CN104791749B - Band pipe laying and evaporation coil direct current couple CFB injection boiler with Natural Circulation - Google Patents
Band pipe laying and evaporation coil direct current couple CFB injection boiler with Natural Circulation Download PDFInfo
- Publication number
- CN104791749B CN104791749B CN201510240964.8A CN201510240964A CN104791749B CN 104791749 B CN104791749 B CN 104791749B CN 201510240964 A CN201510240964 A CN 201510240964A CN 104791749 B CN104791749 B CN 104791749B
- Authority
- CN
- China
- Prior art keywords
- steam
- furnace body
- water
- pipe
- buried
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Landscapes
- Air Supply (AREA)
Abstract
带埋管及蒸发盘管直流与自然循环耦合CFB注汽锅炉,属于油田注汽锅炉技术领域。为解决现有自然循环的循环流化床油田注汽锅炉存在水冷壁管内壁容易结盐垢,长期下去会导致传热恶化而爆管的问题。与炉体前后墙固定的多根埋管的下端均与固定于炉体前后墙外侧面的埋管下集箱连通,与炉体前后墙固定的多根埋管的上端均与固定于炉体前后墙外侧面的埋管上集箱连通,两个埋管上集箱出水口与下汇集集箱连通,下汇集集箱与连接管五的一端连通,蒸发盘管环绕炉体的内周侧壁由下至上缠绕构成炉膛水冷壁,蒸发盘管一端与连接管五的另一端连通,蒸发盘管另一端与上汇集集箱连通,上汇集集箱与汽包内的汽水分离器一连通。本发明用于油田注汽。
The utility model relates to a CFB steam injection boiler with buried pipes and evaporation coils coupled with direct current and natural circulation, which belongs to the technical field of oil field steam injection boilers. In order to solve the problem that the existing natural circulation circulating fluidized bed oilfield steam injection boiler has the problem that the inner wall of the water wall tube is prone to salt scale, which will lead to deterioration of heat transfer and tube burst in the long run. The lower ends of the multiple buried pipes fixed to the front and rear walls of the furnace body are connected to the lower headers of the buried pipes fixed on the outer side of the front and rear walls of the furnace body, and the upper ends of the multiple buried pipes fixed to the front and rear walls of the furnace body are connected to the lower headers fixed to the furnace body. The buried pipes on the outer side of the front and rear walls are connected to the upper header, the outlet of the upper header of the two buried pipes is connected to the lower header, the lower header is connected to one end of the connecting pipe five, and the evaporation coil surrounds the inner circumference of the furnace body The wall is wound from bottom to top to form the water-cooled wall of the furnace. One end of the evaporation coil is connected to the other end of the connecting pipe five, the other end of the evaporation coil is connected to the upper collection header, and the upper collection header is connected to the steam-water separator one in the steam drum. The invention is used for steam injection in oil fields.
Description
技术领域 technical field
本发明涉及一种循环流化床注汽锅炉,属于油田注汽锅炉技术领域。 The invention relates to a circulating fluidized bed steam injection boiler, which belongs to the technical field of oil field steam injection boilers.
背景技术 Background technique
现有油田注汽锅炉绝大部分为燃油、燃气直流注汽锅炉,为了节约运行成本,也有单位开发了燃煤层燃直流注汽锅炉,但随着国家环保标准的日益严格,特别是锅炉大气污染物排放标准GB13271-2014的实施,使得层燃注汽锅炉失去了市场的青睐,这是因为层燃注汽锅炉NOx排放浓度远高于现有排放标准,而且炉内不能脱硫,使得环保投资甚至高于锅炉本体的投资。于是人们把目光投向循环流化床锅炉,因为循环流化床锅炉的NOx排放浓度低于现行环保排放标准,而且炉内添加石灰石在Ca/S摩尔比为2左右时,床温在850~880℃时脱硫效率达到80~90%,具有显著的优越性。 Most of the existing steam injection boilers in oilfields are oil-fired and gas-fired direct-flow steam-injection boilers. In order to save operating costs, some units have developed coal-fired seam-fired direct-flow steam injection boilers. The implementation of the pollutant discharge standard GB13271-2014 has made the layer-fired steam-injection boiler lose the favor of the market. This is because the NOx emission concentration of the layer-fired steam-injection boiler is much higher than the existing emission standard, and the furnace cannot desulfurize, which makes environmental protection investment Even higher than the investment of the boiler itself. So people turn their attention to circulating fluidized bed boilers, because the NOx emission concentration of circulating fluidized bed boilers is lower than the current environmental protection emission standards, and when the limestone is added to the furnace with a Ca/S molar ratio of about 2, the bed temperature is 850~880 The desulfurization efficiency reaches 80~90% at ℃, which has obvious advantages.
