CN202303334U - Energy-saving thermal deaerator - Google Patents
Energy-saving thermal deaerator Download PDFInfo
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- CN202303334U CN202303334U CN2011204001594U CN201120400159U CN202303334U CN 202303334 U CN202303334 U CN 202303334U CN 2011204001594 U CN2011204001594 U CN 2011204001594U CN 201120400159 U CN201120400159 U CN 201120400159U CN 202303334 U CN202303334 U CN 202303334U
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 194
- 238000006392 deoxygenation reaction Methods 0.000 claims abstract description 9
- 239000001301 oxygen Substances 0.000 claims description 15
- 229910052760 oxygen Inorganic materials 0.000 claims description 15
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 14
- 239000007921 spray Substances 0.000 claims description 14
- 239000007789 gas Substances 0.000 claims description 12
- 238000010438 heat treatment Methods 0.000 claims description 12
- 239000007788 liquid Substances 0.000 claims description 7
- 239000008400 supply water Substances 0.000 claims description 5
- 238000000034 method Methods 0.000 abstract description 2
- 239000000243 solution Substances 0.000 description 3
- 230000003635 deoxygenating effect Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000012267 brine Substances 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical compound O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 description 1
- 230000006641 stabilisation Effects 0.000 description 1
- 238000011105 stabilization Methods 0.000 description 1
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Abstract
本实用新型公开了一种节能型热力除氧器,用于锅炉给水除氧,属于热能技术领域,包括储水箱和除氧头,储水箱上设有加热蒸汽进口、冷凝水入口、除氧水出口和第一安全阀,除氧头上设有补给水入口、排汽阀和第二安全阀;还包括一冷凝器,冷凝器上有不凝性气体排放和溢流孔、乏汽进口、冷凝水出口、进水口和出水口;冷凝器的出水口通过出水管路与除氧头的补给水入口相连接;冷凝水出口通过冷凝水管路与冷凝水入口相连接;进水口与除盐水/软化水来水管路相连接;乏汽排放阀的出口通过连接管路与冷凝器的乏汽进口相连接;乏汽排放阀的出口还与外排管路相连接,冷凝器的冷凝水出口位于储水箱的冷凝水入口的上方。本实用新型几乎实现了锅炉给水热力除氧过程中水蒸汽和热量的零排放。
The utility model discloses an energy-saving thermal deaerator, which is used for boiler feed water deaeration, belongs to the technical field of heat energy, and comprises a water storage tank and a deaeration head. The outlet and the first safety valve, the deaeration head is equipped with a feed water inlet, an exhaust valve and a second safety valve; it also includes a condenser with non-condensable gas discharge and overflow holes, exhaust steam inlet, Condensed water outlet, water inlet and water outlet; the water outlet of the condenser is connected to the feed water inlet of the deaeration head through the water outlet pipe; the condensed water outlet is connected to the condensed water inlet through the condensed water pipe; The softened water inlet pipeline is connected; the exhaust steam discharge valve outlet is connected to the exhaust steam inlet of the condenser through the connecting pipeline; the exhaust steam discharge valve outlet is also connected to the external discharge pipeline, and the condensed water outlet of the condenser is Above the condensate inlet of the storage tank. The utility model almost realizes zero discharge of water vapor and heat in the process of boiler feedwater thermal deoxygenation.
Description
技术领域 technical field
本实用新型属于锅炉热能技术领域,特别涉及一种应用于锅炉给水热力除氧的节能型热力除氧器。 The utility model belongs to the technical field of boiler thermal energy, in particular to an energy-saving thermal deaerator applied to thermal deaeration of boiler feed water.
