TW201805529A - Air compressor system - Google Patents

Air compressor system Download PDF

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TW201805529A
TW201805529A TW106119056A TW106119056A TW201805529A TW 201805529 A TW201805529 A TW 201805529A TW 106119056 A TW106119056 A TW 106119056A TW 106119056 A TW106119056 A TW 106119056A TW 201805529 A TW201805529 A TW 201805529A
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Taiwan
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water
path
compressor
cooler
air
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TW106119056A
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Chinese (zh)
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TWI633238B (en
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岡本裕介
井上陽貴
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三浦工業股份有限公司
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04BPOSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS
    • F04B39/00Component parts, details, or accessories, of pumps or pumping systems specially adapted for elastic fluids, not otherwise provided for in, or of interest apart from, groups F04B25/00 - F04B37/00
    • F04B39/16Filtration; Moisture separation
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04BPOSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS
    • F04B39/00Component parts, details, or accessories, of pumps or pumping systems specially adapted for elastic fluids, not otherwise provided for in, or of interest apart from, groups F04B25/00 - F04B37/00
    • F04B39/06Cooling; Heating; Prevention of freezing
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04BPOSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS
    • F04B39/00Component parts, details, or accessories, of pumps or pumping systems specially adapted for elastic fluids, not otherwise provided for in, or of interest apart from, groups F04B25/00 - F04B37/00
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04BPOSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS
    • F04B39/00Component parts, details, or accessories, of pumps or pumping systems specially adapted for elastic fluids, not otherwise provided for in, or of interest apart from, groups F04B25/00 - F04B37/00
    • F04B39/02Lubrication

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Compressor (AREA)
  • Applications Or Details Of Rotary Compressors (AREA)

Abstract

This invention provides an air compressor system using a compressor of water adding type capable of reducing the amount of water being brought outside along with the compressed air so as to reduce the amount of supplement of water from outside. The system has a compressor of water adding type 3, a preseparator 4 for separating air/water in the fluid delivered from the compressor 3, an after cooler 5 for cooling the compressed air after air/water separation by preseparator 4, a water cooler for cooling the separated water after the air/water separation by preseparator 4 and a separator tank 7 to which the compressed air and the separated water are delivered. The the separator tank 7 a compressed air delivery path is connected to an air phase unit and an adding water return tube to compressor 3 is connected to a liquid phase unit.

Description

空氣壓縮系統 Air compression system

本發明係關於一種使用水添加式之壓縮機的空氣壓縮系統。 The present invention relates to an air compression system using a water-added compressor.

以往,如下述專利文獻1之第1圖所示,已知有一種空氣壓縮系統,係具備:螺旋式之水潤滑空氣壓縮機(1),由一對之轉子(37)將其兩端支持在水潤滑滑動軸承(2);分離器(6),將來自該壓縮機(1)之送出流體(與潤滑水一同被送出之壓縮空氣)予以氣水分離;空冷熱交換器(10),係將從該分離器(6)返回至壓縮機(1)之轉子間的水予以冷卻;以及後冷卻器(11),將來自分離器(6)之壓縮空氣予以冷卻。在該系統中,在從空冷熱交換器(10)至壓縮機(1)之轉子間的水配管(22),分岐有軸承供水用水配管(23),被分岐之水係透過冷凍循環器(27)之吸熱用熱交換器(33),或透過旁通配管(24)供給至壓縮機(1)之軸承(2)。 Conventionally, as shown in FIG. 1 of the following Patent Document 1, an air compression system is known, which includes a water-lubricated air compressor (1) of a spiral type, and both ends are supported by a pair of rotors (37). The water-lubricated sliding bearing (2); the separator (6) separates the fluid (compressed air sent out with the lubricating water) from the compressor (1); the air-cooled heat exchanger (10), The water returned from the separator (6) to the rotor between the compressors (1) is cooled; and the after cooler (11) is used to cool the compressed air from the separators (6). In this system, the water piping (22) from the air-cooled heat exchanger (10) to the rotor of the compressor (1) has a bearing water supply piping (23), and the divided water system passes through the refrigeration cycle ( 27) The heat exchanger (33) for heat absorption or the bearing (2) supplied to the compressor (1) through a bypass pipe (24).

(先前技術文獻) (Prior technical literature) (專利文獻) (Patent Literature)

專利文獻1:日本特開2010-43589號公報(段落 [0012]-[0017]、第1圖) Patent Document 1: Japanese Patent Application Laid-Open No. 2010-43589 (paragraph [0012]-[0017], FIG. 1)

在習知技術中,來自壓縮機之送出流體係直接被送出至分離器槽(6),在氣水分離後,壓縮空氣係透過後冷卻器(11)被送出至外部,另一方面,分離水係透過空冷熱交換器(10)回到壓縮機。因此,分離器槽係將來自壓縮機之流體直接導入,亦即在事前未被氣水分離或冷卻之情形下被導入,而維持在比較高溫。因此,伴隨來自分離器槽之壓縮空氣而送出至外部之水分量會變多,為了補足該水分量,需要許多應從外部補給之水量。再者,為了冷卻壓縮空氣,亦必須在比分離器槽更下游處設置後冷卻器。再者,在習知技術中,由壓縮機所產生之壓縮熱,係在空冷式之熱交換器(10、11)中被廢棄至外氣,而未被熱回收。 In the conventional technology, the output stream system from the compressor is directly sent to the separator tank (6). After the gas and water are separated, the compressed air is sent to the outside through the aftercooler (11). On the other hand, the separation The water system returns to the compressor through the air-cooled heat exchanger (10). Therefore, the separator tank directly introduces the fluid from the compressor, that is, it is introduced without being separated or cooled by air and water beforehand, and is maintained at a relatively high temperature. Therefore, the amount of water sent to the outside accompanied by the compressed air from the separator tank increases, and in order to make up for this amount of water, a large amount of water to be replenished from the outside is required. Furthermore, in order to cool the compressed air, an aftercooler must be provided further downstream than the separator tank. Moreover, in the conventional technology, the compression heat generated by the compressor is discarded to the outside air in an air-cooled heat exchanger (10, 11) without being heat recovered.

因此,本發明所欲解決之課題係在於提供一種空氣壓縮系統,係可減低伴隨來自分離器槽之壓縮空氣而排出至外部之水分量,甚至可減少來自外部之補供水量。再者,也以提供一種空氣壓縮系統,係可省略後冷卻器在比分離器槽更下游處的設置。再者,較佳為提供一種可回收壓縮機之壓縮熱的空氣壓縮系統。 Therefore, the problem to be solved by the present invention is to provide an air compression system that can reduce the amount of water discharged to the outside with the compressed air from the separator tank, and can even reduce the amount of supplementary water supplied from the outside. Furthermore, to provide an air compression system, it is possible to omit the arrangement of the after cooler at a position further downstream than the separator tank. Furthermore, it is preferable to provide an air compression system capable of recovering the compression heat of the compressor.

本發明係為了解決上述課題而研創者、申請專利範圍第1項所述之發明係一種空氣壓縮系統,具備: 水添加式之壓縮機;預分離器,將來自該壓縮機之送出流體予以氣水分離;後冷卻器,對由該預分離器氣水分離後之壓縮空氣予以冷卻;水冷卻器,對由前述預分離器氣水分離後之分離水予以冷卻;以及分離器槽,供給通過前述各冷卻器後之壓縮空氣及分離水,且在氣相部連接有壓縮空氣之送出路徑,另一方面在液相部連接有朝前述壓縮機之添加水的返回路徑。 In order to solve the above-mentioned problems, the present invention is an air compression system which is developed by the inventor and is described in item 1 of the patent application scope, and includes: Water-adding compressor; pre-separator, which separates the fluid sent from the compressor for gas-water separation; after-cooler, which cools the compressed air after gas-water separation by the pre-separator; The separated water after the aforementioned pre-separator is cooled by gas-water separation; and a separator tank for supplying compressed air and separated water after passing through the above-mentioned respective coolers, and a compressed air sending path is connected to the gas phase part. The liquid phase part is connected to a return path for adding water to the compressor.

依據申請專利範圍第1項所述之發明,以預分離器將來自水添加式之壓縮機的送出流體予以氣水分離,且以後冷卻器使氣水分離後之壓縮空氣冷卻,另一方面以水冷卻器將分離水予以冷卻後,供給至分離器槽。因此,分離器槽係事先被氣水分離且供給冷卻之流體,而維持在比較低溫。因此,可減低伴隨著來自分離器槽之壓縮空氣而排出至外部之水分量,甚至可減少來自外部之補供水量。此外,在比分離器槽更下游處,設置在壓縮空氣之送出路徑的後冷卻器、及設置在添加水之返回路徑的水冷卻器並非必要者,亦可予以省略。 According to the invention described in the first item of the scope of the patent application, the pre-separator is used to separate the fluid sent from the water-added compressor into the gas-water separation, and the cooler cools the compressed air after the gas-water separation. The water cooler cools the separated water and supplies it to the separator tank. Therefore, the separator tank is separated by air and water in advance and supplied with a cooled fluid, and is maintained at a relatively low temperature. Therefore, the amount of water discharged to the outside accompanied by the compressed air from the separator tank can be reduced, and even the amount of supplementary water supplied from the outside can be reduced. Further, a downstream cooler provided in the compressed air sending path and a water cooler provided in the return path of the added water downstream of the separator tank are not necessary and may be omitted.

此外,以預分離器進行氣水分離,且分成為以後冷卻器進行之壓縮空氣的冷卻、及以水冷卻器進行之分離水的冷卻,藉此可提升各冷卻器之熱交換效率。 In addition, the pre-separator is used for gas-water separation, and is divided into cooling of compressed air by a subsequent cooler and cooling of separated water by a water cooler, thereby improving the heat exchange efficiency of each cooler.

申請專利範圍第2項所述之發明係在申請專利範圍第1項所述之空氣壓縮系統中,前述後冷卻器為壓縮空氣與冷卻水之熱交換器,前述水冷卻器為分離水與冷卻水之熱交換器,在前述各冷卻器中將前述冷卻水予以加 溫以製造溫水。 The invention described in item 2 of the scope of patent application is the air compression system described in item 1 of the scope of patent application. The aforementioned after cooler is a heat exchanger for compressed air and cooling water, and the aforementioned water cooler is for separating water and cooling. Heat exchanger for water, add the aforementioned cooling water to each of the aforementioned coolers Warm to make warm water.