但是,现有的循环流化床燃煤注汽锅炉为自然循环锅炉,如授权公告号为CN202709071U、授权公告日为2013年01月30日的实用新型专利,公开了一种《循环流化床油田注汽锅炉》,该注汽锅炉在运行过程中出现炉膛水冷壁爆管,因为油田注汽锅炉的给水仅仅是软化水,不是除盐水,给水含盐量高达2300mg/kg。采用自然循环,当排污率定为5%时,锅筒内炉水含盐浓度为48300mg/kg,即通过下降管进入水冷壁管的炉水含盐浓度为48300mg/kg。自然循环超高压(14~18MPa)锅炉的循环倍率为5~8,由于油田注汽锅炉容量小(20~-130t/h),高度低,所以取循环倍率为5时,锅炉水冷壁管出口的含盐浓度高达60375mg/kg,这样水冷壁管内近壁面区域因锅水的蒸发导致含盐浓度更高,当含盐浓度超过盐的溶解度时,盐就会在管壁上析出而结垢,久而久之,盐垢越结越厚,导致传热恶化而爆管。 However, the existing circulating fluidized bed coal-fired steam injection boiler is a natural circulation boiler, such as a utility model patent with the authorized announcement number CN202709071U and the authorized announcement date being January 30, 2013, which discloses a "circulating fluidized bed Oilfield Steam Injection Boiler", the furnace water-wall tube burst occurred during the operation of the steam injection boiler, because the feed water of the oil field steam injection boiler is only softened water, not demineralized water, and the salt content of the feed water is as high as 2300mg/kg. Using natural circulation, when the blowdown rate is set at 5%, the salt concentration of the furnace water in the drum is 48300mg/kg, that is, the salt concentration of the furnace water entering the water wall tube through the downcomer is 48300mg/kg. The circulation ratio of the natural circulation ultra-high pressure (14~18MPa) boiler is 5~8. Since the oil field steam injection boiler has a small capacity (20~-130t/h) and low height, when the circulation ratio is 5, the outlet of the boiler water wall tube The salt concentration is as high as 60375mg/kg. In this way, the near wall area of the water-cooled wall tube has a higher salt concentration due to the evaporation of the pot water. When the salt concentration exceeds the solubility of the salt, the salt will precipitate on the tube wall and scale. Over time, the salt scale becomes thicker and thicker, which leads to deterioration of heat transfer and tube burst.
发明内容 Contents of the invention
本发明的目的是为解决现有自然循环的循环流化床油田注汽锅炉存在水冷壁管内壁容易结盐垢,长期下去会导致传热恶化而爆管的问题,进而提供一种带埋管及蒸发盘管直流与自然循环耦合CFB注汽锅炉。它可以燃烧劣质燃料,热值介于1500~3000Kcal/kg之间。 The purpose of the present invention is to solve the problem that the existing natural circulation circulating fluidized bed oil field steam injection boiler has the problem that the inner wall of the water wall tube is easy to form salt scale, which will lead to the deterioration of heat transfer and the tube burst in the long run, and further provides a buried tube And evaporating coil direct current and natural circulation coupling CFB steam injection boiler. It can burn low-quality fuel with a calorific value between 1500~3000Kcal/kg.
本发明中,循环流化床炉膛底部为带埋管的高速床与低速床组合,上部炉膛水冷壁采用直流蒸发盘管沿炉膛四周内侧壁由下至上缠绕构成,尾部低温区布置蒸发器(即蒸发受热面),采用自然循环。 In the present invention, the bottom of the circulating fluidized bed furnace is a combination of a high-speed bed and a low-speed bed with buried pipes. The water-cooled wall of the upper furnace is composed of a direct-flow evaporation coil coiled from bottom to top along the inner walls around the furnace. Evaporation heating surface), using natural circulation.
实现上述目的,本发明的技术方案是: Realize above-mentioned purpose, technical scheme of the present invention is:
带埋管及蒸发盘管直流与自然循环耦合CFB注汽锅炉,包括炉体、连接管一、给煤口、省煤器出水总管、低速床风室、一次风道、二次风道、二次风管、旋风分离器、下降管、蒸汽连接管、连接管四、过热器、蒸发器、省煤器、二次风空气预热器、一次风空气预热器、回料阀、高速床风室、排污口、汽包、尾部烟道、排渣管、低速床布风板、高速床布风板、两根连接管二及两根连接管三;所述的炉体为循环流化床,所述的汽包内设有汽水分离器一和汽水分离器二,所述的汽包的底部设有排污口,所述的炉体的底部设有高速床风室,炉体的底部位于高速床风室两侧各设有一个低速床风室,所述的高速床风室的上部设有高速床布风板,每个所述的低速床风室的上部均设有一个低速床布风板,所述的排渣管的上端穿过高速床风室安装在高速床布风板上,炉体的侧墙下部位于高速床风室上方布置给煤口,炉体上位于给煤口上方布置二次风管,炉体的炉膛出口与旋风分离器连通,所述的旋风分离器底部通过回料阀与炉体下部连通,旋风分离器的出口与尾部烟道连通,所述的尾部烟道内自上而下依次布置过热器、蒸发器、省煤器、二次风空气预热器和一次风空气预热器,所述的一次风空气预热器通过一次风道与所述的高速床风室连通,所述的二次风空气预热器通过二次风道分别与两个低速床风室以及二次风管连通;所述的蒸发器倾斜设置,且蒸发器的进水口一端低于蒸发器的汽水混合物出口一端;所述的省煤器与省煤器出水总管一端连通,省煤器出水总管另一端与两根连接管二的一端连通,所述的带埋管及蒸发盘管直流与自然循环耦合CFB注汽锅炉还包括下汇集集箱、上汇集集箱、至少一根蒸发盘管、两个埋管下集箱、多根埋管、两个埋管上集箱、至少一根连接管五及多个隔板; Direct flow and natural circulation coupling CFB steam injection boiler with buried pipe and evaporator coil, including furnace body, connecting pipe 1, coal inlet, economizer water outlet main pipe, low-velocity bed air chamber, primary air duct, secondary air duct, and secondary air duct Secondary air pipe, cyclone separator, downcomer, steam connecting pipe, connecting pipe four, superheater, evaporator, economizer, secondary air air preheater, primary air air preheater, return valve, high-speed bed Air chamber, sewage outlet, steam drum, tail flue, slag discharge pipe, low-speed bed air distribution plate, high-speed bed air distribution plate, two connecting pipes 2 and 2 connecting pipes 3; the furnace body is circulating fluidized The steam drum is provided with a steam-water separator 1 and a steam-water separator 2, the bottom of the steam drum is provided with a sewage outlet, the bottom of the furnace body is provided with a high-speed bed air chamber, and the bottom of the furnace body There is a low-speed bed air chamber on both sides of the high-speed bed air chamber, the upper part of the high-speed bed air chamber is provided with a high-speed bed air distribution plate, and each of the low-speed bed air chambers is equipped with a low-speed bed air chamber. The air distribution plate, the upper end of the slag discharge pipe passes through the high-speed