JPH06103155B2 - Operating method of atmosphere circulation type fluidized bed furnace - Google Patents

Operating method of atmosphere circulation type fluidized bed furnace

Info

Publication number
JPH06103155B2
JPH06103155B2 JP17597390A JP17597390A JPH06103155B2 JP H06103155 B2 JPH06103155 B2 JP H06103155B2 JP 17597390 A JP17597390 A JP 17597390A JP 17597390 A JP17597390 A JP 17597390A JP H06103155 B2 JPH06103155 B2 JP H06103155B2
Authority
JP
Japan
Prior art keywords
fluidized bed
furnace
gas
atmosphere
circulation
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
JP17597390A
Other languages
Japanese (ja)
Other versions
JPH0464890A (en
Inventor
功 吉中
一義 掛田
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.)
Chugai Ro Co Ltd
Original Assignee
Chugai Ro Co Ltd
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 Chugai Ro Co Ltd filed Critical Chugai Ro Co Ltd
Priority to JP17597390A priority Critical patent/JPH06103155B2/en
Publication of JPH0464890A publication Critical patent/JPH0464890A/en
Publication of JPH06103155B2 publication Critical patent/JPH06103155B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Landscapes

  • Crucibles And Fluidized-Bed Furnaces (AREA)

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は、雰囲気循環式流動層炉の操業方法に関するも
のである。
TECHNICAL FIELD The present invention relates to a method for operating an atmospheric circulation type fluidized bed furnace.

(従来の技術) 従来、雰囲気循環式流動層炉としては、たとえば、第4
図に示すものが公知である。
(Prior Art) Conventionally, as an atmosphere circulation type fluidized bed furnace, for example,
The one shown in the figure is known.

図において、1は炉本体で、この炉本体1の内部には、
アルミナなどの流動粒子が充填されたレトルト2が炉内
壁と所定間隔を保って配設され、ヒータなどの加熱手段
3により加熱されるようになっている。
In the figure, 1 is a furnace body, and inside the furnace body 1,
The retort 2 filled with fluidized particles such as alumina is arranged at a predetermined distance from the inner wall of the furnace, and is heated by the heating means 3 such as a heater.

5は炉蓋で、前記炉本体1の上端面にサンドシール4を
介して設置され、図示しない昇降手段で上下動可能とな
っている。また、前記炉蓋5には、簀子状の材料保持部
材6が垂設され、炉蓋5の下面にはフィルタ7が設けて
ある。
Reference numeral 5 denotes a furnace lid, which is installed on the upper end surface of the furnace body 1 via a sand seal 4 and can be moved up and down by an elevating means (not shown). A material holding member 6 in the shape of a bowl is vertically provided on the furnace lid 5, and a filter 7 is provided on the lower surface of the furnace lid 5.

10は水冷ジャケット式サイクロンで、その流入管11はサ
ンドシール9を介して、前記炉蓋5に設けた排気管8と
接続するようになっている。一方、サイクロン10の排気
管12は、前記レトルト2内の下部に配設したノズル方式
のガス分散手段15に連通する雰囲気循環路13aと大気に
開放する放出路13bとに分岐され、前記雰囲気循環路13a
にはブロア,エダクタ式ジェットポンプ等のガス循環手
段14を備えている。また、前記雰囲気循環路13aのブロ
ア14の下流側には、流量調節弁16を有する保護雰囲気ガ
ス供給管17が接続されている。
Reference numeral 10 is a water-cooled jacket type cyclone, and its inflow pipe 11 is connected to an exhaust pipe 8 provided in the furnace lid 5 via a sand seal 9. On the other hand, the exhaust pipe 12 of the cyclone 10 is branched into an atmosphere circulation passage 13a communicating with the nozzle type gas dispersion means 15 disposed in the lower part of the retort 2 and a discharge passage 13b opening to the atmosphere, and the atmosphere circulation Road 13a
Is equipped with a gas circulation means 14 such as a blower or an eductor type jet pump. A protective atmosphere gas supply pipe 17 having a flow rate control valve 16 is connected to the atmosphere circulation path 13a downstream of the blower 14.

