JPS6218879Y2 - - Google Patents

Info

Publication number
JPS6218879Y2
JPS6218879Y2 JP1981175386U JP17538681U JPS6218879Y2 JP S6218879 Y2 JPS6218879 Y2 JP S6218879Y2 JP 1981175386 U JP1981175386 U JP 1981175386U JP 17538681 U JP17538681 U JP 17538681U JP S6218879 Y2 JPS6218879 Y2 JP S6218879Y2
Authority
JP
Japan
Prior art keywords
steel grains
heat
heat exchanger
steel
passage
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
Application number
JP1981175386U
Other languages
Japanese (ja)
Other versions
JPS5883698U (en
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 filed Critical
Priority to JP17538681U priority Critical patent/JPS5883698U/en
Publication of JPS5883698U publication Critical patent/JPS5883698U/en
Application granted granted Critical
Publication of JPS6218879Y2 publication Critical patent/JPS6218879Y2/ja
Granted legal-status Critical Current

Links

Description

【考案の詳細な説明】 [産業上の利用分野] この考案は排ガス処理として利用される低温ガ
スと高温ガスとの熱交換、又は化学プラントにお
ける液体とガスとの熱交換の手段となるヒートパ
イプを有する熱交換器に係り、特に鋼粒をヒート
パイプにシヨツト又は降り注ぐようにさせ効果的
にフインの清掃を行うことができる熱交換器に関
する。
[Detailed description of the invention] [Field of industrial application] This invention is a heat pipe that is used as a means of heat exchange between low temperature gas and high temperature gas used for exhaust gas treatment, or heat exchange between liquid and gas in chemical plants. The present invention relates to a heat exchanger having a heat pipe, and more particularly to a heat exchanger that allows steel grains to be shot or poured onto a heat pipe to effectively clean the fins.

[従来の技術] 通常、発電所の事業用ボイラ、製鉄所、自家発
ボイラ、その他の燃焼装置に湿式排煙脱硫装置が
設置されているが、この装置からの排ガスは、水
分飽和のため、拡散が悪く、煙突の腐食や白煙の
発生となつている。そのためガス−ガス間接熱交
換器を採用して上記湿式排煙脱硫装置の出口排ガ
スを再加熱することは行われているが、この場合
の熱交換器として、あるいはその他排ガスの熱交
換器として、ヒートパイプ、特にフイン付ヒート
パイプを使用することが提案され実用に供されて
いる。熱交換器にフイン付ヒートパイプを用いた
場合に問題となるのは、排ガス中のダストやガス
状の物質或いはミスト等がフインに付着し伝熱効
果を損うと共にこれらが成長してフインの間隙部
が目詰りを起し、使用できなくなることである。
[Prior Art] Wet flue gas desulfurization equipment is usually installed in commercial boilers of power plants, steel mills, private boilers, and other combustion equipment, but the exhaust gas from this equipment is saturated with water, so Due to poor diffusion, chimneys are corroded and white smoke is produced. Therefore, a gas-gas indirect heat exchanger is used to reheat the exhaust gas at the outlet of the wet flue gas desulfurization equipment, but as a heat exchanger in this case or as a heat exchanger for other exhaust gases, The use of heat pipes, particularly heat pipes with fins, has been proposed and put into practical use. When a heat pipe with fins is used in a heat exchanger, the problem is that dust, gaseous substances, mist, etc. in the exhaust gas adhere to the fins, impairing the heat transfer effect, and growing. The gap becomes clogged and becomes unusable.

従来、これを防止すべくスートブロアを設け、
そのノズル1を第1図に示すように熱交換室に引
き込むとともに複数のフイン付ヒートパイプ2に
臨ませるべく複数個配設し、これより高圧蒸気又
は圧縮空気を噴射させフインに付着した排ガスの
ダスト、ミスト等の汚れを除去している。
Conventionally, a soot blower was installed to prevent this.
As shown in Fig. 1, the nozzle 1 is drawn into the heat exchange chamber, and a plurality of the nozzles are arranged so as to face a plurality of heat pipes 2 with fins. Removes dirt such as dust and mist.

[考案が解決しようとする問題点] しかしながら、この従来の方法は次のような欠
点があつた。
[Problems to be solved by the invention] However, this conventional method has the following drawbacks.

高圧蒸気や圧縮空気を多量に必要とするため
動力費が嵩む。
Power costs are high because large amounts of high-pressure steam and compressed air are required.

