JP3286762B2 - Slurry supply conduit and pressurized fluidized bed combustion furnace - Google Patents

Slurry supply conduit and pressurized fluidized bed combustion furnace

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Publication number
JP3286762B2
JP3286762B2 JP25793192A JP25793192A JP3286762B2 JP 3286762 B2 JP3286762 B2 JP 3286762B2 JP 25793192 A JP25793192 A JP 25793192A JP 25793192 A JP25793192 A JP 25793192A JP 3286762 B2 JP3286762 B2 JP 3286762B2
Authority
JP
Japan
Prior art keywords
slurry
coal
combustion furnace
fluidized bed
water
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 - Lifetime
Application number
JP25793192A
Other languages
Japanese (ja)
Other versions
JPH06109230A (en
Inventor
進 吉岡
博 武▲崎▼
義則 大谷
公大 野中
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mitsubishi Power Ltd
Original Assignee
Babcock Hitachi KK
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Babcock Hitachi KK filed Critical Babcock Hitachi KK
Priority to JP25793192A priority Critical patent/JP3286762B2/en
Publication of JPH06109230A publication Critical patent/JPH06109230A/en
Application granted granted Critical
Publication of JP3286762B2 publication Critical patent/JP3286762B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Fluidized-Bed Combustion And Resonant Combustion (AREA)

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は石灰・水スラリー供給導
管に関し、特に加圧した流動層で石炭を燃焼し、発生し
たスチームによって蒸気タービンを駆動し、さらに高
圧、高温の燃焼ガスでガスタービンを駆動して高効率で
電力を得る加圧流動層ボイラ複合発電プラントの燃焼炉
へ石炭と水の混合スラリーを供給するときの該石炭・水
スラリー(以下、単にスラリーと称することがある)の
供給導管に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a lime / water slurry supply pipe, and more particularly, to burning coal in a pressurized fluidized bed, driving a steam turbine by generated steam, and further using a high pressure, high temperature combustion gas to produce a gas turbine. Of coal / water slurry (hereinafter sometimes simply referred to as slurry) when supplying a mixed slurry of coal and water to a combustion furnace of a pressurized fluidized-bed boiler combined cycle power plant that obtains electric power with high efficiency by driving It relates to a supply conduit.

【0002】[0002]

【従来の技術】加圧流動層ボイラ(燃焼炉)は発生する
スチームおよび高圧の燃焼ガスからエネルギーを得るこ
とができるので高効率の発電が可能である。ただし固体
である石炭粒子を加圧状態の燃焼炉内に連続的に、大量
に安定して供給することが課題の一つである。従来、流
動層燃焼炉へ石炭を供給する方法として、石炭粒子と水
を混合してスラリー状の流体とし該スラリーをポンプで
昇圧および圧送して噴霧ノズルから供給する湿式供給方
式(たとえば特開昭62−155433号公報)があ
る。該スラリー供給方式は、乾式供給方式たとえばロッ
クホッパで昇圧したあと空気輸送する方式に比べ、乾燥
などの前処理が不要で低コストで、また輸送管の摩耗が
少ないので信頼性が高い。しかしながら、発電効率を乾
式供給方式と同等に維持する上で石炭に添加する水の量
をできるだけ少なくしなければならない。このため添加
水量が限定され石炭・水スラリーは粘度が高く、しかも
石炭の最大粒子径は数mmと大きく流動性に乏しい。流
動性に乏しい石炭・水スラリーを流動層燃焼炉へ供給す
るにあたっては、ピストンポンプなどの定量型のポンプ
が用いられ導管を経てノズルから噴霧して燃焼炉内に供
給される。
2. Description of the Related Art A pressurized fluidized-bed boiler (combustion furnace) can obtain energy from generated steam and high-pressure combustion gas, so that high-efficiency power generation is possible. However, one of the issues is to continuously and stably supply solid coal particles into a pressurized combustion furnace in a large amount. Conventionally, as a method of supplying coal to a fluidized bed combustion furnace, a wet supply method in which coal particles and water are mixed to form a slurry-like fluid and the slurry is pressurized and pumped by a pump and supplied from a spray nozzle (for example, 62-155433). The slurry supply method is more reliable than the dry supply method, for example, a method in which pretreatment such as drying is not required and the cost is low, and the abrasion of the transport pipe is small, as compared with a method in which the pressure is increased by a lock hopper and the air is transported. However, the amount of water added to the coal must be reduced as much as possible in order to maintain the power generation efficiency at the same level as in the dry feed system. For this reason, the amount of added water is limited, and the viscosity of the coal / water slurry is high, and the maximum particle size of the coal is as large as several mm and the fluidity is poor. When supplying the coal / water slurry having poor fluidity to the fluidized bed combustion furnace, a fixed-quantity pump such as a piston pump is used, and is sprayed from a nozzle through a conduit and supplied into the combustion furnace.

