JPS5820928A - Device for recovering energy of blast-furnace gas - Google Patents

Device for recovering energy of blast-furnace gas

Info

Publication number
JPS5820928A
JPS5820928A JP56118936A JP11893681A JPS5820928A JP S5820928 A JPS5820928 A JP S5820928A JP 56118936 A JP56118936 A JP 56118936A JP 11893681 A JP11893681 A JP 11893681A JP S5820928 A JPS5820928 A JP S5820928A
Authority
JP
Japan
Prior art keywords
blast furnace
gas
turbine
furnace gas
heater
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.)
Pending
Application number
JP56118936A
Other languages
Japanese (ja)
Inventor
Shinichi Saito
伸一 斉藤
Masaru Ishihara
勝 石原
Shinya Nakano
真也 中野
Takero Sato
佐藤 健朗
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.)
Nippon Steel Corp
Original Assignee
Nippon Steel Corp
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 Nippon Steel Corp filed Critical Nippon Steel Corp
Priority to JP56118936A priority Critical patent/JPS5820928A/en
Publication of JPS5820928A publication Critical patent/JPS5820928A/en
Pending legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D47/00Separating dispersed particles from gases, air or vapours by liquid as separating agent
    • B01D47/10Venturi scrubbers
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P70/00Climate change mitigation technologies in the production process for final industrial or consumer products
    • Y02P70/10Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Separation Of Particles Using Liquids (AREA)
  • Blast Furnaces (AREA)

Abstract

PURPOSE:To supply a high-temperature blast-furnace gas to a turbine and contrive to increase the amount of the generated power, by providing a heater for a gas cleaner train of the titled device operated by using a furnace top pressure turbine. CONSTITUTION:A secondary venturi scrubber 2VS in the gas cleaner train of the titled device is provided with mist separators 4a, 4b which are composed of two-layer Raschig rings and are placed in planes transversing a gas passage between a venturi pipe 2 located on the axis line of the interior of a main body 1 and a discharge pipe 3. The heater 5 is provided at a part on the downstream side, i.e. the discharge pipe 3 side, of the mist separators 4a, 4b where the cross- sectional area of the passage is large.

Description

【発明の詳細な説明】 本願発明は、高炉より導出した高炉ガjEIlc)保有
する圧カエネルゼーを炉頂圧タービン(以下単にタービ
ンと称する)によ〕、電気として回収する装置に関する
ものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an apparatus for recovering pressure energy derived from a blast furnace and retained in the blast furnace as electricity using a furnace top pressure turbine (hereinafter simply referred to as a turbine).

近部会製鉄所における高炉は、高圧操業がさかんに行わ
れて:tp)、その炉容も超大臘で諌高炉炉頂よ)導出
した萬デダヌ#i1.6〜2. II気圧稠度の高圧で
しかも1万Nms’/mi島1度と多量なIメ量に達し
1いるものが多い。この莫大な高炉tJLの圧力エネル
ギーは一般にタービンを設置して電気としてwUIfL
シ省エネルゼー化をlEIりて−る。
The blast furnace at Chibakai Steel Works is frequently operated under high pressure (tp), and its furnace capacity is extremely large, reaching the top of the blast furnace. In many cases, the pressure is as high as 1.2 atmospheric pressures, and the amount of pressure reaches as high as 10,000 Nms'/mi island. The pressure energy of this huge blast furnace tJL is generally converted into electricity by installing a turbine.
I am looking forward to energy saving.

ヒの高炉ガスの圧力エネルギーのa収工1は、〔高炉−
fJ清浄装置列−声−Vン一ガメホルダー〕から構成さ
れてお)、#タービンでの発電量は次式に示す通)であ
る。
A yield 1 of the pressure energy of blast furnace gas in [blast furnace -
The amount of power generated by the turbine is as shown in the following equation.

