JP3658702B2 - Pure steam production equipment - Google Patents
Pure steam production equipment Download PDFInfo
- Publication number
- JP3658702B2 JP3658702B2 JP33859198A JP33859198A JP3658702B2 JP 3658702 B2 JP3658702 B2 JP 3658702B2 JP 33859198 A JP33859198 A JP 33859198A JP 33859198 A JP33859198 A JP 33859198A JP 3658702 B2 JP3658702 B2 JP 3658702B2
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- JP
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- Prior art keywords
- evaporator
- steam
- chamber
- cyclone
- heating
- 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.)
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Description
【0001】
【発明の属する技術分野】
本発明は、製薬及び食品製造の分野で使用される純粋蒸気製造装置に関するものである。
【0002】
【従来の技術】
この種の装置では、加熱缶と蒸発缶及び気液分離器の3構成からなり、供給水をプレヒーターで加温した後加熱缶へ流入し、発生蒸気により蒸気とし飽和水の気液2相流体で蒸発缶に流入させ、蒸発缶で発生した蒸気は気液分離器に送入され液滴が分離されて純粋蒸気が製造されるものであるが、従来の装置では、図5に示すように夫々に独立した構造の加熱器51と蒸発缶52、及び分離器53を、主配管54で接続する構成であった。
【0003】
【発明が解決しようとする課題】
従って、このような従来の装置では、加熱器と蒸発缶、及び分離器を夫々に独立したものとして個別に製造する上に、配管で接続するものであるから広大な面積の設置場所が必要で、また配管の手間及び製作、管理等の面でコスト高になるのを避け得ないという問題点を有していた。
【0004】
本発明は、従来の技術のこのような問題点に鑑みてなされたものであり、その目的とするところは、加熱缶と蒸発缶及び気液分離器を1つに構成して配管による接続を無くすことによって、前述の問題点を解消しょうとするものである。
【0005】
【課題を解決するための手段】
上記の課題を解決するため、本発明に係る純粋蒸気製造装置は、純粋蒸気を製造する装置であって、加熱器の機能を備えた加熱缶部(10)と、蒸気を発生させる機能とサイクロン(8)による気液分離機能を備えた蒸発缶部(20)とを上下一体に結合したものからなり、前記加熱缶部(10)は供給水取入口(1)から取入れた供給水を伝熱管(2、3)を通して加熱し発生蒸気の圧力で蒸気と液滴の混合状態にして蒸発缶部(20)の上部受入口(4)にダイレクトに圧送する構成とされ、また蒸発缶部(20)には上部受入口(4)から圧送された蒸気の混合体が前記装置の中心部に設けられた円筒部(5)内を下降して下部膨張室(6)で膨張拡散するように機能する蒸発缶構造と、膨張室(6)から環状室(7)を上昇して圧力を高め、上記円筒部の外周に設けられたサイクロン(8)により中心内方へ向かって旋回しながら更に液滴を分離して取出口(9)より連続的に取出すように機能する分離器構造とを、備えてなるものである。
【0006】
そして、上記装置は、加熱缶部10の伝熱管2.3を、ストレート管往復型として構成することが好ましい。
【0007】
また、同様の目的で、蒸発缶部20の環状室7のサイクロン8を円周等間隔に数ヶ所設けるとともに、環状室7から中心内方へ向かって旋回しながら下降した後再び上昇するようにサイクロン室11に隔璧12を設けることもできる。
【0008】
【発明の実施の形態】
以下、本発明の実施例を図1乃至図4に基づいて説明する。
【0009】
図1に示すように、加熱缶部10は、本体ケース10aの外面に熱源を取入れる加熱蒸気入口10bと同出口10cを開設し、中空内部にストレート管往復型の伝熱管2、3を設けたものからなる。伝熱管2、3の各上端口は隔板10dで仕切られた上部室10eに開口し中心部の伝熱管3の下端口は蒸発缶20の上部受入口4に開口し、その他の伝熱管3の各下端口は下部室14に夫々開口している。
【0010】
蒸発缶部20は、図1乃至図2に示すように円筒状の缶胴ケース20aをアウターケースにして、その内部に同心に円筒部5と、環状の隔壁12及びその外周サイクロン外筒13とを一体に設けたものからなる。円筒部5は上部端板15に吊持状に支持されてその上部受入口4に伝熱管2の下端口が開口するように臨ませている。円筒部5の下端口5aは缶胴ケース20aの底部との間に下部膨張室6となる空間を形成している。
【0011】
サイクロン8は図3乃至図4に示すようにサイクロン外筒13の上部の外周面に中心内方に向かって旋回流が生じるように接線方向に切設した複数の窓孔8aと奥に向かう程細巾の通路8bを形成するように区切られたガイド小片8cとで形成され、円周等間隔に3乃至4箇所設けるものとする。
【0012】
【作用】
熱源としての加熱蒸気を加熱蒸気入口10bより加熱缶部10内に送り込むと、蒸気は缶内に充満して同出口10cより流出するからこの加熱蒸気の送入及び流出の加減により缶内を所定の温度に保ち、伝熱管2.3を加熱する。
