Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JPS5831926B2 - steam generator - Google Patents
[go: Go Back, main page]

JPS5831926B2 - steam generator - Google Patents

steam generator

Info

Publication number
JPS5831926B2
JPS5831926B2 JP55100974A JP10097480A JPS5831926B2 JP S5831926 B2 JPS5831926 B2 JP S5831926B2 JP 55100974 A JP55100974 A JP 55100974A JP 10097480 A JP10097480 A JP 10097480A JP S5831926 B2 JPS5831926 B2 JP S5831926B2
Authority
JP
Japan
Prior art keywords
steam
hot water
plate
heat exchanger
tank body
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
JP55100974A
Other languages
Japanese (ja)
Other versions
JPS5725819A (en
Inventor
喬 佐藤
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.)
SATO SHOTEN KK
Original Assignee
SATO SHOTEN KK
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 SATO SHOTEN KK filed Critical SATO SHOTEN KK
Priority to JP55100974A priority Critical patent/JPS5831926B2/en
Publication of JPS5725819A publication Critical patent/JPS5725819A/en
Publication of JPS5831926B2 publication Critical patent/JPS5831926B2/en
Expired legal-status Critical Current

Links

Landscapes

  • Beans For Foods Or Fodder (AREA)
  • Cereal-Derived Products (AREA)
  • Commercial Cooking Devices (AREA)
  • Alcoholic Beverages (AREA)

Description

【発明の詳細な説明】 本発明は加工食品原料を蒸す場合に一定量の蒸気を安定
して供給すると共に、前記蒸気中の余剰水分を除去した
蒸気を供給しうる蒸気発生装置に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a steam generator capable of stably supplying a certain amount of steam when steaming processed food raw materials, and also supplying steam after removing excess moisture from the steam. .

米、豆等の加工食品原料、特に醸造用原料を蒸すにあた
っては、均一に蒸し上げることが後の製品の品質を左右
する。
When steaming processed food ingredients such as rice and beans, especially brewing ingredients, uniform steaming determines the quality of the resulting product.

ところで、ボイラーで発生した蒸気を直接蒸し器に導入
した場合は蒸気圧が高いので、蒸気は一部の原料のすき
まを通って上カへ逃げ、原料全部にゆきわたらない欠点
がある。
By the way, when the steam generated in the boiler is directly introduced into the steamer, the steam pressure is high, so the steam escapes to the top through the gaps between some of the raw materials, and has the disadvantage that it does not reach all of the raw materials.

これに対してはボイラーで発生した蒸気を熱交換器内に
導入し、この熱交換器によって再度水を沸かして常圧よ
りやや高い程度の蒸気を発生させ蒸し器に送る方法が採
られている。
To solve this problem, steam generated in a boiler is introduced into a heat exchanger, and the heat exchanger boils the water again to generate steam at a pressure slightly higher than normal pressure, which is then sent to the steamer.

この場合、蒸気が発生するにつれて熱交換器内の水は減
少するので、水を補給してやらなければならない。
In this case, the water in the heat exchanger decreases as steam is generated, so water must be replenished.

ところが熱交換器中に冷水を入れると湯温が下るため今
まで発生していた蒸気の発生は止まり、この結果、加工
食品原料にとって品質の点で致命的となるいわゆる蒸気
むらをおこすことになり、この点の改良が望まれていた
However, when cold water is poured into the heat exchanger, the temperature of the water drops and the steam that was previously generated stops, resulting in so-called steam irregularities that are fatal to the quality of processed food ingredients. , improvement in this respect has been desired.

又、場合によっては熱交換器中に減圧を生じ、熱交換器
を破損する場合もある。
In some cases, reduced pressure may occur in the heat exchanger, resulting in damage to the heat exchanger.

更に、醸造用原料を蒸すに当って、水分の多い蒸気は原
料に過剰の水分を与え製品の品質に好ましくないので蒸
気の水分含有率を下げる必要がある。
Furthermore, when steaming raw materials for brewing, it is necessary to reduce the moisture content of the steam, since steam with a high moisture content imparts excessive moisture to the raw materials, which is unfavorable to the quality of the product.

この点については従来からある装置として熱交換器中の
湯面と蒸気排出口との間に熱風を通したり、又蛇管を設
け、この中に熱湯を通し、蛇管の間を蒸気が通過する際
余分の水分を取除くものがある。
Regarding this point, conventional devices have been used to pass hot air between the hot water level in the heat exchanger and the steam outlet, or to install corrugated pipes, through which hot water is passed, and when the steam passes between the corrugated pipes. There are things that remove excess water.

