JPS62112952A - Hot water production method - Google Patents
Hot water production methodInfo
- Publication number
- JPS62112952A JPS62112952A JP25441685A JP25441685A JPS62112952A JP S62112952 A JPS62112952 A JP S62112952A JP 25441685 A JP25441685 A JP 25441685A JP 25441685 A JP25441685 A JP 25441685A JP S62112952 A JPS62112952 A JP S62112952A
- Authority
- JP
- Japan
- Prior art keywords
- water
- steam
- hot water
- membranes
- 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
Links
Landscapes
- Instantaneous Water Boilers, Portable Hot-Water Supply Apparatuses, And Control Of Portable Hot-Water Supply Apparatuses (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
- Filtering Of Dispersed Particles In Gases (AREA)
Abstract
Description
【発明の詳細な説明】
(産業上の利用分野)
本発明はスチームによる温水の製造方法に関し、特ニパ
イロジエンフリーの温水を安価に、かつ大量に製造する
に適した方法に関するものである。DETAILED DESCRIPTION OF THE INVENTION (Industrial Application Field) The present invention relates to a method for producing hot water using steam, and particularly to a method suitable for producing nipyrodiene-free hot water at low cost and in large quantities.
(従来の技術)
従来よシスチームで温水を製造する方法として(1)V
エル・アンド・チューブやプレート式の熱交換器を用い
た間接式
(2)水に直接スチームを吹き込む直接式の二つの方式
が知られている。(Conventional technology) As a conventional method for producing hot water using system steam, (1) V
Two methods are known: indirect method (2) using an L-and-tube or plate heat exchanger, and direct method (2) in which steam is blown directly into water.
両者のうち間接式が一般に知られているが、近年エネル
ギーコストが問題視されてからは直接式が効率のよさの
ため益々脚光を浴びるようになっている。Of the two, the indirect type is generally known, but since energy costs have become a problem in recent years, the direct type has been attracting more and more attention due to its high efficiency.
(発明が解決しようとする問題点) かかる直接式は次のような特長を有している。(Problem that the invention attempts to solve) This direct method has the following features.
(1)蒸気の熱カロリーが100%水に吸収され、しか
奄凝縮水が全く出ない。(1) 100% of the thermal calories of steam are absorbed by water, and no condensed water is produced.
(2)水への熱伝導は殆んど瞬時に行われるので正確な
温度制御が可能
(3)間接式のようなスケール発生による熱効率の低下
がなく、しかも据付面積が小さくて済むしかしこの方式
はスチームを直接水と接触させるためスチームに含まれ
る異物が水に混入して水が汚染されたり、スチームが水
の中にすぐにとけ込まないで、スチーふの泡が縮合して
大きな泡となシ、これが圧縮するときに破裂して衝撃音
や振動を引き起すという問題があった。(2) Accurate temperature control is possible because heat conduction to the water occurs almost instantaneously. (3) There is no reduction in thermal efficiency due to scale generation as with indirect methods, and the installation area is small. However, this method Since steam is brought into direct contact with water, foreign substances contained in the steam may mix into the water, contaminating the water, or the steam may not dissolve into the water immediately, causing the bubbles in the steam to condense and form large bubbles. Unfortunately, this had the problem of bursting when compressed, causing impact noise and vibration.
(問題点を解決するための手段)
本発明者らは直接式の上記問題点を解決するため鋭意検
討したととろ、意外にも水中に浸漬した中空糸モジュー
ルにスチームを供給して、濾過すると騒音や振動が全く
発生しないことを見出し、更に検討した結果本発明に到
達したものである。(Means for Solving the Problems) The inventors of the present invention have made extensive studies to solve the above-mentioned problems of the direct method, and unexpectedly found that when steam is supplied to a hollow fiber module immersed in water and filtered, noise is generated. They found that no vibrations or vibrations occur at all, and as a result of further study, they arrived at the present invention.
すなわち本発明は多数の中空糸状超精密濾過膜の少くと
も一端を集束固定した中空糸モジュールでろ過されたス
チームと水を接触させることを特徴とする温水の製造方
法である。That is, the present invention is a hot water production method characterized by bringing water into contact with steam filtered through a hollow fiber module in which at least one end of a large number of hollow fiber ultra-fine filtration membranes is fixed in a focused manner.
