JP2012176336A - Pipe washing method in nuclear power plant - Google Patents
Pipe washing method in nuclear power plant Download PDFInfo
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- JP2012176336A JP2012176336A JP2011039280A JP2011039280A JP2012176336A JP 2012176336 A JP2012176336 A JP 2012176336A JP 2011039280 A JP2011039280 A JP 2011039280A JP 2011039280 A JP2011039280 A JP 2011039280A JP 2012176336 A JP2012176336 A JP 2012176336A
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- 238000000034 method Methods 0.000 title claims abstract description 58
- 238000005406 washing Methods 0.000 title abstract description 31
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 131
- 238000001914 filtration Methods 0.000 claims abstract description 31
- 238000001125 extrusion Methods 0.000 claims abstract description 15
- 238000011084 recovery Methods 0.000 claims abstract description 11
- 238000004140 cleaning Methods 0.000 claims description 104
- 238000004519 manufacturing process Methods 0.000 claims description 15
- 238000010276 construction Methods 0.000 claims description 12
- 238000003860 storage Methods 0.000 claims description 9
- 238000004065 wastewater treatment Methods 0.000 claims description 8
- 238000007667 floating Methods 0.000 claims description 3
- 239000008213 purified water Substances 0.000 claims description 2
- 238000005429 filling process Methods 0.000 abstract description 3
- 238000007599 discharging Methods 0.000 abstract 1
- 239000012535 impurity Substances 0.000 description 8
- 239000000428 dust Substances 0.000 description 6
- 238000007796 conventional method Methods 0.000 description 3
- 230000000717 retained effect Effects 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 238000003466 welding Methods 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 238000011001 backwashing Methods 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- 230000003449 preventive effect Effects 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 230000003442 weekly effect Effects 0.000 description 2
- 125000004122 cyclic group Chemical group 0.000 description 1
- 230000001934 delay Effects 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- QOSATHPSBFQAML-UHFFFAOYSA-N hydrogen peroxide;hydrate Chemical compound O.OO QOSATHPSBFQAML-UHFFFAOYSA-N 0.000 description 1
- 238000007689 inspection Methods 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000006386 neutralization reaction Methods 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 238000010248 power generation Methods 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 230000002035 prolonged effect Effects 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 238000004904 shortening Methods 0.000 description 1
- 229920001897 terpolymer Polymers 0.000 description 1
- 229910021642 ultra pure water Inorganic materials 0.000 description 1
- 239000012498 ultrapure water Substances 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
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Abstract
Description
本発明は、配管洗浄方法であって、特に原子力発電所の建設時等における配管洗浄方法に関するものである。 The present invention relates to a pipe cleaning method, and more particularly to a pipe cleaning method during construction of a nuclear power plant.
原子力発電プラントにおける建設時の配管洗浄工程では、工程遅延ポテンシャルを抑えつつ、純水製造能力と貯水可能量を考慮しながら水使用計画を作成し、作業を実施するという課題がある。以下にその背景を説明する。 In the pipe cleaning process at the time of construction in a nuclear power plant, there is a problem that a water use plan is created and the work is carried out in consideration of pure water production capacity and water storage capacity while suppressing process delay potential. The background will be described below.
原子力発電プラントにおける配管洗浄作業は、各系統の使用流体別に、純水やろ過水を使用する水洗浄、油を使用するオイル洗浄、空気や窒素などの気体を使用する気体洗浄の3種類の洗浄方法を用いており、純水を洗浄流体として使用する洗浄方法がその大半を占める。 There are three types of pipe cleaning work in nuclear power plants: water cleaning using pure water and filtered water, oil cleaning using oil, and gas cleaning using gas such as air and nitrogen, depending on the fluid used in each system. Most of the cleaning methods use pure water as a cleaning fluid.
純水を用いる洗浄方法は、図3に示す様に「水張り」、「押出し洗浄」、「循環洗浄」、「水質判定」、「排水処理」の5つの作業工程で構成される。 As shown in FIG. 3, the cleaning method using pure water is composed of five work steps of “water filling”, “extrusion cleaning”, “circulation cleaning”, “water quality determination”, and “drainage treatment”.
