JP2001129537A - Evaporative concentration apparatus - Google Patents

Evaporative concentration apparatus

Info

Publication number
JP2001129537A
JP2001129537A JP31559199A JP31559199A JP2001129537A JP 2001129537 A JP2001129537 A JP 2001129537A JP 31559199 A JP31559199 A JP 31559199A JP 31559199 A JP31559199 A JP 31559199A JP 2001129537 A JP2001129537 A JP 2001129537A
Authority
JP
Japan
Prior art keywords
scale
heat transfer
evaporator
transfer tube
evaporating
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
JP31559199A
Other languages
Japanese (ja)
Inventor
Koichi Hosoda
浩一 細田
Takumi Nanaumi
匠 七海
Tomoko Akiyama
知子 秋山
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.)
Organo Corp
Original Assignee
Organo Corp
Japan Organo Co Ltd
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 Organo Corp, Japan Organo Co Ltd filed Critical Organo Corp
Priority to JP31559199A priority Critical patent/JP2001129537A/en
Publication of JP2001129537A publication Critical patent/JP2001129537A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A20/00Water conservation; Efficient water supply; Efficient water use
    • Y02A20/124Water desalination
    • Y02A20/138Water desalination using renewable energy
    • Y02A20/141Wind power

Landscapes

  • Heat Treatment Of Water, Waste Water Or Sewage (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
  • Investigating Or Analysing Materials By Optical Means (AREA)
  • Cleaning In General (AREA)
  • Treating Waste Gases (AREA)

Abstract

PROBLEM TO BE SOLVED: To periodically monitor the gypsum scale bonded to the heat transfer pipe of an evaporative concentration apparatus to remove the same. SOLUTION: A scale detector 20 monitoring the surfaces of the heat transfer pipes 16 arranged in an evaporator 11 through the observation window 17 of the evaporator 11 is arranged. The scale detector 20 comprises a light source 18 and a photo-detection part 19 and periodically monitors the gypsum scale bonded to the heat transfer pipes 16 when a holding liquid 12 is circulated to be evaporated. When more than a predetermined quantity of scale is bonded, automatic acid washing is performed to remove the scale. The unmanned operation of an evaporative concentration apparatus is enabled and the operation cost thereof is reduced.

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、蒸発濃縮装置に関
し、更に詳しくは、石炭火力発電所からの排煙脱硫排水
である硫酸カルシウム含有排水を処理するために好適な
蒸発濃縮装置に関する。
The present invention relates to an evaporative concentration apparatus, and more particularly, to an evaporative concentration apparatus suitable for treating calcium sulfate-containing wastewater, which is flue gas desulfurization wastewater from a coal-fired power plant.

【0002】[0002]

【従来の技術】多くの石炭火力発電所では、公害の原因
となる燃料中の硫黄分を除去するために石灰石−石膏法
排煙脱硫装置が使用されている。この排煙脱硫装置から
排出される排煙脱硫排水等には、一般に、硫酸イオン及
びカルシウムイオンが高濃度で含まれている。従来、排
煙脱硫排水は、凝集沈殿処理等の方法によって処理され
た後に放流されていたが、近年、処理効率の向上のため
に蒸発濃縮装置を導入することが、各プラントエンジニ
アリングメーカから提案されている。
2. Description of the Related Art In many coal-fired power plants, a limestone-gypsum flue gas desulfurization unit is used to remove sulfur components in fuels that cause pollution. The flue gas desulfurization effluent discharged from the flue gas desulfurization device generally contains high concentrations of sulfate ions and calcium ions. Conventionally, flue gas desulfurization effluent is discharged after being treated by a method such as coagulation sedimentation treatment.In recent years, it has been proposed by each plant engineering manufacturer to introduce an evaporative concentration device to improve treatment efficiency. ing.

