JPS5826906A - High-temperature air mixed steam generator - Google Patents

High-temperature air mixed steam generator

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Publication number
JPS5826906A
JPS5826906A JP12443481A JP12443481A JPS5826906A JP S5826906 A JPS5826906 A JP S5826906A JP 12443481 A JP12443481 A JP 12443481A JP 12443481 A JP12443481 A JP 12443481A JP S5826906 A JPS5826906 A JP S5826906A
Authority
JP
Japan
Prior art keywords
steam
air
pipe
heat
temperature
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.)
Granted
Application number
JP12443481A
Other languages
Japanese (ja)
Other versions
JPS6237282B2 (en
Inventor
北澤 幸男
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP12443481A priority Critical patent/JPS5826906A/en
Publication of JPS5826906A publication Critical patent/JPS5826906A/en
Publication of JPS6237282B2 publication Critical patent/JPS6237282B2/ja
Granted legal-status Critical Current

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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】 本発明は、燃料の燃焼による熱企水等の液体に伝えて蒸
気を発生させる装置に関し、目的とするところは、極め
て合理的で且つ安価な構成でもって乾き度の良い良質の
乾き蒸気2得るようにする事に依り、燃料の節約と装置
全体の小型化を図ることKある。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a device for generating steam by transmitting heat generated by combustion of fuel to a liquid such as water, and an object of the present invention is to reduce dryness with an extremely rational and inexpensive configuration. By obtaining high quality dry steam 2, it is possible to save fuel and downsize the entire device.

現在、工場等に於いて蒸気熱源として最も一般的に使用
されている小型の標準蒸気ボイラから発生する蒸気は、
湿り蒸気中の蒸気(気体)が占める重量的割合を示す乾
き度が極めて悪い邦 湿シ飽和蒸気が倉んどである。この水分の多い湿り飽和
蒸気を、工場等に於いて蒸気で仕事や処理或いは乾燥等
を行なわせる例えばプレス機や乾燥機等の蒸気使用機器
に供給するき、蒸気は機器内の空気に依って潜熱を奪わ
れて凝縮し、更に乾き度が悪くなり、湿り飽和蒸気の保
有熱量は其の乾き度に大きく左右されるから、一定蒸気
量当りの保有熱量が大幅に低下すると共に、湿シ飽和蒸
気の発生水分は機器の熱交換伝熱面等に厚いドレン層を
形成し、この飽和水は熱伝導率が非常に悪い。従って、
蒸気使用機器の熱吸収効率が大幅に低下してしまう為K
、多くの燃料を浪費すると共に装置全体の小型化を阻害
する要因となっている。一方、近年の蒸気ボイラは小型
化されていく傾向にあるが、其の保有水量が少なく、最
も熱を必要とする時にキャリオーバー現象が発生し易く
、乾き度が極端に悪くなって多くのドレン分を保有し、
熱交換時に必要な潜熱緻が少なくなる為に、通常は蒸気
ボイラを数台並設して使用する不経済なことが行なわれ
ている。
Currently, the steam generated from small standard steam boilers, which are most commonly used as steam heat sources in factories, etc.
Warehouses are saturated steam with extremely poor dryness, which indicates the proportion by weight of steam (gas) in the wet steam. This wet saturated steam with a high water content is supplied to steam-using equipment such as presses and dryers that use steam to perform work, processing, or drying in factories, etc., and the steam depends on the air inside the equipment. Latent heat is taken away and condensation occurs, which further deteriorates the dryness.The amount of heat held by wet saturated steam is greatly affected by its dryness, so the amount of heat held per constant amount of steam decreases significantly, and the dryness becomes worse. The moisture generated by steam forms a thick drain layer on the heat exchange and heat transfer surfaces of equipment, and this saturated water has very poor thermal conductivity. Therefore,
K because the heat absorption efficiency of steam-using equipment will be significantly reduced.
This wastes a lot of fuel and is a factor that hinders miniaturization of the entire device. On the other hand, steam boilers in recent years have tended to be smaller, but they hold less water and are prone to carryover when they need the most heat. hold the amount,
Since the amount of latent heat required during heat exchange is reduced, it is usually uneconomical to use several steam boilers in parallel.

