JPS597880A - Drier - Google Patents

Drier

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Publication number
JPS597880A
JPS597880A JP11619982A JP11619982A JPS597880A JP S597880 A JPS597880 A JP S597880A JP 11619982 A JP11619982 A JP 11619982A JP 11619982 A JP11619982 A JP 11619982A JP S597880 A JPS597880 A JP S597880A
Authority
JP
Japan
Prior art keywords
gas
drying
chamber
exhaust gas
combustion
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
JP11619982A
Other languages
Japanese (ja)
Inventor
神成 照雄
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.)
Nippon Furnace Co Ltd
Original Assignee
Nippon Furnace 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 Nippon Furnace Co Ltd filed Critical Nippon Furnace Co Ltd
Priority to JP11619982A priority Critical patent/JPS597880A/en
Publication of JPS597880A publication Critical patent/JPS597880A/en
Pending legal-status Critical Current

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  • Drying Of Solid Materials (AREA)

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 など気体燃料であって該気体燃料の燃焼排ガスの硫黄分
含有量は零に近く、かつ石油臭もないことが条件である
。該気体燃料の燃焼拶「ガスの適徽金乾燥室へ供給する
ことによって乾燥熱エネルギーの節約を図った乾燥装置
である。本発明の乾燥装置においては、熱全放敗する燃
焼室と気体燃料用バーナと排ガス肯よシなる燃焼装置全
独立的に設けることにより気体燃料の燃焼が加温室の圧
力などで影響されることなく常に一定栄注下で円滑に行
なわnるようにし、かつ燃′fa停止中VCたとえ気体
7認科用バーナからガス伐れかめってもガス燃料は燃焼
室から排ガス官全通って外気へ放出され、〃0温室や乾
燥室へ流入きれないようにして再び点火するときに加温
室や乾燥室で爆発が生じないようにし、かつ高温燃焼排
ガスの一部適量を乾燥室へ1〔1僧供給して熱工不ルギ
ーの節約を図るようにし、この場会炎は乾燥室へ入らな
いようにして被乾燥物への引火を防き゛、乾燥室へ送シ
込まれる燃焼リ1ガスが適量だけ混合された気体は空気
および循環気体と充分に混合した後に乾燥室へ供給する
ようにして乾燥室内で局部的に高温の部分やCOやCO
。の高濃度の部分が生ぜず乾燥室内の破乾燥吻?一律に
乾燥するとともに乾′媚¥内に入って作業する作業員が
酸欠や一酸化炭素中毒にならないようにしている。
DETAILED DESCRIPTION OF THE INVENTION It is a gaseous fuel such as the following conditions: the sulfur content of the combustion exhaust gas of the gaseous fuel is close to zero and there is no petroleum odor. This is a drying device which aims to save drying heat energy by supplying the combustion gas to the drying chamber. By providing a completely independent combustion device with a combustion burner and exhaust gas control, the combustion of gaseous fuel can be carried out smoothly under a constant flow rate without being affected by the pressure of the heating chamber. Even if the gas is exhausted from the gas burner during fa stop, the gas fuel will be released from the combustion chamber to the outside air through the exhaust gas pipe, and will be ignited again after preventing it from flowing into the greenhouse or drying room. When drying, make sure that no explosion occurs in the heating chamber or drying chamber, and supply an appropriate amount of high-temperature combustion exhaust gas to the drying chamber in order to save on thermal energy. To prevent ignition of the materials to be dried, prevent the substances from entering the drying chamber, and the gas mixed with an appropriate amount of combustion gas sent to the drying chamber should be thoroughly mixed with air and circulating gas before entering the drying chamber. By supplying CO and CO to locally high temperature areas in the drying room.
. Is the high concentration part of the dried proboscis in the drying room not produced? This ensures uniform drying and prevents workers working inside the dry area from oxygen deprivation and carbon monoxide poisoning.

