JPH1194203A - Steam producing equipment - Google Patents

Steam producing equipment

Info

Publication number
JPH1194203A
JPH1194203A JP9258782A JP25878297A JPH1194203A JP H1194203 A JPH1194203 A JP H1194203A JP 9258782 A JP9258782 A JP 9258782A JP 25878297 A JP25878297 A JP 25878297A JP H1194203 A JPH1194203 A JP H1194203A
Authority
JP
Japan
Prior art keywords
liquid
valve
automatic
boiler
section
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
JP9258782A
Other languages
Japanese (ja)
Inventor
Taizo Kawamura
泰三 川村
Yoshitaka Uchibori
義隆 内堀
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.)
SEDA GIKEN KK
Omron Corp
Original Assignee
SEDA GIKEN KK
Omron Corp
Omron Tateisi Electronics Co
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 SEDA GIKEN KK, Omron Corp, Omron Tateisi Electronics Co filed Critical SEDA GIKEN KK
Priority to JP9258782A priority Critical patent/JPH1194203A/en
Publication of JPH1194203A publication Critical patent/JPH1194203A/en
Pending legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To provide steam producing equipment which can simply prevent concentration of impurities in a liquid in a boiler part which generates steam. SOLUTION: This equipment has a boiler part 2 which turns a liquid into steam by heating, a level detecting means 42 which monitors a liquid level of the boiler part 2, a first automatic on-off valve 43 which is provided in a feed water system 18 feeding the liquid to the boiler part 2, a second automatic on-off valve 44 which is provided in a drainage system 19 draining the liquid in the boiler part 2 and an operating means 46 for start or stop, and it is provided with a control part 4 which controls opening and closure of the first automatic on-off valve 43 on the basis of an output of the level detecting means 42. When an operating means 46b for stop is operated, the first automatic on-off valve 43 is closed, while the second automatic on-off valve 44 is opened so that the whole of the liquid in the boiler part 2 be drained.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、食品の調理、食品
の解凍、殺菌、洗浄、サウナ等に使用される過熱蒸気の
元になる蒸気、又は化学工業において種々の加熱や処理
に使用される蒸気を発生させるための蒸気製造装置に関
する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to steam used as a source of superheated steam used for cooking, thawing, sterilizing, washing, and sauna of foods, or for various heating and treatment in the chemical industry. The present invention relates to a steam production device for generating steam.

【0002】[0002]

【従来の技術】蒸気を発生させるために、所定レベルの
液面を保つように液体が導入される管体と、前記管体に
巻回された励磁コイルと、前記励磁コイルにより発生す
る磁界変化により発熱する発熱体とを具えた電磁誘導加
熱式の蒸気発生装置が着目されるようになっている。
2. Description of the Related Art In order to generate steam, a tube into which a liquid is introduced so as to maintain a liquid level at a predetermined level, an exciting coil wound around the tube, and a change in a magnetic field generated by the exciting coil. Attention has been paid to an electromagnetic induction heating-type steam generator having a heating element that generates heat due to the electromagnetic induction heating.

【0003】この場合、管体内の水の蒸発に応じて、管
体内に水道水が導入されるため、カルキ等の不純物が管
体内で濃縮されていくことになる。そこで、管体内の液
体の不純物濃度を例えば導電計で測定し、所定濃度に達
すると、管体内の液体を排出し、新たな水道水と入れ換
えるという蒸気製造装置が提案されている(特開平9−
122635号公報参照)。
In this case, tap water is introduced into the pipe in accordance with the evaporation of the water in the pipe, so that impurities such as calcium are concentrated in the pipe. Therefore, there has been proposed a steam production apparatus in which the impurity concentration of a liquid in a tube is measured by, for example, a conductivity meter, and when the concentration reaches a predetermined concentration, the liquid in the tube is discharged and replaced with fresh tap water (Japanese Patent Application Laid-Open No. Hei 9 (1997)). −
No. 122635).

【0004】[0004]

【発明が解決しようとする課題】ただし、導電計等で水
内の不純物濃度を精度良く測定するためには、高価な測
定器が必要になって、濃度計を付加することにより制御
系が複雑になるという問題点があった。
However, in order to accurately measure the impurity concentration in water using a conductivity meter or the like, an expensive measuring instrument is required, and the control system becomes complicated by adding a concentration meter. There was a problem of becoming.

【0005】本発明は、このような課題を解決するため
になされたものであり、蒸気を発生させるボイラ部内の
液体の不純物の濃縮を簡単に防止できる蒸気製造装置を
提供することを目的とする。
The present invention has been made to solve such a problem, and an object of the present invention is to provide a steam producing apparatus which can easily prevent concentration of impurities in a liquid in a boiler section for generating steam. .

【0006】[0006]

【課題を解決するための手段】上記課題を解決する請求
項1記載の発明は、液体を加熱して蒸気にするボイラ部
と、前記ボイラ部の液面を監視する液面検出手段と、前
記ボイラ部に液体を供給する給水系統に設けられた第1
自動開閉弁と、前記ボイラ部内の液体を排出する排出系
統に設けられた第2自動開閉弁と、始動又は停止のため
の操作手段を有し、前記液面検出手段の出力に基づいて
前記第1自動開閉弁の開閉を制御する制御部とを具え、
前記制御部は、停止のための操作手段が操作されると、
前記第1自動開閉弁を閉じるとともに、前記ボイラ部内
の液体を全部排出するように前記第2自動開閉弁を開く
ことを特徴とする蒸気製造装置である。
According to a first aspect of the present invention, there is provided a boiler section for heating a liquid to produce a vapor, a liquid level detecting means for monitoring a liquid level in the boiler section, The first water supply system that supplies liquid to the boiler
An automatic opening / closing valve, a second automatic opening / closing valve provided in a discharge system for discharging the liquid in the boiler section, and operating means for starting or stopping, and based on an output of the liquid level detecting means, 1 comprising a control unit for controlling the opening and closing of the automatic on-off valve,
The control unit is configured to operate the operation unit for stopping,
A steam production apparatus, wherein the first automatic on-off valve is closed and the second automatic on-off valve is opened so as to discharge all the liquid in the boiler section.

【0007】請求項2記載の発明は、請求項1におい
て、前記制御部は、始動のための操作手段が操作される
と、前記第2自動開閉弁を閉じるとともに、前記ボイラ
部に所定量の液体を入れるために前記第1自動開閉弁を
開くものである。
According to a second aspect of the present invention, in the first aspect, when the operating means for starting is operated, the control unit closes the second automatic opening / closing valve and sets a predetermined amount in the boiler unit. The first automatic on-off valve is opened to allow the liquid to enter.