本発明は、上記従来の問題点に鑑み、排力°ス熱を利用
して加熱した高温空気を湿り飽和蒸気に混合する極めて
合理的で且つ安価な構成であって、高温空気と湿り飽和
蒸気とを各々圧力調整弁に依って適度な混合比で混合す
る事に依り、従来の問題点?−挙に解消するようにした
ものであり、次に本発明の高温空気混合蒸気発生装置を
、其の一実施例を示した図面に基いて詳説すると、下記
の通りである。
In view of the above-mentioned conventional problems, the present invention has an extremely rational and inexpensive configuration that mixes high-temperature air heated using exhaust gas heat with moist saturated steam, and which combines high-temperature air and moist saturated steam. By mixing each at an appropriate mixing ratio using a pressure regulating valve, there are problems with conventional methods. - The high-temperature air mixed steam generator of the present invention will be explained in detail below based on the drawings showing one embodiment thereof.

即ち、実施例装置の構成は、従来公知の蒸気ボイラと同
一形態のボイラ本体1の上部の排ガス排出口2に、水平
方向に略蛇行形状の二太の加熱空気管3が空気連通室4
に依って連通す乙よう接続内股された断熱筐体5を、連
通形態で取付けると共に、加熱空気管3の入口に、圧力
空気送出源となるコンプレッサ6と圧力空気管7で接続
し、且つ圧力空気管7に空気圧力調整弁8(f−介挿し
、一方、ボイラ本体1の蒸気管9を吸引混合器10に接
続し且つ蒸気管9に蒸気圧力調整弁11を装設し、更に
、加熱空気管3の出口?加熱空気圧送管12に依り混合
器1Gに接続したことを要旨とするものである。
That is, the configuration of the embodiment apparatus is such that a two-thick heated air pipe 3 having a substantially meandering shape in the horizontal direction is connected to an air communication chamber 4 at an exhaust gas discharge port 2 at the top of a boiler body 1 which has the same form as a conventionally known steam boiler.
The insulated housing 5 is installed in a communicating manner, and is connected to the inlet of the heating air pipe 3 by a compressor 6, which serves as a pressure air delivery source, through a pressure air pipe 7. An air pressure regulating valve 8 (f- is inserted into the air pipe 7, and a steam pipe 9 of the boiler main body 1 is connected to a suction mixer 10, and a steam pressure regulating valve 11 is installed in the steam pipe 9. The gist is that the outlet of the air pipe 3 is connected to the mixer 1G via a heated air pressure feed pipe 12.

尚、図中の13は水管体、14.15は水管体13の下
部ドラム及び上部ドラム、16#i上部ドラム15の水
面より上部に形設された蒸気室、17は水位計、18け
ボイラ本体1の下部の火室198に臨ませてボイラ本体
1の下側部に装着されたオイルバーナー、2(l燃焼室
、21は水管体13に添着され燃焼室20の燃焼力。
In the figure, 13 is a water pipe body, 14.15 is a lower drum and an upper drum of the water pipe body 13, a steam chamber formed above the water surface of the 16 #i upper drum 15, 17 is a water level gauge, and 18 boilers. The oil burner 2 (l combustion chamber) is attached to the water pipe body 13 and the oil burner 2 (l combustion chamber) is attached to the water tube body 13 and is attached to the combustion chamber 20 to generate the combustion power of the combustion chamber 20.

スを水管体13の伝熱面に均等に接触するよう導く力゛
イド休、22は断熱筐体5内に於いて水平方向に形設さ
れ排ガスを加熱空気管3の伝熱面に均等に導く邪魔板、
23は断熱筐体εの排気口24に連通接続された排気筒
、26.26は夫々蒸気管9に装設された蒸気弁及び逆
止弁、27Vi、圧力空気管7に設けられた逆止弁、2
8゜29.30は夫々加熱空気圧送管12に設けられた
逆止弁、加熱空気放出調整弁及び逆止弁、31けホット
ウェルタンク(図示せず)の温水を給水管32を介して
下部ドラム14に供給する給水ポンプ金夫々示す。
A force field rest 22 is formed horizontally in the heat insulating casing 5 to guide the exhaust gas so that it evenly contacts the heat transfer surface of the heated air pipe 3. Baffle board to guide,
23 is an exhaust pipe connected to the exhaust port 24 of the heat insulating housing ε, 26 and 26 are a steam valve and a check valve respectively installed in the steam pipe 9, and 27Vi is a check valve installed in the pressure air pipe 7. valve, 2
8゜29.30 is a check valve, a heated air release adjustment valve, a check valve, and a check valve provided in the heated air pressure feed pipe 12, respectively, and hot water from a 31-piece hot well tank (not shown) is connected to the lower part through the water supply pipe 32. The water supply pumps that supply the drum 14 are shown.

