CN211425097U - Primary cooler - Google Patents
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- CN211425097U CN211425097U CN202020077559.5U CN202020077559U CN211425097U CN 211425097 U CN211425097 U CN 211425097U CN 202020077559 U CN202020077559 U CN 202020077559U CN 211425097 U CN211425097 U CN 211425097U
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- 238000001816 cooling Methods 0.000 claims abstract description 70
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 39
- 239000000571 coke Substances 0.000 claims abstract description 17
- 238000010438 heat treatment Methods 0.000 claims description 26
- 238000005057 refrigeration Methods 0.000 claims description 11
- 239000003034 coal gas Substances 0.000 claims description 3
- 239000007789 gas Substances 0.000 description 20
- 239000000498 cooling water Substances 0.000 description 18
- 238000005265 energy consumption Methods 0.000 description 6
- 239000003245 coal Substances 0.000 description 5
- 238000000034 method Methods 0.000 description 4
- 238000004939 coking Methods 0.000 description 3
- 238000002485 combustion reaction Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 230000008569 process Effects 0.000 description 3
- 230000001172 regenerating effect Effects 0.000 description 2
- 239000002918 waste heat Substances 0.000 description 2
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 description 1
- 235000011114 ammonium hydroxide Nutrition 0.000 description 1
- 238000003763 carbonization Methods 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000011280 coal tar Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000000197 pyrolysis Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
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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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/25—Process efficiency
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- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
本实用新型公开了一种初冷器,包括初冷器塔体,在初冷器塔体顶部设有煤气进口,在初冷器塔体底部设有煤气出口,在初冷器塔体中部上下分别设有上段循环水冷却横管和下段循环水冷却横管,上段循环水冷却横管和下段循环水冷却横管的进口和出口分别穿过初冷器塔体侧壁,并置于初冷器塔体外部,其还包括中段风冷冷却横管、过滤器和引风机,中段风冷冷却横管安装于上段循环水冷却横管和下段循环水冷却横管之间的初冷器塔体内部;中段风冷冷却横管的进口与过滤器的出口连接,中段风冷冷却横管的出口与引风机的进风口连接,引风机的出风口与焦炉蓄热室的进气口连接,优点:增加中段空气换热,提高换热效率;换热后的空气进入焦炉蓄热室,提升焦炉的效率。
The utility model discloses a primary cooler, which comprises a primary cooler tower body, a gas inlet is arranged at the top of the primary cooler tower body, a gas outlet is arranged at the bottom of the primary cooler tower body, and the upper and lower parts of the primary cooler tower body are arranged up and down. The upper circulating water cooling horizontal tube and the lower circulating water cooling horizontal tube are respectively provided. The inlet and outlet of the upper circulating water cooling horizontal tube and the lower circulating water cooling horizontal tube respectively pass through the side wall of the primary cooler tower, and are placed in the primary cooler. Outside the cooling tower body, it also includes a middle air-cooled cooling horizontal pipe, a filter and an induced draft fan. The middle air-cooled cooling horizontal pipe is installed in the primary cooler tower body between the upper circulating water cooling horizontal pipe and the lower circulating water cooling horizontal pipe. Inside; the inlet of the middle air-cooled cooling pipe is connected to the outlet of the filter, the outlet of the middle air-cooled cooling pipe is connected to the air inlet of the induced draft fan, and the air outlet of the induced draft fan is connected to the air inlet of the coke oven regenerator. Advantages: increase the air heat exchange in the middle section and improve the heat exchange efficiency; the air after heat exchange enters the coke oven regenerator to improve the coke oven efficiency.
Description
技术领域:Technical field:
本实用新型涉及节能降耗领域,具体涉及一种初冷器。The utility model relates to the field of energy saving and consumption reduction, in particular to a primary cooler.