なお本絹2の発明は乾燥室に温度および気体成分の測定
手段金膜けてガスバーナおよびも調節弁を制御し、かつ
供給きれる乾燥用気体は乾燥室内均一に配給されるよう
にしてろるので乾燥を有効に行わしめ、最尚PM灰にま
で高温の排ガス全乾腺室へ供給することr得しめて熱工
不ルギーの節約が行われかつ作業員が衛生上安全でるる
ように管理した乾燥装置でるる。
In addition, the invention of Honsilu 2 uses a gold film as a means for measuring temperature and gas components in the drying chamber to control the gas burner and the control valve, and the drying gas that can be supplied is evenly distributed within the drying chamber. A drying device that is managed to effectively carry out the process and to supply high-temperature exhaust gas, even PM ash, to the total drying chamber, thereby saving on heat engineering costs and ensuring sanitary safety for workers. Out.

本発明τその実施例ケ示す図によって説明する。The present invention τ will be explained with reference to the drawings showing its embodiments.

不姥明の乾燥装置においては、LPガスあるいは都市ガ
スなど含有饋黄分が少なくかつ石油臭がなく仮乾燥物に
悪影=#全与えない清浄な気体燃料が使用芒扛ることが
条件であってこのような気体燃料用ノくーナ1が使用さ
れる。乾燥室12や加温室4と独立的に気体燃料用バー
ナ1と熱?放散する燃焼室3と排ガス青2とによって構
成される燃焼装置を設ける。この燃焼装置の燃焼室3勿
包むようにして〃目温室4を設ける。すなわち、燃焼室
3内で燃焼が行われるとその燃m熱が燃焼室3から加温
¥4内に放故ざγして該加温室4内ケ流扛る気体が加温
される。該加温室4に気体取入口5と11固徒た(l−
J:fji.数1固の気1本取出口6。
In Fubamei's drying equipment, it is necessary to use a clean gaseous fuel such as LP gas or city gas that has a low sulfur content, does not have a petroleum odor, and does not have a negative impact on the temporarily dried product. Therefore, such a gas fuel nozzle 1 is used. Gaseous fuel burner 1 and heat independently of drying room 12 and heating room 4? A combustion device is provided which is constituted by a combustion chamber 3 and exhaust gas blue 2 which dissipates. A greenhouse 4 is provided so as to enclose the combustion chamber 3 of this combustion device. That is, when combustion occurs in the combustion chamber 3, the heat of the combustion is released from the combustion chamber 3 into the heating chamber 4, thereby warming the gas flowing inside the heating chamber 4. Gas intake ports 5 and 11 were installed in the heating chamber 4 (l-
J:fji. Number 1 koku 1 qi outlet 6.

6′・・・ケ設け、また逍描な1i.直に1基または数
基のファン14.14’・・・全設ける。これらファン
によって加温室4の気体取入口5の位置は若干負圧に保
たれるようにし、またこれらファンによって7JO温室
4内全流nて加温きれ乾燥室12へ供給される気体が攪
拌され混合され該加温室ヰの取出1」6から取出さnる
気体は均一な温度および成分組成となって乾燥室12へ
供給されるようにする。供給源を外に設けかつ空気量調
節弁8ケ有する空気供給#7と排ガス管2から分岐さ扛
、かつ琲ガス量調節弁10を有する排ガス供給管9と供
給源が乾燥室12であってかつ循環気体量調節弁13ケ
有する循環気体供給管11はいづれもその排出端が該別
(Ir+i室4の気体取入口5位置であるようにして設
ける。既述のごとく該気体取入口5位置はファン14に
よって常に若干負の賦圧に保M−Jれているから、各供
給管7、9・、11から加温室4へは容易に空気。
6'... is provided, and a detailed 1i. Directly provide one or several fans 14, 14'...all. The position of the gas intake port 5 of the heating chamber 4 is maintained at a slightly negative pressure by these fans, and the gas supplied to the heated drying chamber 12 through the entire flow inside the 7JO greenhouse 4 is agitated by these fans. The mixed gases taken out from the heating chamber 16 are supplied to the drying chamber 12 with a uniform temperature and composition. The air supply #7 is provided outside and has eight air volume control valves, and the exhaust gas supply pipe 9 is branched from the exhaust gas pipe 2 and has a gas volume control valve 10, and the supply source is the drying chamber 12. In addition, each of the circulating gas supply pipes 11 having 13 circulating gas amount control valves is installed so that its discharge end is at the gas intake port 5 position of the corresponding (Ir+i chamber 4). Since M-J is always maintained at a slightly negative pressure by the fan 14, air easily flows from each supply pipe 7, 9, .