そして、前記材料保持部材6上に載置された材料Wは、
前記ブロア14による循環雰囲気ガスと前記ガス供給管17
からの保護雰囲気ガスとからなる混合雰囲気ガスによっ
て形成される流動層18内で熱処理される。
The material W placed on the material holding member 6 is
Circulating atmosphere gas by the blower 14 and the gas supply pipe 17
The heat treatment is performed in the fluidized bed 18 formed by the mixed atmosphere gas including the protective atmosphere gas from.

一方、レトルト2から排出される雰囲気ガスは、フィル
タ7とサイクロン10とにより雰囲気ガス中の流動粒子が
除去され、一部は放出路13bから大気に放出され、残り
は雰囲気循環路13aにより前述のように循環使用され
る。
On the other hand, in the atmospheric gas discharged from the retort 2, the fluid particles in the atmospheric gas are removed by the filter 7 and the cyclone 10, part of the atmospheric gas is discharged to the atmosphere through the discharge passage 13b, and the rest is discharged by the atmosphere circulation passage 13a. Used as a circulation.

(発明が解決しようとする課題) ところで、流動層炉においては、材料Wを流動層18内へ
の装入時および流動層18内からの抽出時には流動状態と
する必要がある。
(Problems to be Solved by the Invention) In a fluidized bed furnace, it is necessary to bring the material W into a fluid state at the time of charging into the fluidized bed 18 and at the time of extraction from the fluidized bed 18.

したがって、前述した雰囲気循環式流動層炉では、材料
Wの流動層18内への装入あるいは流動層18内からの抽出
に際し、炉蓋が開放された状態で、ブロア等のガス循環
手段14を運転することになる。そのため、空気が流動層
18内に供給されて、流動層18内のO2濃度が上昇する、す
なわち、流動層18内の雰囲気が大巾に汚染されるという
問題がある。また、流動層炉では材料の昇温速度が非常
に速いため(たとえば、約800℃/min)、レトルト2内
の雰囲気が無酸化状態になる以前に、材料Wが600℃以
上に加熱されて材料Wが酸化するという問題を有してい
た。
Therefore, in the above-mentioned atmosphere circulation type fluidized bed furnace, when the material W is charged into the fluidized bed 18 or extracted from the fluidized bed 18, the gas circulation means 14 such as a blower is provided with the furnace lid open. I will drive. Therefore, the air is in the fluidized bed
When it is supplied into the fluidized bed 18, the O 2 concentration in the fluidized bed 18 increases, that is, there is a problem that the atmosphere in the fluidized bed 18 is greatly polluted. Further, in the fluidized bed furnace, since the temperature rising rate of the material is very high (for example, about 800 ° C / min), the material W is heated to 600 ° C or higher before the atmosphere in the retort 2 becomes non-oxidized. There was a problem that the material W was oxidized.

本発明は、流動層内の雰囲気汚染を確実に防止して、材
料の酸化のない処理ができる雰囲気循環式流動層炉の操
業方法を提供することを目的とする。
An object of the present invention is to provide a method for operating an atmospheric circulation type fluidized bed furnace which can surely prevent atmospheric pollution in the fluidized bed and can perform a treatment without material oxidation.

(課題を解決するための手段) 本発明は、前記目的を達成するために、ガス循環手段に
より流動用雰囲気ガスを循環使用する雰囲気循環式流動
層炉において、雰囲気循環路の前記ガス循環手段の上流
側に仕切弁を設け、炉蓋の開放開始から閉鎖終了までの
炉蓋開放期間、前記仕切弁を閉とし、かつ、前記ガス循
環手段の運転を停止するとともに、前記炉蓋開放期間の
うち少なくとも材料の炉内への装入および炉内からの抽
出動作時、保護雰囲気ガスのみによりレトルト内の流動
粒子を流動させるようにしたものである。
(Means for Solving the Problems) In order to achieve the above-mentioned object, the present invention relates to an atmosphere circulation type fluidized bed furnace in which a gas atmosphere for circulation is circulated and used in a gas circulation means of an atmosphere circulation path. A sluice valve is provided on the upstream side, the furnace lid opening period from the start of opening the furnace lid to the end of closing, the sluice valve is closed, and the operation of the gas circulation means is stopped, and the furnace lid opening period is At least at the time of charging the material into the furnace and extracting the material from the furnace, the fluidized particles in the retort are made to flow only by the protective atmosphere gas.