【0008】請求項3記載の発明は、請求項1又は2に
おいて、前記制御部は、前記液面検出手段の出力に基づ
いて前記ボイラ部に補給のための給水を行う前記第1自
動開閉弁の開閉回数を計数し、所定の開閉回数に達する
と、前記第2自動開閉弁を所定時間開きボイラ部に溜ま
った液体を所定量排出するとともに、前記第1自動開閉
弁を開いて排水量に見合った新たな給水を行うものであ
る。
According to a third aspect of the present invention, in the first or second aspect, the control unit supplies the boiler unit with water for replenishment based on an output of the liquid level detection unit. When the predetermined number of times of opening and closing is reached, the second automatic opening and closing valve is opened for a predetermined time to discharge a predetermined amount of liquid accumulated in the boiler section, and the first automatic opening and closing valve is opened to match the drainage amount. New water supply.

【0009】請求項4記載の発明は、請求項1〜3のい
ずれかにおいて、前記ボイラ部は、管体と、前記管体に
巻回された励磁コイルと、前記励磁コイルにより発生す
る磁界変化により発熱するとともに、多数の通路が形成
された導電性材料の発熱体とからなる。
According to a fourth aspect of the present invention, in any one of the first to third aspects, the boiler section includes a tube, an exciting coil wound around the tube, and a magnetic field change generated by the exciting coil. And a heating element made of a conductive material in which a number of passages are formed.

【0010】[0010]

【発明の実施の形態】以下、本発明の実施形態を図面を
参照しつつ説明する。図1は本発明の過熱蒸気製造装置
の機器構成図である。
Embodiments of the present invention will be described below with reference to the drawings. FIG. 1 is an equipment configuration diagram of a superheated steam production apparatus of the present invention.

【0011】図1において、蒸気製造装置1は、ボイラ
部2と、過熱部3と、制御部4と、処理部5とからな
り、過熱蒸気発生用に構成されている。なお、過熱部3
は必須ではなく、ボイラ部2に処理部5を接続したもの
であってもよい。
In FIG. 1, a steam producing apparatus 1 comprises a boiler section 2, a superheat section 3, a control section 4, and a processing section 5, and is configured to generate superheated steam. The heating section 3
Is not essential, and the processing unit 5 may be connected to the boiler unit 2.

【0012】ボイラ部2は、垂直上向きの管体11内
に、発熱体12を収納し、管体11に励磁コイル13を
巻回したものである。管体11は耐熱性、耐蝕性及び耐
圧性に優れたセラミック等の非磁性材料によりパイプ状
に形成されたものである。管体11内に収納された発熱
体12は、前記励磁コイル13により発生する磁界変化
により発熱する金属等の導電性材料により多数の通路を
形成したものである。即ち、ボイラ部2は電磁誘導加熱
部として構成されている。
The boiler unit 2 has a heating element 12 housed in a vertically upward tube 11 and an exciting coil 13 wound around the tube 11. The tube 11 is formed in a pipe shape from a nonmagnetic material such as ceramic having excellent heat resistance, corrosion resistance and pressure resistance. The heating element 12 housed in the tube 11 has a large number of passages formed of a conductive material such as a metal which generates heat due to a change in a magnetic field generated by the exciting coil 13. That is, the boiler unit 2 is configured as an electromagnetic induction heating unit.

【0013】このボイラ部2には、液面制御のための立
ち上げ管体15と、気液分離のためのバイパス管路16
と、管体11と立ち上げ管体15及びバイパス管路16
に対する共通のヘッダ部17とが付設されている。また
ヘッダ部17には、給水系統18と排水系統19とが接
続されている。バイパス管路16は、管体11からの蒸
気を横向きに壁にぶつけて気液分離を行うT字部16a
と、T字部16aで分離された液体をヘッダ部17に戻
す連結部16bと、T字部16aで分離された蒸気を上
向きから横向きに変えるエルボ部16cとからなってい
る。
The boiler section 2 has a rising pipe 15 for controlling the liquid level and a bypass pipe 16 for gas-liquid separation.
, The pipe 11, the rising pipe 15, and the bypass pipe 16
And a common header section 17 is provided. Further, a water supply system 18 and a drainage system 19 are connected to the header section 17. The bypass line 16 is a T-shaped portion 16a that performs vapor-liquid separation by colliding the steam from the tube 11 laterally against a wall.
And a connecting portion 16b for returning the liquid separated by the T-shaped portion 16a to the header portion 17, and an elbow portion 16c for changing the vapor separated by the T-shaped portion 16a from upward to horizontal.

【0014】過熱部3は、水平横向きの管体31内に、
発熱体32を収納し、管体31に励磁コイル33を巻回
したものである。管体31は耐熱性、耐蝕性及び耐圧性
に優れたセラミック等の非磁性材料によりパイプ状に形
成されたものである。管体31内に収納された発熱体3
2は、前記励磁コイル33により発生する磁界変化によ
り発熱する金属等の導電性材料により多数の通路を形成
したものである。即ち、過熱部3も電磁誘導加熱部とし
て構成されている。また、過熱部3の出口側には、処理
部5が接続されている。図示例の処理部5は過熱蒸気で
食品を調理できるように構成されている。
The superheater 3 is placed in a horizontal horizontal tube 31.
The heating element 32 is housed, and the exciting coil 33 is wound around the tube 31. The tube body 31 is formed in a pipe shape from a nonmagnetic material such as ceramics having excellent heat resistance, corrosion resistance and pressure resistance. Heating element 3 housed in tube 31
Reference numeral 2 denotes a structure in which a large number of passages are formed of a conductive material such as a metal which generates heat due to a change in a magnetic field generated by the excitation coil 33. That is, the superheating unit 3 is also configured as an electromagnetic induction heating unit. Further, a processing unit 5 is connected to an outlet side of the superheating unit 3. The processing unit 5 in the illustrated example is configured so that food can be cooked using superheated steam.

