JPH01189315A - Soot removing device for reforming gas - Google Patents

Soot removing device for reforming gas

Info

Publication number
JPH01189315A
JPH01189315A JP1406888A JP1406888A JPH01189315A JP H01189315 A JPH01189315 A JP H01189315A JP 1406888 A JP1406888 A JP 1406888A JP 1406888 A JP1406888 A JP 1406888A JP H01189315 A JPH01189315 A JP H01189315A
Authority
JP
Japan
Prior art keywords
gas
soot
cylindrical housing
housing
removal device
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
JP1406888A
Other languages
Japanese (ja)
Inventor
Isao Nagayanagi
永柳 勲
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.)
Aichi Steel Corp
Original Assignee
Aichi 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 Aichi Steel Corp filed Critical Aichi Steel Corp
Priority to JP1406888A priority Critical patent/JPH01189315A/en
Publication of JPH01189315A publication Critical patent/JPH01189315A/en
Pending legal-status Critical Current

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Abstract

PURPOSE:To effectively remove the soot in a reforming gas only by passing the reforming gas through vacant chambers by sectioning the inner space of a cylindrical housing into plural vacant chambers with partition means and forming clearances connecting neighboring chambers. CONSTITUTION:A gas flowing-in opening 15 and a gas flowing-out opening 16 are formed respectively in the lower part and in the upper part of the cylindrical housing 13 both ends of which are closed. The inner space between the gas flowing-in opening 15 and the gas flowing-out opening 16 in the cylindrical housing 13 is sectioned into plural vacant chambers by partition plates 20, and the clearances connecting neighboring chambers are formed. By this simple structure, the soot in the reforming gas is effectively removed only by flowing the reforming gas through this structure. Consequently, the construction cost is low and the device is allowed to be easily combined with an ordinary atmospheric heat treatment process, and the maintenance for the device is simple because the soot is removed without using a filter element.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は、鉄鋼の雰囲気熱処理に用いられる変成ガス中
のススを除去する装置に関するものである。
DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) The present invention relates to an apparatus for removing soot from a metamorphosed gas used in atmospheric heat treatment of steel.

(従来技術) 鉄鋼の光輝熱処理や浸炭処理に使われる変成ガスは、原
料がスに所定比率の空気を混合して変成炉に圧送し、こ
こで外熱されたレトルト中に充填されたニッケル触媒に
より変成され、ついで変成炉から処理炉へ導入される。
(Prior technology) Shift gas used in the bright heat treatment and carburizing treatment of steel is produced by mixing the raw material with air at a predetermined ratio and pumping it into the shift furnace, where it is heated externally and filled with a nickel catalyst filled in a retort. It is then transformed from the transformation furnace to the processing furnace.

処理炉内の雰囲気の温度、C0ff1、CO2量は熱電
対、ガス分析計により連続的に計測され、その測定値に
基づき、処理炉へ送り込む変成ガスの流量や、変成ガス
と混合させる中性ガス(N2)の流量を適宜調節し、処
理目的に応じた組成の変成ガスに自動i11整される。
The temperature, C0ff1, and CO2 amount of the atmosphere inside the processing furnace are continuously measured by thermocouples and gas analyzers, and based on the measured values, the flow rate of the metamorphic gas sent to the processing furnace and the neutral gas to be mixed with the metamorphic gas are determined. The flow rate of (N2) is adjusted appropriately, and the composition is automatically adjusted to a modified gas according to the processing purpose.

この変成ガスはN2、Co、Co2、N2、CH。This metamorphosed gas is N2, Co, Co2, N2, and CH.

等を組成成分として含むが、そのうちCOは^温では不
安定であり、分解してススを生成する。
Among these, CO is unstable at temperatures, and decomposes to produce soot.

