CN104230040A - Waste heat and sewage circulation utilization and treatment system for ceramic industry - Google Patents

Abstract

The invention relates to a waste heat and sewage circulation utilization and treatment system for the ceramic industry. The system is characterized by comprising a sewage collection device, a water-reside deposition and separation device, an automatic clean water and sludge sucking device, a sludge residue collector, a slurry-medicine cyclone mixing device, a residue pressing device, a waste residue drying device, an automatic residue unloading device, a clean water collection and purification device. By adopting the system, effective recycling and reuse of sewage, waste residues and hot waste gas produced in the ceramic production process are effectively achieved, the treatment cost of sewage, waste residues and hot waste gas is lowered, the operating cost is greatly reduced for ceramic companies, the environment-friendly treatment capability of the ceramic companies is improved, and the environment evaluation of the companies can meet the national requirements.

Description

A kind of ceramic industry waste hot gas effluent cycle utilizes treatment system

Technical field

The present invention relates to a kind of Industrial sewage treatment system.

Background technology

Ceramic production industry uses water rich and influential family, a large amount of waste water can be produced in process of production, containing a large amount of suspended solid in waste water, colourity is higher, some thick suspended substances, through precipitation process, can base be got rid of, and some more tiny, that particle diameter is between 0.02-30 micron subparticle suspended substances, then more difficultly to get rid of quickly, need the long period could natural sedimentation.In today that water resources day is becoming tight, water saving and how to improve the utilization ratio of water, becomes particularly important.At present, although Production of Ceramics producer also processes sewage, still there is more subparticle suspended substance in the clear water after process, can't reach standards for industrial water usage, cannot recirculation utilize.

In addition, the mud that ceramic industry production link produces and sewage, existing treatment process is look for local landfill substantially.And without dehydrating the mud of process, its water ratio is high, Heavy Weight, transport is inconvenience very, and transportation cost is high, and in transportation, easily trickles down, and has a strong impact on surrounding enviroment health.Further, also second stage employ cannot be carried out without the mud dehydrating process.But along with the environmental requirement of country is more and more higher, and land resources is non-renewable, can the place of landfill fewer and feweri, how to enable sewage-mud realize second stage employ and to seem particularly important.

In addition, a large amount of hot waste gass that current ceramic industry produces at production link, mostly need, after the filtration, purification, cooling of repeatedly layer, just can meet environmental requirement, could outwardly give off.This makes ceramic industry just must drop into every year a huge sum of money to cross the hot waste gas that production link produces and carry out that filter purifies, lowering the temperature processes, Energy efficiency not only can not be made to obtain maximum using, but also seriously tie down business capital running, add the production and operation burden of enterprise, make benefit can not get good improvement.

Therefore, for variety of problems noted earlier, change must be made to existing Production of Ceramics management style, to adapt to the evolution of new situations, new environmental requirement.

Summary of the invention

The object of the invention is to solve the problem and deficiency, a kind of ceramic industry waste hot gas effluent cycle is provided to utilize treatment system, sewage, waste residue that this treatment system can realize Production of Ceramics link produces carry out grain slag separation, and can the water after separation be purified, reach the effect of recycle, with can carry out squeezing solid carbon dioxide part to the slag charge after being separated, and the waste hot gas that the slag charge of squeezing solid carbon dioxide part utilizes Production of Ceramics link to produce to be dried, so that transport and recycling.

Technical scheme of the present invention is achieved in that

A kind of ceramic industry waste hot gas effluent cycle utilizes treatment system, its feature is to comprise sewage collection equipment, grain slag precipitation separation device, clear water and mud Automatic Extraction device, Sludge Collector, slurry medicine rotational flow mixing device, pressure slag device, waste residue drying device, automatic clinker-removing device, clear water collection and purification device, wherein

Described sewage collection equipment is connected by sewage discharge place of pipeline with workshop, Ceramics Enterprises production line, with the sewage centralized collection produced in workshop, Ceramics Enterprises production line; Described sewage collection equipment is connected with grain slag precipitation separation device by pipeline, gives grain slag precipitation separation device carry out grain slag separation with sump pump collection come;

Clear water collection and purification device given by the isolated fresh water pump of described grain slag precipitation separation device, the isolated screenings of described grain slag precipitation separation device sends clear water and mud Automatic Extraction device to by pipeline, clear water collection and purification device given by the fresh water pump that described clear water and mud Automatic Extraction device precipitate and isolate, and the scum pump that described clear water and mud Automatic Extraction device precipitate and isolate gives Sludge Collector;

Described Sludge Collector will be collected scum pump and give slurry medicine rotational flow mixing device, pressure slag device is delivered to after slurry medicine rotational flow mixing device mixes medicine, described pressure slag device is connected with waste residue drying device, dry so that slag charge dry for squeezing is sent into waste residue drying device, described waste residue drying device is provided with high temperature hot gas input terminus, this high temperature hot gas input terminus is connected by the high-temperature exhaust emission pipe of pipeline with workshop, Ceramics Enterprises production line, described automatic clinker-removing device is connected with waste residue drying device exit end, unloads to realize slag charge automatic pouring.

