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CN206064382U - Reactor boiler heating system - Google Patents

Reactor boiler heating system Download PDF

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Publication number
CN206064382U
CN206064382U CN201620988041.0U CN201620988041U CN206064382U CN 206064382 U CN206064382 U CN 206064382U CN 201620988041 U CN201620988041 U CN 201620988041U CN 206064382 U CN206064382 U CN 206064382U
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water
steam
reactor
heating system
boiler
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欧华新
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Guangdong Xinhui Chemical Co Ltd
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Zhongshan Xinhui Chemical Products Co ltd
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Abstract

The utility model discloses a reation kettle's boiler heating system, including first reation kettle, second reation kettle and steam boiler, the first reation kettle outside is provided with the cooling intermediate layer, the cooling intermediate layer disposes the cooling water cavity, the cooling water cavity has water inlet and delivery port, steam boiler has a moisturizing mouth and steam outlet, the delivery port is connected through a moisturizing pipeline with the moisturizing mouth, and reation kettle can produce warm water or hot water usually when passing through water-cooling, the utility model discloses a be connected to steam boiler's moisturizing mouth with the delivery port of reation kettle cooling water, make full use of reation kettle's waste heat, reduce steam boiler's thermal power, reduce power consumption, and can reduce the outer row of warm water, more environmental protection safety.

Description

反应釜的锅炉加热系统Reactor boiler heating system

技术领域technical field

本实用新型涉及一种化工产品生产设备,特别是一种反应釜的锅炉加热系统。The utility model relates to a chemical product production equipment, in particular to a boiler heating system of a reaction kettle.

背景技术Background technique

在使用反应釜生产化工产品时,有的化学原料混合后反应有会自发热,需要进行冷却,有的化学反应则需要保持在某一较高温度,故而反应釜需配备冷却系统及加热系统,加热系统通常为热水加热和蒸汽加热,蒸汽加热的加热温度高加热速度快,故而应用较为的广泛,蒸汽加热通常包括一蒸汽锅炉,通过加热水的方式产生蒸汽,通常蒸汽锅炉是直接的加入冷水或通过配置预热装置加入温热水,但是这样加热的功率高,耗电量大。When using a reactor to produce chemical products, some chemical raw materials will react spontaneously after mixing and need to be cooled, while some chemical reactions need to be kept at a higher temperature, so the reactor needs to be equipped with a cooling system and a heating system. The heating system is usually hot water heating and steam heating. The heating temperature of steam heating is high and the heating speed is fast, so it is widely used. Steam heating usually includes a steam boiler, which generates steam by heating water. Usually, the steam boiler is directly added Cold water or add warm water by configuring the preheating device, but the heating power is high and the power consumption is large.

发明内容Contents of the invention

为了克服现有技术的不足,本实用新型提供一种反应釜的锅炉加热系统。In order to overcome the deficiencies of the prior art, the utility model provides a boiler heating system for a reactor.

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:

反应釜的锅炉加热系统,包括第一反应釜、第二反应釜及蒸汽锅炉,所述第一反应釜外侧设置有冷却夹层,所述冷却夹层内配置有冷却水腔,所述冷却水腔具有进水口和出水口,所述蒸汽锅炉具有一补水口及蒸汽排出口,所述出水口与补水口通过一补水管道连接;所述第二反应釜外侧设置有一保温层,在保温层与第二反应釜外壁之间具有一空腔,所述空腔内配置有盘绕第二反应釜外壁的蒸汽管道,所述蒸汽管道内配置有导热油管道,所述蒸汽排出口通过一蒸汽输出管道连接至蒸汽管道的入口端,所述蒸汽管道的出口端设置有外排管道,所述导热油管道的入口端和出口端分别连接至导热油循环装置。The boiler heating system of the reaction kettle includes a first reaction kettle, a second reaction kettle and a steam boiler. A cooling interlayer is arranged outside the first reaction kettle, and a cooling water chamber is arranged in the cooling interlayer, and the cooling water chamber has A water inlet and a water outlet, the steam boiler has a water replenishment port and a steam discharge port, the water outlet and the water replenishment port are connected through a water replenishment pipeline; an insulation layer is arranged on the outside of the second reaction kettle, and the insulation layer and the second There is a cavity between the outer walls of the reaction kettle, and a steam pipe coiled around the outer wall of the second reaction kettle is arranged in the cavity, a heat-conducting oil pipe is arranged in the steam pipe, and the steam outlet is connected to the steam outlet through a steam output pipe. The inlet end of the pipeline and the outlet end of the steam pipeline are provided with an outflow pipeline, and the inlet end and the outlet end of the heat transfer oil pipeline are respectively connected to a heat transfer oil circulation device.

