TWM562297U - Water purification system - Google Patents
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- TWM562297U TWM562297U TW107202982U TW107202982U TWM562297U TW M562297 U TWM562297 U TW M562297U TW 107202982 U TW107202982 U TW 107202982U TW 107202982 U TW107202982 U TW 107202982U TW M562297 U TWM562297 U TW M562297U
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Abstract
本創作有關於一種水質淨化系統。此水質淨化系統包含進水管、沉澱槽、淨化槽、出流槽與出水管,其中進水管係連通沉澱槽,淨化槽設置於沉澱槽與出流槽之間,且出水管係連通出流槽。前述之淨化槽包含曝氣區、水生植物區與濾料區,且水生植物區設置於曝氣區與濾料區之間。曝氣區係藉由入流管連通沉澱槽,且濾料區藉由出流管連通出流槽。入流管之兩連通端分別鄰近於沉澱槽之槽頂與淨化槽之槽頂。出流管之兩連通端分別鄰近於淨化槽之槽底與出流槽之槽底。 This creation is about a water purification system. The water purification system comprises an inlet pipe, a sedimentation tank, a purification tank, an outlet tank and an outlet pipe, wherein the inlet pipe is connected to the sedimentation tank, the purification tank is disposed between the sedimentation tank and the outlet tank, and the outlet pipe is connected to the outlet tank . The foregoing purification tank comprises an aeration zone, an aquatic plant zone and a filter zone, and the aquatic plant zone is disposed between the aeration zone and the filter zone. The aeration zone is connected to the sedimentation tank by the inflow pipe, and the filter material zone is connected to the outflow channel by the outlet pipe. The two communicating ends of the inflow pipe are respectively adjacent to the trough top of the sedimentation trough and the trough top of the purifying trough. The two communicating ends of the outlet pipe are respectively adjacent to the bottom of the septic tank and the bottom of the trough.
Description
本創作係有關一種水質淨化系統,特別是提供一種含有水生植物之間歇曝氣水質淨化系統。 This creation relates to a water purification system, in particular to an intermittent aeration water purification system containing aquatic plants.
根據聯合國環境署(United Nations Environment Programme)之研究,若2025年未提出水資源之解決方案時,全球每3人即有2人會感覺到缺水的壓力,故亟需開拓多元之水資源。其中,水資源之回收更為增加水資源的主要管道之一。據此,對於回收水資源之淨化係急欲發展之目標。為了降低對環境之衝擊與滿足永續發展之概念,生態處理系統(Ecological Treatment System)之水資源回收方法係被提出。 According to the United Nations Environment Programme, if no water solutions are proposed in 2025, two out of every three people in the world will feel the pressure of water shortage, so it is urgent to develop diversified water resources. Among them, the recycling of water resources is one of the main channels for increasing water resources. Accordingly, the purification of recycled water resources is an urgent development goal. In order to reduce the impact on the environment and meet the concept of sustainable development, the ecological treatment system (Ecological Treatment System) water recycling method was proposed.
生態處理系統對於汙染物的去除機制主要包含沉澱、吸附、過濾、硝化、脫硝、植物吸收及生物轉化等部分。雖然生態處理系統可有效去除水中汙染物,但生態處理系統中之各處理機制於不同之汙染環境具有不同之除汙效能,故難以使生態處理系統可應用於各種汙染環境。 The removal mechanism of pollutants in the ecological treatment system mainly includes sedimentation, adsorption, filtration, nitrification, denitrification, plant absorption and biotransformation. Although the ecological treatment system can effectively remove pollutants in water, the various treatment mechanisms in the ecological treatment system have different decontamination effects in different polluted environments, so it is difficult to make the ecological treatment system applicable to various polluted environments.