排ガス,循環気体が流入し、そ牡らの量はそれぞ扛調節
弁8、10、13によって直接的独立的に調節すること
ができる。
Exhaust gas and circulating gas flow in, the amounts of which can be adjusted directly and independently by control valves 8, 10, 13, respectively.

加温室4内では供給さ汎た適・量の空気と適量の排ガス
と適量の画壇気体がファン14゜14’、 14″・・
・によって均一に混合され、燃焼室3の熱放赦によって
所定の温度まで加温ざnlかように均一な所定温度所定
成分刊戒になった気体はファン14’ 、 14“・・
・によって賦勢されてそれぞれ気体取出管6,6′・・
・から排出され、それぞれ乾燥室12に至る乾燥用気体
供給’ft15.15’・・・にょって気送され、そn
ぞれの供給官に設けた1制吐たは複数個の噴出孔16.
16’・・・から乾燥室12内へ供給式れる。
Inside the heating room 4, an appropriate amount of air, an appropriate amount of exhaust gas, and an appropriate amount of gas are supplied by fans 14゜14', 14''...
The gas, which has been uniformly mixed by the combustion chamber 3 and heated to a predetermined temperature by heat release in the combustion chamber 3, is heated to a uniform predetermined temperature and predetermined composition by the fans 14', 14''...
・The gas outlet pipes 6, 6', . . .
The drying gas supply 'ft15.15' is discharged from the drying chamber 12, respectively, and pneumatically blown by the drying gas supply 'ft15.15'.
One or more spout holes 16 for each feeder.
16'... into the drying chamber 12.

該乾燥室12内の一部気体は既述のごとく循環気体量調
節弁13を有する循環気体供給管11を通って再び加温
室4へ供給されるが、他部気体は排風量調節弁18を有
する排風量17を通って外気へ放出される。
A part of the gas in the drying chamber 12 is supplied to the heating chamber 4 again through the circulating gas supply pipe 11 having the circulating gas amount regulating valve 13 as described above, but the other part of the gas is supplied through the exhaust air quantity regulating valve 18. The air is discharged to the outside air through an exhaust air volume 17.

上記の基本発明に関連の第2の発明は上述の乾燥”A 
fitにおいて乾燥室12内に4度・成分組成などの測
定手段19全設けて測定を行い、その測走値にもとづき
バーナ1および各調節弁8.1υ1.13.1 Bに電
気信号の指令r送って燃焼量、排ガス量、空気量、循猿
気体量、排風量などケそれぞれ′mに4量でるるように
自動制岬するようにした乾燥装置でるる。
The second invention related to the above basic invention is the above-mentioned drying “A”.
In the drying chamber 12, all measurement means 19 are installed to measure 4 degrees, component composition, etc., and based on the measured values, an electric signal command r is sent to the burner 1 and each control valve 8.1υ1.13.1B. There is a drying device that automatically controls the combustion amount, exhaust gas amount, air amount, circulating gas amount, exhaust air amount, etc. so that each amount is 4 times a meter.

