CN204675941U - A kind of equipment of microwave purifying process heavy metal ion-containing waste water - Google Patents
A kind of equipment of microwave purifying process heavy metal ion-containing waste water Download PDFInfo
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- CN204675941U CN204675941U CN201520268201.XU CN201520268201U CN204675941U CN 204675941 U CN204675941 U CN 204675941U CN 201520268201 U CN201520268201 U CN 201520268201U CN 204675941 U CN204675941 U CN 204675941U
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- 229910001385 heavy metal Inorganic materials 0.000 title claims abstract description 55
- 238000000034 method Methods 0.000 title claims abstract description 55
- 239000002351 wastewater Substances 0.000 title claims abstract description 48
- 238000001704 evaporation Methods 0.000 claims abstract description 85
- 230000008020 evaporation Effects 0.000 claims abstract description 82
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 64
- 239000007788 liquid Substances 0.000 claims abstract description 44
- 239000012153 distilled water Substances 0.000 claims abstract description 30
- 239000000463 material Substances 0.000 claims abstract description 29
- 238000007599 discharging Methods 0.000 claims abstract description 14
- 238000009413 insulation Methods 0.000 claims description 11
- 239000004810 polytetrafluoroethylene Substances 0.000 claims description 6
- 229920001343 polytetrafluoroethylene Polymers 0.000 claims description 6
- 239000000919 ceramic Substances 0.000 claims description 3
- 239000011358 absorbing material Substances 0.000 claims description 2
- 150000001875 compounds Chemical class 0.000 claims description 2
- 239000011159 matrix material Substances 0.000 claims description 2
- 150000004767 nitrides Chemical class 0.000 claims description 2
- 239000010814 metallic waste Substances 0.000 abstract 1
- 150000002500 ions Chemical class 0.000 description 41
- 238000010438 heat treatment Methods 0.000 description 15
- 238000009833 condensation Methods 0.000 description 12
- 230000005494 condensation Effects 0.000 description 12
- 238000002425 crystallisation Methods 0.000 description 12
- 230000008025 crystallization Effects 0.000 description 12
- 239000012535 impurity Substances 0.000 description 7
- 238000007865 diluting Methods 0.000 description 6
- 238000009854 hydrometallurgy Methods 0.000 description 6
- 229920000742 Cotton Polymers 0.000 description 5
- 239000012141 concentrate Substances 0.000 description 5
- 230000006866 deterioration Effects 0.000 description 5
- 230000000694 effects Effects 0.000 description 5
- 238000005265 energy consumption Methods 0.000 description 5
- 230000003628 erosive effect Effects 0.000 description 5
- 230000002209 hydrophobic effect Effects 0.000 description 5
- 230000000873 masking effect Effects 0.000 description 5
- 239000002245 particle Substances 0.000 description 5
- 238000000746 purification Methods 0.000 description 5
- 230000005855 radiation Effects 0.000 description 5
- 238000011084 recovery Methods 0.000 description 5
- 239000012780 transparent material Substances 0.000 description 5
- 229910010293 ceramic material Inorganic materials 0.000 description 4
- HBMJWWWQQXIZIP-UHFFFAOYSA-N silicon carbide Chemical compound [Si+]#[C-] HBMJWWWQQXIZIP-UHFFFAOYSA-N 0.000 description 4
- 229910010271 silicon carbide Inorganic materials 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 3
- 229910021645 metal ion Inorganic materials 0.000 description 3
- TWNQGVIAIRXVLR-UHFFFAOYSA-N oxo(oxoalumanyloxy)alumane Chemical compound O=[Al]O[Al]=O TWNQGVIAIRXVLR-UHFFFAOYSA-N 0.000 description 3
- 239000013535 sea water Substances 0.000 description 3
- 230000005540 biological transmission Effects 0.000 description 2
- 230000007797 corrosion Effects 0.000 description 2
- 238000005260 corrosion Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000007701 flash-distillation Methods 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 238000005554 pickling Methods 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 238000009834 vaporization Methods 0.000 description 2
- 230000008016 vaporization Effects 0.000 description 2
- 229910052581 Si3N4 Inorganic materials 0.000 description 1
- 238000003723 Smelting Methods 0.000 description 1
- 239000003905 agrochemical Substances 0.000 description 1
- 239000003125 aqueous solvent Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 238000003889 chemical engineering Methods 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000010612 desalination reaction Methods 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 238000005868 electrolysis reaction Methods 0.000 description 1
- -1 ferrous metals Chemical class 0.000 description 1
- 239000013505 freshwater Substances 0.000 description 1
- 238000002386 leaching Methods 0.000 description 1
- 238000005272 metallurgy Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000003973 paint Substances 0.000 description 1
- 238000007747 plating Methods 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- HQVNEWCFYHHQES-UHFFFAOYSA-N silicon nitride Chemical compound N12[Si]34N5[Si]62N3[Si]51N64 HQVNEWCFYHHQES-UHFFFAOYSA-N 0.000 description 1
- 238000010977 unit operation Methods 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- 239000010878 waste rock Substances 0.000 description 1
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- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model relates to a kind of equipment of microwave purifying process heavy metal ion-containing waste water, belongs to microwave metallurgical technical field.This equipment Central Plains batch can passes through fresh feed pump successively, by-pass valve control pipeline connects high-pressure nozzle, high-pressure nozzle arrives evaporation chamber through evaporator room side, evaporator room top and bottom are respectively equipped with vapour outlet and dense material liquid outlet, dense material liquid outlet is divided into two pipelines by discharging pump, a pipeline connection control valve, another pipeline returns high-pressure nozzle pipeline by by-pass valve control, by evaporation bed stationary platen, porous is installed below evaporation chamber high-pressure nozzle and inhales ripple evaporation bed, porous is inhaled ripple evaporation bed surface and is provided with hole, evaporator room top is provided with scum dredger, evaporator room surrounding is provided with thermopair and microwave source according to practical situation, vapour outlet successively with steam condenser, distilled water holding tank is connected with vacuum pump.The utility model not only solves a nonferrous metal waste water process difficult problem, and makes heavy metal ion realize resource utilization.
