JP2011007193A - Intake air filter unit for gas turbine - Google Patents

Intake air filter unit for gas turbine Download PDF

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JP2011007193A
JP2011007193A JP2010167617A JP2010167617A JP2011007193A JP 2011007193 A JP2011007193 A JP 2011007193A JP 2010167617 A JP2010167617 A JP 2010167617A JP 2010167617 A JP2010167617 A JP 2010167617A JP 2011007193 A JP2011007193 A JP 2011007193A
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filter
gas turbine
filter medium
efficiency
unit
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Katsuhiro Ono
克博 大野
Fumio Nakajima
文男 中島
Hitoshi Niinuma
仁 新沼
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Nippon Muki Co Ltd
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Nippon Muki Co Ltd
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Abstract

PROBLEM TO BE SOLVED: To provide an intake air filter unit for a gas turbine, allowing reduction of an installation space for the filter unit without requiring cleaning of an air compressor or the like and filter replacement over a prolonged period of time.SOLUTION: In this intake air filter unit for the gas turbine formed by providing dustproof filters in two or more stages, the filter unit is composed of three stages, that is, a panel-type demister 2, a wind up belt type or windsock type pre-filter 3 and a high performance suction filter 4 for the gas turbine, from an upstream side in an air flow direction, the high performance suction filter for the gas turbine is composed by closely piling low efficiency filtering material and high efficiency filtering material from the upstream side in the air flow direction, filter material area of each filtering material is set in 20-35 m/unit, filtering material of 40-70% filtering efficiency in relation to 0.3 μm diameter particles is arranged in a layer on the upstream side in the air flow direction, filtering material of 90-99.99% filtering efficiency in relation to 0.3 μm diameter particles is arranged in a layer on a downstream side in the air flow direction, and a pressure drop when air volume 50 m/minute is maintained at 150-450 Pa.

Description

本発明は、ガスタービンプラントの空気圧縮機等に対する大気塵の付着を軽減することにより、発電出力の低下を防止し、長時間に亘り空気圧縮機等の洗浄、フィルタの交換を不要とするガスタービン吸気用フィルタユニットに関し、更に詳しくは、フィルタユニットの設置スペースをコンパクト化できるガスタービン吸気用フィルタユニットに関する。   The present invention reduces the generation output by reducing the adhesion of atmospheric dust to an air compressor or the like of a gas turbine plant, and eliminates the need for cleaning the air compressor or replacing a filter over a long period of time. More specifically, the present invention relates to a gas turbine intake filter unit that can reduce the installation space of the filter unit.

図8に示す通り、ガスタービンaは運転時に外気bを吸入する。この外気bには微粉塵や雨水、ミスト、排気ガス中のカーボン微粒子、塩分粒子等の大気塵が浮遊しているので、このような大気塵がガスタービン内部の腐食、汚染の原因となると共に、特に空気圧縮機cに付着して空気圧縮機cの性能低下を生じさせ、発電出力を低下させるという問題がある。そこで大気塵の吸い込みを未然に防止するために、ガスタービンaの空気吸込口dには、空気から大気塵を機械的に分離除去して清浄化するための集塵装置(フィルタユニット)eが設置されている。このフィルタユニットeは、特開平5−106464号公報にも開示されるように、巻取式帯状ガラス繊維の濾材から成る粗フィルタfと、イオン交換繊維フィルタを折込型とした中性能フィルタgの2段式に構成されている。
尚、図中hはガスタービンaのタービン部、iはガスタービンaによって駆動される発電機を示す。前記従来のガスタービン吸気用フィルタユニットは、充分に大気塵を除去できないためガスタービンの発電出力の低下を生じさせ、また、粉塵保持容量が小さいため年2〜3回の頻度でフィルタ交換が必要となる。このため、発電出力を低下させない高効率な吸気用フィルタユニットで年1回義務づけられているガスタービンの定期点検時にフィルタ交換ができる長寿命のガスタービン吸気用フィルタユニットの提案が望まれている。
As shown in FIG. 8, the gas turbine a sucks outside air b during operation. Since atmospheric dust such as fine dust, rain water, mist, carbon fine particles in exhaust gas, and salt particles floats in the outside air b, such atmospheric dust causes corrosion and contamination inside the gas turbine. In particular, there is a problem in that it adheres to the air compressor c and causes a reduction in the performance of the air compressor c, thereby reducing the power generation output. Therefore, in order to prevent the inhalation of atmospheric dust, a dust collector (filter unit) e for mechanically separating and removing atmospheric dust from the air is provided at the air inlet d of the gas turbine a. is set up. As disclosed in Japanese Patent Application Laid-Open No. 5-106464, the filter unit e includes a coarse filter f made of a filter material of a wound belt glass fiber, and a medium performance filter g in which an ion exchange fiber filter is folded. It is configured in two stages.
In the drawing, h represents a turbine portion of the gas turbine a, and i represents a generator driven by the gas turbine a. Since the conventional gas turbine intake filter unit cannot sufficiently remove atmospheric dust, the power generation output of the gas turbine is reduced, and the dust holding capacity is small, so the filter needs to be replaced twice or three times a year. It becomes. For this reason, there is a demand for a long-life gas turbine intake air filter unit that can be replaced during a periodic inspection of a gas turbine that is required once a year with a highly efficient intake air filter unit that does not reduce power generation output.

