JPH0498099A - Shell and tube type heat exchanger - Google Patents
Shell and tube type heat exchangerInfo
- Publication number
- JPH0498099A JPH0498099A JP21429590A JP21429590A JPH0498099A JP H0498099 A JPH0498099 A JP H0498099A JP 21429590 A JP21429590 A JP 21429590A JP 21429590 A JP21429590 A JP 21429590A JP H0498099 A JPH0498099 A JP H0498099A
- Authority
- JP
- Japan
- Prior art keywords
- scale
- baffle plates
- steam
- tube
- heat exchanger
- 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
Links
- 239000000498 cooling water Substances 0.000 abstract description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 6
- 238000007790 scraping Methods 0.000 abstract description 4
- 238000007599 discharging Methods 0.000 abstract 2
- 230000008021 deposition Effects 0.000 abstract 1
- 230000006866 deterioration Effects 0.000 abstract 1
- 210000004907 gland Anatomy 0.000 abstract 1
- 238000000034 method Methods 0.000 abstract 1
- 230000007423 decrease Effects 0.000 description 6
- 238000010586 diagram Methods 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 239000002244 precipitate Substances 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 241001122767 Theaceae Species 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 2
- 230000002093 peripheral effect Effects 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000035515 penetration Effects 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
Landscapes
- Details Of Heat-Exchange And Heat-Transfer (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明はスケール餘去機能を持つシェルアンドチューブ
型熱交換器に関する。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a shell-and-tube heat exchanger having a scale removal function.
丁従来の技術〕
従来のノニルアンドチューブ型熱交換器を第3同と第4
回により説明する。[Conventional technology] The conventional nonyl-and-tube heat exchanger was
This will be explained in parts.
第31にて胴体lの両端部に管板2があり、管板2間に
複数のチューブ3が設けられる。またチューブ3と直交
して複数のじゃま板4が設けられる。管板2には鏡板7
が取付けられ、その一方は上下に2区分されていて上側
に冷却水人口13、下側に冷却水出口14が設けられて
いる。さらに胴体1の両端部には蒸気人口11と蒸気出
口12が設けられ、出口12にはファン10が取付けら
れている0図中5はじゃま板を固定するスティバー、1
6はドレン排出口を示す。31, there are tube sheets 2 at both ends of the body l, and a plurality of tubes 3 are provided between the tube sheets 2. Further, a plurality of baffle plates 4 are provided perpendicularly to the tube 3. The end plate 7 is attached to the tube plate 2.
is attached, one of which is divided into upper and lower sections, with a cooling water outlet 13 provided on the upper side and a cooling water outlet 14 provided on the lower side. Further, a steam port 11 and a steam outlet 12 are provided at both ends of the fuselage 1, and a fan 10 is attached to the outlet 12.In the figure, 5 is a stiver for fixing the baffle plate;
6 indicates a drain outlet.
以上において、第4図に示すように冷却水は入口13よ
りはいりチューブ3を通って出口14より出る。また蒸
気は人口11よりはいすしゃま板4で流れを交互に変え
られながらチューブ3の固りを通り熱を冷却水にうばわ
れて出口12より出る。In the above, as shown in FIG. 4, the cooling water enters from the inlet 13, passes through the tube 3, and exits from the outlet 14. Further, the steam passes through the solidity of the tube 3 while the flow is alternately changed by the cutting plate 4 than the population 11, and the heat is carried away by the cooling water and exits from the outlet 12.
:発明が解決しようとする課邪:
上記従来の熱交換器が地熱蒸気または熱水用C:使用さ
れる場合、寒気の凝縮あるいは温度の低下によって蒸気
熱水中に含まれるスケール成分が析出し、チューブの外
周に付着して熱交接効率を低下させてしまうという問題
があった。又、スケ−ル量が多くなると蒸気通路をふさ
いでしまうため、蒸気が入りにくくなって圧力が上がっ
てしまい、熱交換器の機能を失なわせてしまうおそれが
あった。Problems to be solved by the invention: When the above-mentioned conventional heat exchanger is used for geothermal steam or hot water, scale components contained in the steam hot water will precipitate due to condensation of cold air or a decrease in temperature. , there was a problem that it adhered to the outer periphery of the tube and reduced the heat exchange efficiency. In addition, if the amount of scale increases, it will block the steam passage, making it difficult for steam to enter and increasing the pressure, which may cause the heat exchanger to lose its function.
