JPH0220570Y2 - - Google Patents

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Publication number
JPH0220570Y2
JPH0220570Y2 JP12591484U JP12591484U JPH0220570Y2 JP H0220570 Y2 JPH0220570 Y2 JP H0220570Y2 JP 12591484 U JP12591484 U JP 12591484U JP 12591484 U JP12591484 U JP 12591484U JP H0220570 Y2 JPH0220570 Y2 JP H0220570Y2
Authority
JP
Japan
Prior art keywords
fluidized bed
supply pipe
burner
combustion furnace
fuel
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
JP12591484U
Other languages
Japanese (ja)
Other versions
JPS6143613U (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 JP12591484U priority Critical patent/JPS6143613U/en
Publication of JPS6143613U publication Critical patent/JPS6143613U/en
Application granted granted Critical
Publication of JPH0220570Y2 publication Critical patent/JPH0220570Y2/ja
Granted legal-status Critical Current

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  • Nozzles For Spraying Of Liquid Fuel (AREA)
  • Fluidized-Bed Combustion And Resonant Combustion (AREA)
  • Crucibles And Fluidized-Bed Furnaces (AREA)
  • Pre-Mixing And Non-Premixing Gas Burner (AREA)

Description

【考案の詳細な説明】 産業上の利用分野 本考案は、流動床燃焼炉の下部に渡架せる格子
板上に流動材を充填し、該流動材内に反応管を挿
入し、該流動床燃焼炉の前記格子板と前記反応管
下端との中間の側壁を貫通して、燃料供給設備と
送風機とに接続されたバーナ本体を該流動床燃焼
炉の内部に挿設してなるパイプバーナ型の流動床
用加熱バーナの改良に関する。
[Detailed description of the invention] Industrial application field The present invention is based on a fluidized bed combustion furnace, in which a fluidized material is filled on a grid plate suspended at the bottom of a fluidized bed combustion furnace, a reaction tube is inserted into the fluidized material, and a reaction tube is inserted into the fluidized bed combustion furnace. A pipe burner type in which a burner main body connected to a fuel supply equipment and a blower is inserted into the fluidized bed combustion furnace by penetrating a side wall intermediate between the grid plate and the lower end of the reaction tube of the combustion furnace. This invention relates to improvements in heating burners for fluidized beds.

従来の技術 第4図は、従来の流動床用加熱バーナの概念図
を示す。この流動床用加熱バーナでは、一定の粒
度の粒子(流動材12と呼ぶ)を垂直塔状流動床
燃焼炉11内に一定量投入して蓄え、この流動材
12内には被加熱媒体が流れている反応管13が
挿入装着されている。そして、送風機14及び燃
料供給設備15からは、燃焼用空気及び燃料が排
ガス発生炉16に装備されているバーナ16aに
送られ、燃焼後、排ガスはプレナムチヤンバー1
7に送られるようになつている。一方、送風機1
4から送風管19を通つた空気は、プレナムチヤ
ンバー17へ送気されて耐熱度以下に温度調整さ
れ、格子板18を通して流動床燃焼炉11内へ噴
出し流動材12の流動化及び燃料の着火温度以上
の加熱を行なうようになつている。
BACKGROUND ART FIG. 4 shows a conceptual diagram of a conventional heating burner for a fluidized bed. In this fluidized bed heating burner, a certain amount of particles with a certain particle size (referred to as fluidized material 12) is charged and stored in a vertical column-shaped fluidized bed combustion furnace 11, and a medium to be heated flows in this fluidized material 12. A reaction tube 13 is inserted and mounted. Then, combustion air and fuel are sent from the blower 14 and the fuel supply equipment 15 to the burner 16a installed in the exhaust gas generating furnace 16, and after combustion, the exhaust gas is transferred to the plenum chamber 1.
It is now being sent to 7th. On the other hand, blower 1
The air passing through the blast pipe 19 from 4 is sent to the plenum chamber 17 where the temperature is adjusted to below the heat resistance level, and is ejected through the grid plate 18 into the fluidized bed combustion furnace 11 to fluidize the fluidized material 12 and fuel. It is designed to heat the fuel above the ignition temperature.

