JP3995436B2 - Air washer - Google Patents

Air washer Download PDF

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Publication number
JP3995436B2
JP3995436B2 JP2001238678A JP2001238678A JP3995436B2 JP 3995436 B2 JP3995436 B2 JP 3995436B2 JP 2001238678 A JP2001238678 A JP 2001238678A JP 2001238678 A JP2001238678 A JP 2001238678A JP 3995436 B2 JP3995436 B2 JP 3995436B2
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JP
Japan
Prior art keywords
water
circulating water
spray
air
bank
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JP2001238678A
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Japanese (ja)
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JP2003050091A (en
Inventor
正明 篠原
正 鈴木
俊介 鈴木
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Kubota Corp
Kubota Air Conditioner Ltd
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Kubota Corp
Kubota Air Conditioner Ltd
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Description

【0001】
【発明の属する技術分野】
本発明はエアワッシャに関し、冷水噴霧エアワッシャ等において空気中の塵埃や有害ガスを除去するとともに空気の冷却を行う技術に係るものである。
【0002】
【従来の技術】
従来の冷水噴霧エアワッシャとしては、例えば図7に示すものがある。図7において、エアワッシャは矩形の流路断面を有する本体ケーシング11の内部に所定長さの水噴霧室12を有しており、水噴霧室12はその一端に形成した空気入口13aにおいてダクト(図示せず)に接続しており、このダクトから流入する空気流が水噴霧室12の流路を通って他端に形成した空気出口13bから流出する。
【0003】
水噴霧室12には、空気入口13aの側に第1ワッシャメディア14を配置し、空気出口13bの側に第2ワッシャメディア15を配置しており、各ワッシャメディア14、15は、本体ケーシング11の流路断面とほぼ等しい形状を有している。
【0004】
水噴霧室12の内部には空気流の流れ方向に沿って多段にバンク16を設けており、各バンク16には空気流の上流方向に向けて噴霧水を噴出する複数の噴霧ノズル17を設けている。水噴霧室12の下部には流下する噴霧水を受け止める貯水槽18が設けてあり、貯水槽18に滞留する循環水を各バンク16に循環供給する循環水供給系19が貯水槽18の下部に連通している。
【0005】
循環水供給系19には循環ポンプ20と熱交換器21を設けており、熱交換器21に供給する所定温度の一次冷水によって循環水を所定温度に冷却する。本体ケーシング11の上流側には補給水供給系22が開口し、貯水槽18にはドレン系23およびオーバーフロー系24を接続している。
【0006】
【発明が解決しようとする課題】
上記した従来の構成では、各バンク16の噴霧ノズル17から噴霧する循環水の全量が循環水供給系19を通って熱交換器21に流れ、循環水の全量が熱交換器21において一次冷水との間で熱交換している。
【0007】
エアワッシャにて空気を通常必要な温度にまで冷却するためには、循環水量が空気重量以上(L/G>1.0)に必要であり、熱交換器21から各バンク16へ向かう循環水の送り出し温度と各バンク16から熱交換器21へ戻る循環水の帰り温度との温度差が小さく、循環水の帰り温度が高くならないので、熱交換器21から冷凍機へ戻る一次冷水の出口温度が低くなり、熱交換器21における一次冷水の入口温度と出口温度との間に所定温度差を確保するためには一次冷水の入口温度を低くする必要があり、冷凍機の効率が低下する。循環水量が多く、また循環水の帰り温度と一次冷水の出口温度との温度差が大きくならないので、伝熱面積を広げるために熱交換器21のサイズを大きくする必要がある。
【0008】
本発明は上記した課題を解決するものであり、熱交換器への循環水の帰り温度を高めて循環水の冷却温度差を大きくし、熱交換器における一次冷水の出口温度の低下を防止するエアワッシャを提供することを目的とする。