但し L:発電量(kwHt ) Cp:高炉ガス比熱(kmt/Nm墨℃)Q:高炉fJ
IE流量(胸ν’Hr )T:高炉ガヌ温1!(C) P凰;タービン人側圧カ(’Is/as” )P3:タ
ーk”y出側圧力(KI乃−)ッ:効率 に:断熱指数 この式よ〕所定の高炉tJIEi!l量Qで発電量りを
可能な限)大にするには、′14#IIからタービンに
至る壜での過薯で高炉ガス圧力の低下を最小限にとどめ
ることが必要である。
However, L: Power generation (kwHt) Cp: Blast furnace gas specific heat (kmt/Nm black °C) Q: Blast furnace fJ
IE flow rate (chest ν'Hr) T: Blast furnace Ganu temperature 1! (C) P 凰; Turbine side pressure ('Is/as) P3: Turbine outlet pressure (KI -): Efficiency: insulation index According to this formula] For a given blast furnace tJIEi! In order to maximize the amount of power generated with the quantity Q, it is necessary to minimize the drop in the blast furnace gas pressure due to overloading in the bottle from '14#II to the turbine.

しかし高トターピン間の高炉ガス系路に配列のガス清浄
装置列における高炉ガスの圧力0降下量は着しく大lく
、これが諌タービンの発電効率の低下を招いておplそ
の改善が望まれている。
However, the zero pressure drop of the blast furnace gas in the gas purifier array arranged in the blast furnace gas line between the high-tower pins is quite large, and this causes a decrease in the power generation efficiency of the Isato turbine, so improvement is desired. There is.

この改善策として圧力低下の原因である水洗による温度
降下を補償することが従来がら種々検討されて會えがそ
のいずれも実用上に問題がある。
Various attempts have been made to compensate for the temperature drop due to water washing, which is the cause of the pressure drop, as a countermeasure for this problem, but all of them have problems in practical use.

例えば高炉ガスをガス清浄装置列とタービンとの管路に
多l[O費用を投じてケーシングを介設し、これに加熱
器を入れることが考えられるが、高炉ガスは高速で流れ
るえめ熱交換に紘骸管路の長手方向の広域に亘りて熱交
換器を嬌在せざるを得す現実的にヌベーヌがなく回収発
電量の増大は期待できない。
For example, it is conceivable to insert blast furnace gas into the pipeline between the gas purifier row and the turbine by interposing a casing at great expense and inserting a heater into it, but since blast furnace gas flows at high speed, heat exchange is possible. Since heat exchangers have to be installed over a wide area in the longitudinal direction of the pipeline, there is no realistic nuvene and no increase in the amount of recovered power generation can be expected.

本発明はこれら問題を解決し、回収エネルギーを効率よ
く増大する装置を提供するものであ〕、その特徴とする
ところは、−′炉ガスをガス清浄装置列を介して導出す
る管路に炉頂圧タービンを接続して腋タービンによル、
諌高fガスの有する圧力エネルギーを回収する装置にお
いて、前記ガス清浄装置列に加熱器を配設した高炉ガス
エネルイー回収装置にある。
The present invention solves these problems and provides a device that efficiently increases recovered energy.The features of the present invention are as follows: Connect the top pressure turbine to the axillary turbine,
In the apparatus for recovering the pressure energy of Idaka f gas, there is provided a blast furnace gas energy recovery apparatus in which a heater is disposed in the gas purifier row.

即ち本発明は、ター−yに供給する高炉ガスの加熱昇温
を専用の設備を設けることなく既設々備で最もガス流速
の低下してい為ペンチ1リーメタラバー、バッグフィル
ター、サンドフィルター勢のガス清浄装置で効率よく行
わしめるものである。
That is, the present invention can heat and raise the temperature of the blast furnace gas supplied to the furnace without installing dedicated equipment, and with the lowest gas flow rate among existing equipment, it is possible to clean the gas using pliers, one-way metal rubber, bag filters, and sand filters. This can be done efficiently using equipment.