このように流動材12が蓄えられた場合、格子
板18下方から気体を通気しその流量を増加させ
ていくと、次第に、粒子間の吹抜け流速が速くな
り、粒子が吹上げられ、粒子間の空間が大きくな
り、吹上げられた粒子は再び落下するようにす
る。
When the fluidized material 12 is stored in this way, when gas is ventilated from below the grid plate 18 and its flow rate is increased, the flow velocity between the particles gradually increases, the particles are blown up, and the air flow between the particles increases. The space becomes larger and the particles that were blown up will fall back down.

さらに、通気量を増加させると粒子の上下運動
が激しくなり、多数の気泡が生じ、その気泡の周
りは粒子がその気泡の跡を埋めるように流下する
流動床を形成する。
Furthermore, when the aeration rate is increased, the vertical movement of the particles becomes more intense, producing a large number of bubbles, and around the bubbles a fluidized bed is formed in which the particles flow down to fill the traces of the bubbles.

この流動床は流動床内温度が均一で且つ熱伝達
率が大きいので、この流動床に各種熱交換器など
の反応管13を挿入することにより、局所的熱損
傷がなく、且つ均一加熱として、また、良好な伝
熱として有効である。
This fluidized bed has a uniform internal temperature and a high heat transfer coefficient, so by inserting reaction tubes 13 such as various heat exchangers into this fluidized bed, there is no local thermal damage and uniform heating is achieved. Moreover, it is effective for good heat transfer.

考案が解決しようとする問題点 しかし、格子板18は高温にさらされるととも
に、流動材12の全重量がかゝるので、耐熱的、
強度的にすぐれたものが要求され、或いは、格子
板18の許容条件に応じ、上記排ガス温度をかな
り低く(700〜800℃前後)する必要があり、反応
管13の加熱温度に限界を生じ熱効率の向上が妨
げられる。
Problems to be solved by the invention However, since the grid plate 18 is exposed to high temperatures and the total weight of the fluidized material 12 is heavy, the grid plate 18 is not heat resistant.
A material with excellent strength is required, or depending on the allowable conditions of the grid plate 18, it is necessary to lower the exhaust gas temperature considerably (around 700 to 800°C), which limits the heating temperature of the reaction tube 13 and reduces thermal efficiency. improvement is hindered.

本考案は、このような従来技術の問題点に鑑み
てこれを解決するためになされたもので、高温で
安定燃焼する新規な流動床用加熱バーナを提供す
ることを目的とする。
The present invention was devised in view of the problems of the prior art, and aims to provide a novel heating burner for a fluidized bed that achieves stable combustion at high temperatures.

問題点を解決するための手段 この目的を達成するために、本考案の流動床用
加熱バーナでは、流動床燃焼炉の下部に渡架せる
格子板上に流動材を充填し、該流動材内に反応管
を挿入し、該流動床燃焼炉の前記格子板と前記反
応管下端との中間の側壁を貫通して燃料供給設備
と送風機とに接続されたバーナ本体を該流動床燃
焼炉の内部に挿設してなるパイプバーナ型の流動
床用加熱バーナにおいて、前記バーナ本体を、空
気供給管と該空気供給管内に軸芯を揃えて重合す
る燃料供給管とで構成し、それら両供給管の基端
側を水平部とし先端側を垂直部に折曲げ、かつ、
その垂直部が前記流動床燃焼炉内で前記反応管の
下方に位置するよう上向きに配設せしめ、その垂
直部上端には両供給管を閉遮する盲板を設け、該
盲板の下方に、前記空気供給管に連通する空気ノ
ズルとこの空気ノズルの中心部に挿設され前記燃
料供給管に連通する燃料ノズルとが、円周方向に
複数組をなして斜下方を指向するよう配設された
ことを特徴とする。
Means for Solving the Problems In order to achieve this objective, in the fluidized bed heating burner of the present invention, a fluidized material is filled on a grid plate that spans the lower part of the fluidized bed combustion furnace, and the fluidized material is A reaction tube is inserted into the fluidized bed combustion furnace, and the burner body, which is connected to a fuel supply equipment and a blower, is inserted into the interior of the fluidized bed combustion furnace by passing through a side wall intermediate between the grid plate and the lower end of the reaction tube. In a pipe burner-type heating burner for fluidized bed, the burner body is composed of an air supply pipe and a fuel supply pipe that overlaps with the axes aligned within the air supply pipe, and both supply pipes are connected to each other. Bend the proximal end side to the horizontal part and the distal end side to the vertical part, and
The vertical part is arranged upward so that it is located below the reaction tube in the fluidized bed combustion furnace, and a blind plate is provided at the upper end of the vertical part to close off both supply pipes, and a blind plate is provided below the blind plate. , an air nozzle communicating with the air supply pipe and a fuel nozzle inserted in the center of the air nozzle and communicating with the fuel supply pipe are arranged in plural sets in the circumferential direction and directed diagonally downward. It is characterized by having been.