本発明者等は前記要望に応えるべく、パネル型デミスターあるいはウェザールーバ、巻取帯状型あるいは吹流し型プレフィルタ、箱型中性能フィルタ、及び箱型高性能フィルタの4段式としたものを提案したが、吸気用フィルタユニットが大きくなり設置スペースと設備費が大となる問題があり、その対策が望まれている。そこで、低圧損、高効率、長寿命の観点から中性能フィルタと高性能フィルタを複合化すればよいという結論に到り、複合化に関する先行技術を参照したが各々に問題があった。まず、設置スペースを小さくする目的で、実開昭62−132715号公報に、ケーシング内を流れるガスの下流側に所定の能力を有する濾紙を、その上流側に前記濾紙よりも捕集能力の低い濾紙を多段に設けることが開示されているが、フィルタが小さくならず設置スペースを小さくする目的が達成できないという問題がある。
また、塩分粒子を除去する目的で、実公平3−35373号公報に、撥水性を有する2枚の濾材の間に空隙部を有する間隔保持体を挟み込むことが開示されているが、これは塩分粒子が水滴となっても上流側の濾材裏面に沿って液滴を落下させるためであり、濾材の厚みが大きくなり、8000時間以上の寿命をもたせるために濾材面積を大きくとることができず、また、圧力損失も大きくなるという問題がある。
また、濾過効率(0.1μmDOP)が99.99%以上(いわゆるULPA)の高効率を得る目的で、特開昭54−94176号公報に、濾材を2層で構成し、気流方向に対して下流側の層には粒径0.3μmの粒子に対して99.97%以上の濾過効率を有する濾材を配し、上流側の層には粒径0.3μmの粒子に対して99.97%未満75%以上の濾過効率を有する濾材を配し、これら2層の濾材を密接に重ね合わせた状態でジグザグ状に折り畳むことが開示されているが、これは2段にするものに比べて寸法上の制約および作り易さの観点から濾材を2層にするとしているが、高効率が目的であり、寿命は考慮されておらずガスタービン用として使用した場合は、濾材の目詰まりが早くフィルタ交換を年2〜3回以上実施する必要があるという問題がある。
そこで、出願人は特開平7−253029号公報に開示されるように、前記の課題を解決するために、気流方向の上流側より低効率濾材と高効率濾材を密接して重ね、これら各濾材の濾材面積が25〜35m/台である濾材構成にし、前記濾材は、気流方向に対して上流側の層には、粒径0.3μmの粒子に対して10〜70%の濾過効率の濾材を配し、下流側の層には粒径0.3μmの粒子に対して90〜99.99%の濾過効率の濾材を配するようにしたガスタービン吸気用高性能フィルタを提案した。
ところが、当初評価に使用した大気塵では8000時間以上の寿命となる優れた効果が得られたものの、別の大気塵で再評価したところ、約4300時間でフィルタユニットの圧力損失が急激に上昇して、寿命となることが判明した。この理由は、大気塵中の粒径0.3μmに代表される細かな塵埃の濃度が、当初の約5倍程度と非常に高かったため、下流側の層に負荷が集中したためである。
In order to meet the above-mentioned demands, the present inventors have proposed a panel type demister or weather louver, a take-up band type or windsock type prefilter, a box type medium performance filter, and a box type high performance filter. However, there is a problem that the intake filter unit becomes large and the installation space and equipment cost increase, and countermeasures are desired. Thus, from the viewpoint of low pressure loss, high efficiency, and long life, it was concluded that a medium performance filter and a high performance filter should be combined, and the prior art related to the combination was referred to, but each had problems. First, for the purpose of reducing the installation space, Japanese Utility Model Publication No. 62-132715 discloses a filter paper having a predetermined ability on the downstream side of the gas flowing in the casing, and has a lower collection ability than the filter paper on the upstream side. Although it has been disclosed that filter paper is provided in multiple stages, there is a problem that the purpose of reducing the installation space cannot be achieved without reducing the filter.
In addition, for the purpose of removing salt particles, Japanese Utility Model Publication No. 3-35373 discloses that a gap holder having a void portion is sandwiched between two filter media having water repellency. This is because even if the particles become water droplets, the droplets are dropped along the back surface of the filter medium on the upstream side, the thickness of the filter medium is increased, and the filter medium area cannot be increased in order to have a lifetime of 8000 hours or more. In addition, there is a problem that the pressure loss increases.
Further, for the purpose of obtaining a high efficiency of filtration efficiency (0.1 μm DOP) of 99.99% or more (so-called ULPA), Japanese Patent Application Laid-Open No. 54-94176 discloses that a filter medium is composed of two layers, A filter medium having a filtration efficiency of 99.97% or more with respect to particles having a particle diameter of 0.3 μm is disposed in the downstream layer, and 99.97 with respect to particles having a particle diameter of 0.3 μm is disposed in the upstream layer. It is disclosed that a filter medium having a filtration efficiency of less than 75% and 75% or more is disposed, and these two layers of filter medium are folded in a zigzag shape in a closely overlapped state. The filter medium is assumed to have two layers from the viewpoint of dimensional constraints and ease of production, but the purpose is high efficiency, and the life is not considered, and when used for gas turbines, the filter medium is clogged quickly. It is necessary to carry out filter replacement 2-3 times a year There is a problem in that that.
Therefore, as disclosed in Japanese Patent Application Laid-Open No. 7-253029, in order to solve the above problems, the applicant closely overlaps the low-efficiency filter medium and the high-efficiency filter medium from the upstream side in the airflow direction. The filter medium has an area of 25 to 35 m 2 / unit, and the filter medium has a filtration efficiency of 10 to 70% with respect to particles having a particle diameter of 0.3 μm in the upstream layer with respect to the airflow direction. A high performance filter for gas turbine intake was proposed in which a filter medium was disposed, and a filter medium having a filtration efficiency of 90 to 99.99% with respect to particles having a particle diameter of 0.3 μm was disposed in the downstream layer.
However, although the atmospheric dust used for the initial evaluation had an excellent effect of having a lifetime of 8000 hours or more, when it was re-evaluated with another atmospheric dust, the pressure loss of the filter unit increased rapidly in about 4300 hours. It was found to be a lifetime. The reason for this is that the concentration of fine dust typified by a particle size of 0.3 μm in the atmospheric dust was very high, about 5 times the original, and the load was concentrated on the downstream layer.

