JPH06182134A - Carbon dioxide concentrator - Google Patents
Carbon dioxide concentratorInfo
- Publication number
- JPH06182134A JPH06182134A JP4344061A JP34406192A JPH06182134A JP H06182134 A JPH06182134 A JP H06182134A JP 4344061 A JP4344061 A JP 4344061A JP 34406192 A JP34406192 A JP 34406192A JP H06182134 A JPH06182134 A JP H06182134A
- Authority
- JP
- Japan
- Prior art keywords
- combustion gas
- heat exchanger
- carbon dioxide
- plate
- box body
- 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
Links
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
Landscapes
- Carbon And Carbon Compounds (AREA)
- Separation Of Gases By Adsorption (AREA)
Abstract
Description
【０００１】[0001]
【産業上の利用分野】本発明は、熱交換器を組み込んだ
炭酸ガス濃縮装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a carbon dioxide gas concentrator incorporating a heat exchanger.
【０００２】[0002]
【従来の技術】炭酸ガス濃縮装置は、特開平３−１３１
２５９号等に示されているように、燃焼ガス中の炭酸ガ
スを濃縮する手段によって構成されている。炭酸ガスの
供給は、例えばガス給湯器で燃焼が行なわれ、炭酸ガス
を含む燃焼ガスがブロアーによって炭酸ガス濃縮装置へ
供給される。そして、吸着剤を利用した温度スイング方
式の炭酸ガス濃縮装置において、燃焼ガスの冷却・除湿
を吸着塔の前段で熱交換器により行い、水蒸気吸着塔で
完全に近い除湿を行ない、そして炭酸ガス吸着塔で炭酸
ガスを吸着し、ヒータによる加熱で充分に濃い炭酸ガス
を生成、供給する。2. Description of the Related Art A carbon dioxide concentrator is disclosed in Japanese Patent Laid-Open No. 3-131.
As shown in No. 259, etc., it is constituted by means for concentrating carbon dioxide gas in the combustion gas. The carbon dioxide gas is supplied, for example, by combustion in a gas water heater, and the combustion gas containing carbon dioxide gas is supplied to the carbon dioxide gas concentrator by a blower. Then, in a temperature swing type carbon dioxide gas concentrator using an adsorbent, the combustion gas is cooled and dehumidified by a heat exchanger in the preceding stage of the adsorption tower, and near complete dehumidification is performed in the water vapor adsorption tower. Carbon dioxide is adsorbed in the tower, and a sufficiently rich carbon dioxide is generated and supplied by heating with a heater.
【０００３】しかるに上記従来のフィン・アンド・チュ
ーブ熱交換器はプレートフィンの長辺方向に対し垂直に
燃焼ガスを流していたために、長辺方向とフィン枚数方
向の積の面積が大きくなり、燃焼ガスを均等に各プレー
トフィンに接触させるためには大きなヘッダーが必要で
あった。したがって、大きなスペースが必要となり、炭
酸ガス濃縮装置が大きくなってしまった。また、従来の
フィン・アンド・チューブ熱交換器では燃焼ガスと冷却
水の熱交換が直交式であったために、熱交換効率が低
く、目標温度に燃焼ガスを冷却するため大きな伝熱面積
が必要であった。However, since the conventional fin-and-tube heat exchanger flows the combustion gas perpendicularly to the long side direction of the plate fins, the product area of the long side direction and the number of fins direction becomes large, and the combustion is increased. A large header was required to evenly contact the gas on each plate fin. Therefore, a large space is required, and the carbon dioxide concentrator has become large. Moreover, in the conventional fin-and-tube heat exchanger, the heat exchange of the combustion gas and the cooling water is orthogonal, so the heat exchange efficiency is low and a large heat transfer area is required to cool the combustion gas to the target temperature. Met.
【０００４】[0004]
【発明が解決しようとする課題】本発明の課題とすると
ころは、炭酸ガス濃縮装置を構成する熱交換器の熱交換
効率を向上させ小型にすることおよび、熱交換器内に生
じる結露水を経路から速やかに排水することにある。The object of the present invention is to improve the heat exchange efficiency of the heat exchanger constituting the carbon dioxide concentrating device to make it compact, and to prevent dew condensation water generated in the heat exchanger. It is to drain water quickly from the route.