実施例 以下、本考案の詳細を図示する実施例を参照し
ながら説明する。なお、従来のものと共通する構
成部分については、同一符号を使用するものとす
る。
Embodiments The present invention will now be described in detail with reference to illustrative embodiments. Note that the same reference numerals are used for components common to the conventional one.

第1図において、21はバーナ本体であり、流
動床燃焼炉11の下部に渡架せる格子板18とそ
の上方から流動材12内に挿入せる反応管13下
端との中間に挿設され、燃料供給設備15及び送
風機14に接続されている。そして、該バーナ本
体21は水平部21aと垂直部21bとからな
り、その垂直部21bは前記反応管13と軸芯が
略一致するよう上向きに配設されている。それら
の軸芯は当該流動床燃焼炉11の軸芯とも一致し
ている。
In FIG. 1, 21 is a burner main body, which is inserted between the lattice plate 18 that spans the lower part of the fluidized bed combustion furnace 11 and the lower end of the reaction tube 13 that is inserted into the fluidized material 12 from above. It is connected to supply equipment 15 and blower 14 . The burner body 21 is composed of a horizontal portion 21a and a vertical portion 21b, and the vertical portion 21b is disposed upward so that its axis substantially coincides with the reaction tube 13. Their axes also coincide with the axes of the fluidized bed combustion furnace 11.

前記バーナ本体21は、第2図に示すように、
大径の空気供給管31と該空気供給管31内に軸
芯を揃えて重合する小径の燃料供給管32とで構
成され、これら各供給管31,32は夫々水平部
31a,32aと垂直部31b,32bとに折曲
げられている。即ち、該バーナ本体21の水平部
21aは軸芯を略揃えて重合している空気供給管
水平部31aと燃料供給管水平部32aとからな
り、該バーナ本体21の垂直部21bは軸芯を略
揃えて重合している空気供給管垂直部31bと燃
料供給管垂直部32bとからなる。
The burner body 21, as shown in FIG.
It is composed of a large-diameter air supply pipe 31 and a small-diameter fuel supply pipe 32 that overlaps within the air supply pipe 31 with their axes aligned, and each of these supply pipes 31 and 32 has a horizontal part 31a, 32a and a vertical part. It is bent into 31b and 32b. That is, the horizontal part 21a of the burner main body 21 consists of an air supply pipe horizontal part 31a and a fuel supply pipe horizontal part 32a, which are overlapped with their axes substantially aligned, and the vertical part 21b of the burner main body 21 is arranged with their axes substantially aligned. It consists of an air supply pipe vertical section 31b and a fuel supply pipe vertical section 32b which are substantially aligned and overlapped.

前記バーナ本体21の垂直部21bの上端は盲
板21cで塞がれている。即ち、前記両供給管3
1,32の垂直部31b,32bの上端は同時に
盲板21cで閉遮されている。
The upper end of the vertical portion 21b of the burner body 21 is covered with a blind plate 21c. That is, both the supply pipes 3
The upper ends of the vertical portions 31b and 32b of Nos. 1 and 32 are simultaneously closed off by blind plates 21c.

そして、該盲板21cの下方には、前記空気供
給管31に連通する空気ノズル3aと、この空気
ノズル3aの中心部に挿設され前記燃料供給管3
2に連通する燃料ノズル3bとが組をなして斜下
方を指向するよう設けられている。
Below the blind plate 21c, there is an air nozzle 3a communicating with the air supply pipe 31, and a fuel supply pipe 3 inserted into the center of the air nozzle 3a.
2 and a fuel nozzle 3b communicating with the fuel nozzle 2 are provided so as to form a set and face obliquely downward.

