JPS5836277B2 - Heat storage and regeneration heat exchanger - Google Patents
Heat storage and regeneration heat exchangerInfo
- Publication number
- JPS5836277B2 JPS5836277B2 JP2042476A JP2042476A JPS5836277B2 JP S5836277 B2 JPS5836277 B2 JP S5836277B2 JP 2042476 A JP2042476 A JP 2042476A JP 2042476 A JP2042476 A JP 2042476A JP S5836277 B2 JPS5836277 B2 JP S5836277B2
- Authority
- JP
- Japan
- Prior art keywords
- heat
- heat storage
- damper
- heat exchanger
- hot gas
- 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.)
- Expired
Links
Landscapes
- Air Supply (AREA)
Description
【発明の詳細な説明】
本発明は、熱ガスと受熱ガスとを常時流通させながら、
両ガス間で熱の授受を行なわせる蓄熱再生式熱交換器に
関する。[Detailed Description of the Invention] The present invention provides a method for constantly circulating hot gas and heat-receiving gas.
The present invention relates to a heat storage and regeneration type heat exchanger that transfers heat between both gases.
多量のガスとガスとを熱交換させるに際して、従来使用
されている代表的な蓄熱再生式熱交換器は、回転蓄熱再
生式熱交換器である。A typical regenerative heat exchanger conventionally used for heat exchange between large amounts of gas is a rotary regenerative heat exchanger.
この熱交換器は、蓄熱媒体を収納した円肖状の蓄熱室を
回転させながら、その蓄熱式に熱ガスと受熱ガスとを回
転軸方向に流通させて、両ガス間の熱交換を行なわせる
ものであるが、両ガス間の漏洩現象を減少させるために
は、その回転体に熱膨脹を配慮した特別な工夫を施さね
ばならない。This heat exchanger rotates a round-shaped heat storage chamber containing a heat storage medium, and allows hot gas and heat-receiving gas to flow in the direction of the rotation axis in a heat storage manner, thereby exchanging heat between the two gases. However, in order to reduce the leakage phenomenon between the two gases, the rotating body must be specially designed to take into account thermal expansion.
勿論そうした工夫は特公昭43−4393号公報などに
みられる如く、従来に於ても試みりrn・るが、熱膨脹
に起因する様々な問題の抜本的解決とはなっていない。Of course, such devices have been attempted in the past, as seen in Japanese Patent Publication No. 4393/1983, but they have not fundamentally solved the various problems caused by thermal expansion.
近年、省エネルギーの立場から、各種のプラントから排
出される燃焼ガスの熱回収が不可欠なものとなって来て
おり、特に排煙脱硫乃至ぱ排煙脱硝に際しては、ガス漏
洩の少ない、効率のよい熱回収が必須とされている。In recent years, from the standpoint of energy conservation, heat recovery from combustion gas discharged from various plants has become essential.Especially in flue gas desulfurization and flue gas denitrification, efficient methods with less gas leakage have become essential. Heat recovery is essential.
本発明は、排煙脱硫装置乃至は排煙脱硝装置にも組み込
むことが可能な再生式熱交換器を提案するものであって
、蓄熱室を回転させずに静置させ、しかも熱ガスと受熱
ガスとを連続的にその蓄熱室に流通させながら、前記両
ガスを効率よく熱交換させる蓄熱再生式熱交換器を提供
するものである。The present invention proposes a regenerative heat exchanger that can be incorporated into flue gas desulfurization equipment or flue gas denitrification equipment, in which the heat storage chamber is left stationary without rotating, and the heat exchanger is able to receive heat from hot gas. The present invention provides a heat storage and regeneration type heat exchanger that efficiently exchanges heat between the two gases while continuously circulating the gas through the heat storage chamber.
以下、添付図面にそって本発明をさらに具体的に説明す
ると、第1図は本発明に係る蓄熱再生式熱交換器の一実
施例を、その一部を切欠いて示す斜視図であって、この
熱交換器は、多数枚の金属板からなる蓄熱媒体1を収納
して並列一体に配列された合計8基の蓄熱室2a,2b
,・・・・・・2g,2hを有している。Hereinafter, the present invention will be described in more detail with reference to the accompanying drawings. FIG. 1 is a partially cutaway perspective view showing an embodiment of the heat storage and regeneration type heat exchanger according to the present invention, This heat exchanger consists of a total of eight heat storage chambers 2a and 2b that house heat storage media 1 made of a large number of metal plates and are arranged in parallel.
