JP5959606B2 - Rotating regenerative heat exchanger - Google Patents
Rotating regenerative heat exchanger Download PDFInfo
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- JP5959606B2 JP5959606B2 JP2014247936A JP2014247936A JP5959606B2 JP 5959606 B2 JP5959606 B2 JP 5959606B2 JP 2014247936 A JP2014247936 A JP 2014247936A JP 2014247936 A JP2014247936 A JP 2014247936A JP 5959606 B2 JP5959606 B2 JP 5959606B2
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Description
本発明は、回転再生式熱交換器、特に、ヒーティングエレメントを積層状態で挿入したバスケットを有する回転再生式熱交換器に関する。 The present invention relates to a rotary regenerative heat exchanger, and more particularly to a rotary regenerative heat exchanger having a basket in which heating elements are inserted in a stacked state.
一般に、回転再生式熱交換器は、図4および図5に示すように、ハウジングH内にローター本体Rを回転自在に装備して、該ローター本体Rを放射状のダイヤフラムDにより多数(例えば12又は24)区画したセクター内にバスケットBを挿入し、該バスケットB内に蓄熱体としてのヒーティングエレメントEを積層状態で装填し、該伝熱エレメントEに高温流体(排ガスなど)と低温流体(燃焼用空気など)を交互に接触させることにより、高温流体の熱を低温流体に伝達させるように構成されている。 Generally, in the rotary regenerative heat exchanger, as shown in FIGS. 4 and 5, a rotor main body R is rotatably mounted in a housing H, and the rotor main body R is radiated by a radial diaphragm D (for example, 12 or 12). 24) The basket B is inserted into the partitioned sector, and the heating element E as a heat storage is loaded in the basket B in a stacked state, and a high-temperature fluid (exhaust gas etc.) and a low-temperature fluid (combustion) are loaded into the heat transfer element E. For example, the heat of the high-temperature fluid is transferred to the low-temperature fluid by alternately contacting the air.
ところで、成分(SO3、H2O)を含む未処理ガスおよび処理ガス(DeSOxからのミスト、ミスト成分)を含む排ガスを高温流体とする回転再生式熱交換器においては、長期間(2〜3年以上)の運転によってヒーティングエレメントEを挿入したバスケットBとダイヤフラムDの隙間に、上記ダストが堆積固化したり錆が発生して、全体的に余裕がなく、セクター内がパンパンに膨らんだ状態になって、上記バスケットBを点検や取り換えのためにローター本体Rから抜き出す際に、ダストや錆とバスケットの摩擦力が大きくなって、障害となることが多くあった。特に、点検のために抜き出す場合には、バスケットBの破損を避けなければならず、結局、抜き出しを断念して十分な点検が行えないことがあった。 By the way, in a rotary regenerative heat exchanger that uses an untreated gas containing components (SO 3 , H 2 O) and an exhaust gas containing treated gas (mist from DeSOx, mist component) as a high-temperature fluid, a long-term (2- The dust accumulated and solidified or rusted in the gap between the basket B where the heating element E was inserted and the diaphragm D during the operation for 3 years or more. When the basket B is pulled out of the rotor main body R for inspection or replacement, the frictional force between the dust and rust and the basket is often increased, which is an obstacle. In particular, when pulling out for inspection, breakage of the basket B has to be avoided, and eventually, it has been abandoned that sufficient inspection cannot be performed.
通常、バスケットBは、ローター本体Rにスムーズに出し入れできるように、挿入箇所より数mm小さく製作される。
しかし、これは、ローター本体Rの製作公差を考慮した寸法であり、ダストの進入を阻止するために挿入箇所と同じ寸法のバスケットを製作すると、実際のローター本体Rに挿入出来ないという欠点がある。
Usually, the basket B is manufactured to be several mm smaller than the insertion portion so that it can be smoothly inserted into and removed from the rotor body R.
However, this is a dimension that takes into account the manufacturing tolerance of the rotor body R, and if a basket having the same dimensions as the insertion point is manufactured in order to prevent dust from entering, there is a drawback that it cannot be inserted into the actual rotor body R. .