Description
Technical field
The utility model relates to a kind of equipment of microwave purifying process heavy metal ion-containing waste water, belongs to microwave metallurgical technical field.
Background technology
Along with the fast development of China's industry, heavy metal wastewater thereby quantum of output is increasing.These waste water are mainly from various trade effluents such as mine drainage, waste rock pile leaching water, the mine tailing draining of ore dressing field, non-ferrous metals smelting works' draining, Non-ferrous Metals Processing Factory's pickling waste waters, Electroplate Factory's plating piece washing water, Steel Plant's pickling draining and electrolysis, agricultural chemicals, medicine, paint and dyestuffs.How efficiently to process these heavy metal wastewater therebies, and make it resource utilization, become the problem that people pay close attention to jointly.Evaporation is one of effective way of process heavy metal ion-containing waste water.As one of important chemical engineering unit operation, evaporation is the method with heating, makes solution in condenser, realize condensation, concentrated technology by moisture wherein or after having the vaporization of volatile solvent content under boiling state.Therefore, evaporative process is a heat transfer process, and heat transfer efficiency and speed are the controlling units of evaporative process.For metallurgical, chemical field, evaporation is also one of maximum operating unit of energy consumption.Such as, the concentration and evaporation aspect of aluminum oxide industry seed precipitation solution, evaporation energy consumption accounts for 20 ~ 25% of total production energy consumption, and evaporation cost accounts for 10 ~ 12% of total cost of production.Visible, the raising of evaporization process efficiency, the development of the reduction of energy consumption to fields such as metallurgy, chemical industry have important pushing effect.
At present, the be divided into single-action of evaporation equipment, multiple-effect, secondary steam compression and Multi-stage flash hairdo, multiple-effect Multi-stage flash hairdo etc.Single-effect evaporation efficiency is low, and in order to improve vaporization efficiency, evaporation equipment develops to multiple-effect evaporation gradually.Multi-effect evaporation system is more complicated, and triple effect evaporation needs three pumps, three evaporating pots, three cover heat-exchange systems, and these equipment all need high temperature resistant and withstand voltage, and manufacturing cost is higher.Another because a few effect solution temperature is higher below, corrosion and the damage of pump valve can be caused, thus further increase running cost.
No matter be multiple-effect evaporation, flash distillation or the combination of two kinds of modes, all also there are some core difficult problems needs to solve.First, the heat required for evaporation is mainly derived from heat exchange, and the thermal source usually adopted is steam heat-exchanging mode; No matter adopt that heat-exchanger rig, all there is larger heat loss amount.Secondly, interchanger needs to bear the High Temperature High Pressure impact of hot steam and the corrosion of material, causes have a strong impact on the steady running of equipment.3rd, the impurity composition in solution easily produces fouling on interchanger wall, and heat exchange efficiency is sharply declined, and energy consumption level sharply rises.4th, feed liquid flows into flashing chamber and evaporator room with fluid column shape, and vapour-liquid ratio surface-area is less, and the water molecules of fluid column or large drop internal, due to the constraint effect of surrounding molecular, is difficult to be evaporated.5th, under the high vacuum condition of flashing chamber and evaporator room, drop needs energy that more water molecules is overflowed as steam, but now energy all cannot be passed to drop by transmission of heat by convection and heat trnasfer.