,...2g, 2h.
各蓄熱室はそれぞれ個別にふたつの開口部を有し、一方
の開口部はダンパーを介して熱ガス導入グクト3及び受
熱ガス排出グクト4にそれぞれ連通ずることができ、例
えば、蓄熱室2aはダンパー5aを介して熱ガス導入夕
゛クト3と連通し、夕゛ンパー6aによって受熱ガス排
出ダクト4と連通ずる。Each heat storage chamber has two openings, and one of the openings can be communicated with the hot gas introduction section 3 and the heat receiving gas discharge section 4 via a damper. It communicates with the hot gas introduction duct 3 via the damper 5a, and with the heat receiving gas exhaust duct 4 via the damper 6a.
同様にして各蓄熱室の曲方の開口部はダンパーを介して
熱ガス排出ダクト7及び受熱ガス導入ダクト8にそれぞ
れ連通することができ、例えば、蓄熱室2aはダンパー
9aを介して熱ガス排出夕゛クト7と連通し、グンパー
10aによって受熱ガス導入グクト8と連通ずる。Similarly, the curved opening of each heat storage chamber can be communicated with the hot gas discharge duct 7 and the heat receiving gas introduction duct 8 through dampers. It communicates with the exhaust pipe 7, and communicates with the heat-receiving gas introduction pipe 8 through the pumper 10a.
そして各ターンパーにはグンパー毎に圧縮空気シリンタ
一一式のダンパ開閉機11が設けられている。A damper opening/closing machine 11 for a set of compressed air cylinders is provided in each turner.
次に、上記の如く構或される熱交換器に於で、その熱交
換様式を説明すると、第1図は蓄熱室2a,2b,2g
及び2hがそれぞれ蓄熱状態にあり、蓄熱室2c,2d
,2e及び2fがそれぞれ放熱状態にある場合を示して
いる。Next, to explain the heat exchange mode in the heat exchanger constructed as above, Fig. 1 shows the heat storage chambers 2a, 2b, 2g.
and 2h are in a heat storage state, respectively, and heat storage chambers 2c and 2d
, 2e and 2f are each in a heat dissipation state.
すなわち、蓄熱状態にある各蓄熱室は、熱ガスの導入ダ
クト及び排出ダクトに通ずるグンパーのみが開放状態に
保持され、受熱ガスの導入ダクト及び排出夕゛クトに通
ずるグンパーはすべて閉鎖状態に保持される。In other words, in each heat storage chamber in a heat storage state, only the pumps leading to the hot gas introduction duct and exhaust duct are kept open, and all the pumps leading to the heat receiving gas introduction duct and exhaust duct are kept closed. Ru.
これに対し、放熱状態にある各蓄熱室は、熱ガスの導入
ダクト及び排出ダクトに通ずるダンバーはすべて閉鎖さ
れ、受熱ガスの導入ダクト及び排出夕”クトに通ずるの
みが開放状態に保持されるのである。On the other hand, in each heat storage chamber in the heat dissipation state, all the dampers leading to the hot gas introduction duct and exhaust duct are closed, and only the dampers leading to the heat receiving gas introduction duct and exhaust duct are kept open. be.
而して、熱ガス導入ダクト3から熱交換器内に供給され
た熱ガスは、夕゛ンパー5a,5b,5g及び5hを通
って蓄熱室2a+ 2by2g及び2hに入り、蓄熱媒
体1を刀口熱後、熱ガス排出ダクト7から熱交換器外に
排出される。The hot gas supplied into the heat exchanger from the hot gas introduction duct 3 passes through the dampers 5a, 5b, 5g and 5h, enters the heat storage chambers 2a+2by2g and 2h, and heats the heat storage medium 1. Thereafter, the hot gas is discharged from the heat exchanger through the exhaust duct 7.