依據申請專利範圍第2項所述之發明,在後冷卻器及水冷卻器中,藉由將壓縮熱予以回收並使通水加溫,藉此可製造溫水。 According to the invention described in item 2 of the scope of the patent application, warm water can be produced by recovering the heat of compression in the after cooler and the water cooler and heating the passing water.

申請專利範圍第3項所述之發明係在申請專利範圍第2項所述之空氣壓縮系統中,前述冷卻水係在通過前述後冷卻器之後,通過前述水冷卻器。 The invention described in the third scope of the patent application is the air compression system described in the second scope of the patent application. The cooling water passes through the water cooler after passing through the after cooler.

依據申請專利範圍第3項所述之發明,藉由透過冷卻水依序對後冷卻器及水冷卻器進行加溫,而可製造溫水。藉由使冷卻水先通過後冷卻器,即能以較低溫之冷卻水將壓縮空氣冷卻至所希望之溫度。再者,藉由使由上述方式被加溫之冷卻水通過水冷卻器,即可使冷卻水進一步升溫。 According to the invention described in item 3 of the scope of the patent application, warm water can be produced by sequentially heating the after cooler and the water cooler through the cooling water. By passing the cooling water through the aftercooler first, the compressed air can be cooled to the desired temperature with the cooling water at a lower temperature. Furthermore, by passing the cooling water heated in the above-mentioned manner through a water cooler, the cooling water can be further heated.

再者,申請專利範圍第4項所述之發明係在申請專利範圍第1至3項中任一項所述之空氣壓縮系統中,在來自前述分離器槽之壓縮空氣的送出路徑中,設置有用以將前述分離器槽內保持在設定壓力以上之一次壓調整閥。。 Furthermore, the invention described in item 4 of the scope of patent application is provided in the air compression system described in any one of the scope of claims 1 to 3 in the compressed air delivery path from the separator tank. There is a primary pressure regulating valve for keeping the inside of the separator tank above the set pressure. .

依據申請專利範圍第4項所述之發明,藉由將分離器槽內保持在設定壓力以上,即可確實地使添加水從分離器槽回到壓縮機。 According to the invention described in item 4 of the scope of patent application, by keeping the inside of the separator tank at a set pressure or higher, the added water can be reliably returned from the separator tank to the compressor.

依據本發明之空氣壓縮系統,可減低伴隨著來自分離器槽之壓縮空氣而排出至外部之水分量,甚至可 減少來自外部之補供水量。此外,設置在比分離器槽更下游處的後冷卻器並非必要者,亦可予以省略。再者,亦可將壓縮機之壓縮熱予以回收來製造溫水。 The air compression system according to the present invention can reduce the amount of water discharged to the outside with the compressed air from the separator tank, and can even Reduce external water supply. In addition, an aftercooler provided downstream of the separator tank is not necessary and may be omitted. Furthermore, the compression heat of the compressor can be recovered to produce warm water.

1‧‧‧空氣壓縮系統 1‧‧‧air compression system

2‧‧‧熱回收系統 2‧‧‧Heat Recovery System

3‧‧‧壓縮機 3‧‧‧compressor

4‧‧‧預分離器 4‧‧‧ pre-separator

5‧‧‧後冷卻器 5‧‧‧ after cooler

6‧‧‧水冷卻器 6‧‧‧ water cooler

7‧‧‧分離器槽 7‧‧‧ separator tank

8‧‧‧電動馬達 8‧‧‧ Electric motor

9‧‧‧空氣過濾器 9‧‧‧air filter

10‧‧‧吸入路徑 10‧‧‧ Suction path

11‧‧‧添加水返回路徑 11‧‧‧Add water return path

12‧‧‧送出路徑 12‧‧‧Submission route

13‧‧‧止回閥 13‧‧‧Check valve

14‧‧‧氣相連通路徑 14‧‧‧ gas phase communication path

15‧‧‧液相連通路徑 15‧‧‧Liquid phase communication path

16‧‧‧熱回收用熱交換器 16‧‧‧Heat recovery heat exchanger

17‧‧‧壓縮空氣送出路徑 17‧‧‧Compressed air delivery path

18‧‧‧一次壓調整閥 18‧‧‧ primary pressure regulating valve

19‧‧‧止回閥 19‧‧‧ check valve

20‧‧‧安全閥 20‧‧‧Safety valve

21‧‧‧放氣閥 21‧‧‧ air release valve

22‧‧‧添加水閥 22‧‧‧Add water valve

23‧‧‧濾水器 23‧‧‧ Water Filter

24‧‧‧供水路徑 24‧‧‧ Water supply route

24A‧‧‧第一供水路徑 24A‧‧‧First water supply route

24B‧‧‧第二供水路徑 24B‧‧‧Second Water Supply Path

25‧‧‧排水路徑 25‧‧‧ drainage path

26‧‧‧第一供水閥 26‧‧‧The first water supply valve

27‧‧‧止回閥 27‧‧‧Check valve

28‧‧‧第二供水閥 28‧‧‧Second water supply valve

29‧‧‧排水閥 29‧‧‧Drain valve

30‧‧‧水位檢測器 30‧‧‧Water Level Detector

31‧‧‧壓力感測器 31‧‧‧Pressure sensor

32‧‧‧入口路徑 32‧‧‧ entrance path

33‧‧‧出口路徑 33‧‧‧ Exit route

34‧‧‧回送路徑 34‧‧‧ loopback path

35‧‧‧切換手段 35‧‧‧ Switching means

36‧‧‧熱回收閥 36‧‧‧Heat Recovery Valve

37‧‧‧回送閥 37‧‧‧ return valve

38‧‧‧散熱器 38‧‧‧ Radiator

38A‧‧‧風扇 38A‧‧‧fan

39‧‧‧連絡路徑 39‧‧‧Contact Path

40‧‧‧泵 40‧‧‧ pump

41‧‧‧止回閥 41‧‧‧Check valve

42‧‧‧儲槽 42‧‧‧ storage tank

43‧‧‧出水溫度感測器 43‧‧‧Outlet water temperature sensor

第1圖係顯示本發明一實施例之空氣壓縮系統的概略圖。 FIG. 1 is a schematic diagram showing an air compression system according to an embodiment of the present invention.

以下,依據圖式詳細地說明本發明之具體的實施例。 Hereinafter, specific embodiments of the present invention will be described in detail with reference to the drawings.

第1圖係顯示本發明之一實施例的概略圖,顯示製造壓縮空氣之空氣壓縮系統1、及可藉由該空氣壓縮系統1而回收壓縮熱之熱回收系統2。亦即,在本實施例中,空氣壓縮系統1係具備熱回收系統2,相反而言,熱回收系統2係適用於空氣壓縮系統1。以下,針對空氣壓縮系統1及熱回收系統2依序加以說明。 FIG. 1 is a schematic diagram showing an embodiment of the present invention, showing an air compression system 1 for manufacturing compressed air, and a heat recovery system 2 capable of recovering compression heat by the air compression system 1. That is, in this embodiment, the air compression system 1 is provided with the heat recovery system 2. On the contrary, the heat recovery system 2 is applied to the air compression system 1. Hereinafter, the air compression system 1 and the heat recovery system 2 will be described in order.

≪空氣壓縮系統1之構成≫ ≫Composition of Air Compression System 1≫

首先,針對本實施例之空氣壓縮系統1的構成加以說明。本實施例之空氣壓縮系統1之主要部分為具備:水添加式之壓縮機3;預分離器4,將來自該壓縮機3之送出流體予以氣水分離;後冷卻器4,對由該預分離器4氣水分離後之壓縮空氣予以冷卻;水冷卻器6,對由該預分離器4氣水分離後之分離水予以冷卻;以及分離器槽7,供給通 過各冷卻器5、6後之壓縮空氣及分離水。 First, the configuration of the air compression system 1 of this embodiment will be described. The main part of the air compression system 1 of this embodiment is provided with: a water-adding compressor 3; a pre-separator 4 for gas-water separation of the fluid sent from the compressor 3; and a post-cooler 4 for The compressed air after the gas-water separation of the separator 4 is cooled; the water cooler 6 cools the separated water after the gas-water separation by the pre-separator 4; and the separator tank 7 Compressed air and separated water after passing each cooler 5,6.

壓縮機3係水添加式之空氣壓縮機。壓縮機3之形式雖無特別限定,但可設為例如螺旋式或卷軸式。水添加式之壓縮機3係在空氣之吸入口添加有水(典型而言為精製水(純水)或軟化水),將該添加水利用在壓縮室之密封或壓縮機構之冷卻等,同時將空氣予以壓縮並送出。在該送出時,亦與壓縮空氣一同地送出添加水。 Compressor 3 is a water-added air compressor. The form of the compressor 3 is not particularly limited, but may be, for example, a screw type or a scroll type. Water-adding compressor 3 is to add water (typically purified water (pure water) or demineralized water) to the air inlet, and use the added water in the compression chamber's seal or the cooling of the compression mechanism. Compress the air and send it out. At the time of this sending, the added water is also sent out together with the compressed air.

壓縮機3係在圖示例中藉由電動馬達8而驅動,亦能以其他之原動機驅動。例如,壓縮機3亦可藉由蒸氣馬達(蒸氣引擎)而被驅動。再者,壓縮機3亦可進行導通關斷(on off)控制,亦可進行容量控制(輸出調整)。例如,壓縮機3係對電動馬達8進行導通關斷控制,或對電動馬達8之轉數進行反相器控制。或者,在蒸氣馬達之情形時,控制對蒸氣馬達之給蒸閥的開閉或開度。 The compressor 3 is driven by the electric motor 8 in the example shown in the figure, and can be driven by another prime mover. For example, the compressor 3 may be driven by a steam motor (steam engine). In addition, the compressor 3 may perform on-off control and capacity control (output adjustment). For example, the compressor 3 performs on-off control of the electric motor 8 or inverter control of the number of revolutions of the electric motor 8. Alternatively, in the case of a steam motor, the opening or closing or opening degree of the steaming valve of the steam motor is controlled.