背景技术 Background technique
现有的热力除氧器包括除氧头和储水箱,储水箱上设有加热蒸汽进口、辅助加热蒸汽进口和除氧水出口,除氧头上设有补给水入口和乏汽排放阀。使用时,补给水在除氧头内被加热蒸汽加热,随着补给水温度的升高,溶解在里面的氧气及其他不凝性气体从水中逸出,和蒸汽一起,以乏汽的形式,通过乏汽排放阀一起排掉。乏汽包括氧气、其它不凝性气体及水蒸汽,其中水蒸汽所占比重最大。在排放氧气等不凝性气体的同时,水蒸汽也被白白排放浪费掉。在能源日益紧缺的今天,热力除氧器在除氧的同时,杜绝水蒸汽及热量的排放浪费,是当前热力除氧器急需解决的问题。 The existing thermal deaerator includes a deaerator head and a water storage tank. The water storage tank is provided with a heating steam inlet, an auxiliary heating steam inlet and a deaeration water outlet. The deaeration head is provided with a supply water inlet and a exhaust steam discharge valve. When in use, the make-up water is heated by the heated steam in the oxygen removal head, and as the temperature of the make-up water rises, the dissolved oxygen and other non-condensable gases escape from the water, together with the steam, in the form of exhausted steam, Drain together through the exhaust valve. Exhausted steam includes oxygen, other non-condensable gases and water vapor, of which water vapor accounts for the largest proportion. While discharging non-condensable gases such as oxygen, water vapor is also wasted in vain. Today, when energy is increasingly scarce, thermal deaerators can eliminate the waste of water vapor and heat while deoxidizing, which is an urgent problem to be solved by thermal deaerators.
发明内容 Contents of the invention
本实用新型的目的在于提供一种几乎没有水蒸气和热量外排浪费的节能型热力除氧器。 The purpose of the utility model is to provide an energy-saving thermal deaerator with almost no waste of water vapor and heat.
为实现上述目的,本实用新型采用以下技术方案: In order to achieve the above object, the utility model adopts the following technical solutions:
一种节能型热力除氧器,包括储水箱和除氧头,所述储水箱上有加热蒸汽进口、辅助加热蒸汽入口中、除氧水出口和第一安全阀,所述除氧头上有补给水入口、乏汽排放阀阀和第二安全阀;其特征在于, An energy-saving thermal deaerator, comprising a water storage tank and a deaeration head, the water storage tank has a heating steam inlet, an auxiliary heating steam inlet, a deaeration water outlet and a first safety valve, and the deaeration head has a Make-up water inlet, exhaust steam discharge valve and second safety valve; characterized in that,
它还包括一冷凝器,所述冷凝器上有氧气等不凝性气体排放和冷凝水溢流孔、乏汽进口、冷凝水出口、进水口和出水口;所述储水箱上设有冷凝水入口,所述冷凝水入口处安装有一喷杯;所述冷凝器的出水口通过出水管路与所述除氧头的补给水入口相连接,所述出水管路上设有控制阀;所述冷凝水出口通过冷凝水管路与所述冷凝水入口相连接,所述冷凝水管路上设有止回阀及第一事故阀;所述进水口与除盐水/软化水来水管路相连接,所述除盐水/软化水来水管路上设有控制阀;所述除氧头的补给水入口通过旁通管路与所述除盐水/软化水来水管路相连接,所述旁通管路上设有旁通阀;所述乏汽排放阀的出口通过连接管路与所述冷凝器的乏汽进口相连接,所述连接管路上设有第二事故阀;所述乏汽排放阀的出口与外排管路相连接,所述外排管路上设有外排阀门,所述冷凝器的冷凝水出口位于所述储水箱的冷凝水入口的上方,所述冷凝器的冷凝水出口与所述储水箱的冷凝水入口的高度差大于或等于2米。 It also includes a condenser, on which non-condensable gases such as oxygen discharge and condensed water overflow holes, exhaust steam inlet, condensed water outlet, water inlet and water outlet are arranged on the said condenser; Inlet, a spray cup is installed at the inlet of the condensed water; the water outlet of the condenser is connected with the supply water inlet of the deaeration head through the water outlet pipeline, and a control valve is arranged on the water outlet pipeline; the condensate The water outlet is connected to the condensed water inlet through a condensed water pipeline, and a check valve and a first emergency valve are arranged on the condensed water pipeline; A control valve is provided on the incoming water pipeline of brine/softened water; the feed water inlet of the deaeration head is connected to the incoming water pipeline of desalted water/softened water through a bypass pipeline, and a bypass is provided on the bypass pipeline. valve; the outlet of the exhaust steam discharge valve is connected to the exhaust steam inlet of the condenser through a connecting pipeline, and a second emergency valve is arranged on the connecting pipeline; the outlet of the exhaust steam discharge valve is connected to the exhaust pipe The condensed water outlet of the condenser is located above the condensed water inlet of the water storage tank, and the condensed water outlet of the condenser is connected with the condensed water outlet of the water storage tank. The height difference of the condensate inlet is greater than or equal to 2 meters.