しかし、いずれの装置も熱交換装置自体が大きくなると
いう欠点がある。
However, both devices have the disadvantage that the heat exchange device itself becomes large.

本発明はこれらの欠点を一挙に解決したもので槽本体の
内径より大きめの支持板に蒸気流通孔を穿設し、前記支
持板の下面には蒸気流通孔を穿設した筒体を形成し、前
記筒体の下端口部と槽本体の内径よりやや小さめの土切
円錐板の切口部とを接合した邪魔板と; 温水を連続して供給する温水補給槽と: から成り、槽本体と鏡板との間に前記邪魔板を固定する
と共に槽本体と温水補給槽とを連通させたことを要旨と
する。
The present invention solves these drawbacks all at once, by providing a support plate larger than the inner diameter of the tank body with a steam communication hole, and forming a cylindrical body with a vapor communication hole provided in the lower surface of the support plate. , a baffle plate in which the lower end opening of the cylindrical body is joined to a cut part of a conical cut plate having a diameter slightly smaller than the inner diameter of the tank body; a hot water supply tank that continuously supplies hot water; The gist is that the baffle plate is fixed between the mirror plate and the tank body and the hot water supply tank are communicated with each other.

次に、本考案の一実施例を図面に基づいて説明する。Next, one embodiment of the present invention will be described based on the drawings.

図中1は蛇管式熱交換器で主として槽本体2と鏡板3と
から成り、槽本体2と鏡板3は共に開口周縁にフランジ
2L31を有する。
In the figure, reference numeral 1 denotes a corrugated tube type heat exchanger, which mainly consists of a tank body 2 and a head plate 3. Both the tank body 2 and the head plate 3 have a flange 2L31 on the periphery of the opening.

4は邪魔板で支持板41と筒体42と上切円錐板43と
から成る。
A baffle plate 4 is composed of a support plate 41, a cylindrical body 42, and an upper conical plate 43.

支持板41は邪魔板4を支持すると共に蒸気流通孔41
1を穿設して蒸気中の余剰水分を凝縮付着させるもので
、槽本体2のフランジ21と鏡板3のフランジ31間に
挟着固定するため槽本体2の開口部の内径より大きめに
形成する。
The support plate 41 supports the baffle plate 4 and also includes the steam flow holes 41.
1 is drilled to condense and adhere excess moisture in the steam, and is formed to be larger than the inner diameter of the opening of the tank body 2 in order to be clamped and fixed between the flange 21 of the tank body 2 and the flange 31 of the end plate 3. .

支持板41の下面には支持板41と同様に蒸気中の余剰
水分を凝縮付着させると共に蒸気供給量の調整をも行な
う蒸気流通孔421を穿設した筒体42を形成する。
A cylindrical body 42 is formed on the lower surface of the support plate 41 and has a steam communication hole 421 for condensing excess moisture in the steam and adjusting the amount of steam supplied, similarly to the support plate 41.

筒体42の下端口部には土切円錐板43の切口部を接合
する。
The cut portion of the earth cutting conical plate 43 is joined to the lower end mouth portion of the cylindrical body 42 .

土切円錐板43は湯面から蒸発する蒸気の排気量を調整
すると共に支持板41及び筒体42に凝縮付着した水滴
が滴下する場合に熱交換器1の熱湯中に導く案内板とも
なるものであり、このため熱交換器1の内径よりやや小
さめに形成して、槽本体2との空隙部を設は水滴を落下
するようにしている。
The conical plate 43 adjusts the exhaust amount of steam evaporated from the hot water surface, and also serves as a guide plate for guiding water droplets condensed on the support plate 41 and the cylinder 42 into the hot water of the heat exchanger 1 when they drip. Therefore, the inner diameter of the heat exchanger 1 is slightly smaller than that of the heat exchanger 1, and a gap with the tank body 2 is provided to allow water droplets to fall.

5は温水補給槽で内部には予熱用熱媒を導くための熱交
換用蛇管6を内蔵する。
Reference numeral 5 denotes a hot water replenishment tank, which has a built-in heat exchange flexible pipe 6 for guiding a preheating heat medium.

温水補給槽5には導水管7を連通し、導水管7の流出口
には浮子を有する水位調整弁8を備えて水位の自動制御
を行なう。
A water pipe 7 is connected to the hot water replenishment tank 5, and a water level adjustment valve 8 having a float is provided at the outlet of the water pipe 7 to automatically control the water level.

