TWM610940U - Waste water recycling and processing system - Google Patents
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Abstract
本創作公開一種廢水循環處理系統,其包括一廢水提供裝置、至少一吸附裝置以及一循環裝置。廢水提供裝置是用以提供一廢水。至少一吸附裝置是經配置以通過一第一管線接收廢水,並從廢水中吸附一定量的待處理物質後,通過一第二管線排出經吸附的廢水。循環裝置是經配置以使經吸附的廢水返回到至少一吸附裝置。The invention discloses a waste water recycling treatment system, which includes a waste water supply device, at least one adsorption device and a recycling device. The waste water supply device is used to provide a waste water. At least one adsorption device is configured to receive waste water through a first pipeline, and after adsorbing a certain amount of substances to be treated from the waste water, discharge the adsorbed waste water through a second pipeline. The circulation device is configured to return the adsorbed wastewater to at least one adsorption device.
Description
本創作涉及一種廢水處理系統,特別是涉及一種廢水循環處理系統。This creation relates to a waste water treatment system, in particular to a waste water recycling treatment system.
為了降低廢水(特別是工業廢水以及與有害事業廢棄物相關的廢水)對環境的負面衝擊,廢水需經過處理之後,符合政府所訂定的廢水排放標準才能排放於環境中。一般而言,廢水處理裝置會使用具有吸附性質的吸附材料,將廢水中的有機及無機污染物吸附至吸附材料的表面,以降低廢水中的有機及無機污染物的濃度。In order to reduce the negative impact of wastewater (especially industrial wastewater and wastewater related to hazardous industrial waste) on the environment, wastewater must be treated and meet the wastewater discharge standards set by the government before it can be discharged into the environment. Generally speaking, wastewater treatment devices will use adsorption materials with adsorption properties to adsorb organic and inorganic pollutants in the waste water to the surface of the adsorption materials to reduce the concentration of organic and inorganic pollutants in the waste water.
在目前的廢水處理系統中,其廢水處理裝置中的吸附材料在處理一定量的廢水之後,其吸附廢水中污染物的吸附效能會降低,使得已經過廢水處理裝置處理的廢水中的污染物參數,例如總有機碳、化學需氧量、導電度、總銅、總鎳、總鉬、總銦等仍然未符合放流水標準。然而,此時的吸附材料的吸附能力仍未達飽和,也就是說,吸附材料仍然有能力吸附廢水中的污染物,但其吸附效率已不足以使經過處理的廢水符合放流水標準。因此,需要暫停廢水處理的程序並停止進水,並將再生液或反沖洗液通過吸附材料後,才能恢復廢水處理的程序。藉此,對吸附材料進行再生,使其達到能夠處理廢水中污染物以符合放流水標準的吸附效率。In the current wastewater treatment system, after the adsorption material in the wastewater treatment device treats a certain amount of wastewater, its adsorption efficiency of adsorbing pollutants in the wastewater will be reduced, so that the pollutant parameters in the wastewater that have been treated by the wastewater treatment device , Such as total organic carbon, chemical oxygen demand, conductivity, total copper, total nickel, total molybdenum, total indium, etc. still do not meet the discharge water standards. However, the adsorption capacity of the adsorbent at this time is still not saturated, that is, the adsorbent still has the ability to adsorb pollutants in the waste water, but its adsorption efficiency is no longer sufficient to make the treated waste water meet the discharge water standard. Therefore, it is necessary to suspend the process of wastewater treatment and stop the water intake, and pass the regenerated liquid or backwashing liquid through the adsorbent before the process of wastewater treatment can be resumed. In this way, the adsorption material is regenerated to achieve the adsorption efficiency that can treat the pollutants in the wastewater to meet the discharge water standard.
然而,頻繁的停止進水以及將再生液通入吸附材料進行再生,不但增加廢水處理的時間及成本,還需要消耗大量的再生液、清洗水以及頻繁的更換吸附材料,造成更多工業廢棄物以及衍生污染物。However, frequent stopping of water intake and regenerating liquid into the adsorption material for regeneration will not only increase the time and cost of wastewater treatment, but also consume a large amount of regeneration fluid, cleaning water, and frequent replacement of adsorption materials, resulting in more industrial waste. And derived pollutants.