このスケールを除去するためには、熱交換器を系統より
バイパスするか(予備器または代替え装置を要する場合
がある)または設備全体を停止して分解清掃する必要が
あり、大きなロスとなっていた。In order to remove this scale, it was necessary to bypass the heat exchanger from the system (which may require a standby unit or alternative equipment) or to shut down the entire facility and disassemble it for cleaning, resulting in a large loss. .
〔課題を解決するための手段] 本発明は上記課題を解決するため次の手段を講する。[Means to solve the problem] The present invention takes the following measures to solve the above problems.
すなわち、シェルアンドチューブ型熱交換器として、胴
体内の両端部に管板を持ち同管板間に複数のチューブを
有するシェルアンドチューブ型熱交換器において、上記
チューブとほぼ直交して同チューブを通し摺動可能な複
数のしゃま板と、上記チューブにほぼ平行に設けられ、
周囲にねじを持つとともに上記じゃま板に蝉合する駆動
軸と、同駆動軸を回転駆動する駆動手段とを設ける。In other words, in a shell-and-tube heat exchanger that has tube sheets at both ends in the body and a plurality of tubes between the tube sheets, the tubes are inserted almost orthogonally to the tubes. A plurality of baffle plates that can be slid through and are provided approximately parallel to the tube,
A drive shaft having a thread around its periphery and engaged with the baffle plate, and a drive means for rotationally driving the drive shaft are provided.
上記手段により、チューブの外周面にスケールが析出し
たとき、駆動手段を作動させると、駆動軸が回転し、じ
ゃま板が軸方向に移動する。このときじゃま板はチュー
ブの外周面上を摺動しながら移動するのでスケールがか
き取られる。By the above means, when scale is deposited on the outer peripheral surface of the tube, when the drive means is operated, the drive shaft rotates and the baffle plate moves in the axial direction. At this time, the baffle plate moves while sliding on the outer peripheral surface of the tube, thereby scraping off the scale.
このようにして容易にスケールが除去され、熱交換効率
の低下が防止されるとともに、稼動率が向上する。In this way, scale is easily removed, a decrease in heat exchange efficiency is prevented, and the operating rate is improved.
(実施例)
本発明の一実施例を第1図と第2図により説明する。第
2図は第1図の■−■視図である。(Example) An example of the present invention will be described with reference to FIGS. 1 and 2. FIG. 2 is a view from ■--■ in FIG. 1.
なお、従来例で説明した部分は、同一の番号をつけ説明
を省略し、この発明Gこ関する部分を生体に説明する。The parts explained in the conventional example will be given the same numbers and the explanation will be omitted, and the parts related to the present invention will be explained to the living body.
第1図にて、管板2間に複数のチューブ3が設けられる
(図では1本で代表)。またチューブ3とほぼ直交して
複数のしゃま板4が、設けられる。In FIG. 1, a plurality of tubes 3 are provided between tube sheets 2 (one tube is representative in the figure). Further, a plurality of baffle plates 4 are provided substantially orthogonally to the tube 3.
上方のしゃま板41ま衆気入口11と茶気出口12C・
近くに配置され、下方のしゃま板4は中央に配置される
。また、これらは所定のクリアランでチューブ3を通し
ている。また駆動軸5aが冷却水人口13のない鏡板7
側からチューブ3の軸に平行に冷却水人口13側の管板
2まで貫通挿入されている。さらに駆動軸5aは第2図
に示すように横断面上で、上部、下部、左部および右部
に配置される。また駆動軸5aの周囲にはねじが切られ
ており、しゃま板4と蝉合している。駆動軸5aの冷却
水人口13のない鏡板7側の外部に出た端にはギヤーが
設けられ駆動手段としての駆動装置6に、回転可能に連
結されている。Upper baffle board 41, public air inlet 11 and tea outlet 12C.
The lower baffle plate 4 is placed in the center. Moreover, these are passed through the tube 3 with a predetermined clear run. In addition, the drive shaft 5a is connected to the end plate 7 without the cooling water population 13.