bed air chamber and is installed on the high-speed bed air distribution plate. The secondary air pipe is arranged above the mouth, the furnace outlet of the furnace body is connected with the cyclone separator, the bottom of the cyclone separator is connected with the lower part of the furnace body through the return valve, and the outlet of the cyclone separator is connected with the tail flue. The superheater, evaporator, economizer, secondary air air preheater and primary air air preheater are arranged in sequence from top to bottom in the tail flue, and the primary air air preheater communicates with the The high-speed bed air chamber is connected, and the secondary air air preheater is respectively communicated with the two low-speed bed air chambers and the secondary air pipe through the secondary air duct; One end of the water outlet is lower than the end of the steam-water mixture outlet of the evaporator; the economizer is connected to one end of the economizer outlet main pipe, and the other end of the economizer outlet water main pipe is connected to one end of the two connecting pipes. And evaporating coil direct current and natural circulation coupling CFB steam injection boiler also includes lower collecting header, upper collecting header, at least one evaporating coil, two buried pipe lower headers, multiple buried pipes, two buried pipe upper A header, at least one connecting pipe five and a plurality of partitions;
所述的两根连接管二另一端各与一个埋管下集箱连通,两个埋管下集箱分别固定于炉体前、后墙外侧面下方,所述的多根埋管布置在炉体内的低速床内,且多根埋管分别固定于炉体的前墙和后墙上,与炉体前墙固定的多根埋管的下端均与固定于炉体前墙外侧面的埋管下集箱连通,与炉体后墙固定的多根埋管的下端均与固定于炉体后墙外侧面的埋管下集箱连通,与炉体前墙固定的多根埋管的上端均与固定于炉体前墙外侧面的埋管上集箱连通,与炉体后墙固定的多根埋管的上端均与固定于炉体后墙外侧面的埋管上集箱连通,每个埋管下集箱以及每个埋管上集箱内分别间隔固定有竖直设置的多个隔板,且位于同侧的埋管上集箱和埋管下集箱内的多个隔板分别错位设置,两个埋管上集箱出水口各与一根连接管三的一端连通,两根连接管三的另一端均与下汇集集箱连通,下汇集集箱与至少一根连接管五的一端连通,所述的连接管五的另一端与蒸发盘管的一端连通,连接管五与蒸发盘管的数量相同,至少一根蒸发盘管环绕炉体的内周侧壁由下至上缠绕构成炉膛水冷壁,所有蒸发盘管的另一端与上汇集集箱连通,上汇集集箱通过连接管一与汽包内的汽水分离器一连通;进入汽包内的汽水混合物经汽水分离器一进行汽水分离,分离出的水进入汽包的水空间,经汽水分离器一分离出的蒸汽进入汽包的汽空间,汽包的水空间通过下降管与蒸发器的进水口连通,蒸发器的汽水混合物出口通过连接管四与所述的汽水分离器二连通;经汽水分离器二分离出的蒸汽进入汽包的汽空间,汽包的汽空间通过蒸汽连接管与过热器连通。 The other ends of the two connecting pipes are respectively connected with a lower header of buried pipes, and the lower headers of the two buried pipes are respectively fixed under the outer side of the front and rear walls of the furnace body, and the multiple buried pipes are arranged in the furnace In the low-velocity bed in the body, and multiple buried pipes are respectively fixed on the front wall and rear wall of the furnace body, and the lower ends of the multiple buried pipes fixed to the front wall of the furnace body are all connected to the buried pipes fixed on the outer side of the front wall of the furnace body The lower header is connected, and the lower ends of the multiple buried pipes fixed on the rear wall of the furnace body are connected with the lower header of the buried pipes fixed on the outer side of the rear wall of the furnace body, and the upper ends of the multiple buried pipes fixed on the front wall of the furnace body are all connected. It communicates with the upper header of the buried pipe fixed on the outer side of the front wall of the furnace body, and the upper ends of the multiple buried pipes fixed on the rear wall of the furnace body are all connected with the upper header of the buried pipe fixed on the outer side of the rear wall of the furnace body. The lower header of the buried pipe and the upper header of each buried pipe are respectively fixed with a plurality of partitions vertically arranged at intervals, and the plurality of partitions in the upper header of the buried pipe and the lower header of the buried pipe on the same side are respectively Dislocation setting, the water outlet of the upper header of the two buried pipes is connected to one end of a connecting pipe 3, the other ends of the two connecting pipes 3 are connected to the lower collecting header, and the lower collecting header is connected to at least one connecting pipe 5 The other end of the connecting pipe five is connected with one end of the evaporating coil, the number of connecting pipe five is the same as that of the evaporating coil, and at least one evaporating coil is wound around the inner peripheral side wall of the furnace body from bottom to top It constitutes the water wall of the furnace, and the other ends of all the evaporating coils are connected with the upper collection box, and the upper collection box is connected with the steam-water separator in the steam drum through the connecting pipe one; the steam-water mixture entering the steam drum passes through the steam-water separator one The steam-water separation is carried out, the separated water enters the water space of the steam drum, and the steam separated by the steam-water separator enters the steam space of the steam drum, and the water space of the steam drum communicates with the water inlet of the evaporator through the downcomer, and the The steam-water mixture outlet communicates with the steam-water separator 2 through the connecting pipe 4; the steam separated by the steam-water separator 2 enters the steam space of the steam drum, and the steam space of the steam drum communicates with the superheater through the steam connecting pipe.