故,如何通過結構設計的改良,來降低吸附材料及再生液的消耗以及衍生污染物的產生,並提升廢水循環處理系統的效能,從而克服上述的缺陷,已成為該項事業所欲解決的重要課題之一。Therefore, how to reduce the consumption of adsorbents and regenerated liquid and the generation of derived pollutants through the improvement of the structural design, and to improve the efficiency of the wastewater recycling system, so as to overcome the above-mentioned shortcomings, has become an important issue for this business. One of the topics.
本創作所要解決的技術問題在於,針對現有技術的不足提供一種廢水循環處理系統,其在吸附材料吸附能力尚未飽和但已無法處理廢水以符合放流水標準時,能夠將經吸附的廢水返回到吸附裝置中,以提高吸附材料的吸附量以及污染物的濃縮倍數,因此相較於現有的廢水循環處理系統更具經濟效益。The technical problem to be solved by this creation is to provide a waste water recycling treatment system for the deficiencies of the existing technology, which can return the adsorbed waste water to the adsorption device when the adsorption capacity of the adsorbent material is not yet saturated but the waste water cannot be treated to meet the discharge water standard. In order to increase the adsorption capacity of the adsorbent material and the concentration of pollutants, it is more economical than the existing wastewater recycling system.
為了解決上述的技術問題,本創作所採用的其中一技術方案是提供一種用於處理一廢水的廢水循環處理系統,其包括一廢水提供裝置、至少一吸附裝置以及一循環裝置。廢水提供裝置是用以提供一廢水。至少一吸附裝置是經配置以通過一第一管線接收廢水,並從廢水中吸附一定量的待處理物質後,通過一第二管線排出經吸附的廢水。循環裝置是經配置以使經吸附的廢水返回到至少一吸附裝置。In order to solve the above-mentioned technical problems, one of the technical solutions adopted in this creation is to provide a waste water recycling treatment system for treating a waste water, which includes a waste water supply device, at least one adsorption device and a recycling device. The waste water supply device is used to provide a waste water. At least one adsorption device is configured to receive waste water through a first pipeline, and after adsorbing a certain amount of substances to be treated from the waste water, discharge the adsorbed waste water through a second pipeline. The circulation device is configured to return the adsorbed wastewater to at least one adsorption device.
更進一步地,循環裝置進一步包括一偵測單元,用以偵測經吸附的廢水的一水質參數。Furthermore, the circulation device further includes a detection unit for detecting a water quality parameter of the adsorbed wastewater.
更進一步地,循環裝置包括一循環管線,且當偵測單元偵測到的水質參數小於或等於一標準值時,循環管線與第二管線不連通,以使經吸附的廢水從第二管線排放。Furthermore, the circulation device includes a circulation pipeline, and when the water quality parameter detected by the detection unit is less than or equal to a standard value, the circulation pipeline is disconnected from the second pipeline, so that the adsorbed wastewater is discharged from the second pipeline .
更進一步地,循環裝置包括一循環管線,且當偵測單元偵測到的水質參數大於一標準值時,循環管線與第二管線連通,以使經吸附的廢水從循環管線返回到至少一吸附裝置。Furthermore, the circulation device includes a circulation pipeline, and when the water quality parameter detected by the detection unit is greater than a standard value, the circulation pipeline is connected to the second pipeline, so that the adsorbed wastewater is returned from the circulation pipeline to the at least one adsorption Device.
更進一步地,循環管線是設置在第二管線與廢水提供裝置之間。Furthermore, the circulation pipeline is arranged between the second pipeline and the waste water supply device.
更進一步地,循環管線是設置在第一管線與第二管線之間。Furthermore, the circulation pipeline is arranged between the first pipeline and the second pipeline.
更進一步地,循環管線是設置在第二管線與吸附裝置之間。Furthermore, the circulation pipeline is arranged between the second pipeline and the adsorption device.
