TWI580790B - Blast furnace blast system - Google Patents

Blast furnace blast system Download PDF

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TWI580790B
TWI580790B TW102115105A TW102115105A TWI580790B TW I580790 B TWI580790 B TW I580790B TW 102115105 A TW102115105 A TW 102115105A TW 102115105 A TW102115105 A TW 102115105A TW I580790 B TWI580790 B TW I580790B
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blast
blast furnace
air blowing
nozzle
air
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TW102115105A
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Chinese (zh)
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TW201441377A (en
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xian-wen Du
jian-xiong Cai
Cheng-Peng Ye
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China Steel Corp
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高爐的鼓風系統 Blast furnace blast system

本發明是有關於一種煉鐵系統,特別是指一種高爐的鼓風系統。 The present invention relates to an ironmaking system, and more particularly to a blast furnace blasting system.

近年來,隨著環保意識抬頭,各行各業無不積極節能減碳。而對於煉鐵工業而言,將純化後的高爐爐頂氣(blast furnace top gas,BFG)與焦炭(coke)或粉煤(pulverized coal)經噴鎗與鼓風管吹入高爐的風徑區(raceway)中燃燒,被視為能有降低高爐煉鐵製程之二氧化碳排放量的重要方法。 In recent years, with the rise of environmental awareness, all walks of life have been actively saving energy and reducing carbon. For the ironmaking industry, the purified blast furnace top gas (BFG) and coke or pulverized coal are blown into the wind tunnel of the blast furnace via a spray gun and a blast tube. Combustion in (raceway) is considered to be an important method to reduce CO2 emissions from the blast furnace ironmaking process.

其主要是利用純化後的高爐爐頂氣中所含的氫氣與一氧化碳濃度較高,不僅能在風徑區中燃燒產生煉鐵所需的熱與還原氣體,也能取代部分高價焦炭的消耗,藉此降低二氧化碳的排放量。 The main purpose is to utilize the higher concentration of hydrogen and carbon monoxide contained in the top gas of the purified blast furnace, not only to generate heat and reducing gas required for iron making in the wind tunnel region, but also to replace the consumption of some high-priced coke. Thereby reducing the amount of carbon dioxide emissions.

但是,由於高爐爐頂氣中所含之氫氣與一氧化碳易燃的特性,因此,只要將高爐爐頂氣經噴鎗噴吹到鼓風管中,就會立即與鼓風管中熱鼓風(hot blast)的氧氣反應燃燒,連帶造成焦炭或粉煤提前於鼓風管中裂解燃燒,導致鼓風管的壓損增加,而影響了風徑區的大小,眾所周知 ,若風徑區過大會產生過吹現象,反之風徑區過小則會產生中心堆積現象,而且不論是過吹或是中心堆積現象都不利煉鐵製程的穩定性。 However, due to the flammability of hydrogen and carbon monoxide contained in the top gas of the blast furnace, as long as the blast furnace top gas is sprayed into the blast pipe through the spray gun, it will immediately blast with the hot air in the blast pipe ( Hot blast) Oxygen reaction combustion, which causes coke or pulverized coal to crack and burn ahead of the blast tube, resulting in increased pressure loss of the blast tube, which affects the size of the wind tunnel. If the wind tunnel area is too large, the blowing phenomenon will occur. On the contrary, if the wind path area is too small, the center accumulation phenomenon will occur, and the stability of the iron making process will be unfavorable whether it is over-blowing or central accumulation.

因此,如何控制鼓風管的壓損與風徑區的大小,以提升煉鐵製程的穩定性,成為相關業者所欲改善的問題。 Therefore, how to control the pressure loss of the blast tube and the size of the wind tunnel area to improve the stability of the iron making process has become a problem that the relevant industry desires to improve.

因此,本發明之目的,即在提供一種能穩定壓損,且能提高煉鐵製程之穩定性之高爐的鼓風系統。 Accordingly, it is an object of the present invention to provide an blast system for a blast furnace which can stabilize pressure loss and improve the stability of the iron making process.

於是本發明高爐的鼓風系統,包含至少一鼓風單元。該鼓風單元具有一鼓風管、一連通該鼓風管且伸入該高爐的鼓風嘴,及一伸入該鼓風管的噴鎗機構,該鼓風嘴滿足下式: Thus, the blast system of the blast furnace of the present invention comprises at least one blast unit. The air blowing unit has a blast pipe, a blaster that communicates with the blast pipe and extends into the blast furnace, and a lance mechanism that extends into the blast pipe, and the blasting nozzle satisfies the following formula:

其中,△P t 是該鼓風嘴出風口的壓損、f是磨擦因子、L t 是該鼓風嘴伸入該高爐的長度、D t 是該鼓風嘴的口徑,L R 是風徑區深度。 Where Δ P t is the pressure loss of the air outlet of the air blowing nozzle, f is the friction factor, L t is the length of the air blowing nozzle into the blast furnace, D t is the diameter of the air blowing nozzle, and L R is the air diameter Area depth.