該空気ノズル3aと該燃料ノズル3bとの組
は、例えば第3図においては、円周方向に120度
位相を異にして3組配設されている。しかし、そ
の組の数は任意に選定しそれに応じた所定の位相
角で配設することができる。
For example, in FIG. 3, three sets of the air nozzle 3a and the fuel nozzle 3b are arranged with a phase difference of 120 degrees in the circumferential direction. However, the number of sets can be arbitrarily selected and arranged at a predetermined phase angle corresponding to the number.

作 用 次に、上述のように構成される流動床用加熱バ
ーナの作用を説明する。
Function Next, the function of the fluidized bed heating burner configured as described above will be explained.

第1図において、燃料供給設備15及び送風機
14からバーナ本体21に燃料及び空気が送給さ
れるときには、第2図に示すように、燃料は燃料
供給管32を通して燃料ノズル3bから、空気は
空気供給管31を通して空気ノズル3aから夫々
高速で分散噴出され流動床燃焼炉11内で混合す
る。
In FIG. 1, when fuel and air are supplied from the fuel supply equipment 15 and the blower 14 to the burner body 21, as shown in FIG. They are dispersed and ejected from the air nozzles 3a through the supply pipe 31 at high speed and mixed in the fluidized bed combustion furnace 11.

この場合、予め排ガス発生炉16からの排ガス
がプレナムチヤンバー17へ送給されて、流動床
燃焼炉11内は燃料の着火温度以上に加熱されて
いるので(この加熱後、プレナムチヤンバー17
への排ガスの送給は停止される)、バーナ本体2
1の各空気ノズル3a及び燃料ノズル3bから空
気及び燃料が燃焼炉11内に噴出されると、直ち
に、着火燃焼を始める。
In this case, the exhaust gas from the exhaust gas generating furnace 16 is sent to the plenum chamber 17 in advance, and the inside of the fluidized bed combustion furnace 11 is heated above the ignition temperature of the fuel (after this heating, the plenum chamber 17
), the supply of exhaust gas to the burner body 2 is stopped.
When air and fuel are injected into the combustion furnace 11 from each air nozzle 3a and fuel nozzle 3b, ignition combustion starts immediately.

該燃焼炉11内では、流動床12がスタビライ
サー(保炎器)の働きをし、安定燃焼及び流動化
を得る。その後は、バーナ本体21への空気及び
燃料の各供給量を調整し、安定燃焼の維持及び流
動床温度の高温化を図る。
In the combustion furnace 11, the fluidized bed 12 functions as a stabilizer (flame stabilizer) to achieve stable combustion and fluidization. Thereafter, the amounts of air and fuel supplied to the burner body 21 are adjusted to maintain stable combustion and increase the temperature of the fluidized bed.

この際、バーナ本体21より下方の格子板18
は、プレナムチヤンバー17が主に送風機14か
らの低温の空気を供給されているためにあまり加
熱されないので、かなり高温まで流動材12の温
度を加温できる。
At this time, the lattice plate 18 below the burner body 21
Since the plenum chamber 17 is mainly supplied with low-temperature air from the blower 14, it is not heated much, so the temperature of the fluidized material 12 can be increased to a considerably high temperature.

また、前記バーナ本体21には、比較的低温の
燃料及び燃焼用空気が送給され、該バーナ本体2
1自体を冷却することができ、そのため、耐熱的
に特殊な構造を必要としない。そして、燃料及び
燃焼用空気の増加顕熱は再び流動床燃焼炉11に
投入されるのでヒートロスはない。
Further, relatively low temperature fuel and combustion air are supplied to the burner body 21, and the burner body 21 is supplied with relatively low temperature fuel and combustion air.
1 itself can be cooled, and therefore no special heat-resistant structure is required. Then, the increased sensible heat of the fuel and combustion air is again input into the fluidized bed combustion furnace 11, so there is no heat loss.