【0015】制御部4は、過熱部3の出口に配設され
た、温度計41と、立ち上げ管15に配設されたレベル
計(液面検出手段)42と、給水系統18に取り付けら
れた第1電磁開閉弁(第1自動開閉弁)43と、排水系
統19に取り付けられた第2電磁開閉弁(第2自動開閉
弁)44と、コントローラ45とからなっている。また
制御部4には、スタートボタン46aとストップボタン
46bを有する操作ボックス(操作手段)46が付設さ
れている。この制御部4は、レベル計42からの入力に
基づき、第1電磁開閉弁43をオンオフして供給量を調
整し、ボイラ部2の管体11内の液体レベルが所定値に
なるように制御している。
The control unit 4 is attached to the thermometer 41, the level meter (liquid level detecting means) 42 provided to the riser 15, and the water supply system 18. A first electromagnetic on-off valve (first automatic on-off valve) 43, a second electromagnetic on-off valve (second automatic on-off valve) 44 attached to the drainage system 19, and a controller 45. The control unit 4 is provided with an operation box (operation means) 46 having a start button 46a and a stop button 46b. The control unit 4 controls the first solenoid on-off valve 43 on and off based on the input from the level meter 42 to adjust the supply amount, and controls the liquid level in the tube 11 of the boiler unit 2 to a predetermined value. doing.

【0016】制御部4は、運転時の液面制御以外に、ス
タートボタン46aが操作されると、排水のための第2
電磁開閉弁44を閉じ、給水のための第1電磁開閉弁4
3を開いて所定の液面レベルとする機能、ストップボタ
ン46bが操作されると、給水のための第1電磁開閉弁
43を閉じ、排水のための第2電磁開閉弁44を開いて
ボイラ部2内の全ての液体を排出する機能、及び、通常
運転時において、ボイラ部2の液体内の不純物が濃縮さ
れないように、第1電磁開閉弁43の所定回数の作動に
よる給水毎に、所定量の液体を排出するため第2電磁開
閉弁44を所定時間開く機能を有している。
When the start button 46a is operated in addition to the liquid level control at the time of operation, the control unit 4 performs a second drainage operation.
Close the electromagnetic on-off valve 44 and open the first electromagnetic on-off valve 4 for water supply.
When the stop button 46b is operated, the first solenoid valve 43 for water supply is closed, and the second solenoid valve 44 for drainage is opened to open the boiler unit. A function to discharge all liquid in the boiler unit 2 and a predetermined amount of water for each supply of water by operating the first solenoid on-off valve 43 a predetermined number of times so that impurities in the liquid in the boiler unit 2 are not concentrated during normal operation. Has a function of opening the second electromagnetic on-off valve 44 for a predetermined time in order to discharge the liquid.

【0017】なお、ボイラ部2と過熱部3の励磁コイル
13,33に対する高周波電源装置14,34は、温度
計41からの入力を受けるコントローラ45により、所
定の出力に制御される。また、過熱部3の管体31と発
熱体32を水平な横向きに配設した理由は、過熱部3の
発熱体32の入口側が凝縮水で蓋をされた状態になら
ず、過熱部3における蒸気の通過を確保することによ
り、蒸気製造装置1の立ち上げ時の時間を短縮するため
である。ただし、化学装置などでは、過熱部3は垂直に
配設されることもある。
The high-frequency power supply devices 14 and 34 for the exciting coils 13 and 33 of the boiler unit 2 and the superheater unit 3 are controlled to predetermined outputs by a controller 45 that receives an input from a thermometer 41. Further, the reason why the tube body 31 and the heating element 32 of the superheating section 3 are arranged horizontally horizontally is that the inlet side of the heating element 32 of the superheating section 3 is not covered with condensed water, This is because the time when the steam production device 1 is started up is reduced by ensuring the passage of steam. However, in a chemical device or the like, the superheater 3 may be disposed vertically.

【0018】つぎに、上述した構造の蒸気製造装置1の
作動を、図1の機器図及び図2のフロー図により説明す
る。
Next, the operation of the steam producing apparatus 1 having the above-described structure will be described with reference to the equipment diagram of FIG. 1 and the flowchart of FIG.

【0019】スタートボタン46aを押すとフローが開
始される(S1)。このとき、ボイラ部2及び過熱部3
はドライの空状態になっているので、給水用電磁開閉弁
43が開いて、ボイラ部2への給水を開始する(S
2)。レベル計42でボイラ部2での所定レベルの液面
が確保されるかどうか判断し(S3)、所定レベルに達
すると(S3,YES)、給水用電磁開閉弁43が閉じ
る(S4)。これにより、ボイラ部2に所定量の液体が
満たされたことになり、ボイラ部2及び過熱部3の電磁
誘導加熱部が始動する(S5)。ボイラ部2は液体に漬
かっているため、直ぐに熱交換で蒸気を発生しはじめ
る。ボイラ部2の蒸気の発生が続くと液面が低下してい
くので、レベル計42が下限になったかどうか判断し
(S6)、下限になると(S6,YES)、給水用電磁
開閉弁43を開く(S7)。給水によりレベルが上昇す
るので、レベル計42が上限になったかどうか判断し
(S8)、上限になると(S8,YES)、給水用電磁
開閉弁43を閉じる(S9)。
When the start button 46a is pressed, the flow starts (S1). At this time, the boiler section 2 and the overheating section 3
Is dry, the water supply electromagnetic on-off valve 43 is opened to start water supply to the boiler unit 2 (S
2). The level meter 42 determines whether or not a predetermined level of liquid in the boiler unit 2 is secured (S3). When the level reaches a predetermined level (S3, YES), the water supply electromagnetic on-off valve 43 is closed (S4). As a result, the boiler unit 2 is filled with a predetermined amount of liquid, and the electromagnetic induction heating units of the boiler unit 2 and the superheating unit 3 are started (S5). Since the boiler unit 2 is immersed in the liquid, it immediately starts generating steam by heat exchange. If the generation of steam in the boiler section 2 continues, the liquid level decreases. Therefore, it is determined whether or not the level meter 42 has reached the lower limit (S6). Open (S7). Since the water supply increases the level, it is determined whether or not the level meter 42 has reached the upper limit (S8). When the upper limit has been reached (S8, YES), the water supply electromagnetic on-off valve 43 is closed (S9).