一般而言,當汙染物進入生態處理系統時,生態處理系統主要係以袪氧作用去除有機汙染物,而含氮污染 物之主要去除機制係以氨氣化(Volatilization)、硝化(Nitrification)及脫氮(Denitrification)等機制將汙水中的含氮汙染物之氮轉換成氮氣。然而,當硝化作用不完全時,脫氮作用則無法完全將水中含氮汙染物轉化為氮氣。因此,為確保硝化可完全作用,水中之溶氧量須高於限制濃度。其中,雖然水中之溶氧量可藉由增設曝氣裝置來提升,但曝氣裝置所產生之噴流氣泡會擾亂處理槽內之流場,而降低系統對汙染物之去除效率。此外,上述曝氣設備雖可提升系統水環境之溶氧量,但高溶氧卻會抑制脫硝作用之進行,而干擾水中含氮汙染物轉化為氮氣,進而降低含氮汙染物之去除效率。 In general, when pollutants enter the ecological treatment system, the ecological treatment system mainly removes organic pollutants by oxygenation, and nitrogenous pollution The main removal mechanism of the substance is to convert the nitrogen of the nitrogenous pollutants in the sewage into nitrogen by means of a mechanism such as ammonia gasification (Volatilization), nitrification and denitrification. However, when nitrification is incomplete, denitrification does not completely convert nitrogen-containing contaminants in the water to nitrogen. Therefore, in order to ensure that the nitrification is fully effective, the amount of dissolved oxygen in the water must be higher than the limiting concentration. Among them, although the amount of dissolved oxygen in the water can be increased by adding an aeration device, the jet bubbles generated by the aeration device disturb the flow field in the treatment tank and reduce the removal efficiency of the pollutants by the system. In addition, although the above aeration equipment can increase the dissolved oxygen content of the system water environment, high dissolved oxygen can inhibit the denitration, and the nitrogen-containing pollutants in the water are converted into nitrogen, thereby reducing the removal efficiency of the nitrogen-containing pollutants. .
另外,於水產養殖業之發展中,一般係藉由硝化作用將對養殖標的具高毒性之氨氮轉化為不具毒性之硝酸鹽氮。然而,於室外養殖場中,高濃度之硝酸鹽氮有助於藻類之增生,而易導致水質惡化。為了避免藻類之增生,一般業者係投入水質控制用藥,但養殖標的之品質則連帶被減損,而降低其經濟價值。 In addition, in the development of aquaculture, the highly toxic ammonia nitrogen of the culture standard is generally converted into non-toxic nitrate nitrogen by nitrification. However, in outdoor farms, high concentrations of nitrate nitrogen contribute to the proliferation of algae, which can easily lead to deterioration of water quality. In order to avoid the proliferation of algae, the general industry is investing in water quality control drugs, but the quality of the breeding standard is degraded, which reduces its economic value.
有鑑於此,亟須提供一種水質淨化系統,以有效去除水中汙染物,並改進習知水質淨化系統之缺陷。 In view of this, it is not necessary to provide a water purification system to effectively remove contaminants from water and to improve the defects of conventional water purification systems.
因此,本創作之一態樣是在提供水質淨化系統,藉由劃分為曝氣區、水生植物區與濾料區之淨化槽,此 水質淨化系統可有效降低水中之有機汙染、營養鹽及/或懸浮固體物等汙染物質。 Therefore, one aspect of this creation is to provide a water purification system, which is divided into a septic tank divided into an aeration zone, an aquatic plant zone and a filter zone. The water purification system can effectively reduce pollutants such as organic pollution, nutrients and/or suspended solids in the water.
根據本創作之一態樣,提出一種水質淨化系統。此水質淨化系統包含進水管、沉澱槽、淨化槽、出流槽與出水管。進水管係配置以輸入汙水至沉澱槽中,且出水管係配置以由出流槽輸出已處理水。淨化槽係設置於沉澱槽與出流槽之間,且淨化槽包含曝氣區、水生植物區與濾料區,其中水生植物區係相鄰且設於曝氣區與濾料區之間。 According to one aspect of this creation, a water purification system is proposed. The water purification system includes an inlet pipe, a sedimentation tank, a purification tank, an outflow tank, and an outlet pipe. The inlet pipe is configured to input sewage into the sedimentation tank, and the outlet pipe is configured to output treated water from the outflow tank. The purification tank is disposed between the sedimentation tank and the outlet tank, and the purification tank comprises an aeration zone, an aquatic plant zone and a filter material zone, wherein the aquatic plant flora is adjacent and disposed between the aeration zone and the filter zone.
曝氣區係藉由入流管連通沉澱槽,且濾料區係藉由出流管連通出流槽。其中,入流管之兩連通端分別鄰近於沉澱槽之槽頂與淨化槽之槽頂,且濾料區之兩連通端分別鄰近於淨化槽之槽底與出流槽之槽底。 The aeration zone is connected to the sedimentation tank by the inlet pipe, and the filter zone is connected to the outflow channel by the outlet pipe. The two communicating ends of the inflow tube are respectively adjacent to the top of the trough of the precipitating tank and the top of the trough of the purifying tank, and the two communicating ends of the filter material area are respectively adjacent to the bottom of the trough of the purifying tank and the bottom of the trough of the outflow trough.