(f!川)
本発明によれば上述のように中空糸状超精密濾過膜でろ
過されたスチームを水と接触させることによシ実施例に
示すごとく騒音や振動を発生することなく容易に温水、
特にパイロジエンフリーの温水を製造できるという効果
が得られるが、かかる効果は従来の知見からは全く予想
しがたいことである。(f! River) According to the present invention, by bringing the steam filtered through the hollow fiber ultra-fine filtration membrane into contact with water as described above, hot water can be easily heated without generating noise or vibration as shown in the embodiment. ,
In particular, the effect of producing pyrogen-free hot water is obtained, but such an effect is completely unpredictable from conventional knowledge.
かかる効果を生ずる理由は明かでないが、スチームが超
精密濾過膜の多数の微細孔の各細孔から分散されて噴出
されるため、膜を透過したスチームが直ちに水にとけ込
み、スチームの泡の破裂による衝撃音や振動を防止でき
るものと推察される。The reason for this effect is not clear, but because the steam is dispersed and ejected from each of the many micropores of the ultra-precise filtration membrane, the steam that has passed through the membrane is immediately dissolved in the water, causing the steam bubbles to disappear. It is presumed that the impact noise and vibrations caused by the explosion can be prevented.
(実施例)
次に本発明方法を実施するに適した中空糸モジュール及
び該モジュールを用いたシヌテムについて図面にて説明
する。第1回〜第3図は中空糸モジュールの断面図であ
り、第1図は中空糸状膜2が多数本束ねられ、その両端
が耐熱シール剤20゜20′を用いて固定され、一方の
接着端部20に気密に取着されたボート21をスチーム
配管13と接続する一方、他方の接着端部20/をシー
ル剤で封鎖した膜モジュールの例を示している。(Example) Next, a hollow fiber module suitable for implementing the method of the present invention and a synutem using the module will be explained with reference to the drawings. Figures 1 to 3 are cross-sectional views of hollow fiber modules. Figure 1 shows a large number of hollow fiber membranes 2 bundled together, both ends of which are fixed using heat-resistant sealant 20°20', and one adhesive An example of a membrane module is shown in which a boat 21 airtightly attached to an end 20 is connected to a steam pipe 13, while the other bonded end 20/is sealed with a sealant.
第2図は中空糸状膜2が多数本束ねられ、中央部にてU
字型に曲げられ、両端を一面にて同時に耐熱シール剤2
0を用いて固定されボート21を介して、スチーム配管
13と接続する膜モジュールの例を示している。Figure 2 shows a large number of hollow fiber membranes 2 bundled together, with a U
It is bent into a shape, and heat-resistant sealant 2 is applied on both ends at the same time.
2 shows an example of a membrane module that is fixed using 0 and connected to the steam pipe 13 via a boat 21.
第3図は多数本束ねられた中空糸状膜2の両端を耐熱シ
ール剤20.20’を用いて固定してハウジング11と
一体成形し、該中空糸状膜の両端に設けたボー)21.
21’を水配管17及び温水配管1Bと接続し、該ハウ
ジングに設けられたスチーム入口22を、スチーム配管
13と接続し九膜モジュールの例を示している。FIG. 3 shows a large number of bundled hollow fiber membranes 2, both ends of which are fixed using a heat-resistant sealant 20, 20', integrally molded with the housing 11, and bows (21.
21' is connected to the water pipe 17 and the hot water pipe 1B, and the steam inlet 22 provided in the housing is connected to the steam pipe 13, thereby showing an example of a nine-membrane module.
本発明に用いられる中空糸状超精密濾過膜2とは孔径が
数10〜数100Xの限外濾過膜、あるいは数100〜
数1000Xの精密濾過膜であシ、通常透水率が100
0VmL1000V/am”以上、開孔率が10〜70
%の超精密濾過膜が用いられる。また、スチーム流量に
対して充分な膜面積を有しておく必要がある。かかる膜
面積は膜の細孔径や開孔率、スチームの流量により適宜
選択することができる。The hollow fiber ultra-precise filtration membrane 2 used in the present invention is an ultrafiltration membrane with a pore size of several tens to several hundreds of times, or an ultrafiltration membrane of several hundreds to several hundred times.
It is a precision filtration membrane of several 1000X, and the water permeability is usually 100
0VmL1000V/am” or more, porosity 10-70
% ultra-precise filtration membrane is used. Further, it is necessary to have a sufficient membrane area for the steam flow rate. The membrane area can be appropriately selected depending on the pore diameter and porosity of the membrane, and the flow rate of steam.