所述冷凝器内的管束是横向放置的,所述冷凝器的折流板为单弓型竖直折流板,并且底部开有通液口。 The tube bundles in the condenser are placed horizontally, the baffles of the condenser are single-bow vertical baffles, and a liquid opening is opened at the bottom.
所述通液口是弧度为90度的扇形孔。 The liquid opening is a fan-shaped hole with a radian of 90 degrees.
所述喷杯上开有若干喷孔。 There are several spray holes on the spray cup.
所述冷凝器的冷凝水出口与所述储水箱的冷凝水入口的高度差为2米。 The height difference between the condensed water outlet of the condenser and the condensed water inlet of the water storage tank is 2 meters.
所述冷凝器的冷凝水出口与所述储水箱的冷凝水入口的高度差为3米。 The height difference between the condensed water outlet of the condenser and the condensed water inlet of the water storage tank is 3 meters.
所述冷凝器的冷凝水出口与所述储水箱的冷凝水入口的高度差为5米。 The height difference between the condensed water outlet of the condenser and the condensed water inlet of the water storage tank is 5 meters.
本实用新型提供的技术方案的有益效果是:本实用新型节能型热力除氧器利用除盐水/软化水和冷凝器将除氧头排出的乏汽中的水蒸气冷却形成冷凝水,冷凝水依靠自身水柱产生的压力,通过喷杯,以喷射细线状进入储水箱;同时,除盐水/软化水也吸热升温 ,提前预热,为在除氧头内快速升温除氧提供了有利条件。因此,本实用新型节能型热力除氧器不仅没有外排蒸汽,而且排出的氧气等不凝性气体的温度也接近冷凝器的进水温度,几乎实现了乏汽中水蒸气和热量的零排放。 The beneficial effects of the technical solution provided by the utility model are: the energy-saving thermal deaerator of the utility model uses the demineralized water/softened water and the condenser to cool the water vapor in the exhaust steam discharged from the deoxygenation head to form condensed water, and the condensed water relies on The pressure generated by its own water column enters the water storage tank in a thin line through the spray cup; at the same time, the demineralized water/softened water also absorbs heat and heats up, preheating in advance provides favorable conditions for rapid temperature rise and deoxygenation in the deaeration head. Therefore, the energy-saving thermal deaerator of the utility model not only does not discharge steam, but also the temperature of the discharged non-condensable gas such as oxygen is also close to the inlet water temperature of the condenser, almost realizing zero discharge of water vapor and heat in exhaust steam .
附图说明 Description of drawings
图1是本实用新型结构示意图; Fig. 1 is a structural representation of the utility model;
图2是本实用新型中冷凝器的折流板结构示意图; Fig. 2 is the baffle structure schematic diagram of condenser in the utility model;
图3是本实用新型中的喷杯结构示意图。 Fig. 3 is a structural schematic diagram of the spray cup in the utility model.
附图标记:1-储水箱;2-除氧头;3-第一安全阀;4-加热蒸汽进口;5-乏汽排放阀;6-外排阀门;7-第一事故阀;8-冷凝器;9-氧气等不凝性气体排放和冷凝水溢流孔;10-乏汽进口;11-冷凝水出口;12-进水口;13-出水口;14-旁通阀;15-补给水入口;16-止回阀;17-喷杯;18-除氧水出口;19-通液口;20-喷孔;21-第二安全阀;22-出水管路;23-冷凝水管路;24-除盐水/软化水来水管路;25-旁通管路;26-连接管路;27-第二事故阀;28-外排管路;29-折流板;30-冷凝水入口;31-辅助加热蒸汽入口。 Reference signs: 1-water storage tank; 2-deoxygenation head; 3-first safety valve; 4-heating steam inlet; 5-exhaust steam discharge valve; 6-exhaust valve; Condenser; 9 - Oxygen and other non-condensable gas discharge and condensed water overflow hole; 10 - exhaust steam inlet; 11 - condensed water outlet; 12 - water inlet; 13 - water outlet; 14 - bypass valve; 15 - supply Water inlet; 16-check valve; 17-spray cup; 18-deoxygenated water outlet; 19-liquid opening; 20-spray hole; 21-second safety valve; 22-water outlet pipe; 23-condensate water pipe ;24-demineralized water/softened water inlet pipeline; 25-bypass pipeline; 26-connecting pipeline; 27-second emergency valve; 28-exhaust pipeline; 29-baffle plate; ; 31 - Auxiliary heating steam inlet.