熱交換器1と温水補給槽5−とは連通管9によって連通
され、熱交換器1中の熱湯が減少すれば温水補給槽5内
の温水は連通管9を通って熱交換器1内に流入する。
The heat exchanger 1 and the hot water replenishment tank 5- are communicated with each other by a communication pipe 9, and when the hot water in the heat exchanger 1 decreases, the hot water in the hot water replenishment tank 5 passes through the communication pipe 9 and flows into the heat exchanger 1. Inflow.

この流入作用は熱交換器1と温水補給槽5との高低差を
利用して行なうため温水補給槽5の下部に架台10を設
置する。
Since this inflow action is performed by utilizing the height difference between the heat exchanger 1 and the hot water supply tank 5, a pedestal 10 is installed below the hot water supply tank 5.

架台10の高さは蒸気の排気圧や熱交換器1の大きさ等
によって異なり一定ではないが、はぼ4肌前後である。
The height of the pedestal 10 varies depending on the steam exhaust pressure, the size of the heat exchanger 1, etc., and is not constant, but is approximately 4 cm high.

次に、本発明に係る装置の作動態様を説明する。Next, the operating mode of the device according to the present invention will be explained.

ボイラーより送られてきた高圧蒸気は蛇管11を循環し
て熱交換器1内の水を温め、はとんど常圧の蒸気を発生
させる。
The high-pressure steam sent from the boiler circulates through the corrugated pipe 11 and warms the water in the heat exchanger 1, generating steam at almost normal pressure.

発生した蒸気は排気量を調整する土切円錐板4′3によ
って排気に制限を受ける。
Exhaust of the generated steam is restricted by a cutting conical plate 4'3 that adjusts the exhaust amount.

土切円錐板43を通過した蒸気は筒体42及び支持板4
1の蒸気流通孔42L411を通過して排気口32に向
かう。
The steam that has passed through the earth-cutting conical plate 43 is transferred to the cylinder body 42 and the support plate 4.
The steam passes through the steam distribution hole 42L411 of No. 1 and heads toward the exhaust port 32.

この際、蒸気中の余剰水分は筒体42及び支持板41に
凝縮付着し、水滴となって滴下し土切円錐板43上を滑
べりながら湯中に落下する。
At this time, the excess water in the steam condenses and adheres to the cylinder 42 and the support plate 41, becoming water droplets and falling into the hot water while sliding on the earth cutting conical plate 43.

このようにして過剰水分を除いた蒸気は蒸し器に送られ
るが、蒸気の発生に伴ない熱交換器1中の熱湯は減り始
め水位が低下すると同時に温水補給槽5内の温水は熱交
換器1中に流入する。
The steam with excess water removed in this way is sent to the steamer, but as the steam is generated, the hot water in the heat exchanger 1 begins to decrease and the water level drops, and at the same time the hot water in the hot water supply tank 5 is transferred to the heat exchanger 1. flow inside.

温水補給槽5内の水位が低下すると浮子8が下がり導水
管7の栓を開ける。
When the water level in the hot water replenishment tank 5 decreases, the float 8 lowers and the stopper of the water conduit 7 is opened.

この作動を繰返し、常に一定量の余剰水分を除去した蒸
気を蒸し器に供給する。
This operation is repeated, and a constant amount of steam from which excess moisture has been removed is always supplied to the steamer.

このように本発明は上述の構成を有するので、加工食品
原料を蒸す場合に一定量の余剰水分を除去した常圧より
やや高い程度の醸造用加工原料に適した蒸気を安定して
供給できろ。
As described above, since the present invention has the above-described configuration, when steaming processed food raw materials, it is possible to stably supply steam suitable for brewing processed raw materials at a pressure slightly higher than normal pressure after removing a certain amount of excess moisture. .

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

第1図は本発明の蒸気発生装置の概略断面図、第2図は
邪魔板部分の部分断面図、第3図は邪魔板部分の分解斜
視図。 1・・・・・・熱交換器、2・・・・・・槽本体、3・
・・・・・鏡板、4・・・・・・邪魔板、41・・・・
・・支持板、42・・・・・・筒体、43・・・・・・
土切円錐板、5・・・・・・温水補給槽、6・・・・・
・蛇管、7・・・・・・導水管、8・・・・・・水位調
整弁、9・・・・・・連通管、10・・・・・・架台。
FIG. 1 is a schematic sectional view of the steam generator of the present invention, FIG. 2 is a partial sectional view of the baffle plate portion, and FIG. 3 is an exploded perspective view of the baffle plate portion. 1... Heat exchanger, 2... Tank body, 3.
...Mirror plate, 4...Baffle plate, 41...
...Support plate, 42...Cylinder, 43...
Earth-cutting conical plate, 5...Hot water supply tank, 6...
・Serial pipe, 7... Water conduit pipe, 8... Water level adjustment valve, 9... Communication pipe, 10... Frame.