次に、上記構成とした実施例の動作に付いて説明すると
、オイルバーナー18に依って重油と空気とが混合され
て火室191C霧状に吹き込まれて燃焼し、其れに依っ
て燃焼室20に発生した燃焼がスが、実線矢印で示すよ
うに、水管体13内の水を加熱した後に排ガスとなって
断熱筐体5内に入り、更に、排気筒23t−通って外部
に放出される。そして、高温燃焼ブスの通路中におかれ
た水管体13内の水が加熱される事に依り蒸気室16に
発生した湿り飽和蒸気が、一点鎖線矢印で示すように、
蒸気管9を通って混合器10に送り込まれる。断る場合
、混合器10に送られる飽和蒸気の蒸気圧は、蒸気圧力
調整弁11に依って常に一定に減圧される。
Next, to explain the operation of the embodiment configured as described above, heavy oil and air are mixed by the oil burner 18 and blown into the firebox 191C in the form of mist to be burned. As shown by the solid line arrow, the combustion gas generated at 20 heats the water in the water tube body 13, becomes exhaust gas, enters the heat insulating casing 5, and is further discharged to the outside through the exhaust pipe 23t. Ru. Then, as the water in the water pipe body 13 placed in the passage of the high-temperature combustion bus is heated, moist saturated steam is generated in the steam chamber 16, as shown by the dashed-dotted line arrow.
The steam is fed into a mixer 10 through a steam pipe 9. If the request is refused, the steam pressure of the saturated steam sent to the mixer 10 is always reduced to a constant level by the steam pressure regulating valve 11.

一方、コンプレッサ6から送出された圧力空気が二点鎖
線矢印で示すように、圧力空気調整弁8に依って湿り飽
和蒸気の蒸気圧よりも若干低い圧力に減圧された後に加
熱空気管3に送られ、ボイラ本体1の排ガス排出口2か
ら流入する排ガスから熱を吸収して高温空気となり、加
熱空気圧送管12全通って混合器10に送られ、混合器
10に流入する湿り飽和蒸気に依り吸引されて湿り飽和
蒸気に混合され、然る後K、蒸気使用機器に送られて加
熱や機器の作動等の用途に使用され、熱交換して排出さ
れたスチームドレンがホットウェルタンクに貯えられる
と共に給水ポンプ31に依って水管休13へと循環され
る。
On the other hand, as shown by the two-dot chain arrow, the compressed air sent out from the compressor 6 is reduced to a pressure slightly lower than the steam pressure of the wet saturated steam by the pressure air regulating valve 8, and then sent to the heated air pipe 3. The air absorbs heat from the exhaust gas flowing in from the exhaust gas outlet 2 of the boiler body 1, becomes high temperature air, and is sent to the mixer 10 through the heated air pressure pipe 12, and is heated by the wet saturated steam flowing into the mixer 10. It is sucked in and mixed into wet saturated steam, then sent to steam-using equipment for heating and equipment operation, and the steam drain that is discharged after heat exchange is stored in a hot well tank. At the same time, the water is circulated to the water pipe 13 by the water supply pump 31.

次に、上記実施例の作用効果に付いて説明する。Next, the effects of the above embodiment will be explained.

ボイラ本体1からの湿り飽和蒸気に、排ガス熱を利用し
て加熱した高温空気を混合する事に依り、乾き度の良い
乾燥蒸気となり、其の保有熱量が増大すると共に蒸気の
流速の上昇に依り蒸気使用機器への供給熱量が増大する
大きな利点があるだけでなく、蒸気使用機器に於ける熱
吸収作用に於りて以下のような顕著な効果が得られる。
By mixing the moist saturated steam from the boiler body 1 with high-temperature air heated using exhaust gas heat, it becomes dry steam with good dryness, which increases its heat capacity and increases the flow rate of steam. Not only does this have the great advantage of increasing the amount of heat supplied to steam-using equipment, but also the following remarkable effects can be obtained in terms of heat absorption in steam-using equipment.

即ち、蒸気使用機器から熱交換した後に排出されたスチ
ームドレンの温度が、従来のように湿り飽和蒸気を供給
した場合のスチームドレンの温度よりもかなり低くなる
。この事は、蒸気使用機器に於いて供給熱量が極めて有
効に吸収された事を示しており、蒸気使用機器いては燃
料使用緻が約20パーセント減少する。この現象を理論
的に明確に解明出来なかったが、各種の計測に依る結果
から、恐らく、高温空気が其の保有温度と熱量に依って
蒸気の凝縮しようとする水分を気泡状に吸収する事に依
って液化を防止し、飽和水の保有熱量を蒸気使用機器の
利用温度範囲に維持させて有効な熱吸収全促進させると
共に、蒸気使用機器の伝熱面に生じるドレン層を最小限
に抑制する事に依って該機器の熱吸収効率を上昇させて
いることに依るものと思われる。
That is, the temperature of the steam drain discharged from the steam-using equipment after heat exchange is considerably lower than the temperature of the steam drain when moist saturated steam is supplied as in the conventional case. This shows that the supplied heat is absorbed very effectively in the steam-using equipment, and the fuel consumption of the steam-using equipment is reduced by about 20%. Although this phenomenon could not be clearly explained theoretically, the results from various measurements suggest that high-temperature air probably absorbs the moisture that would otherwise condense in the steam, depending on its retained temperature and amount of heat. This prevents liquefaction, maintains the heat content of saturated water within the operating temperature range of steam-using equipment, promotes effective heat absorption, and minimizes the drain layer that forms on the heat transfer surface of steam-using equipment. This seems to be due to the fact that the heat absorption efficiency of the equipment is increased by doing so.