特開平5−106464号公報JP-A-5-106464 実開昭62−132715号公報Japanese Utility Model Publication No. 62-132715 実公平3−35373号公報Japanese Utility Model Publication No. 3-35373 特開昭54−94176号公報JP 54-94176 A 特開平7−253029号公報Japanese Patent Laid-Open No. 7-253029

このため、粒径0.3μmに代表される細かな塵埃の濃度が高い大気塵であっても、8000時間以上の寿命を確保し、かつ従前のガスタービンプラントの空気圧縮機等に対する大気塵の付着を軽減することにより、発電出力の低下を防止し、長時間に亘り空気圧縮機等の洗浄、フィルタの交換を不要とし、フィルタユニットの設置スペースをコンパクト化できるガスタービン吸気用高性能フィルタとこれを用いたガスタービン吸気用フィルタユニットを提供することを目的とする。   For this reason, even atmospheric dust with a high concentration of fine dust represented by a particle size of 0.3 μm ensures a life of 8000 hours or more and prevents atmospheric dust against the air compressor of a conventional gas turbine plant. A gas turbine intake high-performance filter that prevents the reduction of power generation output by reducing adhesion, eliminates the need to clean the air compressor, filter replacement, etc. over a long period of time, and makes the filter unit installation space compact. It aims at providing the filter unit for gas turbine intake using this.

本発明のガスタービン吸気用フィルタユニットは、以上の課題を解決するために、防塵用フィルタを複数段設けて成るガスタービン吸気用フィルタユニットにおいて、前記防塵用フィルタが気流方向の上流側より、パネル型デミスター、巻取帯状型あるいは吹流し型プレフィルタ、ガスタービン吸気用高性能フィルタの3段から成り、前記ガスタービン吸気用高性能フィルタは、気流方向の上流側より低効率濾材と高効率濾材を密接して重ね、これら各濾材の濾材面積が20〜35m/台である濾材構成にし、気流方向に対して上流側の層には、粒径0.3μmの粒子に対して40〜70%の濾過効率の濾材を配し、下流側の層には粒径0.3μmの粒子に対して90〜99.99%の濾過効率の濾材を配し、風量50m/分の時の圧力損失を150〜450Paとしたことを特徴とする。
また、前記濾材は、気流方向に対して凹凸となるようにジグザグ状に折り畳まれ、その折り曲げ間隔部にシートを波形に屈折したセパレータを挿入し、該セパレータの屈折の波高さを挿入方向後端側の高さを挿入方向先端側の高さより大きくしてテーパー状にしたものが好ましいが、必ずしもセパレータ型に限られず、ミニプリーツ型・ダブルプリーツ型でもよい。
また、本発明のガスタービン吸気用フィルタユニットにおいて、前記プレフィルタが吹流し型で濾材面積が2〜8m/台であることを特徴とする。
In order to solve the above problems, the gas turbine intake filter unit of the present invention is a gas turbine intake filter unit comprising a plurality of stages of dustproof filters. The dustproof filter is disposed on the panel from the upstream side in the airflow direction. The gas turbine intake high-performance filter consists of a low-efficiency filter medium and a high-efficiency filter medium from the upstream side in the airflow direction. The filter medium structure of each filter medium is 20 to 35 m 2 / unit, and the layers upstream of the flow direction are 40 to 70% with respect to the particles having a particle diameter of 0.3 μm. pressure when in arranged filter media filtration efficiency, arranged filter media filtration efficiency of 90 to 99.99% with respect to particles having a particle diameter of 0.3μm is the layer of the downstream side, the air volume 50 m 3 / min It characterized in that the loss was 150~450Pa.
In addition, the filter medium is folded in a zigzag shape so as to be uneven with respect to the air flow direction, and a separator that refracts the sheet into a wave shape is inserted into the folding interval portion, and the refraction wave height of the separator is set to the rear end in the insertion direction. It is preferable that the height on the side is larger than the height on the distal end side in the insertion direction to be tapered, but it is not necessarily limited to the separator type, and may be a mini pleat type or a double pleat type.
In the gas turbine intake filter unit of the present invention, the pre-filter is a blow-off type and has a filter medium area of 2 to 8 m 2 / unit.