所述补水管道上配置有由出水口向补水口方向导通的单向阀。The water replenishment pipeline is provided with a one-way valve leading from the water outlet to the water replenishment port.

所述补水口处配置有一液位开关,所述液位开关能够根据蒸汽锅炉内水位的高度而控制补水口的开关。A liquid level switch is arranged at the water supply port, and the liquid level switch can control the opening and closing of the water supply port according to the height of the water level in the steam boiler.

所述导热油循环装置包括一导热油泵。The heat conduction oil circulation device includes a heat conduction oil pump.

所述蒸汽锅炉还配置有主补水口,所述主补水口与自来水管连接,并配置有开关阀。The steam boiler is also equipped with a main water supply port, which is connected to a tap water pipe and equipped with a switch valve.

所述空腔配置有冷却水进口和冷却水出口。The cavity is configured with a cooling water inlet and a cooling water outlet.

本实用新型的有益效果是:反应釜的锅炉加热系统,包括第一反应釜、第二反应釜及蒸汽锅炉,所述第一反应釜外侧设置有冷却夹层,所述冷却夹层内配置有冷却水腔,所述冷却水腔具有进水口和出水口,所述蒸汽锅炉具有一补水口及蒸汽排出口,所述出水口与补水口通过一补水管道连接,反应釜通过水冷冷却时通常会产生温水或热水,本实用新型通过将反应釜冷却水的出水口连接至蒸汽锅炉的补水口,充分利用了反应釜的余热,减少蒸汽锅炉的热功率,减少耗电量,且能够减少温水的外排,更为的环保安全,进一步,所述第二反应釜外侧设置有一保温层,在保温层与第二反应釜外壁之间具有一空腔,所述空腔内配置有盘绕第二反应釜外壁的蒸汽管道,所述蒸汽管道内配置有导热油管道,所述蒸汽排出口通过一蒸汽输出管道连接至蒸汽管道的入口端,所述蒸汽管道的出口端设置有外排管道,所述导热油管道的入口端和出口端分别连接至导热油循环装置,通过蒸汽管道与导热油管道的配合,加热效果好,加热速度快,保温效果好,热量散失小。The beneficial effect of the utility model is: the boiler heating system of the reactor includes a first reactor, a second reactor and a steam boiler, a cooling interlayer is arranged on the outside of the first reactor, and cooling water is arranged in the cooling interlayer cavity, the cooling water cavity has a water inlet and a water outlet, and the steam boiler has a water replenishment port and a steam discharge port, the water outlet and the water replenishment port are connected through a water replenishment pipe, and the reaction kettle usually produces warm water when it is cooled by water or hot water, the utility model makes full use of the waste heat of the reactor by connecting the water outlet of the cooling water of the reactor to the replenishment port of the steam boiler, reduces the thermal power of the steam boiler, reduces power consumption, and can reduce external heating of warm water. row, which is more environmentally friendly and safe. Further, an insulation layer is arranged on the outside of the second reaction kettle, and a cavity is provided between the insulation layer and the outer wall of the second reaction kettle, and a coil coiled on the outer wall of the second reaction kettle is arranged in the cavity. steam pipe, the steam pipe is equipped with a heat transfer oil pipe, the steam outlet is connected to the inlet end of the steam pipe through a steam output pipe, the outlet end of the steam pipe is provided with an external discharge pipe, and the heat transfer oil The inlet end and the outlet end of the pipeline are respectively connected to the heat transfer oil circulation device. Through the cooperation of the steam pipe and the heat transfer oil pipe, the heating effect is good, the heating speed is fast, the heat preservation effect is good, and the heat loss is small.

附图说明Description of drawings

下面结合附图和实施例对本实用新型进一步说明。Below in conjunction with accompanying drawing and embodiment the utility model is further described.

图1是本实用新型的结构示意图;Fig. 1 is a structural representation of the utility model;

图2是本实用新型图1中A部分的局部放大示意图。Fig. 2 is a partially enlarged schematic diagram of part A in Fig. 1 of the present utility model.