本発明の乾燥装置においては加11に設けるファン14
,14’、14“・・・の作用によって先づ加温室4の
少くとも気体取入口5の位置における圧力を常に、所足
景だけ大気圧よシ低い圧力に保つこと’(r (42,
Lめる。これによって各調冥百弁11,10.13を調
節して直接的に正確に空気量、排ガス1往、備壌気体量
′ff:調節することができる。もし気体取入口5の位
置の圧力が大気圧より高ければ、たとえば排ガス量ケ調
節しようとすれば排ガス管2の分岐点より外側位置にダ
ンパーを設け、従って排カス供給管の排ガス電音間接的
に調節することになる。この場合は燃焼室3も大気圧よ
り高い圧力となり、気体燃料用バーナ1に供ija烙I
しる空気の供給量が気体燃料供給量に比し少なくなるこ
とが生じやすくかように空気不足の状、四で不完全燃焼
が生じ、煤が発生し、COが多量になる。
In the drying apparatus of the present invention, a fan 14 provided in addition 11
, 14', 14"... to keep the pressure at least at the gas intake port 5 of the heating chamber 4 at a pressure lower than the atmospheric pressure at all times' (r (42,
L. As a result, it is possible to directly and accurately adjust the amount of air, the amount of exhaust gas, and the amount of stored gas 'ff: by adjusting each adjustment valve 11, 10.13. If the pressure at the gas intake port 5 is higher than atmospheric pressure, for example, to adjust the amount of exhaust gas, a damper is installed outside the branch point of the exhaust gas pipe 2, so that the exhaust gas electric sound in the exhaust gas supply pipe is indirectly suppressed. It will be adjusted to. In this case, the combustion chamber 3 also has a pressure higher than atmospheric pressure, and the combustion chamber 3 is supplied to the gaseous fuel burner 1.
The amount of air supplied tends to be smaller than the amount of gaseous fuel supplied, and as a result of insufficient air, incomplete combustion occurs, soot is generated, and a large amount of CO is produced.

また大気圧より高い取入口5がら空気や循環気体ケ所定
量取入れるためには、そnぞれ調節弁のほかにファンケ
設けて圧力を高めなければならず、非常に複雅な構造と
なる。
In addition, in order to take in a predetermined amount of air or circulating gas through the intake port 5 whose pressure is higher than atmospheric pressure, it is necessary to provide a fan in addition to a control valve to increase the pressure, resulting in a very complicated structure.

また加湿室4に設けるファン14.14’。Additionally, fans 14 and 14' are provided in the humidifying chamber 4.

14″・・・は攪拌機能ケ有し、す1ガスと空気と循環
気体を完乍に混合して一足の成分組成と一定の温度にし
て取出・庁6から排出させることかできる。−また該乾
燥室12内で乾燥用気体供給官1b、15’・・・およ
びそ扛らの噴出孔16゜16′・・・の配置および循環
気体供給管11の気体吸込口およびすF)載置17を適
当に配管して乾燥室12内の雰囲気をはシーだの温度お
よび気体成分にすることができる。従って前記側だ手段
19は1基丑たは比較的少ない数で跋乾探至12内の装
部の41州気全正確に知ることができ、適当な判IAf
? k下すことができる。従って該乾燥室12内で作業
をする作業員が酸欠や一酸化炭素中毒を起すことなく安
全に作業音することができる。同時に気体燃料用バーナ
IK供給する燃料量をW・1節して常に燃焼室3にかい
て適量の負荷で燃焼させて燃料の無駄1更いを防止する
ことが′できる。かつ800℃乃至500℃の高温排ガ
スを大気中に全量放出することなく、乾燥室1zに2け
る作業員に上述の衛生上の危険が生じない限度の最大量
排ガスを直接的に1ん燥室12へ供給することができる
。またこの排ガスは加温室4ヶ通る間によく混合きれて
いる。一旦完全に混合された混合気体は乾燥室12に主
って分離されることはない。もし上述のファンによる混
合全元分に行わないで排ガスの直接的な乾燥室への供給
を行えばり1ガスは高温であるから乾燥室上部にす1ガ
ス一度の高い部分が発生し、この場合はたとえ少1杖の
排ガス利用でhつても作業員に俯生上の危険が発生し、
かつ乾′R室内における乾燥が均一に能率よく行わ才′
しなくなる。
14''... has a stirring function, and can completely mix gas, air, and circulating gas to a uniform composition and a constant temperature, and can be taken out and discharged from the chamber 6. In the drying chamber 12, the arrangement of the drying gas supply members 1b, 15'... and their ejection holes 16, 16', and the gas suction port of the circulating gas supply pipe 11 and the mounting 17 can be properly piped to adjust the atmosphere in the drying chamber 12 to the same temperature and gas composition as the drying chamber.Therefore, the side means 19 can be used with only one or a relatively small number of drying means 12. You can accurately know all 41 state Qi of the inner parts, and find the appropriate size IAf.
? k can be lowered. Therefore, workers working in the drying chamber 12 can safely work without suffering from oxygen deficiency or carbon monoxide poisoning. At the same time, the amount of fuel supplied to the gaseous fuel burner IK can be set to W.1, so that it is always drawn into the combustion chamber 3 and combusted with an appropriate amount of load, thereby preventing fuel waste. In addition, without releasing the entire amount of high-temperature exhaust gas of 800°C to 500°C into the atmosphere, the maximum amount of exhaust gas that does not pose the above-mentioned sanitary hazard to the workers in the drying room 1z is directly transferred to the drying room 1z. 12. Moreover, this exhaust gas was thoroughly mixed while passing through the four heating chambers. Once completely mixed, the gas mixture is not separated into the drying chamber 12. If exhaust gas is directly supplied to the drying chamber without mixing all the elements using the fan mentioned above, a high temperature area of 1 gas will be generated in the upper part of the drying chamber because 1 gas is high temperature. Even if only a small amount of exhaust gas is used, it poses a serious health hazard to workers.
Also, drying in the drying room can be done uniformly and efficiently.
I won't.