ノズルと対象物との距離が大きくなる程清掃
効果が悪い。
The greater the distance between the nozzle and the object, the worse the cleaning effect.

特に伝熱面であるフインをより多量に設けた
フイン付ヒートパイプは清掃効果が悪く目詰り
を防止できないので定期的な水洗浄も必要にな
る。
In particular, finned heat pipes with a larger number of fins, which serve as heat transfer surfaces, have a poor cleaning effect and cannot prevent clogging, so periodic cleaning with water is required.

かかる欠点を解決する方法として流体に代えて
鋼粒等の固体を吹きつける方法が考えられるが、
大形の熱交換器になつた場合、フイン付ヒートパ
イプ全面を一度に清掃しようとすると大量の鋼粒
が必要となり、又大量の投入又はシヨツトが一時
にフイン付ヒートパイプに当るとフイン付ヒート
パイプの損耗が起ることが予期される。
One possible way to solve this problem is to spray solids such as steel particles instead of fluid.
In the case of a large heat exchanger, if you try to clean the entire surface of the finned heat pipe at once, a large amount of steel particles will be required, and if a large amount of input or shot hits the finned heat pipe at once, the finned heat pipe will It is expected that pipe wear will occur.

そこで、本考案者等は鋼粒による清掃手段を採
用した場合の上記問題点を有効に解決するととも
に上記従来の欠点を解消すべく本考案を創案する
にいたつたものである。
Therefore, the inventors of the present invention have devised the present invention in order to effectively solve the above-mentioned problems when a cleaning means using steel particles is adopted, and also to eliminate the above-mentioned conventional drawbacks.

従つて、本考案の目的とするところは、少量の
鋼粒群をヒートパイプに部分的に当てるようにさ
せて、ヒートパイプを傷つけることなく付着物を
確実に除去でき、しかも鋼粒の投入に要する動力
を低減することができる熱交換器を提供すること
にある。
Therefore, the purpose of the present invention is to allow a small group of steel grains to partially hit the heat pipe so that the deposits can be reliably removed without damaging the heat pipe, and at the same time, it is possible to remove the deposits without damaging the heat pipe. An object of the present invention is to provide a heat exchanger that can reduce the power required.

[問題点を解決するための手段] 本考案の熱交換器は、熱交換室内にヒートパイ
プを配する排ガス利用の熱交換器を鋼粒の投入に
よつて清掃するようにした熱交換器において、排
ガス及びダストの通過を許容するが上記鋼粒の通
過を規制する通気性スクリーンによつて上記ヒー
トパイプが配分されるように熱交換室を小区画に
分割し、この小区画に鋼粒の投入口を各別に設
け、各投入口に小区画単位で鋼粒を投入すべく順
次開成して鋼粒の投入を制御する開閉バルブを介
設されてなるものである。
[Means for Solving the Problems] The heat exchanger of the present invention is a heat exchanger using exhaust gas in which a heat pipe is arranged in a heat exchange chamber, and the heat exchanger is cleaned by introducing steel particles. , the heat exchange chamber is divided into small compartments in which the heat pipes are distributed by a permeable screen that allows the passage of exhaust gas and dust but restricts the passage of the steel grains; Separate input ports are provided, and opening/closing valves are interposed to control the input of steel grains by sequentially opening each input port to input steel grains in small sections.

[作用] まず、最初の小区画に設けた投入口の開閉バル
ブが開かれると、この投入口から鋼粒が投入され
て最初の小区画内のヒートパイプが清掃される。
次いで、上記開閉バルブが閉じられるとともに、
2番目の小区画についてその投入口の開閉バルブ
が開かれて鋼粒が投入され、清掃される。このよ
うにして順次個別的に各小区画内のヒートパイプ
が清掃されていく。
[Operation] First, when the opening/closing valve of the input port provided in the first small section is opened, steel grains are introduced from the input port to clean the heat pipe in the first small section.
Next, the on-off valve is closed, and
The opening/closing valve of the input port of the second sub-section is opened, and the steel grains are input and cleaned. In this way, the heat pipes in each subdivision are sequentially and individually cleaned.

熱交換室は通気性スクリーンによつて分割され
ているため、ある小区画に投入された鋼粒は他の
小区画内に入り込むことがなく、したがつて少い
量の鋼粒で当該小区画内のヒートパイプに隈無く
行き亙る。
Since the heat exchange chamber is divided by a ventilation screen, the steel grains introduced into one compartment will not enter the other compartments, and therefore a small amount of steel grains will be used to fill the corresponding compartment. It goes all over the heat pipe inside.