當使壓縮機3運轉時,外氣會透過空氣過濾器9而從吸入路徑10吸入至壓縮機3內,此時詳細如後述,透過來自分離器槽7之添加水返回路徑11以設定流量添加水。然後,在壓縮機3中被壓縮之空氣係伴隨著添加水被送出至預分離器4。在從壓縮機3至預分離器4之吐出路徑12,設置有止回閥13。 When the compressor 3 is operated, the outside air passes through the air filter 9 and is sucked into the compressor 3 from the suction path 10. At this time, the details are described later. The added water is returned through the return path 11 from the separator tank 7 to set the flow rate. water. Then, the compressed air in the compressor 3 is sent to the pre-separator 4 with the added water. The discharge path 12 from the compressor 3 to the pre-separator 4 is provided with a check valve 13.

此外,水添加式之壓縮機3亦可設為水潤滑式或水噴射式等(換言之亦可包含水潤滑式或水噴射式)。再者,在此之壓縮機3雖係對空氣之吸入口添加水,但亦可在空氣之吸入口以外具備供水口,而對該供水口添加水。 The water-added compressor 3 may be a water-lubricated or water-jet type (in other words, a water-lubricated or water-jet type). In addition, although the compressor 3 here is adding water to the air inlet, it may be provided with a water supply port other than the air inlet, and water may be added to the water supply port.

預分離器4係接受來自壓縮機3之送出流體(與添加水一同被送出之壓縮空氣),並進行氣水分離。亦即,來自壓縮機3之送出流體係在預分離器4中,分成為壓縮空氣及分離水。伴隨於此,預分離器4內係被分為上方之氣相部、及下方之液相部。再者,預分離器4之氣相部係透過氣相連通路徑14而連接於分離器槽7之氣相部,另一方面,預分離器4之液相部係透過液相連通路徑15而連接於分離器槽7之液相部。 The pre-separator 4 receives the fluid sent out from the compressor 3 (compressed air sent out together with the added water) and performs gas-water separation. That is, the outflow system from the compressor 3 is separated into compressed air and separated water in the pre-separator 4. With this, the interior of the pre-separator 4 is divided into a gas phase portion above and a liquid phase portion below. The gas phase portion of the pre-separator 4 is connected to the gas phase portion of the separator tank 7 through the gas-phase communication path 14. On the other hand, the liquid phase portion of the pre-separator 4 is connected to the liquid-phase communication path 15. Connected to the liquid phase portion of the separator tank 7.

在從預分離器4至分離器槽7之氣相連通路徑14,設置有後冷卻器5。後冷卻器5係對由預分離器4氣水分離後之壓縮空氣予以冷卻的手段。在此,就回收壓縮熱之熱回收用熱交換器16而言,後冷卻器5係在不會混合壓縮空氣與冷卻液之情況下進行熱交換。在後冷卻器5中,壓縮空氣係藉由冷卻液而被冷卻,另一方面,冷卻液係藉由壓縮空氣而被加溫。 An after-cooler 5 is provided in the gas-phase communication path 14 from the pre-separator 4 to the separator tank 7. The aftercooler 5 is a means for cooling the compressed air separated by the air-water separation of the pre-separator 4. Here, in the heat recovery heat exchanger 16 for recovering the compression heat, the after cooler 5 performs heat exchange without mixing compressed air and a cooling liquid. In the aftercooler 5, the compressed air is cooled by a cooling liquid, and the cooling liquid is warmed by a compressed air.

在從預分離器4至分離器槽7之液相連通路徑15中,設置有水冷卻器6。水冷卻器6係對由預分離器4氣水分離後之分離水予以冷卻的手段。在此,就回收壓縮熱之熱回收用熱交換器16而言,水冷卻器6係在不會混合壓縮空氣與冷卻液之情況下進行熱交換。在水冷卻器6中,分離水係藉由冷卻液而被冷卻,另一方面,冷卻液係藉由分離水而被加溫。 A water cooler 6 is provided in the liquid-phase communication path 15 from the pre-separator 4 to the separator tank 7. The water cooler 6 is a means for cooling the separated water separated by the gas separator from the pre-separator 4. Here, in the heat recovery heat exchanger 16 for recovering the compression heat, the water cooler 6 performs heat exchange without mixing compressed air and a cooling liquid. In the water cooler 6, the separated water is cooled by the cooling liquid, and the cooled liquid is heated by the separated water.

分離器槽7係接受通過前述各冷卻器5、6後之壓縮空氣及分離水,以進行氣水分離。來自預分離器4 之壓縮空氣係以後冷卻器5進行冷卻,以謀求水分之凝縮,該水分係在分離器槽7被去除。因此,分離器槽7內亦可分為上方之氣相部、及下方之液相部。此外,從預分離器4經由各連通路徑14、15而供給至分離器槽7之流體供給,係藉由壓縮機3之送出壓或水頭壓差而進行。 The separator tank 7 receives compressed air and separated water after passing through each of the coolers 5 and 6 to perform gas-water separation. From pre-separator 4 The compressed air is cooled by the cooler 5 to condense the moisture, which is removed in the separator tank 7. Therefore, the inside of the separator tank 7 can also be divided into a gas phase portion above and a liquid phase portion below. The fluid supply from the pre-separator 4 to the separator tank 7 through the communication paths 14 and 15 is performed by the discharge pressure of the compressor 3 or the head pressure difference.

在分離器槽7之氣相部中,除了前述之氣相連通路徑14之外,亦連接有朝壓縮空氣利用部之壓縮空氣送出路徑17。在壓縮空氣送出路徑17中,從分離器槽7之側依序設置有一次壓調整閥18及止回閥19。該一次壓調整閥18係在壓縮機3之運轉中將分離器槽7內保持在設定壓力以上之閥。在此,一次壓調整閥18係依據一次側(亦即分離器槽7側)之壓力,設為機械性動作之自力閥,依情況亦能以感測器監視一次側之壓力,依據該檢測壓力而進行控制之電動閥。此外,在本實施例中,在分離器槽7之氣相部中,除了安全閥20之外,設置有朝外部之排氣用的放氣閥21。此外,一次壓調整閥18及止回閥19亦可構成為一體型之閥機構。 In addition to the aforementioned gas-phase communication path 14, the gas-phase portion of the separator tank 7 is connected to a compressed-air sending path 17 toward the compressed-air utilization portion. In the compressed air delivery path 17, a primary pressure regulating valve 18 and a check valve 19 are sequentially provided from the side of the separator groove 7. The primary pressure regulating valve 18 is a valve that maintains the inside of the separator tank 7 at a pressure higher than a set pressure during the operation of the compressor 3. Here, the primary pressure regulating valve 18 is a self-operating valve that is mechanically operated according to the pressure on the primary side (that is, the side of the separator tank 7). Depending on the situation, the pressure on the primary side can also be monitored by a sensor. Pressure controlled electric valve. Further, in the present embodiment, in addition to the safety valve 20, a gas release valve 21 for exhausting to the outside is provided in the gas phase portion of the separator tank 7. In addition, the primary pressure regulating valve 18 and the check valve 19 may be configured as an integrated valve mechanism.

在分離器槽7之液相部,除了前述液相連通路徑15之外,連接有朝壓縮機3之添加水返回路徑11。在添加水返回路徑11中,在從分離器槽7之側依序設置有添加水閥22及濾水器23。在壓縮機3之運轉中,藉由打開添加水閥22,透過添加水返回路徑11至將分離器槽7內之儲留水送回壓縮機3。此時,藉由以壓縮機3之運轉所進行之對於壓縮機3之吸入、及分離器槽7內之加壓, 可使添加水從分離器槽7送回壓縮機3。再者,藉由一次壓調整閥18,分離器槽7內係保持在設定壓力以上之前提下,如後所述,壓縮空氣送出路徑17內之壓力(進一步而言為分離器槽7內之壓力)係維持在所希望壓力,因此可一邊將添加水閥22作為孔口發揮功能,一邊能以設定流量將添加水供給至壓縮機3。而且,在將添加水從分離器槽7供給至壓縮機3之際,可藉由濾水器23來去除夾雜物。 In addition to the liquid-phase communication path 15 described above, the liquid-phase portion of the separator tank 7 is connected to a water return path 11 to the compressor 3. In the added water return path 11, a water addition valve 22 and a water filter 23 are provided in this order from the side of the separator tank 7. During the operation of the compressor 3, by opening the adding water valve 22, the stored water in the separator tank 7 is returned to the compressor 3 through the added water return path 11 to the compressor 3. At this time, the suction of the compressor 3 and the pressure in the separator tank 7 are performed by the operation of the compressor 3, The added water can be returned from the separator tank 7 to the compressor 3. In addition, by the primary pressure adjusting valve 18, the inside of the separator tank 7 is lifted before being maintained above the set pressure. As described later, the pressure in the compressed air delivery path 17 (more specifically, the pressure in the separator tank 7) Since the pressure is maintained at a desired pressure, it is possible to supply the added water to the compressor 3 at a set flow rate while the added water valve 22 functions as an orifice. When the added water is supplied from the separator tank 7 to the compressor 3, the water filter 23 can be used to remove the inclusions.

空氣壓縮系統1係更具備供水路徑24及排水路徑25。供水路徑24係將來自離子交換裝置(例如混床式純水裝置或硬水軟化裝置)之供水源的水作為添加水而予以補給之手段。在本實施例中,來自供水源之供水路徑24係被分成第一供水路徑24A及第二供水路徑24B,第一供水路徑24A係連接於吸入至壓縮機3之吸入路徑10,另一方面,第二供水路徑24B係連接於分離器槽7。再者,在第一供水路徑24A設置有第一供水閥26,另一方面,在第二供水路徑24B,依序設置有止回閥27及第二供水閥28。此外,在本實施例中,第一供水閥26係電磁閥,第二供水閥28係設為手動閥。 The air compression system 1 further includes a water supply path 24 and a drainage path 25. The water supply path 24 is a means for replenishing water from a water supply source of an ion exchange device (such as a mixed bed type pure water device or a hard water softening device) as added water. In this embodiment, the water supply path 24 from the water supply source is divided into a first water supply path 24A and a second water supply path 24B. The first water supply path 24A is connected to the suction path 10 that is sucked into the compressor 3. On the other hand, The second water supply path 24B is connected to the separator tank 7. A first water supply valve 26 is provided in the first water supply path 24A, and a check valve 27 and a second water supply valve 28 are provided in the second water supply path 24B in this order. In addition, in this embodiment, the first water supply valve 26 is a solenoid valve, and the second water supply valve 28 is a manual valve.

