TWM630641U - Metal surface treatment fluid recycling system - Google Patents
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Abstract
本創作涉及一種金屬表面處理液回收利用系統，所述回收利用系統包 括依次連接的處理液收集槽、預處理裝置、納濾裝置、真空蒸餾裝置和濃縮液回收槽，所述納濾裝置包括進水槽、一級納濾膜組和二級納濾膜組，所述處理液收集槽中的處理液通過預處理裝置過濾掉固體懸浮物後進入進水槽內，所述進水槽中的廢水進入一級納濾膜組過濾後形成一級濃廢液和一級滲透液，一級滲透液進入二級納濾膜組再次過濾後形成二級濃廢液和二級滲透液，二級滲透液進入真空蒸餾裝置被進一步蒸發濃縮形成蒸餾水和高濃度含酸的濃縮液；本創作將納濾裝置和真空蒸餾裝置相結合，得到高濃度的含酸濃縮液進行回收利用，符合資源利用的最大化。 This creation relates to a metal surface treatment fluid recycling system, the recycling system package It includes a treatment liquid collection tank, a pretreatment device, a nanofiltration device, a vacuum distillation device and a concentrated solution recovery tank connected in sequence, and the nanofiltration device includes a water inlet tank, a first-stage nanofiltration membrane group and a second-stage nanofiltration membrane group. The treatment liquid in the treatment liquid collection tank is filtered by the pretreatment device to filter out the suspended solids and then enters the water inlet tank. The liquid enters the secondary nanofiltration membrane group and is filtered again to form secondary concentrated waste liquid and secondary permeate. The secondary permeate enters the vacuum distillation device and is further evaporated and concentrated to form distilled water and high-concentration acid-containing concentrate. The filtration device and the vacuum distillation device are combined to obtain a high-concentration acid-containing concentrated solution for recycling, which is in line with the maximization of resource utilization.
Description
本創作涉及廢液處理，具體涉及一種金屬表面處理液回收利用系統。 This creation involves waste liquid treatment, specifically a metal surface treatment liquid recycling system.
在金屬表面處理生產過程中，常使用各種強酸(如磷酸、硫酸、硝酸等)，對金屬表面進行酸洗、溶蝕、拋光等工藝處理，當酸液中的金屬達到一定的濃度後，因處理效果達不到工藝要求，酸液就需要重新配製和更換。在這個過程中，產生了大量的含廢酸液，由此帶來兩個問題： In the production process of metal surface treatment, various strong acids (such as phosphoric acid, sulfuric acid, nitric acid, etc.) are often used to carry out pickling, dissolution, polishing and other processes on the metal surface. When the metal in the acid solution reaches a certain concentration, due to the treatment If the effect does not meet the technological requirements, the acid solution needs to be reconstituted and replaced. In this process, a large amount of waste acid-containing liquid is produced, which brings two problems:
一、處理高濃度的含酸廢液，需要消耗大量的堿液進行中和處理或委託有資質單位外運處理，增加成本。 1. To deal with high-concentration acid-containing waste liquid, it is necessary to consume a large amount of acid-containing liquid for neutralization treatment or entrust a qualified unit for outbound treatment, which increases the cost.
二、大量有價值的酸被浪費，如磷酸。 Second, a large amount of valuable acid is wasted, such as phosphoric acid.
因此急需一種新的廢液處理工藝能夠克服上述缺陷。 Therefore, a new waste liquid treatment process is urgently needed to overcome the above-mentioned defects.
為了克服上述缺陷，本創作提供一種金屬表面處理液回收利用系統，該系統將納濾裝置和真空蒸餾裝置相結合，納濾裝置首先將金屬離子和酸液分離，分離出來的含酸滲透液再通過真空蒸餾裝置濃縮得到高濃度的含酸濃縮液進行回收利用，符合資源利用的最大化。 In order to overcome the above-mentioned defects, this creation provides a metal surface treatment liquid recycling system, which combines a nanofiltration device and a vacuum distillation device. The concentrated acid-containing liquid with high concentration is obtained by vacuum distillation device for recycling, which is in line with the maximization of resource utilization.