[実施例] 以下、本考案に係る好適一実施例を添付図面に
従つて説明する。
[Embodiment] A preferred embodiment of the present invention will be described below with reference to the accompanying drawings.

第2図において、3は高温側熱交換器及び低温
側熱交換器から成るガス−ガス間接熱交換器4を
形成する一方の熱交換器である。この熱交換器3
は、その熱交換室3a内に多段に形成し、かつ隣
接の熱交換器5にも水平方向に延出しているフイ
ン付ヒートパイプ6群が配され、そのフインが伝
熱面となつて一方の熱交換器を通過する流体の熱
を他方の熱交換器を通過する流体に伝熱するよう
に構成されている。7は通気性スクリーンであ
り、フイン付ヒートパイプ6群の長手方向に沿つ
て所定の間隔を隔てて、かつ重量方向に沿つて延
出され、これにより熱交換器3aを小区画に分割
するとともに、その分割された小区画を通路8と
なしている。上記通気性スクリーン7は排ガス及
びダストは通過するが後述する鋼粒は通過できな
い網目状のものが使用される。
In FIG. 2, reference numeral 3 designates one heat exchanger forming a gas-gas indirect heat exchanger 4 consisting of a high temperature side heat exchanger and a low temperature side heat exchanger. This heat exchanger 3
In this case, six groups of heat pipes with fins are arranged in multiple stages in the heat exchange chamber 3a and extend horizontally to the adjacent heat exchanger 5, and the fins serve as a heat transfer surface. The heat exchanger is configured to transfer heat from a fluid passing through one heat exchanger to a fluid passing through another heat exchanger. Reference numeral 7 denotes a ventilation screen, which extends along the longitudinal direction of the 6 groups of finned heat pipes at predetermined intervals and along the weight direction, thereby dividing the heat exchanger 3a into small sections. , the divided small sections are used as passages 8. The permeable screen 7 has a mesh shape that allows exhaust gas and dust to pass through, but prevents steel grains, which will be described later, from passing through.

各通路8の上方には、これに連通する鋼粒の投
入口9を各別に設けるとともに、中間に開閉バル
ブ10を介してそれらの基端を単一のホツパ11
に連結している。開閉バルブ10は全部が同時に
開くのではなく、1つのみがタイムスケジユール
により順次開いていくように制御され、開成した
開閉バルブ10に連通している通路8のみにホツ
パ11から所定量の鋼粒が投入されるように構成
されている。
Above each passage 8, an input port 9 for steel grains is provided which communicates with the passage, and the base ends are connected to a single hopper 11 via an opening/closing valve 10 in the middle.
is connected to. The on-off valves 10 are not all opened at the same time, but only one is controlled to open sequentially according to a time schedule, and a predetermined amount of steel grains is supplied from the hopper 11 only to the passage 8 communicating with the opened on-off valve 10. is configured to be input.

第3図に示すように、鋼粒12は、自重で落下
しうる重さを有するとともに、フイン付ヒートパ
イプ6のフインの間隙部を通過し得る粒径を有す
る。
As shown in FIG. 3, the steel grains 12 are heavy enough to fall under their own weight, and have a grain size that allows them to pass through the gaps between the fins of the finned heat pipe 6.

熱交換室3aの外部には、熱交換室の底部口と
上記ホツパ11とを連結する帰還路13が形成さ
れている。この帰還路13は排出物回収分離系1
4と垂直コンベア15と搬送系16とから成り、
排出物回収分離系14で通路8内を流下し底部口
に落下集積した鋼粒12を含む排出物を回収する
とともにこれより鋼粒のみを分離し、この鋼粒を
垂直コンベア15で持ち上げ、搬送系16を介し
て再びホツパ11に戻すように構成されている。
A return path 13 connecting the bottom opening of the heat exchange chamber and the hopper 11 is formed outside the heat exchange chamber 3a. This return path 13 is the exhaust collection and separation system 1
4, a vertical conveyor 15, and a conveyance system 16,
The waste collection and separation system 14 collects the waste containing the steel grains 12 that have flowed through the passage 8 and fallen and accumulated at the bottom opening, and from this, only the steel grains are separated, and the steel grains are lifted and conveyed by the vertical conveyor 15. It is configured to return to the hopper 11 via the system 16.

以上の構成よりなる本熱交換器の作用について
述べる。
The operation of the present heat exchanger having the above configuration will be described.