依據本創作之一實施例,前述之沉澱槽包含覆蓋沉澱槽之隔熱板。 According to an embodiment of the present invention, the foregoing precipitation tank comprises a heat insulation panel covering the precipitation tank.
依據本創作之另一實施例,沉澱槽包含排泥管,且此排泥管設於沉澱槽之槽底。 According to another embodiment of the present invention, the settling tank comprises a drain pipe, and the drain pipe is disposed at the bottom of the tank of the sedimentation tank.
依據本創作之又一實施例,前述之沉澱槽包含液位偵測器。 According to still another embodiment of the present invention, the foregoing precipitation tank includes a liquid level detector.
依據本創作之再一實施例,前述之曝氣區設有整流結構,且此整流結構係相鄰於水生植物區。 According to still another embodiment of the present invention, the aeration zone is provided with a rectifying structure, and the rectifying structure is adjacent to the aquatic plant zone.
依據本創作之又另一實施例,前述之曝氣區包含複數個接觸材。 According to still another embodiment of the present invention, the aeration zone comprises a plurality of contact materials.
依據本創作之再另一實施例,前述之水生植物區包含挺水性植物。 According to still another embodiment of the present invention, the aforementioned aquatic plant area comprises a water-saturated plant.
依據本創作之更另一實施例,前述之濾料區包含複數個過濾材料。 According to still another embodiment of the present invention, the filter media zone comprises a plurality of filter materials.
依據本創作之更另一實施例,前述之出流槽包含至少一個散氣盤。 According to still another embodiment of the present invention, the aforementioned outflow trough comprises at least one diffuser disk.
依據本創作之更另一實施例,前述之出流管設有一控制閥門。 According to still another embodiment of the present invention, the aforementioned outlet pipe is provided with a control valve.
應用本創作之水質淨化系統,藉由結合沉澱槽、淨化槽與出流槽,並將淨化槽劃分為曝氣區、水生植物區與濾料區,汙水中之有機汙染、含氮汙染物(例如:氨氮、亞硝酸鹽氮、硝酸鹽氮與總凱氏氮)、含磷汙染物和懸浮固體物等汙染物質可有效地被去除分離,而淨化水質,並減少水質控制用藥之投加,進而降低水處理成本。 The water purification system of the present application is combined with the sedimentation tank, the purification tank and the outflow tank, and the purification tank is divided into an aeration zone, an aquatic plant zone and a filter material zone, and organic pollution and nitrogen-containing pollutants in the sewage ( For example: ammonia nitrogen, nitrite nitrogen, nitrate nitrogen and total Kjeldahl nitrogen), phosphorus-containing pollutants and suspended solids can be effectively removed and separated to purify water and reduce the dosage of water quality control drugs. In turn, the cost of water treatment is reduced.
100‧‧‧水質淨化系統 100‧‧‧Water purification system
100a‧‧‧進水管 100a‧‧‧ water inlet
100b‧‧‧出水管 100b‧‧‧Outlet
110‧‧‧沉澱槽 110‧‧‧Sedimentation tank
110a‧‧‧排泥管 110a‧‧‧Drain pipe
111‧‧‧導水隔板 111‧‧‧Water guide
120‧‧‧淨化槽 120‧‧‧Septic tank
121‧‧‧曝氣區 121‧‧‧Aeration zone
121a‧‧‧入流管 121a‧‧‧ Inflow tube
121b‧‧‧整流結構 121b‧‧‧Rectification structure
121c‧‧‧蓋體 121c‧‧‧ cover
122‧‧‧水生植物區 122‧‧‧Aquatic plant area
122b‧‧‧挺水性植物 122b‧‧‧ very waterborne plants
123‧‧‧濾料區 123‧‧‧Filter material area
123a‧‧‧出流管 123a‧‧‧ Outflow tube
123b‧‧‧過濾材料 123b‧‧‧Filter materials
130‧‧‧出流槽 130‧‧‧ outflow trough
為了對本創作之實施例及其優點有更完整之理解,現請參照以下之說明並配合相應之圖式。必須強調的是,各種特徵並非依比例描繪且僅係為了圖解目的。相關圖式內容說明如下。 In order to have a more complete understanding of the embodiments of the present invention and its advantages, reference is now made to the following description in conjunction with the corresponding drawings. It must be emphasized that the various features are not drawn to scale and are for illustrative purposes only. The relevant schema description is as follows.