【０００５】[0005]
【課題を解決するための手段】本発明の要旨とするとこ
ろの１つは、請求項１記載のように、炭化水素を有する
燃料から燃焼ガスを得、燃焼ガス中の炭酸ガスを吸着剤
を用い、温度差を利用して濃縮する炭酸ガス濃縮装置２
において、燃焼ガスを冷却するためのフィン・アンド・
チューブ型の熱交換器５を箱体内に収めて燃焼ガス３の
流路に組み込み、この箱体の上部に燃焼ガス流入口２２
を設け、下部に燃焼ガス流出口１５を設け、フィン・ア
ンド・チューブ型の熱交換器５のプレートフィン１３の
長辺方向を箱体の上下方向とし、この箱体内下部に結露
水溜め２６及び、結露水を箱体の外部に排水する結露水
排水口１６を設けたことを特徴とする炭酸ガス濃縮装置
であり、他の１つは請求項２記載のように、燃焼ガス流
出口端部２５を箱体底板１８より突出させ、突出部の上
部にプレートフィン１３の短辺と同じ幅をもち、燃焼ガ
ス流出口１５の外径以上の長さをもつ板体１４を、箱体
底板１８と平行もしくは勾配を付けて配設したことを特
徴とする請求項１記載の炭酸ガス濃縮装置であり、さら
に他の１つは請求項３記載のように、箱体底板１８に、
勾配を持たせることを特徴とする請求項１記載の炭酸ガ
ス濃縮装置である。One of the main points of the present invention is to obtain a combustion gas from a fuel having hydrocarbons and to use carbon dioxide gas in the combustion gas as an adsorbent as described in claim 1. Carbon dioxide gas concentrator 2 which is used and concentrates by utilizing the temperature difference
And fins for cooling the combustion gas at
The tube-type heat exchanger 5 is housed in the box body and installed in the flow path of the combustion gas 3, and the combustion gas inlet 22 is provided at the upper part of the box body.
Is provided, the combustion gas outlet 15 is provided at the bottom, and the long side direction of the plate fins 13 of the fin-and-tube heat exchanger 5 is the vertical direction of the box body. The carbon dioxide gas concentrating device is provided with a dew condensation water discharge port 16 for discharging the dew condensation water to the outside of the box body, and the other one is a combustion gas outlet end portion as described in claim 2. 25 is projected from the box bottom plate 18, and the plate 14 having the same width as the short side of the plate fin 13 at the upper part of the projecting portion and having a length equal to or larger than the outer diameter of the combustion gas outlet 15 is attached to the box bottom plate 18. The carbon dioxide gas concentrating device according to claim 1, wherein the carbon dioxide gas concentrating device is arranged in parallel or with a gradient, and another one is the box bottom plate 18 as described in claim 3.
The carbon dioxide gas concentrating device according to claim 1, characterized in that it has a gradient.
【０００６】[0006]
【作 用】上記の炭酸ガス濃縮装置において、燃焼ガス
を冷却するために、炭酸ガスを箱体内に収められたフィ
ン・アンド・チューブ熱交換器のプレートフィンの長辺
方向と平行に流し、燃焼ガスの流路面積を小さくするこ
とにより、燃焼ガス流路の距離をどの位置においても同
じにすることができ、小さなヘッダーでも均一に全ての
プレートフィンに燃焼ガスを接触させることができる。
また、燃焼ガスと冷却水の流れを対向にすることによ
り、少量の冷却水で燃焼ガスを冷却することができる。
したがって、直交式の熱交換器に比べ熱交換効率を向上
させることができ、水蒸気の結露を促進させることがて
きる。[Operation] In the above carbon dioxide concentrator, in order to cool the combustion gas, the carbon dioxide gas is flowed in parallel with the long side direction of the plate fins of the fin-and-tube heat exchanger housed in the box body and burned. By reducing the gas flow passage area, the distance of the combustion gas flow passage can be made the same at any position, and the combustion gas can be uniformly brought into contact with all plate fins even with a small header.
