CN201852484U - Spray type condensation waste heat recovery device - Google Patents
Spray type condensation waste heat recovery device Download PDFInfo
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- CN201852484U CN201852484U CN2010206133610U CN201020613361U CN201852484U CN 201852484 U CN201852484 U CN 201852484U CN 2010206133610 U CN2010206133610 U CN 2010206133610U CN 201020613361 U CN201020613361 U CN 201020613361U CN 201852484 U CN201852484 U CN 201852484U
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- flue gas
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
- Y02B30/00—Energy efficient heating, ventilation or air conditioning [HVAC]
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Abstract
Description
技术领域technical field
本实用新型属于热回收设备领域,具体涉及一种喷淋式冷凝余热回收装置。The utility model belongs to the field of heat recovery equipment, in particular to a spray type condensation waste heat recovery device.
背景技术Background technique
目前工业锅炉的排烟温度大概在180-250℃,这部分的损失一直是影响锅炉效率的主要原因,高温烟气的排放不仅造成大量热能的浪费,而且对环境的污染也造成很大的影响。因此有效的利用这部分热能,对节能环保有着很大的意义。At present, the exhaust gas temperature of industrial boilers is about 180-250 ° C. The loss of this part has always been the main reason affecting the efficiency of the boiler. The discharge of high-temperature flue gas not only causes a lot of waste of heat energy, but also has a great impact on environmental pollution. . Therefore, the effective use of this part of heat energy is of great significance to energy conservation and environmental protection.
发明内容Contents of the invention
本实用新型的目的是针对上述情况,提供一种喷淋式冷凝余热回收装置。The purpose of this utility model is to provide a spray type condensation waste heat recovery device in view of the above situation.
为此,本实用新型采用的技术方案是:喷淋式冷凝余热回收装置,包括带有支架的方形壳体,壳体上开有进烟口和出烟口,壳体下部与出水管相连;其特征在于:所述出烟口下方的壳体内设有分离器,分离器下方设有喷淋管,喷淋管下方设有若干块淋水板;所述若干块淋水板呈纵向排列,水平放置于壳体内,并与壳体的内壁相连接固定。For this reason, the technical solution adopted by the utility model is: a spray type condensation waste heat recovery device, including a square shell with a bracket, a smoke inlet and a smoke outlet are opened on the shell, and the lower part of the shell is connected to the water outlet pipe; It is characterized in that: a separator is provided in the casing below the smoke outlet, a spray pipe is provided below the separator, and several water spray boards are provided below the spray pipe; the several water spray boards are arranged vertically, It is placed horizontally in the shell and connected and fixed with the inner wall of the shell.
所述壳体内下部设有溢水器,该溢水器与壳体底端的溢水管相连。A water overflow device is provided at the inner lower part of the housing, and the water overflow device is connected with the overflow pipe at the bottom end of the housing.
所述壳体底端与疏水管相连,并设有与疏水管相配合的疏水阀。The bottom end of the housing is connected with a drain pipe, and a drain valve matched with the drain pipe is provided.
所述壳体下部与补水管相连,壳体内与补水管相应的位置上设有浮球阀。The lower part of the housing is connected with the water supply pipe, and a ball float valve is arranged in the housing at a position corresponding to the water supply pipe.
所述壳体上还设有检查门和水位计管。The casing is also provided with an inspection door and a water level gauge tube.
本实用新型的工作原理是这样的:烟气通过进烟口进入壳体内,延壳体内的通道上升;喷淋管向下喷洒出冷凝水,与上升的烟气形成对流,从而实现对流换热的目的;当冷凝水与烟气进行对流,完成换热后,将被储存于壳体的底部内,然后通过出水管送往用热设备;而烟气再经过若干块淋水板及喷淋管的下方,与冷凝水进行换热后,将继续上升绕过喷淋管,通过分离器将水气分离;被分离出的水则向下流入壳体的底部,被分离出的烟气则继续上升由出烟口排出。The working principle of the utility model is as follows: the flue gas enters the shell through the smoke inlet, and rises along the channel in the shell; the spray pipe sprays condensed water downward, and forms convection with the rising flue gas, thereby realizing convective heat exchange The purpose; when the condensed water and the flue gas are convected and the heat exchange is completed, it will be stored in the bottom of the shell, and then sent to the heat-using equipment through the outlet pipe; The lower part of the pipe, after exchanging heat with condensed water, will continue to rise and bypass the spray pipe, and the water and gas will be separated through the separator; the separated water will flow down to the bottom of the shell, and the separated flue gas will Continue to rise and be discharged from the smoke outlet.
