting tank suction pipe which penetrates into the water collecting tank is connected with the water inlet of the jet head. the
进一步作为本实用新型技术方案的改进,高温水泵与射流头间设有用于联接的U形管,出水管与U形管的连接处设有气动阀,气动阀的下方联接有与高温水泵的入水口相连的导回管。 As a further improvement of the technical solution of the utility model, a U-shaped pipe for connection is provided between the high-temperature water pump and the jet head, and a pneumatic valve is provided at the connection between the outlet pipe and the U-shaped pipe, and the inlet of the high-temperature water pump is connected below the pneumatic valve. The return pipe connected to the water port. the
进一步作为本实用新型技术方案的改进,集水罐和加压罐的底部设有用于彼此导通的联接管,联接管上设有开关阀。 As a further improvement of the technical solution of the utility model, the bottom of the water collection tank and the pressurized tank are provided with a connecting pipe for conducting with each other, and an on-off valve is provided on the connecting pipe. the
进一步作为本实用新型技术方案的改进,集水罐上设有进水法兰口。 As a further improvement of the technical solution of the utility model, a water inlet flange is provided on the water collecting tank. the
本实用新型的有益效果:此冷凝水的节能回收装置首先将一定量的冷凝水加入彼此连通的集水罐和加压罐内,并通过高温水泵连通加压罐的底部与设置于加压罐顶部的射流头,在加压罐和集水罐内的水达到一定量后,通过高温水泵带动加压罐内的冷凝水经射流头和喷淋装置喷洒于加压罐内进行其热量的回收,以达到对冷凝水热量密闭回收的效果,同时有助于提高冷凝水的回收质量。 Beneficial effects of the utility model: the energy-saving recovery device for condensed water first adds a certain amount of condensed water into the water collecting tank and the pressurized tank connected to each other, and connects the bottom of the pressurized tank with the high-temperature water pump The jet head on the top, after the water in the pressurized tank and water collection tank reaches a certain amount, the high-temperature water pump drives the condensed water in the pressurized tank to spray in the pressurized tank through the jet head and spray device to recover its heat , in order to achieve the effect of airtight recovery of condensed water heat, and at the same time help to improve the quality of condensed water recovery. the
附图说明 Description of drawings
下面结合附图对本实用新型作进一步说明: Below in conjunction with accompanying drawing, the utility model is further described:
图1是本实用新型实施例整体结构示意图; Fig. 1 is a schematic diagram of the overall structure of the utility model embodiment;
图2是本实用新型实施例整体结构俯视图。 Fig. 2 is a top view of the overall structure of the embodiment of the utility model.
具体实施方式 Detailed ways
参照图1、图2,本实用新型为一种冷凝水节能回收装置,包括通过管道联接的集水罐1和加压罐2,加压罐2内设有用于向加压罐2内高速喷射冷凝水的射流头3,射流头3的出水口设有喷淋装置31,与射流头3的进水口相连设有高温水泵4,高温水泵4的进水口联接于加压罐2的下方,与高温水泵4的出水口相连设有出水管5。
Referring to Fig. 1 and Fig. 2, the utility model is an energy-saving recovery device for condensed water, which includes a
此冷凝水的节能回收装置首先将一定量的冷凝水加入彼此连通的集水罐1和加压罐2内,并通过高温水泵4连通加压罐2的底部与设置于加压罐2顶部的射流头3,在加压罐2和集水罐1内的水达到一定量后,通过高温水泵4带动加压罐2内的冷凝水经射流头3和喷淋装置31喷洒于加压罐2内进行其热量的回收,以达到对冷凝水热量密闭回收的效果,同时有助于提高冷凝水的回收质量。
The energy-saving recovery device for condensed water first adds a certain amount of condensed water into the
作为本实用新型优选的实施方式,与射流头3的入水口相连设有深入集水罐1内的集水罐吸管6。
As a preferred embodiment of the present invention, a water collection
射流头3经过高温水泵4输送一定量的水进行喷淋,同时由于射流头3工作过程中的较强的喷射力,可使得连入集水罐1内的集水罐吸管6同时吸取集水罐1内的冷凝水经射流头3经过喷射,喷射出来的水经过喷淋装置31的分散作用,可成小水珠或者喷雾状落于加压罐2中,从而更有效的实现在加压罐2中吸收冷凝水的热量。
The
作为本实用新型优选的实施方式,高温水泵4与射流头3间设有用于联接的U形管7,出水管5与U形管7的连接处设有气动阀8,气动阀8的下方联接有与高温水泵4的入水口相连的导回管9。
As a preferred embodiment of the present utility model, a U-shaped
气动阀8在集水罐1和加压罐2内的冷凝水处于低水位时关闭,使得冷凝水在集水罐1和加压罐2内循环,当集水罐1和加压罐2内的水到达一定的水位量时,气动阀8打开,使得处理完成的冷凝水可经出水管5排入使用设备,从而使得系统自动运行。
The
导回管9在一方面可以对经过高温水泵4流出并进入射流头3的冷凝水进行分流分压,另一方面可将高压水流引回至高温水泵4,使得两股温度相近、压力不同的流体相混合,并发生能量交换,使得进入高温水泵的高温水获得一定的动压,从而克服汽蚀现象,正常输送高至150℃的水。
On the one hand, the
作为本实用新型优选的实施方式,集水罐1和加压罐2的底部设有用于彼此导通的联接管10,联接管10上设有开关阀11。
As a preferred embodiment of the present invention, the bottoms of the
联接管10可方便在集水罐1和加压罐2间的实现自由的水连通,并通过开关阀11的开关进行控制。
The connecting
作为本实用新型优选的实施方式,集水罐1上设有进水法兰口12。
As a preferred embodiment of the present invention, the water collecting
通过将进水管联接进水法兰口12可将所需处理的冷凝水通过该进水法兰口12送入集水罐1内。
By connecting the water inlet pipe to the water inlet
当然,本发明创造并不局限于上述实施方式,熟悉本领域的技术人员在不违背本实用新型精神的前提下还可作出等同变形或替换,这些等同的变型或替换均包含在本申请权利要求所限定的范围内。 Of course, the present invention is not limited to the above-mentioned embodiments. Those skilled in the art can also make equivalent modifications or replacements without violating the spirit of the present utility model. These equivalent modifications or replacements are all included in the claims of this application. within the limited range. the
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110762513A (en) * | 2019-11-01 | 2020-02-07 | 福建蓝海节能科技有限公司 | Boiler steam condensation bin |
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2011
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110762513A (en) * | 2019-11-01 | 2020-02-07 | 福建蓝海节能科技有限公司 | Boiler steam condensation bin |
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