本發明的有益效果在於:在無法避免高爐爐頂氣提早燃燒的情況下,利用滿足方程式:的鼓風嘴,配合調整該鼓風嘴伸入該高爐的長度與該鼓風嘴的口徑,以在不影響風徑區深度的情形下維持壓損,且能提高煉鐵製程之穩定性。 The beneficial effects of the invention are: in the case that the blast furnace top gas early combustion cannot be avoided, the utilization equation is satisfied: The blaster mouth adjusts the length of the blaster into the blast furnace and the diameter of the blaster to maintain the pressure loss without affecting the depth of the wind tunnel, and can improve the stability of the iron making process.

2‧‧‧鼓風單元 2‧‧‧Blowing unit

200‧‧‧高爐 200‧‧‧ blast furnace

21‧‧‧鼓風管 21‧‧‧Blowing tube

22‧‧‧鼓風嘴 22‧‧‧ blaster

23‧‧‧噴鎗機構 23‧‧‧ spray gun mechanism

本發明之其他的特徵及功效,將於參照圖式的實施方式中清楚地呈現,其中:圖1是一示意圖,說明本發明高爐的鼓風系統的一較佳實施例;圖2、3是比較圖,說明該較佳實施例之穿透因子與風徑區因子的關係;圖4是一示意圖,說明進行模擬實驗之鼓風嘴與風徑區的尺寸條件;及圖5是一比較圖,說明鼓風嘴出風口的壓損與該鼓風嘴伸入該高爐的長度,及該鼓風嘴的口徑間的關係。 Other features and advantages of the present invention will be apparent from the embodiments of the present invention, wherein: FIG. 1 is a schematic diagram illustrating a preferred embodiment of the blast furnace blast furnace system of the present invention; FIGS. Comparing the figures, the relationship between the penetration factor of the preferred embodiment and the wind-diameter zone factor is illustrated; FIG. 4 is a schematic diagram illustrating the dimensional conditions of the blaster nozzle and the wind-diameter zone for performing the simulation experiment; and FIG. 5 is a comparison diagram. The relationship between the pressure loss of the air outlet of the air blowing nozzle and the length of the air blowing nozzle into the blast furnace, and the diameter of the air blowing nozzle.

參閱圖1,本發明高爐的鼓風系統之較佳實施例包含多個鼓風單元2。每一鼓風單元2具有一鼓風管21、一連通該鼓風管21且伸入該高爐200的鼓風嘴22,及一伸入該鼓風管21的噴鎗機構23。由於所述鼓風單元2的結構相同,因此,圖1中僅以一鼓風單元2作說明。 Referring to Figure 1, a preferred embodiment of the blast system of the blast furnace of the present invention comprises a plurality of blower units 2. Each of the air blowing units 2 has a blast tube 21, a blast nozzle 22 that communicates with the blast tube 21 and extends into the blast furnace 200, and a lance mechanism 23 that projects into the blast tube 21. Since the structure of the air blowing unit 2 is the same, only one air blowing unit 2 will be described in FIG.

於本較佳實施例中,該鼓風單元2的噴鎗機構23是兩分別能同時由該鼓風嘴22噴出高爐爐頂氣與粉煤的非對稱雙氣冷式同軸噴鎗(double air-cooled coaxial lance),且所述非對稱雙氣冷式同軸噴鎗是如圖1所示,以偏心方式插入該鼓風管21中,當然,實際應用上,該鼓風單元2的噴鎗機構23也可以是凸出式噴鎗,依然可以達成相同的效果。 In the preferred embodiment, the lance mechanism 23 of the air blowing unit 2 is an asymmetric double air-cooled coaxial spray gun capable of simultaneously ejecting blast furnace top gas and pulverized coal from the blast nozzle 22 (double air -cooled coaxial lance), and the asymmetric double air-cooled coaxial spray gun is inserted into the blast tube 21 in an eccentric manner as shown in FIG. 1. Of course, in practical application, the air blower unit 2 has a spray gun The mechanism 23 can also be a projecting spray gun, and the same effect can still be achieved.

而發明人是進行如圖1所示之高爐的鼓風系統 的模擬實驗,以獲得如圖2、3所示該鼓風系統之穿透因子(Penetration Factor,PF)與風徑區因子(Raceway Factor,RF)的關係圖,再以迴歸分析求得風徑區深度(如圖1中假想線所示)與鼓風動能的關係。 The inventor conducted a simulation experiment of the blast system of the blast furnace as shown in Fig. 1 to obtain the Penetration Factor (P F ) and the wind diameter zone factor of the blast system as shown in Figs. The relationship diagram of Raceway Factor, R F ), and regression analysis to obtain the relationship between the depth of the wind tunnel (shown as the imaginary line in Figure 1) and the kinetic energy of the blast.