(実施例) つぎに、本発明の一実施例を第1図、第2図にしたがっ
て説明する。
(Embodiment) Next, an embodiment of the present invention will be described with reference to FIGS. 1 and 2.

第1図は、第3図と比較すれば明らかなように、構造的
には、雰囲気循環路13aの途中に、下記する仕切弁18を
設けた点においてのみ相違し、他は同一であるため、同
一部分に同一符号を付して説明を省略する。
As is clear from a comparison with FIG. 3, FIG. 1 is structurally different only in that a sluice valve 18 described below is provided in the middle of the atmosphere circulation path 13a, and the others are the same. , The same parts are designated by the same reference numerals and the description thereof will be omitted.

本発明においては、材料Wの熱処理中にあっては、第2
図に示すように、前記仕切弁18を開とし、ブロア14を駆
動してレトルト2内の雰囲気ガスを循環するとともに、
流量調節弁16から所定量の新規な保護雰囲気ガスを雰囲
気循環路13a内に供給する。
In the present invention, during the heat treatment of the material W, the second
As shown in the figure, the sluice valve 18 is opened, the blower 14 is driven to circulate the atmospheric gas in the retort 2, and
A predetermined amount of new protective atmosphere gas is supplied from the flow rate control valve 16 into the atmosphere circulation path 13a.

そして、所定時間経過後、材料Wを抽出するにあたり、
まず、前記仕切弁18を閉じるとともに、ブロア14の駆動
を停止する一方、前記流量調節弁16を全開として、流動
粒子を保護雰囲気ガスのみにより流動させつつ炉蓋5を
上昇させて開蓋する。
Then, when the material W is extracted after a predetermined time has passed,
First, while closing the sluice valve 18 and stopping the drive of the blower 14, the flow rate control valve 16 is fully opened, and the furnace lid 5 is lifted and opened while flowing the fluidized particles only with the protective atmosphere gas.

その後、材料保持部材6が炉本体1から離間して、材料
Wが流動層18内から抽出されると、前記流量調節弁16を
閉とし保護雰囲気ガスの供給を停止する。この状態は、
つぎの材料Wが材料保持部材6上に載置されて流動層18
内に装入されるまで継続する。
After that, when the material holding member 6 is separated from the furnace body 1 and the material W is extracted from the fluidized bed 18, the flow rate control valve 16 is closed and the supply of the protective atmosphere gas is stopped. This state is
The next material W is placed on the material holding member 6 to form the fluidized bed 18
Continue until charged.

材料Wが流動層18内に装入され始めると、前記流量調節
弁16を全開とし、流動粒子を保護雰囲気ガスのみにより
流動させる。
When the material W begins to be charged into the fluidized bed 18, the flow rate control valve 16 is fully opened to cause the fluidized particles to flow only by the protective atmosphere gas.

そして、前記炉蓋5が炉本体1上に載置されると(排気
管8と流入管11は接続される)、前記仕切弁18を開とす
るとともに、前記ブロア14を駆動させ、通常の操業に入
るものである。
Then, when the furnace lid 5 is placed on the furnace body 1 (the exhaust pipe 8 and the inflow pipe 11 are connected), the sluice valve 18 is opened and the blower 14 is driven, and It is going to be in operation.

なお、この間における保護雰囲気ガス供給管17の流量調
節弁16の開度は第2図に示す通りであり、仕切弁18が閉
から開に切換わる短時間、保護雰囲気ガスを多量に供給
するのは、レトルト2内を完全にパージするためであ
る。
The opening of the flow rate control valve 16 of the protective atmosphere gas supply pipe 17 during this period is as shown in FIG. 2, and a large amount of protective atmosphere gas is supplied for a short time when the sluice valve 18 is switched from closed to open. Is for completely purging the inside of the retort 2.

