CN205127741U - Coke oven burnt gas deNOx systems - Google Patents
Coke oven burnt gas deNOx systems Download PDFInfo
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- CN205127741U CN205127741U CN201520718160.XU CN201520718160U CN205127741U CN 205127741 U CN205127741 U CN 205127741U CN 201520718160 U CN201520718160 U CN 201520718160U CN 205127741 U CN205127741 U CN 205127741U
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Abstract
本实用新型实施例公开了一种焦炉燃烧废气脱硝系统，包括焦炉；还包括：烟气管路、SCR脱硝装置及引风机，所述SCR脱硝装置及所述引风机位于所述烟气管路上；所述SCR脱硝装置具有废气入口和废气出口，其废气入口通过烟气管路与焦炉的蓄热室废气出口相连；所述SCR脱硝装置的废气出口通过烟气管路与所述引风机的废气入口相连；通过改变所述焦炉的蓄热室内格子砖的数量及其排布方式，使进入SCR脱硝装置的焦炉燃烧废气的温度达到250℃-450℃。该系统满足了采用SCR技术进行脱硝的要求，能够实现焦化企业产生的焦炉燃烧废气的脱硝处理。
The embodiment of the utility model discloses a coke oven combustion waste gas denitrification system, which includes a coke oven; and also includes: a flue gas pipeline, an SCR denitrification device and an induced draft fan, and the SCR denitration device and the induced draft fan are located in the flue gas On the pipeline; the SCR denitrification device has a waste gas inlet and a waste gas outlet, and its waste gas inlet is connected to the regenerator waste gas outlet of the coke oven through a flue gas pipeline; the waste gas outlet of the SCR denitrification device is connected to the The exhaust gas inlet of the induced draft fan is connected; by changing the number and arrangement of checker bricks in the regenerator of the coke oven, the temperature of the coke oven combustion exhaust gas entering the SCR denitrification device reaches 250°C-450°C. The system meets the requirements of using SCR technology for denitrification, and can realize the denitrification treatment of coke oven combustion waste gas produced by coking enterprises.
Description
技术领域 technical field
本实用新型涉及焦炉燃烧废气净化领域，特别涉及一种焦炉燃烧废气脱硝系统。 The utility model relates to the field of coke oven combustion waste gas purification, in particular to a coke oven combustion waste gas denitrification system.
背景技术 Background technique
焦化企业在生产过程中会产生大量的焦炉燃烧废气，这里所说的焦炉燃烧废气是指由煤气与空气在焦炉立火道内混合燃烧所产生的气体。所产生的焦炉燃烧废气中含有大量的氮氧化物(NOx)。现在各焦化企业的焦炉燃烧废气均需经过立火道、蓄热室、小烟道、废气交换开闭器、分烟道、总烟道、烟囱排入大气，其中蓄热室位于焦炉本体中部是回收废气余热的单元，焦炉燃烧废气的直接排放给环境造成严重污染。我国规定自2015年1月1日起，现有焦化企业必须执行GB16171-2012排放标准。也就是说，焦化企业以后产生的焦炉燃烧废气在排放之前必须经过脱硝(即脱氮氧化物)处理。 Coking enterprises will produce a large amount of coke oven combustion exhaust gas during the production process. The coke oven combustion exhaust gas mentioned here refers to the gas produced by the mixed combustion of coal gas and air in the coke oven vertical flue. The coke oven combustion exhaust gas produced contains a large amount of nitrogen oxides (NO x ). At present, the coke oven combustion waste gas of various coking enterprises needs to be discharged into the atmosphere through the vertical flue, regenerator, small flue, exhaust gas exchange switch, branch flue, main flue, and chimney, and the regenerator is located in the coke oven. The middle part of the main body is the unit for recovering the waste heat of the waste gas, and the direct discharge of the waste gas from the combustion of the coke oven causes serious pollution to the environment. my country stipulates that from January 1, 2015, existing coking enterprises must implement the GB16171-2012 emission standard. That is to say, the coke oven combustion exhaust gas produced by coking enterprises must be denitrified (that is, denitrified oxides) before being discharged.