つtb、該高炉ガス清浄装置列がペンテmリースクツパ
ーであるとIaその内部に充填式遠心分離型勢の建スト
セΔレータ−を配設してこれに高炉ガスを導き広大な横
断面O流路を低速流動せしめつつ更に加熱器に導き加熱
昇温を効率よく行@A。
When the blast furnace gas purifying equipment row is a pentley stopper, a packed centrifugal separator-type stator is arranged inside it, and the blast furnace gas is guided to this through a vast cross-sectional O flow channel. While flowing at a low speed, the mixture is further guided to a heater to efficiently raise the temperature @A.

よp高温の高炉ガスをタービンに供給し発電量の増大を
有利に可能とし九−〇で、水洗浄後の々メト随伴高炉ガ
スから#電ヌトO殆んどを除去して該間接加熱器からの
電ヌト蒸発抜熱量を殆んど皆無にし1高炉fJIQ)1
1iJ熱昇1効率を一段と高′t′*   。
By supplying high-temperature blast furnace gas to the turbine, it is possible to advantageously increase the amount of power generation. Almost eliminates the amount of heat removed by evaporation from the blast furnace fJIQ) 1
1iJ heat rise 1 efficiency is further increased 't'*.

ものである。It is something.

更に本発明において、前記加熱1lIK熱流媒体として
例えは高炉々体冷却設備から0発生蒸気、高温排水、高
炉近傍に設置しである熱風炉からの燃焼廃fJR自体又
はこれの排出管路に設けた熱交換器からの熱流媒体、水
砕製造装置から得られる多量O高温排水、或いは、空気
圧送装置の出側に設は九圧送顕熱回収装置からの熱流媒
体勢安価にしかも容易且り亭量に量られる高温”熱流媒
体を用いる場合は、間接加熱とすることが望ましい。本
発@においては、省土ネルギーの面から専用の熱流媒体
製造装置を設置することもなく既設の熱流媒体製造装置
を有効に利用することが極めて有利である。
Furthermore, in the present invention, the heating 1lIK heat flow medium may be, for example, steam generated from blast furnace body cooling equipment, high temperature waste water, combustion waste fJR itself from a hot blast furnace installed near the blast furnace, or installed in its discharge pipe. The heat flow medium from a heat exchanger, a large amount of high-temperature wastewater obtained from a granulation manufacturing device, or the heat flow medium from a sensible heat recovery device that is installed on the outlet side of an air pumping device is inexpensive, easy to use, and has a small amount of storage. When using a high-temperature heat flow medium that can be measured in It is extremely advantageous to make effective use of the

以下本発Ij1の1実施例を図面と共に詳細に説明する
Hereinafter, one embodiment of the present invention Ij1 will be described in detail with reference to the drawings.

jllmlにおいて、本例の高炉ガスエネルギー回II
L装置は、高炉lνO炉頂から導出した高炉ガス〔圧カ
ニ1.8〜2.84/副2、温度100℃、流量二60
万〜72万Nm”/llr )を!ヌトキャyチャーD
@C−1次ペンテ晶す−ヌクラパーIVB −2次ペン
チ暴リースタッパー2VIl t−順次′導入して清浄
するガス清浄装置列と、前記2次ペンチ轟す−ヌクラバ
ー2YIからO清浄化高炉tヌを定常閉止状にした°高
炉々頂圧非常制御用セf声ン弁svl o上流側に設け
た分岐管1Dから高炉々頂圧定常制御用弁Sv3を介し
てタービ3/ ’rl? K供給して同ターーンを回転
させ連接発電機りを発電出力動作せしめる発電装置と、
該ターに#y 71?を通過した高炉ガスを水封弁v−
、サイレン豐−8を介して一旦ガスホルダー〇Hに貯蔵
し各種燃焼設備に供給する装置とからなる。
At jllml, the blast furnace gas energy cycle II of this example
The L device is a blast furnace gas derived from the top of the blast furnace lνO [pressure crab 1.8 to 2.84/sub 2, temperature 100°C, flow rate 260°C.
10,000 to 720,000 Nm”/llr)!
@C-1st Pente crystallizer Nuclaper IVB -2nd Pliers blower stapper 2VIl t-Sequentially' introduction and cleaning gas purifier line and the secondary pliers roarer Nuclaver 2YI to O cleaning blast furnace tnu The turbine 3/'rl? is in a normally closed state from the branch pipe 1D provided on the upstream side via the blast furnace top pressure steady control valve Sv3. a power generating device that supplies K to rotate the turn and operate the linked generator to generate power;
#y 71 for the target? The blast furnace gas that has passed through the water seal valve v-
, and a device that temporarily stores the gas in the gas holder 〇H via the siren-8 and supplies it to various combustion equipment.