背景技术:Background technique:
煤炭焦化又称煤炭高温干馏。以煤为原料,在隔绝空气条件下,加热到950度左右,炼焦过程主要是在焦炉内进行,现代焦炉主要由三室两区组成,即炭化室、燃烧室、蓄热室、斜道区、炉顶区和基础部分,蓄热室的作用就是利用蓄积废气的热量来预热焦炉炼焦所需的空气和贫煤气。煤在焦炉内经高温干馏生产焦炭,同时获得煤气、煤焦油并回收其它化工产品的一种煤转化工艺。其中,焦炉排出的煤气温度约750度,经循环氨水喷洒冷却后形成80-83度的饱和煤气,为后续煤气净化,需要经初冷器冷却到20-25度的要求。Coal coking is also called high temperature coal retorting. Using coal as raw material, it is heated to about 950 degrees under the condition of isolating air. The coking process is mainly carried out in a coke oven. Modern coke ovens are mainly composed of three chambers and two areas, namely carbonization chamber, combustion chamber, regenerator, and chute. The function of the regenerator is to use the heat of the accumulated exhaust gas to preheat the air and lean gas required for coking in the coke oven. A coal conversion process in which coal is produced by high-temperature dry distillation in a coke oven, and coal gas, coal tar and other chemical products are recovered at the same time. Among them, the temperature of the gas discharged from the coke oven is about 750 degrees. After being sprayed and cooled by the circulating ammonia water, a saturated gas of 80-83 degrees is formed. For the subsequent gas purification, it needs to be cooled to 20-25 degrees by the primary cooler.
现常用的初冷器为横管式初冷器,内部有若干根横向管道,冷却水通过循环制冷系统制冷并在管道中循环。冷却水又分为一段冷却水和二段冷却水,一段冷却水温度一般在25-32度,在初冷器上半部分循环;二段冷却水温度一般在18-25度,在初冷器下半部分循环。热气体由初冷器顶部进入,再由底部出去,热气体在初冷器里遇到横管内的冷却水而降温,使出初冷器的气体温度达到要求。The commonly used primary coolers are horizontal tube primary coolers, which have several horizontal pipes inside, and the cooling water is cooled by a circulating refrigeration system and circulated in the pipes. The cooling water is divided into a first-stage cooling water and a second-stage cooling water. The temperature of the first-stage cooling water is generally 25-32 degrees, and it circulates in the upper part of the primary cooler; The second half loops. The hot gas enters from the top of the primary cooler, and then exits from the bottom. The hot gas encounters the cooling water in the horizontal tube in the primary cooler to cool down, so that the gas temperature of the primary cooler meets the requirements.
上述系统在运行过程中存在以下问题:(1)一段冷却水较二段冷却水温度高,一段冷却和二段冷却换热段较长,导致对高温煤气换热的效率低,降温的效果差,一段冷却水出水配备的循环制冷系统能耗高;(2)通常在初冷器上半部分的一段冷却水换热出来时的温度高达60度以上,此高温水缺少有效利用,导致资源的浪费。The above system has the following problems in the operation process: (1) The temperature of the cooling water in the first stage is higher than that of the cooling water in the second stage, and the heat exchange section between the first stage cooling and the second stage cooling is longer, resulting in low heat exchange efficiency for high temperature gas and poor cooling effect. , the circulating refrigeration system equipped with the first-stage cooling water outlet has high energy consumption; (2) Usually, the temperature of the first-stage cooling water in the upper part of the primary cooler is as high as 60 degrees after heat exchange. waste.
实用新型内容:Utility model content:
本实用新型的目的在于提供一种初冷器。The purpose of this utility model is to provide a primary cooler.