Microwave has been widely used in evaporating and concentrating process, as bright patent CN1579950A " desalination method of sea water by microwave transmission ", the method utilizes the seawater in microwave irradiation distillation pond, makes evaporation of seawater become water vapor, then water vapor is cooled to the method for fresh water.For another example utility model patent CN2880206Y " microwave heating concentrating apparatus ", by installing ultrasonic element bottom evaporator room, makes solvent be atomized, then the microwave component by being, bottom evaporator room heats fog, reaches the object of evaporation concentration.Utilize Microwave Heating aqueous solvent fogmeter face, without coal, greatly save equipment such as evaporation auxiliary facility and evaporation tubes valve etc.
Summary of the invention
For above-mentioned prior art Problems existing and deficiency, the utility model provides a kind of equipment of microwave purifying process heavy metal ion-containing waste water.The utility model heavy metal ion-containing waste water is made through liquid and is dripped, drop flash distillation, carries out high-efficiency evaporating after the step such as microwave reinforced, high vacuum steam discharge and obtain distilled water and concentrated heavy metal ion-containing waste water, and the utility model is achieved through the following technical solutions.
An equipment for microwave purifying process heavy metal ion-containing waste water, comprises head tank 1, cleaner 2, microwave source 3, scum dredger 4, thermopair, vapour outlet 6, high-pressure nozzle 7, evaporator room 8, porous inhales ripple evaporation bed 9, steam condenser 10, distilled water holding tank 11, vacuum pump 12, by-pass valve control, discharging pump 15, dense material liquid outlet 16, fresh feed pump 19, evaporation bed stationary platen 20 and hole 21, described head tank 1 is successively by fresh feed pump 19, by-pass valve control pipeline connects high-pressure nozzle 7, head tank 1 inner lower is provided with cleaner 2, it is inner that high-pressure nozzle 7 arrives evaporator room 8 through evaporator room 8 side, evaporator room 8 top and bottom are respectively equipped with vapour outlet 6 and dense material liquid outlet 16, dense material liquid outlet 16 is divided into two pipelines by discharging pump 15, a pipeline connection control valve, another pipeline returns high-pressure nozzle 7 pipeline by by-pass valve control, by evaporation bed stationary platen 20, porous is installed below evaporator room 8 internal high pressure shower nozzle 7 and inhales ripple evaporation bed 9, porous is inhaled ripple evaporation bed 9 surface and is provided with hole 21, by porous microwave evaporation bed 9, feed liquid can be realized with drop and liquid film two kinds of mode evaporation concentration, the microwave that microwave-absorbing ceramic absorbs can be passed to liquid film and drop with heat mode stereoscopic and omnibearing by evaporation bed 9 and hole 21 simultaneously, evaporator room 8 top is provided with scum dredger 4, evaporator room 8 surrounding is provided with thermopair and microwave source 3 according to practical situation, vapour outlet 6 successively with steam condenser 10, distilled water holding tank 11 is connected with vacuum pump 12.
Described high-pressure nozzle 7 adopts the modified and reinforced King of PTFE to process, and it has fabulous temperature tolerance (-200 to+260 DEG C), the not resistance to viscosity of erosion resistance, resistance to deterioration, hydrophobic and machinability; Meanwhile, it is that electromagnetic wave transparent material does not absorb microwave substantially, thus ensures the even of evaporator room Space Microwave under multimode radiation.
Be provided with thermal insulation layer between described evaporator room 8 and microwave source 3, thermal insulation layer material is mainly insulating cotton.
The absorbing material that it is matrix that described porous suction ripple evaporation bed 9 adopts with oxide compound, nitride or carbide ceramics material is made, as silicon carbide, aluminum oxide, silicon nitride etc.
Described hole 21 aperture is 1 ~ 4mm.
An equipment use method for above-mentioned microwave purifying process heavy metal ion-containing waste water, its concrete steps are as follows:
Step 1, pressure regulate: be first 0.01 ~ 0.03Mpa by vacuum pump 12 by the pressure-controlling of evaporator room 8 and steam condenser 10;
Step 2, purification: joined by heavy metal ion-containing waste water in head tank 1, in head tank 1, cleaner 2 removes macrobead or Conglobation type impurity in heavy metal ion-containing waste water, as sandstone, the solidifying wadding of organism etc.;
Step 3, make drip and masking: then go deimpurity heavy metal ion-containing waste water by fresh feed pump 19 and high-pressure nozzle 7, the drop making heavy metal ion-containing waste water form particle diameter 1 ~ 3mm enters evaporator room 8, in droplets fall process, absorb microwave concentrate, the porous suction ripple evaporation bed 9 arrived in evaporator room 8 when drop forms liquid film and drop;
Step 4, microwave evaporation: while carry out step 3, open the microwave source 3 of evaporator room 8, adopt the drop in microwave direct heating evaporator room 8 and liquid film, porous is inhaled ripple evaporation bed 9 and is absorbed micro-wave energy simultaneously, and indirect heating liquid film and whole evaporator room 8 obtain water vapour;
Step 5, product collection: the water vapour obtained through step 4 is after scum dredger 4, overflowed from evaporator room 8 fast by negative pressure mode, enter steam condenser 10 condensation, water of condensation reclaims through distilled water holding tank 11 and obtains distilled water, and obtains concentrated containing heavy metal solution;
Step 6, product circulation utilize: the distilled water that recovery obtains is as hydrometallurgy each workshop section diluting water or boiler wash water, and directly returning electrolytic process Footwall drift ion containing heavy metal solution or forming metal-salt crystallization through secondary microwave evaporative crystallization after concentrated is reclaimed.