前記七プタム弁8V1は、前記定常制御弁11V=が不
能とな−5た際にこれにかわって炉頂圧制御を行う非常
用としである丸め、下流側をサイレンサーSを介して前
記ガスホル〆−OHK連通接続せしめである。
The seventh valve 8V1 is used for emergency purposes to control the furnace top pressure in place of the steady state control valve 11V when it is disabled. -OHK communication connection is required.

前記2次ベンチ募り−ヌタッパーxvsハ、#Ig図印
1(ロ)に詳細に示す如く、容積1100m’  0本
体1の上部中央部から貫通し、本体10内部中心線上に
位置せしめたペンt&曽−管2と、同ペンテ1リニ管8
0下端開口側から本体上部のIIIIK設けた排出管3
と0間0fJL流路横断1i(85sすに二層0ツシヒ
リング製のイヌトセノ量レータ−4m、4に+と、この
蜜ヌトセパレーター4m、4bO下流側即ち、上記排出
管3@の流路横断面(90−)に配設した間接加熱器5
と、本体底部の會塵水収容郁1&下端に設けた含塵水排
出用調節弁6とから構成しである。
As shown in detail in Figure 1 (B) of the above-mentioned secondary bench recruitment - Nutapper xvs C, a pen T & Zeng with a volume of 1100 m' 0 penetrates from the upper center of the main body 1 and is positioned on the center line inside the main body 10. -Tube 2 and Pente 1 Lini tube 8
0 Exhaust pipe 3 installed at the top of the main body from the lower end opening side
and 0 0fJL flow path cross section 1i (85s two-layer 0 Tschichring made dog tosenolator -4m, 4 +, this honey nut separator 4m, 4bO downstream side, that is, the flow path cross section of the above-mentioned discharge pipe 3@) Indirect heater 5 installed at (90-)
It consists of a dust water storage valve 1 at the bottom of the main body and a dust water discharge control valve 6 provided at the lower end.

前記間接加熱器5祉、外周に放熱用フィン5&を多数突
設した多数本の金属製チー−ブ(内径2s−1外径34
■)5bを平面的に見て矩形状又側面的に見て7段配設
しく各段占有面積50m”)これら各チ纂−ゾ01側を
第3図に示す如く、分配供給ヘッダーS・の周壁に連通
接続し、他側管集会排出ヘッダー5bの周壁に連通接続
し、該分配供給ヘッダー5・を供給本管SCに連通接続
し、又諌集合排出ヘッダーSaを排出本管5DK連通接
続したものである。
The indirect heater 5 has a large number of metal tubes (inner diameter 2s-1 outer diameter 34mm
(2) 5b has a rectangular shape when viewed from above, and 7 stages are arranged when viewed from the side, and each stage occupies an area of 50 m. The distribution supply header 5 is connected in communication with the peripheral wall of the other side pipe collection discharge header 5b, the distribution supply header 5 is connected in communication with the supply main pipe SC, and the joint collection discharge header Sa is connected in communication with the discharge main pipe 5DK. This is what I did.

図中6m 、6bは峡矩形状加熱器5配設の流路横断面
における空間部に配設した盲板である。
In the figure, 6m and 6b are blind plates arranged in the space in the cross section of the channel in which the rectangular heater 5 is arranged.