选择性催化还原技术(SelecitveCatalyticReduction，简称SCR)是比较成熟的脱硝技术，该技术由于具有不形成二次污染、装置结构简单、并且脱硝效率高(可达90％以上)，运行可靠、便于维护等特点，已广泛应用于电力、水泥、玻璃等行业。采用SCR技术进行脱硝时，待脱硝气体的温度要达到250℃以上。但是，焦化企业产生的焦炉燃烧废气在经过蓄热室回收热量后，其温度会下降到250℃以下，无法满足采用SCR技术进行脱硝的要求。 Selective catalytic reduction technology (SelecitveCatalyticReduction, referred to as SCR) is a relatively mature denitrification technology. This technology has no secondary pollution, simple device structure, high denitrification efficiency (up to 90%), reliable operation, and easy maintenance. Features, has been widely used in electric power, cement, glass and other industries. When SCR technology is used for denitrification, the temperature of the gas to be denitrated must reach above 250°C. However, the temperature of coke oven combustion waste gas produced by coking enterprises will drop below 250°C after heat recovery in the regenerator, which cannot meet the requirements of SCR technology for denitrification.
因此，开发出一种能够采用SCR技术实现焦炉燃烧废气脱硝的系统十分必要。 Therefore, it is necessary to develop a system that can use SCR technology to realize denitrification of coke oven combustion exhaust gas.
实用新型内容 Utility model content
本实用新型实施例的目的在于提供一种焦炉燃烧废气脱硝系统，用于解决焦化企业产生的焦炉燃烧废气在经过蓄热室换热后，无法采用SCR技术进行脱硝的问题。技术方案如下： The purpose of the embodiment of the utility model is to provide a coke oven combustion exhaust gas denitrification system, which is used to solve the problem that the coke oven combustion exhaust gas produced by coking enterprises cannot be denitrated by SCR technology after heat exchange in the regenerator. The technical scheme is as follows:
一种焦炉燃烧废气脱硝系统，包括焦炉；还包括：烟气管路、SCR脱硝装置及引风机， A coke oven combustion waste gas denitrification system, including a coke oven; also includes: a flue gas pipeline, an SCR denitrification device and an induced draft fan,
所述SCR脱硝装置及所述引风机位于所述烟气管路上； The SCR denitrification device and the induced draft fan are located on the flue gas pipeline;
所述SCR脱硝装置具有废气入口和废气出口，其废气入口通过烟气管路与焦炉的蓄热室废气出口相连； The SCR denitrification device has a waste gas inlet and a waste gas outlet, and the waste gas inlet is connected to the regenerator waste gas outlet of the coke oven through a flue gas pipeline;
所述SCR脱硝装置的废气出口通过烟气管路与所述引风机的废气入口相连； The exhaust gas outlet of the SCR denitration device is connected to the exhaust gas inlet of the induced draft fan through a flue gas pipeline;
通过改变所述焦炉的蓄热室内格子砖的数量及其排布方式，使进入SCR脱硝装置的焦炉燃烧废气的温度达到250℃-450℃。 By changing the number and arrangement of checker bricks in the regenerator of the coke oven, the temperature of the coke oven combustion exhaust gas entering the SCR denitrification device can reach 250°C-450°C.
在本实用新型的一种具体实施方式中，所述SCR脱硝装置的废气出口与所述引风机的废气入口之间的烟气管路上设置有余热回收装置。 In a specific embodiment of the present invention, a waste heat recovery device is arranged on the flue gas pipeline between the exhaust gas outlet of the SCR denitrification device and the exhaust gas inlet of the induced draft fan.
在本实用新型的一种具体实施方式中，所述SCR脱硝装置的废气出口与所述引风机的废气入口之间的烟气管路上设置有脱硫装置。 In a specific embodiment of the present invention, a desulfurization device is arranged on the flue gas pipeline between the exhaust gas outlet of the SCR denitrification device and the exhaust gas inlet of the induced draft fan.
在本实用新型的一种具体实施方式中，所述余热回收装置的废气出口与引风机的废气入口之间的烟气管路上设置有脱硫装置。 In a specific embodiment of the present invention, a desulfurization device is arranged on the flue gas pipeline between the exhaust gas outlet of the waste heat recovery device and the exhaust gas inlet of the induced draft fan.