The beneficial effects of the utility model are:
1, adopt fresh feed pump and high-pressure nozzle that heavy metal ion-containing waste water is sprayed into evaporator room with drops, and adopt microwave heater directly at evaporation heating indoor drop-wise waste water, utilize microwave to heat advantage rapidly to drop, can reach efficient, fast, the effect of moisture in preferential evaporation drop.
2, when drop falls within porous suction ripple evaporation bed, form liquid film, microwave is by directly heating liquid film with indirect two kinds of modes.
3, water of condensation is reclaimed as hydrometallurgy each workshop section diluting water or boiler wash water; After concentrated containing heavy metal ion solution, directly return electrolytic process Footwall drift ion or form metal-salt crystallization through secondary microwave evaporative crystallization and reclaim.
Accompanying drawing explanation
Fig. 1 is the utility model device structure schematic diagram;
Fig. 2 is the utility model evaporator room local structure schematic diagram;
Fig. 3 is the utility model process flow sheet.
In figure: 1-head tank, 2-cleaner, 3-microwave source, 4-scum dredger, 5-thermopair I, 6-vapour outlet, 7-high-pressure nozzle, 8-evaporator room, 9-porous inhales ripple evaporation bed, 10-steam condenser, 11-distilled water holding tank, 12-vacuum pump, 13-by-pass valve control I, 14-by-pass valve control II, 15-discharging pump, the dense material liquid outlet of 16-, 17-thermopair II, 18-by-pass valve control III, 19-fresh feed pump, 20-evaporates bed stationary platen, 21-hole.
Embodiment
Below in conjunction with the drawings and specific embodiments, the utility model is described in further detail.
Embodiment 1
As illustrated in fig. 1 and 2, the equipment of this microwave purifying process heavy metal ion-containing waste water, comprises head tank 1, cleaner 2, microwave source 3, scum dredger 4, thermopair, vapour outlet 6, high-pressure nozzle 7, evaporator room 8, porous inhales ripple evaporation bed 9, steam condenser 10, distilled water holding tank 11, vacuum pump 12, by-pass valve control, discharging pump 15, dense material liquid outlet 16, fresh feed pump 19, evaporation bed stationary platen 20 and hole 21, described head tank 1 is successively by fresh feed pump 19, by-pass valve control III 18 pipeline connects high-pressure nozzle 7, head tank 1 inner lower is provided with cleaner 2, it is inner that high-pressure nozzle 7 arrives evaporator room 8 through evaporator room 8 side, evaporator room 8 top and bottom are respectively equipped with vapour outlet 6 and dense material liquid outlet 16, dense material liquid outlet 16 is divided into two pipelines by discharging pump 15, a pipeline connection control valve I 13, another pipeline returns high-pressure nozzle 7 pipeline by by-pass valve control II 14, by evaporation bed stationary platen 20, porous is installed below evaporator room 8 internal high pressure shower nozzle 7 and inhales ripple evaporation bed 9, porous is inhaled ripple evaporation bed 9 surface and is provided with hole 21, evaporator room 8 top is provided with scum dredger 4, evaporator room 8 surrounding is provided with thermopair and microwave source 3, thermopair I 5 is inserted into evaporator room 8 top, thermopair II 17 inserts from evaporator room 8 side and arrives to porous suction ripple evaporation bed 9, vapour outlet 6 successively with steam condenser 10, distilled water holding tank 11 is connected with vacuum pump 12.
Wherein high-pressure nozzle 7 adopts the modified and reinforced King of PTFE to process, and it has fabulous temperature tolerance (-200 to+260 DEG C), the not resistance to viscosity of erosion resistance, resistance to deterioration, hydrophobic and machinability; Meanwhile, it is that electromagnetic wave transparent material does not absorb microwave substantially, thus ensures the even of evaporator room Space Microwave under multimode radiation; Be provided with thermal insulation layer between evaporator room 8 and microwave source 3, thermal insulation layer material is mainly insulating cotton; Porous is inhaled ripple evaporation bed 9 and is adopted silicon carbide microwave-absorbing ceramic material to make; Hole 21 aperture is 1mm.
