CN204787259U - Variable flow cartridge type heat carrier heating furnace - Google Patents

Variable flow cartridge type heat carrier heating furnace Download PDF

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Publication number
CN204787259U
CN204787259U CN201520506037.1U CN201520506037U CN204787259U CN 204787259 U CN204787259 U CN 204787259U CN 201520506037 U CN201520506037 U CN 201520506037U CN 204787259 U CN204787259 U CN 204787259U
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China
Prior art keywords
convection
heat carrier
furnace
furnace tube
tube group
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Expired - Lifetime
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CN201520506037.1U
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Chinese (zh)
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李永君
陈敏
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Changzhou Energy Equipment Co ltd
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CHANGZHOU ENERGY ENGINEERING Co Ltd
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Abstract

The utility model discloses a variable flow cartridge type heat carrier heating furnace, including the convection furnace nest of tubes, radiation furnace tube group, furnace body and combustor, the furnace body has the heat preservation casing, furnace and flue gas interface, still including set up the public upper header at furnace body top and all set up under the convection zone of furnace body bottom the collector and the radiant section under the collector, the collector is linked together with the other end that radiation furnace tube organized under the radiant section, when the heat carrier needs the low discharge, the heat carrier at first gets into collector under the convection zone, flow through and collect public upper header behind the convection furnace nest of tubes, the collector gets into the total pipeline of heat supply under compiling the radiant section after the radiation furnace tube that flows through the again group, need when large -traffic when the heat carrier, the heat carrier gets into under the convection zone collector under collector and the radiant section respectively, the convection furnace nest of tubes of flowing through correspondingly respectively again and radiation furnace tube group, then all compile to the public upper header after the entering heat supply and assemble the pipeline. The utility model discloses can make the user rationally select different heat carrier flows according to the difference of heat supply operating mode, unnecessary electrical power loss in the time of can being used for saving the heat carrier low discharge, but also satisfied the big load heat supply requirement of user.

Description

可变流量筒型热载体加热炉Variable flow cylinder type heat carrier heating furnace

技术领域technical field

本实用新型涉及一种可变流量筒型热载体加热炉,属于加热炉技术领域。The utility model relates to a variable flow rate cylindrical heat carrier heating furnace, which belongs to the technical field of heating furnaces.

背景技术Background technique

目前,通用的热载体加热炉,其炉体选择对流段和辐射段炉管或串联或并联的单一结构。此结构要求用户提供的热载体流量必须达到一定的最低流量,然而实际使用过程中,许多用户的实际用热工况会经常变化,有时实际用热量达不到原来设计负荷的一半,于是就会出现用户为了省电,常常只开一半的循环泵,这就会使原有结构的加热炉因流量过低而使炉管结焦损坏。At present, the general-purpose heat carrier heating furnace has a furnace body with a convection section and a radiation section furnace tube or a single structure connected in series or in parallel. This structure requires that the heat carrier flow rate provided by the user must reach a certain minimum flow rate. However, in the actual use process, the actual heat consumption conditions of many users will often change, and sometimes the actual heat consumption cannot reach half of the original design load, so it will In order to save electricity, users often only turn on half of the circulation pump, which will cause the original structure of the heating furnace to coke and damage the furnace tube due to the low flow rate.

发明内容Contents of the invention

本实用新型所要解决的技术问题是克服现有技术的缺陷,提供一种可变流量筒型热载体加热炉,它能够使用户根据供热工况的不同合理选择不同的热载体流量,既能用于节省热载体小流量时不必要的电力损耗,而且还满足了用户大负荷供热要求。The technical problem to be solved by the utility model is to overcome the defects of the prior art, and provide a variable flow tube type heat carrier heating furnace, which can enable users to reasonably select different heat carrier flow rates according to different heating conditions, and can It is used to save unnecessary power loss when the heat carrier has a small flow rate, and also meets the user's large-load heating requirements.