【0009】
【課題を解決するための手段】
上記した課題を解決するために、本発明のエアワッシャは、空気入口から空気出口に向かって空気流が生じる水噴霧室中に空気流の流れ方向に沿って多段にバンクを設け、各バンクに空気流中に噴霧水を噴出する複数の噴霧ノズルを設け、各バンクの各噴霧ノズルから噴霧された噴霧水が流下し、流下した噴霧水を混合して貯留する貯水槽を設け、この貯水槽と空気流の上流側に配置した前段側のバンクとの間に非冷却循環水系を設け、前記貯水槽と空気流の下流側に配置した後段側のバンクとの間に熱交換器を有する冷却循環水系を設けたものである。
【0010】
上記した構成により、貯水槽に滞留する循環水は非冷却循環水系と冷却循環水系とに分流し、非冷却循環水系を流れる循環水は冷却されずに前段側のバンクに循環して噴霧ノズルから空気流中に噴霧され、冷却循環水系を流れる循環水は熱交換器で冷却されて後に後段側のバンクに循環して噴霧ノズルから空気流中に噴霧される。
【0011】
したがって、後段のバンクで噴霧される冷却循環水は、空気を冷却し昇温されて貯水槽に落ち、前段のバンクで噴霧される非冷却循環水はワッシャ入口側の空気を冷却することで、循環水温度以上に昇温されて貯水槽に落ちる。この双方の循環水が貯水槽で混合されることによって、熱交換器入口に入る冷却循環水系の戻り温度は高く維持される。
【0012】
このように、循環水を分流し、分流した一部の循環水を冷却することで、従来のように循環水の全量を冷却する場合に比べて、循環水量および熱負荷の同条件下で熱交換器における循環水の帰り温度を高く維持することができ、熱交換器において一次冷水の入口温度と出口温度との間に確保する所定温度差を従来より高い温度域において設定することができ、冷凍機の運転効率を低下させることがなく、大巾に熱交換器をサイズダウンできる。
【0013】
【発明の実施の形態】
以下、本発明の実施の形態を図面に基づいて説明する。先に図7で示したものと同様の作用を行う部材については同一番号を付して説明を省略する。
【0014】
実施例1
図1に示すように、水噴霧室12の内部には複数のバンク16a、16b、16cを空気入口13aから空気出口13bに向かって生じる空気流の流れ方向に沿って上流側から下流側へ順次に多段に設けており、各バンク16a、16b、16cには空気流の上流側へ向けて噴霧水を噴出する複数の噴霧ノズル17を設けている。
【0015】
噴霧水が流下する貯水槽18と各バンク16a、16b、16cとを連通する循環水供給系19は途中で非冷却循環水系19aと冷却循環水系19bとに分岐しており、非冷却循環水系19aは空気流の上流側に配置した前段側のバンク16a、16bに連通し、冷却循環水系19bは熱交換器21を経て空気流の下流側に配置した後段側のバンク16cに連通している。
【0016】
以下、上記した構成における作用を説明する。循環ポンプ20の駆動により貯水槽18に滞留する循環水は循環水供給系19を通って非冷却循環水系19aと冷却循環水系19bとに分流する。
【0017】
非冷却循環水系19aを流れる循環水は冷却されずに前段側のバンク16a、16bに循環して噴霧ノズル17から空気流中に噴霧され、冷却循環水系19bを流れる循環水は熱交換器21で冷却されて後に後段側のバンク16cに循環して噴霧ノズル17から空気流中に噴霧される。
【0018】
噴霧水は空気流と接触して空気中の塵埃や有害ガスを除去するとともに空気を冷却する。このとき、前段側のバンク16a、16bから噴霧される噴霧水(14℃)と後段側のバンク16cから噴霧される噴霧水(8.5℃)との間には温度差が存在する。
【0019】
図2は水噴霧室12を流れる空気の変化を示す空気線図であり、図3は空気と噴霧水の温度変化を示すグラフである。従来のように循環水の全量を冷却した噴霧水(9.5℃)を噴霧する場合と循環水量および熱負荷を同条件として、前段側のバンク16a、16bから冷却しない噴霧水(14℃)を噴霧し、後段側のバンク16cから冷却した噴霧水(8.5℃)を噴霧することで同じ冷却効果を得ることができる。
【0020】
各バンク16a、16b、16cからの噴霧水は空気流とともに流れてワッシャメディア14、15に衝突し、ワッシャメディア14、15を伝って貯水槽18へ流下し、貯水槽18で混合される。すなわち、非冷却循環水系19aを通った噴霧水は、16℃で貯水槽18に流下し、冷却循環水系19bを通って熱交換器21で冷却された噴霧水は12℃で貯水槽18に流下し、両者の混合水は14℃となり従来の12℃以上に温度が上昇して熱交換器21へ戻る。
【0021】
よって、熱交換器21において一次冷水の入口温度(7℃)を従来(6℃)に比べて高く維持し、入口温度(7℃)と出口温度(12℃)との間に確保する所定温度差を従来より高い温度域において設定することができる。
【0022】
また、熱交換器21を通る循環水量はL/G=0.7相当分で良く、従来(L/G=1.6相当分)の44%でよく、熱交換器21のサイズダウンができる。図4に示すように、循環ポンプ20は非冷却循環水系19aおよび冷却循環水系19bのそれぞれに設けることも可能である。