限外濾過膜は微粒子だけでなくパイロジエンも除去する
事が出来るので、温められるべき水がパイロジエンフリ
ーであれば、その純度を低下させることなく昇温させる
事が出来る。従ってコンパクトな装置でパイロジエンフ
リーの温水を安価に製造する事が可能となる。Ultrafiltration membranes can remove not only particulates but also pyrogenes, so if the water to be heated is pyrogen-free, it can be heated without reducing its purity. Therefore, it becomes possible to produce pyrogen-free hot water at low cost with a compact device.
超精密濾過膜の素材は、使用するスチームの圧力と温度
に耐えられるものであればよく、ポリイミド、ポリアミ
ド、ポリアミドイミドの有機系ポリマーの他、ガラス、
セラミックカーボンの無機系材料等をその具体例として
挙げることが出来る。The material for the ultra-precise filtration membrane may be any material as long as it can withstand the pressure and temperature of the steam used, and in addition to organic polymers such as polyimide, polyamide, and polyamideimide, glass,
Specific examples include inorganic materials such as ceramic carbon.
中でもポリスルホン及びポリイミドが好ましい。Among them, polysulfone and polyimide are preferred.
耐熱シール剤20,20’としては、耐熱性があり、か
つ溶出の少ないものであればよく、例えば100℃での
VヨアーD硬度が70以上のイミダゾ−μ硬化エポキン
樹脂、酸無水硬化エポキン樹脂などが好適に用いられる
。The heat-resistant sealant 20, 20' may be one that is heat resistant and has little elution, such as imidazo-μ hardened Epoquin resin or acid anhydride hardened Epoquin resin with a Vyoar D hardness of 70 or more at 100°C. etc. are preferably used.
中空糸束を耐熱F−A/剤で集束固定する場合には実公
昭60−176り号に示された弾性を有し、かつ可撓性
を有する耐熱シート材を、接着端部近傍の中空糸束外縁
部を囲繞すると、外縁部の中空糸の損傷を防ぐことがで
きる。中空糸束の接着端部を囲繞する耐熱性シート材と
しては、ニトリルゴム、イソプレンゴム、クロロプレン
ゴム、ネオプレンゴム、天然ゴム、ポリウレタン、シリ
コン等を挙げる事が出来る。When a hollow fiber bundle is bundled and fixed with a heat-resistant F-A/agent, a heat-resistant sheet material having the elasticity and flexibility shown in Utility Model Publication No. 176/1983 is used to attach a hollow fiber bundle near the adhesive end. By surrounding the outer edge of the fiber bundle, damage to the hollow fibers at the outer edge can be prevented. Examples of the heat-resistant sheet material surrounding the bonded end of the hollow fiber bundle include nitrile rubber, isoprene rubber, chloroprene rubber, neoprene rubber, natural rubber, polyurethane, and silicone.
本発明を実施するにあたり、スチームは中空繊維の材質
を考慮して、通常圧力2 kg/am”a以下、かつ温
度150℃以下で用いるのが好ましい。In carrying out the present invention, it is preferable to use steam at a pressure of 2 kg/am''a or less and a temperature of 150° C. or less, taking into account the material of the hollow fibers.
上記中空糸モジュールを用いて温水を得る方法として、
具体的には(+)水を貯留している水槽の内部に第1図
または第2図に示す膜モジュールを設置し、該膜を透過
したスチームと水を接触させる方法、(11)中空糸状
膜とハウジングを一体成形し、該ハウジング内に連続的
に供給した水を該膜を透過したスチームと連続的に接触
させる方法等を挙げる事が出来る。As a method of obtaining hot water using the above hollow fiber module,
Specifically, (+) a method in which a membrane module shown in FIG. 1 or 2 is installed inside a water tank storing water and the water is brought into contact with the steam that has passed through the membrane; Examples include a method in which a membrane and a housing are integrally molded, and water continuously supplied into the housing is brought into continuous contact with steam that has passed through the membrane.
第4図は、上記(1)の方法に従って温水を得る場合の
系統図であり、水槽1中にスチーム配管3とこれに接続
された中空糸状膜2を収容した膜モジュールが設置され
ている。スチームをスチーム配管3から供給して槽内の
水を昇温する。スチームは膜2を透過して、膜表面にて
水と接触し、溶解及び凝縮する事によ9水を直接外温す
る。尚、槽内に温度検出端5を設置し、スチーム配管中
に温度調節弁4を設置し、その間に温度制御部6を設置
す石事により、温水を一定温度に制御する事が出来る。FIG. 4 is a system diagram when hot water is obtained according to the method (1) above, in which a membrane module containing a steam pipe 3 and a hollow fiber membrane 2 connected thereto is installed in a water tank 1. Steam is supplied from a steam pipe 3 to raise the temperature of water in the tank. The steam passes through the membrane 2, comes into contact with water on the membrane surface, dissolves and condenses, and directly externally heats the water. Note that hot water can be controlled to a constant temperature by installing a temperature detection end 5 in the tank, installing a temperature control valve 4 in the steam pipe, and installing a temperature control section 6 between them.