この間、受熱ガスは受熱ガス導入夕“クト8から熱交換
器内に供給され、蓄熱室2cy 2d,2e及び2fを
通過することによって、蓄熱媒体から熱の供給を受けな
がら、グンパー6cy 6d,6e及び6fを通って受
熱ガス排出夕゜クト4から熱交換器外に排出される。During this time, the heat-receiving gas is supplied into the heat exchanger from the heat-receiving gas introduction port 8, and passes through the heat storage chambers 2cy 2d, 2e, and 2f, receiving heat from the heat storage medium. and 6f, and is discharged to the outside of the heat exchanger from the heat-receiving gas discharge outlet 4.
そして熱ガスの通過によって蓄熱媒体力切口熱された蓄
熱室と、受熱ガスの通過によって蓄熱媒体が冷却された
蓄熱室とは、それぞれ一定な時間的ずれを持ちながら、
蓄熱状態から放熱状態へ、1た放熱状態から蓄熱状態へ
と順次移行する。There is a certain time lag between the heat storage chamber where the heat storage medium is heated by the passage of the hot gas and the heat storage chamber where the heat storage medium is cooled by the passage of the heat receiving gas.
The state sequentially shifts from the heat storage state to the heat radiation state, and from the heat radiation state to the heat storage state.
つ1り、熱交換器には熱ガスと受熱ガスとが常時供給さ
れるが、各蓄熱室に対する熱ガスと受熱ガスとの分配は
、一定のシーケンス(順序)で行なわれ、これにより、
蓄熱状態にある蓄熱室と放熱状態にある蓄熱室とが常に
同数に保持されるのであって、そうした状況は、各蓄熱
室と熱ガスダクト及び受熱ガスダクトとの間に介在する
個々のダンパーの開閉を、一定のシーケンスによって行
なうことによって達或される。In other words, hot gas and heat-receiving gas are constantly supplied to the heat exchanger, but the distribution of hot gas and heat-receiving gas to each heat storage chamber is performed in a certain sequence.
The number of heat storage chambers in a heat storage state and the number of heat storage chambers in a heat radiation state are always maintained at the same level, and such a situation requires opening and closing of individual dampers interposed between each heat storage chamber and the hot gas duct and heat receiving gas duct. , is achieved by performing them in a certain sequence.
第2図はダンパーの開閉に関するシーケンスの一例を示
す説明図であって、ここでは第1図に示す熱交換器の熱
ガス導入用ダンパー5a,5b・・・・・・5g,5h
と、受熱ガス排出用グンパー6 a r6b・・・・・
・6g,6hとの開閉状態が、時間的にA〜Cの如く変
化する状況が示されている。FIG. 2 is an explanatory diagram showing an example of a sequence regarding opening and closing of dampers, and here, hot gas introduction dampers 5a, 5b, 5g, 5h of the heat exchanger shown in FIG.
And Gumper 6a r6b for discharging heat receiving gas...
・Situations in which the open/close states of 6g and 6h change over time as shown in A to C are shown.
な卦、本発明の熱交換器に於では、熱ガスの排出が行な
われる各グンパーは、その導入が行なわれる各グンパー
と同一の開閉状態にあり、受熱ガスの導入が行なわれる
各ダンパーは、その排出が行なわれる各ダンパーと同一
の開閉状態にある。In the heat exchanger of the present invention, each damper through which hot gas is discharged is in the same open/closed state as each damper through which hot gas is introduced, and each damper through which heat receiving gas is introduced is It is in the same open and closed state as each damper through which the discharge is performed.
さて、第2図のA−Cは各ダンパーの開閉状態の時間的
な推移を示すものであるが、Aで示す通り、ある時点で
はダンパー5a及び5hが全開、5c,5d,5e及び
5fか全閉、5b及び5gが半開半閉の状態にある。Now, A-C in Fig. 2 shows the temporal transition of the open and closed states of each damper, and as shown in A, at a certain point, dampers 5a and 5h are fully open, and dampers 5c, 5d, 5e, and 5f are fully open. Fully closed, 5b and 5g are half open and half closed.
一方、受熱ガス側の夕゛ンパーである6ay 6b,6
g,6hは全閉、6d及び6fは全開、6c及び6fは
半開半閉の状態にある。On the other hand, 6ay 6b, 6 which is the damper on the heat receiving gas side
g and 6h are fully closed, 6d and 6f are fully open, and 6c and 6f are half open and half closed.