Further, by making the flow of the combustion gas and the flow of the cooling water face each other, the combustion gas can be cooled with a small amount of the cooling water.
Therefore, the heat exchange efficiency can be improved as compared with the orthogonal heat exchanger, and the condensation of water vapor can be promoted.
【０００７】また請求項２に記載のように構成すること
により、燃焼ガス流出口より結露水を漏出させることな
く燃焼ガスと結露水を効率的に分離することができる。
さらに、請求項３に記載のように構成することにより、
結露水を速やかに排出し、熱交換器の燃焼ガス流出口に
つながる水蒸気吸着塔へ流出する水蒸量を効率的に低減
させる事が出来る。According to the second aspect of the invention, the combustion gas and the condensed water can be efficiently separated without leaking the condensed water from the combustion gas outlet.
Furthermore, by constructing as described in claim 3,
The condensed water can be quickly discharged, and the amount of water vapor flowing out to the steam adsorption tower connected to the combustion gas outlet of the heat exchanger can be efficiently reduced.
【０００８】[0008]
【実施例】以下本発明を実施例に基づいて詳述する。勿
論、この発明が下記の実施例に限らないことは言うまで
もない。EXAMPLES The present invention will be described in detail below based on examples. Needless to say, the present invention is not limited to the following embodiments.
【０００９】実施例１ 図１は、本発明を説明するシステムの概略図、図２は同
上の燃焼ガス冷却用の熱交換器を正面から見た内部を示
すものである。Embodiment 1 FIG. 1 is a schematic view of a system for explaining the present invention, and FIG. 2 shows the inside of a heat exchanger for cooling a combustion gas when viewed from the front.
【００１０】この炭酸ガス濃縮装置２は給湯器１と、燃
焼ガス３中の炭酸ガスを濃縮する手段とによって構成さ
れている。炭酸ガスの供給は、給湯器１で燃焼が行なわ
れ、炭酸ガスを含む燃焼ガス３がブロアー４によって炭
酸ガス濃縮装置２へ供給される。そして、吸着剤１０を
利用した温度スイング方式の炭酸ガス濃縮装置２におい
て、燃焼ガス３の冷却・除湿を水蒸気吸着塔７の前段で
熱交換器５により行い、水蒸気吸着塔７で完全に近い除
湿を行ない、そして炭酸ガス吸着塔８で炭酸ガスを一定
時間吸着し、その後吸着塔ヒーター９による加熱で充分
に濃い炭酸ガス１１を生成離脱させ、供給出来る。The carbon dioxide gas concentrating device 2 comprises a water heater 1 and means for concentrating carbon dioxide gas in the combustion gas 3. Carbon dioxide gas is burned in the water heater 1, and the combustion gas 3 containing carbon dioxide gas is supplied to the carbon dioxide gas concentrator 2 by the blower 4. Then, in the temperature swing type carbon dioxide gas concentrating device 2 using the adsorbent 10, the combustion gas 3 is cooled and dehumidified by the heat exchanger 5 before the steam adsorption tower 7, and the steam adsorption tower 7 is almost completely dehumidified. Then, the carbon dioxide adsorption tower 8 adsorbs the carbon dioxide gas for a certain period of time, and then the adsorption tower heater 9 heats it to generate and desorb sufficiently rich carbon dioxide gas 11 for supply.
【００１１】続いて、この発明の特徴である熱交換器５
まわりの構成について詳しく説明する。Next, the heat exchanger 5 which is a feature of the present invention.
The surrounding structure will be described in detail.