更に詳説すると、空気は断熱効果を有する為に、蒸気に
空気を混入させる事は、蒸気使用機器に於いてエアー障
害が生じるから・従来から断る装置に於いてタブー視さ
れているが、実施例装着では湿り飽和蒸気とほぼ同温度
まで加熱し九水分の少ない空気を混合させて従来のよう
な不都合の発生を阻止している。又、加熱空気を湿り飽
和蒸気に単に混合したのでけ1空気量が必要以上に多く
なって蒸気使用機器忙エアー障害が発生するから、圧力
調整弁8.11t−設けて空気圧力及び蒸気圧力を各々
一定にし、且つ空気圧力を蒸気圧力よりも若干低くシ、
混合器10に於いて、湿り飽和蒸気により高温空気を吸
引して混合しているから、加熱空気圧送管12の両逆止
弁28.30間の空気圧は湿り飽和蒸気の蒸気圧とほぼ
同圧となって適正な混合比で混合される。しかも、湿り
飽和蒸気で加熱空気を吸引するから、使用蒸気欺に応じ
て加熱空気が吸引混合され、常に適正な混合比に維持さ
れている。又、高温空気の温度が湿り飽和蒸気の温度よ
り若干低い場合に於いても、混合した後は湿り飽和蒸気
の温度より僅かに高温の高温空気混合蒸気が発生する事
が、温度計等に依る実測結果から得られた。但し、高温
空気の温度は湿り飽和蒸気の温度よシ高い方が望ましい
To explain in more detail, since air has an insulating effect, mixing air with steam is considered a taboo in equipment because it will cause air problems in equipment that uses steam, but this example When installed, it is heated to almost the same temperature as wet saturated steam and mixed with air that has a low moisture content, thereby preventing the problems that occur with conventional methods. In addition, simply mixing heated air with moist saturated steam would result in a larger amount of air than necessary, which would cause trouble in the steam-using equipment, so a pressure regulating valve (8.11t) was installed to adjust the air pressure and steam pressure. each constant, and the air pressure is set slightly lower than the steam pressure,
In the mixer 10, high-temperature air is sucked in and mixed with moist saturated steam, so the air pressure between the check valves 28 and 30 of the heated air pressure pipe 12 is almost the same as the steam pressure of the moist saturated steam. The mixture is then mixed at an appropriate mixing ratio. Moreover, since the heated air is sucked in with moist saturated steam, the heated air is sucked and mixed according to the amount of steam used, and an appropriate mixing ratio is always maintained. Also, even if the temperature of the high-temperature air is slightly lower than the temperature of the moist saturated steam, a thermometer etc. will show that after mixing, a high-temperature air mixed steam is generated that is slightly higher than the temperature of the moist saturated steam. Obtained from actual measurement results. However, it is desirable that the temperature of the high-temperature air be higher than the temperature of moist saturated steam.

又、加熱空気放出調整弁29t−常KFM弁して高温空
気を微量であるが大気に放出するようにし、蒸気の使用
量が少ない場合に於いても、加熱空気管3内の空気の流
速の低下に依る空気温度の低下全防止している。
In addition, the heated air release adjustment valve 29t is a regular KFM valve to release a small amount of high-temperature air to the atmosphere, and even when the amount of steam used is small, the flow rate of the air in the heated air pipe 3 can be controlled. This completely prevents the air temperature from dropping due to air temperature drop.

尚、上記実施例では、加熱空気管3の形状を水平方向へ
の蛇行形態としたが、下方から上方へ螺旋形状に巻回し
た形状としても、実施例と同様の効果が得られるのは勿
論である。
In the above embodiment, the shape of the heating air pipe 3 is meandering in the horizontal direction, but it goes without saying that the same effect as in the embodiment can be obtained even if the heating air pipe 3 is spirally wound from the bottom to the top. It is.