【0023】
図5に示すように、バンク16a、16cは水噴霧室12に二段に設けることも可能である。
図6に示すように、貯水槽18は本体ケーシング11とは別途に設けることも可能である。
【0024】
【発明の効果】
以上述べたように本発明によれば、循環水を分流し、分流した一部の循環水を冷却することで、従来のように循環水の全量を冷却する場合に比べて、循環水量および熱負荷の同条件下で熱交換器における循環水の帰り温度を高く維持することができ、熱交換器において一次冷水の入口温度と出口温度との間に確保する所定温度差を従来より高い温度域において設定することができ、冷凍機の運転効率を低下させることがなく、大巾に熱交換器をサイズダウンできる。
【図面の簡単な説明】
【図1】本発明の実施の形態におけるエアワッシャの断面図である。
【図2】同実施の形態における空気線図である。
【図3】同実施の形態における空気と噴霧水の温度変化を示すグラフである。
【図4】本発明の他の実施の形態における要部を示す配管図である。
【図5】本発明のさらに他の実施の形態におけるエアワッシャの断面図である。
【図6】本発明のさらに他の実施の形態におけるエアワッシャの断面図である。
【図7】従来のエアワッシャの断面図である。
【符号の説明】
11 本体ケーシング
12 水噴霧室
13a 空気入口
13b 空気出口
14,15 ワッシャメディア
16a、16b、16c バンク
17 噴霧ノズル
18 貯水槽
19 循環水供給系
19a 非冷却循環水系
19b 冷却循環水系
20 循環ポンプ
21 熱交換器
22 補給水供給系
23 ドレン系
24 オーバーフロー系
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to an air washer and relates to a technique for removing dust and harmful gases in the air and cooling the air in a cold water spray air washer or the like.
[0002]
[Prior art]
An example of a conventional cold water spray air washer is shown in FIG. In FIG. 7, the air washer has a water spray chamber 12 of a predetermined length inside a main body casing 11 having a rectangular channel cross section, and the water spray chamber 12 has a duct ( The airflow flowing in from this duct flows out from the air outlet 13b formed at the other end through the flow path of the water spray chamber 12.
[0003]
In the water spray chamber 12, a first washer medium 14 is disposed on the air inlet 13a side, and a second washer medium 15 is disposed on the air outlet 13b side. It has a shape substantially equal to the cross section of the flow path.
[0004]
Inside the water spray chamber 12, banks 16 are provided in multiple stages along the air flow direction, and each bank 16 is provided with a plurality of spray nozzles 17 that eject spray water toward the upstream direction of the air flow. ing. A water storage tank 18 for receiving the spray water flowing down is provided at the lower part of the water spray chamber 12, and a circulating water supply system 19 for circulating and supplying the circulating water staying in the water storage tank 18 to each bank 16 is provided at the lower part of the water storage tank 18. Communicate.