変成ガスより遊離したススは、変成が大の流量を測定す
るため変成炉と処理炉を接続する管路中に配置した差圧
式流量計のオリアイスやノズル部分、あるいは流量調節
弁に付着し、変成ガス流量の制御精度を劣化させる原因
となるほか、処理炉の内壁、ファン、被処理物に付着し
てこれらに悪影響を与える。
Soot liberated from the metamorphic gas adheres to the oriice, nozzle part, or flow rate control valve of the differential pressure flow meter placed in the pipeline connecting the converting furnace and the processing furnace to measure the flow rate at which the metamorphic gas is generated. In addition to causing deterioration in the control accuracy of gas flow rate, it also adheres to the inner walls of the processing furnace, fans, and objects to be processed, and has an adverse effect on them.

そのため従来、変成ガス中のCOが分解してススが発生
するのを抑制すべく、変成直後、冷却器により変成ガス
をすみやかに冷却していた。
Therefore, conventionally, in order to suppress the generation of soot due to the decomposition of CO in the metamorphic gas, the metamorphic gas has been quickly cooled down by a cooler immediately after metamorphosis.

(発明が解決しようとする問題点) しかし、単に変成がスを冷却するだけでは満足すべき成
果が得られず、依然、ススが付着して流量計や調節弁に
狂いが生ずる等の問題があった。
(Problems to be solved by the invention) However, simply cooling the metamorphic soot does not produce satisfactory results, and there are still problems such as soot adhering to the flow meter and control valves. there were.

本発明はかかる問題点に鑑み、変成ガス中のススを効果
的に除去することのできるvc置を提供することを目的
とするものである。
SUMMARY OF THE INVENTION In view of these problems, it is an object of the present invention to provide a VC system that can effectively remove soot from metamorphic gas.

しかして、本発明者は上記問題点を解決するに際し、第
8図に示すように、面積式流量計aの70−)bの上や
、第9図に示すように、ガス冷却器Cのガス流入通路d
の直後の空室eなどに多量のススが堆積している事実に
着目し、この事実から変成ガスが狭い通路から広い空間
へ流入するとき、その境界部分において多量にススが分
離することを知得した0本発明はかかる知見に基づいて
案出されたものである。
Therefore, in order to solve the above problem, the inventors of the present invention solved the problem by placing a Gas inflow passage d
We focused on the fact that a large amount of soot was deposited in the empty space e immediately after the passage, and from this fact we learned that when metamorphosed gas flows from a narrow passage into a wide space, a large amount of soot separates at the boundary. The present invention was devised based on this knowledge.

(ILffffi、αを解決するための手段)上記目的
に沿う本発明の構成は、下部にガス流入口を、上部にガ
ス流出口を形成し、両層をrR塞した筒状ハウジングと
、この筒状ハウジングの、ガス流入口からガス流出口に
至る内部空間を複数の空室に区画する仕切手段とを備え
、 隣接する空室間を連通ずる周隙を形成したことを要旨と
する。
(Means for solving ILffffi, α) The structure of the present invention in accordance with the above object includes a cylindrical housing in which a gas inlet is formed in the lower part and a gas outlet is formed in the upper part, and both layers are closed by R. The gist of the present invention is to include a partitioning means for partitioning an internal space from a gas inlet to a gas outlet into a plurality of chambers, and to form a circumferential gap that communicates between adjacent chambers.

(作用) 上記構成によれば、下部ガス流入口から筒状ハウジング
内部に流入した変成ガスは仕切手段によって区画された
各空室を巡って上部流出口から流出する。変成ガスが空
室から隣接する空室へ間隙を通って流れ込む際、変成ガ
ス中のススが分離し、仕切手段上に堆積し、筒状ハウジ
ングの外部へ流出するときには変成ガス中のススの殆ど
が除去される。
(Function) According to the above configuration, the metamorphic gas that has flowed into the cylindrical housing from the lower gas inlet passes through each of the chambers partitioned by the partitioning means and flows out from the upper outlet. When the metamorphosed gas flows from a cavity to an adjacent cavity through the gap, the soot in the metamorphosed gas separates and accumulates on the partition means, and when it flows out of the cylindrical housing, most of the soot in the metamorphosed gas is removed. is removed.