【0013】
この状態で供給水を供給水入口1より供給すると、この供給水は下部室14より伝熱管2を通って上部室10eに至り、さらにこの上部室10eより中心部の伝熱管3を通って蒸発缶部20の円筒部5の上部受入口4に送入される。この為供給水は伝熱管2、3を往復通過する間に所定の高温度に加熱されて蒸気が発生し、さらにその圧力で蒸気と飽和水の気液2相流体で円筒室5へ圧送され下端口より膨張室6を経て環状室7を上昇し圧力を高めながらサイクロン8により中心内方へ向かう旋回流となってサイクロン室11及び隔壁12の内側の圧力路15を上昇し分離室16より取出口9へ送出されるものであって、このような流れの間に最終的に液滴が分離除去されて高純度の蒸気が得られるものである。
【0014】
尚、分離室16には液滴のドレン管17が設けられていて余剰の液滴をドレンとして回収する。
【0015】
【発明の効果】
以上説明したように本発明の純粋蒸気製造装置は、加熱器の機能を備えた加熱缶部と、蒸気を発生させる機能と気液分離機能を備えた蒸発缶部とを上下一体に結合したものからなり、前記加熱缶部は供給水取入口から取入れた供給水を伝熱管を通して加熱し発生蒸気の圧力で蒸気と液滴の混合状態にして蒸発缶部の上部受入口にダイレクトに圧送する構成とされ、また蒸発缶部には上部受入口から圧送された蒸気の混合体が円筒部内を下降して下部膨張室で膨張拡散するように機能する蒸発缶構造と、膨張室から環状室を上昇して圧力を高め、サイクロンにより旋回しながら更に液滴を分離して取出口より連続的に取出すように機能する分離機器構造とを、備えたものであるから、供給水取入口から供給水を供給しながら加熱器と蒸発缶及び分離器の機能を備えた1つの装置から連続的に高純度の純粋蒸気が得られるものであり、従来のように加熱器と蒸発缶及び分離器の夫々が独立し夫々を配管に接続したもののように、広大な設置場所を必要としないで、簡易に狭い場所での設置が可能であり、而も配管による接続の手間が省け、製作、管理も簡単となるため、コスト的にも有利である。
【図面の簡単な説明】
【図1】本発明の一実施例を示す純粋蒸気製造装置の全体構造の縦断側面図である。
【図2】図1における下半部の拡大した断面図である。
【図3】図2におけるAーA線矢視の拡大した横断平面図である。
【図4】サイクロン部分の拡大した矢視である。
【図5】従来の装置の配置図である。
【符号の説明】
1 供給水取入口
2.3 伝熱管
4 上部受入口
5 円筒部
6 膨張室
7 環状室
8 サイクロン
9 取出口
10 加熱缶部
11 サイクロン室
12 隔壁
13 サイクロン外筒
14 下部室
20 蒸発缶部[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a pure steam production apparatus used in the fields of pharmaceutical and food production.
[0002]
[Prior art]
This type of equipment consists of three components: a heating can, an evaporation can, and a gas-liquid separator. The supply water is heated by a pre-heater and then flows into the heating can. The vapor generated in the evaporator is fed into the evaporator with the fluid, and the vapor is sent to the gas-liquid separator to separate the liquid droplets to produce pure steam. In the conventional apparatus, as shown in FIG. The
[0003]
[Problems to be solved by the invention]
Therefore, in such a conventional apparatus, the heater, the evaporator, and the separator are individually manufactured as independent ones, and are connected by piping, so that a large installation area is required. In addition, there is a problem that it is inevitable that the cost is high in terms of labor and production and management of piping.
[0004]
The present invention has been made in view of such problems of the prior art, and the object of the present invention is to configure a heating can, an evaporator and a gas-liquid separator as one and connect them by piping. By eliminating it, it tries to solve the above-mentioned problems.