以上説明したように、今回発明したガスタービン吸気用フィルタユニットを用いることにより、粒径0.3μmに代表される細かな塵埃の濃度が高い環境で使用した場合においても、法令による年1回の定期点検時に併せフィルタ交換をすることが可能となるなど、フィルタ交換および圧縮機洗浄などのメンテナンス作業を軽減させることができる。
また、HEPAフィルタに代表される高い捕集効率を有するフィルタ(いわゆる高性能フィルタ)を使用するため、大気塵の付着によるガスタービンの出力低下を抑えられ、且つ、吸気用フィルタユニットがコンパクトとなり省スペース化が図れる。
As described above, by using the gas turbine intake filter unit invented this time, even when used in an environment where the concentration of fine dust typified by a particle size of 0.3 μm is high, once a year in accordance with laws and regulations. Maintenance work such as filter replacement and compressor cleaning can be reduced. For example, it is possible to replace the filter during regular inspection.
In addition, since a filter having high collection efficiency represented by a HEPA filter (so-called high performance filter) is used, the output reduction of the gas turbine due to adhesion of atmospheric dust can be suppressed, and the intake filter unit can be made compact and saved. Space can be achieved.

本発明ガスタービン吸気用フィルタユニットの構成図Configuration of the gas turbine intake filter unit of the present invention 巻取帯状型プレフィルタの部分切断正面図Partial cut front view of a winding band type prefilter 吹流し型プレフィルタの濾材の側面図Side view of the filter media of a streamer type prefilter 前記濾材のヘッド部の正面図Front view of the head of the filter medium 前記吹流し型プレフィルタの平面図Top view of the windsock prefilter 高性能フィルタの斜視図High-performance filter perspective view 前記高性能フィルタの部分切断平面図Partial cut plan view of the high performance filter 従来のガスタービン吸気用フィルタユニットの構成図Configuration diagram of conventional gas turbine intake filter unit

本発明のガスタービン吸気用フィルタユニットを構成する前記パネル型デミスターは、雨水の浸入を防止するためのものであり、従来種々公知のものがあるが、例えば、動植物性繊維および合成繊維をスプリング状にカール加工して多くの小さな弾性体をつくり、これを結合剤で被覆結合したものを板状にして金枠内に封入したものが知られている。このデミスターは、一般には、厚みが10〜50mm、風速2m/sの時の濾過効率(JIS8種,比色法)が15〜60%、圧力損失が10〜100Paである。前記デミスターは圧力損失が小さく、即ち、通気抵抗が小さく、水滴に対して濾過効率が高いことが特徴で、また、汚れた場合に枠から外して洗浄することで再使用できる。もちろん、前記パネル型デミスターのかわりに雨水の浸入を屈折路で防ぐようにした屈折型のウェザールーバ等も使用できる。   The panel-type demister constituting the gas turbine intake filter unit of the present invention is for preventing rainwater from entering, and there are various known ones. For example, animal and vegetable fibers and synthetic fibers are spring-shaped. It is known that a large number of small elastic bodies are made by curling, and these are coated and bonded with a binder into a plate shape and enclosed in a metal frame. In general, the demister has a thickness of 10 to 50 mm, a filtration efficiency (JIS 8 type, colorimetric method) at a wind speed of 2 m / s of 15 to 60%, and a pressure loss of 10 to 100 Pa. The demister is characterized by low pressure loss, that is, low ventilation resistance and high filtration efficiency against water droplets, and when it becomes dirty, it can be reused by removing it from the frame and washing. Of course, instead of the panel type demister, a refraction type weather louver or the like that prevents intrusion of rainwater by a refraction path can be used.