次に、バスケットBの寸法を挿入箇所よりも数十mm程度まで小さくすると、バスケットBの挿入には問題がなくても、ヒーティングエレメントEの通過断面積が減少して熱交換性能に影響を及ぼす欠点があった。
そこで、図6に示すように、複数に分割されたローター本体Rの点検を行う管理箇所のバスケットBの寸法のみを挿入箇所よりも十数mm程度まで小さくする方法も考えられる。
しかしながら、バスケットBの周囲に堆積するダストは、単に、積層されるだけでなく、バスケット材やローター本体材を腐食させて、その表面に錆が成長することで隙間がなくなり、ダストが隙間に圧着されることになることが解明されたため、従来よりも大きな隙間を予め作っておいても長期間の運転でダストによって隙間が消失されることが判明した。また、図4のように、縦軸型の回転再生式熱交換器の場合、バスケットBが正常に挿入されず、斜めに挿入されて流体のバイパスが起こることが予想される。(図7参照)
Next, if the size of the basket B is reduced to about several tens of millimeters from the insertion location, even if there is no problem in the insertion of the basket B, the passage cross-sectional area of the heating element E is reduced and the heat exchange performance is affected. There was a drawback.
Therefore, as shown in FIG. 6, a method is conceivable in which only the size of the basket B at the management location where the rotor main body R divided into a plurality of parts is inspected is made smaller than the insertion location by about a dozen mm.
However, the dust that accumulates around the basket B is not simply stacked, but also corrodes the basket material and rotor body material, and rust grows on the surface, eliminating the gap, and the dust is pressed into the gap. As a result, it was found that even if a gap larger than the conventional gap was created in advance, the gap disappeared due to dust after a long period of operation. Further, as shown in FIG. 4, in the case of the vertical regenerative heat exchanger, it is expected that the basket B is not normally inserted and is inserted obliquely, thereby causing fluid bypass. (See Figure 7)
本発明は、上記従来技術の欠点をなくして、長期間運転してもスムーズにローター本体に出し入れすることができる回転再生式熱交換器を提供することを課題とする。 An object of the present invention is to provide a rotary regenerative heat exchanger that eliminates the disadvantages of the prior art and can be smoothly inserted into and removed from the rotor body even when operated for a long period of time.
本発明の回転再生式熱交換器は、ハウジング内にローター本体を回転自在に装備して、該ローター本体を放射状のダイヤフラムにより多数区画したセクター内に複数のバスケットを挿入し、該バスケット内に蓄熱体としてのヒーティングエレメントを積層状態で装填し、該伝熱エレメントに排ガスなどの高温流体と燃焼用空気などの低温流体を交互に接触させることにより、高温流体の熱を低温流体に伝達させるように構成されことを特徴とする回転再生式熱交換器において、上記ダイヤフラムと対面するバスケットの側板に、数個のスペーサバーを適当な間隔をあけて断続的に取り付けることを特徴とする。また、複数の上記スペーサバーの軸線が、それぞれ上記バスケットの抜き差し方向に向いていることを特徴とする。さらに、複数の上記スペーサバーが、バスケットの中間高さ位置に一列状に配列されることを特徴とする。又更に、上記スペーサバーを1本の長尺状のバーとして構成することを特徴とする。 The rotary regenerative heat exchanger of the present invention is equipped with a rotor body rotatably in a housing, and a plurality of baskets are inserted into a sector in which the rotor body is partitioned by a radial diaphragm, and heat is stored in the basket. A heating element as a body is loaded in a stacked state, and a high-temperature fluid such as exhaust gas and a low-temperature fluid such as combustion air are alternately brought into contact with the heat transfer element so that the heat of the high-temperature fluid is transferred to the low-temperature fluid. The rotary regenerative heat exchanger is characterized in that several spacer bars are intermittently attached to the side plate of the basket facing the diaphragm at appropriate intervals. Further, the axis of the plurality of spacer bars is respectively directed to the insertion / removal direction of the basket. Furthermore, the plurality of spacer bars are arranged in a line at a middle height position of the basket. Still further, the spacer bar is configured as one long bar.