在本实用新型的一种具体实施方式中，所述SCR脱硝装置的废气入口侧的烟气管路上设置有第一切断阀；所述引风机的废气出口侧的烟气管路上设置有第二切断阀。 In a specific embodiment of the present invention, a first cut-off valve is provided on the flue gas pipeline at the exhaust gas inlet side of the SCR denitrification device; a second cut-off valve is arranged on the flue gas pipeline at the exhaust gas outlet side of the induced draft fan. Shut-off valve.
在本实用新型的一种具体实施方式中，所述烟气管路与焦炉的总烟道并联连通。 In a specific embodiment of the present utility model, the flue gas pipeline communicates in parallel with the main flue of the coke oven.
在本实用新型的一种具体实施方式中，所述总烟道上设置有旁路阀门。 In a specific embodiment of the present utility model, a bypass valve is provided on the main flue.
本实用新型提供的焦炉燃烧废气脱硝系统，通过将SCR脱硝装置的废气入口通过烟气管路与焦炉蓄热室的废气出口相连，并通过改变所述焦炉的蓄热室内格子砖的数量及其排布方式，使进入SCR脱硝装置的焦炉燃烧废气的温度达到250℃-450℃，满足了采用SCR技术进行脱硝的要求，能够实现焦化企业产生的焦炉燃烧废气的脱硝处理。 The coke oven combustion waste gas denitrification system provided by the utility model connects the waste gas inlet of the SCR denitrification device with the waste gas outlet of the coke oven regenerator through the flue gas pipeline, and changes the grid brick in the regenerator of the coke oven. The quantity and its arrangement make the temperature of the coke oven combustion exhaust gas entering the SCR denitrification device reach 250°C-450°C, which meets the requirements of using SCR technology for denitrification, and can realize the denitrification treatment of the coke oven combustion exhaust gas generated by coking enterprises.
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 technical solutions in the embodiments of the present invention or the prior art, the following will briefly introduce 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 only some embodiments of the utility model, and those skilled in the art can also obtain other drawings based on these drawings without creative work.
图1为本实用新型提供的第一种焦炉燃烧废气脱硝系统； Fig. 1 is the first coke oven combustion waste gas denitrification system provided by the utility model;
图2为本实用新型提供的第二种焦炉燃烧废气脱硝系统； Fig. 2 is the second coke oven combustion waste gas denitrification system provided by the utility model;
图3为本实用新型提供的第三种焦炉燃烧废气脱硝系统； Fig. 3 is the third coke oven combustion waste gas denitrification system provided by the utility model;
图4为本实用新型提供第四种焦炉燃烧废气脱硝系统； Fig. 4 provides the fourth coke oven combustion waste gas denitrification system for the present invention;
图5为本实用新型提供第五种焦炉燃烧废气脱硝系统。 Fig. 5 is the fifth coke oven combustion waste gas denitrification system provided by the present invention.
具体实施方式 detailed description
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 invention will be clearly and completely described below in conjunction with the accompanying drawings in the embodiments of the present invention. Obviously, the described embodiments are only part of the embodiments of the present invention, not all of them. example. Based on the embodiments of the present utility model, all other embodiments obtained by persons of ordinary skill in the art without making creative efforts belong to the scope of protection of the present utility model.