【0020】このように、蒸発に伴う液体の補給のため
の給水用電磁開閉弁43の開閉動作の回数nを計数する
(S10)。開閉の回数nが例えば5回のnmax に達し
たかどうか判断する(S11)。所定のnmax に達する
と(S11,YES)、排水用電磁開閉弁44を所定時
間開き、ボイラ部2に溜まった液体を所定量排出すると
ともに、開閉の回数nをゼロにクリアする(S12)。
このとき、給水用電磁開閉弁43が作動し、排水用電磁
開閉弁44による排水量に見合った給水が行われる。ス
トップボタン46bが操作されない限り(S13,N
O)、蒸発に見合った給水と、給水回数に応じた所定量
の排水を繰り返す(S6〜S12)。ストップボタン4
6bが操作されると(S13,YES)、ボイラ部2及
び過熱部3の電磁誘導加熱部が停止され(S14)、給
水用電磁開閉弁43が閉じるとともに、排水用電磁開閉
弁44が開き、ボイラ部2内の液体の全部が排出される
(S15)。
In this way, the number n of opening / closing operations of the water supply electromagnetic on-off valve 43 for replenishing the liquid accompanying the evaporation is counted (S10). It is determined whether the number of times n of opening and closing has reached, for example, five times n max (S11). When the predetermined value nmax is reached (S11, YES), the drainage electromagnetic on-off valve 44 is opened for a predetermined time to discharge a predetermined amount of liquid accumulated in the boiler unit 2 and to clear the number of times n of opening and closing to zero (S12). .
At this time, the water supply electromagnetic on-off valve 43 is activated, and water is supplied by the drainage electromagnetic on-off valve 44 according to the amount of drainage. Unless the stop button 46b is operated (S13, N
O), the water supply corresponding to the evaporation and the predetermined amount of drainage corresponding to the number of times of water supply are repeated (S6 to S12). Stop button 4
When 6b is operated (S13, YES), the electromagnetic induction heating units of the boiler unit 2 and the superheating unit 3 are stopped (S14), the water supply electromagnetic on / off valve 43 is closed, and the drainage electromagnetic on / off valve 44 is opened, All of the liquid in the boiler section 2 is discharged (S15).

【0021】図3及び図4は、他の蒸気製造装置を示
す。図3の蒸気製造装置101の過熱部103は、図1
の過熱部3と同じである。ただし、ボイラ部102は、
蒸発缶111をバーナの炎112で加熱して蒸気を発生
させるタイプになっている。蒸発缶111に対して、レ
ベル計LCと給水用電磁開閉弁SV1と排水用電磁開閉
弁SV2が接続される構成は図1と同様である。図4の
蒸気製造装置201は過熱部がなく、ボイラ部202だ
けになっている。このボイラ部202は、蒸発缶211
内に電気抵抗式加熱のシーズヒータ212を配設するタ
イプになっている。蒸発管211に対して、レベル計L
Cと給水用電磁開閉弁SV1と排水用電磁開閉弁SV2
が接続される構成は図1と同様である。このような、蒸
発缶111,211のタイプにあっては、容量が比較的
小さいコンパクトタイプの場合、排水及び給水に時間が
かからず、運転しないときには、蒸発缶111,211
を空にしておくことができる。
3 and 4 show another steam producing apparatus. The superheater 103 of the steam production apparatus 101 of FIG.
Is the same as the superheated section 3 of However, the boiler unit 102
The evaporator 111 is heated by a burner flame 112 to generate steam. The configuration in which the level meter LC, the electromagnetic valve for water supply SV1 and the electromagnetic valve for drainage SV2 are connected to the evaporator 111 is the same as that in FIG. The steam production apparatus 201 of FIG. 4 does not have a superheating section, and has only a boiler section 202. The boiler section 202 includes an evaporator 211
In this type, a sheathed heater 212 for electric resistance heating is provided. Level meter L for evaporation tube 211
C, solenoid valve for water supply SV1 and solenoid valve for drainage SV2
Are connected in the same manner as in FIG. In such a type of the evaporators 111 and 211, in the case of a compact type having a relatively small capacity, drainage and water supply do not take much time, and when the evaporators 111 and 211 are not operated, the evaporators 111 and 211 are not used.
Can be left empty.

【0022】伝熱面積が大きくなるように多層積層構造
体で発熱体を構成すると、ボイラ部における液体の容量
が極端に少なくなり、排水及び給水が数十秒で終わり、
運転しないとき空にしても支障を生じることがない。こ
のような発熱体の構造を図5及び図6により説明する。
なお、発熱体の構造は、大きさが異なるものの、ボイラ
部2及び過熱部3で同じ形態のものを用いることが好ま
しい。
When the heating element is constituted by the multilayer laminated structure so as to increase the heat transfer area, the volume of the liquid in the boiler portion becomes extremely small, and drainage and water supply are completed in several tens of seconds.
There is no problem even if the vehicle is empty when not driving. The structure of such a heating element will be described with reference to FIGS.
In addition, although the structure of a heating element differs in size, it is preferable to use the same shape in the boiler part 2 and the superheating part 3.

【0023】図5の如くジグザグの山型に折り曲げられ
た第1金属板531と平たい第2金属板532とを交互
に積層し、全体として円筒状の積層体に形成したもので
ある。この第1金属板531や第2金属板532の材質
としては、SUS447J1の如きマルテンサイト系ス
テンレスが用いられる。
As shown in FIG. 5, a first metal plate 531 and a flat second metal plate 532 bent in a zigzag mountain shape are alternately laminated to form a cylindrical laminated body as a whole. As a material of the first metal plate 531 and the second metal plate 532, a martensitic stainless steel such as SUS447J1 is used.

【0024】図6に示されるように、第1金属板531
の山(又は谷)533は中心軸534に対して角度αだ
け傾くように配設され、第2金属板532を挟んで隣り
合う第1金属板531の山(又は谷)533は交差する
ように配設されている。そして、隣り合う第1金属板5
31における山(又は谷)533の交差点において、第
1金属板531と第2金属板532がスポット溶接で溶
着され、電気的に導通可能に接合されている。
As shown in FIG. 6, the first metal plate 531
Are arranged so as to be inclined by an angle α with respect to the central axis 534, and the peaks (or valleys) 533 of the first metal plates 531 adjacent to each other with the second metal plate 532 interposed therebetween intersect. It is arranged in. Then, the adjacent first metal plate 5
At the intersection of the peaks (or valleys) 533 in 31, the first metal plate 531 and the second metal plate 532 are welded by spot welding and joined to be electrically conductive.