更進一步地,至少一吸附裝置的數量為複數個,且複數個吸附裝置是設置在第一管線與循環管線之間。Furthermore, the number of at least one adsorption device is plural, and the plural adsorption devices are arranged between the first pipeline and the circulation pipeline.
更進一步地,水質參數為總有機碳、化學需氧量、導電度、總銅、總鎳、總鉬或總銦。Furthermore, the water quality parameter is total organic carbon, chemical oxygen demand, electrical conductivity, total copper, total nickel, total molybdenum or total indium.
更進一步地,廢水提供裝置包括一前處理裝置,前處理裝置用以對廢水進行一前處理。Furthermore, the wastewater supply device includes a pre-treatment device, and the pre-treatment device is used to perform a pre-treatment on the wastewater.
更進一步地,前處理為攔汙、曝氣、沉沙、過濾或除油。Furthermore, the pre-treatment is pollution prevention, aeration, sedimentation, filtration or degreasing.
更進一步地,廢水循環處理系統還進一步包括一逆滲透裝置,逆滲透裝置與至少一吸附裝置連通,用以進一步淨化經吸附的廢水。Furthermore, the wastewater recycling treatment system further includes a reverse osmosis device, which is connected with at least one adsorption device to further purify the adsorbed wastewater.
更進一步地,廢水循環處理系統,還進一步包括一再生劑提供裝置,再生劑提供裝置與至少一吸附裝置連通,用以提供一再生劑以將吸附材料再生。Furthermore, the wastewater recycling treatment system further includes a regenerating agent providing device, which is connected to at least one adsorption device to provide a regenerating agent to regenerate the adsorbent material.
本創作的其中一有益效果在於,本創作所提供的廢水循環處理系統,其能通過“至少一吸附裝置,至少一吸附裝置經配置以通過一第一管線接收廢水,並從廢水中吸附一定量的待處理物質後,通過一第二管線排出經吸附的廢水”以及“一循環裝置,循環裝置經配置以使經吸附的廢水返回到至少一吸附裝置”的技術方案,以提升廢水處理裝置的效能。同時,在處理水的水質參數介於標準值與臨界值之間時持續進行廢水處理的程序,以吸附並去除廢水中的待處理物質,以減少再生液、清洗水以及吸附材料的消耗,並減少再生時所產生的工業廢棄物以及衍生污染物。One of the beneficial effects of this creation is that the wastewater recycling treatment system provided by this creation can pass through "at least one adsorption device, and at least one adsorption device is configured to receive waste water through a first pipeline and absorb a certain amount from the waste water. After the substances to be treated, the adsorbed waste water is discharged through a second pipeline" and the technical solutions of "a circulation device configured to return the adsorbed waste water to at least one adsorption device" to improve the efficiency of the wastewater treatment device efficacy. At the same time, the process of wastewater treatment is continued when the water quality parameters of the treated water are between the standard value and the critical value to absorb and remove the substances to be treated in the wastewater to reduce the consumption of regenerated liquid, cleaning water and adsorption materials, and Reduce industrial waste and derived pollutants generated during regeneration.
為使能更進一步瞭解本創作的特徵及技術內容,請參閱以下有關本創作的詳細說明與圖式,然而所提供的圖式僅用於提供參考與說明,並非用來對本創作加以限制。In order to further understand the features and technical content of this creation, please refer to the following detailed descriptions and drawings about this creation. However, the drawings provided are only for reference and explanation, and are not used to limit this creation.
以下是通過特定的具體實施例來說明本創作所公開有關“廢水循環處理系統”的實施方式,本領域技術人員可由本說明書所公開的內容瞭解本創作的優點與效果。本創作可通過其他不同的具體實施例加以施行或應用,本說明書中的各項細節也可基於不同觀點與應用,在不背離本創作的構思下進行各種修改與變更。另外,本創作的附圖僅為簡單示意說明,並非依實際尺寸的描繪,事先聲明。以下的實施方式將進一步詳細說明本創作的相關技術內容,但所公開的內容並非用以限制本創作的保護範圍。另外,本文中所使用的術語“或”,應視實際情況可能包括相關聯的列出項目中的任一個或者多個的組合。The following are specific examples to illustrate the implementation of the "wastewater recycling system" disclosed in this creation, and those skilled in the art can understand the advantages and effects of this creation from the content disclosed in this specification. This creation can be implemented or applied through other different specific embodiments, and various details in this specification can also be modified and changed based on different viewpoints and applications without departing from the concept of this creation. In addition, the drawings of this creation are merely schematic illustrations, and are not depicted in actual size, and are stated in advance. The following implementations will further describe the related technical content of this creation in detail, but the disclosed content is not intended to limit the protection scope of this creation. In addition, the term "or" used in this document may include any one or a combination of more of the associated listed items depending on the actual situation.