【0003】一般に、硫酸カルシウム含有排水を蒸発濃
縮する場合には、伝熱管等の伝熱部に石膏スケールが付
着し易く、このスケール付着によって、装置運転のエネ
ルギー効率が低下する。このようなスケール付着を防止
する幾つかの手段が知られており、pH調整、種晶とし
ての石膏粒子の添加、及び、スケール分散剤の添加等の
技術が提案されている(例えば、特開平9−13607
8号公報、及び、特開平10−192838号公報)。
In general, when evaporating and concentrating waste water containing calcium sulfate, gypsum scale easily adheres to a heat transfer section such as a heat transfer tube, and this scale adhesion lowers the energy efficiency of the operation of the apparatus. Several means for preventing such scale adhesion are known, and techniques such as pH adjustment, addition of gypsum particles as seed crystals, and addition of a scale dispersant have been proposed (for example, Japanese Patent Application Laid-Open No. 9-13607
No. 8 and JP-A-10-192838).

【0004】[0004]

【発明が解決しようとする課題】上記公報に記載の石膏
スケールの付着防止技術を採用しても、その防止効果に
は限界があり、実際に伝熱管に付着した石膏スケールを
酸洗浄等によって適宜除去しているのが実状である。こ
の場合、石膏スケールが伝熱管に付着したまま蒸発濃縮
装置を運転すると、比較的短時間の運転であっても、そ
の石膏スケールが硬化し、その後に酸洗浄を行っても所
望の効果が得られない。このため、石膏スケールの付着
状況を常時監視する必要があり、その監視のために蒸発
濃縮装置の運転コストが上昇するという問題があった。
Even if the gypsum scale adhesion prevention technology described in the above publication is adopted, its prevention effect is limited, and the gypsum scale actually adhering to the heat transfer tube is appropriately cleaned by pickling. The fact is that it has been removed. In this case, if the evaporating and concentrating apparatus is operated while the gypsum scale is attached to the heat transfer tube, the gypsum scale is hardened even if the operation is performed for a relatively short time, and the desired effect can be obtained even after performing acid washing. I can't. For this reason, it is necessary to constantly monitor the adhesion state of the gypsum scale, and there has been a problem that the operation cost of the evaporating and concentrating apparatus increases due to the monitoring.

【0005】本発明は、上記に鑑み、石膏スケールが付
着しても自動的に除去することができ、これによって、
無人運転を可能にして運転コストの低減を図った蒸発濃
縮装置を提供することを目的とする。
[0005] In view of the above, the present invention can automatically remove gypsum scale even if it adheres.
It is an object of the present invention to provide an evaporative concentration apparatus that enables unmanned operation and reduces operation costs.

【0006】[0006]

【課題を解決するための手段】上記目的を達成するため
に、本発明の蒸発濃縮装置は、加熱のための伝熱管を内
部に有する蒸発器と、保有液を循環させて前記伝熱管に
注ぐ循環装置とを備え、前記保有液を蒸発濃縮する蒸発
濃縮装置において、前記伝熱管の表面を周期的に監視
し、スケールの付着を検出するとスケール検知信号を出
力するスケール検知器と、前記スケール検知信号に応答
して前記伝熱管を洗浄する洗浄装置とを備えることを特
徴とする。
In order to achieve the above object, an evaporating and concentrating apparatus according to the present invention comprises: an evaporator having a heat transfer tube for heating therein; and a circulating liquid to be poured into the heat transfer tube. A evaporating and concentrating apparatus for evaporating and condensing the retained liquid, wherein the evaporating and concentrating apparatus periodically monitors a surface of the heat transfer tube and outputs a scale detection signal when scale adhesion is detected; A washing device for washing the heat transfer tube in response to a signal.

【0007】本発明の蒸発濃縮装置によると、周期的に
伝熱管表面へのスケールの付着の有無を検出し、スケー
ル付着を検出すると、自動的に伝熱管の洗浄が行われる
ので、蒸発濃縮装置の無人運転が可能となり、装置の運
転コストが削減可能となる。
According to the evaporative concentrator of the present invention, the presence or absence of scale adherence to the heat transfer tube surface is periodically detected, and when the scale is detected, the heat transfer tube is automatically cleaned. Unmanned operation becomes possible, and the operation cost of the apparatus can be reduced.