S31「水張り」は、配管内面に付着する配管防錆剤などの水溶性不純物を水に溶解除去させることを目的とし、洗浄対象系統と配管洗浄設備を満水状態にする。 S31 “water filling” is intended to dissolve and remove water-soluble impurities such as a pipe rust preventive agent adhering to the inner surface of the pipe in water, and fills the system to be cleaned and the pipe cleaning equipment with water.
S32「押出し洗浄」は、S31の「水張り」時に溶解した水溶性不純物や、微少粒径で沈殿せず水中に浮遊する微細粉塵(濁度成分)、溶接ノロなどの異物を系統外へ排出することを目的とし、洗浄対象となる洗浄対象系統と配管洗浄設備からなる配管系統の保有水量の4〜5倍程度の大容量の水を全洗浄対象系統に対し一気に押し流す。洗浄対象系統と配管洗浄設備は閉ループを構成せず、洗浄対象系統内を通過した水は直接排水設備へ排出される。S33「循環洗浄」は、洗浄対象系統内を通過した水が循環ストレーナ(ろ過器)などの異物捕捉装置を経由してまた系統内へ戻るよう、洗浄対象系統と配管洗浄設備を閉ループで構成し、「押出し洗浄」を実施した後に水中に残留する濁度成分以外の固形異物を捕捉することを目的とする。 S32 “extrusion cleaning” discharges foreign matters such as water-soluble impurities dissolved during “water filling” in S31, fine dust (turbidity component) that does not precipitate and floats in the water, and welding dust from the system. For this purpose, a large volume of water about 4 to 5 times the amount of water held in the piping system consisting of the cleaning target system and the piping cleaning equipment to be cleaned is swept away all over the cleaning target system. The system to be cleaned and the pipe cleaning facility do not form a closed loop, and the water that has passed through the system to be cleaned is directly discharged to the drainage facility. S33 “Circulation cleaning” is a system that configures the system to be cleaned and the pipe cleaning equipment in a closed loop so that the water that has passed through the system to be cleaned returns to the system through a foreign matter trapping device such as a circulating strainer (filter). The purpose is to capture solid foreign substances other than the turbidity component remaining in the water after performing the “extrusion cleaning”.
S34「水質判定」は、「循環洗浄」作業後に、洗浄水の水質(不純物や濁度)および残留する異物が規定値以下であることを確認する。S35「排水処理」は、上記洗浄作業中に洗浄対象系統と配管洗浄設備から排出した排水の水質が規定値以下となるよう中和や沈降分離等の水質処理を行う。 S34 “Water quality determination” confirms that the water quality (impurities and turbidity) of the cleaning water and the remaining foreign matter are below the specified values after the “circular cleaning” operation. In S35 “drainage treatment”, water quality treatment such as neutralization and sedimentation separation is performed so that the quality of the wastewater discharged from the system to be washed and the pipe washing equipment during the washing operation is not more than a specified value.
原子力発電プラントでは、その発電方法から水を貯水および製造する設備を有しており、その貯水可能量は純水用およびろ過水用の貯水設備を合計すると4、000m3程度、純水製造能力は約750m3/日が通例である。 The nuclear power plant has a facility for water storage and production of water from the power generation method, the water storage amount The total water storage facilities for pure water and for filtration of water 4,000 m 3 approximately, pure water production capacity Is usually about 750 m 3 / day.
純水製造装置は、製造装置のメンテナンス性などから連続使用制限があり一週間の稼動日は6日程度が限界である。それを踏まえると、純水製造量は週換算で約4、500m3/週、月換算で約18、000m3/月が通例である。 The pure water production apparatus has a continuous use restriction due to the maintainability of the production apparatus and the like, and the working day of a week is limited to about 6 days. Based on this, the pure water production is usually about 4,500 m 3 / week on a weekly basis and about 18,000 m 3 / month on a monthly basis.