〔圖1〕係繪示依照本創作之一實施例之水質淨化系統的示意圖。 Fig. 1 is a schematic view showing a water purification system according to an embodiment of the present invention.
以下仔細討論本創作實施例之製造和使用。然而,可以理解的是,實施例提供許多可應用的創作概念,其 可實施於各式各樣的特定內容中。所討論之特定實施例僅供說明,並非用以限定本創作之範圍。 The manufacture and use of the present creative embodiment is discussed in detail below. However, it will be appreciated that embodiments provide many applicable creative concepts, Can be implemented in a wide variety of specific content. The specific embodiments discussed are for illustrative purposes only and are not intended to limit the scope of the present invention.
請參照圖1,其係繪示依照本創作之一實施例之水質淨化系統的示意圖。水質淨化系統100包含進水管100a、沉澱槽110、淨化槽120、出流槽130與出水管100b,其中淨化槽120係設置於沉澱槽110與出流槽130之間。沉澱槽110藉由入流管121a連通淨化槽120,且淨化槽120藉由出流管123a連通出流槽130。其中,入流管121a之兩端的連通位置(即管與槽之連通位置)分別鄰近於沉澱槽110之槽頂與淨化槽120之槽頂,且出流管123a之兩端的連通位置分別鄰近於淨化槽120之槽底與出流槽130之槽底。 Please refer to FIG. 1 , which is a schematic diagram of a water purification system according to an embodiment of the present invention. The water purification system 100 includes an inlet pipe 100a, a sedimentation tank 110, a purification tank 120, an outflow tank 130, and an outlet pipe 100b. The purification tank 120 is disposed between the sedimentation tank 110 and the outlet tank 130. The sedimentation tank 110 communicates with the purification tank 120 through the inlet pipe 121a, and the purification tank 120 communicates with the outlet tank 130 through the outlet pipe 123a. The communication position of the two ends of the inlet pipe 121a (ie, the communication position between the pipe and the groove) is adjacent to the groove top of the sedimentation tank 110 and the top of the tank of the purification tank 120, and the communication positions of the two ends of the outlet pipe 123a are respectively adjacent to the purification. The bottom of the groove of the groove 120 and the bottom of the groove of the outflow groove 130.
進水管100a係配置以輸入汙水至沉澱槽110中。在一些實施例中,進水管100a係連接汙水儲存槽。在一些實施例中,進水管100a可連接輸水泵浦,以將汙水泵送至沉澱槽110中。在一些實施例中,沉澱槽110可為前述之汙水儲存槽,且進水管100a係直接及/或間接連接排出汙水之系統、元件及/或處所。 The inlet pipe 100a is configured to input sewage into the sedimentation tank 110. In some embodiments, the inlet pipe 100a is connected to a sewage storage tank. In some embodiments, the inlet pipe 100a can be connected to a water pump to pump sewage into the settling tank 110. In some embodiments, the settling tank 110 can be the aforementioned sewage storage tank, and the inlet pipe 100a is a system, component, and/or location that directly and/or indirectly connects the discharged sewage.