今、熱ガス及び受熱ガスの蓄熱室2a,2b・・・・・
・2g,2hへの分配を図示のアルファベット順に行な
うものと仮定すれは、ダンパ−5b及び6fの開放と、
グンパー60及び5gの閉鎖を同一速度で行なうことに
より、各ターンパーの開閉状態を第2図のAからBに移
行させることができる。Now, the heat storage chambers 2a, 2b for hot gas and heat receiving gas...
・Assuming that the distribution to 2g and 2h is carried out in the alphabetical order shown in the figure, opening dampers 5b and 6f,
By closing the turnpers 60 and 5g at the same speed, the open/closed state of each turnper can be shifted from A to B in FIG. 2.
同様にしてダンパー50及ん6gの開放と、ダンパー6
d及び5hの閉鎖を同一速度で行なうことにより、各タ
ーンパーの開閉状態を第2図のBからCに移行さぜるこ
とかできるのである。Similarly, dampers 50 and 6g are opened, and damper 6
By closing d and 5h at the same speed, the open/closed state of each turnper can be changed from B to C in FIG. 2.
つ1り、本発明の熱交換器にあっては、個々の蓄熱室の
熱ガス用ダンパーと受熱ガス用グンパーとが同時に開放
されることのない条件下に、熱ガス用の各ダンパーと受
熱カス用の各ダンパーとを、その開閉時期に一定の時間
的ずれを持たせながら、同一方向に、同一速度で順次開
閉させるのであって、これにより本発明の熱交換器では
、蓄熱状態にある蓄熱室と、放熱状態にある蓄熱室とが
常に同数に保持されるのである。In other words, in the heat exchanger of the present invention, each damper for hot gas and the damper for heat receiving gas in each heat storage chamber are not opened at the same time. The dampers for waste are sequentially opened and closed in the same direction and at the same speed, with a certain time lag in their opening and closing timing, and as a result, in the heat exchanger of the present invention, the heat exchanger is in a heat storage state. The number of heat storage chambers and the heat storage chambers in a heat radiating state are always maintained at the same number.
この場合、各ダンパーの開閉は公知のダンパー開閉機構
を利用して行なうことができ、例えは第1図に示す如く
、各夕“ンパー毎に圧縮シリンダ一式のダンハー開閉機
ヲ取り付け、上述のような開閉時期のシーケンスを組み
入れたタイマーと連動する圧縮空気弁の開閉によって、
前記のダンパー開閉機を開閉することができる。In this case, each damper can be opened and closed using a known damper opening/closing mechanism, for example, as shown in Figure 1, a damper opening/closing machine with a set of compression cylinders is installed for each damper, as described above. By opening and closing a compressed air valve that is linked to a timer that incorporates a suitable opening and closing timing sequence,
The damper opening/closing machine can be opened and closed.
以上、本発明の一実施例についてその構成と熱交換様式
を説明したが、本発明の蓄熱再生式熱交換器は図示の具
体例に限定されるものではなく、例えば蓄熱室の基数は
4基、6基、8基、10基の如く任意に選択することが
できる。Although the configuration and heat exchange mode of an embodiment of the present invention have been described above, the heat storage and regeneration type heat exchanger of the present invention is not limited to the specific example shown in the drawings; for example, the number of heat storage chambers is four. , 6 groups, 8 groups, or 10 groups.
しかし、本発明の熱交換器は、常時熱ガスと受熱ガスの
供給を受けて両ガス間の熱の授受を連続的に行なう関係
上、少なくとも4基以上の蓄熱室を具えることが必要で
あって、その総基数は偶数であることが好1しい。However, since the heat exchanger of the present invention is constantly supplied with hot gas and heat-receiving gas and continuously transfers heat between the two gases, it is necessary to include at least four heat storage chambers. The total number of bases is preferably an even number.
上述したところから明らかな通り、少なくとも4基以上
の蓄熱室を有する本発明の蓄熱再生式熱交換器は、蓄熱
状態にある蓄熱室と、放熱状態にある蓄熱室が常に同数
に保持されるため、熱ガスと受熱ガスを同時に、しかも
連続的に供給して両ガス間の熱交換を連続的に行なうこ
とができる。As is clear from the above, the heat storage and regeneration type heat exchanger of the present invention having at least four or more heat storage chambers always maintains the same number of heat storage chambers in a heat storage state and heat storage chambers in a heat radiation state. By supplying the hot gas and the heat-receiving gas simultaneously and continuously, it is possible to continuously perform heat exchange between the two gases.