【0008】ここで、本発明の蒸発濃縮装置の好ましい
態様では、前記スケール検知器によるスケール付着の有
無の検出に先立って循環装置を停止させる。この場合、
循環液の散布に起因する視界の不良が除かれ、スケール
付着の有無の検出精度が向上する。
Here, in a preferred embodiment of the evaporative concentration apparatus of the present invention, the circulating apparatus is stopped before the scale detector detects the presence or absence of scale adhesion. in this case,
Poor visibility due to spraying of circulating fluid is eliminated, and the accuracy of detecting the presence or absence of scale adhesion is improved.

【0009】[0009]

【発明の実施の形態】以下、図面を参照し本発明の実施
形態例に基づいて本発明を更に詳細に説明する。図1
は、本発明の一実施形態例に係る蒸発濃縮装置の構成を
示す模式的ブロック図である。蒸発濃縮装置10は、全
体として円筒形状を有し底部が円錐形状を成す蒸発器1
1を有し、蒸発器11の底部には処理対象となる硫酸カ
ルシウムを含有する保有液12が収容されている。
DESCRIPTION OF THE PREFERRED EMBODIMENTS Hereinafter, the present invention will be described in more detail with reference to the drawings based on embodiments of the present invention. FIG.
FIG. 1 is a schematic block diagram illustrating a configuration of an evaporative concentration device according to an embodiment of the present invention. The evaporator 1 has an evaporator 1 having a cylindrical shape as a whole and a conical bottom.
1, a holding liquid 12 containing calcium sulfate to be treated is stored at the bottom of the evaporator 11.

【0010】蒸発器11内の保有液12は、蒸発器11
の下方に配置された循環ポンプ13によって、蒸発器1
1の底部から抜き出され、配管14を経由して蒸発器1
1内の頂部に設置されたディストリビュータ15に導か
れ、ディストリビュータ15によって蒸発器11の内部
で散布される。蒸発器11の内部には、水平方向に延び
る多数の伝熱管16が水平方向及び垂直方向に多数が並
んで配置されている。ディストリビュータ15によって
散布された保有液は、これら伝熱管16上に落下し、伝
熱管16内を流れる蒸気によって加熱されてその水分が
蒸発し、濃縮液となって蒸発器11の底部に落下する。
この保有液の循環を繰り返すことによって、発電所等か
らの排水である保有液が濃縮される。なお、蒸発により
保有液が減少した分だけ排水供給ライン22及び排水供
給弁23を介して排水を供給し、また適当な頻度で濃縮
液取出し弁24及び濃縮液排出ライン25を経由して濃
縮液を排出するような自動制御を行うことにより、保有
液の体積及び濃度はほぼ一定に保たれる。
The retained liquid 12 in the evaporator 11 is
Of the evaporator 1 by the circulation pump 13 arranged below the
1 is withdrawn from the bottom of the evaporator 1 via a pipe 14.
It is guided to a distributor 15 installed at the top of the inside 1, and is sprayed inside the evaporator 11 by the distributor 15. Inside the evaporator 11, a large number of heat transfer tubes 16 extending in the horizontal direction are arranged in a line in the horizontal direction and the vertical direction. The retained liquid sprayed by the distributor 15 falls onto the heat transfer tubes 16, is heated by the steam flowing in the heat transfer tubes 16, evaporates the water content, and falls as a concentrated liquid to the bottom of the evaporator 11.
By repeating the circulation of the retained liquid, the retained liquid, which is wastewater from a power plant or the like, is concentrated. The wastewater is supplied through the drainage supply line 22 and the wastewater supply valve 23 by an amount corresponding to the decrease in the retained liquid due to the evaporation, and the concentrated liquid is passed through the concentrated liquid takeoff valve 24 and the concentrated liquid discharge line 25 at an appropriate frequency. The volume and the concentration of the retained liquid are kept almost constant by performing automatic control for discharging water.