一方、バーナの燃焼量及び空燃比など燃焼条件
を変えることにより、流動床燃焼炉内温度、空塔
速度などの条件を微調整することが容易である。
On the other hand, by changing the combustion conditions such as the combustion amount of the burner and the air-fuel ratio, it is easy to finely adjust the conditions such as the temperature inside the fluidized bed combustion furnace and the superficial velocity.

さらに、流動床燃焼炉内温度が着火温度以上で
あれば、常に、停止起動ができ、DSS(毎日深夜
停止)操作ができる。
Furthermore, if the internal temperature of the fluidized bed combustion furnace is above the ignition temperature, it is always possible to start and stop, and to perform DSS (Daily Late Night Shutdown) operation.

考案の効果 以上述べたように、本考案の流動床用加熱バー
ナでは、流動床燃焼炉の下部に渡架せる格子板上
に流動材を充填し、該流動材内に反応管を挿入
し、該流動床燃焼炉の前記格子板と前記反応管下
端との中間の側壁を貫通して燃料供給設備と送風
機とに接続されたバーナ本体を該流動床燃焼炉の
内部に挿設してなるパイプバーナ型の流動床用加
熱バーナにおいて、前記バーナ本体を、空気供給
管と該空気供給管内に軸芯を揃えて重合する燃料
供給管とで構成し、それら両供給管の基端側を水
平部とし先端側を垂直部に折曲げ、かつ、その垂
直部が前記流動床燃焼炉内で前記反応管の下方に
位置するよう上向きに配設せしめ、その垂直部上
端には両供給管を閉遮する盲板を設け、該盲板の
下方に、前記空気供給管に連通する空気ノズルと
この空気ノズルの中心部に挿設され前記燃料供給
管に連通する燃料ノズルとが、円周方向に複数組
をなして斜下方を指向するよう配設されたので、
格子板は高温にさらされず、特殊な耐熱的、強度
的にすぐれたものを選定する必要がなく、而も、
流動床燃焼炉内に配設される各種熱交換器などの
反応管の加熱温度を著しく高くとることで熱効率
の向上を図ることができ、さらに、燃料ノズル及
び燃焼用空気ノズルが下方に傾斜していることに
より、流動化して落下してくる流動材を速やかに
下方に滑り落させ、また、各々のノズル内への流
動材の飛込を防止することができる。
Effects of the Invention As described above, in the fluidized bed heating burner of the present invention, a fluidized material is filled on a grid plate that spans the lower part of a fluidized bed combustion furnace, a reaction tube is inserted into the fluidized material, and a reaction tube is inserted into the fluidized material. A pipe formed by inserting a burner main body into the fluidized bed combustion furnace, which is connected to a fuel supply equipment and a blower by penetrating the intermediate side wall between the grid plate and the lower end of the reaction tube of the fluidized bed combustion furnace. In a burner-type fluidized bed heating burner, the burner body is composed of an air supply pipe and a fuel supply pipe that overlaps with the axes aligned within the air supply pipe, and the base ends of both supply pipes are arranged in a horizontal section. The tip side of the tube is bent into a vertical part, and the vertical part is arranged upward so that it is located below the reaction tube in the fluidized bed combustion furnace, and both supply pipes are closed and shielded at the upper end of the vertical part. A blind plate is provided below the blind plate, and a plurality of air nozzles communicating with the air supply pipe and a plurality of fuel nozzles inserted into the center of the air nozzle and communicating with the fuel supply pipe are disposed below the blind plate. Because they were arranged in pairs and oriented diagonally downward,
The lattice plate is not exposed to high temperatures, so there is no need to select a special one with excellent heat resistance and strength.
Thermal efficiency can be improved by significantly increasing the heating temperature of reaction tubes such as various heat exchangers installed in a fluidized bed combustion furnace, and furthermore, the fuel nozzle and combustion air nozzle are tilted downward. By doing so, the fluidized material that is fluidized and falls can be quickly slid down, and the fluidized material can be prevented from jumping into each nozzle.