前記のように、材料保持部材6が上昇状態、すなわち、
材料Wが流動層18外にあるときに、保護雰囲気ガスの供
給を停止するのは、この期間においては、流動状態を保
持する必要がなく、かつ、この状態では、流動槽2内へ
の空気の侵入が少なく、流動層18内の雰囲気が殆ど汚染
されないからであり、また、保護雰囲気ガスの消費量を
軽減するためである。
As described above, the material holding member 6 is in the raised state, that is,
When the material W is outside the fluidized bed 18, the supply of the protective atmosphere gas is stopped so that it is not necessary to maintain the fluidized state in this period, and in this state, the air into the fluidized tank 2 is stopped. This is because there is little invasion of the gas and the atmosphere in the fluidized bed 18 is hardly contaminated, and the consumption of the protective atmosphere gas is reduced.

なお、前記実施例では、材料保持部材6は炉蓋5に一体
に設けた場合を示したが、これに限らないことは云うま
でもない。さらに、ガス分散手段15はノズル方式を示し
たが、第3図に示すように、分散板15a方式であっても
よい。
Although the material holding member 6 is provided integrally with the furnace lid 5 in the above embodiment, it goes without saying that the material holding member 6 is not limited to this. Further, although the gas dispersion means 15 is of the nozzle type, it may be of the dispersion plate 15a type as shown in FIG.

(発明の効果) 以上の説明で明らかなように、本発明によれば、炉蓋が
開状態にあると、仕切弁を閉とするとともにガス循環手
段を停止するため、流動層に空気が侵入せず、材料の酸
化が防止されるとともに、操業開始にあたってのパージ
用保護雰囲気ガスの使用量が軽減される。
(Effects of the Invention) As is apparent from the above description, according to the present invention, when the furnace lid is in the open state, the sluice valve is closed and the gas circulation means is stopped, so that air enters the fluidized bed. Without doing so, the material is prevented from being oxidized and the amount of the protective atmosphere gas for purging used at the start of the operation is reduced.

しかも、材料保持部材が流動層外にあるときには、保護
雰囲気ガスの供給を停止するようにすれば、保護雰囲気
ガスの使用量を大巾に低減し、ランニングコストを安価
にすることができる。
Moreover, when the material holding member is outside the fluidized bed, by stopping the supply of the protective atmosphere gas, the amount of the protective atmosphere gas used can be greatly reduced and the running cost can be reduced.

【図面の簡単な説明】 第1図は本発明を適用する雰囲気循環式流動層炉の概略
図、第2図は第1図のブロア、仕切弁、新規雰囲気ガス
の1サイクルでのサイクルモーション図、第3図はガス
分散手段の他の実施例を示す断面図で、第4図は従来の
雰囲気循環式流動層炉の概略図である。 1……炉本体、2……レトルト、3……加熱手段、5…
…炉蓋、6……材料保持部材、8……排気管、9……サ
ンドシール、11……流入管、13a……開放路、14……ガ
ス循環手段、15……ガス分散手段、16……流量調節弁、
18……仕切弁。
BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a schematic view of an atmospheric circulation type fluidized bed furnace to which the present invention is applied, and FIG. 2 is a cycle motion diagram in one cycle of a blower, a sluice valve, and a new atmospheric gas in FIG. FIG. 3 is a sectional view showing another embodiment of the gas dispersion means, and FIG. 4 is a schematic view of a conventional atmosphere circulation type fluidized bed furnace. 1 ... furnace body, 2 ... retort, 3 ... heating means, 5 ...
… Furnace lid, 6 …… Material holding member, 8 …… Exhaust pipe, 9 …… Sand seal, 11 …… Inflow pipe, 13a …… Open passage, 14 …… Gas circulation means, 15 …… Gas dispersion means, 16 ...... Flow control valve,
18 ... Gate valve.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】ガス循環手段により流動用雰囲気ガスを循
環使用する雰囲気循環式流動層炉において、雰囲気循環
路の前記ガス循環手段の上流側に仕切弁を設け、炉蓋の
開放開始から閉鎖終了までの炉蓋開放期間、前記仕切弁
を閉とし、かつ、前記ガス循環手段の運転を停止すると
ともに、前記炉蓋開放期間のうち少なくとも材料の炉内
への装入および炉内からの抽出動作時、保護雰囲気ガス
のみによりレトルト内の流動粒子を流動させることを特
徴とする雰囲気循環式流動層炉の操業方法。
1. An atmosphere circulation type fluidized bed furnace in which an atmosphere gas for fluidization is circulated and used by a gas circulation means, and a sluice valve is provided on the upstream side of the gas circulation means in an atmosphere circulation path, and the opening and closing of the furnace lid is completed. To the furnace lid open period, the gate valve is closed, and the operation of the gas circulation means is stopped, and at least the material is charged into the furnace and the extraction operation from the furnace is performed during the furnace lid open period. At this time, a method for operating an atmosphere circulation type fluidized bed furnace characterized in that the fluidized particles in the retort are made to flow only by a protective atmosphere gas.
JP17597390A 1990-07-02 1990-07-02 Operating method of atmosphere circulation type fluidized bed furnace Expired - Lifetime JPH06103155B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP17597390A JPH06103155B2 (en) 1990-07-02 1990-07-02 Operating method of atmosphere circulation type fluidized bed furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP17597390A JPH06103155B2 (en) 1990-07-02 1990-07-02 Operating method of atmosphere circulation type fluidized bed furnace

