Patent Number: 
Section: claims

1. A comprehensive joint technology-based apparatus for treatment of a uranium-contaminated soil, the apparatus comprising:an electrokinetic remediation system including a cathode zone and an anode zone set at both sides of the uranium-contaminated soil, and a cathode and an anode disposed respectively in the cathode and anode zones, the cathode and anode being respectively connected to a power transformer with wires;an elution system including a plurality of sprinklers disposed between the cathode zone and the anode zone forming an array;a pumping system including a pumping well disposed in a vicinity of the cathode zone, with a pumping pipeline therein, wherein the pumping pipeline, a pump and a pumping controller are connected to a water collecting sump sequentially;a soil storage tank disposed adjacent to the water collecting sump;a remediation-separation system having one end connected to the soil storage tank and water collecting sump, with another end connected a soil recovery tank, a ground water recovery tank and a uranium recovery tank;a recharge system including a recharge well set in a vicinity of the anode zone, with a recharge pipeline therein; andan inductively coupled plasma atomic emission spectrometer (ICP-AES) configured to measure residual uranium;wherein the recharge pipeline, and a recharge pump are connected to the ground water storage tank sequentially,wherein the sprinklers are used to spray an eluting solution to the contaminated soil,wherein the eluting solution is a 0.2-0.6 M citric acid solution or a sodium bicarbonate solution, andwherein the remediation-separation system is configured to form a uranyl hydroxide deposit from a suspension containing a uranium compound by illuminating the suspension with fluorescent light;wherein the pumping pipeline and the recharge pipeline are approximately 0.95 m in depth across a phreatic layer; and the cathode and anode are inserted approximately 12 m in depth into the contaminated soil, tangent with the phreatic layer, such that a uranium removal efficiency of at least 80.2% is achieved with an eluting duration of 3 h and an eluting solution volume in soil of 30 ml/g. 2. The apparatus of claim 1, further comprising:a catholyte processing system; andan anolyte processing system,the catholyte processing system including a catholyte storage compartment, a catholyte pH controller and a peristaltic pump;wherein the catholyte pH controller is connected to the catholyte storage compartment, while the catholyte storage compartment is connected to the cathode zone through a corresponding pipeline and a peristaltic pump;the anolyte processing system including an anolyte storage compartment, an anolyte pH controller and a peristaltic pump;the anolyte pH controller is connected to the anolyte storage compartment, while the anolyte storage compartment is connected to the anode zone through the corresponding pipeline and the peristaltic pump. 3. The apparatus of claim 1, wherein the remediation-separation system comprises:a photoelectric remediation device,a screen,a solid phase extraction device,an aqueous phase processing device, anda solid phase processing device;wherein one end of the photoelectric remediation device is connected to the water collecting sump and the soil storage tank, and another end is connected to the screen;wherein the screen is respectively connected to the aqueous phase processing device and the solid phase extraction device;the aqueous phase processing device is connected to the ground water recovery tank; the solid phase extraction device is connected to the solid phase processing device and the uranium recovery tank;the solid phase processing device is connected to the soil recovery tank. 4. The apparatus of claim 1, wherein the pumping pipeline and the recharge pipeline are both non-sand concrete tube wells having an inner diameter of about 250-500 mm and a depth of about 35-50 m, and a periphery filled with backfill and gravels, with a filling layer of about 60-100 mm in thickness. 5. A method for use with the apparatus of claim 1, the method comprising:Step 1: installing the comprehensive joint technology-based apparatus for treatment of uranium-contaminated soil at a site contaminated by uranium;Step 2: spraying an eluting solution via multiple sprinklers to the soil until the concentration of eluting solution in the soil is 10-30 ml/g;Step 3: adding the catholyte and anolyte respectively in the cathode zone and the anode zone, and maintaining a voltage between the cathode and anode of 150-600V via the power transformer; keeping the electrokinetic remediation for 2-8 days, and then uranium substances will migrate to the vicinity of anode, leading to gathering of uranium pollutants;Step 4: during the electrokinetic remediation, starting up the pump to transport contaminated ground water in a phreatic layer to the water collecting sump through the pumping pipeline, with the pumping volume of 5-10 m3/h and lasting for 1.5-6 days;Step 5: if the electrokinetic remediation is finished, excavating the soil in the area within the diameter of 1-2.5 m and the depth of 10-20 m centered on the anode zone, and then transport it to the soil storage tank;Step 6: transporting the contaminated soil in the soil storage tank and the contaminated water in the water collecting sump to the remediation-separation system, and mix the soil and ground water to form a suspension; adjust the pH of the suspension to 2.8-3.5, and irradiate the suspension with fluorescent light for 24-36 h for photolysis remediation, to thereby have a uranium compound in the suspension become a uranyl hydroxide deposit; after the photolysis remediation, separate the soil, water, and the uranyl hydroxide deposit, and respectively transport them to the soil recovery tank, the ground water recovery tank and the uranium recovery tank;Step 7: transporting the soil remedied through the photolysis in the soil recovery tank (16) to the vicinity of the anode zone, and start up the recharge pump to transport the remedied ground water in the ground water recovery tank to the recharge well via the recharge pipeline;Step 8: testing the soil remediation effect with the ICP-AES, and repeating Step 1 to Step 7 if needed until the uranium in the soil meets the requirement of the safety standards or is totally removed;wherein after Step 1, the pumping pipeline and the recharge pipeline are approximately 0.95 m in depth across a phreatic layer; and the cathode and anode are inserted approximately 12 m in depth into the contaminated soil, tangent with the phreatic layer, such that a uranium removal efficiency of at least 80.2% is achieved with an eluting duration of 3 h and an eluting solution volume in soil of 30 ml/g. 6. The method of claim 5, wherein a weight/volume ration of soil and ground water in the suspension in Step 6 is 1 g:(10-20) ml. 7. The method of claim 5, wherein the separation of soil, water and uranyl hydroxide in Step 6 is achieved as follows:when the photolysis remediation is finished, solid substances and the solution in the suspension are separated through the screen having openings with a diameter of about 0.22 micron;transporting the obtained ground water through the separation to the aqueous phase processing device to adjust a neutral pH, and then transporting it to the ground water recovery tank;transporting the obtained soil to the solid phase extraction device to recover the uranyl hydroxide precipitate in the soil with the use of the TBP-sulfonated kerosene extraction technique, and then transporting the recovered uranium substances to the uranium recovery tank; andtransporting remaining soil to the solid phase processing device to adjust a neutral pH, and then transport it to the soil recovery tank.