另一方面,排水路徑25係連接在分離器槽7之底部。在排水路徑25設置有排水閥29,藉由打開排水閥29,可謀求來自分離器槽7內之排水。 On the other hand, the drainage path 25 is connected to the bottom of the separator tank 7. A drainage valve 29 is provided in the drainage path 25. By opening the drainage valve 29, drainage from the inside of the separator tank 7 can be achieved.

其他,在分離器槽7設置有水位檢測器30。該水位檢測器30之構成雖無特別限定,但可設為可檢測出不包含例如離子類之精製水.凝縮水之水位的浮標式水位 檢測器。再者,在來自分離器槽7之壓縮空氣送出路徑17,於比一次壓調整閥18或止回閥19更下游處,設置有壓力感測器31。藉由該壓力感測器31,可監視壓縮空氣之送出壓(對壓縮空氣利用部之供給壓)。 In addition, a water level detector 30 is provided in the separator tank 7. Although the structure of the water level detector 30 is not particularly limited, it may be configured to detect purified water that does not contain, for example, ions. Buoy-type water level Detector. Further, a pressure sensor 31 is provided in the compressed air delivery path 17 from the separator tank 7 further downstream than the primary pressure regulating valve 18 or the check valve 19. The pressure sensor 31 can monitor the compressed air supply pressure (supply pressure to the compressed air utilization part).

≪空氣壓縮系統1之動作≫ ≫Operation of Air Compression System 1≫

接著,針對本實施例之空氣壓縮系統1的動作加以說明。以下所述之一連串的控制,基本上係藉由未圖示之控制器而自動進行。亦即,控制器係連接在壓縮機3(具體而言為其馬達8)、放氣閥21、添加水閥22、第一供水閥26、排水閥29、水位檢測器30及壓力感測器31等,且依據水位檢測器30或壓力感測器31之檢測信號等,控制壓縮機3或各閥21、22、26、29等。 Next, the operation of the air compression system 1 of this embodiment will be described. One of the series of controls described below is basically performed automatically by a controller (not shown). That is, the controller is connected to the compressor 3 (specifically, its motor 8), the air release valve 21, the water addition valve 22, the first water supply valve 26, the drain valve 29, the water level detector 30, and the pressure sensor. 31, etc., and controls the compressor 3 or each valve 21, 22, 26, 29, etc. according to the detection signal of the water level detector 30 or the pressure sensor 31 and the like.

首先,針對空氣之流動加以說明。當對壓縮機3之運轉進行開始時,壓縮機3係透過空氣過濾器9吸入空氣,並進行壓縮而送出。從壓縮機3送出之壓縮空氣係透過預分離器4、後冷卻器5及分離器槽7而從壓縮空氣送出路徑17送至壓縮空氣利用部。然而,由於在壓縮空氣送出路徑17設置有一次壓調整閥18,因此在如運轉開始之後,在分離器槽7內之壓力較低之狀態下,一次壓調整閥18會被關閉,往壓縮空氣利用部之壓縮空氣係不會被送出。當一次壓調整閥18之一次側(亦即分離器槽7側)之壓力為設定壓力以上時,一次壓調整閥18會打開,且往壓縮空氣利用部之壓縮空氣會被送出。 First, the flow of air will be described. When the operation of the compressor 3 is started, the compressor 3 sucks air through the air filter 9, compresses it, and sends it out. The compressed air sent from the compressor 3 passes through the pre-separator 4, the after-cooler 5, and the separator tank 7 and is sent from the compressed-air sending path 17 to the compressed-air utilization unit. However, since the primary pressure regulating valve 18 is provided in the compressed air delivery path 17, after the start of the operation, the primary pressure regulating valve 18 will be closed to the compressed air when the pressure in the separator tank 7 is low. The compressed air in the utilization section is not sent out. When the pressure on the primary side of the primary pressure regulating valve 18 (that is, the side of the separator tank 7) is equal to or higher than the set pressure, the primary pressure regulating valve 18 is opened and the compressed air to the compressed air utilization part is sent out.

在壓縮機3之運轉中,壓縮機3係以將壓力感測器31之檢測壓力維持在目標壓力之方式進行控制。例如,壓縮機3之馬達8係被導通關斷控制,或被反相器控制。此外,目標壓力係比一次壓調整閥18之設定壓力高。因此,以後基本上,分離器槽7內係維持在目標壓力。 During the operation of the compressor 3, the compressor 3 is controlled so that the detection pressure of the pressure sensor 31 is maintained at the target pressure. For example, the motor 8 of the compressor 3 is controlled by on-off, or controlled by an inverter. The target pressure is higher than the set pressure of the primary pressure regulating valve 18. Therefore, basically, the separator tank 7 is maintained at the target pressure thereafter.

在壓縮機3之運轉中,藉由打開添加水閥22,能以設定流量將水添加在壓縮機3之出入口。藉此,可謀求壓縮機3之密封、冷卻及潤滑。來自壓縮機3之壓縮空氣係在伴隨添加水之狀態下,被送出至預分離器4。並且,在預分離器4中謀求氣水分離。以預分離器4進行氣水分離後之壓縮空氣,係在以後冷卻器5進行冷卻之後,以分離器槽7更進一步進行氣水分離,且從壓縮空氣送出路徑17送出至外部。另一方面,在預分離器4進行之分離水係以水冷卻器6進行冷卻之後,儲留在分離器槽7,且可透過添加水返回路徑11供給至壓縮機3。 During operation of the compressor 3, by opening the water adding valve 22, water can be added to the inlet and outlet of the compressor 3 at a set flow rate. Thereby, sealing, cooling, and lubrication of the compressor 3 can be achieved. The compressed air from the compressor 3 is sent to the pre-separator 4 with the addition of water. The pre-separator 4 seeks gas-water separation. The compressed air after the air-water separation is performed by the pre-separator 4 is cooled by the cooler 5 later, and the air-water separation is further performed by the separator tank 7, and the compressed air is sent from the compressed air delivery path 17 to the outside. On the other hand, after the separation water from the pre-separator 4 is cooled by the water cooler 6, it is stored in the separator tank 7 and can be supplied to the compressor 3 through the added water return path 11.

在壓縮機3之運轉中,分離器槽7內之水位係維持在設定水位。例如,當以水位檢測器30所進行之檢測水位超過上限水位時,打開排水閥29使水位降低至預定位置。相反地,當以水位檢測器30進行之檢測水位超過下限水位時,打開第一供水閥26並使水位上升至預定位置。在第一供水閥26之開放中,補供水係透過壓縮機3供給至分離器槽7。在此期間,亦可閉鎖添加水閥22。此外,在壓縮機3之停止中,打開第二供水閥28,可直接供水至分離器槽7。 During the operation of the compressor 3, the water level in the separator tank 7 is maintained at a set water level. For example, when the water level detected by the water level detector 30 exceeds the upper limit water level, the drain valve 29 is opened to lower the water level to a predetermined position. Conversely, when the detected water level by the water level detector 30 exceeds the lower limit water level, the first water supply valve 26 is opened and the water level is raised to a predetermined position. When the first water supply valve 26 is opened, the makeup water is supplied to the separator tank 7 through the compressor 3. During this period, the addition water valve 22 may be closed. In addition, when the compressor 3 is stopped, the second water supply valve 28 is opened to directly supply water to the separator tank 7.

另一方面,在壓縮機3停止時,放氣閥21會打開。在壓縮機3之停止中亦預先打開放氣閥21,藉此可防止壓縮機3之逆轉。然後,在壓縮機3再起動時,關閉放氣閥21。 On the other hand, when the compressor 3 is stopped, the purge valve 21 is opened. The air release valve 21 is also opened before the compressor 3 is stopped, thereby preventing the compressor 3 from being reversed. Then, when the compressor 3 is restarted, the purge valve 21 is closed.

依據本實施例之空氣壓縮系統1,以預分離器4將來自壓縮機3之送出流體予以氣水分離,且以後冷卻器5將氣水分離後之壓縮空氣予以冷卻,另一方面以水冷卻器6將分離水予以冷卻之後,供給至分離器槽7。因此,分離器槽7係供給有事前被氣水分離而冷卻之流體,以維持比較低溫。分離器槽7內之溫度係維持在壓縮空氣之露點溫度以下。因此,可減低伴隨著來自分離器槽7之壓縮空氣而排出至外部之水分量,且可進一步減少來自外部之補供水量,且可謀求運轉成本之減低。此外,基本上不需要分別在壓縮空氣送出路徑17設置第二後冷卻器,或在添加水返回路徑11設置第二水冷卻器。 According to the air compression system 1 of this embodiment, the pre-separator 4 separates the fluid sent from the compressor 3 for gas-water separation, and after that, the cooler 5 cools the compressed air after the gas-water separation, and on the other hand, water cooling The separator 6 cools the separation water, and then supplies it to the separator tank 7. Therefore, the separator tank 7 is supplied with a fluid that has been previously separated and cooled by gas and water to maintain a relatively low temperature. The temperature in the separator tank 7 is maintained below the dew point temperature of the compressed air. Therefore, the amount of water discharged to the outside due to the compressed air from the separator tank 7 can be reduced, the amount of supplementary water supplied from the outside can be further reduced, and the running cost can be reduced. In addition, it is basically unnecessary to provide a second aftercooler in the compressed air sending path 17 or a second water cooler in the added water return path 11 respectively.

