JPH0212434Y2 - - Google Patents
Info
- Publication number
- JPH0212434Y2 JPH0212434Y2 JP1984074306U JP7430684U JPH0212434Y2 JP H0212434 Y2 JPH0212434 Y2 JP H0212434Y2 JP 1984074306 U JP1984074306 U JP 1984074306U JP 7430684 U JP7430684 U JP 7430684U JP H0212434 Y2 JPH0212434 Y2 JP H0212434Y2
- Authority
- JP
- Japan
- Prior art keywords
- combustion
- heat exchange
- exchange chamber
- gas
- pipe
- 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
Links
Landscapes
- Incineration Of Waste (AREA)
- Chimneys And Flues (AREA)
Description
【考案の詳細な説明】
本考案は廃棄物の燃焼ストーブに係わり、更に
詳しくは廃タイヤチツプ、廃木材チツプ、廃プラ
スチツク等の廃棄固形物を燃料源とするストーブ
又はそれに類する炉の改良に関する。[Detailed Description of the Invention] The present invention relates to a waste combustion stove, and more particularly to improvements in stoves or similar furnaces that use waste solid materials such as waste tire chips, waste wood chips, and waste plastics as a fuel source.
従来から廃棄物を燃料とする燃焼ストーブは
種々用いられている。以前の構成は、一次燃焼室
と、該一次燃焼室に対して二次空気供給口が形成
された二次燃焼筒を介して連らなる熱交換室と、
該熱交換室に連らなる排気吸引フアンを有する排
気筒より成り、上記一次燃焼室の底部と二次燃焼
筒の間にはガス抜き管が連結されて成り、且つ一
次燃焼室の底部に水タンクを設けたものである。 Conventionally, various types of combustion stoves that use waste as fuel have been used. The previous configuration consisted of a primary combustion chamber, a heat exchange chamber connected to the primary combustion chamber via a secondary combustion cylinder in which a secondary air supply port was formed,
It consists of an exhaust pipe having an exhaust suction fan connected to the heat exchange chamber, a gas vent pipe is connected between the bottom of the primary combustion chamber and the secondary combustion pipe, and a water pipe is connected to the bottom of the primary combustion chamber. It is equipped with a tank.
この構造の装置によると、廃棄固形物を燃料と
して、基本的には暖房の用等に供することはでき
るが次の不具合を有する。即ち、廃タイヤチツプ
等を燃焼させると、黒煙ガス、亜硫酸ガス等の
種々の悪臭ガス、有害ガスが発生し、燃焼ガス中
の黒煙粒子等がストーブ内からストーブ外の室内
へ漏出してしまい、その悪臭等の為に耐えられな
くなる場合がある。 According to the device having this structure, the waste solids can basically be used for purposes such as heating, but it has the following disadvantages. In other words, when waste tire chips and the like are burned, various foul-smelling and harmful gases such as black smoke gas and sulfur dioxide gas are generated, and black smoke particles in the combustion gas leak from inside the stove into the room outside the stove. , the odor may become unbearable.
そこで、特公昭49−25028、特公昭52−20793、
特開昭49−72963、特開昭50−59844、実開昭52−
127339、特開昭49−73734等を組合わせて、一次
燃焼室と、該一次燃焼室に対して二次空気供給口
が形成された二次燃焼筒を介して連らなる熱交換
室と、該熱交換室に連らなる排気吸引フアンを有
する排気筒より成り、上記一次燃焼室の底部と二
次燃焼筒の間にはガス抜き管が連結されて成る廃
棄物の燃焼ストーブに於いて、上記二次燃焼筒の
下方に水タンクを設けると共に、下部がそのタン
クの上方に連らなり、上部ノズルが二次燃焼筒内
に臨み、且つこのノズルが熱交換室の方を向いて
形成された気化管を設ける技術が考慮される。 Therefore, the special public interest rate was 49-25028, the special public interest rate was 52-20793,
Unexamined Japanese Patent Application 1973-72963, Unexamined Japanese Patent Application 1972-59844, Unexamined Japanese Patent Application 1976-5984
127339, JP-A-49-73734, etc., a primary combustion chamber and a heat exchange chamber connected to the primary combustion chamber via a secondary combustion cylinder in which a secondary air supply port is formed; In a waste combustion stove comprising an exhaust pipe having an exhaust suction fan connected to the heat exchange chamber, and a gas vent pipe connected between the bottom of the primary combustion chamber and the secondary combustion pipe, A water tank is provided below the secondary combustion cylinder, the lower part extends above the tank, the upper nozzle faces into the secondary combustion cylinder, and this nozzle faces the heat exchange chamber. Techniques for providing vaporizer tubes are considered.