従来の配管洗浄方法では、月単位で水使用量を考えた場合、純水を18、000から20、000m3程度必要とする期間が2〜3ヶ月連続する。また、週単位で考えた場合、純水使用量のピーク期では、半月(2週)で7、000m3を超える純水使用量が必要な洗浄作業がほぼ連続する。このため、純水製造能力を考慮し、系統毎の洗浄作業の実施間隔を空けることができるよう、工程を設定する必要がある。さらに、緻密な純水使用計画を立てないと、貯水量に制限があることから貯水可能量を超える可能性がある。特に同一プラントでの継続号機の建設では、既設号機の定期検査時の水使用量も考慮する必要があり、純水使用量の管理が非常に難しい問題となっている。 In the conventional pipe cleaning method, when the amount of water used is considered on a monthly basis, a period requiring about 18,000 to 20,000 m 3 of pure water continues for 2 to 3 months. Further, when considered on a weekly basis, in the peak period of pure water usage, cleaning operations that require a pure water usage exceeding 7,000 m 3 are almost continuous in half a month (2 weeks). For this reason, it is necessary to set a process in consideration of the pure water production capacity so that an interval between cleaning operations for each system can be made. Furthermore, unless a precise plan for pure water use is made, there is a possibility that the amount of water that can be stored will be exceeded due to the limited amount of water stored. In particular, in the construction of a continuous unit in the same plant, it is necessary to consider the amount of water used at the regular inspection of the existing units, which makes it very difficult to manage the amount of pure water used.
工程面では、工程を自由に変更できる裕度があれば、系統毎の洗浄作業の実施間隔を空けることができるよう工程を設定することも可能である。ただし、配管洗浄の実施時期は配管群の据付期間の最終盤となり、その直後には系統全体で実施する試運転が控えているため、配管洗浄作業期間の延長や実施時期の延期は非常に難しく、プラント建設工程全体のクリティカルパスを左右する問題に直結してしまうこととなる。 In terms of process, if there is a margin that allows the process to be freely changed, it is possible to set the process so that the cleaning operation interval for each system can be increased. However, the pipe cleaning time will be the final stage of the pipe group installation period, and immediately after that, the trial run to be carried out on the entire system is refrained, so it is very difficult to extend the pipe cleaning work period and postponement of the execution time. This leads to a problem that affects the critical path of the entire plant construction process.
従来の工法では上記で述べた背景があり、配管洗浄では工程遅延ポテンシャルを抑えつつ、純水製造能力と貯水可能量を考慮しながら水使用計画を行い、作業を実施する必要があるという課題があった。 The conventional method has the background described above, and pipe cleaning has a problem that it is necessary to carry out work by planning the water use while considering the pure water production capacity and possible storage capacity while suppressing the process delay potential. there were.
以下に特許文献1、2について図4の工程図を用いて説明する。特許文献1では「押出し洗浄」工程が省かれ、S41の「水張り」の後に直ちにS43の「循環洗浄」に移行する。S44「水質判定」、S45「排水処理」は図3と同様に行う。 Patent Documents 1 and 2 will be described below with reference to the process diagram of FIG. In Patent Document 1, the “extrusion cleaning” step is omitted, and immediately after “water filling” in S41, the process proceeds to “circulation cleaning” in S43. S44 “water quality determination” and S45 “drainage treatment” are performed in the same manner as in FIG.