本創作為了解決其技術問題所採用的技術方案是：一種金屬表面處理液回收利用系統，包括依次連接的處理液收集槽、預處理裝置、納濾裝置、 真空蒸餾裝置和濃縮液回收槽，所述納濾裝置包括進水槽、一級納濾膜組和二級納濾膜組，所述處理液收集槽中的處理液通過預處理裝置過濾掉固體懸浮物後進入進水槽內，所述進水槽中的廢水進入一級納濾膜組過濾後形成一級濃廢液和一級滲透液，一級滲透液進入二級納濾膜組再次過濾後形成二級濃廢液和二級滲透液，含有高濃度金屬離子的一級濃廢液和二級濃廢液進入廢水池處理，二級滲透液進入真空蒸餾裝置被進一步蒸發濃縮形成蒸餾水和高濃度含酸的濃縮液，所述濃縮液進入濃縮液回收槽中待迴圈利用，而蒸餾水進入儲水池待迴圈利用。 The technical solution adopted in this creation in order to solve its technical problems is: a metal surface treatment liquid recycling system, including a treatment liquid collection tank, a pretreatment device, a nanofiltration device, a A vacuum distillation device and a concentrated solution recovery tank, the nanofiltration device includes a water inlet tank, a first-level nanofiltration membrane group and a second-level nanofiltration membrane group, and the treatment liquid in the treatment liquid collection tank is filtered by a pretreatment device to remove solid suspensions After entering the water inlet tank, the waste water in the water inlet tank enters the first-level nanofiltration membrane group for filtration to form a first-level concentrated waste liquid and a first-level permeate, and the first-level permeate enters the second-level nanofiltration membrane group and is filtered again to form a second-level concentrated waste liquid. and secondary permeate, the primary concentrated waste liquid and secondary concentrated waste liquid containing high concentrations of metal ions enter the waste water tank for treatment, and the secondary permeate enters the vacuum distillation device to be further evaporated and concentrated to form distilled water and high-concentration acid-containing concentrated liquid, The concentrated liquid enters the concentrated liquid recovery tank for recycling, while the distilled water enters the water storage tank for recycling.
優選地，所述進水槽中的廢水通過一級高壓泵和一級進料管泵入一級納濾膜組中，所述一級滲透液通過一級滲透液出水管排出後再通過二級高壓泵和二級進料管泵入二級納濾膜組中，所述一級濃廢液通過一級濃廢液出水管排出，且該一級濃廢液出水管上設有一級壓力錶和一級調壓閥，所述二級濃廢液通過二級濃廢液出水管排出，且該二級濃廢液出水管上設有二級壓力錶和二級調壓閥，所述二級滲透液通過二級滲透液出水管排出至真空蒸餾裝置。 Preferably, the wastewater in the water inlet tank is pumped into the first-stage nanofiltration membrane group through the first-stage high-pressure pump and the first-stage feed pipe, and the first-stage permeate is discharged through the first-stage permeate outlet pipe and then passes through the second-stage high-pressure pump and the second-stage high-pressure pump. The feed pipe is pumped into the second-stage nanofiltration membrane group, the first-stage concentrated waste liquid is discharged through the first-stage concentrated waste liquid outlet pipe, and the first-stage concentrated waste liquid outlet pipe is provided with a first-stage pressure gauge and a first-stage pressure regulating valve. The secondary concentrated waste liquid is discharged through the secondary concentrated waste liquid outlet pipe, and the secondary concentrated waste liquid outlet pipe is provided with a secondary pressure gauge and a secondary pressure regulating valve, and the secondary permeate is discharged through the secondary permeate liquid. The water pipe is discharged to the vacuum distillation unit.
優選地，所述一級納濾膜組和二級納濾膜組中採用的納濾膜為耐高壓、耐濃酸且能截留二價及二價以上金屬離子的納濾膜。 Preferably, the nanofiltration membranes used in the first-stage nanofiltration membrane group and the second-stage nanofiltration membrane group are nanofiltration membranes that are resistant to high pressure, resistant to concentrated acid, and capable of retaining divalent metal ions and above.
優選地，所述預處理裝置中的過濾介質為石英砂、活性炭和無煙煤中的至少一種，該預處理裝置用於過濾處理液中粒徑大於1μm的固體懸浮物。 Preferably, the filter medium in the pretreatment device is at least one of quartz sand, activated carbon and anthracite, and the pretreatment device is used for filtering solid suspensions with a particle size greater than 1 μm in the treatment liquid.