このようにすれば二次燃焼筒5を通る燃焼ガス
中に含まれる黒煙粒子を気化水分に吸着せしめ、
可及的にストーブ内で処理し、ストーブ外へ可及
的に排出させないで済む場合もある。然しながら
この技術的考えが有効に活かされる為には、二次
燃焼筒中を流れる燃焼ガス流量に比して、その中
の黒煙粒子を十分吸着できる水分の気化量が得ら
れること。及び気化水分の気化位置が黒煙粒子の
吸着とそれに基くストーブ内処理に適する位置で
あつて、ストーブ内の燃焼ガス流路上に他の障害
を来さないこと等が要求される。 In this way, the black smoke particles contained in the combustion gas passing through the secondary combustion tube 5 are adsorbed to the vaporized moisture,
In some cases, it may be possible to process it within the stove and avoid discharging it outside the stove as much as possible. However, in order for this technical idea to be effectively utilized, the amount of vaporized water that can sufficiently adsorb the black smoke particles in the secondary combustion cylinder must be obtained compared to the flow rate of the combustion gas flowing in the secondary combustion cylinder. It is also required that the vaporization position of the vaporized moisture is suitable for the adsorption of black smoke particles and the subsequent treatment within the stove, and that no other obstructions occur on the combustion gas flow path within the stove.
所が従来の組合わせ技術はこの点が十分解明さ
れていなかつた。従つて本考案の目的とする所
は、二次燃焼筒中に水分を気化せしめて燃焼ガス
中の黒煙粒子をその水分に吸着せしめ、もつて可
及的に燃焼ガス中の黒煙粒子等をストーブ外へ排
出しないようにするに当り、他に特別の工夫を与
えることなくストーブの燃焼に比例して十分な水
分の気化量が得られ、それ故に燃焼に比例して生
ずる燃焼ガス中の黒煙粒子をほとんど逃がす事な
く吸着可能とする手段を提供するにあり、而も水
分の気化位置を燃焼ガス中の黒煙粒子が水分に吸
着され易く、それ故にストーブ外にほとんどでる
ことなくストーブ内で処理し易い位置とできる手
段を提供するにある。 However, in the conventional combination technology, this point has not been fully elucidated. Therefore, the purpose of the present invention is to vaporize moisture in the secondary combustion cylinder and make the black smoke particles in the combustion gas adsorbed to the moisture, thereby reducing the black smoke particles in the combustion gas as much as possible. In order to prevent water from being discharged outside the stove, a sufficient amount of moisture can be vaporized in proportion to the combustion of the stove without any other special measures, and therefore black in the combustion gas produced in proportion to the combustion can be obtained. The purpose of the present invention is to provide a means for adsorbing smoke particles with almost no escaping, and to change the vaporization position of water so that the black smoke particles in the combustion gas are easily adsorbed by the water, so that they hardly come out of the stove and are absorbed into the stove. The purpose is to provide a location and means that allow easy processing.
次に添付図面に従がい本考案の実施例を詳述す
る。 Next, embodiments of the present invention will be described in detail with reference to the accompanying drawings.
第1図に於いて1は一次燃焼室であり上部に蓋
2が、下部の床3の下に一次空気供給口4が形成
されている。次いで5は一次燃焼室1の上部に連
らなる二次燃焼筒であり、一次燃焼室1の下部か
ら導出したガス抜き管6が二次燃焼筒5に接続さ
れていると共に、該二次燃焼筒5には二次空気供
給口7が形成されている。そして二次燃焼筒5の
他端には熱交換室8が接続され、この熱交換室8
の他方側上部には排気吸引フアン9を有する排気
筒10が接続されている。 In FIG. 1, reference numeral 1 denotes a primary combustion chamber, and a lid 2 is formed at the top, and a primary air supply port 4 is formed under a floor 3 at the bottom. Next, 5 is a secondary combustion tube connected to the upper part of the primary combustion chamber 1, and a gas vent pipe 6 led out from the lower part of the primary combustion chamber 1 is connected to the secondary combustion tube 5. A secondary air supply port 7 is formed in the cylinder 5 . A heat exchange chamber 8 is connected to the other end of the secondary combustion cylinder 5.