本实用新型提供了一种焦炉废气脱硝系统，如图1所示，至少包括：包括焦炉1、烟气管路2、SCR脱硝装置3及引风机4， The utility model provides a coke oven waste gas denitrification system, as shown in Figure 1, at least comprising: a coke oven 1, a flue gas pipeline 2, an SCR denitrification device 3 and an induced draft fan 4,
所述SCR脱硝装置3及所述引风机4位于所述烟气管路2上； The SCR denitrification device 3 and the induced draft fan 4 are located on the flue gas pipeline 2;
所述SCR脱硝装置3具有废气入口和废气出口，其废气入口通过烟气管路2与焦炉1的蓄热室废气出口相连； The SCR denitrification device 3 has a waste gas inlet and a waste gas outlet, and the waste gas inlet is connected to the regenerator waste gas outlet of the coke oven 1 through the flue gas pipeline 2;
所述SCR脱硝装置3的废气出口通过烟气管路2与所述引风机4的废气入口相连；所说的引风机4优选配有变频电机，通过对引风机4进行变频调速，既能保证焦炉1正常生产所需要的负压，也能保证焦炉燃烧废气通过SCR脱硝装置3所需要的压力值； The exhaust gas outlet of the SCR denitrification device 3 is connected to the exhaust gas inlet of the induced draft fan 4 through the flue gas pipeline 2; It can ensure the negative pressure required for the normal production of the coke oven 1, and can also ensure the pressure value required for the coke oven combustion exhaust gas to pass through the SCR denitrification device 3;
通过改变所述焦炉1的蓄热室内格子砖的数量及其排布方式，使进入SCR脱硝装置3的焦炉燃烧废气的温度达到250℃-450℃。 By changing the number and arrangement of checker bricks in the regenerator of the coke oven 1, the temperature of the coke oven combustion exhaust gas entering the SCR denitrification device 3 reaches 250°C-450°C.
对于焦炉1的蓄热室内格子砖的数量及其排布方式，只要保证进入SCR脱硝装置3的焦炉燃烧废气的温度达到250℃-450℃，优选为300℃-350℃即可，格子砖的具体数量及其具体的排布方式可以根据焦炉1实际所产生的废气的量及其具体的温度而定，本实用新型在此不进行限定。 As for the number of checker bricks in the regenerator chamber of the coke oven 1 and their arrangement, it is only necessary to ensure that the temperature of the coke oven combustion exhaust gas entering the SCR denitrification device 3 reaches 250°C-450°C, preferably 300°C-350°C. The specific number of bricks and their specific arrangement can be determined according to the amount of waste gas actually produced by the coke oven 1 and its specific temperature, which is not limited by the present invention.
在实际应用中，焦炉燃烧废气从焦炉1的蓄热室废气出口排出，通过烟气管路2进入SCR脱硝装置3，由于改变了焦炉1的蓄热室内格子砖的数量及其排布方式，因此可以使得进入SCR脱硝装置3的焦炉燃烧废气的温度达到SCR脱硝技术的要求，即可以达到250℃-450℃，优选为300℃-350℃；从而可以采用SCR脱硝技术对焦炉燃烧废气进行脱硝处理，脱硝处理过程中所需要的还原剂可以采用氨气或液氨。考虑到经济因素，更优选的采用焦化企业蒸氨工段生产的氨水或蒸氨塔顶排出的氨气。脱硝处理的焦炉废气最后进入到烟囱，然后排放至大气中。 In practical application, the coke oven combustion exhaust gas is discharged from the exhaust gas outlet of the regenerator of coke oven 1, and enters the SCR denitrification device 3 through the flue gas pipeline 2. Therefore, the temperature of the coke oven combustion exhaust gas entering the SCR denitrification device 3 can meet the requirements of the SCR denitrification technology, that is, it can reach 250°C-450°C, preferably 300°C-350°C; thus, the SCR denitrification technology can be used to focus The furnace combustion waste gas is denitrified, and the reducing agent required in the denitrification process can be ammonia gas or liquid ammonia. In consideration of economic factors, it is more preferable to use the ammonia water produced by the ammonia distillation section of the coking enterprise or the ammonia gas discharged from the top of the ammonia distillation tower. The denitrated coke oven exhaust gas finally enters the chimney, and then is discharged into the atmosphere.
需要说明的是，SCR脱硝技术其及所对应的SCR脱硝装置均为现有技术，本实用新型在此无需对其进行赘述。 It should be noted that the SCR denitrification technology and the corresponding SCR denitrification device are both existing technologies, and the present invention does not need to repeat them here.