【0025】結局、手前側の第1金属板531と第2金
属板532との間には、角度αだけ傾いた第1小流路5
35が形成され、第2金属板532と奥側の第1金属板
531との間には、角度−αだけ傾いた第2小流路53
6が形成され、この第1小流路535と第2小流路53
6は角度2×αで交差している。また、第1金属板53
1や第2金属板532の表面には、流体の乱流を生じさ
せるための第3小流路としての孔537が設けられてい
る。さらに、第1金属板531や第2金属板532の表
面は平滑ではなく、梨地加工又はエンボス加工によって
微小な凹凸538が施されている。この凹凸538は山
(又は谷)533の高さに比較して無視できる程度に小
さい。
After all, between the first metal plate 531 and the second metal plate 532 on the near side, the first small flow path 5 inclined by the angle α is provided.
35 is formed, and between the second metal plate 532 and the first metal plate 531 on the back side, the second small flow path 53 inclined by an angle -α
6, the first small flow path 535 and the second small flow path 53
6 intersect at an angle of 2 × α. Also, the first metal plate 53
On the surface of the first or second metal plate 532, a hole 537 is provided as a third small flow path for generating a turbulent flow of the fluid. Furthermore, the surfaces of the first metal plate 531 and the second metal plate 532 are not smooth, but are provided with fine irregularities 538 by satin finish or embossing. The unevenness 538 is negligibly small compared to the height of the peak (or valley) 533.

【0026】励磁コイル13,33に高周波電流を流し
て、発熱体12,32に高周波磁界を作用させると、第
1金属板531と第2金属板532の全体に渦電流が生
じ、発熱体12,32が発熱する。このときの温度分布
は、第1金属板531と第2金属板532の長手方向に
延びた目玉型となり、周辺部より中心部の方が発熱し、
中央部を流れようとする流体(液体又は蒸気)の加熱に
有利になっている。
When a high-frequency current is applied to the exciting coils 13 and 33 to apply a high-frequency magnetic field to the heating elements 12 and 32, an eddy current is generated in the entire first metal plate 531 and the second metal plate 532, and , 32 generate heat. The temperature distribution at this time is an eyeball shape extending in the longitudinal direction of the first metal plate 531 and the second metal plate 532, and the central portion generates heat more than the peripheral portion,
This is advantageous for heating a fluid (liquid or vapor) which is going to flow in the central part.

【0027】また、図6のように、発熱体12,32内
には交差する第1小流路535と第2小流路536が形
成され、周辺と中央との拡散が行われ、加えて第3小通
路を形成する孔537の存在によって、第1小流路53
5と第2小流路536間の厚み方向の拡散も行われる。
したがって、これらの小流路535,536,537に
よって発熱体12,32の全体にわたる流体(液体又は
蒸気)のマクロ的な分散、放散、揮散が生じる。加え
て、表面の微小な凹凸538によってミクロ的な拡散、
放散、揮散も生じる。その結果、発熱体12,32を通
過する流体(液体又は蒸気)は略均一な流れになって、
第1金属板531及び第2金属板532と流体との均一
な接触機会が得られる。その結果液体又は蒸気の均一な
加熱が確保される。
As shown in FIG. 6, a first small flow path 535 and a second small flow path 536 that cross each other are formed in the heating elements 12 and 32, and diffusion between the periphery and the center is performed. Due to the presence of the hole 537 forming the third small passage, the first small passage 53
5 and the second small flow path 536 are also diffused in the thickness direction.
Therefore, these small flow paths 535, 536, and 537 cause macroscopic dispersion, dissipation, and volatilization of the fluid (liquid or vapor) throughout the heating elements 12, 32. In addition, micro-diffusion due to minute irregularities 538 on the surface,
Emission and volatilization also occur. As a result, the fluid (liquid or vapor) passing through the heating elements 12 and 32 becomes a substantially uniform flow,
A uniform contact opportunity between the first metal plate 531 and the second metal plate 532 and the fluid is obtained. As a result, uniform heating of the liquid or vapor is ensured.

【0028】ところで、金属板531,532の厚みが
30ミクロン以上1mm以下であり、高周波電流発生器
による高周波電流の周波数が15〜150KHzの範囲
にあるものが好ましい。金属板の厚みが30ミクロン以
上1mm以下であると、電力が入り易く、又伝熱面積を
大きくとるための波形等の加工による小流路の確保が容
易になる。また、使用する周波数が15KHz〜150
KHzの範囲であると、励磁コイルの銅損や、スイッチ
ング素子の損失を防止できる。特に、損失が少ない周波
数帯としては、20〜70KHzである。また、発熱体
12,32の1立方センチメートル当たりの伝熱面積
が、2.5平方センチメートル以上であるものが好まし
い。発熱体12,32の1立方センチメートル当たりの
表面積が2.5平方センチメートル以上、より好ましく
は5平方センチメートル以上になるように金属板を積層
すると、熱交換の効率を上げることができる。また、発
熱体8の表面積1平方センチメートル当たりで加熱すべ
き流体量が、0.4立方センチメートル以下であるもの
が好ましい。発熱体12,32の表面積1平方センチメ
ートル当たりの流体量を0.4立方センチメートル以
下、より好ましくは0.1立方センチメートル以下にす
ると、流体に対する伝熱の急速応答性が得られる。
It is preferable that the thickness of the metal plates 531 and 532 is 30 μm or more and 1 mm or less, and the frequency of the high-frequency current generated by the high-frequency current generator is in the range of 15 to 150 KHz. When the thickness of the metal plate is 30 μm or more and 1 mm or less, it is easy to supply electric power, and it is easy to secure a small flow path by processing a waveform or the like for obtaining a large heat transfer area. In addition, the frequency used is 15 KHz to 150
When it is in the range of KHz, copper loss of the exciting coil and loss of the switching element can be prevented. In particular, the frequency band having a small loss is 20 to 70 KHz. Further, it is preferable that the heat transfer area per cubic centimeter of the heating elements 12 and 32 is 2.5 square centimeters or more. Heat exchange efficiency can be increased by stacking metal plates so that the surface area per cubic centimeter of the heating elements 12 and 32 is 2.5 square centimeters or more, more preferably 5 square centimeters or more. Further, it is preferable that the amount of fluid to be heated per square centimeter of the surface area of the heating element 8 is 0.4 cubic centimeter or less. When the amount of fluid per square centimeter of the surface area of the heating elements 12 and 32 is 0.4 cubic centimeter or less, and more preferably 0.1 cubic centimeter or less, rapid response of heat transfer to the fluid is obtained.