为了解决上述技术问题,本实用新型的技术方案是:一种可变流量筒型热载体加热炉,包括对流炉管组、辐射炉管组、炉体和燃烧器,炉体具有保温壳体、炉膛和烟气接口,烟气接口设置在炉体的顶部外侧壁上并与炉膛相连通,燃烧器设置在炉体的底部并且其燃烧口通向炉膛,所述的对流炉管组和辐射炉管组均设置在保温壳体内,并且对流炉管组位于辐射炉管组的外围,还包括设置在炉体顶部的公用上集管以及均设置在炉体底部的对流段下集管和辐射段下集管,对流段下集管与对流炉管组的进口相连通,对流炉管组的出口通过公用上集管与辐射炉管组的一端相连通,辐射段下集管与辐射炉管组的另一端相连通;当热载体需小流量时,热载体首先进入对流段下集管,流经对流炉管组后汇集到公用上集管,再流经辐射炉管组后汇集到辐射段下集管进入供热总管线;当热载体需要大流量时,热载体分别进入对流段下集管和辐射段下集管,再分别流经相对应的对流炉管组和辐射炉管组,然后均汇集至公用上集管后进入供热总管线。In order to solve the above-mentioned technical problems, the technical solution of the present invention is: a variable flow tube type heat carrier heating furnace, which includes a convection furnace tube group, a radiation furnace tube group, a furnace body and a burner, and the furnace body has an insulating shell, The furnace and the flue gas interface, the flue gas interface is arranged on the top outer wall of the furnace body and communicates with the furnace, the burner is arranged at the bottom of the furnace body and its combustion port leads to the furnace, the convection furnace tube group and the radiation furnace The tube groups are all arranged in the insulation shell, and the convection furnace tube group is located on the periphery of the radiation furnace tube group, and also includes a common upper header arranged on the top of the furnace body, and a convection section lower header and a radiation section arranged at the bottom of the furnace body The lower header, the lower header of the convection section is connected with the inlet of the convection furnace tube group, the outlet of the convection furnace tube group is connected with one end of the radiation furnace tube group through the common upper header, and the lower header of the radiant section is connected with the radiation furnace tube group The other end is connected; when the heat carrier needs a small flow rate, the heat carrier first enters the lower header of the convection section, flows through the convection furnace tube group and then gathers to the common upper header, and then flows through the radiant furnace tube group and then gathers to the radiation section The lower header enters the heating main pipeline; when the heat carrier needs a large flow, the heat carrier enters the lower header of the convection section and the lower header of the radiation section respectively, and then flows through the corresponding convection furnace tube group and radiant furnace tube group respectively, Then they are all collected into the common upper header and enter the main heating pipeline.

进一步为了控制公用上集管、对流段下集管和辐射段下集管内热载体的流向以便实现筒型热载体加热炉内热载体的串联或并联的流向控制,所述的公用上集管的出口处、对流段下集管的进口处和辐射段下集管的进口处均安装有闸阀。Further, in order to control the flow direction of the heat carrier in the common upper header, the lower header of the convection section and the lower header of the radiant section so as to realize the flow direction control of the heat carrier in the cylindrical heat carrier heating furnace in series or in parallel, the outlet of the common upper header Gate valves are installed at the inlet of the lower header of the convection section and the inlet of the lower header of the radiant section.

采用了上述技术方案后,采用了本结构的热载体加热炉,便于用户在实际用热负荷为设计负荷一半左右时,可采用小流量的串联式运行方式,可少开一半的循环泵,以节省小流量时不必要的循环泵电力损耗,同时能有效地防止因对流炉管内热载体流量偏小而产生的炉管结焦现象;采用了本结构的热载体加热炉,还便于用户在实际用热负荷接近设计负荷时,可采用大流量的并联式运行方式,可有效地满足用户用热要求,并保证用户的有机热载体加热炉的安全运行。After adopting the above technical scheme, the heat carrier heating furnace with this structure is adopted, so that when the actual heat load is about half of the design load, the user can adopt the series operation mode with small flow rate, and half of the circulating pump can be opened to save energy. It saves unnecessary power loss of the circulating pump when the flow rate is small, and can effectively prevent the coking phenomenon of the furnace tube caused by the small heat carrier flow rate in the convection furnace tube; the heat carrier heating furnace with this structure is also convenient for users to use in actual use. When the heat load is close to the design load, the large flow parallel operation mode can be adopted, which can effectively meet the user's heat consumption requirements and ensure the safe operation of the user's organic heat carrier heating furnace.

附图说明Description of drawings

图1为本实用新型的可变流量筒型热载体加热炉的结构示意图。Fig. 1 is a structural schematic diagram of a variable flow rate cylindrical heat carrier heating furnace of the present invention.

具体实施方式Detailed ways

为了使本实用新型的内容更容易被清楚地理解,下面根据具体实施例并结合附图,对本实用新型作进一步详细的说明,In order to make the content of the utility model easier to understand clearly, the utility model will be further described in detail below according to the specific embodiments and in conjunction with the accompanying drawings.