沉澱槽110可包含排泥管110a與111導水隔板,且排泥管110a係設置於沉澱槽110之槽底。當汙水排放至沉澱槽110時,汙水中之懸浮固體可沉降於沉澱槽110之槽底。當槽底之懸浮固體累積至預定量時,此些懸浮固體可經由排泥管110a排出沉澱槽,而使沉澱槽110之汙水容納量可回復至初始之水準。在一些實施例中,沉澱槽110之槽底可包含有助於收集懸浮固體之結構及/或裝置,以加速懸浮 固體之沉降速率,而可提升汙水於沉澱槽110中之澄清速率。導水隔板111設於進水管100a與入流管121a間,並靠近進水管100a。導水隔板111係配置以導水向下,以增加水力效率,並降低短流現象,而可增加沉澱效率。在一些實施例中,導水隔板111可以適當之方式固定於沉澱槽110中。惟須說明的是,導水隔板111之固定結構(例如:固定架)不阻礙汙水中之懸浮固體的沉降,亦不造成短流現象。另外,導水隔板111沒入汙水槽110之汙水的深度可依據所欲達成之沉澱效率來調整。 The sedimentation tank 110 may include drain pipes 110a and 111, and the drain pipe 110a is disposed at the bottom of the sedimentation tank 110. When the sewage is discharged to the sedimentation tank 110, the suspended solids in the sewage may settle at the bottom of the tank of the sedimentation tank 110. When the suspended solids at the bottom of the tank accumulate to a predetermined amount, the suspended solids can be discharged through the sludge discharge pipe 110a, and the sewage capacity of the sedimentation tank 110 can be restored to the initial level. In some embodiments, the bottom of the sedimentation tank 110 may include structures and/or devices that facilitate the collection of suspended solids to accelerate suspension. The rate of solidification of the solids increases the rate of clarification of the sewage in the settling tank 110. The water guiding partition 111 is provided between the inlet pipe 100a and the inlet pipe 121a and is adjacent to the inlet pipe 100a. The water guiding partition 111 is configured to conduct water downward to increase hydraulic efficiency and reduce short-flow phenomenon, thereby increasing precipitation efficiency. In some embodiments, the water deflector 111 can be secured in the settling tank 110 in a suitable manner. It should be noted that the fixed structure of the water guiding partition 111 (for example, the fixing frame) does not hinder the sedimentation of suspended solids in the sewage, nor does it cause a short flow phenomenon. In addition, the depth of the sewage in which the water guiding partition 111 is not admitted to the sewage tank 110 can be adjusted according to the desired precipitation efficiency.
在一些實施例中,沉澱槽110可包含隔熱板(為繪示),且隔熱板係覆蓋沉澱槽110,以避免日光直射沉澱槽110,而可降低汙水溫度,以避免汙水之優養化現象更趨嚴重,進而可抑制汙水所散發之惡臭氣味。 In some embodiments, the precipitation tank 110 may include a heat shield (shown), and the heat shield covers the sedimentation tank 110 to prevent direct sunlight from the sedimentation tank 110, and the sewage temperature may be lowered to avoid sewage. The phenomenon of eutrophication is more serious, which in turn can suppress the foul odor emitted by sewage.
在一些實施例中,沉澱槽110可包含液位偵測器,且此液位偵測器可將訊號傳送至進水管100a之閥門開關,以開啟或關閉閥門,而可允許或禁止汙水之泵送。其中,當液位偵測器所偵測之汙水液位低於前述入流管121a之連通位置時,液位偵測器可傳輸「開啟」之訊號至閥門開關,以允許汙水經由進水管100a被泵送至沉澱槽110中;當液位偵測器所偵測之汙水液位不低於所設定之最高液位時,液位偵測器可傳輸「關閉」之訊號至閥門開關,以禁止汙水之泵送。 In some embodiments, the precipitation tank 110 may include a liquid level detector, and the liquid level detector may transmit a signal to the valve switch of the inlet pipe 100a to open or close the valve, and may allow or prohibit the sewage. Pumping. Wherein, when the liquid level detected by the liquid level detector is lower than the connection position of the inlet pipe 121a, the liquid level detector can transmit an "on" signal to the valve switch to allow the sewage to pass through the water inlet pipe. 100a is pumped into the sedimentation tank 110; when the liquid level detected by the liquid level detector is not lower than the set maximum liquid level, the liquid level detector can transmit a "off" signal to the valve switch To prohibit the pumping of sewage.
請繼續參照圖1。淨化槽120包含曝氣區121、水生植物區122與濾料區123,且水生植物區122係相鄰且 設置於曝氣區121與濾料區123之間。曝氣區121係藉由前述之入流管121a連通沉澱槽110,且濾料區123係藉由出流管123a連通出流槽130。其中,汙水係依序流過曝氣區121、水生植物區122與濾料區123。 Please continue to refer to Figure 1. The purification tank 120 includes an aeration zone 121, an aquatic plant zone 122 and a filter zone 123, and the aquatic plant zone 122 is adjacent and It is disposed between the aeration zone 121 and the filter material zone 123. The aeration zone 121 is connected to the sedimentation tank 110 by the aforementioned inlet pipe 121a, and the filter zone 123 is connected to the outflow channel 130 by the outlet pipe 123a. The sewage system flows through the aeration zone 121, the aquatic plant zone 122 and the filter material zone 123 in sequence.