【0011】蒸発器11の側面には覗き窓17が設けら
れており、その覗き窓17の蒸発器11の外部には、光
源18及び光検出部19から成るスケール検知器20が
設置されている。光源18からの光は、覗き窓17を透
過して伝熱管16の表面に入射しており、その反射光が
覗き窓17を逆に透過して光検出部19に入射する。光
検出部19の出力信号は、制御部21に入力しており、
これを受けた制御部21は、伝熱管表面のスケール付着
の有無を判定する。制御部21は、この判定に基づいて
蒸発濃縮装置10の運転を制御する。
A viewing window 17 is provided on a side surface of the evaporator 11, and a scale detector 20 including a light source 18 and a light detection unit 19 is provided outside the evaporator 11 in the viewing window 17. . The light from the light source 18 passes through the viewing window 17 and is incident on the surface of the heat transfer tube 16, and the reflected light passes through the viewing window 17 and enters the photodetector 19. The output signal of the light detection unit 19 is input to the control unit 21.
Upon receiving this, the control unit 21 determines whether or not scale adheres to the heat transfer tube surface. The control unit 21 controls the operation of the evaporative concentration device 10 based on this determination.

【0012】図2は、上記蒸発濃縮装置の運転を示すフ
ローチャートである。濃縮装置は、その起動指令(ステ
ップS1)を受けて起動工程(ステップS2)に移行
し、付属ポンプやヒータ等がシーケンスプログラムに従
って起動され蒸発器内に排水が供給され、循環ポンプに
より循環される。一定の温度条件及び圧力条件等が満た
されると、保有液の蒸発が始まり、濃縮工程(ステップ
S3)に移行する。この濃縮工程中に、タイマの時間設
定に従って経過時間を計測する(ステップS4)。
FIG. 2 is a flow chart showing the operation of the evaporative concentration apparatus. Upon receiving the start command (step S1), the concentrating apparatus shifts to a start step (step S2), in which an attached pump, a heater, and the like are started according to a sequence program, drainage is supplied into the evaporator, and circulated by the circulation pump. . When certain temperature conditions, pressure conditions, and the like are satisfied, evaporation of the retained liquid starts, and the process proceeds to the concentration step (Step S3). During this concentration step, the elapsed time is measured according to the time setting of the timer (step S4).

【0013】濃縮工程に移行した後、所定の時間が経過
すると、保有液の循環を停止し(ステップS5)、光検
出器の出力を調べ、スケール付着の有無を判定する(ス
テップS6)。光検出器の出力に異常がない(スケール
の付着なし)と判断されると、再びステップS3の濃縮
工程に戻り、保有液を循環しつつ濃縮する。ステップS
6で光検出器の出力に異常があり、スケールの付着あり
と判断されると、ステップS7の洗浄工程に移行する。
[0013] After a predetermined time has passed after the shift to the concentration step, the circulation of the retained liquid is stopped (step S5), and the output of the photodetector is examined to determine whether or not scale has adhered (step S6). If it is determined that there is no abnormality in the output of the photodetector (no scale is attached), the process returns to the concentration step of step S3, and the concentration is performed while circulating the retained liquid. Step S
If it is determined in step 6 that the output of the photodetector is abnormal and that the scale is attached, the flow shifts to the cleaning step of step S7.

【0014】ステップS7の洗浄工程では、図1に図示
しない洗浄液導入管から酸等の洗浄液が導入されて、1
時間程度の洗浄液の循環による伝熱管の化学洗浄が行わ
れる。次いで、ステップS8に移行し、再び光検出器の
出力が調べられ、伝熱管の洗浄が有効に行われたか否か
が判断される。所望の洗浄効果が得られなかったと判断
された場合には、ステップS9でその洗浄回数を判断し
て、再びステップS7の洗浄工程に戻り、化学洗浄を繰
り返す。ステップS9で洗浄工程が所定時間内に所定回
数Nを越えたと判断された場合には、最終的に所望の洗
浄効果が得られないものとして、アラームを出して装置
を停止する(ステップS11)。
In the cleaning step of step S7, a cleaning liquid such as an acid is introduced from a cleaning liquid introduction pipe not shown in FIG.
Chemical cleaning of the heat transfer tube is performed by circulating a cleaning solution for about an hour. Next, the process proceeds to step S8, where the output of the photodetector is checked again to determine whether the heat transfer tube has been effectively cleaned. If it is determined that the desired cleaning effect has not been obtained, the number of times of cleaning is determined in step S9, and the process returns to the cleaning step of step S7 to repeat the chemical cleaning. If it is determined in step S9 that the number of times of the cleaning process has exceeded the predetermined number N within the predetermined time, it is determined that the desired cleaning effect cannot be finally obtained, an alarm is issued, and the apparatus is stopped (step S11).