本発明の回転再生式熱交換器は、下記の効果を奏する。
1) ダストを含む高温流体がバスケットの側板とダイヤフラムの間へ進入する量が減少し、その結果、堆積量が減少する。
2) スペーサバーとダイヤフラムの接触摩擦が小さいため、従来、抜き差しが困難であった熱交換装置のバスケットをスムーズに抜き差しできる。
The rotary regenerative heat exchanger of the present invention has the following effects.
1) The amount of high temperature fluid containing dust entering between the side plate of the basket and the diaphragm is reduced, and as a result, the amount of deposition is reduced.
2) Since the contact friction between the spacer bar and the diaphragm is small, it is possible to smoothly insert and remove the basket of the heat exchange device, which has been difficult to insert and remove.
以下、本発明の回転再生式熱交換器の一実施例について、図面を参照しながら説明する。 Hereinafter, an embodiment of the regenerative heat exchanger of the present invention will be described with reference to the drawings.
図1において、1はバスケットであって、ダイヤフラム2の間に数個(本実施例では10個)装填されている。これらのバスケット1は、点検や交換時に矢印X方向に抜き差しするようになっている。 In FIG. 1, reference numeral 1 denotes a basket, and several (10 in the present embodiment) are loaded between the diaphragms 2. These baskets 1 are inserted and removed in the direction of arrow X during inspection and replacement.
図2からも明らかなように、バスケット1の内部には、多数枚のヒーティングエレメント3が積層状態で収納されている。1aは側板であって、上記ダイヤフラム2に向かい合っている。 As apparent from FIG. 2, a large number of heating elements 3 are housed in the basket 1 in a stacked state. Reference numeral 1a denotes a side plate that faces the diaphragm 2 described above.
上記ダイヤフラム2に対面する、バスケット1の側板1aには、数個(本実施例では3本)の金属製のスペーサバー4が適当な間隔をあけて断続的に取り付けられている。これらのスペーサバー4の軸線は、それぞれ上記バスケット1の抜き差し方向(矢印X)に向いている。また、これらのスペーサバー4は、バスケット1の中間高さ位置に一列状に配列するのが摩擦抵抗が少なくて好ましいが、これに限定するものではなく、多少、上下にばらついて配置してもよい。各スペーサバー4は、例えば、厚み16mm、巾38mm、長さ100mmであるが、これに限定するものではない。 Several (three in this embodiment) metal spacer bars 4 are intermittently attached to the side plate 1a of the basket 1 facing the diaphragm 2 with appropriate intervals. The axis lines of these spacer bars 4 are each directed in the insertion / removal direction (arrow X) of the basket 1. These spacer bars 4 are preferably arranged in a row at the intermediate height position of the basket 1 because of low frictional resistance, but the present invention is not limited to this, and the spacer bars 4 may be arranged with some variation in the vertical direction. Good. Each spacer bar 4 has, for example, a thickness of 16 mm, a width of 38 mm, and a length of 100 mm, but is not limited thereto.
図1(A)に示す、1つのセクター内に円周方向に1個入るバスケット1は、図2(B)に示すように、両側の側板1aにスペーサバー4を取り付け、また、2個以上入る場合は、上記バスケット1にスペーサバー4を取り付ける。なお、スペーサバー4の取り付けに伴い、外形寸法が合致するよう、バスケット1そのものの寸法は、ダイヤフラムとの間隔が大きすぎると熱交換性能に影響するので、適正なものとする。 As shown in FIG. 2 (B), the basket 1 shown in FIG. 1 (A) that fits in one circumferential direction has a spacer bar 4 attached to the side plates 1a on both sides, and two or more. When entering, the spacer bar 4 is attached to the basket 1. It should be noted that the dimensions of the basket 1 itself are appropriate so that when the spacer bar 4 is attached, the dimensions of the basket 1 itself are appropriate because the heat exchange performance is affected if the distance from the diaphragm is too large.