[第一實施例][First Embodiment]
請參閱圖1至圖3所示,其為本創作第一實施例廢水循環處理系統的示意圖。本創作第一實施例提供一種廢水循環處理系統S,用於處理一廢水,其包括一廢水提供裝置10、一吸附裝置20以及一循環裝置30。廢水提供裝置10以及吸附裝置20經配置以通過一第一管線P1彼此流體連通,並使吸附裝置20接收廢水提供裝置10所提供的廢水。吸附裝置20具有一吸附材料(圖中未示出),用於吸附廢水中的待處理物質,以產生經過吸附處理的廢水(圖中未示出),也就是處理水,吸附裝置20可以通過一第二管線P2排出處理水。舉例來說,本創作的廢水可以是具有有機污染物或是無機污染物的廢水,而待處理物質則可以分別是有機污染物或無機污染物,但本創作並不以此為限。此外,吸附裝置20具有的吸附材料可以是,例如離子交換樹脂或活性碳,或是其他吸附材料,本創作不以吸附裝置20及吸附材料的種類,或其所能處理的污染物為限。循環裝置30包括一循環管線P3,循環單元30可以控制處理水是直接通過第二管線P2排出或是通過循環管線P3返回到吸附裝置20。Please refer to Figures 1 to 3, which are schematic diagrams of the wastewater recycling treatment system according to the first embodiment of the creation. The first embodiment of the present invention provides a waste water recycling treatment system S for treating waste water, which includes a waste
進一步而言,在第一實施例中,循環裝置30可以進一步包括一偵測單元(圖中未示出),並通過偵測單元偵測處理水中的待處理物質相關的一水質參數,且循環裝置30是通過水質參數,以控制處理水排出吸附裝置20之後的流向。進一步而言,當偵測單元偵測到處理水中的待處理物質的水質參數小於或等於一標準值時,循環裝置30可以將吸附裝置20通過第二管線P2排出的處理水直接排放。反之,當偵測單元偵測到處理水中的待處理物質的水質參數大於標準值時,循環裝置30將處理水通過循環管線P3返回到吸附裝置20。藉此,循環裝置30可以在處理水的水質參數小於或等於標準值(符合放流水標準)時,直接將處理水排出,並在處理水的水質參數大於標準值時,將處理水返回到吸附裝置20(即再次經過廢水處理程序)中,以進一步去除水中的待處理物質。Furthermore, in the first embodiment, the
舉例來說,在其中一實施方式中,偵測單元可以包括至少一偵測器(圖中未示出),且至少一偵測器可以偵測第二管線P2以及循環管線P3中處理水的水質參數,但本創作不以至少一偵測器的設置位置及數量為限。此外,在其中一實施方式中,循環裝置30可以進一步包括一控制器(圖中未示出)以及一控制閥(圖中未示出),且控制器電性連接控制閥以及偵測單元,循環裝置30可以通過控制器控制閥的通斷以控制處理水排出吸附裝置20之後的流向,但本創作並不以此為限。舉例來說,循環裝置30的控制器可以通過控制控制閥關閉,使循環管線P3與第二管線P2不連通,以使經吸附的廢水從第二管線P2排放。另一方面,循環裝置30的控制器可以通過控制設置在循環管線P3上的控制閥開啟,同時關閉另一設置在第二管線P2上的控制閥,使循環管線P3與第二管線P2連通,以使經吸附的廢水從循環管線P3返回吸附裝置20。此外,舉例來說,水質參數可以是總有機碳、化學需氧量、導電度、總銅、總鎳、總鉬、總銦,或其他放流水標準所規範的參數。然而,本創作不以上述所舉的例子為限。For example, in one of the embodiments, the detection unit may include at least one detector (not shown in the figure), and the at least one detector may detect the amount of water in the second pipeline P2 and the circulating pipeline P3. Water quality parameters, but this creation is not limited by the location and number of at least one detector. In addition, in one of the embodiments, the
復參閱圖1至圖3所示,在本創作第一實施例中,經吸附的廢水(處理水)可以經循環管線P3返回吸附裝置20。也就是說,處理水可以是返回廢水提供裝置10(如圖1所示)、返回第一管線P1(如圖2所示)或是直接返回吸附裝置20(如圖3所示),只要處理水能夠經由循環管線P3返回吸附裝置20,本創作並不限制其返回的路徑或方式。Referring again to FIGS. 1 to 3, in the first embodiment of the present creation, the adsorbed wastewater (treated water) can be returned to the