[0005]
[Means for Solving the Problems]
In order to solve the above problems, a pure steam production apparatus according to the present invention is an apparatus for producing pure steam, a heating can part (10) having a function of a heater, a function of generating steam, and a cyclone. The heating can part (10) is integrally connected to the evaporator part (20) having a gas-liquid separation function according to (8), and the heating can part (10) transmits the supply water taken from the supply water inlet (1). It is configured to be heated through the heat pipes (2, 3) and mixed with steam and droplets by the pressure of the generated steam and directly pumped to the upper inlet (4) of the evaporator section (20). 20), the vapor mixture pumped from the upper receiving port (4) descends in the cylindrical portion (5) provided at the center of the apparatus and expands and diffuses in the lower expansion chamber (6). A functioning evaporator structure and the pressure rising from the expansion chamber (6) to the annular chamber (7) Enhance the separator structure that functions to retrieve sequentially the outlet (9) collected by further separating the droplets while swirling towards the center inside the cyclone (8) provided on the outer periphery of the cylindrical portion Is provided.
[0006]
And it is preferable that the said apparatus comprises the heat exchanger tube 2.3 of the heating can part 10 as a straight tube reciprocating type.
[0007]
For the same purpose,
[0008]
DETAILED DESCRIPTION OF THE INVENTION
Embodiments of the present invention will be described below with reference to FIGS.
[0009]
As shown in FIG. 1, the heating can 10 has a heating steam inlet 10b and an
[0010]
As shown in FIG. 1 and FIG. 2, the
[0011]
As shown in FIG. 3 to FIG. 4, the
[0012]
[Action]
When heated steam as a heat source is fed into the heated can 10 from the heated steam inlet 10b, the steam fills the can and flows out from the
[0013]
When supply water is supplied from the supply water inlet 1 in this state, the supply water passes from the
[0014]
The
[0015]
【The invention's effect】
As described above, the pure steam production apparatus of the present invention is a unit in which a heating can part having a heater function and an evaporator part having a function of generating steam and a gas-liquid separation function are integrally connected in the vertical direction. The heating can part is configured to heat the feed water taken from the feed water inlet through a heat transfer tube, mix the steam and liquid droplets with the pressure of the generated steam, and directly pump it to the upper inlet of the evaporator part In the evaporator section, the evaporator structure functions so that the vapor mixture pumped from the upper receiving port descends in the cylindrical section and expands and diffuses in the lower expansion chamber, and the annular chamber rises from the expansion chamber. In this case, the separator is equipped with a separating device structure that functions to increase the pressure and rotate the cyclone to further separate droplets and continuously remove them from the outlet. While supplying the heater and evaporator and The pure steam of high purity can be obtained continuously from one device with the function of the separator, and each of the heater, the evaporator and the separator is independent and connected to the piping as in the past. In this way, it is possible to easily install in a narrow place without the need for a vast installation place, and it eliminates the labor of connection by piping, and it is easy to manufacture and manage, which is advantageous in terms of cost. is there.
[Brief description of the drawings]
FIG. 1 is a longitudinal side view of an entire structure of a pure steam production apparatus showing an embodiment of the present invention.
FIG. 2 is an enlarged cross-sectional view of a lower half portion in FIG.
FIG. 3 is an enlarged cross-sectional plan view taken along line AA in FIG. 2;
FIG. 4 is an enlarged arrow view of a cyclone portion.
FIG. 5 is a layout view of a conventional apparatus.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 Supply water inlet 2.3
Claims (3)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP33859198A JP3658702B2 (en) | 1998-11-30 | 1998-11-30 | Pure steam production equipment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP33859198A JP3658702B2 (en) | 1998-11-30 | 1998-11-30 | Pure steam production equipment |
Related Child Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2004351779A Division JP2005127710A (en) | 2004-12-03 | 2004-12-03 | Pure vapor manufacturing apparatus |
Publications (2)
Publication Number | Publication Date |
---|---|
JP2000161602A JP2000161602A (en) | 2000-06-16 |
JP3658702B2 true JP3658702B2 (en) | 2005-06-08 |
Family
ID=18319621
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP33859198A Expired - Lifetime JP3658702B2 (en) | 1998-11-30 | 1998-11-30 | Pure steam production equipment |
Country Status (1)
Country | Link |
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JP (1) | JP3658702B2 (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2003190725A (en) | 2001-12-25 | 2003-07-08 | Maruyasu Industries Co Ltd | Gas-liquid separator |
JP4978981B2 (en) * | 2005-06-07 | 2012-07-18 | 兼松エンジニアリング株式会社 | Water / air separation device for suction work vehicle and suction work vehicle equipped with this device |
-
1998
- 1998-11-30 JP JP33859198A patent/JP3658702B2/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
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JP2000161602A (en) | 2000-06-16 |
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