本实用新型的优点在于:实现了对流式换热,并通过壳体内水平放置有若干块淋水板,可以大大增加了烟气与冷凝水的接触面积,使烟气的热量能得到充分的利用;同时,能够通过水位计管查看水位,通过检查门查看设备,并能利用溢水器与浮球阀能够保持壳体底部的水位,以提高系统的使用安全性;在需要清洗、检查或维修设备时,能通过疏水阀及疏水管可将壳体底部的存水排尽,更便于工作人员对设备进行清洗、检查或维修。The utility model has the advantages of realizing convective heat exchange, and by placing several water-drenching plates horizontally in the casing, the contact area between the flue gas and condensed water can be greatly increased, so that the heat of the flue gas can be fully utilized ;At the same time, the water level can be checked through the water level gauge tube, the equipment can be checked through the inspection door, and the water level at the bottom of the shell can be maintained by using the overflow device and the float valve to improve the safety of the system; when cleaning, inspection or maintenance of equipment is required , The water at the bottom of the shell can be drained through the drain valve and the drain pipe, which is more convenient for the staff to clean, inspect or maintain the equipment.
附图说明Description of drawings
图1为本实用新型主视图。Fig. 1 is a front view of the utility model.
图2为本实用新型侧视图。Fig. 2 is a side view of the utility model.
具体实施方式:Detailed ways:
以下结合附图和实施例对本实用新型做进一步详细的描述Below in conjunction with accompanying drawing and embodiment the utility model is described in further detail
参见附图。本实施例包括带有支架2的壳体9,壳体9上开有进烟口4和出烟口7;壳体9下部与出水管11相连,所述出烟口7下方的壳体9内设有分离器6,分离器6下方设有喷淋管8,喷淋管8下方设有若干块淋水板5;淋水板5呈纵向排列,水平放置于壳体9内,并与壳体9的内壁相连接固定;淋水板5是由多块斜向排列的钢板组成的。See attached picture. This embodiment includes a
所述壳体9内下部设有溢水器3,该溢水器3与壳体9底端的溢水管1相连。A
所述壳体9底端与疏水管12相连,并设有与疏水管12相配合的疏水阀。The bottom end of the
所述壳体9下部还与补水管14相连,壳体9内与补水管14相应的位置上设有浮球阀。The lower part of the
所述壳体上还设有上、下检查门15、10和高、低水位计管13、16。The housing is also provided with upper and
本实施例的工作原理是这样的:烟气通过进烟口4进入壳体9内,延壳体9内的通道上升;喷淋管8向下喷洒出冷凝水,与上升的烟气形成对流,从而实现对流换热的目的;当冷凝水与烟气进行对流,完成换热后,将被储存于壳体9的底部内,然后通过出水管11送往用热设备;而烟气再经过3块淋水板5及喷淋管8的下方,与冷凝水进行换热后,将继续上升绕过喷淋管8,通过分离器6将水气分离;被分离出的水则向下流入壳体9的底部,被分离出的烟气则继续上升由出烟口7排出。The working principle of this embodiment is as follows: the flue gas enters the
Claims (5)
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CN2010206133610U CN201852484U (en) | 2010-11-18 | 2010-11-18 | Spray type condensation waste heat recovery device |
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CN2010206133610U CN201852484U (en) | 2010-11-18 | 2010-11-18 | Spray type condensation waste heat recovery device |
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104215091A (en) * | 2013-05-31 | 2014-12-17 | 中国电力工程顾问集团华北电力设计院工程有限公司 | Flue gas afterheat and water recycling device |
CN104930875A (en) * | 2015-06-29 | 2015-09-23 | 广西农垦糖业集团红河制糖有限公司 | Thermostat used for condensate heat radiation |
-
2010
- 2010-11-18 CN CN2010206133610U patent/CN201852484U/en not_active Expired - Fee Related
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104215091A (en) * | 2013-05-31 | 2014-12-17 | 中国电力工程顾问集团华北电力设计院工程有限公司 | Flue gas afterheat and water recycling device |
CN104930875A (en) * | 2015-06-29 | 2015-09-23 | 广西农垦糖业集团红河制糖有限公司 | Thermostat used for condensate heat radiation |
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C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20110601 Termination date: 20171118 |
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CF01 | Termination of patent right due to non-payment of annual fee |