本xA明に係る乾燥装置は魚類の乾燥、海苔の乾燥、タ
バコの巣の乾深、製茶用2茸頬の乾燥9煎餅の乾燥、あ
るいは壁装作業などに使用することができ、無害、無臭
の高温燃焼排ガスの一部適量會乾燥堅内に流すことによ
って大巾な省エネルギー全図ることができる。
The drying equipment according to this xAme can be used for drying fish, drying seaweed, drying tobacco nests, drying mushroom cheeks for tea making, drying rice crackers, or wall covering work, etc., and is harmless and odorless. By channeling an appropriate amount of the high-temperature combustion exhaust gas into the dry chamber, a large amount of energy can be saved.

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

図は本発明に・隆る乾燥装置てめる。 1は気体燃料用バーナ 2は排ガス管 3は燃焼至 4
は加諷室 5は気体取入口 6は気体取出口 7は空気
供給・U 8は空気量調ゴi)弁 9fd排ガス供給′
肯 10は排ガス量調節弁 11は循環気体供給管 1
2は乾燥室 13は循環気体量調節弁 14はファン1
5は乾燥用気体供給庁 16は噴出孔17は排風管 1
8は排風量調節弁 19は側矩手段
The figure shows a drying device according to the present invention. 1 is a gaseous fuel burner 2 is an exhaust gas pipe 3 is a combustion pipe 4
is the adjustment chamber 5 is the gas intake port 6 is the gas outlet port 7 is the air supply/U 8 is the air volume adjustment valve 9fd Exhaust gas supply'
10 is the exhaust gas amount control valve 11 is the circulating gas supply pipe 1
2 is a drying chamber 13 is a circulating gas amount control valve 14 is a fan 1
5 is a drying gas supply agency 16 is a blowout hole 17 is an exhaust pipe 1
8 is an exhaust air volume control valve 19 is a side rectangular means

Claims (1)