As shown in Figure 3, the equipment use method of this above-mentioned microwave purifying process heavy metal ion-containing waste water, its concrete steps are as follows:
Step 1, pressure regulate: be first 0.01Mpa by vacuum pump 12 by the pressure-controlling of evaporator room 8 and steam condenser 10;
Step 2, purification: by 30L containing Zn
2+the effluent containing heavy metal ions of 1mg/L joins in head tank 1, and in head tank 1, macrobead sandstone impurity in heavy metal ion-containing waste water removed by cleaner 2, prevents drop impurity blocking high shower nozzle 7 and wearing and tearing pipeline;
Step 3, make drip and masking: then go deimpurity heavy metal ion-containing waste water by fresh feed pump 19 and high-pressure nozzle 7, the drop making heavy metal ion-containing waste water form particle diameter 3mm enters evaporator room 8, in droplets fall process, absorb microwave concentrate, the porous suction ripple evaporation bed 9 arrived in evaporator room 8 when drop forms liquid film and drop;
Step 4, microwave evaporation: while carry out step 3, open the microwave source 3 of evaporator room 8, adopt the drop in microwave direct heating evaporator room 8 and liquid film, porous is inhaled ripple evaporation bed 9 and is absorbed micro-wave energy simultaneously, and indirect heating liquid film and whole evaporator room 8 obtain water vapour; Wherein microwave source 3 microwave power is 800W, frequency is 2.45GHz;
Step 5, product collection: the water vapour obtained through step 4 is after scum dredger 4, overflowed from evaporator room 8 fast by negative pressure mode, enter steam condenser 10 condensation, water of condensation reclaims through distilled water holding tank 11 and obtains 28.3L distilled water, and it is concentrated containing heavy metal solution to obtain 1.4L, the result obtained is as shown in table 1;
Step 6, product circulation utilize: the distilled water that recovery obtains is as hydrometallurgy each workshop section diluting water or boiler wash water, and directly returning electrolytic process Footwall drift ion containing heavy metal solution or forming metal-salt crystallization through secondary microwave evaporative crystallization after concentrated is reclaimed.
Table 1 embodiment 1 result table
。
Embodiment 2
The equipment of this microwave purifying process heavy metal ion-containing waste water, comprises head tank 1, cleaner 2, microwave source 3, scum dredger 4, thermopair, vapour outlet 6, high-pressure nozzle 7, evaporator room 8, porous inhales ripple evaporation bed 9, steam condenser 10, distilled water holding tank 11, vacuum pump 12, by-pass valve control, discharging pump 15, dense material liquid outlet 16, fresh feed pump 19, evaporation bed stationary platen 20 and hole 21, described head tank 1 is successively by fresh feed pump 19, by-pass valve control pipeline connects high-pressure nozzle 7, head tank 1 inner lower is provided with cleaner 2, it is inner that high-pressure nozzle 7 arrives evaporator room 8 through evaporator room 8 side, evaporator room 8 top and bottom are respectively equipped with vapour outlet 6 and dense material liquid outlet 16, dense material liquid outlet 16 is divided into two pipelines by discharging pump 15, a pipeline connection control valve, another pipeline returns high-pressure nozzle 7 pipeline by by-pass valve control, by evaporation bed stationary platen 20, porous is installed below evaporator room 8 internal high pressure shower nozzle 7 and inhales ripple evaporation bed 9, porous is inhaled ripple evaporation bed 9 surface and is provided with hole 21, evaporator room 8 top is provided with scum dredger 4, evaporator room 8 surrounding is provided with thermopair and microwave source 3 according to practical situation, vapour outlet 6 successively with steam condenser 10, distilled water holding tank 11 is connected with vacuum pump 12.
Wherein high-pressure nozzle 7 adopts the modified and reinforced King of PTFE to process, and it has fabulous temperature tolerance (-200 to+260 DEG C), the not resistance to viscosity of erosion resistance, resistance to deterioration, hydrophobic and machinability; Meanwhile, it is that electromagnetic wave transparent material does not absorb microwave substantially, thus ensures the even of evaporator room Space Microwave under multimode radiation; Be provided with thermal insulation layer between described evaporator room 8 and microwave source 3, thermal insulation layer material is mainly insulating cotton; Described porous is inhaled ripple evaporation bed 9 and is adopted silicon carbide microwave-absorbing ceramic material to make; Described hole 21 aperture is 4mm.