【００１２】熱交換器５は、燃焼ガス３を冷却するため
に、フィン・アンド・チューブ熱交換器を箱体内に収
め、炭酸ガス濃縮装置２の燃焼ガス流路の一部として組
み込み、燃焼ガス３を外気と接触させない構造とした。
そして、箱体の上部に燃焼ガス流入口２２を設け、下部
に燃焼ガス流出口１５を設け、熱交換器５のプレートフ
ィン１３の長辺方向を箱体の上下方向を一致させ、燃焼
ガス３をプレートフィン１３と平行に流すことにより、
燃焼ガス３の流量面積を小さくできるために、全てのプ
レートフィン１３に荷均等に燃焼ガス３を接触させるこ
とができた。これによりヘッダー１２を小型にすること
に成功した。また、冷却水流入口２３を熱交換器５の下
部に設置し、冷却水流出口２４を熱交換器５の上部に設
置することにより、燃焼ガス３と冷却水６を対向流方式
で熱交換できるために、熱交換率を向上させることがで
き、水蒸気の結露を促進できた。In order to cool the combustion gas 3, the heat exchanger 5 contains a fin-and-tube heat exchanger in the box body and incorporates it as a part of the combustion gas flow path of the carbon dioxide gas concentrator 2. 3 has a structure that does not come into contact with the outside air.
Then, the combustion gas inlet 22 is provided in the upper part of the box body, the combustion gas outlet 15 is provided in the lower part, and the long side direction of the plate fins 13 of the heat exchanger 5 is aligned with the vertical direction of the box body, and the combustion gas 3 By flowing in parallel with the plate fin 13,
Since the flow area of the combustion gas 3 can be reduced, the combustion gas 3 can be uniformly contacted with all the plate fins 13. This succeeded in making the header 12 small. Further, since the cooling water inlet 23 is installed in the lower part of the heat exchanger 5 and the cooling water outlet 24 is installed in the upper part of the heat exchanger 5, the combustion gas 3 and the cooling water 6 can exchange heat by the counterflow method. In addition, the heat exchange rate could be improved and the condensation of water vapor could be promoted.
【００１３】次に、熱交換器５の内部のプレートフィン
群１７に結露した結露水２０が自重もしくはガス流速に
よって落下したとき、箱体底板１８にある燃焼ガス流出
口１５より結露水２０が漏出しないように、箱体内下部
に結露水を溜める結露水溜め２６を設け、燃焼ガス流出
口端部２５を箱体底板１８より突出させ、熱交換器５の
プレートフィン群１７と燃焼ガス流出口１５の突出部２
８の間に、傾斜をもたせた板体１４を設置することによ
り、熱交換器５のプレートフィン群１７より落下し、燃
焼ガス流出口１５より漏出しようとする結露水２０を板
体１４により、結露水溜め２６に落し込む。さらに、結
露水溜め２６の結露水２０を燃焼ガス３の流路外に排出
するための結露水２０の結露水排水口１６を設けた構造
とすることで、箱体底板の部分に溜る結露水２０を速や
かに排出することができた。このとき結露水溜め２６に
多少結露水が溜っても、燃焼ガス流出口端部２５を箱体
底板より突出させているために燃焼ガス流出口１５より
結露水２０が漏出することはなかった。Next, when the condensed water 20 condensed on the plate fin group 17 inside the heat exchanger 5 falls due to its own weight or the gas flow velocity, the condensed water 20 leaks from the combustion gas outlet 15 on the bottom plate 18 of the box body. In order not to do so, a condensed water reservoir 26 for collecting condensed water is provided in the lower part of the box body, the combustion gas outlet end 25 is projected from the box bottom plate 18, and the plate fin group 17 of the heat exchanger 5 and the combustion gas outlet 15 are provided. Protruding part 2
By installing the plate body 14 having an inclination between 8 and 8, the condensed water 20 that falls from the plate fin group 17 of the heat exchanger 5 and tries to leak from the combustion gas outlet 15 is provided by the plate body 14. Drop into the condensed water reservoir 26. Further, the dew condensation water drainage port 16 of the dew condensation water 20 for discharging the dew condensation water 20 from the dew condensation water reservoir 26 to the outside of the flow path of the combustion gas 3 is provided, so that the dew condensation water accumulated on the bottom plate of the box body is formed. 20 could be discharged quickly. At this time, even if some dew condensation water was accumulated in the dew condensation water reservoir 26, the dew condensation water 20 did not leak from the combustion gas outflow port 15 because the combustion gas outflow end portion 25 is projected from the box bottom plate.
