SYSTEM AND METHOD FOR CONTROLING AMOUNT OF LIQUID CARBON SOURCE RELEASED TO CONSTRUCTED WETLAND

Abstract

A system for controlling the amount of a liquid carbon source released to a constructed wetland, includes: a carbon source pool, a carbon source pipe, a peristaltic pump, a programmable logic controller (PLC), a computer, a first flow meter, a first chemical oxygen demand (COD) sensor, a first total nitrogen (TN) sensor, a second TN sensor, a second COD sensor, an inlet pipe, and an outlet pipe. The first flow meter, the first COD sensor, and the TN sensor are disposed on the inlet pipe; the second COD sensor and the second TN sensor are disposed on the outlet pipe; the inlet pipe and the outlet pipe are connected to the constructed wetland; the carbon source pipe is connected to the carbon source pool via the peristaltic pump; the computer, the peristaltic pump, the first flow meter, and all sensors are connected to the PLC controller.

Claims

1. A system for controlling the amount of a liquid carbon source released to a constructed wetland, the system comprising: a carbon source pool, a carbon source pipe, a peristaltic pump, a programmable logic controller (PLC), a computer, a first flow meter, a first chemical oxygen demand (COD) sensor, a first total nitrogen (TN) sensor, a second TN sensor, a second COD sensor, an inlet pipe, and an outlet pipe; wherein: the first flow meter, the first COD sensor, and the TN sensor are disposed on the inlet pipe; the second COD sensor and the second TN sensor are disposed on the outlet pipe; the inlet pipe and the outlet pipe are connected to the constructed wetland; the carbon source pipe is connected to the carbon source pool via the peristaltic pump; the computer, the peristaltic pump, the first flow meter, and all sensors are connected to the PLC controller; and the first flow meter is configured to measure a flow of an influent to the constructed wetland; the first COD sensor is configured to monitor a concentration of COD (COD.sub.in) in the influent; the first TN sensor is configured to monitor a concentration of TN (TN.sub.in) in the influent; the second TN sensor is configured to monitor a concentration of TN (TN.sub.out) in an effluent from the constructed wetland; and the second COD sensor is configured to monitor a concentration of COD (COD.sub.out) in the effluent.

2. The system of claim 1, wherein the system further comprises a carbon source powder bag and a stirrer both disposed in the carbon source pool; the carbon source bag is used to hold a carbon source prepared from plants; the carbon source is mixed with water and stirred by the stirrer to form the liquid carbon source.

3. The system of claim 1, wherein the system further comprises a second flow meter disposed on the carbon source pipe and connected to the PLC controller to monitor the flow of the liquid carbon source released to the constructed wetland.

4. The system of claim 1, wherein the system further comprises a water distribution channel disposed between the inlet pipe and the constructed wetland; and a water temperature sensor, a dissolved oxygen (DO) sensor, a turbidity sensor, a pH sensor, and a conductivity sensor are disposed in the water distribution channel.

5. A method for controlling an amount of a liquid carbon source released to a constructed wetland for treatment of polluted water using the system of claim 1, the method comprising: S1. disposing the carbon source pipe in a water distribution channel in the constructed wetland; S2. gathering aquatic plant straws from the constructed wetland; grinding the aquatic plant straws into powders; and soaking the powders in the carbon source pool; passing a resulting mixture through a filter so that the liquid carbon source is separated from carbon residues; S3. receiving, by the PLC controller, data from the first flow meter, the first COD sensor, the first TN sensor, the second TN sensor, and the second COD sensor; and sending the data to the computer to calculate a preset volume (V) of the liquid carbon source to be released to the constructed wetland; S4. calculating the preset volume (V) of the liquid carbon source released to the constructed wetland according to following formula:
V=(Q*(5*(TN.sub.in−TN.sub.out)−(COD.sub.in−COD.sub.out))/COD equivalent of carbon source from plant)/ρ; where, V is a volume of the liquid carbon source; Q is a volume flow rate of the influent flowing into the constructed wetland (unit: m.sup.3/d); TN.sub.in is a concentration of total nitrogen (TN) in the influent flowing into the constructed wetland (unit: mg/L); TN.sub.out t is a concentration of total nitrogen in the qualified effluent flowing out of the constructed wetland (unit: mg/L); COD.sub.in is a concentration of COD in the influent flowing into the constructed wetland (unit: mg/L); COD.sub.out is a concentration of COD in the qualified effluent flowing out of the constructed wetland (unit mg/L); and ρ is a density of the liquid carbon source (unit: 1.0 g/mL); when the influent has a ratio of COD.sub.in to TN.sub.in of greater than 6, the carbon source is not an impact factor hindering denitrification in the constructed wetland, and thus the liquid carbon source is not released; and S5. sending the preset volume to the PLC controller; and controlling, by the PLC controller, operations of the peristaltic pump and a regulating valve connected to the peristaltic pump, so that the preset volume (V) of the liquid carbon source is added to the constructed wetland via the carbon source pipe; and monitoring, by a second flow meter disposed on the carbon source pipe and connected to the PLC controller, the flow of the liquid carbon source released to the constructed wetland.