(実施例) 以下に本発明の一実施例を図面に基づき説明する。第1
図は本発明の第1の実施例を示す一部破断斜視図、第2
図はそのa**面図、第3図は同じく上蓋を取り外した
状態の平面図である。
(Example) An example of the present invention will be described below based on the drawings. 1st
The figures are a partially cutaway perspective view showing the first embodiment of the present invention, and the second figure is a partially cutaway perspective view showing the first embodiment of the present invention.
The figure is an a** side view of the same, and FIG. 3 is a plan view of the same with the top cover removed.

11図ないし第3図において、10は本発明の実施例を
示すスス除去装置であり、上M11と下蓋12により上
下両端面が閉塞された中空円筒形のハウジング13を有
し、上M11と下蓋12はボルト14によりハウジング
13に締着されている。ハウジング13の底面付近には
ガス流入ロ15が、上面付近にはガス流入ロ145同じ
開口面積のガス流出ロ16が設けられている。またハウ
ジング13の外周にはハウジング13を縦に設置できる
ように足部17.17が取り付けられている。さらにハ
ウジング13の下部には空気抜きコック18が設けられ
ている。
11 to 3, reference numeral 10 denotes a soot removal device showing an embodiment of the present invention, which has a hollow cylindrical housing 13 whose upper and lower end surfaces are closed by an upper M11 and a lower lid 12. The lower cover 12 is fastened to the housing 13 with bolts 14. A gas inlet hole 15 is provided near the bottom surface of the housing 13, and a gas outlet hole 16 having the same opening area as the gas inlet hole 145 is provided near the top surface. Furthermore, foot portions 17.17 are attached to the outer periphery of the housing 13 so that the housing 13 can be installed vertically. Further, an air vent cock 18 is provided at the bottom of the housing 13.

ハウジング13の内部には仕切手段としで、同径の5枚
の円形仕切板20が水平に配設され、各円形仕切板20
はプレート21により適宜の間隔を設けて連結され、こ
れらの円形仕切板群20は上蓋11の裏面に垂設したプ
レート22により?)ウジング13内に吊り下げちりて
いる。
Inside the housing 13, five circular partition plates 20 having the same diameter are arranged horizontally as partition means, and each circular partition plate 20
are connected by plates 21 at appropriate intervals, and these circular partition plate groups 20 are connected by plates 22 vertically provided on the back surface of the upper lid 11. ) It is hanging inside Uzing 13 and is dusty.

各プレート21の長さは円形仕切板20の直径よりも若
干短く、それぞれ取付方向を異にして取り付けられてい
る。また円形仕切板20はノ1ウノング13の内径より
も小さい直径を有し、ノ1ウノング13の中心線に直交
するように、かつ中心をハウジング13の中心線から不
規則にずらして配設されている。
The length of each plate 21 is slightly shorter than the diameter of the circular partition plate 20, and each plate 21 is attached in a different direction. Further, the circular partition plate 20 has a diameter smaller than the inner diameter of the first opening 13, and is disposed so as to be perpendicular to the center line of the first opening 13 and with its center irregularly shifted from the center line of the housing 13. ing.

ハウジング13−の、ガス流入口15からガス流出口1
6に至る内部空間は、これら円形仕切板20により複数
の空室Rに区画され、隣接する空室同士は、ハウジング
13の内壁と各円形仕切板20の外周面の間に形成され
た間隙を介して連通されている。この各間隙の面積はガ
ス流入ロ15の開口面積とほぼ同じになるように円形仕
切板20の直径が設定されている。また円形仕切板20
の中心をハウジング13の中心線から不規則にずらして
配置したことにより、各Ill隙の幅は最も狭い部分と
最も広い部分が形成され、その間は連続的に変化し、隣
合う間隙の同@部分の位置が相対的にずれている。
From the gas inlet 15 to the gas outlet 1 of the housing 13-
6 is divided into a plurality of cavities R by these circular partition plates 20, and adjacent cavities are separated by a gap formed between the inner wall of the housing 13 and the outer peripheral surface of each circular partition plate 20. communicated through. The diameter of the circular partition plate 20 is set so that the area of each gap is approximately the same as the opening area of the gas inflow hole 15. In addition, the circular partition plate 20
By arranging the center of the housing 13 with its center irregularly shifted from the center line of the housing 13, the width of each Ill gap forms a narrowest part and a widest part, and the width between them changes continuously, and the width of the adjacent gap The positions of the parts are shifted relative to each other.