再者,依據本實施例之空氣壓縮系統1,以預分離器4進行氣水分離,且分成為以後冷卻器5進行之壓縮空氣的冷卻、及以水冷卻器6進行之分離水的冷卻,藉此可使各冷卻器5、6之熱交換效率。伴隨於此,可使構成各冷卻器5、6之熱交換器小型化。 Furthermore, according to the air compression system 1 of this embodiment, the air-water separation is performed by the pre-separator 4, and is divided into the cooling of the compressed air by the cooler 5 and the cooling of the separated water by the water cooler 6, Thereby, the heat exchange efficiency of each cooler 5 and 6 can be made. With this, the heat exchangers constituting the respective coolers 5 and 6 can be miniaturized.

≪熱回收系統2之構成≫ ≫Construction of heat recovery system 2≫

接著,針對本實施例之熱回收系統2的構成加以說明。本實施例之熱回收系統2係將壓縮機3之壓縮熱利用 在冷卻液之加溫而進行熱回收之系統,且可切換熱回收之有無。 Next, the configuration of the heat recovery system 2 of this embodiment will be described. The heat recovery system 2 of this embodiment uses the compression heat of the compressor 3 A system that performs heat recovery when the coolant is warmed, and the presence or absence of heat recovery can be switched.

冷卻液雖無特別限定,但典型上為水。就該水而言,依據用途,除了使用自來水之外,亦可使用軟化水或精製水(純水)等。例如,在利用熱回收系統2對蒸氣鍋爐之供水之預熱的情形時,係採用如後所述進行脫氣處理之軟化水。以下,冷卻液係作為水(亦即冷卻水)加以說明,其他液體之情形亦同。換言之,在以下說明中,冷卻水可非如文字所述之水,亦可為水以外之冷卻液。 Although the cooling liquid is not particularly limited, it is typically water. This water can be used in addition to tap water, demineralized water, purified water (pure water), etc., depending on the application. For example, in the case of using the heat recovery system 2 to preheat the water supply of the steam boiler, demineralized water subjected to degassing treatment as described later is used. Hereinafter, the cooling liquid is described as water (that is, cooling water), and the same applies to other liquids. In other words, in the following description, the cooling water may be not water as described in the text, or a cooling liquid other than water.

本實施例之熱回收系統2之主要部分係具備:藉由壓縮機3之壓縮熱而將冷卻水予以加溫之熱回收用熱交換器16(後冷卻器5、水冷卻器6);冷卻水往該熱回收用熱交換器16流動之入口路徑32;冷卻水從熱回收用熱交換器16流動的出口路徑33;連接出口路徑33入口路徑32之冷卻水的回送路徑34;切換後述之通液路徑與循環路徑之切換手段35(熱回收閥36、回送閥37);以及將循環路徑之循環冷卻水予以冷卻之散熱器38。 The main part of the heat recovery system 2 of this embodiment is provided with: a heat recovery heat exchanger 16 (after cooler 5, water cooler 6) for heating cooling water by the compression heat of the compressor 3; cooling; An inlet path 32 through which water flows to the heat recovery heat exchanger 16; an outlet path 33 through which cooling water flows from the heat recovery heat exchanger 16; a return path 34 for cooling water connected to the outlet path 33 and the inlet path 32; Switching means 35 (heat recovery valve 36, return valve 37) for the liquid flow path and the circulation path; and a radiator 38 for cooling the circulating cooling water of the circulation path.

熱回收用熱交換器16係在本實施例中為後冷卻器5及水冷卻器6。在後冷卻器5中,將壓縮空氣與冷卻水進行熱交換,並以冷卻水將壓縮空氣予以冷卻,另一方面以壓縮空氣來加溫冷卻水。將壓縮空氣所具有之壓縮熱利用在冷卻水之加溫,可謀求熱回收。另一方面,水冷卻器6係將添加水(在預分離器之分離水)與冷卻水進行熱交換,並以冷卻水將添加水予以冷卻,另一方面以添加水 將冷卻水予以加溫。將添加水所具有之壓縮熱利用在冷卻水之加溫,可謀求熱回收。 The heat recovery heat exchanger 16 is an after cooler 5 and a water cooler 6 in this embodiment. In the aftercooler 5, heat is exchanged between the compressed air and the cooling water, the compressed air is cooled by the cooling water, and the cooling water is heated by the compressed air. The heat of compression of compressed air is used for heating the cooling water, and heat recovery can be achieved. On the other hand, the water cooler 6 performs heat exchange between the added water (separated water in the pre-separator) and the cooling water, and cools the added water with the cooling water, and on the other hand, adds water Warm the cooling water. The compression heat of the added water is used for heating the cooling water, and heat recovery can be achieved.

此外,後冷卻器5及水冷卻器6,係在本實施例中,冷卻水會依序通過。因此,在本實施例中,後冷卻器5與水冷卻器6係以連絡路徑39相連接。再者,冷卻水係從入口路徑32依序經由後冷卻器5、連絡路徑39及水冷卻器6而流動至出口路徑33。以下,使以連絡路徑39所連接之後冷卻器5與水冷卻器6對位,並簡稱為熱回收用熱交換器16。 In addition, the after cooler 5 and the water cooler 6 are in this embodiment, and the cooling water will sequentially pass through. Therefore, in this embodiment, the aftercooler 5 and the water cooler 6 are connected by a communication path 39. The cooling water flows from the inlet path 32 to the outlet path 33 in this order through the aftercooler 5, the communication path 39, and the water cooler 6. Hereinafter, the cooler 5 and the water cooler 6 are aligned after being connected by the communication path 39, and are simply referred to as a heat recovery heat exchanger 16 for heat recovery.

在從供水源至熱回收用熱交換器16之入口路徑32,往熱回收用熱交換器16依序設置有泵40、止回閥41及散熱器38。藉由使泵40動作,可使冷卻水通過熱回收用熱交換器16。散熱器38係在本實施例中為空冷式,並對冷卻水及外氣(以風扇38A進行之通風)進行熱交換。詳細雖如後述,但例如散熱器38之入口側的冷卻水溫度比外氣溫度高時,可藉由使散熱器38之風扇38A動作,而能以風扇38A所進行之通風將冷卻水予以冷卻。 A pump 40, a check valve 41, and a radiator 38 are sequentially provided in the inlet path 32 from the water supply source to the heat recovery heat exchanger 16 to the heat recovery heat exchanger 16. By operating the pump 40, the cooling water can pass through the heat recovery heat exchanger 16. The radiator 38 is air-cooled in this embodiment, and performs heat exchange between cooling water and outside air (ventilation by a fan 38A). Although the details are described later, for example, when the temperature of the cooling water at the inlet side of the radiator 38 is higher than the outside air temperature, the cooling water can be cooled by the ventilation of the fan 38A by operating the fan 38A of the radiator 38. .

在從熱回收用熱交換器16之出口路徑33,設置有熱回收閥36。在壓縮機3之運轉中,藉由打開熱回收閥36使泵40動作,使冷卻水通過熱回收用熱交換器16,而可謀求壓縮熱之回收。熱回收閥36係在本實施例中,由可開度調整之電動閥所構成。 A heat recovery valve 36 is provided in the exit path 33 from the heat recovery heat exchanger 16. During the operation of the compressor 3, the pump 40 is operated by opening the heat recovery valve 36, and the cooling water is passed through the heat recovery heat exchanger 16 to recover the compression heat. The heat recovery valve 36 is constituted by an electric valve whose opening degree can be adjusted in this embodiment.

比熱回收閥36更上游側之出口路徑33、與比泵40更上游側之入口路徑32,係以回送路徑34相連接。 此時,在入口路徑32與回送路徑34之連接部位,較佳為預先設置冷卻水之儲槽42。然而,儲槽42係可依情況省略其設置。再者,儲槽42並非設置在入口路徑32中之與回送路徑34的連接部位,亦可設置在比該連接部位更下游(較佳為比泵40更上游)之位置。此外,泵40係除了設置在入口路徑32中之比與回送路徑34之連接部位更下游處以外,亦可設置在連絡路徑39、或出口路徑33中之與回送路徑34之連接部位更上游的位置。 An outlet path 33 upstream of the heat recovery valve 36 and an inlet path 32 upstream of the pump 40 are connected by a return path 34. At this time, it is preferable that a storage tank 42 for cooling water is provided in advance at a connection portion between the inlet path 32 and the return path 34. However, the storage tank 42 may be omitted according to circumstances. In addition, the storage tank 42 is not provided in a connection portion of the inlet path 32 and the return path 34, and may be provided at a position further downstream (preferably more upstream than the pump 40) than the connection position. In addition, the pump 40 may be provided further downstream than the connection portion of the inlet path 32 and the return path 34, and may also be provided upstream of the connection path 39 or the connection path of the return path 34 in the outlet path 33. position.

在回送路徑34中設置有回送閥37。回送閥37係在本實施例中由電動閥所構成。詳細雖如後述,但藉由選擇性地打開熱回收閥36與回送閥37中之任一方,即可切換透過回送路徑34使通過熱回收用熱交換器16後之冷卻水送回入口路徑32,或不透過回送路徑34而送至出口路徑33之下游。 A return valve 37 is provided in the return path 34. The return valve 37 is constituted by an electric valve in this embodiment. Although the details are described later, by selectively opening either the heat recovery valve 36 or the return valve 37, it is possible to switch through the return path 34 to return the cooling water that has passed through the heat recovery heat exchanger 16 to the inlet path 32. , Or sent downstream of the exit path 33 without passing through the loopback path 34.