また、本発明のガスタービン吸気用フィルタユニットを構成する前記プレフィルタとしては巻取帯状型かあるいは吹流し型を用いるわけであるが、巻取帯状型は図2に示す通り、ガラス繊維製濾材から成る帯状濾材10が吸気空気路11を遮るように張設されており、濾材10が巻き取られている送出用ロール12が上部に設置される一方、その送出用ロール12から取り出された濾材10を巻き取る巻取用ロール13が下部に設置されている。この巻取帯状型プレフィルタは、一般には、濾材材質がガラス繊維及びポリエステル繊維等を用いた不織布であり、濾材厚みが20〜70mm、平均繊維径が15〜60μmで、風速2.5m/sの時の圧力損失が40〜80Pa、濾過効率(JIS15種、重量法)が60〜90%、粉塵保持容量が500〜1300g/mである。
ただし、巻取帯状型は濾材の巻取り用駆動装置の保守メンテナンスが必要となるため完全なメンテナンスフリーとするには、濾材面積を広くした下記吹流し型が好ましい。
吹流し型は、図3乃至図5に示す通り、濾材20を多数の袋体21を連続させた形状とし、この濾材20をその開口部22に合わせて複数本の桟23を備えたヘッド部24を介して枠体25に螺子26で取り付けるものである。
このプレフィルタは、濾材は平均厚みが5〜25mm、材質がポリエステル、アクリル等の有機繊維の乾式不織布、平均繊維径が5〜60μm、目付が50〜600g/m、風速2.5m/sの時の圧力損失が20〜300Pa、効率(JIS15種,重量法)が60〜99%で、この濾材を用いて濾材面積が2〜8m/台、外形寸法がタテ592mm×ヨコ592mm×奥行き500mmの吹流し型プレフィルタとした。ただし、形態はこれに限定されるものではなく濾材面積を所望のものにできる形状のものであればよい。
濾材面積が2m/台未満の場合は所望のフィルタユニットの寿命が得られず、濾材面積が8m/台を越える場合は、圧力損失が高くなり好ましくない。従って濾材面積は2〜8m/台が好ましい。
尚、このフィルタの性能は風量50m/分の時の圧力損失が20〜80Pa、効率(JIS15種,重量法)が60〜99%、粉塵保持容量が500〜4000g/台である。
In addition, as the pre-filter constituting the gas turbine intake filter unit of the present invention, a winding band type or a blower type is used, and the winding band type is formed from a glass fiber filter medium as shown in FIG. The belt-shaped filter medium 10 is stretched so as to block the intake air passage 11, and the feed roll 12 around which the filter medium 10 is wound is installed on the upper side, while the filter medium 10 taken out from the feed roll 12 is provided. A take-up roll 13 is installed at the bottom. In general, the wound belt-shaped prefilter is a nonwoven fabric using glass fiber, polyester fiber, or the like as a filter medium material. The filter medium thickness is 20 to 70 mm, the average fiber diameter is 15 to 60 μm, and the wind speed is 2.5 m / s. The pressure loss is 40 to 80 Pa, the filtration efficiency (JIS 15 species, weight method) is 60 to 90%, and the dust holding capacity is 500 to 1300 g / m 2 .
However, since the winding belt-shaped mold requires maintenance of the filter medium winding drive device, the following blow-off mold with a wide filter medium area is preferable for complete maintenance-free.
As shown in FIGS. 3 to 5, the streamer type has a shape in which a large number of bag bodies 21 are made continuous with a filter medium 20, and a head section 24 having a plurality of bars 23 with the filter medium 20 aligned with its opening 22. It attaches to the frame 25 with the screw 26 via.
In this prefilter, the filter medium has an average thickness of 5 to 25 mm, the material is a dry nonwoven fabric of organic fibers such as polyester and acrylic, the average fiber diameter is 5 to 60 μm, the basis weight is 50 to 600 g / m 2 , and the wind speed is 2.5 m / s. The pressure loss is 20 to 300 Pa, the efficiency (JIS 15 types, weight method) is 60 to 99%, the filter medium area is 2 to 8 m 2 / unit using this filter medium, and the external dimensions are vertical 592 mm × horizontal 592 mm × depth. A 500 mm windsock prefilter was obtained. However, the form is not limited to this, and any shape can be used as long as the filter medium area can be made desired.
When the filter medium area is less than 2 m 2 / unit, the desired filter unit life cannot be obtained, and when the filter medium area exceeds 8 m 2 / unit, the pressure loss increases, which is not preferable. Accordingly, the filter medium area is preferably 2 to 8 m 2 / unit.
The filter has a pressure loss of 20 to 80 Pa at an air volume of 50 m 3 / min, an efficiency (JIS 15 type, weight method) of 60 to 99%, and a dust holding capacity of 500 to 4000 g / unit.