【0003】なお、従来重油の代替燃料として開発され
たCWM(石炭・水ミクスチャー)がある。これは石炭
の平均粒子径が数10μmの微粒子であり、また水分量
も35wt%前後で、さらに粘度低下のための界面活性
剤が添加される。したがって、本発明に係わる石炭・水
スラリーの粘度が10〜20Pa・sであるのに対し、
CWMは1Pa・s前後で粘度がかなり低い。
[0003] There is CWM (coal / water mixture) which has been developed as a fuel alternative to heavy oil. This is a fine particle having an average particle diameter of several tens of μm of coal, having a water content of about 35 wt%, and further adding a surfactant for decreasing the viscosity. Therefore, while the viscosity of the coal / water slurry according to the present invention is 10 to 20 Pa · s,
CWM has a very low viscosity at around 1 Pa · s.

【0004】[0004]

【発明が解決しようとする課題】上述したスラリー湿式
供給方式はポンプから燃焼炉の噴霧ノズルまで石炭・水
スラリーを供給する導管において、特に内径の異なる導
管相互の接続部において、スラリーを噴霧するために前
記導管内径を縮小する必要性がある場合、重油あるい
はCWMなどの低粘性液を供給すると同様に任意に導管
径を縮小したところ、供給導管に詰まりを生じスラリー
の供給が不能になる問題点があった。そこで、本発明の
目的は、例えば石炭・水スラリー等のスラリーを閉塞さ
せることなく円滑に輸送する供給導管を提供し、さらに
信頼性のより高い加圧流動層燃焼炉を実現することであ
る。
THE INVENTION Problems to be Solved] In the conduit for supplying coal-water slurry to the spray nozzle of the combustion furnace slurry wet feed system described above from the pump, particularly Oite conduit interconnections portions having different inner diameter, spraying the slurry If it is necessary to reduce the inner diameter of the conduit in order to reduce the diameter of the conduit arbitrarily in the same way as supplying a low-viscosity liquid such as heavy oil or CWM, the supply conduit will be clogged and the slurry cannot be supplied. There was a problem. Therefore, an object of the present invention is to provide a supply conduit for smoothly transporting a slurry such as a coal / water slurry without clogging, and to realize a more reliable pressurized fluidized bed combustion furnace.

【0005】[0005]