【0029】上述した構造の発熱体による加熱において
は、電気エネルギーから熱エネルギーへの変換効率が9
2%と極めて高いことが確認されている。例えば、10
0mm径、長さ200mm、表面積2.2〜6.2m2
の発熱体12,32を用いた場合、流体の膜厚(1cm
3 当たりの水膜量)が0.5〜0.2mmと極めて薄膜
状であり、発熱体12,32を構成する金属板531、
532も薄いため、温度差も極めて小さく、熱伝達を素
早く促進できる。したがって、過熱部3がコンパクトで
あっても、大量の過熱蒸気を発生させることが可能にな
る。
In the heating by the heating element having the above-described structure, the conversion efficiency from electric energy to heat energy is 9%.
It has been confirmed that it is as high as 2%. For example, 10
0mm diameter, length 200mm, surface area 2.2-6.2m 2
When the heating elements 12 and 32 are used, the thickness of the fluid (1 cm
( Amount of water film per 3 ) is extremely thin as 0.5 to 0.2 mm, and the metal plates 531 and
Since 532 is also thin, the temperature difference is extremely small and heat transfer can be promptly promoted. Therefore, even if the superheater 3 is compact, a large amount of superheated steam can be generated.

【0030】図7乃至図10は、電磁誘導加熱部に用い
られる他の発熱体を示す。図5及び図6の発熱体は加熱
効率に優れるが、これに限られるものではない。図7の
ように、金属板をクロスさせて断面が格子状となった筒
体の発熱体501であっても、電磁誘導加熱が可能で、
ボイラ部の液体量が少なくなる。図8のように、一枚の
金属板を相互間に隙間を有する程度のコイル状に巻いた
発熱体502であっても、電磁誘導加熱が可能で、ボイ
ラ部の液体量が少なくなる。図9のように、金属たわし
を詰めた発熱体503であっても、電磁誘導加熱が可能
で、ボイラ部の液体量が少なくなる。更に図10のよう
に、導電性セラミックの筒体の軸方向に多数の貫通穴を
開口させた発熱体504であっても、電磁誘導加熱が可
能で、ボイラ部の液体量が少なくなる。
FIGS. 7 to 10 show other heating elements used in the electromagnetic induction heating section. The heating elements of FIGS. 5 and 6 have excellent heating efficiency, but are not limited thereto. As shown in FIG. 7, even with a cylindrical heating element 501 having a cross section formed by crossing metal plates into a lattice shape, electromagnetic induction heating is possible,
The amount of liquid in the boiler is reduced. As shown in FIG. 8, even with a heating element 502 in which a single metal plate is wound into a coil shape having a gap between them, electromagnetic induction heating is possible and the amount of liquid in the boiler section is reduced. As shown in FIG. 9, even with the heating element 503 packed with a metal scourer, electromagnetic induction heating is possible, and the amount of liquid in the boiler section is reduced. Further, as shown in FIG. 10, even with the heating element 504 having a large number of through holes opened in the axial direction of the conductive ceramic cylinder, electromagnetic induction heating is possible, and the amount of liquid in the boiler section is reduced.

【0031】なお、励磁コイル13,33は、リッツ線
を撚り合わせたものが好ましく、管体11,31の外周
に巻回されるか、又は管体の肉厚内に巻回して埋設され
る。管体11,31は、励磁コイル13,33を保持
し、流体通路を区画し、その通路内に発熱する発熱体1
2,32を収納するものであるため、耐蝕性、耐熱性、
耐圧性があって非磁性体の材質で形成される。具体的に
は、セラミック等の無機質材料、FRP(繊維強化プラ
スチック)、フッ素樹脂等の樹脂材料、ステンレス等の
非磁性金属等が用いられるが、セラミックが最も好まし
い。発熱体12,32には、強磁性体の導電性材料であ
って、且つ耐蝕性に優れたマルテンサイト系ステンレス
が好ましいが、これに限らない。非磁性又は弱磁性の導
電性材料であるSUS304であってもよいし、非磁性
の導電性材料である炭素又は炭素化合物(セラミック)
も使用可能である。
The exciting coils 13 and 33 are preferably formed by twisting litz wires, and are wound around the outer circumference of the tubes 11, 31 or wound and embedded in the thickness of the tubes. . The tubes 11 and 31 hold the exciting coils 13 and 33, define a fluid passage, and generate heat in the passage.
Because it accommodates 2, 32, corrosion resistance, heat resistance,
It is made of a non-magnetic material that has pressure resistance. Specifically, an inorganic material such as ceramic, a resin material such as FRP (fiber reinforced plastic), a fluororesin, a non-magnetic metal such as stainless steel, or the like is used, but ceramic is most preferable. The heating elements 12 and 32 are preferably, but not limited to, martensitic stainless steel which is a ferromagnetic conductive material and has excellent corrosion resistance. SUS304 which is a nonmagnetic or weak magnetic conductive material may be used, or carbon or a carbon compound (ceramic) which is a nonmagnetic conductive material
Can also be used.

【0032】また、図示例は、大気圧の過熱蒸気100
%による非酸素雰囲気とすることができる装置であった
が、過熱蒸気に空気、窒素その他のガスを混ぜて、高温
渇き状態の混合ガスを得る装置とすることもできる。こ
の場合、図1のa点に所定の加熱気体を吹き込む構造に
すればよい。更に、液体としての水を過熱蒸気にする場
合を説明したが、水以外の沸点を有する炭化水素類の液
体でも本装置が適用可能である。
The illustrated example shows a superheated steam 100 at atmospheric pressure.
Although the apparatus can be a non-oxygen atmosphere in terms of%, it can also be an apparatus in which air, nitrogen or other gas is mixed with superheated steam to obtain a mixed gas in a high temperature thirst state. In this case, a structure may be adopted in which a predetermined heated gas is blown into the point a in FIG. Further, the case where water as a liquid is converted into superheated steam has been described, but the present apparatus can be applied to liquids of hydrocarbons having a boiling point other than water.

【0033】[0033]

【実施例】水道水からの蒸気発生量6.5kg/Hr
(定格時)、使用過熱蒸気温度250°C(定格時)の
能力を有する図1の蒸気製造装置を一日のうち数時間を
運転し、停止した後、翌日に数時間運転することを繰り
返した。
[Example] 6.5 kg / Hr of steam generated from tap water
(At rated time), operating the steam production apparatus of FIG. 1 having the capability of using superheated steam temperature of 250 ° C. (at rated time) for several hours in a day, stopping and then operating for several hours the next day Was.

【0034】毎日、運転の停止時に、ボイラ部内の水が
排出されるため、ボイラ部内の液体の不純物濃度が濃縮
されることなく、またボイラ部内の発熱体にスケールが
沈殿することがなかった。
Since the water in the boiler is discharged every day when the operation is stopped, the impurity concentration of the liquid in the boiler is not concentrated, and the scale does not precipitate on the heating element in the boiler.