本实用新型由如下技术方案实施:The utility model is implemented by the following technical solutions:
一种初冷器,包括初冷器塔体,在所述初冷器塔体顶部设有煤气进口,在所述初冷器塔体底部设有煤气出口,在所述初冷器塔体中部上下分别设有上段循环水冷却横管和下段循环水冷却横管,所述上段循环水冷却横管和下段循环水冷却横管的进口和出口分别穿过所述初冷器塔体侧壁,并置于所述初冷器塔体外部,其还包括中段风冷冷却横管、过滤器和引风机,所述中段风冷冷却横管安装在所述上段循环水冷却横管和所述下段循环水冷却横管之间的所述初冷器塔体内部,所述中段风冷冷却横管的进口和出口分别穿过所述初冷器塔体侧壁,并置于所述初冷器塔体外部;A primary cooler, comprising a primary cooler tower body, a gas inlet is provided at the top of the primary cooler tower body, a gas outlet is provided at the bottom of the primary cooler tower body, and a middle part of the primary cooler tower body is provided The upper and lower circulating water cooling horizontal pipes and the lower circulating water cooling horizontal pipes are respectively provided. It is placed on the outside of the primary cooler tower body, and it also includes a middle-section air-cooled cooling transverse pipe, a filter and an induced draft fan, and the middle-section air-cooled cooling transverse pipe is installed on the upper circulating water cooling transverse pipe and the lower section. The inside of the primary cooler tower body between the circulating water cooling horizontal tubes, the inlet and outlet of the middle air-cooled cooling horizontal tube pass through the side wall of the primary cooler tower body respectively, and are placed in the primary cooler outside the tower;
所述中段风冷冷却横管的进口与所述过滤器的出口连接,所述中段风冷冷却横管的出口与所述引风机的进风口连接,所述引风机的出风口与焦炉蓄热室的空气进气口连接。The inlet of the middle-section air-cooling and cooling horizontal pipe is connected with the outlet of the filter, the outlet of the middle-section air-cooling and cooling horizontal pipe is connected with the air inlet of the induced draft fan, and the air outlet of the induced draft fan is connected with the coke oven accumulator. The air inlet of the hot chamber is connected.
优选的,其还包括供暖系统;在所述上段循环水冷却横管的出口分别通过管路与循环制冷系统的进口和所述供暖系统的进口连通,所述循环制冷系统的出口和所述供暖系统的出口分别通过管路与所述上段循环水冷却横管的进口连通,在所述上段循环水冷却横管的出口和所述供暖系统之间的管路上设有供暖控制阀。Preferably, it also includes a heating system; the outlet of the upper circulating water cooling horizontal pipe is communicated with the inlet of the circulating refrigeration system and the inlet of the heating system respectively through pipelines, and the outlet of the circulating refrigeration system is connected to the heating system. The outlet of the system is respectively communicated with the inlet of the upper circulating water cooling horizontal pipe through pipelines, and a heating control valve is provided on the pipeline between the outlet of the upper circulating water cooling horizontal pipe and the heating system.
本实用新型的优点:增加中段风冷冷却横管对初冷器塔体中的热煤气风冷换热,提升降低煤气温度的效果,提高换热效率,减少循环制冷系统的能耗;并且换热后的高温空气排进焦炉蓄热室内,能够提高蓄热焦炉内的温度,使空气和贫煤气的燃烧效率得到提升,降低能耗;其次,在冬季可以将上段循环水冷却横管出口出来的高温冷却水导进供暖系统,用于厂区供暖,对上段循环水冷却横管的冷却水余热进行有效利用,减少供暖系统的能耗。The advantages of the utility model: increase the air-cooled heat exchange of the hot gas in the primary cooler tower body by the middle-section air-cooled cooling horizontal pipe, improve the effect of reducing the gas temperature, improve the heat exchange efficiency, and reduce the energy consumption of the circulating refrigeration system; The heated high-temperature air is discharged into the coke oven regenerative chamber, which can increase the temperature in the regenerative coke oven, improve the combustion efficiency of air and lean gas, and reduce energy consumption; secondly, in winter, the upper circulating water can be used to cool the horizontal pipe The high-temperature cooling water from the outlet is led into the heating system for heating the plant area, and the waste heat of the cooling water in the upper circulating water cooling horizontal pipe is effectively utilized to reduce the energy consumption of the heating system.
附图说明:Description of drawings:
为了更清楚地说明本实用新型实施例或现有技术中的技术方案,下面将对实施例或现有技术描述中所需要使用的附图作简单地介绍,显而易见地,下面描述中的附图仅仅是本实用新型的一些实施例,对于本领域普通技术人员来讲,在不付出创造性劳动的前提下,还可以根据这些附图获得其他的附图。In order to more clearly illustrate the embodiments of the present utility model or the technical solutions in the prior art, the following briefly introduces the accompanying drawings that need to be used in the description of the embodiments or the prior art. Obviously, the accompanying drawings in the following description These are just some embodiments of the present invention, and for those of ordinary skill in the art, other drawings can also be obtained from these drawings without creative effort.
图1是本实用新型整体结构的示意图。Figure 1 is a schematic diagram of the overall structure of the present invention.