具体实施方式 Detailed ways
为使本实用新型的目的、技术方案和优点更加清楚,下面将结合附图对本实用新型实施方式作进一步地详细描述。 In order to make the purpose, technical solutions and advantages of the present utility model clearer, the implementation of the present utility model will be further described in detail below in conjunction with the accompanying drawings.
一种节能型热力除氧器,如图1、图2、图3所示,包括储水箱1和除氧头2,所述储水箱1上有加热蒸汽进口4、辅助加热蒸汽入口31、除氧水出口18和第一安全阀3,所述除氧头2上有补给水入口15、乏汽排放阀阀5和第二安全阀21;其特征在于,
An energy-saving thermal deaerator, as shown in Fig. 1, Fig. 2 and Fig. 3, comprises a
它还包括一冷凝器8,所述冷凝器8上有氧气等不凝性气体排放和冷凝水溢流孔9、乏汽进口10、冷凝水出口11、进水口12和出水口13;所述储水箱1上设有冷凝水入口30,所述冷凝水入口30处安装有一喷杯17;所述冷凝器的出水口13通过出水管路22与所述除氧头的补给水入口15相连接,所述出水管路22上设有控制阀;所述冷凝水出口11通过冷凝水管路23与所述冷凝水入口30相连接,所述冷凝水管路23上设有止回阀16及第一事故阀7,止回阀16的作用是杜绝储水箱内的蒸汽进入冷凝器;所述进水口12与除盐水/软化水来水管路24相连接,所述除盐水/软化水来水管路24上设有控制阀;所述除氧头的补给水入口15通过旁通管路25与所述除盐水/软化水来水管路24相连接,所述旁通管路25上设有旁通阀14;所述乏汽排放阀5的出口通过连接管路26与所述冷凝器的乏汽进口10相连接,所述连接管路26上设有第二事故阀27;所述乏汽排放阀5的出口与外排管路28相连接,所述外排管路28上设有外排阀门6,所述冷凝器的冷凝水出口11位于所述储水箱的冷凝水入口30的上方,所述冷凝器的冷凝水出口11与所述储水箱的冷凝水入口30的高度差大于或等于2米,以使冷凝水柱自身产生的压力大于储水箱内部蒸汽压力,不需要任何外部动力,仅仅依靠冷凝水自身产生压力,即可把凝结水打入储水箱。氧气等不凝性气体排放和冷凝水溢流孔9既可以用来排气,也可以在冷凝水较多时用来排水以避免因冷凝器满水而影响除氧头的除氧效果。
It also includes a condenser 8, on which non-condensable gases such as oxygen are discharged and condensed
使用时,除盐水/软化水来水经过冷凝器后进入除氧器的除氧头,然后向储水箱中通入加热蒸汽对来水进行热力除氧,等储水箱出水达到除氧效果,一切稳定之后,关闭外排阀门,打开第二事故阀让乏汽进入冷凝器。乏汽在冷凝器内被除盐水/软化水来水冷凝,放出热量;同时,除盐水/软化水来水也吸热升温,提前预热,为在除氧头内快速升温除氧提供了有利条件。乏汽中的水蒸汽在冷凝器中冷凝放热后变成冷凝水,冷凝水依靠自身水柱产生的压力回到除氧器的储水箱;而乏汽中的氧气等不凝性气体,经过冷却,降温至接近除盐水/软化水进水温度后,则通过不凝性气体排放和溢流孔不断地被排到冷凝器外面。 When in use, the desalted water/softened water enters the deaerator head of the deaerator after passing through the condenser, and then heats steam into the water storage tank to perform thermal deaeration of the incoming water. After stabilization, close the exhaust valve and open the second emergency valve to allow exhaust steam to enter the condenser. The exhaust steam is condensed by the desalinated water/softened water in the condenser to release heat; at the same time, the desalted water/softened water also absorbs heat and heats up, preheating in advance provides advantages for rapid temperature rise and deoxygenation in the deoxygenation head condition. The water vapor in the exhaust steam condenses and releases heat in the condenser to become condensed water, and the condensed water returns to the water storage tank of the deaerator by the pressure generated by its own water column; while the non-condensable gases such as oxygen in the exhaust steam are cooled , after cooling down to close to the demineralized water/demineralized water inlet temperature, it is continuously discharged out of the condenser through the non-condensable gas discharge and overflow holes.