切換手段35係在本實施例中,由熱回收閥36及回送閥37所構成。藉由切換熱回收閥36與回送閥37之各開閉,而可將冷卻水之流路切換成下述之通液路徑與循環路徑之任一者 The switching means 35 is composed of a heat recovery valve 36 and a return valve 37 in this embodiment. By switching the opening and closing of each of the heat recovery valve 36 and the return valve 37, the cooling water flow path can be switched to any one of the following liquid flow path and circulation path

通液路徑係在關閉回送閥37之狀態下打開熱回收閥36而實現。通液路徑係包含入口路徑32、熱回收用熱交換器16、及出口路徑33,且不包含回送路徑34之路徑。在設為通液路徑之狀態下使泵40動作時,來自入口路徑32之冷卻水會經由熱回收用熱交換器16,通過出口路徑33之熱回收閥36而被導出(熱回收實施狀態)。此時, 在儲槽42中,由供水源適當地供水。換言之,在通液路徑使泵40動作中,在入口路徑32供給有來自供水源之水。 The liquid flow path is realized by opening the heat recovery valve 36 with the return valve 37 closed. The liquid flow path includes a path of the inlet path 32, the heat recovery heat exchanger 16, and the outlet path 33, and does not include the return path 34. When the pump 40 is operated with the liquid flow path set, the cooling water from the inlet path 32 is discharged through the heat recovery heat exchanger 16 and the heat recovery valve 36 of the outlet path 33 (heat recovery implementation state). . at this time, The storage tank 42 is appropriately supplied with water from a water supply source. In other words, while the pump 40 is operated in the liquid-passing path, water from the water supply source is supplied to the inlet path 32.

循環路徑係在關閉熱回收閥36之狀態下,藉由打開回送閥37而實現。循環路徑係包含比回送路徑34之連接部位更下游側之入口路徑32、熱回收用熱交換器16、比回送路徑34之連接部位更上游側之出口路徑33、及回送路徑34的路徑。在設為循環路徑之狀態下使泵40

Figure TW201805529AD00001
動作時,來自泵40之冷却水係透過熱回收用熱交換器16及回送路徑34被送回泵40而循環。此時,藉由使散熱器38動作,即可在散熱器38中將循環冷卻水予以冷卻(熱回收停止狀態)。此外,在循環路徑使冷卻水循環之期間,無須從供水源對儲槽42進行新的供水。 The circulation path is realized by opening the return valve 37 with the heat recovery valve 36 closed. The circulation path is a path including an inlet path 32 downstream of the connection part of the return path 34, a heat recovery heat exchanger 16, an outlet path 33 upstream of the connection part of the return path 34, and a return path 34. Make the pump 40 with the circulation path set
Figure TW201805529AD00001
During operation, the cooling water from the pump 40 is sent back to the pump 40 through the heat recovery heat exchanger 16 and the return path 34 to circulate. At this time, by operating the radiator 38, the circulating cooling water can be cooled in the radiator 38 (heat recovery stopped state). In addition, while cooling water is circulated in the circulation path, it is not necessary to supply fresh water to the storage tank 42 from the water supply source.

出口路徑33係在熱回收閥36之出口側設置有出水溫度感測器43。另一方面,入口路徑32係在散熱器38之入口側設置有供水溫度感測器(省略圖示)。供水溫度感測器係只要在入口路徑32中之比散熱器38更上游側處,亦可依情況來檢測水源之水溫。然而,係在入口路徑32設置有儲槽42時,供水溫度感測器係較佳為設置在入口路徑32中之儲槽42或比儲槽42更下游處,且設置在比散熱器38更上游處。除此之外,本實施例之熱回收系統2亦可檢測外氣溫度,亦可設置外氣溫度感測器(省略圖示)。 The outlet path 33 is provided with an outlet temperature sensor 43 on the outlet side of the heat recovery valve 36. On the other hand, the inlet path 32 is provided with a water supply temperature sensor (not shown) on the inlet side of the radiator 38. The water supply temperature sensor can detect the water temperature of the water source as long as it is on the upstream side of the inlet path 32 than the radiator 38. However, when the storage tank 42 is provided in the inlet path 32, the water supply temperature sensor is preferably provided in the storage tank 42 in the inlet path 32 or downstream of the storage tank 42 and is provided more than the radiator 38. Upstream. In addition, the heat recovery system 2 of this embodiment can also detect the outside air temperature, and an outdoor air temperature sensor (not shown) can also be provided.

≪熱回收系統2之動作≫ ≫Operation of heat recovery system 2≫

接著,針對本實施例之熱回收系統2的動作加以說 明。以下所述之一連串的控制係藉由未圖示之控制器而自動進行。亦即,控制器係除了連接在泵40、散熱器38(具體而言為其風扇38A的馬達)、熱回收閥36及回送閥37,且連接在出水溫度感測器43、供水溫度感測器及外氣溫度感測器等,並依據各溫度感測器之檢測信號等,來控制泵40、風扇38A及各閥36、37等。 Next, the operation of the heat recovery system 2 of this embodiment will be described. Bright. One of the series of controls described below is automatically performed by a controller (not shown). That is, the controller is connected to the pump 40, the radiator 38 (specifically, the motor of its fan 38A), the heat recovery valve 36, and the return valve 37, and is connected to the outlet temperature sensor 43 and the water supply temperature sensor. And the outside air temperature sensor, etc., and control the pump 40, the fan 38A, and the valves 36, 37, etc. according to the detection signals and the like of each temperature sensor.

在壓縮機3之動作中(亦即壓縮空氣之製造中),使泵40動作,並使冷卻水通過熱回收用熱交換器16。藉此,在熱回收用熱交換器16中,可使來自壓縮機3之送出流體(壓縮空氣或添加水)冷卻,並且以來自送出流體之壓縮熱來加溫冷卻水。以此方式製造之溫水係依據溫水利用部之使用負荷(出口路徑33末端之溫水利用部之溫水要求的有無),藉由切換手段35來切換流路。亦即,在溫水利用部中需要溫水時,切換成通液路徑,且在溫水利用部中不需要溫水時,切換成循環路徑。 During the operation of the compressor 3 (that is, during the production of compressed air), the pump 40 is operated, and the cooling water is passed through the heat recovery heat exchanger 16. Accordingly, in the heat recovery heat exchanger 16, the fluid (compressed air or added water) sent from the compressor 3 can be cooled, and the cooling water can be heated by the heat of compression from the fluid sent out. The hot water manufactured in this way is switched by the switching means 35 in accordance with the use load of the hot water utilization part (presence or absence of the warm water requirement of the hot water utilization part at the end of the outlet path 33). That is, when warm water is required in the warm water utilization section, the liquid flow path is switched, and when warm water is not required in the warm water utilization section, the circuit is switched to the circulation path.

例如,可透過出口路徑33將在熱回收用熱交換器16經加溫之溫水供水至蒸氣鍋爐之供水槽,且依據該供水槽內之水位,來切換通液路徑及循環路徑。此時,例如當供水槽內之水位低於下限水位時,只要供給供給溫水作為通液路徑,至超過上限水位為止即可。再者,當供水槽內之水位超過上限水位時,切換成循環路徑即可。 For example, the heated water in the heat recovery heat exchanger 16 can be supplied to the water supply tank of the steam boiler through the outlet path 33, and the liquid passing path and the circulation path can be switched according to the water level in the water supply tank. At this time, for example, when the water level in the water supply tank is lower than the lower limit water level, it is only necessary to supply and supply warm water as a liquid flow path until the upper limit water level is exceeded. Furthermore, when the water level in the water supply tank exceeds the upper limit water level, it may be switched to a circulation path.

此外,在將熱回收系統2使用在對於蒸氣鍋爐之供水槽的供水之預熱時(換言之為使用對蒸氣鍋爐之供水槽的供水作為冷卻水時),係在入口路徑32中,供給 以硬水軟化裝置及脫氣裝置(脫酸素裝置)進行處理之脫氣軟化水。此時,在儲槽42中,為了防止氧之再溶存,較佳為在儲槽42之水面將塑膠珠浮在一面。 In addition, when the heat recovery system 2 is used for preheating the water supply to the water boiler's water supply tank (in other words, when the water supply to the water boiler's water supply tank is used as cooling water), it is supplied to the inlet path 32 and supplied. Deaerated softened water treated by a hard water softening device and a degassing device (deacidification device). At this time, in order to prevent re-dissolution of oxygen in the storage tank 42, it is preferable to float plastic beads on one side of the water surface of the storage tank 42.

為了在使冷卻水通水於熱回收用熱交換器16之期間,實施熱回收(換言之為往外部之出水),係將切換手段35切換成通液路徑。在通液路徑中,關閉回送閥37,另一方面打開熱回收閥36。再者,詳細所後所述,典型而言係使風扇38A停止。此時,來自供水源之水係在熱回收用熱交換器16被加溫,且送至出口路徑33之下游的溫水利用部。此時,以將出水溫度感測器43之檢測溫度維持在設定溫度之方式調整熱回收閥36之開度,可供給對溫水利用部設定溫度之溫水。 In order to carry out heat recovery (in other words, water to the outside) while cooling water is passed through the heat recovery heat exchanger 16, the switching means 35 is switched to a liquid-passing path. In the liquid flow path, the return valve 37 is closed, and the heat recovery valve 36 is opened. In addition, as will be described in detail later, the fan 38A is typically stopped. At this time, the water from the water supply source is heated in the heat recovery heat exchanger 16 and sent to the warm water utilization section downstream of the outlet path 33. At this time, the opening degree of the heat recovery valve 36 is adjusted so that the detection temperature of the outlet temperature sensor 43 is maintained at a set temperature, and hot water with a temperature set to the warm water utilization unit can be supplied.

為了在使冷卻水通水於熱回收用熱交換器16之期間,停止熱回收(換言之為往外部之出水),將切換手段35切換成循環路徑。在循環路徑中,關閉熱回收閥36,另一方面打開回送閥37。此外,使散熱器38之風扇38A動作。此時,以熱回收用熱交換器16進行加溫之冷卻水,係經由回送路徑34而送回至入口路徑32,在以散熱器38冷卻之後,再供給至熱回收用熱交換器16。亦即,一面使冷卻水在熱回收用熱交換器16循環,一面以散熱器38散熱至外氣。 In order to stop the heat recovery (in other words, the water is discharged to the outside) while cooling water is passed through the heat recovery heat exchanger 16, the switching means 35 is switched to a circulation path. In the circulation path, the heat recovery valve 36 is closed, and the return valve 37 is opened. In addition, the fan 38A of the heat sink 38 is operated. At this time, the cooling water heated by the heat recovery heat exchanger 16 is returned to the inlet path 32 via the return path 34, and after being cooled by the radiator 38, it is supplied to the heat recovery heat exchanger 16. That is, the cooling water is circulated in the heat recovery heat exchanger 16 while being radiated to the outside air by the radiator 38.