图中:焦炉蓄热室1、初冷器塔体2、煤气进口3、煤气出口4、上段循环水冷却横管5、下段循环水冷却横管6、中段风冷冷却横管7、过滤器8、引风机9、供暖系统10、供暖控制阀11、循环制冷系统12。In the figure: coke oven regenerator 1,
具体实施方式:Detailed ways:
下面将结合本实用新型实施例中的附图,对本实用新型实施例中的技术方案进行清楚、完整地描述,显然,所描述的实施例仅仅是本实用新型一部分实施例,而不是全部的实施例。基于本实用新型中的实施例,本领域普通技术人员在没有作出创造性劳动前提下所获得的所有其他实施例,都属于本实用新型保护的范围。The technical solutions in the embodiments of the present utility model will be clearly and completely described below with reference to the accompanying drawings in the embodiments of the present utility model. Obviously, the described embodiments are only a part of the embodiments of the present utility model, rather than all the implementations. example. Based on the embodiments of the present invention, all other embodiments obtained by those of ordinary skill in the art without creative work fall within the protection scope of the present invention.
如图1所示,一种初冷器,包括初冷器塔体2,在初冷器塔体2顶部设有煤气进口3,在初冷器塔体2底部设有煤气出口4,在初冷器塔体2中部上下分别设有上段循环水冷却横管5和下段循环水冷却横管6,上段循环水冷却横管5和下段循环水冷却横管6的进口和出口分别穿过初冷器塔体2侧壁,并置于初冷器塔体2外部,其还包括中段风冷冷却横管7、过滤器8和引风机9,中段风冷冷却横管7安装在上段循环水冷却横管5和下段循环水冷却横管6之间的初冷器塔体2内部,中段风冷冷却横管7的进口和出口分别穿过初冷器塔体2侧壁,并置于初冷器塔体2外部;As shown in Figure 1, a kind of primary cooler includes primary
中段风冷冷却横管7的进口与过滤器8的出口连接,中段风冷冷却横管7的出口与引风机9的进风口连接,引风机9的出风口与焦炉蓄热室1的空气进气口连接。The inlet of the middle air-cooling and cooling
通过引风机9将空气从中段风冷冷却横管7的进口引入,过滤器8过滤掉空气中的杂质,中段风冷冷却横管7中的空气为低温空气,可以对初冷器塔体2中的热煤气换热冷却,提升降低煤气温度的效果,提高换热效率;并且换热后空气从中段风冷冷却横管7的出口排进焦炉蓄热室1内,中段风冷冷却横管7排出的空气为高温空气,能够增加焦炉内的温度,使焦炉的燃烧效率得到提升,降低能耗。Air is introduced into the inlet of the mid-section air-cooled and cooled
其还包括供暖系统10;在上段循环水冷却横管5的出口分别通过管路与循环制冷系统12的进口和供暖系统10的进口连通,循环制冷系统12的出口和供暖系统10的出口分别通过管路与上段循环水冷却横管5的进口连通,在上段循环水冷却横管5的出口和供暖系统10之间的管路上设有供暖控制阀11。通常情况下,上段循环水冷却横管5换热后的冷却水会先进入循环制冷系统12,降低冷却水温度后,再重回上段循环水冷却横管5冷却换热;由于上段循环水冷却横管5出口出来的冷却水温度高达60度以上,因此在冬季可以将上段循环水冷却横管5出口出来的冷却水导进供暖系统10,进行供暖后再回上段循环水冷却横管5,重新投入换热工作中;具体操作为,打开供暖控制阀11,使上段循环水冷却横管5出口出来的冷却水一部分进入供暖系统10;对上段循环水冷却横管5的冷却水余热进行有效利用,减少供暖系统10的能耗。供暖系统10为各厂区、办公楼或宿舍使用。It also includes a
以上所述仅为本实用新型的较佳实施例而已,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 are only preferred embodiments of the present invention, and are not intended to limit the present invention. Any modification, equivalent replacement, improvement, etc. made within the spirit and principle of the present invention shall be included in the within the protection scope of the present invention.
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CN115468441A (en) * | 2022-08-31 | 2022-12-13 | 中冶焦耐(大连)工程技术有限公司 | Modular detachable plate type gas cooler |
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