本発明のガスタービン吸気用フィルタユニットに用いるガスタービン吸気用高性能フィルタは、高効率濾材と低効率濾材との組み合わせで得られるものであるが、高効率濾材としては、粒径0.3μmの粒子に対して90〜99.99%の濾過効率のものを用いる。
これは、90%未満では、ガスタービンの圧縮機の塵埃付着が防止できず、99.99%を越える場合は、塵埃付着防止には有効であるが圧力損失が増大し、寿命が短くなる問題を生ずるからである。
また、低効率濾材としては、粒径0.3μmの粒子に対して40〜70%の濾過効率のものを用いる。これは、40%未満では粒径0.3μmに代表される細かな塵埃の濃度が高い大気塵の場合には下流側の高効率濾材の負担が大きくなり、70%を越える場合は濾材の目詰まりが早くなる問題が生ずるからである。
これら高効率濾材30aと低効率濾材30bは、密接して重ね合わせられ、濾材面積を増加させるために吸気空気の流れ方向に対して凹凸となるようジグザグ状に折り畳んでおり、それを箱型の枠体31にシール材32を介して組み込み、その折り曲げ間隔部にシートを波形に屈折したセパレータ33が挿入されている。
尚、図示の様に、セパレータ33の屈折の波高さを挿入方向後端側の高さH1を挿入方向先端側H2の高さより大きくしてテーパー状に形成したいわゆる傾斜型セパレータを用いることにより、通常のセパレータの様に屈折の波高さを全長に亘り均等にしたものに比べてフィルタを多風量で高性能にすることができる。
この高性能フィルタは、一般には、各濾材の合計の厚みが0.4〜2.0mm、目付が100〜200g/m、風速5.3cm/sの時の圧力損失が50〜450Pa、効率(0.3μmDOP)が90〜99.9%で、セパレータは材質がアルミニウム、ステンレス等の金属箔、クラフト、合繊等の紙、ポリアリレート、ポリエチレンテレフタレート等の合成樹脂フィルムで、該濾材をジグザグに折り畳みセパレータを間挿して、外形寸法がタテ610mm×ヨコ610mm×奥行き290mmの場合は濾材面積が25〜35m/台、外形寸法がタテ594mm×ヨコ594mm×奥行き290mmの場合は濾材面積が20〜30m/台の高性能フィルタとした。この濾材面積が20m/台未満では、圧力損失が高くなって寿命が短くなり、35m/台を越えると濾材と濾材の間隔保持ができないという問題がある。従って、濾材面積は20〜35m/台とする。
尚、このフィルタの性能は風量50m/分の時の圧力損失が150〜450Pa、効率(0.3μmDOP)が90〜99.99%、粉塵保持容量が1000〜3000g/台である。
The high performance filter for gas turbine intake used in the filter unit for gas turbine intake of the present invention is obtained by a combination of a high efficiency filter medium and a low efficiency filter medium. The high efficiency filter medium has a particle size of 0.3 μm. A filter having a filtration efficiency of 90 to 99.99% based on the particles is used.
If it is less than 90%, dust adhesion of the compressor of the gas turbine cannot be prevented, and if it exceeds 99.99%, it is effective for preventing dust adhesion, but pressure loss increases and life is shortened. It is because it produces.
Moreover, as a low efficiency filter medium, the thing of the filtration efficiency of 40 to 70% is used with respect to the particle | grains with a particle size of 0.3 micrometer. This is because the load of the high-efficiency filter medium on the downstream side becomes large in the case of atmospheric dust with a high concentration of fine dust represented by a particle size of 0.3 μm if it is less than 40%, and the mesh of the filter medium if it exceeds 70%. This is because there is a problem that clogging is accelerated.
These high-efficiency filter media 30a and low-efficiency filter media 30b are closely overlapped and folded in a zigzag shape so as to be uneven with respect to the flow direction of the intake air in order to increase the filter media area. A separator 33 is inserted into the frame 31 via a sealing material 32, and a sheet 33 is bent into a wavy interval portion.
As shown in the figure, by using a so-called inclined separator in which the wave height of the refraction of the separator 33 is formed in a tapered shape by making the height H1 on the rear end side in the insertion direction larger than the height on the front end side H2 in the insertion direction. The filter can have high airflow and high performance as compared with a normal separator in which the wave height of refraction is made uniform over the entire length.
This high-performance filter generally has a total thickness of each filter medium of 0.4 to 2.0 mm, a basis weight of 100 to 200 g / m 2 , a pressure loss of 50 to 450 Pa at a wind speed of 5.3 cm / s, and an efficiency. (0.3 μm DOP) is 90 to 99.9%, and the separator is made of metal foil such as aluminum or stainless steel, paper such as craft or synthetic fiber, synthetic resin film such as polyarylate, polyethylene terephthalate, etc. When a folding separator is inserted and the outer dimensions are vertical 610 mm × width 610 mm × depth 290 mm, the filter medium area is 25 to 35 m 2 / unit, and when the outer dimensions are vertical 594 mm × width 594 mm × depth 290 mm, the filter medium area is 20 to A high-performance filter of 30 m 2 / unit was used. If the area of the filter medium is less than 20 m 2 / unit, the pressure loss increases and the life is shortened. If the area exceeds 35 m 2 / unit, there is a problem that the distance between the filter medium and the filter medium cannot be maintained. Therefore, the filter medium area is 20 to 35 m 2 / unit.
The performance of this filter is such that the pressure loss at an air flow rate of 50 m 3 / min is 150 to 450 Pa, the efficiency (0.3 μm DOP) is 90 to 99.99%, and the dust holding capacity is 1000 to 3000 g / unit.

以下、本発明の実施例を図面に付き説明する。
図1は、本発明ガスタービン吸気用フィルタユニットの実施例を示すもので、ガスタービンの吸気用ダクトに設置したケーシング1内にガスタービンの連続運転にとって有害な塵埃などを吸気空気中から除去するために、ウェザールーバ2、吹き流し型プレフィルタ3、更に本発明の高性能フィルタ4からなる3段式のフィルタユニット5を設けるようにした。
Embodiments of the present invention will be described below with reference to the drawings.
FIG. 1 shows an embodiment of a gas turbine intake filter unit according to the present invention, in which dust harmful to the continuous operation of the gas turbine is removed from the intake air in a casing 1 installed in the intake duct of the gas turbine. For this purpose, a three-stage filter unit 5 comprising a weather louver 2, a blow-off type prefilter 3, and a high performance filter 4 of the present invention is provided.