S43「循環洗浄」では、循環ストレーナと循環フィルタを用いて比較的大きな異物の捕捉と微細異物の捕捉とを行う。従って水使用量の問題は解決するが、押出し洗浄作業工程を実施せず懸濁物質を取り除くろ過装置を用いることにより別の課題が発生する。押出し洗浄を実施しない特許文献1では、懸濁物質を捕捉するため循環フィルタにろ過精度が100μm以下の非常に微細なフィルタを用いる。このとき、押出し洗浄にてその大半を系統外へ排出していた懸濁物質が循環閉ループ内に留まり、その全てが循環通水の初期段階に高ろ過精度のフィルタに通水されるため循環フィルタの目詰まりが多発する。これに伴い、フィルタ逆洗回数の増加やフィルタ交換など高ろ過精度の循環フィルタのメンテナンス作業が洗浄作業工程中に発生し、洗浄作業工程自体の長期化をもたらし、建設全体のクリティカル工程を左右する工程遅延ポテンシャルが発生することとなる。 In S43 “circulation cleaning”, a relatively large foreign matter and a fine foreign matter are caught using a circulation strainer and a circulation filter. Therefore, although the problem of the amount of water used is solved, another problem arises by using a filtration device that removes suspended substances without carrying out the extrusion washing operation process. In Patent Document 1 in which extrusion cleaning is not performed, a very fine filter having a filtration accuracy of 100 μm or less is used as a circulation filter in order to capture suspended substances. At this time, most of the suspended solids discharged out of the system by extrusion cleaning remain in the closed loop, and all of them are passed through a filter with high filtration accuracy in the initial stage of circulating water. Clogging frequently occurs. Along with this, maintenance work for high-filtration precision circulation filters, such as increasing the number of filter backwashes and filter replacement, occurs during the cleaning work process, resulting in prolonged cleaning work process itself and affecting the critical process of the entire construction. A process delay potential is generated.
特許文献2においても、孔径2.5μm程度の非常に微細なフィルタを用いるため、特許文献1と同様にフィルタの日詰まりが多発し、循環フィルタのメンテナンス作業に伴う工程遅延ポテンシャルが発生することとなる。 Also in Patent Document 2, since a very fine filter having a pore diameter of about 2.5 μm is used, the filter is clogged frequently as in Patent Document 1, and a process delay potential associated with maintenance work of the circulation filter is generated. Become.
特許文献3は、対象を超純水製造および供給装置に限定しており、また微粒子の剥離や分散に塩基性過酸化水素水を用いる特殊洗浄方法であるため、原子力発電設備の建設時等の配管洗浄作業とは技術分野が異なり、また洗浄の対象も水溶性不純物や溶接ノロ、粉塵などの異物を対象としていない。
特許文献4は、実施形態に示すように水洗浄のうち高圧ジェット洗浄を対象とするものであり、設備構成も図1とは異なり、またその廃液処理方法を示すものであるため対象とする技術分野が異なる。 Patent Document 4 is intended for high-pressure jet cleaning of water cleaning as shown in the embodiment, and the equipment configuration is different from that shown in FIG. The fields are different.
原子力発電所の建設時等に実施する配管洗浄作業において、従来工法および公知例で
は、以下の課題が挙げられる。
(1)循環洗浄工程において、微細フィルタを用い初期通水すると、有機配管防錆剤と、配管内の粉塵、溶接ノロなどの異物によりフィルタの目詰まりを起こす。この微細フィルタの目詰まりにより逆洗や清掃などの追加作業が発生し、洗浄期間延長の要因となる。
(2)今後計画されている原子力プロジェクトの建設(建築工程)は、環境影響やコスト縮減の観点から、現状よりも更なる工程短縮が要求されており、予想することが難しい建設工事終盤での(1)による工事工程遅延等の影響は非常に厳しい状況を産むため、抜本的な改善が一段と求められている。
(3)原子力発電所の配管洗浄作業は、膨大な純水使用量を要するため水使用量の低減が課題である。
In the pipe cleaning work carried out at the time of construction of a nuclear power plant, the following problems are raised in the conventional method and known examples.
(1) In the circulation cleaning process, when the initial water flow is performed using a fine filter, the filter is clogged with the organic pipe anticorrosive agent and foreign matters such as dust and welding dust in the pipe. Due to the clogging of the fine filter, additional work such as backwashing and cleaning occurs, which causes an extension of the cleaning period.
(2) The construction of the nuclear project (construction process) planned in the future requires further process shortening than the current situation from the viewpoint of environmental impact and cost reduction. Since the effects of construction process delays due to (1) are very severe, drastic improvements are required.