従って、本発明の熱交換器は、多量の熱ガスから熱を回
収する場合に、極めて好適である。Therefore, the heat exchanger of the present invention is extremely suitable for recovering heat from a large amount of hot gas.
しかのみならず、本発明の熱交換器は、熱による膨脹収
縮が最も生起する蓄熱室が静置状態にあるため、回転蓄
熱再生式熱交換器に於けるが如き回転体の熱影響に対す
る配慮が必要でないという構造上の利点もある。In addition, in the heat exchanger of the present invention, since the heat storage chamber in which expansion and contraction due to heat occurs most often is in a stationary state, consideration must be given to the thermal influence of the rotating body such as in a rotary heat storage and regeneration type heat exchanger. It also has the structural advantage that it is not necessary.
第1図は本発明に係る蓄熱再生式熱交換器の一実施例を
、その一部を切欠いて示す斜視図である。
第2図は第1図に示した蓄熱再生式熱交換器に於げる夕
”ンパーの開閉シーケンスを示す説明図である。
1・・・蓄熱媒体、2a”h・・・蓄熱室、3・・・熱
ガス導入ダクト、4・・・受熱ガス排出ダクト、5a〜
h・・・熱ガス導入ダンパー、6a”−h・・・受熱ガ
ス排出ダンパー、7・・・熱ガス排出タークト、8・・
・受熱ガス導入グンハー、9a・・・熱ガス排出ダンパ
ー、10a・・・受熱ガス導入ダンパー 11・・・グ
ンパー開閉機。FIG. 1 is a partially cutaway perspective view showing an embodiment of a heat storage and regeneration type heat exchanger according to the present invention. Fig. 2 is an explanatory diagram showing the opening/closing sequence of the evening chamber in the heat storage and regeneration type heat exchanger shown in Fig. 1. 1... Heat storage medium, 2a''h... Heat storage chamber, 3 ...Hot gas introduction duct, 4...Heat receiving gas discharge duct, 5a~
h...Hot gas introduction damper, 6a"-h...Heat-receiving gas discharge damper, 7...Hot gas discharge turctor, 8...
- Heated gas introduction Gunhar, 9a...Hot gas discharge damper, 10a...Heat receiving gas introduction damper 11...Gumper opening/closing machine.
Claims (1)
体に配列させ、各蓄熱室の一方の開口部を熱ガス導入ダ
クト及び受熱ガス排出ダクトに夕゛ンパーを介して連通
させると共に、曲方の開口部を熱ガス排出ダクト及び受
熱ガス導入ダクトにダンパーを介して連通させ、さらに
前記の各ダンパーを時間的にずらして開閉させるダンパ
ー開閉機構を設えた蓄熱再生式熱交換器。1 At least four heat storage chambers containing a heat storage medium are arranged in parallel and integrated, one opening of each heat storage chamber is communicated with the hot gas introduction duct and the heat receiving gas discharge duct via a damper, and A heat storage and regeneration type heat exchanger, which has one opening communicated with a hot gas discharge duct and a heat receiving gas introduction duct via a damper, and is further provided with a damper opening/closing mechanism that opens and closes each of the dampers in a temporally staggered manner.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2042476A JPS5836277B2 (en) | 1976-02-26 | 1976-02-26 | Heat storage and regeneration heat exchanger |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2042476A JPS5836277B2 (en) | 1976-02-26 | 1976-02-26 | Heat storage and regeneration heat exchanger |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS52103743A JPS52103743A (en) | 1977-08-31 |
JPS5836277B2 true JPS5836277B2 (en) | 1983-08-08 |
Family
ID=12026642
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2042476A Expired JPS5836277B2 (en) | 1976-02-26 | 1976-02-26 | Heat storage and regeneration heat exchanger |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5836277B2 (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20060054301A1 (en) * | 2004-02-19 | 2006-03-16 | Mcray Richard F | Variable area mass or area and mass species transfer device and method |
-
1976
- 1976-02-26 JP JP2042476A patent/JPS5836277B2/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
JPS52103743A (en) | 1977-08-31 |
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