本发明相对于现有技术的有益效果是: The beneficial effect of the present invention relative to prior art is:
1、由于炉内埋管及蒸发盘管采用直流,埋管及蒸发盘管再也不会爆管。这是因为给水含盐浓度为2300mg/kg时,当炉膛水冷壁出口质量含气率为90%时,炉水中的含盐浓度为23000mg/kg,而实际运行的直流注汽锅炉给水含盐浓度最高为7000mg/kg,炉膛水冷壁内位于炉膛出口处的质量含气率为80%时运行正常,从没有爆管,这时炉水含盐浓度为35000mg/kg (7000/0.2 mg/kg =35000 mg/kg),由此可以证明,炉内埋管及炉膛水冷壁采用直流是安全可靠的。 1. Since the buried pipes and evaporating coils in the furnace adopt direct current, the buried pipes and evaporating coils will never burst again. This is because when the salt concentration of the feed water is 2300mg/kg, when the gas content rate of the outlet mass of the furnace water wall is 90%, the salt concentration in the furnace water is 23000mg/kg, while the actual operating once-through steam injection boiler feed water salt concentration The highest is 7000mg/kg. When the mass gas content in the furnace water wall at the furnace outlet is 80%, the operation is normal, and there has never been a tube explosion. At this time, the salt concentration of the furnace water is 35000mg/kg (7000/0.2 mg/kg = 35000 mg/kg), it can be proved that it is safe and reliable to use direct current for the buried pipe in the furnace and the water wall of the furnace.
2、位于尾部的蒸发器布置在低于550℃的温区内,蒸发器的管材采用12Cr1MoVG,由于该材料允许壁温为580℃,所以,蒸发器管内部即使部分被盐垢堵死,也不会发生爆管,这样就彻底解决受热面爆管问题,保证锅炉安全稳定运行。 2. The evaporator located at the tail is arranged in a temperature zone lower than 550°C. The pipe material of the evaporator is 12Cr1MoVG. Since the wall temperature of this material is allowed to be 580°C, even if the inside of the evaporator pipe is partially blocked by salt scale, it will not There will be no tube explosion, which completely solves the problem of tube explosion on the heating surface and ensures the safe and stable operation of the boiler.
3、蒸发盘管向火侧表面覆盖一层60~80mm的耐火耐磨材料,蒸发盘管因磨损而发生爆管问题就彻底消除。 3. The surface of the evaporating coil facing the fire side is covered with a layer of 60~80mm refractory and wear-resistant material, and the problem of pipe burst due to wear and tear of the evaporating coil can be completely eliminated.
附图说明 Description of drawings
图1是本发明的整体结构主视图; Fig. 1 is the overall structure front view of the present invention;
图2是埋管进出水示意图; Figure 2 is a schematic diagram of water inflow and outflow of buried pipes;
图3是图2的K向视图; Fig. 3 is the K direction view of Fig. 2;
图4是给水循环路径示意图; Fig. 4 is a schematic diagram of the water supply circulation path;
图5是图1的A局部放大图。 FIG. 5 is a partially enlarged view of A in FIG. 1 .
图中,炉体1、连接管一2、蒸发盘管3、连接管二4、给煤口5、连接管三6、省煤器出水总管7、埋管下集箱8、埋管9、埋管上集箱10、低速床风室11、一次风道12、二次风道13、二次风管14、旋风分离器15、下降管16、蒸汽连接管17、连接管四18、过热器19、蒸发器20、省煤器21、二次风空气预热器22、一次风空气预热器23、回料阀24、高速床风室25、下汇集集箱26、排污口27、汽水分离器一28a、汽水分离器二28b、汽包29、尾部烟道30、排渣管31、连接管五32、竖直隔板33、耐火耐磨材料34、上汇集集箱35、低速床布风板36和高速床布风板37。 In the figure, furnace body 1, connecting pipe 1 2, evaporation coil 3, connecting pipe 2 4, coal inlet 5, connecting pipe 3 6, economizer water outlet main pipe 7, buried pipe lower header 8, buried pipe 9, Buried pipe upper header 10, low-velocity bed air chamber 11, primary air duct 12, secondary air duct 13, secondary air duct 14, cyclone separator 15, descending pipe 16, steam connecting pipe 17, connecting pipe 4 18, overheating device 19, evaporator 20, economizer 21, secondary air air preheater 22, primary air air preheater 23, return valve 24, high-speed bed air chamber 25, lower collection box 26, sewage outlet 27, Steam-water separator 1 28a, steam-water separator 2 28b, steam drum 29, tail flue 30, slag discharge pipe 31, connecting pipe 5 32, vertical partition 33, refractory and wear-resistant material 34, upper collection box 35, low speed Bed cloth wind plate 36 and high-speed bed cloth wind plate 37.