具体实施方式detailed description

参照图1、图2,图1、图2是本实用新型一个具体实施例的结构示意图,如图所示,反应釜的锅炉加热系统,包括第一反应釜1、第二反应釜2及蒸汽锅炉3,所述第一反应釜1外侧设置有冷却夹层,所述冷却夹层内配置有冷却水腔11,所述冷却水腔11具有进水口111和出水口112,所述蒸汽锅炉3具有一补水口31及蒸汽排出口32,所述出水口112与补水口31通过一补水管道33连接;反应釜通过水冷冷却时通常会产生温水或热水,本实用新型通过将反应釜冷却水的出水口连接至蒸汽锅炉的补水口,充分利用了反应釜的余热,减少蒸汽锅炉的热功率,减少耗电量,且能够减少温水的外排,更为的环保安全。With reference to Fig. 1, Fig. 2, Fig. 1, Fig. 2 are the structural representations of a specific embodiment of the present utility model, as shown in the figure, the boiler heating system of reactor comprises first reactor 1, second reactor 2 and steam Boiler 3, a cooling interlayer is arranged on the outside of the first reaction kettle 1, a cooling water cavity 11 is arranged in the cooling interlayer, the cooling water cavity 11 has a water inlet 111 and a water outlet 112, and the steam boiler 3 has a The water replenishment port 31 and the steam discharge port 32, the water outlet 112 is connected with the water replenishment port 31 through a water replenishment pipeline 33; when the reaction kettle is cooled by water cooling, warm water or hot water is usually produced, and the utility model passes the outlet of the cooling water of the reaction kettle The water port is connected to the water supply port of the steam boiler, which makes full use of the waste heat of the reaction kettle, reduces the thermal power of the steam boiler, reduces power consumption, and can reduce the discharge of warm water, which is more environmentally friendly and safe.

进一步,所述第二反应釜2外侧设置有一保温层,在保温层与第二反应釜2外壁之间具有一空腔21,所述空腔21内配置有盘绕第二反应釜2外壁的蒸汽管道22,所述蒸汽管道22内配置有导热油管道23,所述蒸汽排出口32通过一蒸汽输出管道34连接至蒸汽管道22的入口端,所述蒸汽管道22的出口端设置有外排管道,所述导热油管道23的入口端和出口端分别连接至导热油循环装置,通过蒸汽管道与导热油管道的配合,加热效果好,加热速度快,保温效果好,热量散失小。Further, an insulation layer is provided on the outside of the second reactor 2, and a cavity 21 is provided between the insulation layer and the outer wall of the second reactor 2, and a steam pipe coiled around the outer wall of the second reactor 2 is arranged in the cavity 21. 22, the steam pipe 22 is equipped with a heat transfer oil pipe 23, the steam outlet 32 is connected to the inlet end of the steam pipe 22 through a steam output pipe 34, and the outlet end of the steam pipe 22 is provided with an external discharge pipe, The inlet end and the outlet end of the heat transfer oil pipeline 23 are respectively connected to the heat transfer oil circulation device, and through the cooperation of the steam pipe and the heat transfer oil pipeline, the heating effect is good, the heating speed is fast, the heat preservation effect is good, and the heat loss is small.

优选的,所述补水管道33上配置有由出水口112向补水口31方向导通的单向阀4,防止蒸汽从补水管道33排出。Preferably, the water supply pipe 33 is provided with a one-way valve 4 leading from the water outlet 112 to the water supply port 31 to prevent steam from being discharged from the water supply pipe 33 .

优选的,所述补水口31处配置有一液位开关5,所述液位开关5能够根据蒸汽锅炉3内水位的高度而控制补水口31的开关,防止蒸汽锅炉3内的水量过大而造成压力过大或降低蒸汽的温度。Preferably, the water replenishment port 31 is provided with a liquid level switch 5, and the liquid level switch 5 can control the switch of the water replenishment port 31 according to the height of the water level in the steam boiler 3, so as to prevent excessive water in the steam boiler 3 from causing Excessive pressure or reduced steam temperature.

优选的,所述导热油循环装置包括一导热油泵,通过导热油泵使得导热油管道23内的导热油发生旋环,保证温度均匀。Preferably, the heat-conducting oil circulation device includes a heat-conducting oil pump, through which the heat-conducting oil in the heat-conducting oil pipeline 23 is rotated to ensure uniform temperature.

优选的,所述蒸汽锅炉3还配置有主补水口35,所述主补水口35与自来水管连接,并配置有开关阀351,以便第一反应釜1中的输出的水量不足时,对蒸汽锅炉3进行补水,在主补水口35还可配置一加热装置,对自来水进行预热。Preferably, the steam boiler 3 is also equipped with a main water supply port 35, the main water supply port 35 is connected with a tap water pipe, and is equipped with a switch valve 351, so that when the output water in the first reactor 1 is insufficient, the steam The boiler 3 replenishes water, and a heating device can also be configured at the main water replenishment port 35 to preheat tap water.