It is penetrated and inserted from the side parallel to the axis of the tube 3 to the tube plate 2 on the cooling water port 13 side. Furthermore, as shown in FIG. 2, the drive shafts 5a are arranged at the upper, lower, left, and right parts on the cross section. Further, a thread is cut around the drive shaft 5a, and the drive shaft 5a is engaged with the baffle plate 4. A gear is provided at the end of the drive shaft 5a that extends outside on the end plate 7 side where the cooling water port 13 is not provided, and is rotatably connected to a drive device 6 as a drive means.
また、胴体1内面に沿って複数のノズル8を持つノズル
管が、チューブ3に沿って複数段けられ薬液供給管15
につながれている。Further, a nozzle pipe having a plurality of nozzles 8 is provided along the inner surface of the body 1 in multiple stages along the tube 3, and a chemical solution supply pipe 15 is provided.
is connected to.
以上の構成において、次にこの熱交換器を地熱タービン
のグランド蒸気復水器に使用した場合6二つき、作用効
果を説明する。In the above configuration, the operation and effect will be explained next when this heat exchanger is used in a ground steam condenser of a geothermal turbine.
グランド芸気復水器は、タービン車室の車軸貫通部にお
ける軸シール部より茶気と大気の両方を、グランFM気
復水器内圧を大気圧より少し低くすることによって導く
ための装置である。The Grand FM air condenser is a device that guides both air and air from the shaft seal in the axle penetration part of the turbine casing by lowering the internal pressure of the Grand FM air condenser slightly below atmospheric pressure. .
蒸気空気入口IIから入った茶気は、冷却水人口13よ
り入った水がチューブ3内を通過しているため熱をうば
われ、しゃま板4で形成された通路を通る間に凝縮して
水となリドレン排出口16より糸外へすてられる。グラ
ンド茶気復水器内圧は、ファン10によって流入した空
気を排出しているため、大気圧より少し低く保たれてい
る。The brown air entering from the steam air inlet II loses its heat as the water entering from the cooling water port 13 passes through the tube 3, and condenses while passing through the passage formed by the baffle plate 4. Water is thrown out of the thread from the red drain outlet 16. The internal pressure of the grand tea condenser is kept slightly lower than atmospheric pressure because the fan 10 exhausts the air that has flowed into the condenser.
地熱蒸気が凝縮する際、温度低下に伴って蒸気中に含ま
れているスケールが析出するが、グランド蒸気復水器に
おいては、チューブ3の外周面に析出するため、蒸気の
通路面積が減少し、熱伝達効率が低下することになる。When geothermal steam condenses, the scale contained in the steam precipitates as the temperature decreases, but in the grand steam condenser, it precipitates on the outer circumferential surface of the tube 3, so the steam passage area decreases. , the heat transfer efficiency will decrease.
スケールの析出が始まったとき、駆動装置6を作動さゼ
ると、駆動軸5aは回転し、駆動軸5aとσ合するじゃ
ま板4aはチューブ3上を摺動して、スケールをかき落
しながら一方側へ移動する。また駆動軸5aが逆転する
と、逆方向に上記と同様に移動し、スチールをかき落し
ながら移動する。このようにしてスケールは除去される
。When scale precipitation begins, when the drive device 6 is activated, the drive shaft 5a rotates, and the baffle plate 4a, which is in σ alignment with the drive shaft 5a, slides on the tube 3 and scrapes off the scale. Move to one side. Further, when the drive shaft 5a is reversed, it moves in the opposite direction in the same manner as above, and moves while scraping off the steel. In this way scale is removed.
除去されたスケールは、胴体1下部に設けられたポケッ
ト9に落下しドレン排出口16より排出されるため、し
ゃま板4a下部の蒸気通路を狭くすることはない。The removed scale falls into the pocket 9 provided at the bottom of the body 1 and is discharged from the drain outlet 16, so that it does not narrow the steam passage under the baffle plate 4a.
またこのとき、薬液供給管15からスケール溶解に有効
な薬液または水を供給して、ノズル8から噴出し、スケ
ールを溶解させたり、洗浄したりしてスケール除去効果
を高めることもできる。At this time, a chemical solution or water effective for dissolving scale can be supplied from the chemical supply pipe 15 and ejected from the nozzle 8 to dissolve or wash the scale, thereby increasing the scale removal effect.