(3) Pipe cleaning work at nuclear power plants requires a large amount of pure water to be used, so reducing the amount of water used is an issue.
本発明は、純水製造装置から供給された純水を洗浄用ポンプを有する供給系統を経由して洗浄対象系統に供給し、洗浄対象系統得を洗浄した後の洗浄水を循環ストレーナーとろ過フィルターと水質判定装置を有する回収系統に回収し、さらに排水処理設備に接続する排水系統と、前記供給系統に接続する循環系統とに分岐させる配管洗浄設備を有する原子力発電プラントの配管洗浄方法において、前記配管洗浄設備と洗浄対象系統に純水を充填する水張り工程と、前記配管洗浄設備と洗浄対象系統の保有水量の1乃至2倍程度の純水を前記供給系統、洗浄対象系統、回収系統、排水系統を経由して前記排水処理設備に排水する押出し洗浄工程と、純水を前記供給系統、洗浄対象系統、回収系統における前記循環ストレーナー及び前記ろ過フィルター、前記循環系統を経由して循環させる循環洗浄工程とを有することを特徴とする。 The present invention supplies pure water supplied from a pure water production apparatus to a system to be cleaned via a supply system having a cleaning pump, and the cleaning water after cleaning the system to be cleaned is supplied with a circulation strainer and a filtration filter. In a pipe cleaning method for a nuclear power plant having a pipe cleaning facility for branching into a drainage system connected to a wastewater treatment facility and a circulation system connected to the supply system, The water filling process for filling the pipe cleaning equipment and the system to be cleaned with pure water, and the supply system, the system to be cleaned, the recovery system, and the drainage of pure water about 1 to 2 times the amount of water held in the pipe cleaning equipment and the system to be cleaned An extrusion cleaning process for draining the wastewater treatment facility via a system, and the circulating strainer and the filtration filter in the supply system, the system to be cleaned, and the recovery system. Terpolymer, and having a circulation cleaning process of circulating through the circulation system.
また、原子力発電プラントの配管洗浄方法において、前記洗浄対象系統は原子力発電プラントの建設時の配管系統であることを特徴とする。 Further, in the pipe cleaning method for a nuclear power plant, the system to be cleaned is a pipe system at the time of construction of the nuclear power plant.
また、原子力発電プラントの配管洗浄方法において、前記ろ過フィルターのろ過精度は、前記循環ストレーナーのろ過精度より細かく、水中に浮遊する微細異物を捕捉するサイズであることを特徴とする。 In the pipe cleaning method of a nuclear power plant, the filtration accuracy of the filtration filter is finer than the filtration accuracy of the circulation strainer, and is a size that captures fine foreign matters floating in water.
また、原子力発電プラントの配管洗浄方法において、前記ろ過フィルターのろ過精度は、0.1〜100ミクロンであり、前記循環ストレーナーのろ過精度は60〜120メッシュであることを特徴とする。 In the pipe cleaning method for a nuclear power plant, the filtration accuracy of the filtration filter is 0.1 to 100 microns, and the filtration accuracy of the circulation strainer is 60 to 120 mesh.
また、原子力発電プラントの配管洗浄方法において、前記洗浄対象系統を洗浄後の純水の水質が規定値以下であることを確認する水質判定工程を有することを特徴とする。 The pipe cleaning method for a nuclear power plant further includes a water quality determination step for confirming that the quality of pure water after cleaning the system to be cleaned is below a specified value.
また、原子力発電プラントの配管洗浄方法において、前記配管洗浄設備は、前記純水製造装置により製造した純水を貯留する貯水タンクを有することを特徴とする。 Further, in the pipe cleaning method for a nuclear power plant, the pipe cleaning equipment includes a water storage tank for storing pure water produced by the pure water production apparatus.