優選地，所述真空蒸餾裝置包括蒸發罐、冷凝器和緩衝槽，所述蒸發罐與真空泵相連接，該蒸發罐內部設有加熱管、底部設有加熱夾套，該蒸發罐外部設有廢液入口、濃縮液出口、蒸汽入口、蒸汽水出口和水汽出口，所述冷凝器外部設有水汽入口、蒸餾水出口、冷卻水入口和冷卻水出口，二級滲透液通過廢液入口進入蒸發罐內，加熱蒸汽通過蒸汽入口進入加熱管和夾套對外部的廢液進行加熱，被換熱後的蒸汽變成水經過蒸汽水出口流出蒸發罐，廢 水中被加熱後的水汽經過水汽出口進入冷凝器中，被濃縮後的廢水濃縮液通過濃縮液出口排入濃縮液回收槽，水汽在冷凝器中被冷卻水冷凝後通過蒸餾水出口排入緩衝槽，蒸餾水在緩衝槽中穩定後通過排液泵泵出回收利用。 Preferably, the vacuum distillation device includes an evaporation tank, a condenser and a buffer tank, the evaporation tank is connected to a vacuum pump, a heating pipe is arranged inside the evaporation tank, a heating jacket is arranged at the bottom, and a waste gas is arranged outside the evaporation tank Liquid inlet, concentrated liquid outlet, steam inlet, steam water outlet and water vapor outlet, the condenser is provided with a water vapor inlet, a distilled water outlet, a cooling water inlet and a cooling water outlet, and the secondary permeate enters the evaporation tank through the waste liquid inlet , the heating steam enters the heating tube and the jacket through the steam inlet to heat the external waste liquid, and the heat-exchanged steam turns into water and flows out of the evaporation tank through the steam water outlet. The heated water vapor in the water enters the condenser through the water vapor outlet, and the concentrated waste water concentrate is discharged into the concentrated liquid recovery tank through the concentrated liquid outlet. The water vapor is condensed by the cooling water in the condenser and discharged into the buffer tank through the distilled water outlet. After the distilled water is stabilized in the buffer tank, it is pumped out by the drain pump for recycling.
本創作還提供了一種金屬表面處理液回收利用系統，包括如下步驟：步驟一：金屬表面處理液使用後流入處理液收集槽內，處理液收集槽中高金屬離子濃度的含酸廢水通過管路進入預處理裝置中過濾掉粒徑大於1μm的固體懸浮物後，進入納濾裝置的進水槽中；步驟二：一級高壓泵將進水槽中的廢液泵入一級納濾膜組，調節一級調壓閥使一級納濾膜組的滲透壓維持在4.5Mpa~5.5Mpa之間，一級納濾膜組在該壓力下將二價及二價以上的金屬離子截留在一級濃廢液中，而通過一級納濾膜組的一級滲透液排出至二級納濾膜組；步驟三：二級高壓泵將一級滲透液泵入二級納濾模組中，調節二級調壓閥使二級納濾膜組的滲透壓維持在5.0Mpa~6.0Mpa之間，二級納濾膜組在該壓力下將二價及二價以上的金屬離子進一步截留在二級濃廢液中，而通過二級納濾膜組的二級滲透液排出至真空蒸餾裝置；步驟四：含微量金屬離子的二級滲透液在真空蒸餾裝置中被進一步蒸發濃縮，真空蒸餾裝置在真空度為80Kpa~90Kpa的條件下，將二級滲透液中水分在溫度為40℃~50℃下蒸發分離，當廢液中的酸濃度升高至預設濃度後真空蒸餾裝置停止運行，含微量金屬離子且含高濃度酸的濃縮液排出蒸發罐並收集於濃縮液回收槽中以被再利用，同時蒸發的水回收作為工業水使用。 This creation also provides a metal surface treatment liquid recycling system, which includes the following steps: Step 1: After the metal surface treatment liquid is used, it flows into the treatment liquid collection tank, and the acid-containing wastewater with high metal ion concentration in the treatment liquid collection tank enters through the pipeline. After the solid suspended matter with a particle size larger than 1 μm is filtered out in the pretreatment device, it enters the water inlet tank of the nanofiltration device; Step 2: The first-stage high-pressure pump pumps the waste liquid in the water inlet tank into the first-stage nanofiltration membrane group, and adjusts the first-stage pressure regulation The valve keeps the osmotic pressure of the first-stage nanofiltration membrane group between 4.5Mpa and 5.5Mpa. Under this pressure, the first-stage nanofiltration membrane group traps metal ions with divalent and above in the first-stage concentrated waste liquid, and passes through the first-stage nanofiltration membrane group. The primary permeate of the nanofiltration membrane group is discharged to the secondary nanofiltration membrane group; step 3: the secondary high pressure pump pumps the primary permeate into the secondary nanofiltration module, and adjusts the secondary pressure regulating valve to make the secondary nanofiltration membrane The osmotic pressure of the group is maintained between 5.0Mpa and 6.0Mpa. Under this pressure, the secondary nanofiltration membrane group further traps metal ions with divalent and above in the secondary concentrated waste liquid, and passes through the secondary nanofiltration membrane. The secondary permeate of the membrane group is discharged to the vacuum distillation device; Step 4: the secondary permeate containing trace metal ions is further evaporated and concentrated in the vacuum distillation device. The water in the secondary permeate is evaporated and separated at a temperature of 40°C to 50°C. When the acid concentration in the waste liquid rises to the preset concentration, the vacuum distillation device stops running, and the concentrated solution containing trace metal ions and high concentration acid It is discharged from the evaporation tank and collected in the concentrated liquid recovery tank to be reused, and the evaporated water is recovered for use as industrial water.