本実施例は以上の構成よりなり、次にその作用を説明す
る。
The present embodiment has the above configuration, and its operation will be explained next.

第4図は本実施例装置を組み入れた雰囲気調整工程の概
略説明図である。
FIG. 4 is a schematic explanatory diagram of an atmosphere adjustment process incorporating the apparatus of this embodiment.

第4図において、30は変成炉であり、耐熱性のレトル
ト31が装@されており、レトルト31内には耐熱材に
酸化ニッケルを浸み込ませた触媒32が充填され、バー
ナ33により外部から高温に加熱されている。流量形3
4により計測された原料ガスと、流量形35により計測
された空気はミキサ36により所定比率で混合され、が
ス混合ポンプ37で加圧されたのち、自動ガス調節弁3
8、逆火防止弁39を経て、変成炉30へ圧送され、レ
トルト31内のニッケル触媒32によって反応が促進さ
れ、変成ガスが生成される。こうして生成された変成ガ
スは、COが分解しでススが発生するのを抑制するため
、変成直後、ガス冷却器40により急冷される。
In FIG. 4, reference numeral 30 denotes a conversion furnace, which is equipped with a heat-resistant retort 31. The retort 31 is filled with a catalyst 32 made of a heat-resistant material impregnated with nickel oxide. is heated to a high temperature. Flow type 3
The raw material gas measured by 4 and the air measured by flow rate type 35 are mixed at a predetermined ratio by mixer 36, and after being pressurized by gas mixing pump 37, automatic gas control valve 3
8. Passing through the flashback prevention valve 39, the gas is fed under pressure to the shift furnace 30, and the reaction is promoted by the nickel catalyst 32 in the retort 31 to generate shift gas. The thus generated metamorphosed gas is rapidly cooled by a gas cooler 40 immediately after the metamorphosis in order to suppress the generation of soot due to decomposition of CO.

冷却された変成ガスはついで、上述したスス除去装置1
0へ導入される。
The cooled metamorphosed gas is then passed through the soot removal device 1 described above.
0 is introduced.

ガス流入口15からハウジング13内へ流入した変成ガ
スは、円形仕切板20で区画された下方の空室から上方
の空室へと、間隙を通って流れ、ガス流出口16からハ
ウジング13の外部へ流出する。空室に流れ込んだ変成
ガスは間隙を通って隣接する空室へ流入するが、隣合う
間隙の幅広部分の相対的な位置が互いにずらしてあり、
また各空室内には方向を異にしてプレート21が設けで
あるため、渦巻き状の流れとなって各空室を巡りガス流
出ロ16から流出する。そして、間隙を通過して空室に
流入する際、変J& ffスス中ススが分離して、円形
仕切板20上に堆積し、一部は底面12へ落下する。
The metamorphosed gas that has flowed into the housing 13 from the gas inlet 15 flows through the gap from the lower cavity divided by the circular partition plate 20 to the upper cavity, and then flows from the gas outlet 16 to the outside of the housing 13. leaks to. The metamorphosed gas that has flowed into the cavity flows into the adjacent cavity through the gap, but the relative positions of the wide parts of the adjacent gaps are shifted from each other.
Further, since the plates 21 are provided in each cavity in different directions, the gas flows out from the gas outlet hole 16 in a spiral flow around each cavity. Then, when passing through the gap and flowing into the empty room, the soot in the modified J&FF soot separates and accumulates on the circular partition plate 20, and a portion falls to the bottom surface 12.