如图1所示,一种可变流量筒型热载体加热炉,包括对流炉管组5、辐射炉管组6、炉体和燃烧器1,炉体具有保温壳体4、炉膛4-1和烟气接口8,烟气接口8设置在炉体的顶部外侧壁上并与炉膛4-1相连通,燃烧器1设置在炉体的底部并且其燃烧口通向炉膛4-1,对流炉管组5和辐射炉管组6均设置在保温壳体4内,并且对流炉管组5位于辐射炉管组6的外围,还包括设置在炉体顶部的公用上集管7以及均设置在炉体底部的对流段下集管3和辐射段下集管2,对流段下集管3与对流炉管组5的进口相连通,对流炉管组5的出口通过公用上集管7与辐射炉管组6的一端相连通,辐射段下集管2与辐射炉管组6的另一端相连通;当热载体需小流量时,热载体首先进入对流段下集管3,流经对流炉管组5后汇集到公用上集管7,再流经辐射炉管组6后汇集到辐射段下集管2进入供热总管线;当热载体需要大流量时,热载体分别进入对流段下集管3和辐射段下集管2,再分别流经相对应的对流炉管组5和辐射炉管组6,然后均汇集至公用上集管7后进入供热总管线。辐射炉管组6的内侧为辐射室9,辐射炉管组6和保温壳体4之间为对流室,对流炉管组5位于该对流室内。As shown in Figure 1, a variable flow tube type heat carrier heating furnace includes a convection furnace tube group 5, a radiation furnace tube group 6, a furnace body and a burner 1, and the furnace body has an insulating shell 4 and a furnace 4-1 And the flue gas interface 8, the flue gas interface 8 is arranged on the top outer wall of the furnace body and communicates with the furnace 4-1, the burner 1 is arranged at the bottom of the furnace body and its combustion port leads to the furnace 4-1, the convection furnace The tube group 5 and the radiation furnace tube group 6 are both arranged in the heat preservation shell 4, and the convection furnace tube group 5 is located at the periphery of the radiation furnace tube group 6, and also includes a common upper header 7 arranged on the top of the furnace body and is arranged on the The lower header 3 of the convection section and the lower header 2 of the radiation section at the bottom of the furnace body, the lower header 3 of the convection section communicates with the inlet of the convection furnace tube group 5, and the outlet of the convection furnace tube group 5 is connected to the radiation section through the common upper header 7. One end of the furnace tube group 6 is connected, and the lower header 2 of the radiation section is connected with the other end of the radiation furnace tube group 6; when the heat carrier needs a small flow rate, the heat carrier first enters the lower header 3 of the convection section and flows through the convection furnace The tube groups 5 are then collected into the common upper header 7, and then flow through the radiant furnace tube group 6 and then converge to the lower header 2 of the radiant section to enter the main heating pipeline; when the heat carrier requires a large flow rate, the heat carrier enters the lower convection section respectively The header 3 and the lower header 2 of the radiant section flow through the corresponding convection furnace tube group 5 and the radiant furnace tube group 6 respectively, and then they all converge to the common upper header 7 and then enter the main heating pipeline. The inner side of the radiation furnace tube group 6 is a radiation chamber 9, and the convection chamber is between the radiation furnace tube group 6 and the heat preservation shell 4, and the convection furnace tube group 5 is located in the convection chamber.

为了控制公用上集管7、对流段下集管3和辐射段下集管2内热载体的流向以便实现筒型热载体加热炉内热载体的串联或并联的流程控制,公用上集管7的出口处、对流段下集管3的进口处和辐射段下集管2的进口处均安装有闸阀。In order to control the flow direction of the heat carrier in the common upper header 7, the lower header 3 of the convection section and the lower header 2 of the radiant section so as to realize the process control of the series or parallel connection of the heat carrier in the cylindrical heat carrier heating furnace, the outlet of the upper header 7 is shared Gate valves are installed at the inlet of the lower header 3 of the convection section and the inlet of the lower header 2 of the radiation section.

本实用新型的工作原理如下:The working principle of the utility model is as follows:

燃煤等燃料由燃烧器1燃烧后,产生的高温烟气经辐射室9辐射换热后进入依次连通的对流炉管组5内外侧的对流室,经辐射、对流换热后经烟气接口8排出炉体。After coal and other fuels are burned by the burner 1, the high-temperature flue gas produced passes through the radiation chamber 9 for radiation heat exchange and then enters the convection chambers inside and outside the convection furnace tube group 5 that are connected in sequence, and passes through the flue gas interface after radiation and convection heat exchange. 8 discharge the furnace body.

