Steam hot leaching method for sludge treatment
A technology of sludge and heat soaking, which is applied in the direction of pyrolysis sludge treatment, dehydration/drying/concentrated sludge treatment, etc. It can solve the problems of high technical energy consumption and complicated process, and achieve simple reprocessing, simple equipment and economical The effect of energy consumption
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Embodiment 1
[0029] The sludge extraction reactor 2 is equipped with a material frame 3 containing sludge. The upper end of the material frame is open, and the periphery and bottom are 200 mesh ceramic filters. The material frame is hung in the reactor 2, and the material frame is Put 2.5kg of sludge to be treated. The water content of the sludge to be treated is 81.4%, and the dried solid TOC is 217mg / g. It is placed in the material frame 3, the reactor 2 is sealed, and the gauge pressure is evacuated to -0.07MPa.
[0030] The processing flow is as figure 1 As shown, 1.2kg of 200℃ steam is introduced into the reactor 2 from the steam distributor 1 on the upper part of the reactor, and the temperature in the reactor is maintained at 150℃ for 20 hours; the leaching liquid produced during the steam heating and leaching process and The condensed water is collected in the kettle liquid collector 4 at the bottom of the reactor 2.
[0031] After the extraction is completed, it is naturally cooled t...
Embodiment 2
[0034] The sludge leaching reactor 2 is equipped with a material frame 3 containing sludge. The upper end of the material frame is open, and the surrounding and bottom are 300 mesh stainless steel filters. The material frame support is placed in the reactor 2 inside the material frame There are 8 tons of sludge to be processed. The moisture content of the sludge to be treated is 80.8%, the dried solid TOC (total organic carbon) is 214mg / g, the reactor 2 is sealed, and the gauge pressure is evacuated to -0.06MPa.
[0035] Pass 3 tons of 600℃ steam from the steam distributor 1 on the upper part of the reactor into the reactor 2, and keep the temperature in the reactor at 300℃ for 5 hours; the leachate and condensate produced during the steam heating and extraction process Collect at the bottom of reactor 2 to become kettle liquid.
[0036] After the extraction is completed, it is naturally cooled to room temperature, and the kettle liquid is discharged at a time; the residual sludge...
Embodiment 3
[0039] The same parts as in Example 2 will not be described again, and the difference is that there are two sets of sludge leaching reactors 2, which operate alternately. First, after the leaching of the first reactor is complete, the exhaust steam in it is released into the second reactor to be heated 2; after the pressure is released, 1.5 tons of fresh steam at 300°C is continued to flow into the second reactor. In the two reaction kettles 2, there are 4.5 tons of sludge to be processed in the material frame. Keep the temperature in the kettle at 200°C for 10 hours.
[0040] Using two sets of devices for hot extraction can save steam consumption and lower the cost. For the first set of equipment operating alternately, before the reaction, the moisture content of the sludge to be treated was 82.3%, and the TOC value of the dry sludge was 221mg / g; after the treatment, the TOC of the sludge biscuit base was 61mg / g, which was the original sludge. 27.6% of mud TOC, BOD of easily bi...
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