[0005]
The circulating water supply system 19 is provided with a circulation pump 20 and a heat exchanger 21, and the circulating water is cooled to a predetermined temperature by primary cold water having a predetermined temperature supplied to the heat exchanger 21. A makeup water supply system 22 opens on the upstream side of the main casing 11, and a drain system 23 and an overflow system 24 are connected to the water storage tank 18.
[0006]
[Problems to be solved by the invention]
In the conventional configuration described above, the total amount of circulating water sprayed from the spray nozzles 17 of each bank 16 flows to the heat exchanger 21 through the circulating water supply system 19, and the total amount of circulating water is converted into primary cold water in the heat exchanger 21. Heat exchange between.
[0007]
In order to cool the air to a normally required temperature with an air washer, the amount of circulating water is required to be greater than the weight of air (L / G> 1.0), and the circulating water from the heat exchanger 21 toward each bank 16 is required. The temperature difference between the feed temperature of the circulating water and the return temperature of the circulating water returning from each bank 16 to the heat exchanger 21 is small and the return temperature of the circulating water does not increase, so the outlet temperature of the primary cold water returning from the heat exchanger 21 to the refrigerator In order to secure a predetermined temperature difference between the inlet temperature and the outlet temperature of the primary chilled water in the heat exchanger 21, it is necessary to lower the inlet temperature of the primary chilled water, which reduces the efficiency of the refrigerator. Since the amount of circulating water is large and the temperature difference between the return temperature of the circulating water and the outlet temperature of the primary cold water does not increase, it is necessary to increase the size of the heat exchanger 21 in order to widen the heat transfer area.
[0008]
This invention solves the above-mentioned subject, raises the return temperature of the circulating water to a heat exchanger, enlarges the cooling temperature difference of circulating water, and prevents the fall of the outlet temperature of the primary cold water in a heat exchanger. The purpose is to provide an air washer.
[0009]
[Means for Solving the Problems]
In order to solve the above-described problems, the air washer of the present invention is provided with banks in multiple stages along the flow direction of the air flow in a water spray chamber in which an air flow is generated from the air inlet toward the air outlet. Provided with a plurality of spray nozzles for spraying spray water in the air flow, spray water sprayed from each spray nozzle of each bank flows, and a reservoir for mixing and storing the spray water that has flowed down is provided. cooling and uncooled circulating water system is provided between the front side of the bank arranged on the upstream side of the air flow, having a heat exchanger between the rear stage side of the bank arranged on the downstream side of the water tank and the air flow A circulating water system is provided.
[0010]
With the configuration described above, the circulating water staying in the water storage tank is divided into an uncooled circulating water system and a cooled circulating water system, and the circulating water flowing through the uncooled circulating water system is circulated to the bank on the preceding stage without being cooled and is supplied from the spray nozzle. The circulating water sprayed in the air stream and flowing through the cooling circulating water system is cooled by the heat exchanger and then circulated to the bank on the rear stage side and sprayed from the spray nozzle into the air stream.
[0011]
Therefore, the cooling circulating water sprayed in the latter bank cools the air and is heated to fall into the water storage tank, and the non-cooling circulating water sprayed in the preceding bank cools the air on the washer inlet side, The temperature rises above the circulating water temperature and falls to the water tank. By mixing both the circulating water in the water storage tank, the return temperature of the cooling circulating water system entering the heat exchanger inlet is kept high.
[0012]
In this way, the circulating water is diverted, and a part of the diverted circulating water is cooled, so that compared with the conventional case where the entire amount of circulating water is cooled, heat is generated under the same conditions of the circulating water amount and the heat load. The return temperature of the circulating water in the exchanger can be kept high, and a predetermined temperature difference that is ensured between the inlet temperature and the outlet temperature of the primary cold water in the heat exchanger can be set in a higher temperature range than before. The heat exchanger can be greatly downsized without reducing the operating efficiency of the refrigerator.