進一步而言,在第一實施例中,本創作的廢水循環處理系統S可以進一步包括一再生劑提供裝置(圖中未示出),再生劑提供裝置與吸附裝置20連通,用以提供一再生劑以將吸附裝置20中的吸附材料再生。舉例來說,再生劑提供裝置可以是一儲存槽,而再生劑可以是離子交換樹脂再生液(用以再生離子交換樹脂),例如硫酸(H
2SO
4)或液鹼(NaOH),或者水蒸氣(用以再生活性碳),但本創作並不以此為限。當循環裝置30偵測單元偵測到處理水中的待處理物質的水質參數大於一臨界值時,循環裝置30(所包括的控制器)可以控制設置在第一管線P1上的一進水閥(圖中未示出,與控制器電性連接)關閉,使廢水提供裝置10停止提供廢水至吸附裝置20。接著,再生劑提供裝置可以提供再生劑至吸附裝置20以對其中的吸附材料進行再生。
Furthermore, in the first embodiment, the wastewater recycling treatment system S of the present invention may further include a regenerant supply device (not shown in the figure), and the regenerant supply device is in communication with the
以一工業污水處理廠為例,其放流水水質之總銅濃度限值為100 mg/L(即處理水水質參數的標準值),當處理水的水質參數大於標準值(總銅濃度超過100 mg/L)時,離子交換樹脂塔(吸附裝置20)中離子交換樹脂(吸附材料)的單位質量吸附量只有其最大吸附量的30%。此時,循環裝置30的控制器可以通過控制設置在循環管線P3上的控制閥開啟,同時關閉另一設置在第二管線P2上的控制閥,使循環管線P3與第二管線P2連通,以使經吸附的廢水從循環管線P3返回吸附裝置20中,持續吸附水中的有機污染物(待處理物質)直至處理水中的總銅濃度大於臨界值,例如廢水進流的90%(以總銅濃度為1600 mg/L的廢水為例,即1440 mg/L),即停止廢水進水,此時吸附材料的單位質量吸附量以達其最大吸附量的90%。接著,通過提供離子交換樹脂再生液,例如硫酸、液鹼等,對離子交換樹脂進行再生。值得注意的是,本創作的標準值以及臨界值,都可以根據實際的需求或依廢水處理程序以及放流水標準進行調整,本創作並不以上述所舉的例子為限。Taking an industrial sewage treatment plant as an example, the total copper concentration limit of its discharged water quality is 100 mg/L (that is, the standard value of the water quality parameter of the treated water). When the water quality parameter of the treated water is greater than the standard value (the total copper concentration exceeds 100 mg/L), the adsorption capacity per unit mass of the ion exchange resin (adsorption material) in the ion exchange resin tower (adsorption device 20) is only 30% of its maximum adsorption capacity. At this time, the controller of the
藉此,本創作第一實施例提供的廢水循環處理系統S可以在其吸附裝置20中的吸附材料的吸附效率下降但未達飽和(未達吸附材料單位質量所的最大吸附量),但處理水的水質參數已經大於標準值時,使處理水返回到吸附裝置20,以使吸附裝置20的吸附材料持續吸附廢水中的待處理物質,且不會排放超過標準值的處理水。此外,當處理水的水質參數大於臨界值時,循環裝置30(控制器)停止廢水提供裝置10的廢水進水至吸附裝置20,並通過再生劑提供裝置(圖中未示出)提供再生劑,以恢復吸附裝置20的吸附材料的吸附效率。As a result, the wastewater recycling treatment system S provided in the first embodiment of the present creation can reduce the adsorption efficiency of the adsorption material in its