【００１４】この様な構造をとることにより、熱交換器
５後の水蒸気吸着塔８へ流入する水蒸気量の低減を図る
ことができた。By adopting such a structure, the amount of water vapor flowing into the water vapor adsorption tower 8 after the heat exchanger 5 can be reduced.
【００１５】一定の水蒸気を吸着した後吸着剤は吸着塔
ヒーター９により加熱して水蒸気を脱離する。After adsorbing a certain amount of water vapor, the adsorbent is heated by the adsorption tower heater 9 to desorb the water vapor.
【００１６】水蒸気吸着塔８では吸着材１０で残りの水
蒸気を吸着除去した後濃縮炭酸ガス１１のみが放出され
る。In the water vapor adsorption tower 8, only the concentrated carbon dioxide gas 11 is released after the remaining water vapor is adsorbed and removed by the adsorbent 10.
【００１７】実施例２ 実施例１のシステムにおいて、図３に示すように、箱体
底板１８の部分を、結露水排水口１６に向かって下り勾
配にする事により、速やかに結露水２０を結露水排水口
１６に落し込むことができた。さらに、傾斜をもたせた
板体１４を箱体底板１８に配設された結露水排水口１６
に向かって下り勾配に配設させることにより、速やかに
箱体底板１８に落し込み、結露水排水口１６に落し込む
ことができた。Embodiment 2 In the system of Embodiment 1, as shown in FIG. 3, by making the bottom part of the box body 18 slope down toward the dew condensation water discharge port 16, the dew condensation water 20 is quickly condensed. It could be dropped into the water drainage port 16. Furthermore, the plate body 14 having an inclination is provided with the dew condensation water drain port 16 provided on the box bottom plate 18.
By arranging it in a downward slope toward, it was possible to quickly drop it into the box bottom plate 18 and into the condensed water drainage port 16.
【００１８】実施例３ 図４は、結露水排水口１６を燃焼ガス流出口１５と同じ
側に取付け、箱体底板１８の部分に、結露水排水口１６
に向かって下り勾配を持たせたものを示す。これによ
り、燃焼ガス３と結露水２０の流れが同じ方向となるた
めに、実施例２よりさらに結露水２０を速やかに結露水
排水口１６に落し込む事が出来、再加湿されることをさ
らに低減させることができた。Embodiment 3 In FIG. 4, the dew condensation water drain port 16 is attached to the same side as the combustion gas outflow port 15, and the dew condensation water drain port 16 is attached to the bottom plate 18 of the box body.
Shown with a downward slope toward. Thereby, the flow of the combustion gas 3 and the flow of the dew condensation water 20 are in the same direction, so that the dew condensation water 20 can be dropped into the dew condensation water discharge port 16 more quickly than in the second embodiment, and the re-humidification is further prevented. Could be reduced.
【００１９】実施例４ 図５、図６の実施例では、箱体の内部に設置されている
板体１４を、図に示すようにＬ型の板体１４の垂直方向
の面が箱体壁面１９と平行になるように設置する。これ
は、上記例のような燃焼ガス流出口１５をおおう一枚板
だけの板体１４では、箱体壁面１９と板体１４の隙間に
燃焼ガス３が流れ込んで渦を巻いてしまい、それによっ
て箱体壁面１９に沿いながら落ちる結露水２０を舞い上
がらせてしまうからである。よって、燃焼ガス流出口１
５付近の箱体壁面１９に沿いながら落ちる結露水２０
を、箱体壁面１９と板体１４の箱体壁面１９と平行な面
により挟み込む。これにより箱体壁面１９の面に沿いな
がら落ちる結露水２０の舞い上がりがなくなり、燃焼ガ
ス流出口１５より水滴の吐出がなくなった。Embodiment 4 In the embodiment shown in FIGS. 5 and 6, the plate 14 installed inside the box has a vertical wall surface of the L-shaped plate 14 as shown in the figure. Install so that it is parallel to 19. This is because in the plate body 14 having only one plate covering the combustion gas outlet 15 as in the above example, the combustion gas 3 flows into the gap between the box body wall surface 19 and the plate body 14 and swirls, which causes This is because the condensed water 20 falling along the box wall surface 19 will rise. Therefore, the combustion gas outlet 1
Condensation water 20 falling along the wall 19 of the box near 5
Is sandwiched between the box body wall surface 19 and the plane of the plate body 14 parallel to the box body wall surface 19. As a result, the dew condensation water 20 falling along the surface of the box wall surface 19 was prevented from rising, and no water droplet was discharged from the combustion gas outlet 15.