【0035】[0035]

【発明の効果】以上説明したように、請求項1の発明に
よると、毎日運転の停止時にボイラ部が空になるとき
に、ボイラ部内で濃縮された不純物が排出されるため、
ボイラ部に特に濃度計等の制御機器を設けなくても、毎
日の運転を支障なく継続することができる。
As described above, according to the first aspect of the present invention, when the boiler section is emptied when the operation is stopped every day, the impurities concentrated in the boiler section are discharged.
Even without providing a control device such as a concentration meter in the boiler unit, daily operation can be continued without any trouble.

【0036】請求項2の発明によると、ボイラ部が空に
なった状態でも、スタートボタンを操作すると、自動的
にボイラ部に給水される。
According to the second aspect of the present invention, even when the boiler section is empty, when the start button is operated, water is automatically supplied to the boiler section.

【0037】請求項3の発明によると、ボイラ部の連続
運転が続いたとしても、ボイラ内の液体が給水に応じて
排出されるため、長時間の運転が可能になる。
According to the third aspect of the present invention, even if continuous operation of the boiler section continues, the liquid in the boiler is discharged according to the water supply, so that long-time operation is possible.

【0038】請求項4の発明によると、発熱体として、
流体が分散、拡散、放散、揮散させられる形態のものを
使用することよって、極めて熱交換性が高くなって配管
途中に組み込めるので、コンパクトの機器構成で、大量
の蒸気を連続的に得ることが出来るとともに、ボイラ部
における流体量が少なくなって、ボイラ部の液体の全部
排出に要する時間や空から所定液面までの時間が短くて
済む。また、電磁誘導加熱によると、発熱体にスケール
の付着が殆どなく、長期間の運転でも、発熱体を点検又
は交換する必要がない。
According to the invention of claim 4, as the heating element,
By using a fluid that can be dispersed, diffused, diffused, and volatilized, heat exchange becomes extremely high and it can be installed in the middle of piping, so a large amount of steam can be obtained continuously with a compact device configuration. As much as possible, the amount of fluid in the boiler section is reduced, and the time required for completely discharging the liquid in the boiler section and the time from the sky to a predetermined liquid level are reduced. Further, according to the electromagnetic induction heating, there is almost no adhesion of scale to the heating element, and there is no need to check or replace the heating element even during long-term operation.

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

【図1】本発明の蒸気製造装置の機器構成図である。FIG. 1 is a diagram showing the equipment configuration of a steam production apparatus of the present invention.

【図2】本発明の蒸気製造装置の運転のフロー図であ
る。
FIG. 2 is a flowchart of the operation of the steam production apparatus of the present invention.

【図3】本発明の他の蒸気製造装置の機器構成図であ
る。
FIG. 3 is a view showing the configuration of another steam production apparatus according to the present invention.

【図4】本発明の他の蒸気製造装置の機器構成図であ
る。
FIG. 4 is a view showing the configuration of another steam production apparatus according to the present invention.

【図5】発熱体の全体斜視図である。FIG. 5 is an overall perspective view of a heating element.

【図6】発熱体の詳細構造図である。FIG. 6 is a detailed structural diagram of a heating element.

【図7】他の発熱体の構造図である。FIG. 7 is a structural view of another heating element.

【図8】他の発熱体の構造図である。FIG. 8 is a structural diagram of another heating element.

【図9】他の発熱体の構造図である。FIG. 9 is a structural diagram of another heating element.

【図10】他の発熱体の構造図である。FIG. 10 is a structural view of another heating element.

【符号の説明】[Explanation of symbols]

1 蒸気製造装置 2 ボイラ部 4 制御部 11 管体 12 発熱体 13 励磁コイル 18 給水系統 19 排水系統 42 レベル計(液面検出手段) 43 第1電磁開閉弁(第1自動開閉弁) 44 第2電磁開閉弁(第2自動開閉弁) 45 コントローラ 46 操作ボックス 46a スタートボタン(始動のための操作手段) 46b ストップボタン(停止のための操作手段) 531 第1金属板 532 第2金属板 535 第1小流路 536 第2小流路 537 第3小流路 DESCRIPTION OF SYMBOLS 1 Steam production apparatus 2 Boiler part 4 Control part 11 Tube 12 Heating element 13 Excitation coil 18 Water supply system 19 Drainage system 42 Level meter (liquid level detection means) 43 1st electromagnetic on-off valve (1st automatic on-off valve) 44 2nd Electromagnetic on-off valve (second automatic on-off valve) 45 Controller 46 Operation box 46a Start button (operation means for starting) 46b Stop button (operation means for stopping) 531 First metal plate 532 Second metal plate 535 First Small channel 536 Second small channel 537 Third small channel

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 液体を加熱して蒸気にするボイラ部と、
前記ボイラ部の液面を監視する液面検出手段と、前記ボ
イラ部に液体を供給する給水系統に設けられた第1自動
開閉弁と、前記ボイラ部内の液体を排出する排出系統に
設けられた第2自動開閉弁と、始動又は停止のための操
作手段を有し、前記液面検出手段の出力に基づいて前記
第1自動開閉弁の開閉を制御する制御部とを具え、前記
制御部は、停止のための操作手段が操作されると、前記
第1自動開閉弁を閉じるとともに、前記ボイラ部内の液
体を全部排出するように前記第2自動開閉弁を開くこと
を特徴とする蒸気製造装置。
1. A boiler section for heating a liquid into steam.
A liquid level detecting means for monitoring the liquid level of the boiler section; a first automatic opening / closing valve provided in a water supply system for supplying liquid to the boiler section; and a discharge system for discharging liquid in the boiler section. A second automatic on-off valve, and a control unit having an operation unit for starting or stopping, and controlling opening and closing of the first automatic on-off valve based on an output of the liquid level detection unit, wherein the control unit is When the operating means for stopping is operated, the first automatic opening / closing valve is closed and the second automatic opening / closing valve is opened so as to discharge all the liquid in the boiler section. .
【請求項2】 前記制御部は、始動のための操作手段が
操作されると、前記第2自動開閉弁を閉じるとともに、
前記ボイラ部に所定量の液体を入れるために前記第1自
動開閉弁を開く請求項1記載の蒸気製造装置。
2. The control section, when operating means for starting is operated, closes the second automatic on-off valve,
The steam production device according to claim 1, wherein the first automatic on-off valve is opened to allow a predetermined amount of liquid to enter the boiler unit.
【請求項3】 前記制御部は、前記液面検出手段の出力
に基づいて前記ボイラ部に補給のための給水を行う前記
第1自動開閉弁の開閉回数を計数し、所定の開閉回数に
達すると、前記第2自動開閉弁を所定時間開きボイラ部
に溜まった液体を所定量排出するとともに、前記第1自
動開閉弁を開いて排水量に見合った新たな給水を行う請
求項1又は2記載の蒸気製造装置。
3. The control section counts the number of times of opening and closing the first automatic on-off valve for supplying water to the boiler section for replenishment based on an output of the liquid level detecting means, and reaches a predetermined number of times of opening and closing. Then, the second automatic opening / closing valve is opened for a predetermined time to discharge a predetermined amount of liquid accumulated in the boiler section, and the first automatic opening / closing valve is opened to perform new water supply corresponding to the drainage amount. Steam production equipment.
【請求項4】 前記ボイラ部は、管体と、前記管体に巻
回された励磁コイルと、前記励磁コイルにより発生する
磁界変化により発熱するとともに、多数の通路が形成さ
れた導電性材料の発熱体とからなる請求項1〜3のいず
れかに記載の熱蒸気製造装置。
4. The boiler section includes a tube, an exciting coil wound around the tube, and a conductive material formed with a large number of passages while generating heat by a change in a magnetic field generated by the exciting coil. The hot steam producing apparatus according to any one of claims 1 to 3, comprising a heating element.
JP9258782A 1997-09-24 1997-09-24 Steam producing equipment Pending JPH1194203A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9258782A JPH1194203A (en) 1997-09-24 1997-09-24 Steam producing equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9258782A JPH1194203A (en) 1997-09-24 1997-09-24 Steam producing equipment