本実施例では、以上のように構成されているので、ダストを含む高温流体が上記バスケット1の側板1aとダイヤフラム2の間へ進入する量が減少し、その結果、堆積量が減少するだけでなく、スペーサバー4とダイヤフラム2の接触摩擦が小さいため、従来、抜き差しが困難であった熱交換装置のバスケットをスムーズに抜き差しできるようになった。 In the present embodiment, since it is configured as described above, the amount of high temperature fluid including dust entering between the side plate 1a of the basket 1 and the diaphragm 2 is reduced, and as a result, only the amount of deposition is reduced. In addition, since the contact friction between the spacer bar 4 and the diaphragm 2 is small, it has become possible to smoothly insert and remove the basket of the heat exchange device that has been difficult to remove and insert.
図3は、本願発明の別の実施例を示すもので、上記複数個のスペーサバー4を1本の長尺状のバーとして、バスケット1の側板1aの中間高さ位置に抜き差し方向に配向して取り付ける。本実施例では、更にダストの堆積量が減少する。 FIG. 3 shows another embodiment of the present invention. The plurality of spacer bars 4 are formed as one long bar and are oriented in the insertion / removal direction at the intermediate height position of the side plate 1a of the basket 1. And attach. In this embodiment, the amount of accumulated dust is further reduced.
1 バスケット
1a 側板
2 ダイヤフラム
3 ヒーティングエレメント
4 スペーサバー
H ハウジング
R ローター本体
1 Basket 1a Side plate 2 Diaphragm 3 Heating element 4 Spacer bar H Housing R Rotor body
Claims (3)
上記ダイヤフラムと対面するバスケットの側板に、該側板とは別体の、楕円形断面の1本の長尺状のバーとして構成されたスペーサバーを取り付けることを特徴とする回転再生式熱交換器。 A rotor main body is rotatably mounted in a housing, a plurality of baskets are inserted into a sector in which the rotor main body is partitioned by a radial diaphragm, and heating elements as heat storage bodies are loaded in a stacked state in the basket. and, wherein the heating element by contacting a low temperature fluid such as high temperature fluid and the combustion air, such as exhaust gas alternately rotating regenerative heat exchanger that is configured to transfer heat of the hot fluid to the cold fluid In the vessel
A rotary regenerative heat exchanger characterized in that a spacer bar configured as a single elongated bar having an elliptical cross section is attached to a side plate of a basket facing the diaphragm.
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JP2014247936A JP5959606B2 (en) | 2014-12-08 | 2014-12-08 | Rotating regenerative heat exchanger |
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JP2014247936A JP5959606B2 (en) | 2014-12-08 | 2014-12-08 | Rotating regenerative heat exchanger |
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JP2010255680A Division JP5717409B2 (en) | 2010-11-16 | 2010-11-16 | Rotating regenerative heat exchanger |
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JP5959606B2 true JP5959606B2 (en) | 2016-08-02 |
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JP2017048973A (en) | 2015-09-02 | 2017-03-09 | アルヴォス インコーポレイテッド | Heat transfer element laminated body |
Family Cites Families (7)
Publication number | Priority date | Publication date | Assignee | Title |
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JPS5442055A (en) * | 1977-09-09 | 1979-04-03 | Abc Trading Co | Rotary convection heattexchanger capable of maintenance |
JPS5818090A (en) * | 1981-07-25 | 1983-02-02 | Seibu Giken:Kk | Rotary type heat exchanger |
JPS60223994A (en) * | 1984-04-20 | 1985-11-08 | Nippon Kokan Kk <Nkk> | Rotary heat exchanger |
US4561492A (en) * | 1985-01-22 | 1985-12-31 | The Air Preheater Company, Inc. | Element basket assembly for heat exchanger |
US5048595A (en) * | 1991-03-04 | 1991-09-17 | Abb Air Preheater, Inc. | Rotary regenerative air preheater basket sealing |
US5911271A (en) * | 1998-08-27 | 1999-06-15 | Abb Air Preheater, Inc. | Floating bypass seal for rotary regenerative heat exchangers |
US5913359A (en) * | 1998-10-26 | 1999-06-22 | Abb Air Preheater, Inc. | Bypass seals for rotary regenerative heat exchangers |
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