An exhaust pipe 10 having an exhaust suction fan 9 is connected to the upper part of the other side.
そして、二次燃焼筒5の下方に水タンク11を
設け、その水タンク11中の液W中に、下部が浸
漬せる気化管12を設け、その気化管12の上部
ノズル13を、二次燃焼筒7内に臨ませる。この
場合、上部ノズル13は、二次燃焼筒5の最も下
流位置に開口すると共に、ノズル13の開口部が
熱交換室8の方に向くようにして配設される。加
えて水タンク11を熱交換室8の壁面に隣接さ
せ、熱交換室8からの伝導伝熱によつて水タンク
11中の水Wの蒸発を可能にする。勿論、一次燃
焼室1からの放射熱によつても水タンク11中の
水Wは加熱される。更に熱交換室8内に、複数の
邪魔板14,15を上下に配し、複数のガス通路
16,17,18を形成する。この場合、邪魔板
14,15の内、燃焼ガスの流れ方向に沿つて第
1番目に位置する邪魔板14は、上記二次燃焼筒
5の出口近くに対向させ、且つその邪魔板14を
上から下へ向けて配設する。そして、第1番目の
ガス通路16あたりの下方底部に、外部から挿脱
できる燃焼ガス中の黒煙粒子等の収集皿19を設
ける。外部から挿脱できるようにするには、熱交
換室8の下方底部に開閉板を設け、それを開閉す
ることによつて収集皿19を引出式に挿脱するよ
うにする例を上げることができる。 A water tank 11 is provided below the secondary combustion tube 5, a vaporization pipe 12 is provided whose lower part is immersed in the liquid W in the water tank 11, and the upper nozzle 13 of the vaporization pipe 12 is connected to the secondary combustion pipe 12. Face the inside of tube 7. In this case, the upper nozzle 13 opens at the most downstream position of the secondary combustion cylinder 5 and is arranged such that the opening of the nozzle 13 faces toward the heat exchange chamber 8 . In addition, the water tank 11 is placed adjacent to the wall surface of the heat exchange chamber 8, so that the water W in the water tank 11 can be evaporated by conductive heat transfer from the heat exchange chamber 8. Of course, the water W in the water tank 11 is also heated by the radiant heat from the primary combustion chamber 1. Furthermore, a plurality of baffle plates 14, 15 are arranged above and below in the heat exchange chamber 8, and a plurality of gas passages 16, 17, 18 are formed. In this case, the baffle plate 14 located first among the baffle plates 14 and 15 along the flow direction of the combustion gas is opposed to the outlet near the outlet of the secondary combustion cylinder 5, and the baffle plate 14 is placed upward. Place it from the bottom down. A collection tray 19 for collecting black smoke particles in the combustion gas is provided at the bottom of the first gas passage 16, which can be inserted and removed from the outside. In order to be able to insert and remove it from the outside, it is possible to provide an opening/closing plate at the lower bottom of the heat exchange chamber 8, and by opening and closing it, the collection pan 19 can be inserted and removed in a pull-out manner. can.
このような構成に基き、燃焼動作を説明する。 The combustion operation will be explained based on such a configuration.