As shown in Figure 3, the equipment use method of this above-mentioned microwave purifying process heavy metal ion-containing waste water, its concrete steps are as follows:
Step 1, pressure regulate: be first 0.03Mpa by vacuum pump 12 by the pressure-controlling of evaporator room 8 and steam condenser 10;
Step 2, purification: by 30L containing Zn
2+1mg/L, Cu
2+1mg/L metal ion waste water joins in head tank 1, and in head tank 1, the impurity such as sandstone in heavy metal ion-containing waste water, the solidifying wadding of organism removed by cleaner 2;
Step 3, make drip and masking: then go deimpurity heavy metal ion-containing waste water by fresh feed pump 19 and high-pressure nozzle 7, the drop making heavy metal ion-containing waste water form particle diameter 1mm enters evaporator room 8, in droplets fall process, absorb microwave concentrate, the porous suction ripple evaporation bed 9 arrived in evaporator room 8 when drop forms liquid film and drop;
Step 4, microwave evaporation: while carry out step 3, open the microwave source 3 of evaporator room 8, adopt the drop in microwave direct heating evaporator room 8 and liquid film, porous is inhaled ripple evaporation bed 9 and is absorbed micro-wave energy simultaneously, and indirect heating liquid film and whole evaporator room 8 obtain water vapour; Wherein in microwave source 3, microwave power is 1200W, frequency is 2.45GHz;
Step 5, product collection: the water vapour obtained through step 4 is after scum dredger 4, overflowed from evaporator room 8 fast by negative pressure mode, enter steam condenser 10 condensation, water of condensation reclaims through distilled water holding tank 11 and obtains 25.8L distilled water, and it is concentrated containing heavy metal solution to obtain 3.9L, result is as shown in table 2;
Step 6, product circulation utilize: the distilled water that recovery obtains is as hydrometallurgy each workshop section diluting water or boiler wash water, and directly returning electrolytic process Footwall drift ion containing heavy metal solution or forming metal-salt crystallization through secondary microwave evaporative crystallization after concentrated is reclaimed.
Table 2 embodiment 2 result table
。
Embodiment 3
The equipment of this microwave purifying process heavy metal ion-containing waste water, comprises head tank 1, cleaner 2, microwave source 3, scum dredger 4, thermopair, vapour outlet 6, high-pressure nozzle 7, evaporator room 8, porous inhales ripple evaporation bed 9, steam condenser 10, distilled water holding tank 11, vacuum pump 12, by-pass valve control, discharging pump 15, dense material liquid outlet 16, fresh feed pump 19, evaporation bed stationary platen 20 and hole 21, described head tank 1 is successively by fresh feed pump 19, by-pass valve control pipeline connects high-pressure nozzle 7, head tank 1 inner lower is provided with cleaner 2, it is inner that high-pressure nozzle 7 arrives evaporator room 8 through evaporator room 8 side, evaporator room 8 top and bottom are respectively equipped with vapour outlet 6 and dense material liquid outlet 16, dense material liquid outlet 16 is divided into two pipelines by discharging pump 15, a pipeline connection control valve, another pipeline returns high-pressure nozzle 7 pipeline by by-pass valve control, by evaporation bed stationary platen 20, porous is installed below evaporator room 8 internal high pressure shower nozzle 7 and inhales ripple evaporation bed 9, porous is inhaled ripple evaporation bed 9 surface and is provided with hole 21, evaporator room 8 top is provided with scum dredger 4, evaporator room 8 surrounding is provided with thermopair and microwave source 3 according to practical situation, vapour outlet 6 successively with steam condenser 10, distilled water holding tank 11 is connected with vacuum pump 12.
Wherein high-pressure nozzle 7 adopts the modified and reinforced King of PTFE to process, and it has fabulous temperature tolerance (-200 to+260 DEG C), the not resistance to viscosity of erosion resistance, resistance to deterioration, hydrophobic and machinability; Meanwhile, it is that electromagnetic wave transparent material does not absorb microwave substantially, thus ensures the even of evaporator room Space Microwave under multimode radiation; Be provided with thermal insulation layer between described evaporator room 8 and microwave source 3, thermal insulation layer material is mainly insulating cotton; Described porous is inhaled ripple evaporation bed 9 and is adopted silicon carbide microwave-absorbing ceramic material to make; Described hole 21 aperture is 4mm.
As shown in Figure 3, the equipment use method of this above-mentioned microwave purifying process heavy metal ion-containing waste water, its concrete steps are as follows:
Step 1, pressure regulate: be first 0.03Mpa by vacuum pump 12 by the pressure-controlling of evaporator room 8 and steam condenser 10;
Step 2, purification: by 30L containing Zn
2+20mg/L, Cu
2+20mg/L metal ion waste water joins in head tank 1, and in head tank 1, cleaner 2 removes sandstone and organic impurities in heavy metal ion-containing waste water;
Step 3, make drip and masking: then go deimpurity heavy metal ion-containing waste water by fresh feed pump 19 and high-pressure nozzle 7, the drop making heavy metal ion-containing waste water form particle diameter 2mm enters evaporator room 8, in droplets fall process, absorb microwave concentrate, the porous suction ripple evaporation bed 9 arrived in evaporator room 8 when drop forms liquid film and drop;
Step 4, microwave evaporation: while carry out step 3, open the microwave source 3 of evaporator room 8, adopt the drop in microwave direct heating evaporator room 8 and liquid film, porous is inhaled ripple evaporation bed 9 and is absorbed micro-wave energy simultaneously, and indirect heating liquid film and whole evaporator room 8 obtain water vapour; Wherein in microwave source 3, microwave power is 1500W, frequency is 2.45GHz;
Step 5, product collection: the water vapour obtained through step 4 is after scum dredger 4, overflowed from evaporator room 8 fast by negative pressure mode, enter steam condenser 10 condensation, water of condensation reclaims through distilled water holding tank 11 and obtains 26.2L distilled water, and it is concentrated containing heavy metal solution to obtain 3.6L, result is as shown in table 3;
Step 6, product circulation utilize: the distilled water that recovery obtains is as hydrometallurgy each workshop section diluting water or boiler wash water, and directly returning electrolytic process Footwall drift ion containing heavy metal solution or forming metal-salt crystallization through secondary microwave evaporative crystallization after concentrated is reclaimed.