本創作的有益效果是： The beneficial effects of this creation are:
1、本系統主要包括預處理裝置、納濾裝置和真空蒸餾裝置，高金屬離子的含酸廢液首先經預處理裝置，過濾掉粒徑大於1μm的固體懸浮物後，再進入納濾 裝置，利用納濾膜分離技術將含酸廢液中二價及多價金屬離子有效截留；去除雜質後的含酸廢液進一步經真空蒸餾裝置蒸發濃縮，當酸濃度達到85%以上後，可以直接回用。因此利用本系統處理含酸廢液，可有效分離含酸廢液中的雜質及金屬離子，同時對酸液進行蒸發提濃，實現含酸廢液去雜濃縮再利用，符合資源利用的最大化。 1. The system mainly includes a pretreatment device, a nanofiltration device and a vacuum distillation device. The acid-containing waste liquid with high metal ions first passes through the pretreatment device to filter out the solid suspended matter with a particle size larger than 1 μm, and then enters the nanofiltration device. The device uses nanofiltration membrane separation technology to effectively intercept divalent and polyvalent metal ions in the acid-containing waste liquid; the acid-containing waste liquid after removing impurities is further evaporated and concentrated by a vacuum distillation device. When the acid concentration reaches more than 85%, it can be reuse directly. Therefore, using this system to treat the acid-containing waste liquid can effectively separate impurities and metal ions in the acid-containing waste liquid, and at the same time, the acid liquid can be evaporated and concentrated, so as to realize the de-impurity, concentration and reuse of the acid-containing waste liquid, which is in line with the maximization of resource utilization. .
2、本系統中採用的納濾裝置，是利用納濾膜分離技術分離淨化含酸廢液中的雜質特別是可以截留金屬離子的功能；納濾膜是20世紀80年代發明的新型分離膜，是介於超濾膜和反滲透膜之間的、根據吸附擴散原理以壓力驅差為驅動力的膜，是一種加壓膜分離技術，即在一定的壓力下，使小分子溶質和溶劑穿過一定孔徑的特製的薄膜，而使大分子溶質不能透過，留在膜的一邊；本創作中納濾膜除了對大分子溶質截留外，還對二價及二價以上金屬離子有較高的截留率，本系統中納濾裝置為二級納濾，以單級納濾膜組串聯方式連接，一級納濾膜組金屬離子截留率可達75%~80%，二級納濾膜組截留率可達85%~90%，因此採用二級串聯式納濾膜元件可以將二價及二價以上金屬離子與酸分離，使得濃縮後的酸液中金屬離子含量符合處理液的標準，確保酸液可以直接回收利用。 2. The nanofiltration device used in this system is to use the nanofiltration membrane separation technology to separate and purify the impurities in the acid-containing waste liquid, especially the function of intercepting metal ions; the nanofiltration membrane is a new type of separation membrane invented in the 1980s. It is a membrane between ultrafiltration membrane and reverse osmosis membrane, which is driven by pressure displacement according to the principle of adsorption and diffusion. A special membrane with a certain pore size makes the macromolecular solute impermeable and stays on one side of the membrane; in this creation, the nanofiltration membrane not only intercepts macromolecular solutes, but also has higher resistance to divalent and above metal ions. Rejection rate, the nanofiltration device in this system is a two-stage nanofiltration, which is connected in series with a single-stage nanofiltration membrane group. The rate can reach 85%~90%. Therefore, the use of two-stage series nanofiltration membrane elements can separate the divalent and above metal ions from the acid, so that the metal ion content in the concentrated acid solution meets the standard of the treatment solution, ensuring that The acid solution can be directly recycled.