在实际应用中，经过SCR脱硝装置3脱硝处理后的焦炉燃烧废气还有较高的温度，可以进一步地回收其中的热量。具体的，如图2所示，可以在SCR脱硝装置3的废气出口与所述引风机4的废气入口之间的烟气管路上设置有余热回收装置5，对于余热回收装置5的具体形式可以采用现有技术的相关技术方案来实现，本实用新型在此不进行限定，例如，余热回收装置5具体可以为本领域常用的余热锅炉。 In practical applications, the coke oven combustion waste gas after the denitrification treatment by the SCR denitrification device 3 still has a relatively high temperature, and the heat therein can be further recovered. Specifically, as shown in Figure 2, a waste heat recovery device 5 can be arranged on the flue gas pipeline between the exhaust gas outlet of the SCR denitrification device 3 and the exhaust gas inlet of the induced draft fan 4, and the specific form of the waste heat recovery device 5 can be It is realized by adopting related technical solutions of the prior art, and the utility model is not limited here. For example, the waste heat recovery device 5 may specifically be a waste heat boiler commonly used in the field.
在实际应用中，还可以根据需要在烟气管路2上增加脱硫装置对焦炉燃烧废气进行脱硫处理，进一步地消除废气中的污染物。 In practical applications, a desulfurization device can also be added to the flue gas pipeline 2 for desulfurization treatment of coke oven combustion waste gas to further eliminate pollutants in the waste gas.
具体的，如图3所示，脱硫装置6可以设置在SCR脱硝装置3的废气出口与所述引风机4的废气入口之间，也可以如图4所示，将脱硫装置6设置在余热回收装置5的废气出口与引风机4的废气入口之间。具体如何设置可以根据是否需要进行热量回收以及脱硫装置6进行脱硫处理时所需要的温度而定。 Specifically, as shown in Figure 3, the desulfurization device 6 can be arranged between the exhaust gas outlet of the SCR denitrification device 3 and the exhaust gas inlet of the induced draft fan 4, or as shown in Figure 4, the desulfurization device 6 can be arranged in the waste heat recovery Between the exhaust gas outlet of the device 5 and the exhaust gas inlet of the induced draft fan 4. The specific setting can be determined according to whether heat recovery is required and the temperature required for the desulfurization device 6 to perform desulfurization treatment.
在上述的各实施例中，可以在SCR脱硝装置3的废气入口侧的烟气管路2上设置有第一切断阀；在引风机4的废气出口侧的烟气管路2上设置有第二切断阀。当烟气管路2上的任一装置出现问题时，可以关闭第一切断阀及第二切断阀进行维修处理。 In each of the above-mentioned embodiments, a first cut-off valve can be provided on the flue gas pipeline 2 on the exhaust gas inlet side of the SCR denitrification device 3; Two cut-off valves. When any device on the flue gas pipeline 2 has a problem, the first shut-off valve and the second shut-off valve can be closed for maintenance.
对于焦化企业，一般焦炉燃烧废气是经过焦炉的总烟道进入烟囱，最后排入大气。对于这样的焦炉装置，为了实现本实用新型的目的，可以将上述各实施例中的烟气管路2与焦炉的总烟道并联连通，并在总烟道上设置旁路阀门。例如，在图4所示的实施例的基础上，将烟气管路2与焦炉的总烟道并联连通，所形成的焦炉燃烧废气脱硝系统如图5所示，当需要对焦炉燃烧废气进行脱硝、脱硫及余热回收时，就可以关闭总烟道上的旁路阀门10，打开烟气管路2上的第一切断阀7及第二切断阀8；焦炉燃烧废气就可以通过烟气管路2经过各装置后进入烟囱，并排入大气；当不需要对焦炉燃烧废气进行处理，或者烟气管路2上的任一装置出现问题时，可以关闭第一切断阀7及第二切断阀8，并打开旁路阀门10，以使焦炉燃烧废气通过总烟道9进入烟囱，并排入大气。 For coking enterprises, the waste gas from coke oven combustion generally enters the chimney through the main flue of the coke oven, and finally is discharged into the atmosphere. For such a coke oven device, in order to achieve the purpose of the utility model, the flue gas pipeline 2 in the above-mentioned embodiments can be connected in parallel with the main flue of the coke oven, and a bypass valve can be set on the main flue. For example, on the basis of the embodiment shown in Figure 4, the flue gas pipeline 2 is connected in parallel with the main flue of the coke oven, and the coke oven combustion waste gas denitrification system formed is shown in Figure 5. When the combustion exhaust gas is denitrified, desulfurized and waste heat is recovered, the bypass valve 10 on the main flue can be closed, and the first shut-off valve 7 and the second shut-off valve 8 on the flue gas pipeline 2 can be opened; the coke oven combustion exhaust gas can pass through The flue gas pipeline 2 enters the chimney after passing through various devices, and is discharged into the atmosphere; when there is no need to treat the coke oven combustion waste gas, or when there is a problem with any device on the flue gas pipeline 2, the first shut-off valve 7 can be closed And the second cut-off valve 8, and open the bypass valve 10, so that the coke oven combustion waste gas enters the chimney through the main flue 9, and is discharged into the atmosphere.