若是运行时冷凝器或止回阀出现故障,可以打开旁通阀和外排阀门,关闭第一事故阀和第二事故阀来处理故障,而不影响的除氧头的正常除氧效果。 If the condenser or the check valve fails during operation, the bypass valve and the exhaust valve can be opened, and the first emergency valve and the second emergency valve can be closed to deal with the failure without affecting the normal deoxygenation effect of the oxygen removal head.
所述冷凝器8内的管束是横向放置的,所述冷凝器8的折流板29为单弓型竖直折流板,并且底部开有通液口19。
The tube bundles in the condenser 8 are placed horizontally, and the
所述通液口19是弧度为90度的扇形孔。 The liquid opening 19 is a fan-shaped hole with a radian of 90 degrees.
所述喷杯17上设有若干喷孔20,使冷凝水以喷射细线状进入储水箱,增大了与加热蒸汽的接触面积以便迅速加热除氧。
The
所述冷凝器的冷凝水出口11与所述储水箱的冷凝水入口30的高度差为2米。 The height difference between the condensed water outlet 11 of the condenser and the condensed water inlet 30 of the water storage tank is 2 meters.
所述冷凝器的冷凝水出口11与所述储水箱的冷凝水入口30的高度差为3米。 The height difference between the condensed water outlet 11 of the condenser and the condensed water inlet 30 of the water storage tank is 3 meters.
所述冷凝器的冷凝水出口11与所述储水箱的冷凝水入口30的高度差为5米。 The height difference between the condensed water outlet 11 of the condenser and the condensed water inlet 30 of the water storage tank is 5 meters.
所述冷凝器的冷凝水出口11与所述喷杯17的高度差根据需要可取2米以上的其它值。
The height difference between the condensed water outlet 11 of the condenser and the
以上所述仅为本实用新型的较佳实施例,并不用以限制本实用新型,凡在本实用新型的精神和原则之内,所作的任何修改、等同替换、改进等,均应包含在本实用新型的保护范围之内。 The above descriptions are only preferred embodiments of the present utility model, and are not intended to limit the present utility model. Any modifications, equivalent replacements, improvements, etc. made within the spirit and principles of the present utility model shall be included in this utility model. within the scope of protection of utility models.
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN104085940A (en) * | 2014-06-13 | 2014-10-08 | 江苏巴威节能服务有限公司 | Condensate water and demineralized water mixed recovery two-stage deoxygenization apparatus |
| CN105570871A (en) * | 2016-01-19 | 2016-05-11 | 北新集团建材股份有限公司 | Automatic condensation water return system |
| CN106195999A (en) * | 2016-08-30 | 2016-12-07 | 江苏太湖锅炉股份有限公司 | The low discharge water replanishing device of steam generator system |
| CN108826270A (en) * | 2018-05-16 | 2018-11-16 | 冯萍 | A kind of energy saving and environment friendly thermal deaerator |
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2011
- 2011-10-19 CN CN2011204001594U patent/CN202303334U/en not_active Expired - Lifetime
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104085940A (en) * | 2014-06-13 | 2014-10-08 | 江苏巴威节能服务有限公司 | Condensate water and demineralized water mixed recovery two-stage deoxygenization apparatus |
| CN104085940B (en) * | 2014-06-13 | 2015-09-30 | 江苏巴威工程技术股份有限公司 | Secondary deaerating plant is reclaimed in the mixing of condensed water demineralized water |
| CN105570871A (en) * | 2016-01-19 | 2016-05-11 | 北新集团建材股份有限公司 | Automatic condensation water return system |
| CN106195999A (en) * | 2016-08-30 | 2016-12-07 | 江苏太湖锅炉股份有限公司 | The low discharge water replanishing device of steam generator system |
| CN108826270A (en) * | 2018-05-16 | 2018-11-16 | 冯萍 | A kind of energy saving and environment friendly thermal deaerator |
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Assignee: BEIJING SHOUGANG COLD ROLLING THIN PLATE CO., LTD. Assignor: Capital Iron & Steel General Company Contract record no.: 2015990001019 Denomination of utility model: Energy-saving thermal deaerator Granted publication date: 20120704 License type: Common License Record date: 20151209 |
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Address after: 100041 Shijingshan Road, Beijing, No. 68, No. Patentee after: Shougang Group Co. Ltd. Address before: 100041 Shijingshan Road, Beijing, No. 68, No. Patentee before: Capital Iron & Steel General Company |
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