以上のようにしてスケールが容易に除去され、熱交換効
率の低下が防止される。As described above, scale is easily removed and a decrease in heat exchange efficiency is prevented.
[発明の効果] 以上に説明したように、本発明は次の効果を奏する。[Effect of the invention] As explained above, the present invention has the following effects.
(1) チューブの周りのスケールが容易に除去でき
る。(1) Scale around the tube can be easily removed.
(2)シたがって高い熱交換効率を維持できる。(2) Therefore, high heat exchange efficiency can be maintained.
(3)分解清掃のための予備器または代替設備が不要で
ある。(3) There is no need for spare equipment or alternative equipment for disassembly and cleaning.
(4)設備を停止することなく、連続運転ができる。(4) Continuous operation is possible without stopping the equipment.
第1図は本発明の一実施例の構成図、第2図は同実施例
の第1図の■−■視図、第3図は従来例の構成図、第4
図は同従来例の作用説明図である。
1・・・罰俸 2・・・管板3・・・チュ
ーブ(代表して1本のみ図示しである)4.4a・・・
じゃま板 5・・・スティバー5a・・・駆動軸
6・・・駆動装置7・・・鏡i
8・・・ノズル9・・・ボケ、ト10・・・ファンFig. 1 is a block diagram of an embodiment of the present invention, Fig. 2 is a perspective view of Fig. 1 of the same embodiment, Fig. 3 is a block diagram of a conventional example, and Fig. 4 is a block diagram of a conventional example.
The figure is an explanatory diagram of the operation of the conventional example. 1... Penalty salary 2... Tube plate 3... Tube (only one representative is shown) 4.4a...
Baffle plate 5...Stiver 5a...Drive shaft
6... Drive device 7... Mirror i
8...Nozzle 9...Bokeh, To 10...Fan
Claims (1)
を有するシェルアンドチューブ型熱交換器において、上
記チューブとほぼ直交して同チューブを通し摺動可能な
複数のじゃま板と、上記チューブにほぼ平行に設けられ
、周囲にねじを持つとともに上記じゃま板に螺合する駆
動軸と、同駆動軸を回転駆動する駆動手段とを備えてな
ることを特徴とするシェルアンドチューブ型熱交換器。In a shell-and-tube heat exchanger having tube sheets at both ends in the body and a plurality of tubes between the tube sheets, a plurality of baffle plates slidable through the tubes substantially perpendicular to the tubes; A shell-and-tube heat exchanger characterized by comprising: a drive shaft that is provided substantially parallel to the tube, has a thread around the periphery, and is screwed into the baffle plate; and a drive means that rotationally drives the drive shaft. exchanger.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP21429590A JPH0498099A (en) | 1990-08-15 | 1990-08-15 | Shell and tube type heat exchanger |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP21429590A JPH0498099A (en) | 1990-08-15 | 1990-08-15 | Shell and tube type heat exchanger |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0498099A true JPH0498099A (en) | 1992-03-30 |
Family
ID=16653366
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP21429590A Pending JPH0498099A (en) | 1990-08-15 | 1990-08-15 | Shell and tube type heat exchanger |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0498099A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR20200011480A (en) * | 2017-05-26 | 2020-02-03 | 알파 라발 올미 에스.피.에이 | Cylindrical Manifold Equipment with Bypass |
CN113776366A (en) * | 2021-09-24 | 2021-12-10 | 宁波安信化工装备有限公司 | Heat exchanger convenient to clean |
-
1990
- 1990-08-15 JP JP21429590A patent/JPH0498099A/en active Pending
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR20200011480A (en) * | 2017-05-26 | 2020-02-03 | 알파 라발 올미 에스.피.에이 | Cylindrical Manifold Equipment with Bypass |
US11073347B2 (en) | 2017-05-26 | 2021-07-27 | Alfa Laval Olmi S.P.A. | Shell-and-tube equipment with bypass |
CN113776366A (en) * | 2021-09-24 | 2021-12-10 | 宁波安信化工装备有限公司 | Heat exchanger convenient to clean |
CN113776366B (en) * | 2021-09-24 | 2023-11-07 | 宁波安信化工装备有限公司 | Heat exchanger capable of being cleaned conveniently |
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