ホツパ11には、1つの通路内を清掃するに足
る少量の鋼粒12が蓄えられ、まず1番目の開閉
弁10が開成される。この開成により鋼粒12は
投入口9の傾斜によつて転がり落ちその開口より
これに連通した通路8内に流下する。この流下の
際、鋼粒12は通路8と交叉するフイン付ヒート
パイプ6のフイン等の外周面に衝突又は接触しこ
れに付着するダストを掻き落す。また熱交換室3
aの内壁面のダストも同様に除去する。通路8が
通気性スクリーン7により仕切られているので他
の通路8に入れ込まず、鋼粒12はその自重によ
り上から下まで均一に流れ、多段に配されている
フイン付ヒートパイプ6に隈無く行き届くことに
なる。従つて、この通路8内のダスト除去を完全
に行い得る。
A small amount of steel grains 12 sufficient to clean the inside of one passage is stored in the hopper 11, and the first on-off valve 10 is opened. As a result of this opening, the steel grains 12 roll down due to the slope of the input port 9 and flow down through the opening into the passage 8 communicating therewith. During this flow, the steel grains 12 collide with or come into contact with the outer circumferential surface of the fins, etc. of the finned heat pipe 6 that intersects with the passage 8, and scrape off the dust adhering thereto. Also heat exchange room 3
Dust on the inner wall surface of a is also removed in the same way. Since the passage 8 is partitioned by a breathable screen 7, the steel grains 12 do not enter other passages 8, and the steel grains 12 flow uniformly from top to bottom due to their own weight. It will reach you without any trouble. Therefore, the dust inside this passage 8 can be completely removed.

次に、回収分離させた少量の鋼粒12は再び帰
還路13を経てホツパ11に戻され、そして、2
番目の開閉弁10を開成することによつて、今度
は次の通路内の清掃を行う。このように順次通路
8毎に清掃を行つていく。この具体的態様は、例
えば第4図に示すように、熱交換室3aを点線で
示す通気性スクリーン7で縦方向に8個の小区画
A〜Hに分割し、これら小区画に対し所定のタイ
ムスケジユールにより逐次鋼粒を投入していき、
この鋼粒は1区間分のものを繰り返し使用してい
くことが考えられる。
Next, the small amount of recovered and separated steel grains 12 is returned to the hopper 11 via the return path 13, and then
By opening the second on-off valve 10, the next passage is cleaned. In this way, cleaning is performed sequentially for each passage 8. In this specific embodiment, for example, as shown in FIG. 4, the heat exchange chamber 3a is vertically divided into eight small sections A to H by a ventilation screen 7 indicated by dotted lines, and predetermined Steel grains are added sequentially according to the time schedule,
It is conceivable that the steel grains for one section are repeatedly used.

一方、熱交換器本来の機能が発揮されるために
は排ガスが熱交換室8内を均一に通過していくこ
とが要求されるが、上記通気性スクリーン7は排
ガスaの通過には全く支承がなく、従つて第3
図、又は第4図に示す如く排ガスの流入方向に対
してスクリーン7を垂直に垂下することも可能で
ある。
On the other hand, in order for the heat exchanger to perform its original function, it is required that the exhaust gas uniformly pass through the heat exchange chamber 8, but the ventilation screen 7 does not support the passage of the exhaust gas a at all. Therefore, the third
It is also possible to hang the screen 7 perpendicularly to the inflow direction of the exhaust gas as shown in FIG.

従つて、一度に熱交換室3aの全断面に大量に
鋼粒12を投入落下させるものと異なり、区画さ
れた1つの通路のみに投入させるものであるか
ら、一度に投入量は少量で済み、しかもこの量は
通路内のフイン付ヒートパイプ6を清掃するには
充分な量であるから完全な清掃をすることができ
る。
Therefore, unlike the method in which a large amount of steel grains 12 is introduced and dropped over the entire cross section of the heat exchange chamber 3a at once, the steel grains 12 are introduced only into one partitioned passage, so only a small amount can be introduced at one time. Moreover, since this amount is sufficient to clean the finned heat pipe 6 in the passage, complete cleaning can be achieved.

また、少量の鋼粒がフイン付ヒートパイプ6に
当るだけであり、過度の衝撃力がフイン付ヒート
パイプに加わるのを避けることができるから、フ
イン付ヒートパイプの寿命を延ばすことが可能で
ある。
In addition, since only a small amount of steel grains hit the finned heat pipe 6, it is possible to avoid applying excessive impact force to the finned heat pipe, so it is possible to extend the life of the finned heat pipe. .