3、本系統中採用的真空蒸餾裝置，是在高真空條件下(-80Kpa~-90Kpa)進行的連續蒸餾過程，酸液中水分在低溫下(40℃~50℃)被蒸發分離，可有效提高酸的濃度，同時由於操作溫度遠低於物質常壓下的沸點溫度，且加熱時間非常短，不會對酸液本身造成破壞，從而實現了酸液的回收再利用。 3. The vacuum distillation device used in this system is a continuous distillation process under high vacuum conditions (-80Kpa~-90Kpa). The water in the acid solution is evaporated and separated at low temperature (40℃~50℃), which can effectively The concentration of acid is increased, and at the same time, because the operating temperature is far lower than the boiling point temperature of the substance under normal pressure, and the heating time is very short, it will not cause damage to the acid liquid itself, thus realizing the recovery and reuse of the acid liquid.
100:納濾裝置 100: Nanofiltration device
110:進水槽 110: Intake tank
120:一級納濾膜組 120: First-grade nanofiltration membrane group
121:一級高壓泵 121: First stage high pressure pump
122:一級進料管 122: Primary feed pipe
123:一級濃廢液出水管 123: First-class concentrated waste liquid outlet pipe
124:一級壓力錶 124: Level 1 pressure gauge
125:一級調壓閥 125: Primary pressure regulator
126:一級滲透液出水管 126: Primary permeate outlet pipe
130:二級納濾膜組 130: Secondary Nanofiltration Membrane Group
131:二級高壓泵 131: Secondary high pressure pump
132:二級進料管 132: Secondary feed pipe
133:二級濃廢液出水管 133: Secondary concentrated waste liquid outlet pipe
134:二級壓力錶 134: Secondary pressure gauge
135:二級調壓閥 135: Secondary pressure regulator
136:二級滲透液出水管 136: Secondary permeate outlet pipe
200:真空蒸餾裝置 200: Vacuum distillation unit
210:蒸發罐 210: Evaporation tank
211:加熱管 211: Heating tube
212:夾套 212: Jacket
213:廢液入口 213: Waste liquid inlet
214:濃縮液出口 214: concentrate outlet
215:蒸汽入口 215: Steam inlet
216:蒸汽水出口 216: Steam water outlet
217:計量器 217: Gauge
220:冷凝器 220: Condenser
221:篩檢程式 221: Screening Program
222:水汽入口 222: Water vapor inlet
223:蒸餾水出口 223: Distilled water outlet
224:冷卻水入口 224: Cooling water inlet
225:冷卻水出口 225: Cooling water outlet
230:計量罐 230:Measuring tank
231:自動閥 231: Automatic valve
240:緩衝槽 240: Buffer slot
250:真空泵 250: vacuum pump
260:排液泵 260: Drain pump
300:處理液收集槽 300: Treatment liquid collection tank
400:預處理裝置 400: Pretreatment device
500:濃縮液回收槽 500: Concentrate recovery tank
圖1為本創作的工藝流程圖；圖2為本創作中納濾裝置的結構示意圖；圖3為本創作中真空蒸餾裝置的結構示意圖。 Fig. 1 is the process flow diagram of the creation; Fig. 2 is the structural schematic diagram of the nanofiltration device in the creation; Fig. 3 is the structural schematic diagram of the vacuum distillation device in the creation.
下面將結合本創作實施例，對本創作實施例中的技術方案進行清楚、完整地描述，顯然，所描述的實施例僅僅是本創作一部分實施例，而不是全部的實施例。基於本創作中的實施例，本領域普通技術人員在沒有做出創造性勞動前提下所獲得的所有其他實施例，都屬於本創作保護的範圍。 The technical solutions in the creative embodiments will be described clearly and completely below in conjunction with the creative embodiments. Obviously, the described embodiments are only a part of the embodiments of the present creation, rather than all the embodiments. Based on the embodiments in this creation, all other embodiments obtained by those of ordinary skill in the art without making creative efforts fall within the scope of protection of this creation.