ガス流出口16から流出した変成がスは流量調節弁41
、差圧式流量形42を通って図示略の処理炉へ導入され
るが、本実施例のスス除去装r!110により、変成〃
人中のススが殆ど除去されているので、流量調節弁41
や差圧式流量形42のオlj フイスやノズルに付着す
るススの量は極めて僅かとなる。
The metamorphic gas flowing out from the gas outlet 16 flows through the flow control valve 41.
, and is introduced into a processing furnace (not shown) through a differential pressure type flow type 42, but the soot removal equipment r! Transmutation by 110
Since most of the soot in the human body has been removed, the flow rate control valve 41
The amount of soot that adheres to the orifice and nozzle of the differential pressure type flow type 42 is extremely small.

変成ガスから分離しススは、変成がスの圧送を停止した
後、上蓋11をハウジング13から外し、仕切板20を
取り出して掃除する。掃除後、再び操業を開始するとき
には、空気抜きコック18を閏いてハウジング13中の
空気を排出する。
The soot separated from the converted gas is cleaned after the pumping of the converted gas is stopped, the upper cover 11 is removed from the housing 13, and the partition plate 20 is taken out and cleaned. After cleaning, when starting the operation again, the air in the housing 13 is discharged by using the air vent cock 18.

尚、本実施例では中空円筒形のハウジング13と円形の
仕切板20を例示したが、筒状ハウジングや仕切板の形
態はこれに限定されるものではなく、例えば、筒状ハウ
ジングを中空円錐体とすることも可能である。また隣接
する空室を連通する間隙も仕切板に直接、穿設してもよ
い。
In this embodiment, a hollow cylindrical housing 13 and a circular partition plate 20 are illustrated, but the shapes of the cylindrical housing and the partition plate are not limited to these. For example, the cylindrical housing may be replaced with a hollow cone. It is also possible to do this. Furthermore, gaps that communicate adjacent chambers may also be formed directly in the partition plate.

次に本発明の第2の実施例を説明する。第5図は第2実
施例を示す一部破断斜視図、第6図はその縦断断面図、
第7図は同じく上蓋を取り外した状態の平面図である。
Next, a second embodiment of the present invention will be described. FIG. 5 is a partially cutaway perspective view showing the second embodiment, FIG. 6 is a longitudinal sectional view thereof,
FIG. 7 is a plan view with the top cover removed.

第5図ないし第7図において、スス除去装置50は、上
1i51と漏斗状の下蓋52により上下両端面を閉塞し
た中空円筒形のハウジング53を有し、上蓋51と下蓋
52はボルト54によりハウジング53に締着されてい
る。ハウジング53の底面付近にはガス流入口55が、
上面付近にはガス流入ロ55と同じ開口面積のブス流出
口5Gが設けられている。またハウジング53の外周に
はハウジング53を縦に設置できるように足部57゜5
7が取り付けられている。、′!−らにハウジング53
の下部には空気抜きコック58が設けられている。
5 to 7, the soot removal device 50 has a hollow cylindrical housing 53 whose upper and lower end surfaces are closed by an upper lid 51 and a funnel-shaped lower lid 52. It is fastened to the housing 53 by. A gas inlet 55 is located near the bottom of the housing 53.
A bus outlet 5G having the same opening area as the gas inlet 55 is provided near the top surface. Further, the outer periphery of the housing 53 has a leg portion 57°5 so that the housing 53 can be installed vertically.
7 is installed. ,′! - more housing 53
An air vent cock 58 is provided at the bottom of the.

前記漏斗状下蓋52の中央にはスス排出口52aが形成
され、この排出口52aにボールバルブ59が螺着され
ている。
A soot discharge port 52a is formed in the center of the funnel-shaped lower lid 52, and a ball valve 59 is screwed into this discharge port 52a.