具体实施方式 detailed description
具体实施方式一:如图1~图5所示,带埋管及蒸发盘管直流与自然循环耦合CFB注汽锅炉,包括炉体1、连接管一2、给煤口5、省煤器出水总管7、低速床风室11、一次风道12、二次风道13、二次风管14、旋风分离器15、下降管16、蒸汽连接管17、连接管四18、过热器19、蒸发器20、省煤器21、二次风空气预热器22、一次风空气预热器23、回料阀24、高速床风室25、排污口27、汽包29、尾部烟道30、排渣管31、低速床布风板36、高速床布风板37、两根连接管二4及两根连接管三6;所述的炉体1为循环流化床,所述的汽包29内设有汽水分离器一28a和汽水分离器二28b,所述的汽包29的底部设有排污口27,所述的炉体1的底部设有高速床风室25,炉体1的底部位于高速床风室25两侧各设有一个低速床风室11(即炉体1的底部设有高速床和低速床组合),所述的高速床风室25的上部设有高速床布风板37,每个所述的低速床风室11的上部均设有一个低速床布风板36,所述的排渣管31的上端穿过高速床风室25安装在高速床布风板37上(这一结构及运行参数已在公开号为CN 102901212B、公开日为2015年03月11日的发明专利《一种燃劣质燃料低倍率循环流化床热水锅炉及其燃烧方法》中公开),炉体1的侧墙下部位于高速床风室25上方布置给煤口5,炉体1上位于给煤口5上方布置二次风管14,炉体1的炉膛出口与旋风分离器15连通,所述的旋风分离器15底部通过回料阀24与炉体1下部连通,旋风分离器15的出口与尾部烟道30连通,所述的尾部烟道30内自上而下依次布置过热器19、蒸发器20、省煤器21、二次风空气预热器22和一次风空气预热器23,所述的一次风空气预热器23通过一次风道12与所述的高速床风室25连通,所述的二次风空气预热器22通过二次风道13分别与两个低速床风室11以及二次风管14连通;所述的蒸发器20倾斜设置,且蒸发器20的进水口一端低于蒸发器20的汽水混合物出口一端;所述的省煤器21与省煤器出水总管7一端连通,省煤器出水总管7另一端与两根连接管二4的一端连通,所述的带埋管及蒸发盘管直流与自然循环耦合CFB注汽锅炉还包括下汇集集箱26、上汇集集箱35、至少一根蒸发盘管3、两个埋管下集箱8、多根埋管9、两个埋管上集箱10、至少一根连接管五32及多个隔板33; Specific implementation mode 1: As shown in Figures 1 to 5, a CFB steam injection boiler with buried pipes and evaporation coils coupled with direct current and natural circulation includes a furnace body 1, a connecting pipe 1, a coal inlet 5, and an economizer water outlet Main pipe 7, low-speed bed air chamber 11, primary air duct 12, secondary air duct 13, secondary air duct 14, cyclone separator 15, downcomer 16, steam connecting pipe 17, connecting pipe 4 18, superheater 19, evaporation 20, economizer 21, secondary air air preheater 22, primary air air preheater 23, return valve 24, high-speed bed air chamber 25, sewage outlet 27, steam drum 29, tail flue 30, exhaust Slag pipe 31, low-speed bed air distribution plate 36, high-speed bed air distribution plate 37, two connecting pipes two 4 and two connecting pipes three 6; the furnace body 1 is a circulating fluidized bed, and the steam drum 29 Steam-water separator one 28a and steam-water separator two 28b are arranged inside, the bottom of the steam drum 29 is provided with a sewage outlet 27, the bottom of the furnace body 1 is provided with a high-speed bed air chamber 25, and the bottom of the furnace body 1 A low-speed bed air chamber 11 is provided on both sides of the high-speed bed air chamber 25 (that is, the bottom of the furnace body 1 is provided with a high-speed bed and a low-speed bed combination), and the upper part of the high-speed bed air chamber 25 is provided with a high-speed bed air distribution chamber. plate 37, each of the low-speed bed air chambers 11 is provided with a low-speed bed air distribution plate 36, and the upper end of the slag discharge pipe 31 passes through the high-speed bed air chamber 25 and is installed on the high-speed bed air distribution plate 37 (This structure and operating parameters have been disclosed in the invention patent "A Low-rate Circulating Fluidized Bed Hot Water Boiler Burning Inferior Fuel and Its Combustion Method" with the publication number CN 102901212B and the publication date of March 11, 2015 ), the lower part of the side wall of the furnace body 1 is located above the high-speed bed air chamber 25 and the coal inlet 5 is arranged, and the secondary air pipe 14 is arranged on the furnace body 1 above the coal inlet 5, and the furnace outlet of the furnace body 1 and the cyclone separator 15 The bottom of the cyclone separator 15 communicates with the lower part of the furnace body 1 through the return valve 24, and the outlet of the cyclone separator 15 communicates with the tail flue 30, and the tail flue 30 is arranged in sequence from top to bottom. 19, evaporator 20, economizer 21, secondary air air preheater 22 and primary air air preheater 23, the primary air air preheater 23 passes through the primary air duct 12 and the high-speed bed The air chamber 25 communicates, and the secondary air air preheater 22 communicates with the two low-speed bed air chambers 11 and the secondary air pipe 14 respectively through the secondary air channel 13; the evaporator 20 is arranged obliquely, and evaporates One end of the water inlet of the evaporator 20 is lower than the steam-water mixture outlet end of the evaporator 20; the economizer 21 communicates with one end of the economizer water outlet pipe 7, and the other end of the economizer water outlet pipe 7 is connected to two connecting pipes 24 One end is connected, and the CFB steam injection boiler with buried pipe and evaporating coil coupled with direct current and natural circulation also includes a lower collecting header 26, an upper collecting header 35, at least one evaporating coil 3, and two buried pipes lower collecting Box 8, multiple buried pipes 9, two buried pipe upper headers 10, at least one connecting pipe 5 32 and multiple partitions 33;