【００２０】実施例５ 図７は、箱体の内部に設置されている板体１４を示すよ
うな半球状の形状にし、燃焼ガス流出口端部２５を箱体
底板１８より突出させる。板体の直径をプレートフィン
の短辺と同じ長さとし、板体１４は上部を凸として、半
球面状板体端部２７を、突出部２８の燃焼ガス流出口端
部２５より、低い位置に取り付ける。これにより、燃焼
ガス流出口１５付近の箱体壁面１９に沿いながら落ちる
結露水２０が、燃焼ガス３の流速によって舞い上がって
も、結露水２０が燃焼ガス流出口１５に漏出しない。Embodiment 5 In FIG. 7, the plate 14 installed inside the box is formed in a hemispherical shape, and the combustion gas outlet end 25 is projected from the box bottom plate 18. The diameter of the plate body is set to the same length as the short side of the plate fin, the plate body 14 has a convex upper portion, and the hemispherical plate body end portion 27 is located at a position lower than the combustion gas outlet end portion 25 of the protruding portion 28. Install. As a result, even if the condensed water 20 that falls along the wall surface 19 of the box near the combustion gas outlet 15 rises up due to the flow velocity of the combustion gas 3, the condensed water 20 does not leak to the combustion gas outlet 15.
【００２１】[0021]
【発明の効果】請求項１記載の発明によれば、箱体内に
収めた熱交換器のプレートフィンの長辺方向と平行に燃
焼ガスを流すことにより、燃焼ガスの流路面積が小さく
でき、全てのプレートフィンに均等に燃焼ガスを接触さ
せることができた。また、冷却水を燃焼ガスの流れ方向
と逆に箱体の下部より流入させ上部より流出させたの
で、燃焼ガスと冷却水の熱交換方式が対向式となり、直
交式のものより、熱交換効率を向上させることができ
た。したがって、熱交換器を小型にすることができ、水
蒸気の結露を促進させることができた。請求項２記載の
発明によれば、燃焼ガス流出口端部を箱体底板より突出
させ、突出部の上部に燃焼ガス流出口の外径以上の長さ
で、プレートフィンの短辺と同じ幅をもつ形状の板体
を、フィン・アンド・チューブ熱交換器と燃焼ガス流出
口の中間に、箱体底板１８と平行もしくは勾配を付けて
設置し、結露水を燃焼ガスの流路外に排出する結露水排
水口を設け、さらに、請求項３に記載された発明によれ
ば、箱体底板の部分に、燃焼ガス流出口方向に下り勾配
を持たせる事により、炭酸ガス中の水蒸気量を低減でき
る。According to the first aspect of the present invention, the flow area of the combustion gas can be reduced by flowing the combustion gas parallel to the long side direction of the plate fins of the heat exchanger housed in the box. The combustion gas could be contacted evenly on all plate fins. In addition, since the cooling water flows in from the lower part of the box and flows out from the upper part in the direction opposite to the flow direction of the combustion gas, the heat exchange method of the combustion gas and the cooling water is the opposite type, and the heat exchange efficiency is better than that of the orthogonal type. Was able to improve. Therefore, the heat exchanger can be downsized and the condensation of water vapor can be promoted. According to the second aspect of the present invention, the combustion gas outlet end is projected from the box bottom plate, and the length above the outer diameter of the combustion gas outlet is the same as the short side of the plate fin above the protruding portion. The plate with the shape of the box is installed in the middle of the fin-and-tube heat exchanger and the combustion gas outlet in parallel with the box bottom plate 18 or with a gradient, and the condensed water is discharged out of the flow path of the combustion gas. According to the invention described in claim 3, by further providing a dew condensation water drainage port, the box bottom plate portion is provided with a downward slope in the combustion gas outlet direction so that the amount of water vapor in the carbon dioxide gas is reduced. It can be reduced.