ウェザールーバ2は、金属板をその断面が略くの字状に折り曲げ加工することで雨水の浸入を防ぐようにしたもので、使用風速約2.5m/sに対し、圧力損失が約20Pa、雨滴の捕集効率が88%(重量法)で、外径寸法が縦約2600mm×横3300mm×奥行き約200mmのものをケーシング1内に1台設置するようにした。   The weather louver 2 is formed by bending a metal plate into a substantially U-shaped cross section so as to prevent the intrusion of rainwater. The pressure loss is about 20 Pa for a wind speed of about 2.5 m / s. One unit having a raindrop collection efficiency of 88% (weight method) and an outer diameter of about 2600 mm in length, 3300 mm in width, and about 200 mm in depth was installed in the casing 1.

プレフィルタ3は、ポリエステル繊維による不織布濾材(平均繊維径19μm、平均目付330g/m、平均厚さ18mm)を6山分折り込み、金枠で固定して、濾材面積が4m/台、外形寸法が縦592mm×横592mm×奥行き500mmとなるフィルタを用い、ケーシング1内に20台(4段×5列)設置するようにした。なお、このプレフィルタの性能は、使用風量約50m/minに対し、初期圧力損失が約60Pa、捕集効率(JIS15種粉体、重量法)98%である。 The prefilter 3 is a nonwoven fabric filter material made of polyester fiber (average fiber diameter 19 μm, average weight 330 g / m 2 , average thickness 18 mm) is folded into six piles, fixed with a metal frame, and the filter medium area is 4 m 2 / unit. Using a filter having dimensions of 592 mm in length, 592 mm in width, and 500 mm in depth, 20 units (4 stages × 5 rows) were installed in the casing 1. The performance of this prefilter is such that the initial pressure loss is about 60 Pa and the collection efficiency (JIS 15 seed powder, weight method) is 98% with respect to the used air volume of about 50 m 3 / min.

高性能フィルタ4には、気流方向の上流側に粒径0.3μmの粒子に対し、捕集効率約40%のガラス繊維ペーパ濾材と、下流側に粒径0.3μmの粒子に対し捕集効率約97%のガラス繊維ペーパ濾材を密接に重ねて、アルミニウム箔のセパレータを挿入して、ジグザグ状に折り込み、濾材面積が25m/台、外形寸法が縦610mm×横610mm×奥行き290mmとなるフィルタを用い、ケーシング1内に20台(4段×5列)設置するようにした。この高性能フィルタの性能は、使用風量約50m/minに対し、初期圧力損失が約250Pa、捕集効率(計数法、対象0.3μm粒子)97%である。 The high-performance filter 4 collects a glass fiber paper filter with a collection efficiency of about 40% for particles with a particle size of 0.3 μm on the upstream side in the airflow direction, and for particles with a particle size of 0.3 μm on the downstream side. A glass fiber paper filter medium with an efficiency of about 97% is closely stacked, an aluminum foil separator is inserted and folded in a zigzag shape, the filter medium area is 25 m 2 / unit, and the external dimensions are 610 mm long × 610 mm wide × 290 mm deep. A filter was used, and 20 units (4 stages × 5 rows) were installed in the casing 1. The performance of this high-performance filter is an initial pressure loss of about 250 Pa and a collection efficiency (counting method, target 0.3 μm particles) of 97% with respect to an operating air volume of about 50 m 3 / min.

前記ウェザールーバ2、プレフィルタ3及び高性能フィルタ4から構成される本実施例のガスタービン吸気用フィルタユニット5を、前記同様のウェザールーバ2及びプレフィルタ3、並びに上流側濾材を粒径0.3μm粒子に対し捕集効率約15%のガラス繊維ペーパ濾材と、下流側に粒径0.3μmの粒子に対し捕集効率97%のガラス繊維ペーパ濾材を密接に重ねた高性能フィルタから構成される吸気用フィルタユニットを比較例として、それぞれのフィルタユニットに対して、平均重量濃度約0.13mg/m、粒径0.3〜0.5μmの平均個数濃度500,000個/0.1cfと細かい塵埃の濃度が高い外気を連続的に流し続け、その期間中のガスタービンの出力低下やフィルタの寿命(圧力損失が686Paに達するまでの時間)などについて評価した。前記各吸気用フィルタユニットの構成を下記表1に、また試験結果を表2に示す。 The gas turbine intake filter unit 5 of the present embodiment, which is composed of the weather louver 2, the pre-filter 3 and the high-performance filter 4, has the same weather louver 2, pre-filter 3 and upstream filter medium with a particle size of 0. It consists of a glass fiber paper filter medium with a collection efficiency of about 15% for 3 μm particles and a high-performance filter closely packed with 97% glass fiber paper filter medium for particles with a particle diameter of 0.3 μm on the downstream side. As a comparative example, the filter unit for intake air having an average weight concentration of about 0.13 mg / m 3 and an average number concentration of particles having a particle size of 0.3 to 0.5 μm is 500,000 / 0.1 cf. Continue to continuously flow outside air with a high concentration of fine dust, and during that period the output of the gas turbine decreases and the filter life (until the pressure loss reaches 686 Pa) Were evaluated for such time). The configuration of each of the intake filter units is shown in Table 1 below, and the test results are shown in Table 2.