优选的,所述空腔21配置有冷却水进口211和冷却水出口212,以便反应釜中反应完成后对其进行冷却,所述的冷却水出口212也可连接至蒸汽锅炉的补水口,利用余热,在本实施例中,所述的第一反应釜1、第二反应釜2是指泛指的化工反应釜,其可为一个或多个的组合,即蒸汽锅炉同时与多个的反应釜连接,并不局限于本实施例中所述的内容。Preferably, the cavity 21 is equipped with a cooling water inlet 211 and a cooling water outlet 212, so that it can be cooled after the reaction in the reactor is completed, and the cooling water outlet 212 can also be connected to the water supply port of the steam boiler, using Waste heat, in this embodiment, the first reactor 1 and the second reactor 2 refer to chemical reactors in general, which can be a combination of one or more, that is, the steam boiler simultaneously reacts with multiple The kettle connection is not limited to the content described in this embodiment.

以上对本实用新型的较佳实施进行了具体说明,当然,本实用新型还可以采用与上述实施方式不同的形式,熟悉本领域的技术人员在不违背本发明精神的前提下所作的等同的变换或相应的改动,都应该属于本实用新型的保护范围内。The preferred implementation of the present utility model has been specifically described above. Of course, the present utility model can also adopt forms different from the above-mentioned embodiments, and those skilled in the art can make equivalent transformations or modifications without violating the spirit of the present invention. Corresponding changes should all belong to the protection scope of the present utility model.

Claims (6)

1. the boiler heating system of reactor, it is characterised in that:Including the first reactor(1), the second reactor(2)And steam kettle Stove(3), first reactor(1)Outside is provided with cooling sandwith layer, is configured with cooling water cavity in the cooling sandwith layer(11), institute State cooling water cavity(11)With water inlet(111)And outlet(112), the steam boiler(3)With a water supplement port(31)And Steam outlet(32), the outlet(112)With water supplement port(31)By a moisturizing pipeline(33)Connection;Second reaction Kettle(2)Outside is provided with a heat-insulation layer, in heat-insulation layer and the second reactor(2)There is between outer wall a cavity(21), the sky Chamber(21)The second reactor of coiling is configured with inside(2)The jet chimney of outer wall(22), the jet chimney(22)Inside it is configured with and leads Hot oil pipeline(23), the steam outlet(32)By a steam output pipe(34)It is connected to jet chimney(22)Entrance End, the jet chimney(22)The port of export be provided with outer discharge pipe, the heat conducting oil pipe(23)Arrival end and the port of export It is respectively connecting to conducting oil circulation apparatus.
2. the boiler heating system of reactor according to claim 1, it is characterised in that:The moisturizing pipeline(33)On match somebody with somebody It is equipped with by outlet(112)To water supplement port(31)The check valve of direction conducting(4).
3. the boiler heating system of reactor according to claim 1, it is characterised in that:The water supplement port(31)Place's configuration There is a liquid-level switch(5), the liquid-level switch(5)Can be according to steam boiler(3)The height of interior water level and control water supplement port (31)Switch.
4. the boiler heating system of reactor according to claim 1, it is characterised in that:The conducting oil circulation apparatus bag Include a Heat-transfer Oil Pump.
5. the boiler heating system of reactor according to claim 1, it is characterised in that:The steam boiler(3)Also match somebody with somebody It is equipped with main water supplement port(35), the main water supplement port(35)It is connected with running water pipe, and is configured with switch valve(351).
6. the boiler heating system of reactor according to claim 1, it is characterised in that:The cavity(21)It is configured with cold But water inlet(211)And coolant outlet(212).
CN201620988041.0U 2016-08-30 2016-08-30 Reactor boiler heating system Active CN206064382U (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107321571A (en) * 2017-07-31 2017-11-07 浙江越千树数码科技有限公司 Coating machine glue flow directing device
CN112629274A (en) * 2020-12-24 2021-04-09 安徽省绩溪县华宇防火滤料有限公司 Waste heat recovery system in glass fiber production process

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107321571A (en) * 2017-07-31 2017-11-07 浙江越千树数码科技有限公司 Coating machine glue flow directing device
CN112629274A (en) * 2020-12-24 2021-04-09 安徽省绩溪县华宇防火滤料有限公司 Waste heat recovery system in glass fiber production process
CN112629274B (en) * 2020-12-24 2024-01-09 安徽省绩溪县华宇防火滤料有限公司 Waste heat recovery system in glass fiber production process

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Address after: 528400 Tanbeibaili Administrative Zone, Dongsheng Town, Zhongshan City, Guangdong Province

Patentee after: Guangdong Xinhui Chemical Co., Ltd.

Address before: 528400 Tanbeibaili Administrative Zone, Dongsheng Town, Zhongshan City, Guangdong Province

Patentee before: Zhongshan Xinhui Chemical Products Co., Ltd.