【特許請求の範囲】 ■ 気体燃料用バーナ1と熱を放散する燃焼室3と排ガ
ス管2を有する燃焼装置を設け、核熱を放散する燃焼室
3を包んで加温室4を設け、該力1温至4に気体収入口
5と1個または数個の気体取出口6,6′・・・r設け
、草気量調節弁8を有する空気供給管7と前1把排ガス
看2から分岐されかつ排ガス量調節外10を有する排カ
ス供給管9と供給端か°′乾燥室12でめジ、かつ菌環
気体妙調節弁13を有する循環気体供給計11をいづれ
も刊出端が該気体取出口5に至るようにして設け、該加
温室4に1基または数基のファン14.14’・・・金
設けて該加温至4の気体取入[コ5の位置は常に負圧に
保たれるようにし、該気体取出管も、6′・・・からそ
れぞ扛乾燥室12に至るl不乃至数本の乾燥用気体供給
・115.15’・・・牙設け、該乾燥室12に排風量
調]V1’i弁18を有する排風量17を設けた乾燥装
置。 2 気体燃料用バーナ1と熱全放散する燃焼室3と排ガ
ス管2を有する燃焼装置を設け、該熱全放散する燃焼室
3を包んで加温室4を設け、該〃目温室4に気体取入口
5と1個または数個の気体取出口6.6′・・・を設け
、空気調節弁8をMする空気供給管7と前記排ガス管2
から分岐されかつ排ガス量調節弁10ケ有する排ガス供
給前9と供給端が゛ 乾燥室12でめジ、かつ循環気体
量調節弁13?ll″有するイla m気体供給’1f
ll’にいづれも排出端が該気体取入口5に至るように
して設け、該加温室4に1基または数基のファン14.
14’・・・を設けて該加温室4の気体取入口5の位置
は常に負圧に保たれるようにし、該気体取出管6,6′
からそれぞれ乾燥室12に至る1本乃至数本の乾燥用気
体供給酢15,15’・・・全設け、該乾燥室12に排
颯鼠調節Jρ18ヶMするIJL風看17を設けた乾燥
装置において、該乾燥室12に温度・成分組成などの測
定手段19を設け、該測だ手段19からの電気信号によ
ってバーナ1および谷調節弁8.10.13.18が制
御はれるようにした乾燥装置。
[Claims] ■ A combustion device having a burner 1 for gaseous fuel, a combustion chamber 3 for dissipating heat, and an exhaust gas pipe 2 is provided, a heating chamber 4 is provided surrounding the combustion chamber 3 for dissipating nuclear heat, and a heating chamber 4 is provided surrounding the combustion chamber 3 for dissipating nuclear heat. A gas inlet port 5 and one or several gas outlet ports 6, 6'...r are provided in the first temperature range 4, and an air supply pipe 7 having an air flow control valve 8 is branched from the front 1 exhaust gas port 2. The exhaust gas supply pipe 9 and the exhaust gas supply pipe 9 having an exhaust gas amount adjustment valve 10 and the supply end are connected to each other in the drying chamber 12, and the circulating gas supply meter 11 having a microorganism gas adjustment valve 13 is connected to the outlet end thereof. One or more fans 14. The gas extraction pipes are also connected to one or more drying gas supply tubes from 6'... to the drying chamber 12. A drying device in which a drying chamber 12 is provided with an exhaust air volume 17 having an exhaust air volume control valve 18. 2 A combustion device having a burner 1 for gaseous fuel, a combustion chamber 3 for dissipating all heat, and an exhaust gas pipe 2 is provided, a heating chamber 4 is provided surrounding the combustion chamber 3 for dissipating all heat, and a gas intake is provided in the greenhouse 4. An air supply pipe 7 and the exhaust gas pipe 2 are provided with an inlet 5 and one or several gas outlet ports 6, 6', and an air control valve 8.
The exhaust gas supply front 9 and the supply end, which are branched from the drying chamber 12 and have 10 exhaust gas amount adjustment valves, are connected to each other in the drying chamber 12, and the circulating gas amount adjustment valve 13? ll″Ila m gas supply’1f
The heating chamber 4 is provided with one or several fans 14.
14'... are provided so that the position of the gas intake port 5 of the heating chamber 4 is always maintained at a negative pressure, and the gas outlet pipes 6, 6'
1 to several bottles of drying gas supply vinegar 15, 15' leading to the drying chamber 12, respectively. The drying chamber 12 is equipped with measuring means 19 for measuring temperature, component composition, etc., and the burner 1 and the valley control valves 8, 10, 13, and 18 are controlled by electric signals from the measuring means 19. Device.
JP11619982A 1982-07-06 1982-07-06 Drier Pending JPS597880A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11619982A JPS597880A (en) 1982-07-06 1982-07-06 Drier

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11619982A JPS597880A (en) 1982-07-06 1982-07-06 Drier

Publications (1)

Publication Number Publication Date
JPS597880A true JPS597880A (en) 1984-01-17

Family

ID=14681283

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11619982A Pending JPS597880A (en) 1982-07-06 1982-07-06 Drier

Country Status (1)

Country Link
JP (1) JPS597880A (en)

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4932960A (en) * 1972-07-25 1974-03-26
JPS5075091A (en) * 1973-10-24 1975-06-20

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4932960A (en) * 1972-07-25 1974-03-26
JPS5075091A (en) * 1973-10-24 1975-06-20

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