【課題を解決するための手段】上記の問題点を解決する
ために鋭意検討を行ったところ、石炭・水スラリーを円
滑に輸送する導管径の減少率をある特定範囲以下にすべ
きことがわかった。すなわち、本発明は石炭・水スラリ
を供給する燃料供給導管を具備する加圧流動層燃焼炉
において、スラリ中の水分が20〜35wt%、かつ、
該スラリの粘度が10〜20Pa・sである石炭・水ス
ラリの供給導管の絞り部の絞り角度を、該スラリの流動
方向に向けて、供給導管の中心線に対する縮小角度を5
度以下にした石炭・水スラリ供給導管を具備する加圧流
動層燃焼炉である。
The present inventors have made intensive studies to solve the above-mentioned problems, and found that the reduction rate of the diameter of the conduit for smoothly transporting the coal / water slurry should be within a specific range. all right. That is, the present invention relates to a pressurized fluidized bed combustion furnace having a fuel supply conduit for supplying coal / water slurry.
In the above, the water in the slurry is 20 to 35 wt%, and
Coal / water slurry whose viscosity is 10-20 Pa · s
The throttle angle of the throttle section of the slurry supply conduit is determined by the flow rate of the slurry.
In direction, the contraction small angle of relative to the center line of the supply conduit 5
Pressurized flow with sub-coal and water slurry supply conduit
This is a moving bed combustion furnace.

【0006】[0006]

【作用】本発明が適用されるスラリーとして、加圧流動
層燃焼炉用の燃料である石炭・水スラリーを例にとり以
下説明する。発電効率を乾式供給方式と同等に維持する
上で石炭・水スラリー中の水分は、石炭の種類によって
異なるが20〜35wt%程度の範囲に限定される。そ
の結果得られるスラリーは粘度が10〜20Pa・s
で、しかも石炭の最大粒子径は数ミリメーターと大きく
流動性に乏しい。このようなスラリーを管径をある角度
以上に減少した導管内を流動させようとすると、断面縮
少部において石炭粒子群の圧密化が起こり、スラリーは
水分を分離して固着してしまう。従来技術におけるCW
Mのように粘度が低い場合には石炭粒子同志の間ですべ
りを生じ、連続の式を満足して圧密化することはない
が、上述の性質をもつ石炭・水スラリーでは管壁と石炭
粒子および石炭粒子同志の間ですべりを生じることがで
きず、石炭粒子が停滞し、圧密化してしまうと考えられ
る。
The slurry to which the present invention is applied will be described below with reference to a coal / water slurry as a fuel for a pressurized fluidized bed combustion furnace. In order to maintain the power generation efficiency equal to that of the dry supply system, the water content in the coal / water slurry is limited to a range of about 20 to 35 wt%, though it depends on the type of coal. The resulting slurry has a viscosity of 10-20 Pa · s
In addition, the maximum particle size of coal is as large as several millimeters and poor in fluidity. If such a slurry is caused to flow in a conduit whose pipe diameter is reduced to a certain angle or more, the coal particles are consolidated in the reduced cross section, and the slurry separates water and adheres. CW in the prior art
When the viscosity is low as in M, slippage occurs between the coal particles and the compaction does not occur by satisfying the continuity equation. It is considered that no slip occurs between the coal particles and the coal particles, and the coal particles stagnate and become compacted.

【0007】これに対して本発明のごとくスラリー供給
導管径の縮小角度を、導管の中心線に対する角度を5度
以下、好ましくは3度以下に選ぶことにより、管壁と石
炭粒子および石炭粒子同志の間にすべりを生じ、スラリ
ーは断面縮小部で閉塞することなく流通することができ
る。
On the other hand, according to the present invention, the angle of reduction of the diameter of the slurry supply conduit is selected to be 5 degrees or less, preferably 3 degrees or less with respect to the center line of the conduit, so that the pipe wall and the coal particles and the coal particles can be reduced. Slip occurs between the members, and the slurry can flow without being blocked at the reduced section.