第5図は上記(11)の方法に従って温水を得る場合の
系統図であり、第1図に示す膜モジュールがハウジング
11内に設置され一体となり、ボート21にスチーム配
管13、またハウジングに設けられた水入口に水配管1
7が接続されている。スチーム配管13からスチームを
供給し、それと同時に水配管17から水を供給する事に
よりハウジング内で温水が製造され、ハウジングの側壁
に設けた温水出口に接続された温水配管18から連続的
に温水を得る事が出来る。尚、ハウジングの温水出口近
傍に温度検出端15を設置し、スチーム配管中にこの検
出端と連動する温度調節弁14を設置し、その間に温度
制御部16を設置する事により、温水を一定温度に制御
する事が出来る。FIG. 5 is a system diagram when hot water is obtained according to the method (11) above, in which the membrane module shown in FIG. Water pipe 1 at the water inlet
7 is connected. Hot water is produced within the housing by supplying steam from the steam pipe 13 and water from the water pipe 17 at the same time, and hot water is continuously supplied from the hot water pipe 18 connected to the hot water outlet provided on the side wall of the housing. You can get it. In addition, by installing a temperature detection end 15 near the hot water outlet of the housing, installing a temperature control valve 14 interlocked with this detection end in the steam piping, and installing a temperature control unit 16 between them, the hot water can be kept at a constant temperature. can be controlled.
第6図も第3図者示す膜モジュールを用いて上記(1)
の方法に従って温水を得る場合の系統図であり、第6図
に示す中空糸状膜2はハウジング11に設置され一体と
なシ、該膜側に水配管17が接続され、ハウジング側に
スチーム配管13が接続されている。スチーム配管13
からスチームを供給し、それと同時に水配管17から水
を供給する。Figure 6 also shows the above (1) using the membrane module shown in Figure 3.
6 is a system diagram for obtaining hot water according to the method of FIG. 6, in which the hollow fiber membrane 2 shown in FIG. is connected. Steam piping 13
Steam is supplied from the pipe 17, and at the same time water is supplied from the water pipe 17.
該膜t−2の外側から内側にスチームは透過し、該膜内
の水温は入口部よシ加温され、出口部にて連続的に温水
を得る事が出来る。尚、温水配管18に温度検出端15
を設置し、スチーム配管中に温度調節弁14を設置し、
その間に温度制御部16を設置する事によシ、温水を一
定温度に制御する事が出来る。Steam permeates from the outside to the inside of the membrane t-2, the water temperature inside the membrane is warmed at the inlet, and hot water can be continuously obtained at the outlet. In addition, the temperature detection end 15 is connected to the hot water pipe 18.
and a temperature control valve 14 in the steam piping.
By installing a temperature control section 16 between them, it is possible to control the hot water to a constant temperature.
以下、実施例によ)本発明を更に具体的に説明する。The present invention will be explained in more detail below by way of examples.
実施例1 第4図に示す系統図に従って実験を行なった。Example 1 Experiments were conducted according to the systematic diagram shown in FIG.
水温30℃を有するパイロジエンフリーレベルの水17
01を貯留した水槽の底部に特開昭58−114702
号の実施例1に従って得られたポリスルホン製中空糸状
限外沖過膜(膜面積3.5が)を設置し、圧力1.2
kglom”Gのスチームを20kg/Hrの流量で供
給した。その結果、運転開始4時間後に水槽中の水の温
度が60℃に上昇した。運転中、へンマーリング等の騒
音は皆無であシ、又、水質ハ初期のパイロジエンフリー
レベμが運転終了迄維持出来た。Pyrogen-free level water with water temperature 30℃ 17
JP 58-114702 at the bottom of the water tank storing 01
A hollow fiber ultrafiltration membrane made of polysulfone (membrane area: 3.5 mm) obtained according to Example 1 of the above issue was installed, and a pressure of 1.2 mm was installed.
kglom"G of steam was supplied at a flow rate of 20 kg/Hr. As a result, the temperature of the water in the water tank rose to 60°C 4 hours after the start of operation. During operation, there was no noise such as humming and no noise. In addition, the initial pyrogen-free level μ of water quality could be maintained until the end of the operation.