【0015】一方、ステップS8で所望の洗浄効果が得
られたと判断された場合には、ステップS10に移行
し、装置の初期設定を確認し、再びステップS3の濃縮
工程に移行するか、或いは、ステップS11の停止工程
に移行するかを、その初期設定に基づいて判断する。
On the other hand, if it is determined in step S8 that the desired cleaning effect has been obtained, the flow shifts to step S10, confirms the initial settings of the apparatus, and shifts again to the concentration step in step S3, or Whether to shift to the stop step of step S11 is determined based on the initial setting.

【0016】上記実施形態例では、蒸発濃縮器の蒸発器
11の内部が高温且つ腐食雰囲気であることに鑑み、ス
ケール検知器20を蒸発器11の外部に設置した。しか
し、これに代えてスケール検知器を内部に配置してもよ
い。一般に、伝熱管に付着した石膏スケールは、伝熱管
の金属光沢面の場合よりも反射光を弱めるため、伝熱管
への石膏スケールの付着は反射光を検出することで可能
である。光源としては、発光ダイオード(LED)又は
半導体レーザ等を利用することが好ましく、また、光検
出部19としては、通常の光センサの他に、白黒CCD
カメラや、カラーCCDカメラ等が利用できる。カラー
CCDカメラ等を利用する場合には、石膏スケールの白
色が容易に検出できる。特に、石膏スケールが鉄分を含
有する場合には赤みがかった色を帯びるので、この場合
にはカラーCCDカメラの使用が特に好ましい。
In the above embodiment, the scale detector 20 is provided outside the evaporator 11 in consideration of the high temperature and corrosive atmosphere inside the evaporator 11 of the evaporator. However, a scale detector may be arranged inside instead. Generally, gypsum scale attached to a heat transfer tube weakens reflected light as compared with the case of a metallic glossy surface of the heat transfer tube, so that gypsum scale can be attached to the heat transfer tube by detecting reflected light. It is preferable to use a light emitting diode (LED) or a semiconductor laser as a light source, and as the light detecting unit 19, besides a normal light sensor, a monochrome CCD
Cameras and color CCD cameras can be used. When a color CCD camera or the like is used, the white color of the gypsum scale can be easily detected. In particular, when the gypsum scale contains iron, the color becomes reddish. In this case, it is particularly preferable to use a color CCD camera.

【0017】光検出部19の出力レベルの判定には、予
め実験的に決定したしきい値を設定する。特に、伝熱管
16の表面の反射が良好な位置に予め光源18及び光検
出部19を設定し、その上でしきい値を設定することが
好ましい。また、伝熱管16上で石膏スケールが付着し
やすい位置は、蒸発器11の構造やディストリビュータ
15の配置等により、装置毎に大きく異なる。従って、
石膏スケールが付着しやすい伝熱管位置も装置毎に調査
することが好ましい。
To determine the output level of the light detecting section 19, a threshold value experimentally determined in advance is set. In particular, it is preferable to set the light source 18 and the light detection unit 19 in advance at a position where the reflection on the surface of the heat transfer tube 16 is good, and then set the threshold value thereon. Further, the position on the heat transfer tube 16 where the gypsum scale is likely to adhere greatly differs from device to device depending on the structure of the evaporator 11, the arrangement of the distributor 15, and the like. Therefore,
It is preferable to investigate the position of the heat transfer tube to which the gypsum scale easily adheres for each device.

【0018】以上、本発明をその好適な実施形態例に基
づいて説明したが、本発明の蒸発濃縮装置は、上記実施
形態例の構成にのみ限定されるものではなく、上記実施
形態例の構成から種々の修正及び変更を施したものも、
本発明の範囲に含まれる。
Although the present invention has been described based on the preferred embodiment, the evaporating and concentrating apparatus of the present invention is not limited to the configuration of the above-described embodiment, but rather the configuration of the embodiment. Various modifications and changes from
It is included in the scope of the present invention.