【0008】[0008]

【実施例】次に図面をもって本発明の一実施例を詳細に
説明する。まず、本実施例を適用する加圧流動層燃焼炉
に対する石炭・水スラリーの供給系統を図2に示す。流
動層燃焼炉101は加圧容器104内に収納されてお
り、その底部に空気分散板105が設けられ、その上に
流動媒体粒子102が充填されている。加圧空気106
は加圧容器104内に供給されたあと燃焼用空気107
として、空気分散板105を通って燃焼炉101内に供
給され流動媒体粒子102を流動化して流動層109を
形成する。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Next, an embodiment of the present invention will be described in detail with reference to the drawings. First, a supply system of coal / water slurry to a pressurized fluidized bed combustion furnace to which this embodiment is applied is shown in FIG. The fluidized-bed combustion furnace 101 is housed in a pressurized container 104, and an air dispersion plate 105 is provided at the bottom thereof, on which a fluid medium particle 102 is filled. Pressurized air 106
Is the combustion air 107 after being supplied into the pressurized container 104.
Then, the fluidized medium particles 102 supplied through the air dispersion plate 105 into the combustion furnace 101 are fluidized to form the fluidized bed 109.

【0009】流動層燃焼炉101にはスラリー導管7を
通じてポンプ6によって、スラリータンク121に貯留
されている石炭・水スラリー120が圧送され、スラリ
ー噴霧ノズル110から流動層109内に供給され、燃
焼される。燃焼ガスは燃焼炉101の上部から排出さ
れ、サイクロン103でダストを除去したあと導管10
8を通ってガスタービン(図示を省略)に導入される。
A coal / water slurry 120 stored in a slurry tank 121 is pumped into a fluidized bed combustion furnace 101 by a pump 6 through a slurry conduit 7, supplied from a slurry spray nozzle 110 into a fluidized bed 109, and burned. You. The combustion gas is discharged from the upper part of the combustion furnace 101, and the dust is removed by the cyclone 103.
8 and is introduced into a gas turbine (not shown).

【0010】スラリータンク121内の石炭・水スラリ
ー120は上流のスラリー調整タンク(図示を省略)で
所定の粒径分布に調整された石炭粒子と該石炭粒子に対
する所定割合の清浄水および炉内脱硫用の石灰石粒子と
が混合、撹拌された後、導管4を通ってスラリータンク
121に補給され、貯留される。該タンク121内での
石炭・水スラリー120は電動機122によって回転さ
れる撹拌翼123によって撹拌され、流動性が保たれ
る。スラリー貯留タンク121の底部はバルブ5を介し
てスラリーポンプ6に接続されている。
The coal / water slurry 120 in the slurry tank 121 has coal particles adjusted to a predetermined particle size distribution in an upstream slurry adjusting tank (not shown), a predetermined ratio of clean water to the coal particles, and desulfurization in the furnace. After mixing and stirring with the limestone particles for use, the slurry is supplied to the slurry tank 121 through the conduit 4 and stored. The coal / water slurry 120 in the tank 121 is stirred by the stirring blade 123 rotated by the electric motor 122, so that the fluidity is maintained. The bottom of the slurry storage tank 121 is connected to the slurry pump 6 via the valve 5.

【0011】スラリー導管7の途中には切替バルブ3を
介してスラリータンク121へのスラリー循環導管8が
設けられる。またスラリー噴霧ノズル110内を空気で
パージするための加圧空気10のパージ空気供給管11
およびバルブ9が切替バルブ3の後流で、かつ切替バル
ブ3にできるだけ近い位置のスラリー導管7に設けられ
る。また、後述の図3にその詳細を示すので図2では図
示を省略するが、噴霧ノズル110にはスラリーを流動
層燃焼炉101内に噴霧、分散させるための噴霧空気の
導管および冷却水の導管が接続される。
In the middle of the slurry conduit 7, there is provided a slurry circulation conduit 8 to the slurry tank 121 via the switching valve 3. A purge air supply pipe 11 for pressurized air 10 for purging the inside of the slurry spray nozzle 110 with air.
And a valve 9 is provided in the slurry conduit 7 downstream of the switching valve 3 and as close as possible to the switching valve 3. Although not shown in FIG. 2 since the details are shown in FIG. 3 described later, the spray nozzle 110 has a spray air conduit and a cooling water conduit for spraying and dispersing the slurry in the fluidized bed combustion furnace 101. Is connected.