所述的两根连接管二4另一端各与一个埋管下集箱8连通,两个埋管下集箱8分别固定于炉体1前、后墙外侧面下方,所述的多根埋管9布置在炉体1内的低速床内,且多根埋管9分别固定于炉体1的前墙和后墙上,与炉体1前墙固定的多根埋管9的下端均与固定于炉体1前墙外侧面的埋管下集箱8连通,与炉体1后墙固定的多根埋管9的下端均与固定于炉体1后墙外侧面的埋管下集箱8连通,与炉体1前墙固定的多根埋管9的上端均与固定于炉体1前墙外侧面的埋管上集箱10连通,与炉体1后墙固定的多根埋管9的上端均与固定于炉体1后墙外侧面的埋管上集箱10连通,每个埋管下集箱8以及每个埋管上集箱10内分别间隔固定有竖直设置的多个隔板33,且位于同侧的埋管上集箱10和埋管下集箱8内的多个隔板33分别错位设置(作用是保证埋管9内水的质量流速大于1000kg/m2.s),两个埋管上集箱10出水口各与一根连接管三6的一端连通,两根连接管三6的另一端均与下汇集集箱26连通,下汇集集箱26与至少一根连接管五32的一端连通,所述的连接管五32的另一端与蒸发盘管3的一端连通,连接管五32与蒸发盘管3的数量相同,至少一根蒸发盘管3环绕炉体1的内周侧壁由下至上缠绕构成炉膛水冷壁,所有蒸发盘管3的另一端与上汇集集箱35连通,上汇集集箱35通过连接管一2与汽包29内的汽水分离器一28a连通;进入汽包29内的汽水混合物经汽水分离器一28a进行汽水分离,分离出的水进入汽包29的水空间,经汽水分离器一28a分离出的蒸汽进入汽包29的汽空间,汽包29的水空间通过下降管16与蒸发器20的进水口连通,蒸发器20的汽水混合物出口通过连接管四18与所述的汽水分离器二28b连通;经汽水分离器二28b分离出的蒸汽进入汽包29的汽空间,汽包29的汽空间通过蒸汽连接管17与过热器19连通。 The other ends of the two connecting pipes 2 and 4 are respectively connected with a lower header 8 of buried pipes. Tube 9 is arranged in the low-velocity bed in body of furnace 1, and many buried pipes 9 are respectively fixed on the front wall and back wall of body of furnace 1, and the lower ends of many buried pipes 9 fixed with the front wall of body of furnace 1 are all connected with The buried tube lower header 8 fixed on the outer side of the front wall of the furnace body 1 communicates with the lower end of the multiple buried tubes 9 fixed on the rear wall of the furnace body 1 and the buried tube lower header fixed on the outer side of the rear wall of the furnace body 1 8 connected, the upper ends of the multiple buried pipes 9 fixed on the front wall of the furnace body 1 are connected with the buried pipe upper header 10 fixed on the outer side of the front wall of the furnace body 1, and the multiple buried pipes fixed on the rear wall of the furnace body 1 The upper ends of 9 are all communicated with the buried pipe upper header 10 fixed on the outer side of the rear wall of the furnace body 1, and each buried pipe lower header 8 and each buried pipe upper header 10 are respectively fixed with vertically arranged multiple headers at intervals. A partition 33, and multiple partitions 33 in the upper header 10 of the buried pipe and the lower header 8 of the buried pipe on the same side are respectively misplaced (the function is to ensure that the mass flow rate of the water in the buried pipe 9 is greater than 1000kg/m 2 .s), the water outlets of the upper header 10 of the two buried pipes are connected with one end of a connecting pipe 36, and the other ends of the two connecting pipes 36 are connected with the lower collecting header 26, and the lower collecting header 26 is connected with the One end of at least one connecting pipe five 32 is connected, and the other end of the connecting pipe five 32 is connected with one end of the evaporation coil 3, the number of connecting pipe five 32 is the same as that of the evaporation coil 3, and at least one evaporation coil 3 The inner peripheral side wall surrounding the furnace body 1 is wound from bottom to top to form a furnace water wall. The other ends of all the evaporation coils 3 communicate with the upper collection box 35, and the upper collection box 35 is connected to the steam drum 29 through the connecting pipe 1. The steam-water separator-28a is connected; the steam-water mixture entering the steam drum 29 is separated from the steam-water through the steam-water separator-28a, and the separated water enters the water space of the steam drum 29, and the steam separated by the steam-water separator-28a enters the steam drum The steam space of 29, the water space of steam drum 29 is communicated with the water inlet of evaporator 20 by downcomer 16, and the steam-water mixture outlet of evaporator 20 is communicated with described steam-water separator 2 28b through connecting pipe 4 18; The steam separated by device two 28b enters the steam space of the steam drum 29, and the steam space of the steam drum 29 communicates with the superheater 19 through the steam connecting pipe 17.
具体实施方式二:如图1所示,具体实施方式一所述的带埋管及蒸发盘管直流与自然循环耦合CFB注汽锅炉,所述的蒸发器20与水平面之间的夹角为α,α=5~10°。 Specific embodiment two: as shown in Figure 1, the direct current and natural circulation coupling CFB steam injection boiler with buried pipe and evaporation coil described in specific embodiment one, the angle between the evaporator 20 and the horizontal plane is α , α=5~10°.