又、タイムスケジユールにより一度に投入する
鋼粒12の量は一通路8分のみとすることによ
り、その回収に際してもその少量分の鋼粒運搬エ
ネルギーで足るから、動力費の節減を図ることが
できる。
In addition, by setting the amount of steel grains 12 to be introduced at one time for only 8 minutes per passage due to the time schedule, when recovering the steel grains, the energy for transporting the steel grains is sufficient for that small amount, so it is possible to reduce power costs. .

尚、上記実施例では鋼粒12を熱交換室3aの
上方から投入する場合を示したが、シヨツト粒と
して側面から噴射させるようしても同様な作用効
果を奏し得る。
In the above embodiment, the steel grains 12 are injected from above into the heat exchange chamber 3a, but the same effect can be obtained even if the steel grains 12 are injected from the side as shot grains.

[考案の効果] 以上、要するに本考案によれば次のような優れ
た効果を発揮する。
[Effects of the invention] In summary, the present invention provides the following excellent effects.

(1) 少量の鋼粒で完全な熱交換器のダスト除去を
行い得るので効率が上がり熱交換器を小形化で
きる一方、大形の熱交換器の清掃にも対処でき
る。
(1) It is possible to completely remove dust from a heat exchanger with a small amount of steel particles, increasing efficiency and making the heat exchanger more compact, while also making it possible to clean large heat exchangers.

(2) 一時に大量の鋼粒がヒートパイプに当たらな
いのでヒートパイプの損耗を少くすることがで
き寿命を延ばすることが可能である。
(2) Since a large amount of steel grains do not hit the heat pipe at once, it is possible to reduce wear and tear on the heat pipe and extend its life.

(3) 一度に使用する鋼粒量が少量なのでこれらを
運搬投入する動力エネルギーを低減することが
でき省資源化、省エネルギー化を図ることがで
きる。
(3) Since the amount of steel grains used at one time is small, the power energy needed to transport and input them can be reduced, resulting in resource and energy savings.

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

第1図は従来の熱交換器の清掃方法を説明する
概略図、第2図は本考案に係る熱交換器の好適一
実施例を示す概略正面図、第3図は同上一通路を
示す要部側断面図、第4図は同上変形例を示す概
略平面図である。 図中、3は熱交換器、3aは熱交換室、6はヒ
ートパイプの例を示すフイン付ヒートパイプ、7
は通気性スクリーン、8は通路、9は鋼粒の投入
口、10は開閉バルブ、11はホツパ、12は鋼
粒、13は帰還路、aは排ガスである。
Fig. 1 is a schematic diagram illustrating a conventional method for cleaning a heat exchanger, Fig. 2 is a schematic front view showing a preferred embodiment of the heat exchanger according to the present invention, and Fig. 3 is a schematic diagram showing one passage of the same. FIG. 4 is a schematic plan view showing a modification of the same as the above. In the figure, 3 is a heat exchanger, 3a is a heat exchange chamber, 6 is a heat pipe with fins showing an example of a heat pipe, and 7 is a heat exchanger.
8 is a ventilation screen, 8 is a passage, 9 is an inlet for steel grains, 10 is an on-off valve, 11 is a hopper, 12 is a steel grain, 13 is a return path, and a is an exhaust gas.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 熱交換室内にヒートパイプを配する排ガス利用
の熱交換器を鋼粒の投入によつて清掃するように
した熱交換器において、排ガス及びダストの通過
を許容するが上記鋼粒の通過を規制する通気性ス
クリーンによつて上記ヒートパイプが配分される
ように上記熱交換室を小区画に分割し、この小区
画に鋼粒の投入口を各別に設け、各投入口に小区
画単位で鋼粒を投入すべく順次開成して鋼粒の投
入を制御する開閉バルブを介設したことを特徴と
する熱交換器。
In a heat exchanger that uses exhaust gas and has a heat pipe arranged in the heat exchange chamber and is cleaned by introducing steel grains, the passage of exhaust gas and dust is allowed, but the passage of the steel grains is restricted. The heat exchange chamber is divided into small sections so that the heat pipes are distributed by a ventilation screen, each of which is provided with an inlet for steel grains, and each inlet is injected with steel grains in small sections. 1. A heat exchanger characterized in that an opening/closing valve is provided to control the injection of steel grains by sequentially opening and closing the valves to control the injection of steel grains.
JP17538681U 1981-11-27 1981-11-27 Heat exchanger Granted JPS5883698U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP17538681U JPS5883698U (en) 1981-11-27 1981-11-27 Heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP17538681U JPS5883698U (en) 1981-11-27 1981-11-27 Heat exchanger