【図 １】本発明の一実施例のシステムを表わす概略
図。FIG. 1 is a schematic diagram showing a system according to an embodiment of the present invention.
【図 ２】同上の要部断面図。FIG. 2 is a sectional view of a main part of the same.
【図 ３】本発明の要部の異なる実施例を示す断面図。FIG. 3 is a cross-sectional view showing an embodiment in which the main part of the present invention is different.
【図 ４】本発明の要部の他の異なる実施例を示す断面
図。FIG. 4 is a sectional view showing another different embodiment of the main part of the present invention.
【図 ５】本発明の要部の更に異なる実施例を示す断面
図。FIG. 5 is a sectional view showing still another embodiment of the main part of the present invention.
【図 ６】同上の縦断面図。FIG. 6 is a vertical sectional view of the above.
【図 ７】本発明の要部の更に異なる実施例を示す断面
図。FIG. 7 is a sectional view showing still another embodiment of the main part of the present invention.
１ 給湯器 ２ 炭酸ガス濃縮装置 ３ 燃焼ガス ４ ブロアー ５ 熱交換器 ６ 冷却水 ７ 水蒸気吸着塔 ８ 炭酸ガス吸着塔 ９ 吸着塔ヒーター １０ 吸着材 １１ 濃縮炭酸ガス １２ ヘッダー １３ プレートフィン １４ 板体 １５ 燃焼ガス流出口 １６ 結露水排水口 １７ プレートフィン群 １８ 箱体底板 １９ 箱体壁面 ２０ 結露水 ２１ 冷却水パイプ ２２ 燃焼ガス流入口 ２３ 冷却水流入口 ２４ 冷却水流出口 ２５ 燃焼ガス流出口端部 ２６ 結露水溜め ２７ 半球面状板体端部 ２８ 突出部 1 Water Heater 2 Carbon Dioxide Concentrator 3 Combustion Gas 4 Blower 5 Heat Exchanger 6 Cooling Water 7 Steam Adsorption Tower 8 Carbon Dioxide Adsorption Tower 9 Adsorption Tower Heater 10 Adsorbent 11 Concentrated Carbon Dioxide 12 Header 13 Plate Fin 14 Plate 15 Combustion Gas outlet 16 Condensate drainage 17 Plate fin group 18 Box bottom plate 19 Box wall 20 Condensation water 21 Cooling water pipe 22 Combustion gas inlet 23 Cooling water inlet 24 Cooling water outlet 25 Combustion gas outlet end 26 Condensation water Reservoir 27 Hemispherical plate body end 28 Projection
─────────────────────────────────────────────────────
─────────────────────────────────────────────────── ───
【手続補正書】[Procedure amendment]
【提出日】平成５年３月８日[Submission date] March 8, 1993
【手続補正１】[Procedure Amendment 1]
【補正対象書類名】明細書[Document name to be amended] Statement
【補正対象項目名】００１４[Correction target item name] 0014
【補正方法】変更[Correction method] Change
【補正内容】[Correction content]
【００１４】この様な構造をとることにより、熱交換器
５後の水蒸気吸着塔７へ流入する水蒸気量の低減を図る
ことができた。By adopting such a structure, the amount of water vapor flowing into the water vapor adsorption tower 7 after the heat exchanger 5 can be reduced.
【手続補正２】[Procedure Amendment 2]
【補正対象書類名】明細書[Document name to be amended] Statement
【補正対象項目名】００１６[Correction target item name] 0016
【補正方法】変更[Correction method] Change
【補正内容】[Correction content]
【００１６】水蒸気吸着塔７では吸着材１０で残りの水
蒸気を吸着除去した後燃焼ガス３が放出される。In the water vapor adsorption tower 7 , the combustion gas 3 is released after the remaining water vapor is adsorbed and removed by the adsorbent 10.