【0019】[0019]

【発明の効果】以上、説明したように、本発明の蒸発濃
縮装置によると、伝熱管の表面に付着するスケールを周
期的に監視し、スケールが付着した旨が検出された場合
にはこれを洗浄装置によって除去する構成を採用したの
で、蒸発濃縮装置の無人運転が可能となり、装置の運転
コストが低減できる効果がある。
As described above, according to the evaporating and concentrating apparatus of the present invention, the scale adhering to the surface of the heat transfer tube is periodically monitored, and when the adhering of the scale is detected, the scale is detected. Since the configuration in which the evaporating and concentrating device is removed by the cleaning device is employed, an unmanned operation of the evaporating and concentrating device can be performed, and the operation cost of the device can be reduced.

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

【図1】本発明の一実施形態例に係る蒸発濃縮器のブロ
ック図。
FIG. 1 is a block diagram of an evaporative concentrator according to an embodiment of the present invention.

【図2】図1の蒸発濃縮器の動作を示すフローチャー
ト。
FIG. 2 is a flowchart showing the operation of the evaporative concentrator of FIG.

【符号の説明】[Explanation of symbols]

10:蒸発濃縮器 11:蒸発器 12:保有液 13:循環ポンプ 14:循環配管 15:ディストリビュータ 16:伝熱管 17:覗き窓 18:光源 19:光検出部 20:スケール検知器 21:制御部 22:排水供給ライン 23:排水供給弁 24:濃縮廃液取出し弁 25:濃縮液排出ライン 10: Evaporation concentrator 11: Evaporator 12: Retained liquid 13: Circulation pump 14: Circulation pipe 15: Distributor 16: Heat transfer tube 17: Viewing window 18: Light source 19: Light detection unit 20: Scale detector 21: Control unit 22 : Drainage supply line 23 : Drainage supply valve 24 : Concentrated waste liquid discharge valve 25 : Concentrated liquid discharge line

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) B01D 53/77 C02F 5/00 610J B08B 9/023 620B C02F 1/00 G01N 21/47 B 5/00 610 B01D 53/34 125R 620 B08B 9/02 D G01N 21/47 (72)発明者 秋山 知子 東京都江東区新砂1丁目2番8号 オルガ ノ株式会社内 Fターム(参考) 2G059 AA05 BB08 CC01 EE02 GG01 GG02 HH02 KK04 MM05 3B116 AA13 AB53 BB62 CD42 CD43 4D002 AA02 AC01 BA02 BA20 CA01 DA05 DA16 EA07 FA03 GA02 GA03 GB20 HA05 4D034 AA11 BA07 CA18 4D076 AA06 AA07 BA14 BA23 CD42 CD43 DA05 DA25 EA08X EA26X EA49 HA06 JA02 JA03 ──────────────────────────────────────────────────の Continued on the front page (51) Int.Cl. 7 Identification code FI Theme coat ゛ (Reference) B01D 53/77 C02F 5/00 610J B08B 9/023 620B C02F 1/00 G01N 21/47 B 5/00 610 B01D 53/34 125R 620 B08B 9/02 D G01N 21/47 (72) Inventor Tomoko Akiyama 1-2-8 Shinsuna, Koto-ku, Tokyo Organo Corporation F-term (reference) 2G059 AA05 BB08 CC01 EE02 GG01 GG02 HH02 KK04 MM05 3B116 AA13 AB53 BB62 CD42 CD43 4D002 AA02 AC01 BA02 BA20 CA01 DA05 DA16 EA07 FA03 GA02 GA03 GB20 HA05 4D034 AA11 BA07 CA18 4D076 AA06 AA07 BA14 BA23 CD42 CD43 DA05 DA25 EA08 JA03 JA03