蓋2を用いて、先ず廃タイヤチツプT等の廃棄
固形物を投入すると共に着火用の紙P等を投入
し、着火する。すると、一次空気供給口4からの
一次空気の供給を受けて酸化燃焼が開始され、燃
焼ガスが二次燃焼筒5の方へ向かう。他方一次燃
焼室1の下方へ溜まるガスの一部はガス抜き管6
を介して、同じように二次燃焼筒5へ向流する。
二次燃焼筒5に於いては、二次空気供給口7から
二次空気が供給されているので、よりよく再燃焼
される。そして、熱交換室8へ流入する前に、水
タンク11中の液Wが熱交換室8からの伝導伝熱
によつて、且つ周囲からの放射伝熱により蒸発せ
しめられて、気化管12を介してノズル13より
蒸気となつて二次燃焼筒5内へ吸引流出している
ので、上記の二次燃焼筒5内を通る燃焼ガスとこ
の蒸気がここで混合される。即ち、第2図に示す
如く廃棄物を燃焼させた時の燃焼ガス中には黒煙
粒子、亜硫酸ガス成分粒子Aが含まれているが、
それらの粒子Aは、水蒸気Bに接触せしめられる
ことにより、その水蒸気粒子の中に溶解し、吸着
される。この場合、燃焼ガス及びその中の黒煙粒
子の発生量は燃焼時間、燃焼の大小に比例する。
他方熱交換室8の伝導伝熱により蒸発する水分量
も燃焼時間、燃焼に大小に比例する。故に発生黒
煙粒子に対して、その黒煙粒子を吸着するに都合
の良い気化水分の量を設定し易く、黒煙粒子又は
水分の何れか一方が他に対して過剰になることも
なく、ほとんど吸着される。そして、それら黒煙
粒子と蒸気成分が互いに吸着しあつたものが、燃
焼ガスと共に熱交換室8に流入するものの、先ず
邪魔板14による邪魔もあつて、そのまま排気筒
10の方へ吸引排出されず、熱交換室8の下方へ
落下し、収集皿19上に捕集される。従つて悪臭
成分等を除かれた燃焼ガスのみが、ガス通路1
6,17を経て排気筒10内を通り、排気吸引フ
アン9によつて外部へ排出されるものである。こ
れらにより室内の空気が熱交換室8と対流接触し
暖められ、且つストーブ全体の放射熱により室内
が暖められる。そして、排気固形物を燃焼した時
に生ずる悪臭成分や、有害成分が可及的に除去さ
れるので、周囲環境を汚すこともなく、且つ室内
へ悪臭等を放出しないので、使い易いものであ
る。 Using the lid 2, firstly, waste solid materials such as waste tire chips T are put in, and paper P for ignition is also put in and ignited. Then, primary air is supplied from the primary air supply port 4, oxidative combustion is started, and the combustion gas is directed toward the secondary combustion tube 5. On the other hand, some of the gas that accumulates below the primary combustion chamber 1 is removed by the gas vent pipe 6.
Similarly, it flows counter-currently to the secondary combustion cylinder 5 via.
In the secondary combustion cylinder 5, secondary air is supplied from the secondary air supply port 7, so that re-combustion is better performed. Then, before flowing into the heat exchange chamber 8, the liquid W in the water tank 11 is evaporated by conduction heat transfer from the heat exchange chamber 8 and radiant heat transfer from the surroundings, and the vaporization tube 12 is evaporated. Since the steam is drawn and discharged from the nozzle 13 into the secondary combustion cylinder 5 through the nozzle 13, the combustion gas passing through the secondary combustion cylinder 5 and this steam are mixed here. That is, as shown in Fig. 2, the combustion gas when waste is combusted contains black smoke particles and sulfur dioxide gas component particles A;
When these particles A are brought into contact with water vapor B, they are dissolved in the water vapor particles and adsorbed therein. In this case, the amount of combustion gas and black smoke particles generated therein is proportional to the combustion time and the size of combustion.
On the other hand, the amount of water evaporated by conductive heat transfer in the heat exchange chamber 8 is also proportional to the combustion time and combustion. Therefore, it is easy to set the amount of vaporized moisture that is convenient for adsorbing the generated black smoke particles, and there is no possibility that either the black smoke particles or the moisture will be excessive compared to the other. Almost absorbed. The black smoke particles and vapor components adsorbed to each other flow into the heat exchange chamber 8 along with the combustion gas, but are first blocked by the baffle plate 14 and are sucked and discharged directly toward the exhaust stack 10. First, it falls below the heat exchange chamber 8 and is collected on the collection pan 19. Therefore, only the combustion gas from which malodorous components have been removed enters the gas passage 1.
6 and 17, the exhaust pipe 10, and is discharged to the outside by the exhaust suction fan 9. As a result, indoor air comes into convective contact with the heat exchange chamber 8 and is warmed, and the room is warmed by the radiant heat of the entire stove. Moreover, the malodorous components and harmful components produced when the exhaust solids are burned are removed as much as possible, so that the surrounding environment is not polluted, and no malodors are emitted into the room, making it easy to use.
加えて、上記気化管12のノズル13は二次燃
焼筒5の最下流近くにあるので、水分に吸着され
た黒煙粒子等が二次燃焼筒5内に落下してそこに
溜留するおそれがない。 In addition, since the nozzle 13 of the vaporizer pipe 12 is located near the most downstream side of the secondary combustion tube 5, there is a risk that black smoke particles etc. adsorbed by moisture may fall into the secondary combustion tube 5 and accumulate there. There is no.