需要說明的是，本申請的說明書和權利請求書及上述附圖中的術語“第一”、“第二”等是用於區別類似的物件，而不必用於描述特定的順序或先後次序。應該理解這樣使用的資料在適當情況下可以互換，以使這裡描述的本申請的實施方式例如能夠以除了在這裡圖示或描述的那些以外的順序實施。此外，術語“包括”和“具有”以及他們的任何變形，意圖在於覆蓋不排他的包含，例如，包含了一系列步驟或單元的過程、方法、系統、產品或設備不必限於清楚地列出的那些步驟或單元，而是可包括沒有清楚地列出的或對於這些過程、方法、產品或設備固有的其它步驟或單元。 It should be noted that the terms "first", "second" and the like in the description and claims of the present application and the above drawings are used to distinguish similar items, and are not necessarily used to describe a specific sequence or sequence. It is to be understood that the materials so used are interchangeable under appropriate circumstances to enable the embodiments of the application described herein to be practiced, for example, in sequences other than those illustrated or described herein. Furthermore, the terms "comprising" and "having" and any variations thereof, are intended to cover non-exclusive inclusion, for example, a process, method, system, product or device comprising a series of steps or units is not necessarily limited to those expressly listed Rather, those steps or units may include other steps or units not expressly listed or inherent to these processes, methods, products or devices.
為了便於描述，在這裡可以使用空間相對術語，如“在……之上”、“在……上方”、“在……上表面”、“上面的”等，用來描述如在圖中所示的一個器件或特徵與其他器件或特徵的空間位置關係。應當理解的是，空間相對術語旨在包含除了器件在圖中所描述的方位之外的在使用或操作中的不同方位。例如，如果附圖中的器件被倒置，則描述為“在其他器件或構造上方”或“在其他器件或構造之上”的器件之後將被定位為“在其他器件或構造下方”或“在其他器件或構造之下”。因而，示例性術語“在……上方”可以包括“在……上方”和“在……下方”兩種方位。該器件也可以其他不同方式定位(旋轉90度或處於其他方位)，並且對這裡所使用的空間相對描述作出相應解釋。 For ease of description, spatially relative terms, such as "on", "over", "on the surface", "above", etc., may be used herein to describe what is shown in the figures. The spatial positional relationship of one device or feature shown to other devices or features. It should be understood that spatially relative terms are intended to encompass different orientations of the device in use or operation in addition to the orientation depicted in the figures. For example, if the device in the figures is turned over, elements described as "above" or "over" other devices or features would then be oriented "below" or "over" the other devices or features under other devices or constructions". Thus, the exemplary term "above" can encompass both an orientation of "above" and "below." The device may also be otherwise oriented (rotated 90 degrees or at other orientations) and the spatially relative descriptions used herein interpreted accordingly.
實施例：如圖1-3所示，一種金屬表面處理液回收利用系統，包括依次連接的處理液收集槽300、預處理裝置400、納濾裝置100、真空蒸餾裝置200和濃縮液回收槽500，所述納濾裝置100包括進水槽110、一級納濾膜組120和二級納濾膜組130，所述處理液收集槽300中的處理液通過預處理裝置400過濾掉固體懸浮物後進入進水槽110內，所述進水槽110中的廢水進入一級納濾膜組120過濾後形成一級濃廢液和一級滲透液，一級滲透液進入二級納濾膜組130再次過濾後形成二級濃廢液和二級滲透液，含有高濃度金屬離子的一級濃廢液和二級濃廢液進入廢水池處理，二級滲透液進入真空蒸餾裝置200被進一步蒸發濃縮形成蒸餾水和高濃度含酸的濃縮液，所述濃縮液進入濃縮液回收槽500中待迴圈利用，而蒸餾水進入儲水池待迴圈利用。
Example: As shown in Figures 1-3, a metal surface treatment liquid recycling system includes a treatment
本系統主要針對金屬離子含量較高的金屬表面含酸處理液的回收利用，在傳統回收系統中僅將廢液中的酸和水分離，對於酸液中金屬離子則無法分離，而如果酸液中的金屬離子超過一定含量時則無法使用，如採用傳統的回收系統濃縮後的酸液中依然含有高濃度的金屬離子，因此無法直接使用。本創作中採用納濾膜將酸和金屬離子先分離後，再通過真空蒸餾裝置將廢液中的酸濃縮，得到的濃縮液可直接用於金屬表面處理，如酸洗、溶蝕、拋光等工藝中。因此本系統將納濾裝置和真空蒸餾裝置相結合，納濾裝置首先將金屬離子和酸液分離，僅得到了少量高濃度金屬離子的廢濃液即納濾裝置的截留液需要進一步處理外，納濾裝置的滲透液通過真空蒸餾裝置得到的水和濃縮液皆可以回收利用，符合資源利用的最大化。 This system is mainly aimed at the recovery and utilization of the acid-containing treatment liquid on the metal surface with high metal ion content. In the traditional recovery system, only the acid and water in the waste liquid are separated, and the metal ions in the acid liquid cannot be separated. When the metal ion in the acid exceeds a certain content, it cannot be used. For example, the acid solution concentrated by the traditional recovery system still contains a high concentration of metal ions, so it cannot be used directly. In this creation, nanofiltration membrane is used to separate the acid and metal ions first, and then the acid in the waste liquid is concentrated by a vacuum distillation device. The obtained concentrated liquid can be directly used for metal surface treatment, such as pickling, dissolution, polishing and other processes middle. Therefore, this system combines a nanofiltration device with a vacuum distillation device. The nanofiltration device first separates the metal ions from the acid solution, and only a small amount of high-concentration metal ion waste concentrate is obtained, that is, the retentate of the nanofiltration device needs further treatment. The permeate of the filtration device can be recycled and the concentrated solution obtained by the vacuum distillation device can be recycled, which is in line with the maximization of resource utilization.