Publications (2)

Publication Number Publication Date
JPS5883698U JPS5883698U (en) 1983-06-06
JPS6218879Y2 true JPS6218879Y2 (en) 1987-05-14

Family

ID=29967731

Family Applications (1)

Application Number Title Priority Date Filing Date
JP17538681U Granted JPS5883698U (en) 1981-11-27 1981-11-27 Heat exchanger

Country Status (1)

Country Link
JP (1) JPS5883698U (en)

Families Citing this family (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
LT3827815T (en) 2008-09-10 2023-10-10 Ptc Therapeutics, Inc. Treatment of pervasive developmental disorders with redox-active therapeutics
CA2766100C (en) 2009-06-29 2018-05-22 Incyte Corporation Pyrimidinones as pi3k inhibitors
WO2011075643A1 (en) 2009-12-18 2011-06-23 Incyte Corporation Substituted heteroaryl fused derivatives as pi3k inhibitors
EP2558463A1 (en) 2010-04-14 2013-02-20 Incyte Corporation Fused derivatives as i3 inhibitors
TW201249844A (en) 2010-12-20 2012-12-16 Incyte Corp N-(1-(substituted-phenyl)ethyl)-9H-purin-6-amines as PI3K inhibitors
WO2012125629A1 (en) 2011-03-14 2012-09-20 Incyte Corporation Substituted diamino-pyrimidine and diamino-pyridine derivatives as pi3k inhibitors
WO2012135009A1 (en) 2011-03-25 2012-10-04 Incyte Corporation Pyrimidine-4,6-diamine derivatives as pi3k inhibitors
IL299533A (en) 2011-09-02 2023-02-01 Incyte Holdings Corp Heterocyclylamines as pi3k inhibitors
AR090548A1 (en) 2012-04-02 2014-11-19 Incyte Corp BICYCLIC AZAHETEROCICLOBENCILAMINS AS PI3K INHIBITORS
JP5840063B2 (en) * 2012-04-13 2016-01-06 新日鉄住金エンジニアリング株式会社 Shot ball spraying device, shot ball spraying method and boiler for shot cleaning

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5432864A (en) * 1977-08-16 1979-03-10 Mitsui Eng & Shipbuild Co Ltd Method of recovering heat and its device

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS56112491U (en) * 1980-01-28 1981-08-31

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5432864A (en) * 1977-08-16 1979-03-10 Mitsui Eng & Shipbuild Co Ltd Method of recovering heat and its device

Also Published As

Publication number Publication date
JPS5883698U (en) 1983-06-06

Similar Documents

Publication Publication Date Title
US4464183A (en) Heat recovery process in coal gasification
JPS6218879Y2 (en)
US6511637B2 (en) Air pollution control assembly and method
CN106440833A (en) Wet-process dust removal, desulfurization and denitrification system and method for flue gas
US4986966A (en) Retrofit flue gas scrubber system
CN207179706U (en) A kind of emission-control equipment of the steam-cured boiler of pile tube
CN207591515U (en) Suitable for the flue gas processing device of civil heating stove
KR20200020348A (en) Wet ane cooling type gas cleaning apparatus
JP2010264401A (en) Flue gas denitration apparatus
CN107560494B (en) A kind of On Line Foul Removing Technology device
CN206980393U (en) A kind of filler spray column of improved multistage dedusting
JPS5891A (en) Heat exchanger
CN108518701A (en) A kind of cold coacervation device of phase transformation
US4655802A (en) Heat exchanger for a furnace using heat of exhaust gas
CN210786644U (en) Boiler spraying dust-settling device
JPS5892799A (en) Cleaning method of heat-exchanger and device thereof
CN217540791U (en) Combustion smoke dust removal system
CN212253699U (en) Hot gas recycling system of ceramic kiln
JPH06126114A (en) Chemical feeding apparatus in precoat-type bag filter apparatus
JPS6314221Y2 (en)
KR102075062B1 (en) Waste heat recovery boiler with separating type lower drum for easy dust removal and easy water circulation
CN113294797B (en) High-efficient dust collector of boiler waste smoke
CN115854743B (en) Quenching and dedusting integrated equipment and soil remediation technology applying same
JP2521837Y2 (en) Pre-coated bag filter device
CN208990415U (en) Integral type second level cloth bag filter cartridge dust remover