第3図に示す例は、熱交換室8内に、3つの邪
魔板20,21,22を配し且つ気化管12を液
W中に浸漬しないようにしたものであつて、この
例の場合も先の例と実質的に同一である。又第4
図に示す例は、水タンク23を二次燃焼筒5の周
りに配すると共に気化管24の水タンクの液W中
に浸漬する部分にジエツト孔25の複数を形成し
たものであつて、この例の場合も先の例と実質的
に同一である。 In the example shown in FIG. 3, three baffle plates 20, 21, and 22 are arranged in the heat exchange chamber 8, and the vaporizing tube 12 is prevented from being immersed in the liquid W. is also substantially the same as the previous example. Also the fourth
In the example shown in the figure, a water tank 23 is arranged around the secondary combustion tube 5, and a plurality of jet holes 25 are formed in the part of the vaporizing pipe 24 that is immersed in the liquid W of the water tank. The example case is also substantially the same as the previous example.
以上詳述した如くこの考案はによれば、燃焼ガ
ス中の黒煙粒子を蒸発水分に吸着可能であつてス
トーブ外へ可及的に排出させないことは勿論のこ
と、気化管12を介して気化する水分は、熱交換
室8の伝導伝熱によつて主に可能にされ、この熱
交換室8の伝導伝熱量はストーブ全体の燃焼時間
や燃焼の大小に比例する。故に水分気化量は燃焼
の状態に比例する。他方燃焼ガス中の黒煙粒子の
発生も燃焼時間やその大小に比例する。故に黒煙
粒子を十分吸着するのに都合の良い水分気化量を
定め易く、燃焼ガス中の黒煙粒子のストーブ外へ
の排出を可及的に抑制できる。加えて、二次燃焼
筒5の最下流近くに気化管12のノズル13があ
り、その出口に対向して第一の邪魔板が位置する
ので、水分に対して黒煙粒子が吸着され易く、而
もその下方に収集皿19があるからより良く収集
し易い。これらのことから燃焼ガス中の黒煙粒子
をよりよく排除しやすい。 As detailed above, according to this invention, the black smoke particles in the combustion gas can be adsorbed to the evaporated moisture, and not only can they be prevented from being discharged outside the stove as much as possible, but they can also be vaporized through the vaporization pipe 12. This moisture is mainly made possible by conductive heat transfer in the heat exchange chamber 8, and the amount of conductive heat transfer in the heat exchange chamber 8 is proportional to the overall combustion time of the stove and the size of combustion. Therefore, the amount of moisture vaporized is proportional to the state of combustion. On the other hand, the generation of black smoke particles in the combustion gas is also proportional to the combustion time and its size. Therefore, it is easy to determine the amount of water vaporization that is convenient for sufficiently adsorbing black smoke particles, and the emission of black smoke particles in the combustion gas to the outside of the stove can be suppressed as much as possible. In addition, the nozzle 13 of the vaporizer pipe 12 is located near the most downstream side of the secondary combustion tube 5, and the first baffle plate is located opposite the outlet of the nozzle 13, so that black smoke particles are easily absorbed by moisture. Moreover, since there is a collecting tray 19 below it, it is easier to collect the waste. For these reasons, black smoke particles in the combustion gas can be better removed.
添付図面は本考案の実施例を示し、第1図は第
一の実施例を示す縦断側面図、第2図は要部拡大
図、第3図は第二の実施例を示す縦断側面図、第
4図は第三の実施例を示す縦断側面図であり、図
中1は一次燃焼室、4は一次空気供給口、5は二
次燃焼筒、6はガス抜き管、7は二次空気供給
口、8は熱交換室、9は排気吸引フアン、10は
排気筒、11は水タンク、12は気化管、13は
ノズル、14,15は邪魔板、19は収集皿、2
0,21,22は邪魔板、23は水タンク、24
は気化管、25はジエツト孔、Pは紙、Tは廃タ
イヤチツプ等の廃棄固形物、Wは水、Aは黒煙粒
子等の成分、Bは水蒸気である。
The accompanying drawings show embodiments of the present invention, FIG. 1 is a longitudinal side view showing the first embodiment, FIG. 2 is an enlarged view of the main parts, and FIG. 3 is a longitudinal side view showing the second embodiment. FIG. 4 is a longitudinal side view showing the third embodiment, in which 1 is a primary combustion chamber, 4 is a primary air supply port, 5 is a secondary combustion tube, 6 is a gas vent pipe, and 7 is a secondary air Supply port, 8 is a heat exchange chamber, 9 is an exhaust suction fan, 10 is an exhaust pipe, 11 is a water tank, 12 is a vaporization pipe, 13 is a nozzle, 14, 15 is a baffle plate, 19 is a collection pan, 2
0, 21, 22 are baffle plates, 23 is a water tank, 24
25 is a vaporizer tube, 25 is a jet hole, P is paper, T is a waste solid such as waste tire chips, W is water, A is a component such as black smoke particles, and B is water vapor.