如圖2所示，所述進水槽110中的廢水通過一級高壓泵121和一級進料管122泵入一級納濾膜組120中，所述一級滲透液通過一級滲透液出水管126排出後再通過二級高壓泵131和二級進料管132泵入二級納濾膜組130中，所述一級濃廢液通過一級濃廢液出水管123排出，且該一級濃廢液出水管123上設有一級壓
力錶124和一級調壓閥125，所述二級濃廢液通過二級濃廢液出水管133排出，且該二級濃廢液出水管133上設有二級壓力錶134和二級調壓閥135，所述二級滲透液通過二級滲透液出水管136排出至真空蒸餾裝置200。壓力錶用於顯示壓力，一級調壓閥125用於控制一級納濾膜組產生滲透液和濃廢液的比例，同樣，二級調壓閥135用於控制二級納濾膜組130產生滲透液和濃廢液的比例；納濾膜是20世紀80年代發明的新型分離膜，是介於超濾膜和反滲透膜之間的、根據吸附擴散原理以壓力驅差為驅動力的膜，是一種加壓膜分離技術，即在一定的壓力下，使小分子溶質和溶劑穿過一定孔徑的特製的薄膜，而使大分子溶質不能透過，留在膜的一邊。納濾膜在應用中，對二價及多價金屬離子有較高的截留率，本系統中納濾裝置為二級納濾，以單級納濾膜組串聯方式連接，一級納濾膜組金屬離子截留率可達75%~80%，二級納濾膜組130截留率可達85%~90%，從而使得絕大多數的金屬離子被截留在少量的一級和二級濃廢液中，而滲透液中含有微量的金屬離子可滿足拋光液等使用需求。
As shown in FIG. 2 , the waste water in the
所述一級納濾膜組120和二級納濾膜組130中採用的納濾膜為耐高壓、耐濃酸且能截留二價及二價以上金屬離子的納濾膜。本創作中納濾膜除了對大分子溶質截留外，還對二價及二價以上金屬離子有較高的截留率，因此可以將二價及二價以上金屬離子與酸分離，使得濃縮後的酸液中金屬離子含量符合處理液的標準，確保酸液可以直接回收利用。
The nanofiltration membranes used in the first-stage
所述預處理裝置400中的過濾介質為石英砂、活性炭和無煙煤中的至少一種，該預處理裝置400用於過濾處理液中粒徑大於1μm的固體懸浮物。
The filter medium in the
如圖3所示，所述真空蒸餾裝置200包括蒸發罐210、冷凝器220和緩衝槽240，所述蒸發罐210與真空泵250相連接，該蒸發罐210內部設有加熱管211、底部設有加熱夾套212，該蒸發罐210外部設有廢液入口213、濃縮液出口214、蒸汽入口215、蒸汽水出口216和水汽出口，所述冷凝器220外部設有水汽入口222、
蒸餾水出口223、冷卻水入口224和冷卻水出口225，二級滲透液通過廢液入口213進入蒸發罐210內，加熱蒸汽通過蒸汽入口215進入加熱管211和夾套212對外部的廢液進行加熱，被換熱後的蒸汽變成水經過蒸汽水出口流出蒸發罐210，廢水中被加熱後的水汽經過水汽出口進入冷凝器220中，被濃縮後的廢水濃縮液通過濃縮液出口214排入濃縮液回收槽500，水汽在冷凝器220中被冷卻水冷凝後通過蒸餾水出口排入緩衝槽240，蒸餾水在緩衝槽240中穩定後通過排液泵260泵出回收利用。所述蒸發罐的水汽出口與冷凝器的水汽入口222之間的管路上設有篩檢程式221用於過濾水汽中的雜質，所述蒸發罐中的廢液入口213處設有計量器217用於記錄入水量，所述冷凝器220與緩衝槽240之間還設有計量罐230，所述計量罐230與緩衝槽240之間安裝自動閥231；所述真空整理裝置是在高真空條件下(-80Kpa~-90Kpa)進行的連續蒸餾過程，酸液中水分在低溫下(40℃~50℃)被蒸發分離，可有效提高酸的濃度，同時由於操作溫度遠低於物質常壓下的沸點溫度，且加熱時間非常短，不會對酸液本身造成破壞。
As shown in FIG. 3 , the
本創作金屬表面處理液回收利用系統：包括如下步驟：步驟一：金屬表面處理液使用後流入處理液收集槽300內，處理液收集槽中高金屬離子濃度的含酸廢水通過管路進入預處理裝置400中過濾掉粒徑大於1μm的固體懸浮物後，進入納濾裝置的進水槽110中；步驟二：一級高壓泵121將進水槽110中的廢液泵入一級納濾膜組120，調節一級調壓閥125使一級納濾膜組120的滲透壓維持在4.5Mpa~5.5Mpa之間，一級納濾膜組120在該壓力下將二價及二價以上的金屬離子截留在一級濃廢液中，而通過一級納濾膜組120的一級滲透液排出至二級納濾膜組130；步驟三：二級高壓泵131將一級滲透液泵入二級納濾模組130中，調節二級調壓閥135使二級納濾膜組130的滲透壓維持在5.0Mpa~6.0Mpa之間，二級納濾膜組