前記供給本管jlICFi、流量調節弁5・を介設し、
高炉々体冷却装置等の既設の高温水発生源11fK連過
接続し、goco高温水が供給される。流量調節“弁5
・は諌排出管3内に軟は九ガメ温跋検出器5gからo、
fヌ温度検出値i&と予しめ設定しである目標温度値T
・と比較しそ011!に応じて、開度指令信号Coを出
力する制御@shによって該高温水供給量を調節制御す
る。
The supply main pipe jlICFi and a flow rate control valve 5 are interposed,
Goco high-temperature water is supplied by continuous connection to an existing high-temperature water generation source 11fK such as a blast furnace body cooling system. Flow rate adjustment valve 5
・In the exhaust pipe 3, there is a nine-game temperature detector 5g to o,
f Nu temperature detection value i & and preset target temperature value T
・Compare with Shiso011! Accordingly, the high temperature water supply amount is adjusted and controlled by the control @sh that outputs the opening command signal Co.

今前記1次ペンチ纂す−ヌIラバーIVIを出良60万
Nus”/ Hr % 60 CL 1 ”e/−の高
炉ガスを上記構成02次ペンチ番リーヌ?ツノ者−2v
8に導入したところ、電ヌトーkAレーター4bO出側
の高炉ffi性状は、1.6 h/ex”、40C随伴
建メト量011 /N11l”であ〉、間接加熱器5の
出伺O高FガJ”性状は、1.68Kr/am”  、
l 0℃ であシ、極めて小さい圧損量で多量O高炉t
ヌを所望温度に加熱昇温し且つ、次Oター♂ン〒l?に
安定供給することができ九。
Now, assemble the primary pliers - Nu I rubber IVI with the blast furnace gas of 600,000 Nus"/Hr% 60 CL 1"e/- and the secondary pliers with the above composition? Horned person-2v
8, the blast furnace ffi properties on the outlet side of the electric heater 4bO were 1.6 h/ex", the amount of 40C associated metal methane was 011/N11l", and the outlet O height of the indirect heater 5 was Ga J” property is 1.68Kr/am”,
l 0℃, large amount O blast furnace with extremely small pressure loss
Heat the nu to the desired temperature, and then turn O-turn 〒l? 9. Can provide stable supply.

これによって前記間接加熱lI5を設は危かり良2次ペ
ンチェリーヌ!ラバー使用時Ofj O00kWHr 
   +に比し、タービンTRTOji電量は1400
kWHr 。
As a result, the above-mentioned indirect heating lI5 can be set up in a dangerous manner. Ofj when using rubber O00kWHr
Compared to +, the amount of electricity of the turbine TRTOji is 1400
KWHr.

400 kWI(r増となル企業メリット紘多大′&4
0となる。
400 KWI
It becomes 0.

尚本例において、間接加熱器としてフィン付金属チュー
ブを用いたがこれに限ることなくフィンのない単なるチ
^−ブ等その他適宜な形状のチ為−)を用いるとよい。
In this example, a metal tube with fins is used as the indirect heater, but the present invention is not limited to this, and it is preferable to use a simple tube without fins or any other suitable shape.

又Zヌトセノ量レータ−として充填式を用いたがこれも
本例に限ることなく遠心分離型のミヌトセノ母レータ等
その他ミスト分離効率の高い適宜なミヌトセ/臂レータ
−を用いてよい。
Furthermore, although a filling type was used as the Z Nutoceno meter, this is not limited to this example, and any other appropriate Minutoceno/Archive rater having high mist separation efficiency, such as a centrifugal type Minutoceno mother generator, may be used.

尚、バッグフィルター又祉サンドフィルターを用いたと
きにはきヌトセノ臂レータ−を省略することができる。
Incidentally, when a bag filter or a sand filter is used, the armature generator can be omitted.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本発明の1実施例を示す全体側面説明図、絽2
図は、第1図側翼部の詳細側断面説明図であ)、第3図
は、第2図の矢視A−ムからの横断面図である。 Bv:高炉 D@C:ダストキャッチャー VB2 : 1次ペンチ凰す−ヌク2パーVli!、 
: 2次ペンチエリ−ヌクラバーTRT’ :タービン 4m、4b : ミヌトセノやレータ−5:間接加熱器 第2園 U 第3図
FIG. 1 is an overall side explanatory view showing one embodiment of the present invention.
The figure is a detailed side sectional explanatory view of the side wing portion in FIG. 1), and FIG. 3 is a cross-sectional view taken from arrow A--m in FIG. Bv: Blast Furnace D@C: Dust Catcher VB2: 1st Pliers - Nuku 2 Par Vli! ,
:Secondary Pentier Nuclever TRT' :Turbine 4m, 4b :Minutosenoya Rater 5:Indirect Heater 2nd Garden U Fig. 3