叙上の如く本発明の高温空気混合蒸気発生装置に依ると
、余熱であって従来では熱損失となっていた排力°スを
熱源として空気を加熱する事、及び既設の蒸気ボイラを
改造する事なくボイラ本体の外部に所要部分を付設する
のみで構成出来る事に依郵、極めて合理的で安価な構成
でもって、燃料消費fを大幅に低減出来、装置全体の小
型化を図れるものであり、本発明は極めて高い工業的価
値と顕著な実用的効果を奏するものである。
As mentioned above, according to the high-temperature air mixed steam generator of the present invention, it is possible to heat the air using the residual heat, which conventionally resulted in heat loss, as a heat source, and to remodel an existing steam boiler. It is an extremely rational and inexpensive structure that can be constructed by simply attaching the necessary parts to the outside of the boiler body without any problems, and it is possible to significantly reduce fuel consumption f and downsize the entire device. Therefore, the present invention has extremely high industrial value and remarkable practical effects.

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

第1図は未発明の高温空気混合蒸気発生装置の一実施例
の切断正面図である。 1・・・ボイラ本体、   2・・・排ガス排出口、3
・・・加熱空気管、  5・・・断熱筐体、6・・・コ
ンプレッサ、 7・・・圧力空気管、8・・・空気圧力
調整弁、9・・・蒸気管、10・・・混合器%   1
1・・・蒸気圧力調整弁。 特許出願天上 縛幸 男 代理人 弁理士杉 木    巌 同 弁理士杉 木 勝 徳
FIG. 1 is a cutaway front view of an embodiment of an uninvented high-temperature air mixed steam generator. 1... Boiler body, 2... Exhaust gas outlet, 3
...Heating air pipe, 5...Insulated casing, 6...Compressor, 7...Pressure air pipe, 8...Air pressure regulating valve, 9...Steam pipe, 10...Mixing Equipment% 1
1...Steam pressure regulating valve. Patent application Tenjyo Shibuyuki Male agent Patent attorney Iwaodo Sugi Patent attorney Katsunori Sugi

Claims (1)

【特許請求の範囲】 α)ボイラ本体の排ガス排出口に、加熱空気管を内装し
た断熱筒体を連通接続すると共に、加熱空気管の入口と
圧力空気送出源とを接続する管路に空気圧力調整弁を介
挿し、加熱空気管の出口とボイラ本体の蒸気管とを混合
器に接続し。 且つ蒸気管KM気圧力調整弁を装設して成ることを特徴
とする高温空気混合蒸気発生装置。
[Claims] α) An insulating cylinder with a heated air pipe inside is connected in communication with the exhaust gas discharge port of the boiler body, and an air pressure is applied to the pipe line connecting the inlet of the heated air pipe and the pressurized air delivery source. Insert a regulating valve and connect the outlet of the heated air pipe and the steam pipe of the boiler body to the mixer. A high temperature air mixed steam generator characterized in that the steam pipe is equipped with a KM air pressure regulating valve.
JP12443481A 1981-08-08 1981-08-08 High-temperature air mixed steam generator Granted JPS5826906A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12443481A JPS5826906A (en) 1981-08-08 1981-08-08 High-temperature air mixed steam generator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12443481A JPS5826906A (en) 1981-08-08 1981-08-08 High-temperature air mixed steam generator

Publications (2)

Publication Number Publication Date
JPS5826906A true JPS5826906A (en) 1983-02-17
JPS6237282B2 JPS6237282B2 (en) 1987-08-12

Family

ID=14885388

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12443481A Granted JPS5826906A (en) 1981-08-08 1981-08-08 High-temperature air mixed steam generator

Country Status (1)

Country Link
JP (1) JPS5826906A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6174035U (en) * 1984-10-19 1986-05-19
JPS6323506U (en) * 1986-07-24 1988-02-16
JPS6323505U (en) * 1986-07-24 1988-02-16
JP2017161198A (en) * 2016-03-11 2017-09-14 アズビル株式会社 Dryness adjusting device and dryness adjustment method

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6174035U (en) * 1984-10-19 1986-05-19
JPH0328244Y2 (en) * 1984-10-19 1991-06-18
JPS6323506U (en) * 1986-07-24 1988-02-16
JPS6323505U (en) * 1986-07-24 1988-02-16
JPH037685Y2 (en) * 1986-07-24 1991-02-26
JPH0424245Y2 (en) * 1986-07-24 1992-06-08
JP2017161198A (en) * 2016-03-11 2017-09-14 アズビル株式会社 Dryness adjusting device and dryness adjustment method

Also Published As

Publication number Publication date
JPS6237282B2 (en) 1987-08-12

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