Publications (1)

Publication Number Publication Date
JPH1194203A true JPH1194203A (en) 1999-04-09

Family

ID=17325010

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9258782A Pending JPH1194203A (en) 1997-09-24 1997-09-24 Steam producing equipment

Country Status (1)

Country Link
JP (1) JPH1194203A (en)

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006170511A (en) * 2004-12-15 2006-06-29 Tlv Co Ltd Gas-liquid separator
WO2010047393A1 (en) 2008-10-23 2010-04-29 ホシザキ電機株式会社 Steam generator
JP2010108602A (en) * 2008-10-28 2010-05-13 Shimada Phys & Chem Ind Co Ltd High-frequency induction heating device
US7730830B2 (en) 2004-03-22 2010-06-08 Sharp Kabushiki Kaisha Steam cooking apparatus
JP2012022829A (en) * 2010-07-13 2012-02-02 Kansai Electric Power Co Inc:The Induction heating type heating device
US8161870B2 (en) 2005-08-01 2012-04-24 Sharp Kabushiki Kaisha Heating cooker
JP2013517428A (en) * 2010-01-19 2013-05-16 マーヴィン ウェスリー ウォード Clean multi-energy generation system, apparatus and method
KR101876117B1 (en) * 2017-01-25 2018-07-06 엘지전자 주식회사 Steam generator and cooker comprising the same
EP3575685A4 (en) * 2017-01-26 2020-10-28 LG Electronics Inc. -1- Steam generator and cooking apparatus including same

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01134101A (en) * 1987-11-19 1989-05-26 Ebara Corp Intermittent blow device for boiler
JPH01169902U (en) * 1988-04-28 1989-11-30
JPH03204501A (en) * 1989-12-29 1991-09-06 Noritz Corp Steam generating device of electrical heating type
JPH0445302A (en) * 1990-06-13 1992-02-14 Matsushita Electric Ind Co Ltd Steam generator
JPH0552506U (en) * 1991-12-17 1993-07-13 株式会社サムソン Boiler automatic blower
JPH08135903A (en) * 1994-11-08 1996-05-31 Matsushita Electric Ind Co Ltd Steam heating apparatus
JPH094804A (en) * 1995-06-22 1997-01-10 Matsushita Electric Ind Co Ltd Steam generator

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01134101A (en) * 1987-11-19 1989-05-26 Ebara Corp Intermittent blow device for boiler
JPH01169902U (en) * 1988-04-28 1989-11-30
JPH03204501A (en) * 1989-12-29 1991-09-06 Noritz Corp Steam generating device of electrical heating type
JPH0445302A (en) * 1990-06-13 1992-02-14 Matsushita Electric Ind Co Ltd Steam generator
JPH0552506U (en) * 1991-12-17 1993-07-13 株式会社サムソン Boiler automatic blower
JPH08135903A (en) * 1994-11-08 1996-05-31 Matsushita Electric Ind Co Ltd Steam heating apparatus
JPH094804A (en) * 1995-06-22 1997-01-10 Matsushita Electric Ind Co Ltd Steam generator

Cited By (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7730830B2 (en) 2004-03-22 2010-06-08 Sharp Kabushiki Kaisha Steam cooking apparatus
JP2006170511A (en) * 2004-12-15 2006-06-29 Tlv Co Ltd Gas-liquid separator
US8161870B2 (en) 2005-08-01 2012-04-24 Sharp Kabushiki Kaisha Heating cooker
WO2010047393A1 (en) 2008-10-23 2010-04-29 ホシザキ電機株式会社 Steam generator
US9253824B2 (en) 2008-10-23 2016-02-02 Hoshizaki Denki Kabushiki Kaisha Steam generator
JP2010108602A (en) * 2008-10-28 2010-05-13 Shimada Phys & Chem Ind Co Ltd High-frequency induction heating device
JP2013517428A (en) * 2010-01-19 2013-05-16 マーヴィン ウェスリー ウォード Clean multi-energy generation system, apparatus and method
US10066556B2 (en) 2010-01-19 2018-09-04 Marvin W. Ward System, apparatus and method for clean, multi-energy generation
JP2012022829A (en) * 2010-07-13 2012-02-02 Kansai Electric Power Co Inc:The Induction heating type heating device
KR101876117B1 (en) * 2017-01-25 2018-07-06 엘지전자 주식회사 Steam generator and cooker comprising the same
WO2018139839A1 (en) * 2017-01-25 2018-08-02 엘지전자 주식회사 Steam generator and cooking apparatus including same
EP3575694A4 (en) * 2017-01-25 2020-12-09 LG Electronics Inc. -1- Steam generator and cooking apparatus including same
US11382449B2 (en) 2017-01-25 2022-07-12 Lg Electronics Inc. Steam generator and cooking apparatus including steam generator
EP3575685A4 (en) * 2017-01-26 2020-10-28 LG Electronics Inc. -1- Steam generator and cooking apparatus including same
US11828458B2 (en) 2017-01-26 2023-11-28 Lg Electronics Inc. Steam generator and cooking apparatus including steam generator

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