【0012】図2に示す上記系統において、たとえばポ
ンプ6の吐出管2の径がスラリー導管7の必要管径より
大きすぎて、吐出管2とスラリー導管7の接続部におい
て管径を縮小管1をもって縮小せざるを得ないことがあ
る。図1はその縮小管1の詳細断面図であり、スラリー
流入口フランジ21とスラリー流出口フランジ22の中
心を結ぶ中心線20と縮小管1の管内壁がなす角度θ1
(=縮小管部1の中心線20に対する縮小角θ1)は5
度以下、好ましくは3度以下に選ばれる。石炭・水スラ
リーはスラリータンク121およびその上流の調整タン
ク(図示を省略)で混合されはするものの、時には混合
が不十分で流動性のより乏しい混合状態の部分もあり、
信頼性を十分に確保する上からは縮小角θ1は3度以下
に選ぶことが好ましい。
In the above-mentioned system shown in FIG. 2, for example, the diameter of the discharge pipe 2 of the pump 6 is too large than the required diameter of the slurry pipe 7, and the diameter of the pipe is reduced at the connection between the discharge pipe 2 and the slurry pipe 7. Sometimes it is necessary to reduce with. FIG. 1 is a detailed cross-sectional view of the reduction tube 1, and shows an angle θ 1 formed between a center line 20 connecting the centers of the slurry inlet flange 21 and the slurry outlet flange 22 and the inner wall of the reduction tube 1.
(= Reduction angle θ 1 with respect to the center line 20 of the reduction tube 1 ) is 5
Degrees or less, preferably 3 degrees or less. Although the coal / water slurry is mixed in the slurry tank 121 and a regulating tank (not shown) upstream of the slurry, sometimes there is a part in a mixed state where mixing is insufficient and fluidity is poor,
From the viewpoint of ensuring sufficient reliability, it is preferable to select the reduction angle θ 1 to be 3 degrees or less.

【0013】[0013]

【0014】記実施例ではスラリー供給導管を加圧流
動層燃焼炉に適用した場合を説明したが、本発明はこれ
に限らず、その他の燃焼炉あるいはスラリー状の流体の
供給装置にも適用できる。
[0014] While the above SL embodiment has been described the case of applying the slurry supply conduit to a pressurized fluidized bed combustion furnace, the present invention is not limited thereto, applied to the supply device of the other combustion furnace or slurry fluid it can.

【0015】[0015]

【発明の効果】本発明によれば、たとえば加圧流動層燃
焼炉等の燃焼炉への石炭・水スラリーの供給において、
スラリー供給導管が閉塞を生じることがなくなるので信
頼性の高い燃焼炉を提供することができる。
According to the present invention, for example, in supplying coal / water slurry to a combustion furnace such as a pressurized fluidized bed combustion furnace,
Since slurry supply conduits it is not necessary to produce a closure can be provided a highly reliable combustion furnace.

【図面の簡単な説明】[Brief description of the drawings]

【図1】 本発明の一実施例のスラリー供給導管の縮小
管部の断面図である。
FIG. 1 is a cross-sectional view of a reduced tube portion of a slurry supply conduit according to an embodiment of the present invention.

【図2】 本発明の一実施例を適用する加圧流動層燃焼
炉へ石炭・水スラリーの供給系統図である
FIG. 2 is a supply system diagram of a coal / water slurry to a pressurized fluidized bed combustion furnace to which an embodiment of the present invention is applied .