Beneficial effect of the present invention:

(1) basis is bright is collected unified for the sewage of Production of Ceramics by sewage collection equipment, and in collection process, add the dirty water decontamination handles medicine, then be pumped into grain slag precipitation separation device and carry out natural sedimentation purification, most of grain slag is effectively separated, separation obtains clear water and send clear water collection and purification device again to purify, to reach the requirement that can reuse, be separated the slag slurry obtained to enter into clear water again and carry out precipitation with mud Automatic Extraction device and be separated with grain slag, to be separated through clear water the fresh water pump obtained with mud Automatic Extraction device to deliver to clear water collection and purification device and again purify, and to be separated through clear water the scum pump obtained with mud Automatic Extraction device and to deliver to Sludge Collector and carry out unifying to collect, then, being pumped into pressure slag device more as required, to carry out moisture content squeezing dry, be pumped in pressure slag device process in the process, starch medicine rotational flow mixing device by body refuse and medicine is mixed into slag charge, to improve body refuse degree of purification, through the slag charge that pressure slag device squeezing solid carbon dioxide divides, be sent to waste residue drying device to dry, drop under 10% to make the water ratio of body refuse, reach the requirement meeting and again return utilization, and the hyperthermia drying hot gas that waste residue drying device is used, then collected from Production of Ceramics link (the heat extraction mouth as kiln) by pipeline, hyperthermia drying hot gas is dried after utilization through waste residue drying device, and temperature significantly reduces, after being extremely beneficial to secondary-cleaned, the external world can be given off, from waste residue drying device every pallet slag charge out, carry out after automatic clinker-removing through automatic clinker-removing device, obtain water ratio lower than 10% slag charge, then can recycling, but the water after the process of clear water collection and purification device, then can pumped back production link, and what realize water is cycled to repeat utilization.

(2) the present invention have effectively achieved to Production of Ceramics link produce sewage, waste residue, waste hot gas effective recycling, reduce the processing cost of Ceramics Enterprises sewage, waste residue, waste hot gas, for Ceramics Enterprises has saved a large amount of operational cost, but also improve Ceramics Enterprises environmental protection treatment ability, make enterprise's environmental impact assessment reach national requirements.

Accompanying drawing explanation

Fig. 1 is frame principle figure of the present invention.

Fig. 2 is system principle schematic diagram of the present invention.

Fig. 3 is the structural principle schematic diagram of sewage collection equipment of the present invention.

Fig. 4 is the structural principle schematic diagram of grain slag precipitation separation device of the present invention.

Fig. 5 is the structural principle schematic diagram of the eddy flow slagging device of grain slag precipitation separation device of the present invention.

Fig. 6 is the structural principle schematic diagram of clear water of the present invention and mud Automatic Extraction device.

Fig. 7 is the structural principle schematic diagram of slurry medicine rotational flow mixing device of the present invention.

Fig. 8 is the structural principle schematic diagram of pressure slag device of the present invention.

Fig. 9 is the cross section structure schematic diagram of the oven dry body of heater inlet end of waste residue drying device of the present invention.

Figure 10 is the cross section structure schematic diagram of the oven dry body of heater exit end of waste residue drying device of the present invention.

Figure 11 is the side structure schematic diagram of waste residue drying device of the present invention.

Figure 12 is the structural principle schematic diagram of automatic clinker-removing device of the present invention.

Figure 13 is the structural principle schematic diagram of clear water collection and purification device of the present invention.

Embodiment

As shown in Figure 1 and Figure 2, a kind of ceramic industry waste hot gas effluent cycle of the present invention utilizes treatment system, it comprises sewage collection equipment 1, grain slag precipitation separation device 2, clear water and mud Automatic Extraction device 3, Sludge Collector 4, slurry medicine rotational flow mixing device 5, pressure slag device 6, waste residue drying device 7, automatic clinker-removing device 8, clear water collection and purification device 9, wherein

Described sewage collection equipment 1 is connected by sewage discharge place of pipeline with workshop, Ceramics Enterprises production line, with the sewage centralized collection produced in workshop, Ceramics Enterprises production line; Described sewage collection equipment 1 is connected with grain slag precipitation separation device 2 by pipeline, gives grain slag precipitation separation device 2 carry out grain slag separation with sump pump collection come;