在通液路徑使冷卻水通水之期間,亦可依據供水溫度感測器之檢測溫度、及外氣溫度感測器之檢測溫度,如下方式控制散熱器38之風扇38A。亦即,在位於通 液路徑之狀態下,當供水溫度感測器之檢測溫度比外氣溫度感測器之檢測溫度更低時,使散熱器38之風扇38A動作。藉此,可藉由外氣並以散熱器38使冷卻水加溫(亦即將散熱器38利用作為加熱器),而可進行對熱回收用熱交換器16之冷卻水的預熱。另一方面,在位於通液路徑之狀態下,供水溫度感測器之檢測溫度比外氣溫度感測器之檢測溫度更高時,使散熱器38之風扇38A停止。藉此,避免藉由外氣以散熱器38使冷卻水冷卻之缺失。 While the cooling water is flowing through the liquid-passing path, the fan 38A of the radiator 38 can also be controlled as follows according to the detection temperature of the water supply temperature sensor and the detection temperature of the outside air temperature sensor. That is, in In the state of the liquid path, when the detection temperature of the water supply temperature sensor is lower than that of the outside air temperature sensor, the fan 38A of the radiator 38 is operated. Thereby, the cooling water can be heated by the outside air and the radiator 38 (that is, the radiator 38 is used as a heater), and the cooling water of the heat recovery heat exchanger 16 can be preheated. On the other hand, when the detection temperature of the water-supply temperature sensor is higher than the detection temperature of the outside-air temperature sensor in the state of being in the liquid-passing path, the fan 38A of the radiator 38 is stopped. Thereby, the lack of cooling water cooling by the radiator 38 by the outside air is avoided.

然而,在本實施例中,如前所述,入口路徑32係在回送路徑34之連接部位或比該連接部位更下游處,設置有冷卻水之儲槽42。此時,在將切換手段35設為通液路徑之熱回收中,在儲槽42中,儲留有來自供水源之較低溫的冷卻水。因此,之後將切換手段35作為循環路徑而停止熱回收之際,首先可使儲槽42內之比較的低溫的冷卻水在熱回收用熱交換器16循環。藉此,可抑制以切換手段35進行切換時之冷卻水的溫度變化。 However, in this embodiment, as described above, the inlet path 32 is provided at the connection portion of the return path 34 or downstream of the connection portion, and a cooling water storage tank 42 is provided. At this time, in the heat recovery in which the switching means 35 is a liquid-passing path, the storage tank 42 stores lower-temperature cooling water from a water supply source. Therefore, when the heat recovery is stopped using the switching means 35 as a circulation path, the comparatively low-temperature cooling water in the storage tank 42 can first be circulated in the heat recovery heat exchanger 16. This makes it possible to suppress a change in the temperature of the cooling water when switching is performed by the switching means 35.

接著,針對本實施例之熱回收系統2的變形例加以說明。首先,散熱器38之設置位置係只要在循環路徑內,則無特別限定。例如,在前述實施例中,散熱器38係設置在入口路徑32(比與回送路徑34之連接部位更下游側之入口路徑32),但亦可設置在出口路徑33(比與回送路徑34之連接部位更上游側之出口路徑33)或回送路徑34。然而,再將散熱器38設置在入口路徑32時,如前所述,在通液路徑中,以供水溫度與外氣溫度之關係進行冷 卻水之預熱。另一方面,在將散熱器38設置在出口路徑33或回送路徑34之情形時,於通液路徑中,不論供水溫度或外氣溫度為何,預先使散熱器38之風扇38A停止即可。在此情形下,供水溫度感測器或外氣溫度感測器之設置係可予以省略。此外,在將散熱器38設置在任一位置之情形時,亦在循環路徑中使散熱器38之風扇38A動作。 Next, a modification of the heat recovery system 2 of this embodiment will be described. First, the installation position of the radiator 38 is not particularly limited as long as it is within the circulation path. For example, in the foregoing embodiment, the radiator 38 is provided on the inlet path 32 (the inlet path 32 on the downstream side than the connection portion with the return path 34), but may be provided on the outlet path 33 (than the return path 34). The connection point is further upstream from the exit path 33) or the return path 34. However, when the radiator 38 is installed in the inlet path 32, as described above, in the liquid-passing path, the cooling is performed according to the relationship between the water supply temperature and the outside air temperature. But the water is warming up. On the other hand, when the radiator 38 is provided in the outlet path 33 or the return path 34, in the liquid flow path, the fan 38A of the radiator 38 may be stopped in advance regardless of the water supply temperature or the outside air temperature. In this case, the arrangement of the water supply temperature sensor or the outside air temperature sensor may be omitted. In addition, when the radiator 38 is installed at any position, the fan 38A of the radiator 38 is also operated in the circulation path.

此外,切換手段35係只要可在通液路徑及循環路徑切換冷卻水之流動,則無特別限定,例如亦可由設置在出口路徑33與回送路徑34之連接部位的三方閥、或設置在入口路徑32與回送路徑34之連接部位的三方閥所構成。 In addition, the switching means 35 is not particularly limited as long as the cooling water flow can be switched between the liquid-passing path and the circulation path. For example, the switching means 35 may be a three-way valve provided at a connection portion between the outlet path 33 and the return path 34, or an inlet path 32 is a three-way valve connected to the return path 34.

再者,在前述實施例中,在使冷卻水通過後冷卻器5之後,雖通過水冷卻器6,但依情況亦可在通過水冷卻器6之後,通過後冷卻器5。然而,先通過後冷卻器5者係具有下述優點:在可確實地進行壓縮空氣之冷卻之情形下,可更進一步地以水冷卻器6使藉由上述方式加溫過之冷卻水升溫。 Furthermore, in the foregoing embodiment, the cooling water is passed through the aftercooler 5 and then passed through the water cooler 6, but it may be passed through the aftercooler 5 after passing through the water cooler 6 as appropriate. However, passing the aftercooler 5 first has the advantage that, when the compressed air can be reliably cooled, the water cooler 6 can further increase the temperature of the cooling water heated in the above-mentioned manner.

再者,在前述實施例中,在使冷卻水串聯地通過作為熱回收用熱交換器16之後冷卻器5及水冷卻器6,亦可依情況並聯地通過。亦即,在入口路徑32之下游中,使冷卻水分為二邊,使一方通過後冷卻器5,並使另一方通過水冷卻器6之後,並使之合流而通過出口路徑33。 Furthermore, in the aforementioned embodiment, after passing the cooling water in series as the heat recovery heat exchanger 16, the cooler 5 and the water cooler 6 may pass in parallel as appropriate. That is, downstream of the inlet path 32, the cooling water is made to have two sides, and one side passes through the aftercooler 5 and the other side passes through the water cooler 6, and then merges and passes through the outlet path 33.

此外,在前述實施例中,雖將後冷卻器5與水冷卻器6之雙方設為熱回收用熱交換器16,但依情況亦 可將任一方作為熱回收用熱交換器16。例如,亦可僅將後冷卻器5作為熱回收用熱交換器16,並且使來自入口路徑32之冷卻水通過後冷卻器5,且從出口路徑33導出。此時,水冷卻器6係藉由其他手段(例如以風扇進行之通風),來冷卻來自預分離器4之分離水。相反地,僅將水冷卻器6作為熱回收用熱交換器16,並使來自入口路徑32之冷卻水通過水冷卻器6,且從出口路徑33導出。此時,後冷卻器5係藉由其他手段(例如以風扇進行之通風),來冷卻來自壓縮機3之壓縮空氣即可。 In addition, in the foregoing embodiment, although both the after cooler 5 and the water cooler 6 are set as the heat recovery heat exchanger 16, it may be Either one can be used as the heat recovery heat exchanger 16. For example, only the aftercooler 5 may be used as the heat recovery heat exchanger 16, and the cooling water from the inlet path 32 may pass through the aftercooler 5 and be led out from the outlet path 33. At this time, the water cooler 6 cools the separated water from the pre-separator 4 by other means (for example, ventilation by a fan). In contrast, only the water cooler 6 is used as the heat recovery heat exchanger 16, and the cooling water from the inlet path 32 passes through the water cooler 6 and is led out from the outlet path 33. At this time, the aftercooler 5 may cool the compressed air from the compressor 3 by other means (for example, ventilation by a fan).

再者,在前述實施例中,亦可在冷卻水於通液路徑之通水中,依據出水溫度感測器43之檢測溫度來調整熱回收閥36之開度,且依據出水溫度感測器43之檢測溫度對泵40進行反相器控制,並將出水溫度控制成一定。或是,依情況省略該出水溫度一定控制之實施。 Furthermore, in the foregoing embodiment, the opening degree of the heat recovery valve 36 can also be adjusted according to the detection temperature of the outlet temperature sensor 43 in the cooling water in the through water of the liquid flow path, and according to the outlet temperature sensor 43 The detected temperature is controlled by the inverter of the pump 40, and the outlet temperature is controlled to be constant. Or, the implementation of the certain control of the outlet water temperature is omitted according to the situation.

再者,在前述實施例中,雖使水通過熱回收用熱交換器16,但如前所述使水以外之液體通過。亦即,熱回收用熱交換器16係在將壓縮空氣或添加水予以冷卻之際,並不限定於水冷式,亦可作為利用其他液體之液冷式。 Furthermore, in the aforementioned embodiment, although water was passed through the heat recovery heat exchanger 16, liquids other than water were passed through as described above. That is, the heat recovery heat exchanger 16 is not limited to a water-cooled type when cooling compressed air or added water, and may be a liquid-cooled type using another liquid.