也就是說,本創作提供的廢水循環處理系統S可以在處理水的水質參數介於標準值與臨界值之間時持續進行廢水處理的程序,以吸附並去除廢水中的待處理物質,以減少再生液、清洗水以及吸附材料的消耗,同時減少再生時所產生的工業廢棄物以及衍生污染物。此外,有助於提升再生液經再生吸附材料後形成具有待處理物質的溶液之濃度,同時增加其濃縮倍數。That is to say, the wastewater recycling treatment system S provided by this creation can continue the wastewater treatment process when the water quality parameter of the treated water is between the standard value and the critical value, so as to absorb and remove the substances to be treated in the wastewater to reduce The consumption of regeneration fluid, cleaning water and adsorption materials, while reducing industrial waste and derived pollutants generated during regeneration. In addition, it helps to increase the concentration of the regenerated liquid after regenerating the adsorption material to form a solution with the substance to be treated, and at the same time increase its concentration.
在其中一實施方式中,廢水循環處理系統S的廢水提供裝置10可以進一步包括前處理裝置(圖中未示出),以減少吸附裝置20吸附廢水中待處理物質的負擔。廢水可以在前處理裝置中進行前處理。舉例來說,前處理可以是攔汙、曝氣、沉沙、過濾、除油等通常用於廢水前處理的步驟。然而,本創作不以上述所舉的例子為限。廢水在經過廢水提供裝置10的前處理裝置前處理之後,通過第一管線P1輸入吸附裝置20。In one of the embodiments, the waste
在其中一實施方式中,廢水循環處理系統S可以進一步包括一逆滲透裝置(圖中未示出),逆滲透裝置可以與吸附裝置20流體連通,並使處理水在通過第二管線P2排出之前,先通過逆滲透裝置,以進一步淨化處理水。In one of the embodiments, the wastewater recycling treatment system S may further include a reverse osmosis device (not shown in the figure). The reverse osmosis device may be in fluid communication with the
[第二實施例][Second Embodiment]
請參閱圖4至圖6所示,其為本創作第一實施例廢水循環處理系統的示意圖。本創作第二實施例提供一種廢水循環處理系統S,用於處理廢水,其包括廢水提供裝置10、複數個吸附裝置以及循環裝置30,且複數個吸附裝置可以是彼此並聯的設置。本創作第二實施例與第一實施例最大的差別在於第二實施例具有至少兩個彼此並聯設置的吸附裝置。以下,將以複數個吸附裝置的數量為兩個,分別為一第一吸附裝置20A以及一第二吸附裝置20B的情形說明,但本創作不以吸附裝置的數量為限。Please refer to Figures 4 to 6, which are schematic diagrams of the wastewater recycling treatment system according to the first embodiment of the creation. The second embodiment of the present invention provides a wastewater recycling treatment system S for wastewater treatment, which includes a
在其中一實施方式中,廢水提供裝置10以及第一吸附裝置20A與第二吸附裝置20B經配置以分別通過第一管線P1、P1’連通,並使第一吸附裝置20A以及第二吸附裝置20B分別接收廢水提供裝置10所提供的廢水。第一吸附裝置20A以及第二吸附裝置20B分別具有一吸附材料(圖中未示出),用於吸附廢水中的待處理物質,以產生經過吸附處理的廢水(圖中未示出),也就是處理水,而第一吸附裝置20A以及第二吸附裝置20B可以分別通過第二管線P2、P2’排出處理水。接著,循環裝置30可以控制處理水是分別通過第二管線P2、P2’直接排出或是通過循環管線P3、P3’分別返回到第一吸附裝置20A以及第二吸附裝置20B。In one of the embodiments, the