[0013]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, embodiments of the present invention will be described with reference to the drawings. Members that perform the same operations as those shown in FIG. 7 are assigned the same reference numerals, and descriptions thereof are omitted.
[0014]
Example 1
As shown in FIG. 1, a plurality of banks 16a, 16b, and 16c are provided in the water spray chamber 12 in order from the upstream side to the downstream side along the flow direction of the air flow generated from the air inlet 13a to the air outlet 13b. In each of the banks 16a, 16b, and 16c, a plurality of spray nozzles 17 for spraying spray water toward the upstream side of the air flow are provided.
[0015]
A circulating water supply system 19 that communicates between the water storage tank 18 through which the spray water flows and the banks 16a, 16b, and 16c branches on the way into an uncooled circulating water system 19a and a cooled circulating water system 19b, and an uncooled circulating water system 19a. Is communicated with the upstream banks 16a and 16b disposed upstream of the air flow, and the cooling circulation water system 19b is communicated with the downstream bank 16c disposed downstream of the air flow via the heat exchanger 21.
[0016]
Hereinafter, the operation of the above-described configuration will be described. The circulating water staying in the water storage tank 18 by the driving of the circulation pump 20 is divided into the uncooled circulating water system 19a and the cooled circulating water system 19b through the circulating water supply system 19.
[0017]
The circulating water flowing through the non-cooled circulating water system 19a is not cooled and circulated to the banks 16a and 16b on the preceding stage and sprayed into the air stream from the spray nozzle 17, and the circulating water flowing through the cooling circulating water system 19b is passed through the heat exchanger 21. After being cooled, it is circulated to the bank 16c on the rear stage side and sprayed from the spray nozzle 17 into the air flow.
[0018]
The spray water contacts the air flow to remove dust and harmful gases in the air and cool the air. At this time, there is a temperature difference between the spray water (14 ° C.) sprayed from the banks 16a and 16b on the front side and the spray water (8.5 ° C.) sprayed from the bank 16c on the back side.
[0019]
FIG. 2 is an air diagram showing changes in air flowing through the water spray chamber 12, and FIG. 3 is a graph showing changes in temperature of air and spray water. Spray water (9.5 ° C.) in which the entire amount of circulating water is cooled as in the conventional case and spray water (14 ° C.) that is not cooled from the banks 16a and 16b on the previous stage, under the same conditions as the amount of circulating water and heat load. The same cooling effect can be obtained by spraying spray water (8.5 ° C.) cooled from the bank 16c on the rear stage side.
[0020]
The spray water from each bank 16 a, 16 b, 16 c flows with the air flow and collides with the washer media 14, 15, travels down the washer media 14, 15 to the water storage tank 18, and is mixed in the water storage tank 18. That is, the spray water that has passed through the uncooled circulating water system 19a flows down to the water storage tank 18 at 16 ° C., and the sprayed water that has been cooled by the heat exchanger 21 through the cooling circulating water system 19b flows down to the water storage tank 18 at 12 ° C. Then, the mixed water of both becomes 14 ° C., the temperature rises to 12 ° C. or higher, and returns to the heat exchanger 21.
[0021]
Therefore, in the heat exchanger 21, the inlet temperature (7 ° C.) of the primary cold water is maintained higher than the conventional temperature (6 ° C.), and the predetermined temperature is ensured between the inlet temperature (7 ° C.) and the outlet temperature (12 ° C.). The difference can be set in a higher temperature range than before.
[0022]
Further, the amount of circulating water passing through the heat exchanger 21 may be equivalent to L / G = 0.7, 44% of the conventional amount (corresponding to L / G = 1.6), and the size of the heat exchanger 21 can be reduced. . As shown in FIG. 4, the circulation pump 20 can also be provided in each of the non-cooling circulation water system 19a and the cooling circulation water system 19b.