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

第1図は本考案の流動床用加熱バーナの概要
図、第2図は同上流動床用加熱バーナの要部縦断
面図、第3図は第2図の−線断面図、第4図
は従来の流動床用加熱バーナの概要図である。 11……流動床燃焼炉、12……流動材、13
……反応管、14……送風機、15……燃料供給
設備、18……格子板、21……バーナ本体、3
1……空気供給管、32……燃料供給管、21
a,31a,32a……水平部、21b,31
b,32b……垂直部、21c……盲板、3a…
…空気ノズル、3b……燃料ノズル。
Fig. 1 is a schematic diagram of the fluidized bed heating burner of the present invention, Fig. 2 is a vertical sectional view of the main part of the same fluidized bed heating burner, Fig. 3 is a sectional view taken along the - line in Fig. 2, and Fig. 4 is a FIG. 1 is a schematic diagram of a conventional fluidized bed heating burner. 11... Fluidized bed combustion furnace, 12... Fluidized material, 13
... Reaction tube, 14 ... Blower, 15 ... Fuel supply equipment, 18 ... Grid plate, 21 ... Burner body, 3
1...Air supply pipe, 32...Fuel supply pipe, 21
a, 31a, 32a...horizontal part, 21b, 31
b, 32b...vertical part, 21c...blind plate, 3a...
...Air nozzle, 3b...Fuel nozzle.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 流動床燃焼炉の下部に渡架せる格子板上に流動
材を充填し、該流動材内に反応管を挿入し、該流
動床燃焼炉の前記格子板と前記反応管下端との中
間の側壁を貫通して燃料供給設備と送風機とに接
続されたバーナ本体を該流動床燃焼炉の内部に挿
設してなるパイプバーナ型の流動床用加熱バーナ
において、前記バーナ本体を空気供給管と該空気
供給管内に軸芯を揃えて重合する燃料供給管とで
構成し、それら両供給管の基端側を水平部とし先
端側を垂直部に折曲げ、かつ、その垂直部が前記
流動床燃焼炉内で前記反応管の下方に位置するよ
う上向きに配設せしめ、その垂直部上端には両供
給管を閉遮する盲板を設け、該盲板の下方に、前
記空気供給管に連通する空気ノズルとこの空気ノ
ズルの中心部に挿設され前記燃料供給管に連通す
る燃料ノズルとが、円周方向に複数組をなして斜
下方を指向するよう配設されたことを特徴とする
流動床用加熱バーナ。
A fluidized material is filled on a lattice plate that spans the lower part of the fluidized bed combustion furnace, a reaction tube is inserted into the fluidized material, and a side wall is formed between the lattice plate and the lower end of the reaction tube of the fluidized bed combustion furnace. In a pipe burner-type heating burner for a fluidized bed, in which a burner body is inserted into the fluidized bed combustion furnace and is connected to a fuel supply equipment and a blower through a pipe, the burner body is connected to an air supply pipe. It consists of an air supply pipe and a fuel supply pipe that overlaps with their axes aligned, and the proximal ends of both supply pipes are horizontal and the distal ends are bent into a vertical part, and the vertical part is the fluidized bed combustion It is disposed upward so as to be located below the reaction tube in the furnace, and a blind plate is provided at the upper end of the vertical part to close off both supply pipes, and a blind plate is provided below the blind plate to communicate with the air supply pipe. A fluid flow system characterized in that an air nozzle and a fuel nozzle inserted in the center of the air nozzle and communicating with the fuel supply pipe are arranged in plural sets in the circumferential direction so as to face diagonally downward. Floor heating burner.
JP12591484U 1984-08-21 1984-08-21 Heating burner for fluidized bed Granted JPS6143613U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12591484U JPS6143613U (en) 1984-08-21 1984-08-21 Heating burner for fluidized bed

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12591484U JPS6143613U (en) 1984-08-21 1984-08-21 Heating burner for fluidized bed

Publications (2)

Publication Number Publication Date
JPS6143613U JPS6143613U (en) 1986-03-22
JPH0220570Y2 true JPH0220570Y2 (en) 1990-06-05

Family

ID=30684602

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12591484U Granted JPS6143613U (en) 1984-08-21 1984-08-21 Heating burner for fluidized bed

Country Status (1)

Country Link
JP (1) JPS6143613U (en)

Also Published As

Publication number Publication date
JPS6143613U (en) 1986-03-22

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