本発明は、系統保有水量の1乃至2倍程度の水を使用する押出し洗浄を実施することで、従来工法の問題点であった水使用量を大幅に削減するとともに、水張り作業で水に溶解した不純物の残留を防ぎ系統外排出を行うことが可能となる。 The present invention drastically reduces the amount of water used, which was a problem of the conventional method, by performing extrusion cleaning using water that is about 1 to 2 times the amount of water retained in the system, and is dissolved in water by water filling work. It is possible to prevent the remaining impurities from being discharged out of the system.
また、ろ過フィルタを含む設備構成において循環洗浄を実施することで、水使用量を低減した押出し洗浄を採用することに伴う残留微細異物の捕捉を行うとともに、捕捉時間増加とともにフィルターに蓄積する微細異物について、低水使用量で事前に押出し洗浄を行うことでその大半を排出することが可能となり、フィルターの目詰まり回数を低減し、逆洗や清掃等の追加作業を削減することが可能となる。 In addition, by carrying out cyclic cleaning in the equipment configuration including the filtration filter, it captures residual fine foreign matter that accompanies the adoption of extrusion cleaning with reduced water consumption, and fine foreign matter that accumulates in the filter as the capture time increases As a result, most of the water can be discharged by performing extrusion cleaning in advance with low water consumption, reducing the number of clogging of the filter, and reducing additional work such as backwashing and cleaning. .
図1および図2にて、本発明に係わる実施形態について詳細に例を述べる。図1は本発明に係わる設備構成の概要を示すものであり、従来例からの特徴は水中に浮遊する微細な異物(濁度成分)を捕捉するろ過フィルターを有する点である。 1 and 2, examples of the embodiment according to the present invention will be described in detail. FIG. 1 shows an outline of the equipment configuration according to the present invention, and a feature from the conventional example is that it has a filtration filter for capturing fine foreign matters (turbidity components) floating in water.
図1に示す配管洗浄設備において、純水製造装置1で製造された純水は貯水タンク2に貯蔵される。3は洗浄用ポンプ4と複数の切替弁5を有する供給系統で、プラント配管等からなる洗浄対象系統6に、洗浄時に純水を供給する。ここで洗浄対象系統は、水が滞留するおそれのある機器類を外した状態の配管系を準備する。このようにすることによって、適切な水量で円滑な洗浄が可能となる。
In the pipe cleaning facility shown in FIG. 1, pure water produced by the pure water production apparatus 1 is stored in a water storage tank 2.
7は洗浄後の純水を回収する回収系統であり、循環ストレーナー8、水質判定装置9、濾過フィルター10及び複数の切替弁5を有する。回収系統7を通過した洗浄水(洗浄後の純水)は、排水系統11を経由して排水処理設備13に排水されるか、或いは循環系統12を経由して再び供給系統3に供給される。上記配管洗浄設備の各装置は、図示しない制御装置に接続され、一定のシーケンスで作業工程に従って運用される。
Reference numeral 7 denotes a collection system for collecting pure water after washing, and includes a circulation strainer 8, a water quality determination device 9, a
次に、図2に示す洗浄作業工程において、S21「水張り」では、貯水タンク2の純水を供給して洗浄対象系統と配管洗浄設備を満水状態にし、配管防錆剤等の水溶性不純物を純水に溶解させる。次にS22「押出し洗浄」では、満水にした洗浄対象系統と配管洗浄設備の保有水量の1乃至2倍程度の使用水量を洗浄用ポンプ4により供給系統3、洗浄対象系統6、回収系統7、排水系統11を経由して排水処理設備12に流出させ、水溶性不純物や微細異物を排出する。次にS23「循環洗浄」で、供給系統3、洗浄対象系統6、回収系統7、循環系統12からなる閉ループを構成し、循環ストレーナー8で比較的大きな異物を捕捉し、ろ過フィルター10で洗浄水中の微細異物を捕捉する。循環ストレーナー8のろ過精度を60〜120メッシュ、ろ過フィルター10のろ過精度を0.1〜100ミクロン程度とすれば、上記異物を適切に除去できる。
Next, in the cleaning operation process shown in FIG. 2, in S21 “water filling”, pure water in the water storage tank 2 is supplied to fill the system to be cleaned and the pipe cleaning equipment to a full state, and water-soluble impurities such as pipe rust preventives are removed. Dissolve in pure water. Next, in S22 “push-out cleaning”, the
その後S24「水質判定」で洗浄水の水質と残留異物が規定値以下であることを確認し、S25「排水処理」で水質処理を行う。 Thereafter, in S24 “water quality determination”, it is confirmed that the quality of the washing water and the remaining foreign matter are not more than specified values, and the water quality treatment is performed in S25 “drainage treatment”.