[0023]
As shown in FIG. 5, the banks 16 a and 16 c can be provided in two stages in the water spray chamber 12.
As shown in FIG. 6, the water storage tank 18 can be provided separately from the main body casing 11.
[0024]
【The invention's effect】
As described above, according to the present invention, the circulating water is diverted, and a part of the diverted circulating water is cooled, so that the amount of circulating water and heat are reduced as compared with the conventional case where the entire amount of circulating water is cooled. The return temperature of the circulating water in the heat exchanger can be kept high under the same load conditions, and a predetermined temperature difference is ensured between the inlet temperature and the outlet temperature of the primary chilled water in the heat exchanger. The heat exchanger can be greatly reduced in size without reducing the operating efficiency of the refrigerator.
[Brief description of the drawings]
FIG. 1 is a cross-sectional view of an air washer in an embodiment of the present invention.
FIG. 2 is an air diagram in the same embodiment.
FIG. 3 is a graph showing temperature changes of air and spray water in the same embodiment.
FIG. 4 is a piping diagram showing a main part in another embodiment of the present invention.
FIG. 5 is a cross-sectional view of an air washer according to still another embodiment of the present invention.
FIG. 6 is a cross-sectional view of an air washer according to still another embodiment of the present invention.
FIG. 7 is a cross-sectional view of a conventional air washer.
[Explanation of symbols]
11 Body casing 12 Water spray chamber 13a Air inlet 13b Air outlets 14, 15 Washer media 16a, 16b, 16c Bank 17 Spray nozzle 18 Water tank 19 Circulating water supply system 19a Uncooled circulating water system 19b Cooling circulating water system 20 Circulating pump 21 Heat exchange Equipment 22 Makeup water supply system 23 Drain system 24 Overflow system

Claims (1)

空気入口から空気出口に向かって空気流が生じる水噴霧室中に空気流の流れ方向に沿って多段にバンクを設け、各バンクに空気流中に噴霧水を噴出する複数の噴霧ノズルを設け、各バンクの各噴霧ノズルから噴霧された噴霧水が流下し、流下した噴霧水を混合して貯留する貯水槽を設け、この貯水槽と空気流の上流側に配置した前段側のバンクとの間に非冷却循環水系を設け、前記貯水槽と空気流の下流側に配置した後段側のバンクとの間に熱交換器を有する冷却循環水系を設けたことを特徴とするエアワッシャ。In the water spray chamber in which an air flow is generated from the air inlet to the air outlet, banks are provided in multiple stages along the air flow direction, and each bank is provided with a plurality of spray nozzles that eject spray water into the air flow. Spray water sprayed from each spray nozzle of each bank flows down, a water storage tank is provided for mixing and storing the spray water that has flowed down, and between this water storage tank and the upstream bank disposed upstream of the air flow the uncooled circulating water system is provided, an air washer, characterized in that a cooling circulating water system having a heat exchanger between the rear stage side of the bank arranged on the downstream side of the water tank and the air flow.
JP2001238678A 2001-08-07 2001-08-07 Air washer Expired - Lifetime JP3995436B2 (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105423454A (en) * 2015-12-10 2016-03-23 宜宾海丝特纤维有限责任公司 Method and device for increasing temperature of central air conditioner through condensate water

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Publication number Priority date Publication date Assignee Title
JP4687941B2 (en) * 2003-06-09 2011-05-25 清水建設株式会社 Pollutant removal device
CN109107656A (en) * 2018-11-02 2019-01-01 贵州大学 A kind of the mineral crushing device and its method of mining industry
CN110743284B (en) * 2019-10-15 2021-08-27 蓝城乐居建设管理集团有限公司 Tower crane spraying system

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105423454A (en) * 2015-12-10 2016-03-23 宜宾海丝特纤维有限责任公司 Method and device for increasing temperature of central air conditioner through condensate water

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