其中,穿透因子是,而風徑區因子是0.5/ρ s gd p L R 是風徑區深度、D t 是該鼓風嘴22的口徑、ρ是氣體密度、V ave 是氣體速度、ρ s 是粒子密度、g是重力加速圖,d p 是粒子直徑。 Where the penetration factor is And the wind diameter zone factor is 0.5 / ρ s gd p , L R is the depth of the wind tunnel, D t is the diameter of the blast nozzle 22, ρ is the gas density, V ave is the gas velocity, ρ s is the particle density, g is the gravity acceleration map, d p Is the particle diameter.

由於風徑區因子與速度的平方成正比,因此,圖2以準二維模型所迴歸出的PF-RF曲線,在加速段時約為速度的1.2次方,而減速段時約為速度的1.6次方;圖3以三維模型所迴歸出的PF-RF曲線,在加速段與減速段皆與速度的1次方正比。由上述可知,風徑區深度是與鼓風嘴22的口徑成1次方正比,而與速度呈1~1.6次方的關係,即Since the wind-span zone factor is proportional to the square of the velocity, the P F -R F curve regressed by the quasi-two-dimensional model in Fig. 2 is about 1.2 times the velocity in the acceleration segment, and about 0.8 in the deceleration segment. The speed of the 1.6th power; Figure 3 is a three-dimensional model of the P F -R F curve, both in the acceleration section and the deceleration section are proportional to the speed of the first power. As can be seen from the above, the depth of the wind-diameter region is proportional to the diameter of the blast nozzle 22, and the relationship with the speed is 1 to 1.6, that is, .

再依據穆迪圖表(Moody Chart)可知,該鼓風嘴22出風口的壓損是與該鼓風嘴22伸入該高爐200的長度,及流體動能成正比,而與該鼓風嘴22的口徑成反比,即According to the Moody Chart, the pressure loss of the air outlet of the air blowing nozzle 22 is proportional to the length of the air blowing nozzle 22 extending into the blast furnace 200, and the fluid kinetic energy, and the air blowing nozzle 22 The caliber is inversely proportional, ie .

其中,△P t 是該鼓風嘴22出風口的壓損、f是磨擦因子、L t 是該鼓風嘴22伸入該高爐200的長度、D t 是該鼓風嘴22的口徑,流體動能。 Where Δ P t is the pressure loss of the air outlet of the air blowing nozzle 22, f is the friction factor, L t is the length of the air blowing nozzle 22 extending into the blast furnace 200, and D t is the diameter of the air blowing nozzle 22, Fluid kinetic energy.

而在不影響風徑區深度的前提下(亦即維持相 同鼓風動能),可由兩式,推得 ,而在磨擦因子(f)與風徑區深度(L R )相同的 情形下上式可簡化為,也就是說該鼓風嘴22出風口的壓損(△P t ),是與該鼓風嘴22伸入該高爐200的長度(L t )成正比,而與該鼓風嘴22的口徑(D t )的2.25~3次方成反比。 Without prejudice to the depth of the wind tunnel (ie maintaining the same blast kinetic energy), versus Two styles, pushed And when the friction factor ( f ) is the same as the wind path depth ( L R ), the above equation can be simplified to That is, the pressure loss (Δ P t ) of the air outlet of the air blowing nozzle 22 is proportional to the length ( L t ) of the air blowing nozzle 22 extending into the blast furnace 200, and the diameter of the air blowing nozzle 22 ( D t ) is inversely proportional to the 2.25~3 power.

參閱圖4、5,為驗證本發明的效果,發明人以圖4所示,預定風徑區深度為950mm,伸入該高爐200的長度(L t )分別為405mm與470mm,且口徑(D t )分別為120mm、130mm及135mm的鼓風嘴22進行模擬實驗,其結果如圖5所示。 Referring to Figures 4 and 5, in order to verify the effect of the present invention, the inventors, as shown in Figure 4, have a predetermined wind-diameter zone depth of 950 mm, and the length ( L t ) of the blast furnace 200 is 405 mm and 470 mm, respectively, and the diameter ( D) t ) Simulation experiments were carried out on the blast nozzles 22 of 120 mm, 130 mm and 135 mm, respectively, and the results are shown in Fig. 5.