進一步而言,循環裝置30可以進一步包括偵測單元(圖中未示出),並通過偵測單元偵測處理水中的待處理物質相關的水質參數,且循環裝置30是通過水質參數,以控制處理水排出第一吸附裝置20A以及第二吸附裝置20B之後的流向。進一步而言,當偵測單元偵測到第一吸附裝置20A以及第二吸附裝置20B分別排出的處理水中待處理物質的水質參數都小於或等於標準值時,循環裝置30可以分別將通過第二管線P2、P2’排出的處理水直接排放。另一方面,當偵測單元偵測到第一吸附裝置20A排出的處理水中待處理物質的水質參數小於或等於標準值,且第二吸附裝置20B排出的處理水中待處理物質的水質參數大於標準值時,循環裝置30可以將通過第二管線P2排出的處理水直接排放,並將通過第二管線P2’排出的處理水通過循環管線P3’返回到第二吸附裝置20B。另一方面,當偵測單元偵測到第一吸附裝置20A以及第二吸附裝置20B處理水中的待處理物質的水質參數都大於標準值時,循環裝置30將處理水通過循環管線P3、P3’分別返回到第一吸附裝置20A以及第二吸附裝置20B。藉此,循環裝置30可以在處理水的水質參數小於或等於標準值(符合放流水標準)時,直接將處理水排出,並在處理水的水質參數大於標準值時,將處理水分別返回到第一吸附裝置20A以及第二吸附裝置20B(即再次經過廢水處理程序)中,以進一步去除水中的待處理物質。Furthermore, the
復參閱圖4至圖6所示,在本創作第二實施例中,經吸附的廢水(處理水)可以經循環管線P3返回吸附裝置20。也就是說,處理水可以是返回廢水提供裝置10(如圖4所示)、分別返回第一管線P1、P1’(如圖5所示)或是分別直接返回第一吸附裝置20A以及第二吸附裝置20B(如圖6所示),只要處理水能夠經由循環管線P3、P3’分別返回第一吸附裝置20A以及第二吸附裝置20B,本創作並不限制其返回的路徑或方式。Referring again to FIGS. 4 to 6, in the second embodiment of the present creation, the adsorbed waste water (treated water) can be returned to the
進一步而言,本創作的廢水循環處理系統S可以進一步包括一再生劑提供裝置(圖中未示出),再生劑提供裝置與第一吸附裝置20A以及第二吸附裝置20B連通,用以提供一再生劑以將吸附裝置20中的吸附材料再生。當循環裝置30偵測單元偵測到第一吸附裝置20A或第二吸附裝置20B的處理水中的待處理物質的水質參數大於一臨界值時,循環裝置30(所包括的控制器)可以控制設置在第一管線P1或第一管線P1’上的一進水閥(圖中未示出,與控制器電性連接)關閉,使廢水提供裝置10停止提供廢水至第一吸附裝置20A或第二吸附裝置20B。接著,再生劑提供裝置可以提供再生劑至吸附裝置20以對其中的吸附材料進行再生。Furthermore, the wastewater recycling treatment system S of the present invention may further include a regenerant supply device (not shown in the figure), and the regenerant supply device is in communication with the
藉此,本創作第二實施例提供的廢水循環處理系統S可以在吸附材料的吸附效率下降但未達飽和,但處理水的水質參數已經大於標準值時,將處理水返回到第一吸附裝置20A以及第二吸附裝置20B,以使吸附材料持續吸附廢水中的待處理物質,且不會排放超過標準值的處理水。此外,當處理水的水質參數大於臨界值時,循環裝置30停止廢水進水至第一吸附裝置20A以及第二吸附裝置20B,並通過再生劑提供裝置(圖中未示出)提供再生劑,以恢復吸附材料的吸附效率。Thereby, the wastewater recycling treatment system S provided by the second embodiment of the present creation can return the treated water to the first adsorption device when the adsorption efficiency of the adsorbent material is reduced but not saturated, but the water quality parameter of the treated water is already greater than the standard value. 20A and the
進一步而言,再生劑提供裝置(圖中未示出)是與第一吸附裝置20A以及第二吸附裝置20B分別流體連通,也就是說,當第一吸附裝置20A以及第二吸附裝置20B其中之一必須停止廢水進水並進行再生時,另一吸附裝置(第二吸附裝置20B或第一吸附裝置20A)仍然可以持續進行廢水處理的程序,兩者彼此獨立。因此,本創作第二實施例提供的廢水循環處理系統S有助於進一步提高廢水處理的效能。另外,須說明的是,本創作第二實施例是以兩個吸附裝置(第一吸附裝置20A以及第二吸附裝置20B)彼此並聯為例說明,所屬領域具有通常知識者可以依實際需求或廢水處理程序調整吸附裝置的數量、串並聯方式,本創作並不以此為限。此外,關於廢水循環處理系統S的其他技術特徵與實現方式,已描述於前述實施例,在此不再贅述。Furthermore, the regenerant supply device (not shown in the figure) is in fluid communication with the