Claims (1)
空気7供給口が形成された二次燃焼筒5を介して
連らなる熱交換室8と、該熱交換室8に連らなる
排気吸引フアン9を有する排気筒10より成り、
上記一次燃焼室1の底部と二次燃焼筒5の間には
ガス抜き管6が連結されて成る廃棄物の燃焼スト
ーブであつて、上記二次燃焼筒5に気化管12を
設けた廃棄物の燃料ストーブに於いて; 上記気化管12のノズル13を上記二次燃料筒
5の最下流近くに設けると共に、気化管12の下
部が連なる水タンク11を上記熱交換室8の壁面
に隣接して設け、而も熱交換室8に配設されたガ
ス通路を区画する為の複数の邪魔板の内、燃焼ガ
スの流れ方向に沿つて第1番目に位置する邪魔板
は、上記二次燃焼筒5の出口近くに対向させて上
から下へ向けて配設されて成り、燃焼ガス中の黒
煙粒子等の収集皿19は上記の第1番目の邪魔板
が区画する第一の燃焼ガス通路の下方に配設され
ている事を特徴とする廃棄物の燃焼ストーブ。[Claims for Utility Model Registration] A primary combustion chamber 1, a heat exchange chamber 8 connected to the primary combustion chamber 1 via a secondary combustion tube 5 in which a secondary air 7 supply port is formed; It consists of an exhaust pipe 10 having an exhaust suction fan 9 connected to a heat exchange chamber 8,
This is a waste combustion stove in which a gas venting pipe 6 is connected between the bottom of the primary combustion chamber 1 and the secondary combustion cylinder 5, and the secondary combustion cylinder 5 is provided with a vaporizing pipe 12. In the fuel stove; the nozzle 13 of the vaporizing pipe 12 is provided near the most downstream side of the secondary fuel cylinder 5, and the water tank 11 connected to the lower part of the vaporizing pipe 12 is arranged adjacent to the wall surface of the heat exchange chamber 8. Among the plurality of baffle plates arranged in the heat exchange chamber 8 for partitioning the gas passages, the baffle plate located first along the flow direction of the combustion gas is used for the secondary combustion. The collecting tray 19 for collecting black smoke particles in the combustion gas is arranged facing the tube 5 near the outlet from above and facing downward. A waste combustion stove characterized by being disposed below a passageway.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP7430684U JPS60185838U (en) | 1984-05-21 | 1984-05-21 | waste combustion stove |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP7430684U JPS60185838U (en) | 1984-05-21 | 1984-05-21 | waste combustion stove |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS60185838U JPS60185838U (en) | 1985-12-09 |
| JPH0212434Y2 true JPH0212434Y2 (en) | 1990-04-09 |
Family
ID=30614478
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP7430684U Granted JPS60185838U (en) | 1984-05-21 | 1984-05-21 | waste combustion stove |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS60185838U (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108954340B (en) * | 2018-07-24 | 2020-08-07 | 台州市黄岩五星车业有限公司 | Plastic refuse burns purification integral type's refuse treatment device |
Family Cites Families (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS4925028A (en) * | 1972-06-29 | 1974-03-06 | ||
| JPS4973734A (en) * | 1972-11-20 | 1974-07-16 | ||
| JPS4972963A (en) * | 1972-11-20 | 1974-07-15 | ||
| JPS5059844A (en) * | 1973-09-27 | 1975-05-23 | ||
| JPS5220793A (en) * | 1975-08-11 | 1977-02-16 | Goro Matsumoto | Display purpose discharge lamp |
| JPS5540405Y2 (en) * | 1976-03-25 | 1980-09-20 |
-
1984
- 1984-05-21 JP JP7430684U patent/JPS60185838U/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS60185838U (en) | 1985-12-09 |
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