A Salt Wastewater Treatment System Inhibiting Scaling
A technology for saline wastewater and treatment systems, applied in multi-stage water treatment, water/sewage treatment, water/sewage multi-stage treatment, etc., can solve problems such as large scaling risks, achieve inhibition or elimination of scaling, and increase exposure The effect of surface and high concentration treatment efficiency
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Embodiment 1
[0045] figure 1 A schematic diagram of the modular structure of the saline wastewater treatment system of the present invention is shown. Such as figure 1 As shown, the wastewater treatment system of the present invention at least includes a wastewater softening unit 1 , a wastewater reduction unit 2 , an electrodialysis unit 3 , a tubular microfiltration unit 4 and a dosing unit 5 .
[0046] The wastewater softening unit 1 at least includes a homogeneous water tank 101, a coagulation tank 102, a flocculation tank 103, a sedimentation tank 104, a first filter 105 and a first intermediate tank 106, wherein the waste water is in the homogeneous water tank 101, the coagulation tank 102, The transfer flow between the flocculation tank 103 and the sedimentation tank 104 can provide transfer driving force through several lift pumps. The homogeneous water tank 101 is used to improve the uneven distribution of dispersed substances in the waste water, which can make the waste water g...
Embodiment 2
[0058] This embodiment is a further improvement on Embodiment 1, and repeated content will not be repeated here.
[0059] figure 2 with image 3 Two different modes of operation of the electrodialyzer are shown. Such as figure 2 with image 3As shown, the electrodialyzer 301 has a cathode 305 and an anode 306 corresponding to each other, wherein the anode is arranged at the left end of the casing 309, and the cathode is arranged at the right end of the casing. Two anion exchange membranes and two cation exchange membranes arranged alternately at intervals are arranged between the cathode and the anode. In the direction extending from the anode to the cathode, there are cation exchange membranes, anion exchange membranes, cation exchange membranes, and anion exchange membranes in sequence, so that two concentrated waters that are mirror-symmetrical to the fresh water chamber 308 are defined by the anion exchange membranes and the cation exchange membranes Room 307.
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Embodiment 3
[0072] This embodiment is a further improvement on Embodiment 1 and Embodiment 2, and repeated content will not be repeated here.
[0073] Figure 4 It shows another preferred treatment process of saline wastewater in the present invention. Such as Figure 4 As shown, for the convenience of description, a fresh water chamber and a concentrated water chamber defined by one first ion exchange membrane and two second ion exchange membranes are defined as a membrane stack unit 6 . N membrane stack units can be set between the cathode and anode of the electrodialyzer as required, where N≥1.
[0074] Preferably, the electrodialysis unit further includes a first booster pump 601, a second booster pump 602, a first reversing valve 603, a second reversing valve 604, N membrane stack units 6, a first exchange tube 605 and a second reversing valve Two exchange tubes 606 . The second intermediate water tank can communicate with the first exchange pipe and the second exchange pipe resp...
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