A high bed temperature circulating fluidized bed boiler with steam parameters of 700°C and above

A circulating fluidized bed and steam parameter technology, applied in steam boilers, fluidized bed combustion equipment, steam generation, etc., can solve the problems of difficult to achieve and balance the efficiency of circulating fluidized bed boiler units, so as to ensure long-term high efficiency operation, improve power generation efficiency, and improve the effect of heat transfer intensity in the furnace

Active Publication Date: 2015-10-28
DONGFANG BOILER GROUP OF DONGFANG ELECTRIC CORP
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

Therefore, in order to consider the heat-carrying capacity of the tubes on the heating surface, and the steam flow rate should not be too low, it is difficult to balance the two; the above all limit the implementation of the steam parameters of 700°C and above in the circulating fluidized bed combustion technology, so that the circulating flow It is difficult to realize the further improvement of the efficiency of the chemical bed boiler unit

Method used

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  • A high bed temperature circulating fluidized bed boiler with steam parameters of 700°C and above
  • A high bed temperature circulating fluidized bed boiler with steam parameters of 700°C and above
  • A high bed temperature circulating fluidized bed boiler with steam parameters of 700°C and above

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Experimental program
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Effect test

Embodiment 1

[0025] Such as figure 1As shown, this embodiment is a high bed temperature circulating fluidized bed boiler with steam parameters of 700°C and above, including an air chamber 14, a single furnace 11, a single air distribution plate 15 and several air caps (not shown). Air distribution device, primary air system with fan 16 and air duct, secondary air system with fan 17 and air duct, horizontal flue 18, two cyclone separators 1, two external heat exchangers 2, The tail flue 3 and the cyclone separator 1 are connected to the horizontal flue 18, the tail flue 3 and the lower part of the furnace 11, and the two ends of the two external heat exchangers 2 are respectively connected to the respective cyclone separator 1 and the lower part of the furnace 11 , the surroundings of the furnace 11 and the furnace roof are composed of water-cooled walls 19 with upper and lower headers, and the shrinkage ratio (that is, L1 / L2 in the figure) of the lower part of the furnace 11 along the dept...

Embodiment 2

[0032] Such as figure 2 , image 3 Shown, this embodiment is compared with embodiment one, and its difference is only: its hearth 26 is single furnace hearth double air distribution plate structure, and the bottom is provided with two air distribution plates 22, and several air caps are respectively provided on two air distribution plates 22 (not shown), the shrinkage ratio of the lower part of the furnace 26 along the depth direction (that is, L3 / L4 in the figure) is 0.22, and three cyclone separators 1 and three external heat exchangers 2 are respectively arranged on both sides of the furnace 26 Among them, three external heat exchangers 2 are provided with medium-temperature superheaters 5, and the other three external heat exchangers 2 are provided with high-temperature reheaters 8, and the inner diameter of the tubes used in the low-temperature reheaters 7 is 46 mm. The internal diameter of the pipe used in the high temperature reheater 8 is 48mm.

[0033] The working ...

Embodiment 3

[0035] Such as Figure 4 Shown, this embodiment is compared with embodiment two, and its difference is only: furnace hearth 27 is annular furnace hearth, and its bottom is provided with annular air distribution plate, and this air distribution plate is provided with several wind caps; Described furnace hearth 27 bottom is along The shrinkage ratio in the depth direction (that is, L5 / L6 in the figure) is 0.48, and the ratio of the pressure drop per unit height of the furnace outlet area to the average unit height pressure drop of the furnace (the ratio of the bed pressure drop to the furnace height) (usually 0.2~ 0.5) and then increased by about 0.05, thereby increasing the heat transfer intensity in the furnace, which can meet the needs of steam parameters on the heating surface. Six cyclone separators 1 and six external heat exchangers 2 are arranged around the furnace 27; the furnace temperature and unit efficiency are still equivalent to those of the first embodiment.

[0...

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Abstract

The invention discloses a circulating fluidized bed boiler with a high bed temperature and with a steam parameter of 700 DEG C and above. The boiler comprises an air compartment, an air distributor, a combustion chamber, a primary air system, a second air system, a horizontal flue, a plurality of cyclone separators, a plurality of external heat exchangers and a rear flue. The contraction ratio of the lower part of the combustion chamber along the depth direction is 0.22-0.48. A flue gas damper is arranged in the rear flue. The rear flue contains at least two parallel flues. A low-temperature superheater is arranged in one parallel flue. A low-temperature reheater is arranged in the other parallel flue. A medium-temperature superheater is arranged in one external heat exchanger. A high-temperature reheater is arranged in one external heat exchanger. A high-temperature superheater is arranged in the combustion chamber. The boiler can effectively raise the heat-transfer intensity inside the combustion chamber, the bed temperature can reach 950 DEG C and above, the steam parameter can reach 700 DEG C and above, and therefore the aims of raising power generating efficiency of coal power units and reducing pollutant discharge are achieved, and long and high-efficient running of the device can be guaranteed.

Description

technical field [0001] The invention relates to a circulating fluidized bed boiler, in particular to a circulating fluidized bed boiler used for ultra-supercritical power generation with steam parameters of 700°C and above. Background technique [0002] my country has become the world's largest energy producer and consumer. The proportion of coal in the energy structure has been around 70% in the past ten years, and it is expected to continue until the middle of this century. However, in my country's coal resources, low-quality coal with high sulfur content and high ash content accounts for a relatively high proportion. Therefore, improving the power generation efficiency of units and reducing pollutant emissions are the central tasks of the power industry. [0003] Improving steam parameters is one of the most effective ways to obtain higher power generation efficiency. In fact, after the 600°C grade ultra-supercritical power generation technology matured, developed cou...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): F23C10/00F22B31/08
Inventor 聂立苏虎周棋巩李明黄敏杨雪芬尹莉梁红伟鲁佳易
Owner DONGFANG BOILER GROUP OF DONGFANG ELECTRIC CORP
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