具体实施方式三:如图1所示,具体实施方式一所述的带埋管及蒸发盘管直流与自然循环耦合CFB注汽锅炉,所述的蒸发盘管3的数量为1根,蒸发盘管3的外管径(直径)为Φ51mm~Φ108mm。 Specific embodiment three: as shown in Figure 1, the direct current and natural circulation coupling CFB steam injection boiler with buried pipe and evaporating coil described in specific embodiment 1, the number of the evaporating coil 3 is 1, and the evaporating coil The outer pipe diameter (diameter) of the tube 3 is Φ51 mm to Φ108 mm.
具体实施方式四:如图1所示,具体实施方式一所述的带埋管及蒸发盘管直流与自然循环耦合CFB注汽锅炉,所述的蒸发盘管3的数量为2~6根,2~6根蒸发盘管3环绕炉体1的内周侧壁由下至上同步缠绕构成炉膛水冷壁,每根蒸发盘管3的外管径(直径)为Φ51mm~Φ108mm,以满足注汽锅炉容量在7~130t/h之间的需要。 Embodiment 4: As shown in Figure 1, the CFB steam injection boiler with buried pipes and evaporator coils coupled with direct current and natural circulation described in Embodiment 1, the number of the evaporator coils 3 is 2 to 6, 2~6 evaporating coils 3 surround the inner peripheral side wall of the furnace body 1 and are synchronously wound from bottom to top to form a furnace water wall. The capacity needs to be between 7 and 130t/h.
具体实施方式五:如图1所示,具体实施方式一、二、三或四所述的带埋管及蒸发盘管直流与自然循环耦合CFB注汽锅炉,所述的蒸发盘管3朝向炉体1向火侧的外表面覆盖一层60~80mm厚的耐火耐磨材料34,目的是防止蒸发盘管3磨损。 Specific embodiment five: as shown in Figure 1, the direct current and natural circulation coupled CFB steam injection boiler with buried pipe and evaporating coil described in specific embodiment 1, 2, 3 or 4, the evaporating coil 3 faces the furnace The outer surface of the body 1 on the fire side is covered with a layer of 60-80 mm thick refractory and wear-resistant material 34, in order to prevent the evaporation coil 3 from being worn.
工作过程是:如图1~图5所示,一次风经一次风空气预热器23预热后通过一次风道12送入炉体1的高速床风室25内,再进入炉体1的炉膛参与燃烧;二次风经二次风空气预热器22预热后通过二次风道13分别送入炉体1的低速床风室11和二次风管14内,实现分级燃烧。 The working process is: as shown in Figures 1 to 5, the primary air is preheated by the primary air preheater 23 and sent into the high-speed bed air chamber 25 of the furnace body 1 through the primary air duct 12, and then enters the furnace body 1. The furnace participates in the combustion; the secondary air is preheated by the secondary air air preheater 22 and sent to the low-velocity bed air chamber 11 and the secondary air pipe 14 of the furnace body 1 respectively through the secondary air channel 13 to realize staged combustion.
工质侧:给水经省煤器21加热后通过省煤器出水总管7,分别进入两根连接管二4内,并经两个埋管下集箱8进入多根埋管9内,再经多根埋管9进入两个埋管上集箱10内,之后经两根连接管三6进入至下汇集集箱26内,再由连接管五32引入蒸发盘管3内,由于蒸发盘管3与上汇集集箱35均连通,则再经上汇集集箱35及连接管一2进入汽包29内,并经汽水分离器一28a汽水分离(汽水分离器一28a是旋风分离器,分离效率达到99.9%),分离出的蒸汽进入汽包29的汽空间,分离出的水进入汽包29的水空间,分离出的水通过下降管16进入蒸发器20内,蒸发器20产生的汽水混合物通过连接管三18引入汽包29内的汽水分离器二28b实现汽水分离,分离出的蒸汽进入汽包29的汽空间。所述的炉膛水冷壁及蒸发器20产生的蒸汽汇合后通过蒸汽连接管17进入过热器19加热至设定温度,向井下注汽。 Working fluid side: After the feed water is heated by the economizer 21, it passes through the economizer outlet water main pipe 7, enters the two connecting pipes 24 respectively, and enters the multiple buried pipes 9 through the lower header 8 of the two buried pipes, and then passes through the A plurality of buried pipes 9 enter the upper header 10 of the two buried pipes, and then enter the lower collecting header 26 through two connecting pipes 3 6, and then lead into the evaporation coil 3 through the connecting pipe 5 32, because the evaporation coil 3 is all communicated with the upper collection header box 35, then enters the steam drum 29 through the upper collection header box 35 and the connecting pipe-2, and separates the steam and water through the steam-water separator-28a (the steam-water separator-28a is a cyclone separator, which separates The efficiency reaches 99.9%), the separated steam enters the steam space of the steam drum 29, the separated water enters the water space of the steam drum 29, the separated water enters the evaporator 20 through the downcomer 16, and the steam water produced by the evaporator 20 The mixture is introduced into the steam-water separator 2 28b in the steam drum 29 through the connecting pipe 3 18 to realize steam-water separation, and the separated steam enters the steam space of the steam drum 29 . The steam generated by the water-cooled wall of the furnace and the evaporator 20 is combined and enters the superheater 19 through the steam connection pipe 17 to be heated to a set temperature, and then injects steam downhole.
所述的CFB即表示为循环流化床。 The CFB is referred to as a circulating fluidized bed.