【符号の説明】[Explanation of symbols]

1…縮小管部、2…ポンプの吐出管、6…スラリーポン
プ、7…スラリー導管、10…加圧空気、20…縮小管
部の中心線、101…流動層燃焼炉、103…サイクロ
ン、104…加圧容器、105…空気分散板、106…
加圧空気、107…燃焼用空気、109…流動層、11
0…スラリー噴霧ノズル、120…石炭・水スラリー、
121…スラリータンク、θ…中心線に対する縮小角
DESCRIPTION OF SYMBOLS 1 ... Reduction pipe part, 2 ... Pump discharge pipe, 6 ... Slurry pump, 7 ... Slurry conduit, 10 ... Pressurized air, 20 ... Center line of reduction pipe part, 101 ... Fluidized bed combustion furnace, 103 ... Cyclone, 104 ... Pressure container, 105 ... Air dispersion plate, 106 ...
Pressurized air, 107: combustion air, 109: fluidized bed, 11
0: Slurry spray nozzle, 120: Coal / water slurry,
121: slurry tank, θ 1 : reduction angle with respect to the center line

───────────────────────────────────────────────────── フロントページの続き (72)発明者 野中 公大 広島県呉市宝町6番9号 バブコック日 立株式会社 呉工場内 (56)参考文献 特開 昭61−223420(JP,A) 特開 昭62−13923(JP,A) 特開 昭57−80115(JP,A) 実開 昭60−38330(JP,U) 実開 平4−92128(JP,U) (58)調査した分野(Int.Cl.7,DB名) F23K 3/00 F23C 10/22 ──────────────────────────────────────────────────続 き Continuation of the front page (72) Inventor Kodai Nonaka 6-9 Takara-cho, Kure-shi, Hiroshima Babcock Hitachi Ltd. Inside the Kure factory (56) References JP-A-61-223420 (JP, A) JP-A-62-13923 (JP, A) JP-A-57-80115 (JP, A) JP-A-60-38330 (JP, U) JP-A-4-92128 (JP, U) (58) Fields investigated (Int) .Cl. 7 , DB name) F23K 3/00 F23C 10/22

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 石炭・水スラリーを供給する燃料供給導
管を具備する加圧流動層燃焼炉において、スラリ中の水
分が20〜35wt%、かつ、該スラリの粘度が10〜
20Pa・sである石炭・水スラリの供給導管の絞り部
の絞り角度を、該スラリの流動方向に向けて、供給導管
の中心線に対する縮小角度を5度以下にした石炭・水ス
ラリ供給導管を具備することを特徴とする加圧流動層燃
焼炉。
1. A fuel supply system for supplying a coal / water slurry
In a pressurized fluidized bed combustion furnace equipped with tubes, the water in the slurry
20 to 35 wt%, and the viscosity of the slurry is 10 to
Restriction section of coal / water slurry supply pipe of 20 Pa · s
The aperture angle, toward a flow direction of the slurry, coal and Myzus that the reduced small angle of below 5 degrees with respect to the center line of the supply conduit
Pressurized fluidized bed fuel characterized by having a rally supply conduit
Furnace.
JP25793192A 1992-09-28 1992-09-28 Slurry supply conduit and pressurized fluidized bed combustion furnace Expired - Lifetime JP3286762B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP25793192A JP3286762B2 (en) 1992-09-28 1992-09-28 Slurry supply conduit and pressurized fluidized bed combustion furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP25793192A JP3286762B2 (en) 1992-09-28 1992-09-28 Slurry supply conduit and pressurized fluidized bed combustion furnace

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JPH06109230A JPH06109230A (en) 1994-04-19
JP3286762B2 true JP3286762B2 (en) 2002-05-27

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JPS5780115A (en) * 1980-11-06 1982-05-19 Nippon Kokan Kk <Nkk> Atomization of sludge
JPS6038330U (en) * 1983-08-19 1985-03-16 技術研究組合 医療福祉機器研究所 fluid transfer mechanism
JPS61223420A (en) * 1985-03-28 1986-10-04 Mitsubishi Chem Ind Ltd Combustion of water slurry fuel
JPS6213923A (en) * 1985-07-10 1987-01-22 Kawasaki Steel Corp Device for blowing coal-water slurry into shaft furnace
JP2545251Y2 (en) * 1990-12-25 1997-08-25 石川島播磨重工業株式会社 Fuel nozzle of pressurized fluidized bed boiler

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