Claims (1)

【特許請求の範囲】 1 蛇管式熱交換器から成る蒸気発生装置に於て、槽本
体の内径より大きめの支持板に蒸気流通孔を穿設し、前
記支持板の下面には蒸気流通孔を穿設した筒体を形威し
前記筒体の下端口部と槽本体の内径よりやや小さめの土
切円錐板の切口部とを接合した邪魔板と; 温水を連続して供給する温水補給槽と; から成り、槽本体と鏡板との間に邪魔板を固定すると共
に槽本体と温水補給槽とを連通させたことを特徴とする
蒸気発生装置。
[Scope of Claims] 1. In a steam generation device consisting of a corrugated tube heat exchanger, a support plate having a diameter larger than the inner diameter of the tank body is provided with steam communication holes, and a steam communication hole is provided in the lower surface of the support plate. a baffle plate shaped like a bored cylindrical body and joined to a lower end opening of the cylindrical body and a cut portion of a conical cut plate having a diameter slightly smaller than the inner diameter of the tank body; a hot water replenishment tank that continuously supplies hot water; A steam generator comprising: and; characterized in that a baffle plate is fixed between the tank body and the end plate, and the tank body and the hot water supply tank are communicated with each other.
JP55100974A 1980-07-21 1980-07-21 steam generator Expired JPS5831926B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP55100974A JPS5831926B2 (en) 1980-07-21 1980-07-21 steam generator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP55100974A JPS5831926B2 (en) 1980-07-21 1980-07-21 steam generator

Publications (2)

Publication Number Publication Date
JPS5725819A JPS5725819A (en) 1982-02-10
JPS5831926B2 true JPS5831926B2 (en) 1983-07-09

Family

ID=14288315

Family Applications (1)

Application Number Title Priority Date Filing Date
JP55100974A Expired JPS5831926B2 (en) 1980-07-21 1980-07-21 steam generator

Country Status (1)

Country Link
JP (1) JPS5831926B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0347730U (en) * 1989-09-14 1991-05-07

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6338801A (en) * 1986-08-05 1988-02-19 株式会社 タツミ・フ−ド・マシナリ Method and device for supplying steam for heating food
JP2599653B2 (en) * 1991-05-31 1997-04-09 ウエツトマスター株式会社 Indirect steam humidifier
JP2006322683A (en) * 2005-05-20 2006-11-30 Mitsubishi Heavy Ind Ltd Steam generator
JP6842317B2 (en) * 2017-02-20 2021-03-17 ホシザキ株式会社 Steam generator

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0347730U (en) * 1989-09-14 1991-05-07

Also Published As

Publication number Publication date
JPS5725819A (en) 1982-02-10

Similar Documents

Publication Publication Date Title
CA1158544A (en) Coal gas purification apparatus
EA002652B1 (en) Vessel and wort processing method for producing beer
JPS5831926B2 (en) steam generator
JP2008194571A (en) Liquid concentration system
FI91301B (en) The steam box
US1631162A (en) Vertical film-type evaporator
JPH0472156B2 (en)
JP3247095U (en) Solid Distillation Equipment
CN208591557U (en) It is condensed falling film evaporator
JP2729417B2 (en) Decompression evaporative cooling equipment
RU191874U1 (en) Steam generator for a bath stove
US2971453A (en) Milk treating system with deaerator
JP2803189B2 (en) Inhaler
JP4472102B2 (en) Steam heating device
US747943A (en) Generator for refrigerating apparatus.
JPS589094Y2 (en) water heater
WO2008136711A1 (en) Method and arrangement for generating smoke from liquid smoke condensates
JPS5932849Y2 (en) Water heater using exhaust heat from bathtub
JPS6119283Y2 (en)
JPS629835Y2 (en)
JP2929878B2 (en) Drain inflow shock prevention device for feed water heater
JP4472103B2 (en) Steam heating device
JPH07243647A (en) Steam cooling apparatus
JPH0252902A (en) Reduced pressure steam generator
JPH0370916A (en) Method and device for heating steam