由圖5可知,在相同長度的情形下,增加口徑(D t )確實能降低該鼓風嘴22出風口的壓損;而在相同口徑(D t )的情形下,縮短長度(L t )也能降低該鼓風嘴22出風口的壓損(△P t ),且對於該鼓風嘴22出風口的壓損(△P t )而言,口徑(D t )的影響大於長度(L t )的影響。 As can be seen from Fig. 5, in the case of the same length, the increase of the diameter ( D t ) can actually reduce the pressure loss of the air outlet of the air blowing nozzle 22; and in the case of the same aperture ( D t ), the length ( L t ) is shortened. The pressure loss (Δ P t ) of the air outlet of the air blowing nozzle 22 can also be reduced, and the influence of the diameter ( D t ) is greater than the length ( L ) for the pressure loss (Δ P t ) of the air outlet of the air blowing nozzle 22 t ) the impact.

綜上所述,本發明高爐的鼓風系統在無法避免高爐爐頂氣提早燃燒的情況下,利用滿足方程式:的鼓風嘴22,配合調整該鼓風嘴22伸入該高爐200的長度與該鼓風嘴22的口徑,以在不影響風徑區深度的情形下維持壓損,且能提高煉鐵製程之穩定性,故確實能達成本發明之目的。 In summary, the blast system of the blast furnace of the present invention utilizes the satisfaction equation in the case where the blast furnace top gas cannot be prevented from being prematurely burned: The blaster 22 adjusts the length of the blast furnace 22 into the blast furnace 200 and the diameter of the blast nozzle 22 to maintain the pressure loss without affecting the depth of the wind tunnel region, and can improve the iron making process. The stability of the invention is indeed achieved by the object of the present invention.

惟以上所述者,僅為本發明之較佳實施例而已 ,當不能以此限定本發明實施之範圍,即大凡依本發明申請專利範圍及專利說明書內容所作之簡單的等效變化與修飾,皆仍屬本發明專利涵蓋之範圍內。 However, the above is only the preferred embodiment of the present invention. The scope of the present invention is not limited thereto, that is, the simple equivalent changes and modifications made by the present invention in the scope of the invention and the scope of the patent specification are still within the scope of the invention.

2‧‧‧鼓風單元 2‧‧‧Blowing unit

200‧‧‧高爐 200‧‧‧ blast furnace

21‧‧‧鼓風管 21‧‧‧Blowing tube

22‧‧‧鼓風嘴 22‧‧‧ blaster

23‧‧‧噴鎗機構 23‧‧‧ spray gun mechanism

Claims (4)

一種高爐的鼓風系統,包含:至少一鼓風單元,具有一鼓風管、一連通該鼓風管且伸入該高爐的鼓風嘴,及一伸入該鼓風管的噴鎗機構,該鼓風嘴滿足下式: 其中,△P t 是該鼓風嘴出風口的壓損、f是磨擦因子、L t 是該鼓風嘴伸入該高爐的長度、D t 是該鼓風嘴的口徑,L R 是風徑區深度。 An blast system of a blast furnace, comprising: at least one blast unit, having a blast tube, a blast nozzle connecting the blast tube and extending into the blast furnace, and a lance mechanism extending into the blast tube The blaster meets the following formula: Where Δ P t is the pressure loss of the air outlet of the air blowing nozzle, f is the friction factor, L t is the length of the air blowing nozzle into the blast furnace, D t is the diameter of the air blowing nozzle, and L R is the air diameter Area depth. 如請求項1所述高爐的鼓風系統,其中,該鼓風單元的噴鎗機構是同時由該鼓風嘴噴出高爐爐頂氣與粉煤。 The blast system of the blast furnace according to claim 1, wherein the blasting mechanism of the blast unit simultaneously ejects blast furnace top gas and pulverized coal from the blast nozzle. 如請求項1所述高爐的鼓風系統,其中,該鼓風單元的噴鎗機構是非對稱雙氣冷式同軸噴鎗。 The blast furnace blast furnace system of claim 1, wherein the blasting unit of the blast unit is an asymmetric dual air cooled coaxial lance. 如請求項1所述高爐的鼓風系統,包含多個鼓風單元。 The blast system of the blast furnace according to claim 1, comprising a plurality of air blowing units.
TW102115105A 2013-04-26 2013-04-26 Blast furnace blast system TWI580790B (en)

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Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0776713A (en) * 1993-09-10 1995-03-20 Nippon Steel Corp Operation of shifting layer type scrap melting furnace
JP2006241526A (en) * 2005-03-03 2006-09-14 Nippon Steel Corp Burner for blowing powdered coal in blast furnace, and powdered coal blowing method using the same

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0776713A (en) * 1993-09-10 1995-03-20 Nippon Steel Corp Operation of shifting layer type scrap melting furnace
JP2006241526A (en) * 2005-03-03 2006-09-14 Nippon Steel Corp Burner for blowing powdered coal in blast furnace, and powdered coal blowing method using the same

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