前記ハウジング53の内部には、4個の漏斗体60が積
み重ねて配設され、各漏斗体60の注ぎ口GOaは筒状
ハウジング53の中心線に沿って、下1i52に向けら
れている。最下部の漏斗体60は他に比べで長い注ぎ口
60a゛を有し、取付バー61により下M52に取り付
けられ、注ぎ口60a゛の開口端面が下蓋52の排出口
52aに近接して対向している。最下部の漏斗体60の
上に順に3個の漏斗体60が積み上げられており、隣合
う漏斗体60間は取付バー62により適宜の間隔が設け
られている。そして各漏斗体60の中心線はハウジング
53の中心線から不規則にずらして配置されている。ま
た各漏斗体60の広口部60bの開口端面の外径はハウ
ジング53の内径よりも小さく設定されている。
Inside the housing 53, four funnel bodies 60 are arranged in a stacked manner, and the spout GOa of each funnel body 60 is directed downward 1i52 along the center line of the cylindrical housing 53. The funnel body 60 at the bottom has a spout 60a'' that is longer than the others, and is attached to the lower M52 by a mounting bar 61, and the opening end surface of the spout 60a'' is close to and faces the outlet 52a of the lower lid 52. are doing. Three funnel bodies 60 are stacked in order on the lowest funnel body 60, and appropriate intervals are provided between adjacent funnel bodies 60 by attachment bars 62. The center line of each funnel body 60 is irregularly shifted from the center line of the housing 53. Further, the outer diameter of the opening end surface of the wide mouth portion 60b of each funnel body 60 is set smaller than the inner diameter of the housing 53.

ハウジング53の、ガス流入ロ55からガス流出ロ56
に至る内部空間は、これら各漏斗体60により複数の空
室に区画され、隣接する空室同士はハウジング53の内
壁と各漏斗体60の広口部60bの外周端面の間に形成
された間隙を介して連通されている。各間隙の面積はガ
ス流入ロ55の開口面積とほぼ同じになるように広口部
60bの端面外径が設定されている。また各漏斗体60
の中心をハウジング53の中心線から不規則にずらして
配置したことにより、各間隙の幅は最も狭い部分と最も
広い部分が形成され、その間は連続的に変化し、隣合う
間隙の同幅部分の位置が相対的にずれている。
From the gas inlet hole 55 to the gas outlet hole 56 of the housing 53
The internal space leading to the funnel body 60 is divided into a plurality of chambers by each of the funnel bodies 60, and adjacent cavities are separated by a gap formed between the inner wall of the housing 53 and the outer peripheral end surface of the wide mouth portion 60b of each funnel body 60. communicated through. The outer diameter of the end face of the wide opening portion 60b is set so that the area of each gap is approximately the same as the opening area of the gas inflow hole 55. Also, each funnel body 60
By arranging the center of the housing 53 with its center irregularly shifted from the center line of the housing 53, the width of each gap forms a narrowest part and a widest part, and changes continuously between them, and the same width part of the adjacent gap. The position of is relatively shifted.

本実施例は以上の構成よりなり、ガス流入ロ55からハ
ウジング53内へ流入した変成が又は漏斗体60によっ
て区画された下方の空室から上方の空室へと、間隙を通
って流れ、ガス流出ロ5Gからハウジング53の外部へ
流出する。空室に流れ込んだ変成ガスは間隙を通って隣
接する空室へ流入するが、隣合う間隙の幅広部分の相対
的な位置が互いにずらしであるため、変成ガスは渦巻き
状の流れとなって各空室を巡りガス流出ロ56から流出
する。そして間隙を通過するとき変成ガス中のススが分
離し、分離したススは漏斗体60の内側を伝って注ぎ口
60aから落下する。注ぎ口60mはハウジング53の
中心線に沿い、下蓋52に向けられているので、上方の
漏斗体60がら落下したススは順に下方にある漏斗体6
0の注ぎ口60aをとおって、下MS2まで落下し、二
二に堆積する。
The present embodiment has the above-described configuration, and the metamorphic gas that has flowed into the housing 53 from the gas inflow hole 55 flows through the gap from the lower cavity partitioned by the funnel body 60 to the upper cavity, and the gas It flows out of the housing 53 from the outflow hole 5G. The metamorphosed gas that has flowed into the cavity flows into the adjacent cavity through the gap, but because the relative positions of the wide parts of the adjacent gaps are shifted from each other, the metamorphosed gas becomes a spiral flow and flows into each cavity. The gas circulates around the vacant room and flows out from the gas outflow hole 56. When passing through the gap, the soot in the metamorphic gas separates, and the separated soot travels inside the funnel body 60 and falls from the spout 60a. Since the spout 60m is along the center line of the housing 53 and is directed toward the lower lid 52, the soot that has fallen from the upper funnel body 60 is in turn poured into the lower funnel body 6.
It passes through the spout 60a of No. 0, falls to the lower MS2, and is deposited on No. 22.