Table 3 embodiment 3 result table
。
Embodiment 4
The equipment of this microwave purifying process heavy metal ion-containing waste water, comprises head tank 1, cleaner 2, microwave source 3, scum dredger 4, thermopair, vapour outlet 6, high-pressure nozzle 7, evaporator room 8, porous inhales ripple evaporation bed 9, steam condenser 10, distilled water holding tank 11, vacuum pump 12, by-pass valve control, discharging pump 15, dense material liquid outlet 16, fresh feed pump 19, evaporation bed stationary platen 20 and hole 21, described head tank 1 is successively by fresh feed pump 19, by-pass valve control pipeline connects high-pressure nozzle 7, head tank 1 inner lower is provided with cleaner 2, it is inner that high-pressure nozzle 7 arrives evaporator room 8 through evaporator room 8 side, evaporator room 8 top and bottom are respectively equipped with vapour outlet 6 and dense material liquid outlet 16, dense material liquid outlet 16 is divided into two pipelines by discharging pump 15, a pipeline connection control valve, another pipeline returns high-pressure nozzle 7 pipeline by by-pass valve control, by evaporation bed stationary platen 20, porous is installed below evaporator room 8 internal high pressure shower nozzle 7 and inhales ripple evaporation bed 9, porous is inhaled ripple evaporation bed 9 surface and is provided with hole 21, evaporator room 8 top is provided with scum dredger 4, evaporator room 8 surrounding is provided with thermopair and microwave source 3 according to practical situation, vapour outlet 6 successively with steam condenser 10, distilled water holding tank 11 is connected with vacuum pump 12.
Wherein high-pressure nozzle 7 adopts the modified and reinforced King of PTFE to process, and it has fabulous temperature tolerance (-200 to+260 DEG C), the not resistance to viscosity of erosion resistance, resistance to deterioration, hydrophobic and machinability; Meanwhile, it is that electromagnetic wave transparent material does not absorb microwave substantially, thus ensures the even of evaporator room Space Microwave under multimode radiation; Be provided with thermal insulation layer between described evaporator room 8 and microwave source 3, thermal insulation layer material is mainly insulating cotton; Described porous is inhaled ripple evaporation bed 9 and is adopted aluminum oxide microwave-absorbing ceramic material to make; Described hole 21 aperture is 3mm.
As shown in Figure 3, the equipment use method of this above-mentioned microwave purifying process heavy metal ion-containing waste water, its concrete steps are as follows:
Step 1, pressure regulate: be first 0.02Mpa by vacuum pump 12 by the pressure-controlling of evaporator room 8 and steam condenser 10;
Step 2, purification: by 30L containing Zn
2+10mg/L, Mg
2+20mg/L, Cu
2+20mg/L metal ion waste water joins in head tank 1, and in head tank 1, cleaner 2 removes sandstone and organic impurities in heavy metal ion-containing waste water;
Step 3, make drip and masking: then go deimpurity heavy metal ion-containing waste water by fresh feed pump 19 and high-pressure nozzle 7, the drop making heavy metal ion-containing waste water form particle diameter 3mm enters evaporator room 8, in droplets fall process, absorb microwave concentrate, the porous suction ripple evaporation bed 9 arrived in evaporator room 8 when drop forms liquid film and drop;
Step 4, microwave evaporation: while carry out step 3, open the microwave source 3 of evaporator room 8, adopt the drop in microwave direct heating evaporator room 8 and liquid film, porous is inhaled ripple evaporation bed 9 and is absorbed micro-wave energy simultaneously, and indirect heating liquid film and whole evaporator room 8 obtain water vapour; Wherein in microwave source 3, microwave power is 1500W, frequency is 2.45GHz;
Step 5, product collection: the water vapour obtained through step 4 is after scum dredger 4, overflowed from evaporator room 8 fast by negative pressure mode, enter steam condenser 10 condensation, water of condensation reclaims through distilled water holding tank 11 and obtains 26.4L distilled water, and it is concentrated containing heavy metal solution to obtain 2.5L, result is as shown in table 4;
Step 6, product circulation utilize: the distilled water that recovery obtains is as hydrometallurgy each workshop section diluting water or boiler wash water, and directly returning electrolytic process Footwall drift ion containing heavy metal solution or forming metal-salt crystallization through secondary microwave evaporative crystallization after concentrated is reclaimed.