実施例2
第5図に従って実験を行なった。水(1130℃を有ス
るパイロジエンフリーレベルの水を380 e7Hrの
流量で水配管17よpハウジング11に供給し、該ハウ
ジング内に設置された、特開昭58−91822号の実
施例1の方法に従って得られたポリヌルホン製中空糸状
精密濾過膜(膜面積3.5が)に、圧力1.2 kgl
om”Gのスチームを20 kg/Hrノ流量テスチー
ム配管13よシ供給した。その結果ハウジング出口部1
8よシロ0℃の温水が連続的に400にの流量で製造出
来た。運転中、ハンマーリング等のIifは皆無であシ
、又、水質は初期のパイロジエンフリーレペ〃が運転終
了迄維持出来た。Example 2 An experiment was conducted according to FIG. Embodiment 1 of JP-A No. 58-91822, in which water (having a temperature of 1130° C. and a pyrogen-free level) was supplied from the water pipe 17 to the housing 11 at a flow rate of 380 e7Hr, and installed in the housing. A pressure of 1.2 kgl was applied to a hollow fiber precision filtration membrane made of polynulfone (membrane area: 3.5 mm) obtained according to the method of
Steam at a flow rate of 20 kg/Hr was supplied through the test steam pipe 13.
It was possible to continuously produce hot water of 8 to 0 degrees Celsius at a flow rate of 400 degrees Celsius. During operation, there was no IIF such as hammering, and water quality could be maintained until the end of operation using the initial pyrogen-free repeller.
(効果)
以上のように本発明方法は騒音や振動を発生することな
く、容易に渇水を製造できる。また中空糸として限外濾
過膜を用いるとパイロジエンフリーの温水が容易に製造
できるため、特に医療用部品など高度の洗浄を要求され
る分野、あるいは食品分野等における温水の製造に有用
である。(Effects) As described above, the method of the present invention can easily produce drought conditions without generating noise or vibration. In addition, when an ultrafiltration membrane is used as a hollow fiber, pyrogen-free hot water can be easily produced, so it is particularly useful for producing hot water in fields that require high-level cleaning such as medical parts, or in the food field.
第1図〜第3図は本発明方法を実施するに適した中空糸
モジュールの断面図であジ、第4図〜第6図は上記中空
糸モジュールを用いたシステムのフロー図である。
(2)・・・・・・中空糸状膜 Ql)・・・・・
・ハウジングa4・・・・・・スチーム配管 Q7)
・・・・・・水配管(至)・・・・・・温水配管1 to 3 are cross-sectional views of a hollow fiber module suitable for carrying out the method of the present invention, and FIGS. 4 to 6 are flow diagrams of a system using the hollow fiber module described above. (2)...Hollow fiber membrane Ql)...
・Housing a4...Steam piping Q7)
・・・・・・Water piping (to)・・・Hot water piping
Claims (1)
した中空糸モジュールでろ過されたスチームと水を接触
させることを特徴とする温水の製造方法。A hot water production method characterized by bringing water into contact with steam filtered through a hollow fiber module in which at least one end of a large number of hollow fiber ultra-precise filtration membranes is fixed in a focused manner.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP25441685A JPS62112952A (en) | 1985-11-12 | 1985-11-12 | Hot water production method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP25441685A JPS62112952A (en) | 1985-11-12 | 1985-11-12 | Hot water production method |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS62112952A true JPS62112952A (en) | 1987-05-23 |
JPH023896B2 JPH023896B2 (en) | 1990-01-25 |
Family
ID=17264671
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP25441685A Granted JPS62112952A (en) | 1985-11-12 | 1985-11-12 | Hot water production method |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS62112952A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2013158693A (en) * | 2012-02-03 | 2013-08-19 | Mitsubishi Rayon Cleansui Co Ltd | Device for inspecting flaw of hollow fiber membrane module and method for inspecting flaw |
-
1985
- 1985-11-12 JP JP25441685A patent/JPS62112952A/en active Granted
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2013158693A (en) * | 2012-02-03 | 2013-08-19 | Mitsubishi Rayon Cleansui Co Ltd | Device for inspecting flaw of hollow fiber membrane module and method for inspecting flaw |
Also Published As
Publication number | Publication date |
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JPH023896B2 (en) | 1990-01-25 |
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