在一些實施例中,曝氣區121可包含複數個高接觸面積之接觸材,而有助於硝化菌滋生。其次,曝氣區121可設有噴流曝氣馬達,以藉由噴出之微細氣泡提升空氣與水之接觸面積,而提升曝氣區121之溶氧效率。如此一來,硝化菌之滋生與溶氧量之提升,曝氣區121有利於進行硝化與生物氧化作用,而可去除汙水中之含氮營養鹽與有機汙染物,進而提升水質。 In some embodiments, the aeration zone 121 may comprise a plurality of contact materials of high contact area to aid in the growth of nitrifying bacteria. Next, the aeration zone 121 may be provided with a jet aeration motor to increase the dissolved oxygen efficiency of the aeration zone 121 by raising the contact area of the air with the water by the microbubbles. In this way, the growth of nitrifying bacteria and the increase of dissolved oxygen, the aeration zone 121 is beneficial for nitrification and biooxidation, and can remove nitrogenous nutrients and organic pollutants in the sewage, thereby improving water quality.
在一些實施例中,曝氣區121可設有整流結構121b。整流結構121b係相鄰於水生植物區122,且曝氣後之汙水可藉由整流結構121b之整流,平穩地流入水生植物區122中。換言之,整流結構121b係設於可使整流後之曝氣水直接流入水生植物區122的位置。在一些實施例中,淨化槽120可選擇性地包含整流區(未繪示)。整流區係相鄰且設於曝氣區121與水生植物區122之間,且前述之整流結構可設於整流區中。在一些具體例中,整流結構121b可為蜂巢式多孔管整流結構、其他適當之整流結構,或此些整流結構之任意組合。 In some embodiments, the aeration zone 121 can be provided with a rectifying structure 121b. The rectifying structure 121b is adjacent to the aquatic plant area 122, and the aerated sewage can be smoothly flowed into the aquatic plant area 122 by rectification by the rectifying structure 121b. In other words, the rectifying structure 121b is disposed at a position where the rectified aeration water can be directly flowed into the aquatic plant area 122. In some embodiments, the septic tank 120 can optionally include a rectification zone (not shown). The rectification zone is adjacent and disposed between the aeration zone 121 and the aquatic plant zone 122, and the aforementioned rectifying structure may be disposed in the rectification zone. In some embodiments, the rectifying structure 121b can be a honeycomb porous tube rectifying structure, other suitable rectifying structures, or any combination of such rectifying structures.
在一些實施例中,曝氣區121可設有蓋體121c,且蓋體121c覆蓋曝氣區121,而可避免日光直接照 射曝氣區121c之汙水,進而避免硝化與氧化作用之效能降低。此外,蓋體121c亦可避免曝氣區121之汙水惡臭飄散。 In some embodiments, the aeration zone 121 may be provided with a cover 121c, and the cover 121c covers the aeration zone 121, and the direct sunlight may be avoided. The sewage in the aeration zone 121c is injected to avoid the decrease in the efficiency of nitrification and oxidation. In addition, the cover body 121c can also prevent the odor of the sewage in the aeration zone 121 from being dispersed.
在一些實施例中,基於淨化槽120之長度(沿著汙水之一水平流動方向)為100%,曝氣區121之長度可為15%至25%。在一具體例中,基於淨化槽120之長度為100%,曝氣區121之長度可為21.5%。 In some embodiments, the length of the aeration zone 121 may be 15% to 25% based on the length of the septic tank 120 (the horizontal flow direction along one of the sewage) is 100%. In a specific example, based on the length of the purification tank 120 being 100%, the length of the aeration zone 121 may be 21.5%.
水生植物區122包含挺水性植物122b,且水生植物區122之槽底具有土壤,以供挺水性植物122b植生。在一些具體例中,挺水性植物122b可包含但不限於蘆葦、燈心草、香蒲、狼尾草、風車草、培地茅、其他適當之挺水性植物,或上述植物之任意混合。 The aquatic plant area 122 comprises a water-stained plant 122b, and the bottom of the aquatic plant area 122 has soil for the water-borne plants 122b to grow. In some embodiments, the water-storing plant 122b can include, but is not limited to, reed, rush, cattail, pennisetum, windmill grass, medusa, other suitable aqueous plants, or any mixture of the above.