下蓋52上に堆積したススは、変成がスの圧送を停止し
た後、ボールバルブ59を繰作して排出口52mを開け
ば、漏斗状の下蓋52の内側を伝ってハウジング53の
外部へ自重落下する。掃除後操業を再開するときは、空
気抜きコック58を開いて中の空気を排出する。
After stopping the pumping of metamorphic soot, the soot deposited on the lower lid 52 can be removed by operating the ball valve 59 to open the discharge port 52m, and the soot can flow along the inside of the funnel-shaped lower lid 52 to the outside of the housing 53. Falling under its own weight. When restarting operation after cleaning, the air vent cock 58 is opened to discharge the air inside.

(発明の効果) 本発明によれば、筒状ハウジングの内部空間を仕切手段
により複数の空室に区画し、隣接する空室を連通する間
隙を形成した極めて簡単な構成により、単に変成ガスを
通すだけで変成ガス中のススを効果的に除去できる。そ
のため製造コストも安く、既存の雰囲気熱処理工程に組
み込むことも容易であり、またフィルタニレメンを使わ
ずにススを除去できるので、装置の保守、管理も極めて
簡単である。
(Effects of the Invention) According to the present invention, the internal space of the cylindrical housing is divided into a plurality of chambers by a partitioning means, and a gap is formed to communicate the adjacent chambers. Soot in metamorphosed gas can be effectively removed just by passing it through. Therefore, the manufacturing cost is low, it is easy to incorporate into the existing atmospheric heat treatment process, and since soot can be removed without using a filter, maintenance and management of the device is extremely simple.

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

第1図は本発明の第1の実施例を示す一部破断斜視図、
第2図はその縦断断面図、第3図は同じく上蓋を取り外
した状態の平面図、PlfJ4図は第1実施例装置を組
み入れた雰囲気調整工程の説明図、第5図は本発明の第
2実施例を示す一部破断斜視。 図、第6図は第2実施例の縦断断面図、第7図は同じく
第2実施例装置の上蓋を外した平面図、第8図はススの
堆積した状態を示す面積式流量形の断面図、第9図は同
じくススの堆積上状態を示す冷却器の流入通路の部分断
面図である。 13.53・・・筒状ハウジング、11.51・・・上
蓋、12.52・・・下蓋、52a・・・排出口、15
.55・・・ガス流入口、16.56・・・ガス流出口
、20・・・仕切板、60・・・漏斗体、60a・・・
注ぎ口、60b・・・広口部、 第 1 図 鉋 2図 第3図 第5図 第6図 第7図 第8r2 第 9図
FIG. 1 is a partially cutaway perspective view showing a first embodiment of the present invention;
Fig. 2 is a longitudinal sectional view thereof, Fig. 3 is a plan view with the top cover removed, Fig. PlfJ4 is an explanatory diagram of the atmosphere adjustment process incorporating the first embodiment device, and Fig. 5 is the second embodiment of the present invention. A partially broken perspective view showing an example. Figure 6 is a vertical sectional view of the second embodiment, Figure 7 is a plan view of the second embodiment with the top cover removed, and Figure 8 is a cross section of the area type flow rate type showing the state in which soot has accumulated. FIG. 9 is a partial sectional view of the inlet passage of the cooler, also showing the state in which soot is deposited. 13.53... Cylindrical housing, 11.51... Upper lid, 12.52... Lower lid, 52a... Discharge port, 15
.. 55... Gas inlet, 16.56... Gas outlet, 20... Partition plate, 60... Funnel, 60a...
Spout, 60b...wide mouth part, Fig. 1 Planer Fig. 2 Fig. 3 Fig. 5 Fig. 6 Fig. 7 Fig. 8r2 Fig. 9