6. The method of claim 5, wherein the computer acquires the data from an online monitoring device that monitors the flow, TN concentration and COD concentration of the influent in real time.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

[0026] FIG. 1 is a schematic diagram of a system for controlling the amount of a liquid carbon source released to a constructed wetland for purifying polluted water according to one embodiment of the disclosure; and

[0027] FIG. 2 is a flow chart of a method for controlling the amount of a liquid carbon source prepared from aquatic plants and released to a constructed wetland for purifying polluted water according to one embodiment of the disclosure.

[0028] In the drawings, the following reference numbers are used: 1. PLC controller, 2. Computer; 3. Carbon source pool; 4. Carbon source powder bag; 5. Peristaltic pump; 6. Inlet pipe; 7. First water quality sensor; 8. Stirrer; 9. Water distribution channel; 10. Wetland pool; 11. Carbon source pipe; 12. Wetland plants; 13. Water catchment channel; 14. Outlet pipe; 15. Second water quality sensor; 16. First flow meter; and 17. Second flow meter.

DETAILED DESCRIPTION

[0029] The disclosure gathers aquatic plants from the constructed wetland to prepare a liquid carbon source and provides a system by which a desired volume of the liquid carbon source is calculated and added to the constructed wetland for purifying polluted water.

[0030] Referring to FIG. 1, the system comprises a carbon source pool 3, a carbon source pipe 11, a peristaltic pump 5, a PLC controller 1, a computer 2, a first flow meter 16, a first water quality sensor 7, a second water quality sensor 15, a second flow meter 17, a carbon source powder bag 4 and a stirrer 8. The carbon source pipe 11 is connected to the carbon source pool 3 via the peristaltic pump 5. The second flow meter 17 is disposed on the carbon source pipe 11 to monitor the volume of the liquid carbon source released to the constructed wetland. The carbon source bag is used to hold a carbon source prepared from plants. The carbon source is then mixed with water and stirred thoroughly by the stirrer to form the liquid carbon source. The disclosure designs a submerged surface flow constructed wetland for use in combination with the system to precisely control the amount of the liquid carbon source. The artificial wetland comprises a wetland pool 10, wetland plants 12, a water distribution channel 9, a water catchment channel 13, an inlet pipe 6, an outlet pipe 14; the wetland plants 12 are arranged in the wetland pool 10; the water distribution channel 9 and the water catchment channel 13 are disposed on both ends of the wetland pool 10; the water distribution channel 9 comprises a side wall on which the inlet pipe 6 is disposed; the water catchment channel 13 comprises a side wall on which the outlet pipe 14 is disposed on; the first flow meter 16 and the first water quality sensor 7 are disposed on the inlet pipe 6; the first water quality sensor 7 comprises a first COD sensor and a TN sensor configured to monitor the concentrations of COD and TN in the influent, respectively; the second water quality sensor 15 is disposed on the outlet pipe 14 and comprises a second COD sensor and a second TN sensor configured to monitor the COD and TN in the effluent, respectively. The computer 2, the peristaltic pump 5, the second flow meter 17, the first flow meter 16, and all sensors are connected to the PLC controller 1.

[0031] The first flow meter is configured to measure the flow of the influent flowing into the constructed wetland; the first COD sensor is configured to monitor the concentration of COD (COD.sub.in) in the influent; the first TN sensor is configured to monitor the concentration of TN (TN.sub.in) in the influent; the second TN sensor is configured to monitor the concentration of TN (TN.sub.out) in the effluent; the second COD sensor is configured to monitor the concentration of COD (COD.sub.out) in the effluent.

[0032] The system further comprises a water temperature sensor, a DO sensor, a turbidity sensor, a pH sensor, and a conductivity sensor, all of which are disposed in the water distribution channel 9 and connected to the PLC controller 1; the water temperature sensor is configured to measure the influent temperature; the DO sensor is configured to measure the amount of DO in the influent; the influent temperature and the DO concentration are key indexes for determining the ability of the constructed wetland to perform nitrification and denitrification, thereby analyzing the ability of the constructed wetland to remove contaminations; the turbidity sensor, the pH sensor, and the conductivity sensor are configured to monitor the turbidity, pH value, and the conductivity of the influent, respectively, which are auxiliary indexes for determining the influent quality of the constructed wetland.

[0033] FIG. 2 is a flow chart illustrating a precise control of the amount of a liquid carbon source released to a constructed wetland. The following more details are described by reference to FIGS. 1 and 2.