在用户采用小负荷、小流量热载体运行时:热载体由对流段下集管3进入,流经对流炉管组5到达辐射段与对流段的公用上集管7,然后进入辐射炉管组6后进入辐射段下集管2,然后经外部连接管线进入系统供热管线。When the user operates with small load and small flow heat carrier: the heat carrier enters from the lower header 3 of the convection section, flows through the convection furnace tube group 5 to reach the common upper header 7 of the radiation section and the convection section, and then enters the radiant furnace tube group After 6, it enters the lower header 2 of the radiant section, and then enters the system heating pipeline through the external connecting pipeline.

在用户采用大负荷、大流量热载体运行时:热载体同时并行进入辐射段下集管2和对流段下集管3,分别流经辐射炉管组6和对流炉管组5,分别汇集到辐射段与对流段的公用上集管7后经外部连接管线进入系统供热管线。When the user operates with a large load and a large flow of heat carrier: the heat carrier enters the lower header 2 of the radiation section and the lower header 3 of the convection section at the same time, flows through the radiation furnace tube group 6 and the convection furnace tube group 5 respectively, and collects them respectively. The common upper header 7 of the radiation section and the convection section enters the heating pipeline of the system through the external connecting pipeline.

以上所述的具体实施例,对本实用新型解决的技术问题、技术方案和有益效果进行了进一步详细说明,所应理解的是,以上所述仅为本实用新型的具体实施例而已,并不用于限制本实用新型,凡在本实用新型的精神和原则之内,所做的任何修改、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 specific embodiments described above have further described the technical problems, technical solutions and beneficial effects solved by the utility model in detail. It should be understood that the above descriptions are only specific embodiments of the utility model and are not intended to be used To limit the utility model, any modification, equivalent replacement, improvement, etc. made within the spirit and principles of the utility model shall be included in the protection scope of the utility model.

Claims (2)

1. a changeable flow cartridge type heat medium heater, comprise convection coil group (5), radiating furnace tube group (6), body of heater and burner (1), body of heater has insulation shell (4), burner hearth (4-1) and flue gas interface (8), the top outer wall that flue gas interface (8) is arranged on body of heater is connected with burner hearth (4-1), burner (1) is arranged on the bottom of body of heater and its port leads to burner hearth (4-1), described convection coil group (5) and radiating furnace tube group (6) are all arranged in insulation shell (4), and convection coil group (5) is positioned at the periphery of radiating furnace tube group (6), it is characterized in that: also comprise the public upper header (7) being arranged on body of heater top and the convection section lower collector pipe (3) being all arranged on bottom of furnace body and radiant section lower collector pipe (2), convection section lower collector pipe (3) is connected with the import of convection coil group (5), the outlet of convection coil group (5) is connected by public upper header (7) one end with radiating furnace tube group (6), radiant section lower collector pipe (2) is connected with the other end of radiating furnace tube group (6), when heat carrier needs low discharge, first heat carrier enters convection section lower collector pipe (3), be pooled to public upper header (7) after flowing through convection coil group (5), then be pooled to radiant section lower collector pipe (2) after flowing through radiating furnace tube group (6) and enter heat supply main pipe line, when heat carrier needs large discharge, heat carrier enters convection section lower collector pipe (3) and radiant section lower collector pipe (2) respectively, flow through corresponding convection coil group (5) and radiating furnace tube group (6) more respectively, after being then all collected to public upper header (7), enter heat supply main pipe line.
2. changeable flow cartridge type heat medium heater according to claim 1, is characterized in that: the import department of the exit of described public upper header (7), the import department of convection section lower collector pipe (3) and radiant section lower collector pipe (2) is all provided with gate valve.
CN201520506037.1U 2015-07-13 2015-07-13 Variable flow cartridge type heat carrier heating furnace Expired - Lifetime CN204787259U (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106940088A (en) * 2017-03-28 2017-07-11 天津辰创环境工程科技有限责任公司 A kind of squirrel-cage heating furnace

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106940088A (en) * 2017-03-28 2017-07-11 天津辰创环境工程科技有限责任公司 A kind of squirrel-cage heating furnace

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Address after: 213000 No. 18 venture Road, Xinbei District, Jiangsu, Changzhou

Patentee after: Changzhou Energy Equipment Co.,Ltd.

Address before: 213033 No. 18 Chuangye Road, Xinbei District, Changzhou City, Jiangsu Province

Patentee before: CHANGZHOU ENERGY ENGINEERING Co.,Ltd.

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Granted publication date: 20151118

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