Claims (5)

【特許請求の範囲】[Claims] (1)下部にガス流入口を、上部にガス流出口を形成し
、両端を閉塞した筒状ハウジングと、 この筒状ハウジングの、ガス流入口からガス流出口に至
る内部空間を複数の空室に区画する仕切手段とを備え、 隣接する空室間を連通する間隙を形成したことを特徴と
する変成ガス用スス除去装置。
(1) A cylindrical housing with a gas inlet at the bottom and a gas outlet at the top, closed at both ends, and an internal space from the gas inlet to the gas outlet of the cylindrical housing that is divided into a plurality of empty spaces. What is claimed is: 1. A soot removal device for metamorphic gas, comprising: a partition means for partitioning into two spaces, and a gap communicating between adjacent spaces is formed.
(2)前記筒状ハウジングを、両端を閉塞した中空円筒
体とし、前記仕切手段をこの中空円筒体の内径よりも小
さい直径を有する円板とし、各円板を中空円筒体の中心
線にほぼ直交させたことを特徴とする特許請求の範囲第
1項に記載の変成ガス用スス除去装置。
(2) The cylindrical housing is a hollow cylinder with both ends closed, the partition means is a disk having a diameter smaller than the inner diameter of the hollow cylinder, and each disk is aligned approximately with the center line of the hollow cylinder. The soot removal device for converted gas according to claim 1, characterized in that the soot removal device is orthogonal to each other.
(3)前記円板の中心を中空円筒体の中心線から不規則
にずらして配置したことを特徴とする特許請求の範囲第
2項に記載の変成ガス用スス除去装置。
(3) The soot removal device for converted gas according to claim 2, characterized in that the center of the disk is irregularly shifted from the center line of the hollow cylindrical body.
(4)前記筒状ハウジングに、中心部にスス排出口を形
成した漏斗状の底面を設け、 前記仕切手段を、広口部の端面の外径が筒状ハウジング
の内径よりも小さい複数の漏斗体とし、各漏斗体の注ぎ
口を筒状ハウジングの中心線に沿って底面に向け、各漏
斗体を隣合う漏斗体間に適宜の間隔を設けて積み重ねた
ことを特徴とする特許請求の範囲第1項に記載の変成ガ
ス用スス除去装置。
(4) The cylindrical housing is provided with a funnel-shaped bottom surface with a soot discharge port formed in the center, and the partitioning means is formed of a plurality of funnels each having an outer diameter of the end surface of the wide-mouthed portion smaller than the inner diameter of the cylindrical housing. Claim 1, characterized in that the spout of each funnel is directed toward the bottom surface along the center line of the cylindrical housing, and the funnels are stacked with appropriate spacing between adjacent funnels. The soot removal device for converted gas according to item 1.
(5)前記各漏斗体の中心線を前記筒状ハウジングの中
心線から不規則にずらして配置したことを特徴とする特
許請求の範囲第3項に記載の変成ガス用スス除去装置。
(5) The soot removal device for converted gas according to claim 3, wherein the center line of each funnel body is irregularly shifted from the center line of the cylindrical housing.
JP1406888A 1988-01-25 1988-01-25 Soot removing device for reforming gas Pending JPH01189315A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1406888A JPH01189315A (en) 1988-01-25 1988-01-25 Soot removing device for reforming gas

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1406888A JPH01189315A (en) 1988-01-25 1988-01-25 Soot removing device for reforming gas

Publications (1)

Publication Number Publication Date
JPH01189315A true JPH01189315A (en) 1989-07-28

Family

ID=11850783

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1406888A Pending JPH01189315A (en) 1988-01-25 1988-01-25 Soot removing device for reforming gas

Country Status (1)

Country Link
JP (1) JPH01189315A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100352151B1 (en) * 2000-05-08 2002-09-12 주식회사 가이아 Deodorization apparatus

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100352151B1 (en) * 2000-05-08 2002-09-12 주식회사 가이아 Deodorization apparatus

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