Claims (1)

【特許請求の範囲】 高炉ガスをガス清浄装置列を介して導出する管路に炉頂
圧タービンを接続して該タービンによシ該高炉fスの有
する圧力エネルギーを回収する装置にお−て、 前記ex情浄装置列に加熱器を配設せしめたことを特徴
とすゐ高炉!メエネルギー回収装置。
[Scope of Claim] A device for connecting a furnace top pressure turbine to a conduit that leads blast furnace gas through a gas purifying device array, and recovering pressure energy possessed by the blast furnace gas by the turbine. , A blast furnace characterized in that a heater is disposed in the above-mentioned EX air conditioner row! Energy recovery device.
JP56118936A 1981-07-29 1981-07-29 Device for recovering energy of blast-furnace gas Pending JPS5820928A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP56118936A JPS5820928A (en) 1981-07-29 1981-07-29 Device for recovering energy of blast-furnace gas

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP56118936A JPS5820928A (en) 1981-07-29 1981-07-29 Device for recovering energy of blast-furnace gas

Publications (1)

Publication Number Publication Date
JPS5820928A true JPS5820928A (en) 1983-02-07

Family

ID=14748887

Family Applications (1)

Application Number Title Priority Date Filing Date
JP56118936A Pending JPS5820928A (en) 1981-07-29 1981-07-29 Device for recovering energy of blast-furnace gas

Country Status (1)

Country Link
JP (1) JPS5820928A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0711544A2 (en) 1994-10-18 1996-05-15 Kao Corporation Dentifrice composition

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0711544A2 (en) 1994-10-18 1996-05-15 Kao Corporation Dentifrice composition

Similar Documents

Publication Publication Date Title
CN112435765B (en) High-temperature gas cooled reactor steam generator small-flow cooling system and control method
CN202902316U (en) Smoke water cooling dust collecting device
US4738224A (en) Waste heat steam generator
JPS5820928A (en) Device for recovering energy of blast-furnace gas
CN213807869U (en) Gas turbine air inlet double-loop cooling system utilizing refrigerating capacity allowance of refrigerating station
CN205679106U (en) A kind of phase-change thermal energy recovery system
CN207865355U (en) A kind of thermoelectricity station-service waste-heat recovery device
CN216935092U (en) Dust-removing heat exchanger
CN206257695U (en) Steam type airheater
CN205295383U (en) Converter low temperature section residual heat from flue gas system
CN213362526U (en) Waste heat recovery recycles device for thermal power plant
CN206069361U (en) Hydrogen cooled generator group hydrogen cleaning purifying plant
CN111306526B (en) Drainage main pipe system recycling and discharging device of auxiliary system of coal-fired steam drum boiler
CN211291105U (en) Zinc oxide smoke and dust heat utilizes device and multistage collection device
CN113339770A (en) Intensive energy-saving sulfur trioxide gas cooling system for sulfonation process and cooling method thereof
CN207294699U (en) Cold process system between a kind of novel powdered coal temperature gasification and high dedusting
CN202869322U (en) Chimney with heat energy recovery device
CN205988967U (en) A kind of cold bed waste-heat recovery device
CN205300366U (en) Low -level (stack -gas) economizer of convenient maintenance
CN206488664U (en) Flue gas heat-exchange unit
CN105318738A (en) Metallurgical furnace waste heat utilizing device
CN206419968U (en) A kind of station boiler low-temperature flue gas heat recovering device
CN217041926U (en) Carbon dioxide capture device
CN105087079B (en) A kind of gasification furnace power failure self-protecting device and method
CN220829123U (en) Heat exchanger with dust removal function