本創作的其中一有益效果在於,本創作所提供的廢水循環處理系統S,其能通過“至少一吸附裝置20,至少一吸附裝置20經配置以通過一第一管線P1接收廢水,並從廢水中吸附一定量的待處理物質後,通過一第二管線P2排出經吸附的廢水”以及“一循環裝置30,循環裝置30經配置以使經吸附的廢水返回到至少一吸附裝置20”的技術方案,以提升廢水處理裝置的效能。同時,在處理水的水質參數介於標準值與臨界值之間時持續進行廢水處理的程序,以吸附並去除廢水中的待處理物質,以減少再生液、清洗水以及吸附材料的消耗,並減少再生時所產生的工業廢棄物以及衍生污染物。One of the beneficial effects of this creation is that the waste water recycling treatment system S provided by this creation can pass through "at least one
以上所公開的內容僅為本創作的優選可行實施例,並非因此侷限本創作的申請專利範圍,所以凡是運用本創作說明書及圖式內容所做的等效技術變化,均包含於本創作的申請專利範圍內。The content disclosed above is only a preferred and feasible embodiment of this creation, and does not limit the scope of patent application for this creation. Therefore, all equivalent technical changes made using this creation specification and schematic content are included in the application for this creation. Within the scope of the patent.
S:廢水循環處理系統
10:廢水提供裝置
20:吸附裝置
20A:第一吸附裝置
20B:第二吸附裝置
30:循環裝置
P1,P1’:第一管線
P2,P2’:第二管線
P3,P3’:循環管線
S: Wastewater recycling system
10: Wastewater supply device
20:
圖1為本創作第一實施例廢水循環處理系統的其中一示意圖。Figure 1 is a schematic diagram of the wastewater recycling treatment system according to the first embodiment of the creation.
圖2為本創作第一實施例廢水循環處理系統的另一示意圖。Figure 2 is another schematic diagram of the wastewater recycling treatment system according to the first embodiment of the creation.
圖3為本創作第一實施例廢水循環處理系統的又一示意圖。Figure 3 is another schematic diagram of the wastewater recycling treatment system according to the first embodiment of the creation.
圖4為本創作第二實施例廢水循環處理系統的其中一示意圖。Fig. 4 is a schematic diagram of the wastewater recycling treatment system according to the second embodiment of the creation.
圖5為本創作第二實施例廢水循環處理系統的另一示意圖。Fig. 5 is another schematic diagram of the wastewater recycling treatment system according to the second embodiment of the creation.
圖6為本創作第二實施例廢水循環處理系統的又一示意圖。Fig. 6 is another schematic diagram of the wastewater recycling treatment system according to the second embodiment of the creation.
S:廢水循環處理系統 S: Wastewater recycling system
10:廢水提供裝置 10: Wastewater supply device
20:吸附裝置 20: Adsorption device
30:循環裝置 30: Circulation device
P1:第一管線 P1: The first pipeline
P2:第二管線 P2: second pipeline
P3:循環管線 P3: Circulation pipeline
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