Publications (2)

Publication Number Publication Date
JPH0464890A JPH0464890A (en) 1992-02-28
JPH06103155B2 true JPH06103155B2 (en) 1994-12-14

Family

ID=16005483

Family Applications (1)

Application Number Title Priority Date Filing Date
JP17597390A Expired - Lifetime JPH06103155B2 (en) 1990-07-02 1990-07-02 Operating method of atmosphere circulation type fluidized bed furnace

Country Status (1)

Country Link
JP (1) JPH06103155B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1314944A4 (en) 2000-08-09 2004-12-15 Asahi Tec Corp Hot air blow type fluidized bed furnace, rotary type heat treatment furnace, heat treatment device, and heat treatment method
JP2011149559A (en) * 2010-01-19 2011-08-04 Tani Kikan Kogyo Kk Heating device

Also Published As

Publication number Publication date
JPH0464890A (en) 1992-02-28

Similar Documents

Publication Publication Date Title
JP2001324271A (en) Twin furnace for immersion melting of polluted aluminum scrap metal
KR102255643B1 (en) Melting furnace
JPH06103155B2 (en) Operating method of atmosphere circulation type fluidized bed furnace
US5806444A (en) Method and an installation for treating waste by drying, sublimination, oxidation, and combustion
JP3408464B2 (en) Clean oven
JPS59173515A (en) Diesel particulate filter regenerating device
TR201807308T4 (en) WASTE PROCESSING FURNACE AND METHOD
US5191844A (en) Process and apparatus for the treatment of dust or like material which is capable of trickle flow
JPH0552524U (en) Batch type fluidized bed furnace treatment material charging / extracting device
JPH1114265A (en) Sand flow, roasting device, and its roasting method of self-curing resin sand for casting in fluidized roaster
JPH058393U (en) Processing material charging / extracting device for batch type fluidized bed furnace
JPH0320676B2 (en)
US2438812A (en) Furnace and method of operating same
JPS6414588A (en) Sintering furnace
JPH05172325A (en) Method of reducing nox in batch type burning furnace and device to reduce nox
JPH0448108A (en) Organic material removing fluidized bed apparatus
JPS5829995B2 (en) Coal gasifier using molten iron heat transfer medium
JPS6345678Y2 (en)
JPH04263786A (en) Operating method of fluidized bed type heating and cleaning furnace
JPH04118923A (en) Heat treatment furnace
KR100725090B1 (en) Apparatus to remove gas fume and thereof method
JPH0586457B2 (en)
JPH0470554B2 (en)
JPH0830570B2 (en) Operation method of batch type fluidized bed type heating and cleaning furnace
JPH05317402A (en) Sterilization treatment method by hot water and apparatus therefor