再者,在以熱回收用熱交換器16進行熱回收而製造溫水之際,在前述實施例中,雖使水(冷卻水)通過熱回收用熱交換器16,但亦可如下述方式構成。亦即,亦可在熱回收用熱交換器16與其他熱交換器(以下,稱為通水加溫用熱交換器)之間,使例如乙二醇等不凍液或水循 環,並且以熱回收用熱交換器16對該循環液及壓縮空氣等進行熱交換,另一方面,在通水加溫用熱交換器中對前述循環液及通水進行熱交換,且在通水加溫用熱交換器中對通水進行加溫以製造溫水。 In addition, in the case where warm water is produced by performing heat recovery by the heat recovery heat exchanger 16, although water (cooling water) is passed through the heat recovery heat exchanger 16 in the foregoing embodiment, the following method may be used. Make up. That is, between the heat recovery heat exchanger 16 and another heat exchanger (hereinafter referred to as a heat exchanger for water heating), an antifreeze or water such as ethylene glycol may be circulated. And heat exchange between the circulating liquid and compressed air in the heat recovery heat exchanger 16; on the other hand, the circulating liquid and the passing water are heat exchanged in the heat exchanger for water heating, and The through-water heating heat exchanger heats the through-water to produce warm water.

本發明之空氣壓縮系統1並不限定於前述實施例(包含變形例)之構成(包含控制),亦可適當地變更。特別是,只要具備下述構件,則其他構成並無特別限定:(a)水添加式之壓縮機3;(b)預分離器4,將來自壓縮機3之送出流體予以氣水分離;後冷卻器5,對由預分離器4氣水分離後之壓縮空氣予以冷卻;水冷卻器6,對由預分離器4氣水分離後之分離水予以冷卻;分離器槽7,供給通過各冷卻器5、6後之壓縮空氣及分離水,且在氣相部連接有壓縮空氣之送出路徑17,另一方面在液相部連接有朝壓縮機3之添加水返回路徑11。 The air compression system 1 of the present invention is not limited to the configuration (including control) of the aforementioned embodiment (including the modification), and may be appropriately changed. In particular, the other components are not particularly limited as long as the following components are provided: (a) a water-adding compressor 3; (b) a pre-separator 4 that separates the fluid sent from the compressor 3 by gas-water separation; The cooler 5 cools the compressed air separated by the air-water separation by the pre-separator 4; the water cooler 6 cools the separated water separated by the air-water separation by the pre-separator 4; the separator tank 7 is supplied through each cooling The compressed air and separated water after the devices 5 and 6 are connected to the compressed air sending path 17 in the gas phase part, and the added water return path 11 to the compressor 3 is connected to the liquid phase part.

例如,在前述實施例中,雖在後冷卻器5及水冷卻器6中,成為謀求熱回收之構成,但這並非必要者。亦即,後冷卻器5係只要可冷卻壓縮空氣即可,並無特別限定該構成,亦可為例如空冷式(以風扇進行之冷卻)。同樣地,水冷卻器6係可冷卻分離水,該構成並無特別限定,例如亦可為空冷式(以風扇進行之冷卻)。 For example, in the foregoing embodiment, the after-cooler 5 and the water cooler 6 have a structure for recovering heat, but this is not necessary. That is, the after-cooler 5 is only required to be capable of cooling compressed air, and the structure is not particularly limited, and may be, for example, an air-cooled type (cooling by a fan). Similarly, the water cooler 6 is capable of cooling and separating water, and the structure is not particularly limited. For example, the water cooler 6 may be an air cooling type (cooling by a fan).

或者,即使後冷卻器5及/或水冷卻器6為液冷式(典型來說為水冷式),亦可在例如冷卻塔或冷卻器之液冷卻裝置之間使液體循環。亦即,在前述實施例中,亦可僅作為循環路徑之構成,在後冷卻器5或水冷卻器6、 與散熱器38之間,使冷卻水循環。再者,與此相反地,在前述實施例中,亦可省略回送路徑34之設置,作為僅通液路徑之構成。 Alternatively, even if the after cooler 5 and / or the water cooler 6 are liquid-cooled (typically, water-cooled), liquid can be circulated between liquid cooling devices such as a cooling tower or a cooler. That is, in the foregoing embodiment, it may be used only as a configuration of the circulation path. In the after cooler 5 or the water cooler 6, Cooling water is circulated between the radiator 38 and the radiator 38. In addition, on the contrary, in the foregoing embodiment, the arrangement of the return path 34 may be omitted as a configuration of only the liquid-passing path.

附加在本發明之空氣壓縮系統1之熱回收系統2亦可適當地利用在前述實施例中例示之蒸氣鍋爐的供水予熱以外的用途。例如,亦可將在熱回收系統2中製造之溫水利用作為工廠或事業所之空調,亦可利用在各種製造程式中之保溫或洗淨等。 The heat recovery system 2 added to the air compression system 1 of the present invention can also suitably use applications other than water supply preheating of the steam boiler exemplified in the foregoing embodiment. For example, the warm water produced in the heat recovery system 2 may be used as an air conditioner in a factory or an office, and may also be used for heat preservation or cleaning in various manufacturing processes.

1‧‧‧空氣壓縮系統 1‧‧‧air compression system

2‧‧‧熱回收系統 2‧‧‧Heat Recovery System

3‧‧‧壓縮機 3‧‧‧compressor

4‧‧‧預分離器 4‧‧‧ pre-separator

5‧‧‧後冷卻器 5‧‧‧ after cooler

6‧‧‧水冷卻器 6‧‧‧ water cooler

7‧‧‧分離器槽 7‧‧‧ separator tank

8‧‧‧電動馬達 8‧‧‧ Electric motor

9‧‧‧空氣過濾器 9‧‧‧air filter

10‧‧‧吸入路徑 10‧‧‧ Suction path

11‧‧‧添加水返回路徑 11‧‧‧Add water return path

12‧‧‧送出路徑 12‧‧‧Submission route

13‧‧‧止回閥 13‧‧‧Check valve

14‧‧‧氣相連通路徑 14‧‧‧ gas phase communication path

15‧‧‧液相連通路徑 15‧‧‧Liquid phase communication path

16‧‧‧熱回收用熱交換器 16‧‧‧Heat recovery heat exchanger

17‧‧‧壓縮空氣送出路徑 17‧‧‧Compressed air delivery path

18‧‧‧一次壓調整閥 18‧‧‧ primary pressure regulating valve

19‧‧‧止回閥 19‧‧‧ check valve

20‧‧‧安全閥 20‧‧‧Safety valve

21‧‧‧放氣閥 21‧‧‧ air release valve

22‧‧‧添加水閥 22‧‧‧Add water valve

23‧‧‧濾水器 23‧‧‧ Water Filter

24‧‧‧供水路徑 24‧‧‧ Water supply route

24A‧‧‧第一供水路徑 24A‧‧‧First water supply route

24B‧‧‧第二供水路徑 24B‧‧‧Second Water Supply Path

25‧‧‧排水路徑 25‧‧‧ drainage path

26‧‧‧第一供水閥 26‧‧‧The first water supply valve

27‧‧‧止回閥 27‧‧‧Check valve

28‧‧‧第二供水閥 28‧‧‧Second water supply valve

29‧‧‧排水閥 29‧‧‧Drain valve

30‧‧‧水位檢測器 30‧‧‧Water Level Detector

31‧‧‧壓力感測器 31‧‧‧Pressure sensor

32‧‧‧入口路徑 32‧‧‧ entrance path

33‧‧‧出口路徑 33‧‧‧ Exit route

34‧‧‧回送路徑 34‧‧‧ loopback path

35‧‧‧切換手段 35‧‧‧ Switching means

36‧‧‧熱回收閥 36‧‧‧Heat Recovery Valve

37‧‧‧回送閥 37‧‧‧ return valve

38‧‧‧散熱器 38‧‧‧ Radiator

38A‧‧‧風扇 38A‧‧‧fan

39‧‧‧連絡路徑 39‧‧‧Contact Path

40‧‧‧泵 40‧‧‧ pump

41‧‧‧止回閥 41‧‧‧Check valve

42‧‧‧儲槽 42‧‧‧ storage tank

43‧‧‧出水溫度感測器 43‧‧‧Outlet water temperature sensor

Claims (4)

一種空氣壓縮系統,具備:水添加式之壓縮機;預分離器,將來自該壓縮機之送出流體予以氣水分離;後冷卻器,對由該預分離器氣水分離後之壓縮空氣予以冷卻;水冷卻器,對由前述預分離器氣水分離後之分離水予以冷卻;分離器槽,供給通過前述各冷卻器後之壓縮空氣及分離水,且在氣相部連接有壓縮空氣之送出路徑,另一方面在液相部連接有朝前述壓縮機之添加水的返回路徑。 An air compression system includes: a water-adding compressor; a pre-separator that separates the fluid sent from the compressor for gas-water separation; and an after-cooler that cools the compressed air that is separated by the pre-separator from gas-water separation Water cooler, which cools the separated water separated by the aforementioned pre-separator; the separator tank supplies compressed air and separated water after passing through the aforementioned coolers, and the compressed air is connected to the gas phase. On the other hand, the liquid phase portion is connected to a return path for adding water to the compressor. 如申請專利範圍第1項所述之空氣壓縮系統,其中,前述後冷卻器為壓縮空氣與冷卻水之熱交換器,前述水冷卻器為分離水與冷卻水之熱交換器,在前述各冷卻器中將前述冷卻水予以加溫以製造溫水。 The air compression system according to item 1 of the scope of patent application, wherein the after cooler is a heat exchanger for compressed air and cooling water, and the water cooler is a heat exchanger for separating water and cooling water. The aforementioned cooling water is heated in a vessel to produce warm water. 如申請專利範圍第2項所述之空氣壓縮系統,其中,前述冷卻水係在通過前述後冷卻器之後,通過前述水冷卻器。 The air compression system according to item 2 of the scope of patent application, wherein the cooling water passes through the water cooler after passing through the after cooler. 如申請專利範圍第1項至第3項中任一項所述之空氣壓縮系統,其中,在來自前述分離器槽之壓縮空氣的送出路徑中,設置有用以將前述分離器槽內保持在設定壓力以上之一次壓調整閥。 The air compression system according to any one of claims 1 to 3, wherein the compressed air from the separator tank is provided with a path for keeping the inside of the separator tank at a set position. Primary pressure adjustment valve above pressure.
TW106119056A 2016-08-08 2017-06-08 Air compressor system TWI633238B (en)

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