Claims (5)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201510240964.8A CN104791749B (en) | 2015-05-13 | 2015-05-13 | Band pipe laying and evaporation coil direct current couple CFB injection boiler with Natural Circulation |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201510240964.8A CN104791749B (en) | 2015-05-13 | 2015-05-13 | Band pipe laying and evaporation coil direct current couple CFB injection boiler with Natural Circulation |
Publications (2)
Publication Number | Publication Date |
---|---|
CN104791749A CN104791749A (en) | 2015-07-22 |
CN104791749B true CN104791749B (en) | 2016-08-24 |
Family
ID=53556778
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201510240964.8A Expired - Fee Related CN104791749B (en) | 2015-05-13 | 2015-05-13 | Band pipe laying and evaporation coil direct current couple CFB injection boiler with Natural Circulation |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN104791749B (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN114321942B (en) * | 2021-12-29 | 2025-03-07 | 上海市政工程设计研究总院(集团)有限公司 | Incinerator |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0722556A1 (en) * | 1993-10-08 | 1996-07-24 | Foster Wheeler Energia Oy | Supercritical steam pressurized circulating fluidized bed boiler |
CN1563793A (en) * | 2004-03-30 | 2005-01-12 | 沈阳戴维国际机电设备有限公司 | Oil field steam filling boiler of circulation fluidized bed using water coal slurry as fuel |
CN101033683A (en) * | 2006-03-09 | 2007-09-12 | 秦文韬 | Stem-injection technique for oil recovery by heat |
CN201053671Y (en) * | 2007-04-20 | 2008-04-30 | 赵文利 | Thick oil thermal recovery injection circulated fluid bed boiler system |
CN202709071U (en) * | 2012-07-31 | 2013-01-30 | 太原锅炉集团有限公司 | Oil field gas injection boiler for circulating fluidized bed |
CN102901212A (en) * | 2012-10-22 | 2013-01-30 | 哈尔滨工业大学 | Low-range circulating fluidized bed water boiler for combusting inferior fuel and combustion method thereof |
-
2015
- 2015-05-13 CN CN201510240964.8A patent/CN104791749B/en not_active Expired - Fee Related
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0722556A1 (en) * | 1993-10-08 | 1996-07-24 | Foster Wheeler Energia Oy | Supercritical steam pressurized circulating fluidized bed boiler |
CN1563793A (en) * | 2004-03-30 | 2005-01-12 | 沈阳戴维国际机电设备有限公司 | Oil field steam filling boiler of circulation fluidized bed using water coal slurry as fuel |
CN101033683A (en) * | 2006-03-09 | 2007-09-12 | 秦文韬 | Stem-injection technique for oil recovery by heat |
CN201053671Y (en) * | 2007-04-20 | 2008-04-30 | 赵文利 | Thick oil thermal recovery injection circulated fluid bed boiler system |
CN202709071U (en) * | 2012-07-31 | 2013-01-30 | 太原锅炉集团有限公司 | Oil field gas injection boiler for circulating fluidized bed |
CN102901212A (en) * | 2012-10-22 | 2013-01-30 | 哈尔滨工业大学 | Low-range circulating fluidized bed water boiler for combusting inferior fuel and combustion method thereof |
Also Published As
Publication number | Publication date |
---|---|
CN104791749A (en) | 2015-07-22 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN102889570B (en) | Tower-type boiler with primary reheater and secondary reheater | |
CN104791748B (en) | Double; two once-through cycle fluid bed injection boilers with pipe laying and evaporation coil | |
CN103591575B (en) | 350MW supercritical circulating fluidized bed boiler and steam/water circulating method | |
CN103363517B (en) | A kind of high bed temperature CFBB of 700 DEG C and above steam parameter | |
TW201533392A (en) | Superheated steam boiler of horizontal circulating fluidizing bed | |
CN102297423A (en) | Membrane type water-cooled wall four-flue biomass circulating fluidized bed boiler | |
CN103017153A (en) | 300MW subcritical circulating fluidized bed boiler and working method | |
CN102635844A (en) | Boiler system using waste heat of flue gas of rotary hearth furnace | |
CN110220182A (en) | A kind of biomass direct-fired energy-saving circulating fluidized bed superhigh-pressure high-temp reheated steam boiler | |
CN105318307B (en) | A kind of double-barrel transverse formula expansion chamber sprays denitration corner tube boiler | |
CN104791751B (en) | Direct current vertical evaporation tube afterbody Natural Circulation manifold type CFB injection boiler in stove | |
CN203656913U (en) | 350MW supercritical circulating fluidized bed boiler | |
CN201412821Y (en) | A superheated steam injection boiler without desalination of feed water | |
CN109945158A (en) | A Hedging Tower Type 660MW Secondary Reheat Boiler | |
CN104791749B (en) | Band pipe laying and evaporation coil direct current couple CFB injection boiler with Natural Circulation | |
CN104791752B (en) | The double once-through cycle fluid bed injection boiler of vertical evaporation tube in a kind of stove | |
CN208579525U (en) | Efficient biomass boiler | |
CN102679309B (en) | 350MW MW supercritical W flame anthracite boiler | |
CN202013015U (en) | Vertical half gas positive burning heating boiler | |
CN105485894A (en) | Pulverized coal type water heating boiler | |
CN109990257A (en) | Heat recovery coke oven high temperature and high pressure reheat waste heat boiler | |
CN205897085U (en) | Bubbling fluidized bed boiler of burming biomass granule | |
CN202993180U (en) | 300MW subcritical circulating fluidized bed boiler | |
CN105444144B (en) | For using the 300MWCFB boilers and layout method of oil shale | |
CN203431838U (en) | High-bed-temperature circulating fluidized bed boiler with 700 DEG C and above steam parameter |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
EXSB | Decision made by sipo to initiate substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
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: 20160824 |
|
CF01 | Termination of patent right due to non-payment of annual fee |