Figure 2011007193
Figure 2011007193

Figure 2011007193
Figure 2011007193

前記表2から明らかなように、比較例の構成では、ガスタービンの出力低下防止や省スペース化・メンテナンスという面では良好な結果となるが、粒径0.3μmに代表される細かな塵埃の濃度が高い環境で使用した場合には寿命が4300時間と短くなり、フィルタ交換が年2回程度必要となる。
これに対し今回の発明となる実施例の構成は、粒径0.3μmに代表される細かな塵埃の濃度が高い環境で使用した場合においても、ガスタービンの出力低下防止や省スペース化が図れるとともに8000時間(1年間相当)以上のメンテナンスフリーを達成することができる。
As can be seen from Table 2, the configuration of the comparative example gives good results in terms of prevention of gas turbine output reduction, space saving, and maintenance, but the fine dust typified by a particle size of 0.3 μm. When used in a high-concentration environment, the lifetime is shortened to 4300 hours, and the filter needs to be replaced about twice a year.
In contrast, the configuration of the embodiment of the present invention can prevent gas turbine output from decreasing and save space even when used in an environment where the concentration of fine dust represented by a particle size of 0.3 μm is high. In addition, maintenance-free for 8000 hours (equivalent to one year) or more can be achieved.

発電出力の低下を防止し、長時間に亘り空気圧縮機等の洗浄、フィルタの交換を不要とするガスタービン吸気用フィルタユニットタユニットを提供できるので、産業上の利用可能性を有する。   Since it is possible to provide a filter unit for gas turbine intake that prevents a decrease in power generation output and does not require cleaning of an air compressor or the like and replacement of a filter for a long time, it has industrial applicability.

1 ケーシング
2 ウェザールーバ
3 巻取帯状型あるいは吹流し型プレフィルタ
4 高性能フィルタ
5 ガスタービン吸気用フィルタユニット
30a 高効率濾材
30b 低効率濾材
31 枠体
32 シール材
33 セパレータ
DESCRIPTION OF SYMBOLS 1 Casing 2 Weather louver 3 Winding band type or wind-flow type pre filter 4 High performance filter 5 Gas turbine intake filter unit 30a High efficiency filter medium 30b Low efficiency filter medium 31 Frame body 32 Seal material 33 Separator

Claims (3)

防塵用フィルタを複数段設けて成るガスタービン吸気用フィルタユニットにおいて、前記防塵用フィルタが気流方向の上流側より、パネル型デミスター、巻取帯状型あるいは吹流し型プレフィルタ、ガスタービン吸気用高性能フィルタの3段から成り、前記ガスタービン吸気用高性能フィルタは、気流方向の上流側より低効率濾材と高効率濾材を密接して重ね、これら各濾材の濾材面積が20〜35m/台である濾材構成にし、気流方向に対して上流側の層には、粒径0.3μmの粒子に対して40〜70%の濾過効率の濾材を配し、下流側の層には粒径0.3μmの粒子に対して90〜99.99%の濾過効率の濾材を配し、風量50m/分の時の圧力損失を150〜450Paとしたことを特徴とするガスタービン吸気用フィルタユニット。 In a gas turbine intake filter unit having a plurality of dustproof filters, the dustproof filter is a panel type demister, a take-up band type or blown type prefilter, and a high performance filter for gas turbine intake from the upstream side in the air flow direction. The high-performance filter for gas turbine intake has a low-efficiency filter medium and a high-efficiency filter medium closely stacked from the upstream side in the airflow direction, and the filter medium area of each of these filter media is 20 to 35 m 2 / unit. The filter medium is configured such that a filter medium having a filtration efficiency of 40 to 70% with respect to particles having a particle diameter of 0.3 μm is disposed in the upstream layer with respect to the air flow direction, and a particle diameter of 0.3 μm is disposed in the downstream layer. 90 to 99.99% filtration arranged filter media efficiency, the filter for a gas turbine inlet air, characterized in that the pressure loss when the air volume 50 m 3 / min was 150~450Pa against particles Knit. 前記濾材は気流方向に対して凹凸となるようにジグザグ状に折り畳まれ、その折り曲げ間隔部にシートを波形に屈折したセパレータを挿入し、該セパレータの屈折の波高さを挿入方向後端側の高さを挿入方向先端側の高さより大きくしてテーパー状にしたことを特徴とする請求項1記載のガスタービン吸気用フィルタユニット。   The filter medium is folded in a zigzag shape so as to be uneven with respect to the airflow direction, and a separator that refracts the sheet into a corrugated shape is inserted into the folding interval, and the refraction wave height of the separator is set to a height on the rear end side in the insertion direction. 2. The gas turbine intake filter unit according to claim 1, wherein the filter unit has a taper shape with a height larger than a height at a distal end side in the insertion direction. 前記プレフィルタが吹流し型で濾材面積が2〜8m/台であることを特徴とする請求項1記載のガスタービン吸気用フィルタユニット。 2. The gas turbine intake filter unit according to claim 1, wherein the prefilter is a blow-off type and has a filter medium area of 2 to 8 m 2 / unit.
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