Table 4 embodiment 4 result table
Below by reference to the accompanying drawings embodiment of the present utility model is explained in detail, but the utility model is not limited to above-mentioned embodiment, in the ken that those of ordinary skill in the art possess, various change can also be made under the prerequisite not departing from the utility model aim.
Claims (5)
1. an equipment for microwave purifying process heavy metal ion-containing waste water, is characterized in that: comprise head tank (1), cleaner (2), microwave source (3), scum dredger (4), thermopair, vapour outlet (6), high-pressure nozzle (7), evaporator room (8), porous inhales ripple evaporation bed (9), steam condenser (10), distilled water holding tank (11), vacuum pump (12), by-pass valve control, discharging pump (15), dense material liquid outlet (16), fresh feed pump (19), evaporation bed stationary platen (20) and hole (21), described head tank (1) is successively by fresh feed pump (19), by-pass valve control pipeline connects high-pressure nozzle (7), head tank (1) inner lower is provided with cleaner (2), it is inner that high-pressure nozzle (7) arrives evaporator room (8) through evaporator room (8) side, evaporator room (8) top and bottom are respectively equipped with vapour outlet (6) and dense material liquid outlet (16), dense material liquid outlet (16) is divided into two pipelines by discharging pump (15), a pipeline connection control valve, another pipeline returns high-pressure nozzle (7) pipeline by by-pass valve control, evaporator room (8) internal high pressure shower nozzle (7) below is installed porous by evaporation bed stationary platen (20) and is inhaled ripple evaporation bed (9), porous is inhaled ripple evaporation bed (9) surface and is provided with hole (21), evaporator room (8) top is provided with scum dredger (4), evaporator room (8) surrounding is provided with thermopair and microwave source (3) according to practical situation, vapour outlet (6) successively with steam condenser (10), distilled water holding tank (11) is connected with vacuum pump (12).
2. the equipment of microwave purifying process heavy metal ion-containing waste water according to claim 1, is characterized in that: described high-pressure nozzle (7) adopts the modified and reinforced King of PTFE to process.
3. the equipment of microwave purifying process heavy metal ion-containing waste water according to claim 1, is characterized in that: be provided with thermal insulation layer between described evaporator room (8) and microwave source (3).
4. the equipment of microwave purifying process heavy metal ion-containing waste water according to claim 1, is characterized in that: described porous suction ripple evaporation bed (9) employing oxide compound, nitride or carbide ceramics material are that the absorbing material of matrix is made.
5. the equipment of microwave purifying process heavy metal ion-containing waste water according to claim 1, is characterized in that: described hole (21) aperture is 1 ~ 4mm.
Priority Applications (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520268201.XU CN204675941U (en) | 2015-04-29 | 2015-04-29 | A kind of equipment of microwave purifying process heavy metal ion-containing waste water |
| PCT/CN2016/079611 WO2016173424A1 (en) | 2015-04-29 | 2016-04-19 | Microwave flash evaporation process, apparatus and application |
| US15/515,460 US10632396B2 (en) | 2015-04-29 | 2016-04-19 | Microwave flash evaporation process and apparatus and use thereof |
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| CN201520268201.XU CN204675941U (en) | 2015-04-29 | 2015-04-29 | A kind of equipment of microwave purifying process heavy metal ion-containing waste water |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2016173424A1 (en) * | 2015-04-29 | 2016-11-03 | 昆明理工大学 | Microwave flash evaporation process, apparatus and application |
| CN106830140A (en) * | 2017-01-22 | 2017-06-13 | 广东美的厨房电器制造有限公司 | Microwave distillation component and the distilling apparatus with it |
| CN114949890A (en) * | 2022-05-27 | 2022-08-30 | 杭州东日节能技术有限公司 | Microwave-heated filler type evaporator and method for concentrating fluorine-containing dilute sulfuric acid |
-
2015
- 2015-04-29 CN CN201520268201.XU patent/CN204675941U/en active Active
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2016173424A1 (en) * | 2015-04-29 | 2016-11-03 | 昆明理工大学 | Microwave flash evaporation process, apparatus and application |
| US10632396B2 (en) | 2015-04-29 | 2020-04-28 | Kunming University Of Science And Technology | Microwave flash evaporation process and apparatus and use thereof |
| CN106830140A (en) * | 2017-01-22 | 2017-06-13 | 广东美的厨房电器制造有限公司 | Microwave distillation component and the distilling apparatus with it |
| CN114949890A (en) * | 2022-05-27 | 2022-08-30 | 杭州东日节能技术有限公司 | Microwave-heated filler type evaporator and method for concentrating fluorine-containing dilute sulfuric acid |
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