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 加熱のための伝熱管を内部に有する蒸発
器と、保有液を循環させて前記伝熱管に注ぐ循環装置と
を備え、前記保有液を蒸発濃縮する蒸発濃縮装置におい
て、 前記伝熱管の表面を周期的に監視し、スケールの付着を
検出するとスケール検知信号を出力するスケール検知器
と、 前記スケール検知信号に応答して前記伝熱管を洗浄する
洗浄装置とを備えることを特徴とする蒸発濃縮装置。
1. An evaporating and concentrating apparatus, comprising: an evaporator internally having a heat transfer tube for heating; and a circulating device for circulating a retained liquid and pouring the retained liquid into the heat transfer tube. The surface of the heat tube is periodically monitored, and a scale detector that outputs a scale detection signal when scale adhesion is detected; and a cleaning device that cleans the heat transfer tube in response to the scale detection signal. Evaporating concentrator.
【請求項2】 前記スケール検知器によるスケール付着
の有無の検出に先立って循環装置を停止させる、請求項
1に記載の蒸発濃縮装置。
2. The evaporating and concentrating apparatus according to claim 1, wherein a circulation device is stopped before the scale detector detects the presence or absence of scale adhesion.
JP31559199A 1999-11-05 1999-11-05 Evaporative concentration apparatus Pending JP2001129537A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP31559199A JP2001129537A (en) 1999-11-05 1999-11-05 Evaporative concentration apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP31559199A JP2001129537A (en) 1999-11-05 1999-11-05 Evaporative concentration apparatus

Publications (1)

Publication Number Publication Date
JP2001129537A true JP2001129537A (en) 2001-05-15

Family

ID=18067207

Family Applications (1)

Application Number Title Priority Date Filing Date
JP31559199A Pending JP2001129537A (en) 1999-11-05 1999-11-05 Evaporative concentration apparatus

Country Status (1)

Country Link
JP (1) JP2001129537A (en)

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KR100960393B1 (en) 2009-12-18 2010-05-28 주식회사 스케일크리너 System for monitoring the scale state of a pipe and scaling the pipe
WO2012128257A1 (en) * 2011-03-22 2012-09-27 三菱重工業株式会社 Exhaust gas processing system and method, spray-drying device and method for dehydrated filtrate from desulfurization wastewater
KR101317757B1 (en) 2011-11-28 2013-10-18 장동현 Apparatus for treatment wastewater
CN107042063A (en) * 2017-06-21 2017-08-15 大唐环境产业集团股份有限公司 A kind of absorption tower observation device
JP2019015427A (en) * 2017-07-04 2019-01-31 オルガノ株式会社 cooling tower
JP2021004759A (en) * 2019-06-25 2021-01-14 栗田工業株式会社 Fouling diagnosis device of wetted member
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Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100960393B1 (en) 2009-12-18 2010-05-28 주식회사 스케일크리너 System for monitoring the scale state of a pipe and scaling the pipe
WO2012128257A1 (en) * 2011-03-22 2012-09-27 三菱重工業株式会社 Exhaust gas processing system and method, spray-drying device and method for dehydrated filtrate from desulfurization wastewater
US8715402B2 (en) 2011-03-22 2014-05-06 Mitsubishi Heavy Industries, Ltd. Air pollution control system and air pollution control method, spray drying device of dewatering filtration fluid from desulfurization discharged water, and method thereof
US8883107B2 (en) 2011-03-22 2014-11-11 Mitsubishi Heavy Industries, Ltd. Air pollution control system, air pollution control method, spray drying device of dewatering filtration fluid from desulfurization discharged water, and method thereof
US9409117B2 (en) 2011-03-22 2016-08-09 Mitsubishi Hitachi Power Systems, Ltd. Air pollution control system, air pollution control method, spray drying device of dewatering filtration fluid from desulfurization discharged water, and method thereof
KR101317757B1 (en) 2011-11-28 2013-10-18 장동현 Apparatus for treatment wastewater
CN107042063A (en) * 2017-06-21 2017-08-15 大唐环境产业集团股份有限公司 A kind of absorption tower observation device
JP2019015427A (en) * 2017-07-04 2019-01-31 オルガノ株式会社 cooling tower
JP2021004759A (en) * 2019-06-25 2021-01-14 栗田工業株式会社 Fouling diagnosis device of wetted member
JP7259590B2 (en) 2019-06-25 2023-04-18 栗田工業株式会社 Fouling diagnosis device for wetted parts
WO2022065322A1 (en) * 2020-09-25 2022-03-31 株式会社ササクラ Management device managing vacuum vaporization-type fresh water generation device
CN113458093A (en) * 2021-07-16 2021-10-01 光大环保技术研究院(南京)有限公司 Synchronous flushing distribution pipe of direct contact type evaporator and use method thereof

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