可以理解的是，图1-图3所示的具体实施方案也可以参照上述图5的技术方案将烟气管路2与焦炉的总烟道并联连通。 It can be understood that the specific embodiments shown in Fig. 1-Fig. 3 can also refer to the above-mentioned technical solution in Fig. 5 to connect the flue gas pipeline 2 in parallel with the main flue of the coke oven.
通过上述各实施例可以看出，本实用新型提供的焦炉燃烧废气脱硝系统，通过将SCR脱硝装置的废气入口通过烟气管路与焦炉蓄热室的废气出口相连，并通过改变所述焦炉的蓄热室内格子砖的数量及其排布方式，使进入SCR脱硝装置的焦炉燃烧废气的温度达到250℃-450℃，满足了采用SCR技术进行脱硝的要求，能够实现焦化企业产生的焦炉燃烧废气的脱硝处理，可以使得最终排放的焦炉燃烧废气中氮氧化物的含量小于150mg/m3，低于国家的GB16171-2012排放标准。而且，在对焦炉燃烧废气脱硝的基础上，还可以对其进行脱硫及余热回收处理，进一步地消除焦炉燃烧废气中的有害物质及回收有用的热量。 It can be seen from the above embodiments that the coke oven combustion waste gas denitrification system provided by the utility model connects the waste gas inlet of the SCR denitrification device with the waste gas outlet of the coke oven regenerator through the flue gas pipeline, and by changing the The number and arrangement of checker bricks in the regenerator chamber of the coke oven make the temperature of the coke oven combustion exhaust gas entering the SCR denitrification device reach 250°C-450°C, which meets the requirements of using SCR technology for denitrification and can realize the production of coking enterprises. The denitrification treatment of coke oven combustion exhaust gas can make the content of nitrogen oxides in the final coke oven combustion exhaust gas less than 150mg/m 3 , which is lower than the national GB16171-2012 emission standard. Moreover, on the basis of denitrification of coke oven combustion exhaust gas, it can also be desulfurized and waste heat recovery treatment to further eliminate harmful substances in coke oven combustion exhaust gas and recover useful heat.
需要说明的是，在本文中，诸如第一和第二等之类的关系术语仅仅用来将一个实体或者操作与另一个实体或操作区分开来，而不一定要求或者暗示这些实体或操作之间存在任何这种实际的关系或者顺序。而且，术语“包括”、“包含”或者其任何其他变体意在涵盖非排他性的包含，从而使得包括一系列要素的过程、方法、物品或者设备不仅包括那些要素，而且还包括没有明确列出的其他要素，或者是还包括为这种过程、方法、物品或者设备所固有的要素。在没有更多限制的情况下，由语句“包括一个……”限定的要素，并不排除在包括所述要素的过程、方法、物品或者设备中还存在另外的相同要素。 It should be noted that in this article, relational terms such as first and second are only used to distinguish one entity or operation from another entity or operation, and do not necessarily require or imply that there is a relationship between these entities or operations. There is no such actual relationship or order between them. Furthermore, the term "comprises", "comprises" or any other variation thereof is intended to cover a non-exclusive inclusion such that a process, method, article, or apparatus comprising a set of elements includes not only those elements, but also includes elements not expressly listed. other elements of or also include elements inherent in such a process, method, article, or apparatus. Without further limitations, an element defined by the phrase "comprising a ..." does not exclude the presence of additional identical elements in the process, method, article or apparatus comprising said element.