フロントページの続き (72)発明者 真継 伸 大阪府門真市大字門真1048番地松下電工株 式会社内 (72)発明者 中岡 敬善 大阪府門真市大字門真1048番地松下電工株 式会社内 (72)発明者 伊藤 之一 大阪府門真市大字門真1048番地松下電工株 式会社内Continuation of the front page (72) Shin Inoue, Shinobu 1048, Kadoma, Kadoma, Osaka Prefecture, Matsushita Electric Works Co., Ltd. Inventor Noriichi Ito 1048, Kadoma, Kadoma, Osaka Prefecture Matsushita Electric Works Co., Ltd.
Claims (3)
得、燃焼ガス中の炭酸ガスを吸着剤を用い、温度差を利
用して濃縮する炭酸ガス濃縮装置２において、燃焼ガス
を冷却するためのフィン・アンド・チューブ型の熱交換
器５を箱体内に収めて燃焼ガス３の流路に組み込み、こ
の箱体の上部に燃焼ガス流入口２２を設け、下部に燃焼
ガス流出口１５を設け、フィン・アンド・チューブ型の
熱交換器５のプレートフィン１３の長辺方向を箱体の上
下方向とし、この箱体内下部に結露水溜め２６及び、結
露水を箱体の外部に排水する結露水排水口１６を設けた
ことを特徴とする炭酸ガス濃縮装置。1. A carbon dioxide concentrating device 2 for obtaining a combustion gas from a fuel containing hydrocarbons and concentrating carbon dioxide gas in the combustion gas using an adsorbent and utilizing a temperature difference, for cooling the combustion gas. The fin-and-tube type heat exchanger 5 is housed in the box body and incorporated in the flow path of the combustion gas 3, the combustion gas inlet 22 is provided in the upper part of the box body, and the combustion gas outlet 15 is provided in the lower part. The long side direction of the plate fins 13 of the fin-and-tube type heat exchanger 5 is the vertical direction of the box body, and the dew condensation water reservoir 26 is provided at the lower part of the box body, and the dew condensation water is discharged to the outside of the box body. A carbon dioxide gas concentrating device having a drainage port 16.
より突出させ、突出部の上部にプレートフィン１３の短
辺と同じ幅をもち、燃焼ガス流出口１５の外径以上の長
さをもつ板体１４を、フィン・アンド・チューブ熱交換
器と燃焼ガス流出口の中間に、箱体底板１８と平行もし
くは勾配を付けて配設したことを特徴とする請求項１記
載の炭酸ガス濃縮装置。2. The combustion gas outlet end 25 is attached to the box bottom plate 18.
The plate 14 having a width equal to the short side of the plate fin 13 at the upper portion of the protruding portion and having a length equal to or larger than the outer diameter of the combustion gas outlet 15 is burned with the fin-and-tube heat exchanger. The carbon dioxide gas concentrating device according to claim 1, wherein the carbon dioxide gas concentrating device is arranged in the middle of the gas outlet in parallel with the bottom plate 18 of the box or with a slope.
特徴とする請求項１記載の炭酸ガス濃縮装置。3. The carbon dioxide gas concentrating device according to claim 1, wherein the box bottom plate 18 has a gradient.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4344061A JPH06182134A (en) | 1992-12-24 | 1992-12-24 | Carbon dioxide concentrator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4344061A JPH06182134A (en) | 1992-12-24 | 1992-12-24 | Carbon dioxide concentrator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH06182134A true JPH06182134A (en) | 1994-07-05 |
Family
ID=18366355
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP4344061A Pending JPH06182134A (en) | 1992-12-24 | 1992-12-24 | Carbon dioxide concentrator |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH06182134A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103663452A (en) * | 2013-12-11 | 2014-03-26 | 江西哈特斯金属材料有限公司 | Method for recovering tungsten carbide from waste hard alloy |
| JP2015148420A (en) * | 2014-02-10 | 2015-08-20 | パナソニックＩｐマネジメント株式会社 | range hood |
-
1992
- 1992-12-24 JP JP4344061A patent/JPH06182134A/en active Pending
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103663452A (en) * | 2013-12-11 | 2014-03-26 | 江西哈特斯金属材料有限公司 | Method for recovering tungsten carbide from waste hard alloy |
| JP2015148420A (en) * | 2014-02-10 | 2015-08-20 | パナソニックＩｐマネジメント株式会社 | range hood |
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