本実施形態では、押出し洗浄工程において系統保有水量の1から2倍程度の水を使用し、水溶性不純物および微細異物の大部分を系統外へ排出する押出し洗浄を実施する。その後に循環洗浄工程において、図1に示す循環ストレーナー8、ろ過フィルター10を含む配管洗浄設備の閉ループによって循環洗浄を実施し、残留した一部の微細異物の捕捉と比較的大きな異物の捕捉を行う。なお、水張り工程、水質判定工程、排水処理工程については、従来工法および公知例同様に作業を実施する。
In the present embodiment, in the extrusion cleaning process, water that is about 1 to 2 times the amount of water retained in the system is used, and the extrusion cleaning is performed in which most of the water-soluble impurities and fine foreign matters are discharged out of the system. Thereafter, in the circulation cleaning step, circulation cleaning is performed by a closed loop of the pipe cleaning equipment including the circulation strainer 8 and the
このように、従来洗浄対象の洗浄対象系統および配管洗浄設備の保有水量の4〜5倍の容量の純水を用いていたものに比較し1〜2倍程度の水量で足りるため、従来水量の20〜40%の水量で洗浄が可能となり、大幅な水量削減が可能となる。 In this way, the amount of water required is about 1 to 2 times that of the conventional water to be cleaned and 4 to 5 times the amount of pure water retained by the pipe cleaning equipment. Washing is possible with a water amount of 20 to 40%, and the water amount can be significantly reduced.
1:純水製造装置
3:供給系統
4:洗浄用ポンプ
6:洗浄対象系統
8:循環ストレーナー
7:回収系統
9:水質判定装置
10:ろ過フィルター
11:排水系統
12:排水処理設備
13:循環系統
1: Pure water production device 3: Supply system 4: Cleaning pump 6: Cleaning target system 8: Circulation strainer 7: Recovery system 9: Water quality determination device 10: Filtration filter 11: Drainage system 12: Wastewater treatment facility 13: Circulation system
Claims (6)
前記配管洗浄設備と洗浄対象系統に純水を充填する水張り工程と、前記配管洗浄設備と洗浄対象系統の保有水量の1乃至2倍程度の純水を前記供給系統、洗浄対象系統、回収系統、排水系統を経由して前記排水処理設備に排水する押出し洗浄工程と、純水を前記供給系統、洗浄対象系統、回収系統における前記循環ストレーナー及び前記ろ過フィルター、前記循環系統を経由して循環させる循環洗浄工程と
を有することを特徴とする原子力発電プラントの配管洗浄方法。 Purified water supplied from the pure water production device is supplied to the system to be cleaned via a supply system having a cleaning pump, and the cleaning water after cleaning the system to be cleaned is circulated with a strainer, a filtration filter, and a water quality determination device. In a pipe cleaning method for a nuclear power plant having a pipe cleaning facility for branching into a drainage system connected to a wastewater treatment facility and a circulation system connected to the supply system,
A water filling step for filling the pipe cleaning equipment and the system to be cleaned with pure water, and the supply system, the system to be cleaned, the recovery system for pure water that is about 1 to 2 times the amount of water held in the pipe cleaning equipment and the system to be cleaned; Extrusion cleaning process for draining to the wastewater treatment facility via a drainage system, and circulation for circulating pure water via the supply system, the system to be cleaned, the circulation strainer and the filtration filter in the recovery system, and the circulation system A piping cleaning method for a nuclear power plant, characterized by comprising a cleaning step.
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