本说明书中的各个实施例均采用相关的方式描述，各个实施例之间相同相似的部分互相参见即可，每个实施例重点说明的都是与其他实施例的不同之处。 Each embodiment in this specification is described in a related manner, the same and similar parts of each embodiment can be referred to each other, and each embodiment focuses on the differences from other embodiments.
以上所述仅为本实用新型的较佳实施例而已，并非用于限定本实用新型的保护范围。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，均包含在本实用新型的保护范围内。 The above descriptions are only preferred embodiments of the present utility model, and are not intended to limit the protection scope of the present utility model. All modifications, equivalent replacements, improvements, etc. made within the spirit and principles of the present utility model are included in the protection scope of the present utility model.
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Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN106039958A (en) * | 2016-07-08 | 2016-10-26 | 山东源根化学技术研发有限公司 | Novel method for denitrifying coke oven waste gas |
| CN107174928A (en) * | 2017-07-07 | 2017-09-19 | 文安县天华密度板有限公司 | A kind of flue gas coproduction density board produces the method and device of desulphurization denitration |
| CN108686504A (en) * | 2017-04-05 | 2018-10-23 | 辽宁中弘信冶金技术有限公司 | The processing system and method for flue gases of cock oven |
| CN109059012A (en) * | 2018-08-16 | 2018-12-21 | 天津大学 | Ground flare closed type combusting device vent gas denitrating system and method |
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| CN110332814A (en) * | 2019-07-10 | 2019-10-15 | 成渝钒钛科技有限公司 | Coke oven flue gas waste heat utilization equipment and method thereof |
| CN110500603A (en) * | 2019-08-22 | 2019-11-26 | 山东郓城正华玻璃科技有限公司 | A kind of glass factory's exhaust gas denitration method |
| CN115090108A (en) * | 2022-06-17 | 2022-09-23 | 天津铁厂有限公司 | Treatment device and process for reducing nitrogen oxides in coke oven flue gas |
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- 2015-09-16 CN CN201520718160.XU patent/CN205127741U/en not_active Expired - Lifetime
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN106039958A (en) * | 2016-07-08 | 2016-10-26 | 山东源根化学技术研发有限公司 | Novel method for denitrifying coke oven waste gas |
| CN108686504A (en) * | 2017-04-05 | 2018-10-23 | 辽宁中弘信冶金技术有限公司 | The processing system and method for flue gases of cock oven |
| CN107174928A (en) * | 2017-07-07 | 2017-09-19 | 文安县天华密度板有限公司 | A kind of flue gas coproduction density board produces the method and device of desulphurization denitration |
| CN109059012A (en) * | 2018-08-16 | 2018-12-21 | 天津大学 | Ground flare closed type combusting device vent gas denitrating system and method |
| CN109059012B (en) * | 2018-08-16 | 2023-10-10 | 天津大学 | Ground torch closed combustor exhaust gas denitration system and method |
| CN109550348A (en) * | 2018-10-29 | 2019-04-02 | 中国石油天然气集团有限公司 | Viscous crude fireflood produces the processing method and processing device of fixed gas in gas |
| CN110332814A (en) * | 2019-07-10 | 2019-10-15 | 成渝钒钛科技有限公司 | Coke oven flue gas waste heat utilization equipment and method thereof |
| CN110500603A (en) * | 2019-08-22 | 2019-11-26 | 山东郓城正华玻璃科技有限公司 | A kind of glass factory's exhaust gas denitration method |
| CN115090108A (en) * | 2022-06-17 | 2022-09-23 | 天津铁厂有限公司 | Treatment device and process for reducing nitrogen oxides in coke oven flue gas |
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Address after: 100176 Fifth Floor 501, Building 15, No. 2, No. 31 Courtyard, Kechuang Thirteenth Street, Daxing Economic and Technological Development Zone, Beijing Patentee after: HUATAI YONGCHUANG (BEIJING) TECHNOLOGY Co.,Ltd. Address before: 101318 14-C, Hui Hui Garden, B zone, Shunyi District airport industry, Beijing Patentee before: BEIJING HUATAI COKING ENGINEERING CONSULTING Corp. |
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