於水生植物區122中,其可藉由物理沉降、吸附與過濾等機制去除懸浮固體物、營養鹽與微生物。其中,挺水性植物122b之底部根莖與砂土可藉由有機物之礦化、硝化、脫硝及/或同化等作用機制,去除汙水中之有機物和/或含氮汙染物,並可去除水中之微生物。挺水性植物122b之攝取作用亦可同時去除水中之營養鹽與重金屬。此外,日光之輻射照射與原生動物之掠食可去除病原菌。 In the aquatic plant area 122, suspended solids, nutrients and microorganisms can be removed by mechanisms such as physical sedimentation, adsorption and filtration. Among them, the bottom rhizome and sand of the water-borne plant 122b can remove organic matter and/or nitrogenous pollutants in the sewage by mineralization, nitrification, denitrification and/or assimilation of organic matter, and can remove water. microorganism. The uptake of the aqueous plant 122b can also remove nutrients and heavy metals from the water. In addition, radiation exposure to sunlight and predation of protozoa can remove pathogens.
當前述之曝氣區121設有整流結構121b時,藉由整流結構121b,曝氣區121中擾動之汙水可平穩地流入水生植物區122,而不會翻攪植物122b之根部土壤。其次,藉由整流結構121b之阻隔,曝氣區121中之噴流曝氣馬達所噴出的強勁氣泡流不會影響水生植物區122,而可避免水生植 物區122之汙水形成紊流狀態,進而不降低挺水性植物122b之淨水效果。 When the aeration zone 121 is provided with the rectifying structure 121b, the disturbed sewage in the aeration zone 121 can smoothly flow into the aquatic plant area 122 without reversing the root soil of the plant 122b by the rectifying structure 121b. Secondly, by the barrier of the rectifying structure 121b, the strong bubble flow emitted by the jet aeration motor in the aeration zone 121 does not affect the aquatic plant area 122, and the aquatic planting can be avoided. The sewage in the object area 122 forms a turbulent state, thereby not reducing the water purification effect of the water-storing plant 122b.
在一些實施例中,基於淨化槽120之長度為100%,水生植物區122之長度可為55%至65%。在一具體例中,基於淨化槽120之長度為100%,水生植物區122之長度可為62.4%。 In some embodiments, the length of the aquatic plant area 122 can be from 55% to 65% based on the length of the purification tank 120 being 100%. In one embodiment, the length of the aquatic plant area 122 can be 62.4% based on the length of the purification tank 120 being 100%.
經水生植物區122後,汙水係進一步流入濾料區123中。其中,濾料區123可包含複數個過濾材料123b。在一些實施例中,此些過濾材料123b彼此可堆疊形成具有複雜孔道路徑之過濾塊體。藉由此些孔道路徑,水中殘留之懸浮固體物可被有效地去除分離。在一些具體例中,此些過濾材料123b可包含但不限於礫石、廢磚塊、廢石塊、廢輪胎切片、其他適當之過濾材料,或上述材料之任意混合。在一些實施例中,為了維持前述過濾塊體之外型與過濾材料123b之堆疊穩定度,水生植物區122與濾料區123之間可設有固定網(未繪示)或其他固定裝置,且此固定網或固定裝置不影響水之流動,故流經水生植物區122之水可自由地流入濾料區123中。較佳地,此固定網或固定裝置不對流過之水產生壓力降。 After passing through the aquatic plant area 122, the sewage system further flows into the filter material zone 123. The filter material region 123 may include a plurality of filter materials 123b. In some embodiments, such filter materials 123b may be stacked on each other to form a filter block having a complex channel path. By means of these pore paths, the suspended solids remaining in the water can be effectively removed and separated. In some embodiments, such filter material 123b can include, but is not limited to, gravel, waste bricks, waste rock, waste tire chips, other suitable filter materials, or any combination of the foregoing. In some embodiments, in order to maintain the stacking stability of the filter block and the filter material 123b, a fixed net (not shown) or other fixing device may be disposed between the aquatic plant area 122 and the filter material area 123. Moreover, the fixed net or the fixing device does not affect the flow of water, so the water flowing through the aquatic plant area 122 can freely flow into the filter material area 123. Preferably, the fixed mesh or fixture does not create a pressure drop across the water flowing therethrough.