130在該壓力下將二價及二價以上的金屬離子進一步截留在二級濃廢液中，而通過二級納濾膜組130的二級滲透液排出至真空蒸餾裝置200；步驟四：含微量金屬離子的二級滲透液在真空蒸餾裝置200中被進一步蒸發濃縮，真空蒸餾裝置200在真空度為80Kpa~90Kpa的條件下，將二級滲透液中水分在溫度為40℃~50℃下蒸發分離，當廢液中的酸濃度升高至預設濃度後真空蒸餾裝置停止運行，含微量金屬離子且含高濃度酸的濃縮液排出蒸發罐並收集於濃縮液回收槽500中以被再利用，同時蒸發的水回收作為工業水使用。最後得到的濃縮液酸的品質百分數可達85%以上，而金屬離子如鋁離子含量極低，符合金屬表面處理劑的使用需求；本創作中通過二級串聯納濾納濾膜組可以去除掉85-90%的金屬離子，通過真空蒸餾裝置將酸濃度提高至85%以上而達到使用需求，同時水也可以被回收利用。
The metal surface treatment liquid recycling system of this invention includes the following steps: Step 1: After the metal surface treatment liquid is used, it flows into the treatment
應當指出，對於本領域的普通技術人員來說，在不脫離本創作構思的前提下，還可以做出若干變形和改進，這些都屬於本創作的保護範圍。因此，本創作專利的保護範圍應以所附請求項為准。 It should be pointed out that for those of ordinary skill in the art, some modifications and improvements can be made without departing from the concept of the present creation, which all belong to the protection scope of the present creation. Therefore, the scope of protection of this patent for creation shall be subject to the appended claims.
100:納濾裝置 100: Nanofiltration device
110:進水槽 110: Intake tank
120:一級納濾膜組 120: First-grade nanofiltration membrane group
121:一級高壓泵 121: First stage high pressure pump
122:一級進料管 122: Primary feed pipe
123:一級濃廢液出水管 123: First-class concentrated waste liquid outlet pipe
124:一級壓力錶 124: Level 1 pressure gauge
125:一級調壓閥 125: Primary pressure regulator
126:一級滲透液出水管 126: Primary permeate outlet pipe
130:二級納濾膜組 130: Secondary Nanofiltration Membrane Group
131:二級高壓泵 131: Secondary high pressure pump
132:二級進料管 132: Secondary feed pipe
133:二級濃廢液出水管 133: Secondary concentrated waste liquid outlet pipe
134:二級壓力錶 134: Secondary pressure gauge
135:二級調壓閥 135: Secondary pressure regulator
136:二級滲透液出水管 136: Secondary permeate outlet pipe
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