[0034] Rural wastewater was treated and discharged to the constructed wetland for high-level treatment. The constructed wetland was 200 m.sup.3/d in size. The effluent quality of the constructed wetland should meet the emission requirements issued by “Environmental Quality Standards for Surface Water” (GB3838-2002).

[0035] The water quality of the constructed wetland was determined as follows:

TABLE-US-00001 TABLE 1 Indexes of influent and effluent of constructed wetland Contaminant COD.sub.Cr mg/L TN mg/L Influent quality 25 6.5 effluent quality 20 1.0

1. PREPARATION A LIQUID CARBON SOURCE FROM AQUATIC PLANTS IN CONSTRUCTED WETLAND

[0036] Common aquatic plants such as reed, yellow calamus, shallot and calamus, were gathered from the constructed wetland and ground into powders with a length of 1-1.5 cm and a width of 0.3-0.5 cm by a pulverizer. The carbon source powder bag 4 was disposed in the carbon source pool; the powders were placed in the carbon source powder bag 4; the water was added to the carbon source pool to soak the powders; the amount of the carbon source pool was 50 L; according to the laboratory test results, an optimal solubility of a carbon source in water was achieved by soaking 500 g of the powders in the water for 24 hours and thoroughly mixing the mixture by the stirrer 8.

2. DETERMINATION OF THE AMOUNT OF THE LIQUID CARBON SOURCE

[0037] The influent quality was monitored and analyzed to determine COD.sub.in of 25 mg/L and TN.sub.in of 6.5 mg/L. When COD.sub.in/TN.sub.in was less than 6, the carbon source was considered a major factor affecting denitrification in the constructed wetland. The PLC controller 1 controlled the peristaltic pump 5 to pump the liquid carbon source into the constructed wetland.

[0038] The computer 2 used formulas to determine that the effluent quality met the emission requirements issued by “Environmental Quality Standards for Surface Water” (GB3838-2002). According to the engineering experience, the density of the liquid carbon source was estimated to be 1000 kg/m.sup.3; the COD equivalent of the liquid carbon source from aquatic plants (such as yellow calamus) was estimated to be 0.159 (g.Math.COD)/g; and the amount of the liquid carbon source released to the constructed wetland was calculated as follows:

[00001]$\begin{array}{c}V=(Q^{*}\left(5^{*}\left(T{N}_{\mathrm{in}}-T{N}_{\mathrm{out}}\right)-\left(CO{D}_{\mathrm{in}}-CO{D}_{\mathrm{out}}\right)\right)/\mathrm{COD}\\ \mathrm{equivalent}\mathrm{of}\mathrm{plant}\mathrm{carbon}\mathrm{source})/\rho ;\\ =(200m^3/d*\left(5g/m^3{(}^{*}6.5-10\right)-\\ \left(25\right)20g/m^3)/0.159\left(g.\mathrm{COD}\right)/g)/\rho =\\ 28301\mathrm{mL}\approx 28.3L\end{array}$

[0039] The volume calculated was input to the PLC controller 1 by the computer 2, and the PLC controller 1 controlled the peristaltic pump 5 to pump the liquid carbon source into the constructed wetland.

[0040] According to the engineering experience, the maximum volume (V.sub.max) of the carbon source pool was 50 L.

[0041] When the volume (V) of the liquid carbon source was greater than or equal to the maximum volume (V.sub.max) of the carbon source pool, the amount of the liquid carbon source released to the constructed wetland was controlled to be 50 L by the PLC controller.

3. RELEASE OF THE LIQUID CARBON SOURCE TO THE CONSTRUCTED WETLAND

[0042] 28.3 L of the liquid carbon source was released to the constructed wetland a day. The peristaltic pump 5 offered a flow rate of greater than or equal to 28.3 L/d (i.e. 19.65 mL/min). The liquid carbon source was pumped through the water distribution channel 9 and directed into the constructed wetland.

4. EFFLUENT QUALITY MONITORING

[0043] The hydraulic retention time was 0.87 d; the liquid carbon source was released at time T0; the denitrification started to occur at time T1; T1=T0+0.87 d; the sludge age for denitrification in the subsurface flow constructed wetland was 3 d according to engineering experience and literature data; the denitrification stopped at T2; T2=T0+0.87 d+3 d.

[0044] The effluent quality was monitored at T0, T1 and T2; when the TN in the effluent was not removed to a low concentration after T2 and the ratio of COD.sub.Cr to TN was equal to or lower than 6, the computer 2 repeated the step 2 and the liquid carbon source was then released to the constructed wetland.

[0045] It will be obvious to those skilled in the art that changes and modifications may be made, and therefore, the aim in the appended claims is to cover all such changes and modifications.