在一些實施例中,濾料區123之孔隙率可為35%至45%。在一具體例中,濾料區123之孔隙率可為41%。在一些實施例中,淨化槽120之平均孔隙率可為85%至91%。在一具體例中,淨化槽120之孔隙率可為88%。 In some embodiments, the filter zone 123 may have a porosity of from 35% to 45%. In one embodiment, the filter zone 123 may have a porosity of 41%. In some embodiments, the septic tank 120 may have an average porosity of 85% to 91%. In one embodiment, the porosity of the purge tank 120 can be 88%.
在一些實施例中,基於淨化槽120之長度為100%,濾料區123之長度可為10%至20%。在一具體例中,基於淨化槽120之長度為100%,濾料區123之長度可為16.1%。 In some embodiments, the length of the filter media zone 123 can be from 10% to 20% based on the length of the purge tank 120 being 100%. In one embodiment, the length of the filter zone 123 may be 16.1% based on the length of the purge tank 120 being 100%.
在一些實施例中,淨化槽120可選擇性地設有沉水馬達,以滿足曝氣之需求。 In some embodiments, the septic tank 120 can be selectively provided with a submersible motor to meet the needs of aeration.
經濾料區123過濾後之水係經由出流管123a流入出流槽130中。流入出流槽130之水可進一步進行後曝氣處理,以曝氣調整水中之溶氧量,而可滿足後續用水之需求。在一些實施例中,出流槽130可包含至少一散氣盤,以對出流槽130中之水進行曝氣。在一些實施例中,出流槽130可選擇性地包含空氣壓縮泵浦,以進行後曝氣處理。 The water filtered through the filter medium region 123 flows into the outflow tank 130 through the outlet pipe 123a. The water flowing into the outflow tank 130 can be further subjected to a post-aeration treatment to adjust the dissolved oxygen amount in the water by aeration to meet the demand for subsequent water. In some embodiments, the outflow channel 130 can include at least one diffuser disk to aerate water in the outflow channel 130. In some embodiments, the outflow channel 130 can optionally include an air compression pump for post aeration treatment.
為了控制汙水於淨化槽120中之停留時間,出流管123a可設有控制閥門(未繪示)。 In order to control the residence time of the sewage in the purification tank 120, the outlet pipe 123a may be provided with a control valve (not shown).
經後曝氣處理後之已處理水可經由出水管100b從出流槽130流出,而可進一步直接泵送至用水處所,或者泵送至儲水槽,以待使用。在一些實施例中,出水管100b可連接輸水泵浦,而可經由出水管100b泵送已處理水。 The treated water after the post-aeration treatment may flow out of the outflow tank 130 via the outlet pipe 100b, and may be further pumped directly to the water space or pumped to the water storage tank for use. In some embodiments, the outlet pipe 100b can be connected to the water pump and the treated water can be pumped via the outlet pipe 100b.
依據本創作前述之內容及實施例可知,本創作藉由結合沉澱槽、淨化槽與出流槽,並將淨化槽劃分為曝氣區、水生植物區與濾料區,而可有效分離去除水中之有機汙染、營養鹽及/或懸浮固體物等。 According to the foregoing content and examples of the present creation, the present invention can effectively separate and remove water by combining a sedimentation tank, a purification tank and an outflow tank, and dividing the purification tank into an aeration zone, an aquatic plant zone and a filter material zone. Organic pollution, nutrients and/or suspended solids.
其次,本創作之水質淨化系統不須投入水質控制用藥,而可降低處理成本,故有助於養殖漁業之長期發展,並提升其附加價值及養殖標的之品質。 Secondly, the water purification system of this creation does not need to be put into the water quality control medicine, but can reduce the treatment cost, so it contributes to the long-term development of the culture fishery and enhances the added value and the quality of the culture target.
此外,本創作之水質淨化系統不須耗費大量之動力,而可降低水處理之能源成本。 In addition, the water purification system of the present invention does not require a lot of power, but can reduce the energy cost of water treatment.
雖然本創作已以實施方式揭露如上,然其並非用以限定本創作,在本創作所屬技術領域中任何具有通常知識者,在不脫離本創作之精神和範圍內,當可作各種之更動與潤飾,因此本創作之保護範圍當視後附之申請專利範圍所界定者為準。 Although the present invention has been disclosed in the above embodiments, it is not intended to limit the present invention, and any person having ordinary knowledge in the technical field of the present invention can make various changes without departing from the spirit and scope of the present invention. Retouching, therefore, the scope of protection of this creation is subject to the definition of the scope of the patent application attached.
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