Clear water collection and purification device 9 given by the isolated fresh water pump of described grain slag precipitation separation device 2, the isolated screenings of described grain slag precipitation separation device 2 sends clear water and mud Automatic Extraction device 3 to by pipeline, clear water collection and purification device 9 given by the fresh water pump that described clear water and mud Automatic Extraction device 3 precipitate and isolate, and the scum pump that described clear water and mud Automatic Extraction device 3 precipitate and isolate gives Sludge Collector 4;

Described Sludge Collector 4 will be collected scum pump and give slurry medicine rotational flow mixing device 5, pressure slag device 6 is delivered to after slurry medicine rotational flow mixing device 5 mixes medicine, described pressure slag device 6 is connected with waste residue drying device 7, dry so that slag charge dry for squeezing is sent into waste residue drying device 7, described waste residue drying device 7 is provided with high temperature hot gas input terminus, this high temperature hot gas input terminus is connected by the high-temperature exhaust emission pipe of pipeline with workshop, Ceramics Enterprises production line, described automatic clinker-removing device 8 is connected with waste residue drying device 7 exit end, unloads to realize slag charge automatic pouring.

As depicted in figs. 1 and 2, principle of work of the present invention is roughly such: first by sewage collection equipment 1 by workshop, Ceramics Enterprises production line 10 such as, the sewage of the sewage that polishing departement produces is unified to be collected, and in collection process, add the dirty water decontamination handles medicine, then be pumped into grain slag precipitation separation device 2 and carry out natural sedimentation purification, most of grain slag is effectively separated, separation obtains clear water and send clear water collection and purification device 9 again to purify, to reach the requirement that can reuse, be separated the slag slurry obtained to enter into clear water again and carry out precipitation with mud Automatic Extraction device 3 and be separated with grain slag, to be separated through clear water the fresh water pump obtained with mud Automatic Extraction device 3 to deliver to clear water collection and purification device 9 and again purify, and to be separated through clear water the scum pump obtained with mud Automatic Extraction device 3 and to deliver to Sludge Collector 4 and carry out unifying to collect, then, being pumped into pressure slag device 6 more as required, to carry out moisture content squeezing dry, be pumped in pressure slag device 6 process in the process, medicine is mixed into by slurry medicine rotational flow mixing device 5 pairs of slag charges, to improve body refuse degree of purification, the slag charge that solid carbon dioxide divides is squeezed through pressure slag device 6, be sent to waste residue drying device 7 to dry, drop under 10% to make the water ratio of body refuse, reach the requirement meeting and again return utilization, and the hyperthermia drying hot gas that waste residue drying device 7 is used, then by pipeline from Production of Ceramics link as the heat extraction mouth of kiln is collected, namely as shown in Figure 1, hyperthermia drying hot gas is dried after utilization through waste residue drying device 7, temperature significantly reduces, after being extremely beneficial to secondary-cleaned, the external world can be given off, from waste residue drying device 7 every pallet slag charge out, after automatic clinker-removing device 8 carries out automatic clinker-removing, obtain water ratio lower than 10% slag charge, then can recycling, but the water after the process of clear water collection and purification device 9, then can pumped back production link, and what realize water is cycled to repeat utilization.

As shown in Figure 3, described sewage collection equipment 1 comprises sewage collecting pool 11, sump pump 12, sewage input tube 13, medicine pond 14, Automatic Dosing mechanism 15, dispatch pipe 16, tail pipe 17, wherein said sewage input tube 13 is connected with sewage collecting pool 11, described medicine pond 13 is connected with sewage input tube 13 by water pipe, and described Automatic Dosing mechanism 15 is serially connected with on the water pipe between medicine pond 13 and sewage input tube 13; One end of described tail pipe 17 is connected with the input terminus of sump pump 12, and the other end of this tail pipe 17 stretches in sewage collecting pool 11; Described dispatch pipe 16 is connected to the output terminal of sump pump 12, and the other end of this dispatch pipe 16 is connected to grain slag precipitation separation device 2, namely as shown in Figure 2.This device not only has the function of collecting sewage, and also have for sewage adds the function of pollution treatment medicine automatically, and the pollution treatment medicine added is without the need to additionally stirring, namely in sewage input tube in flow process; simultaneously fully can be mixed, avoid stirring.Described Automatic Dosing mechanism 15 is made up of water pump, Flow-rate adjustment controller and control apparatus unit.For the ease of equipment repair and maintenance, the water pipe generally between Automatic Dosing mechanism 15 and medicine pond 13 is also serially connected with valve 18.In addition, in order to tail pipe 17 blocks by oversized particles quickly, prevent from burning out water pump, as shown in Figure 1, the other end port of described tail pipe 17 is also set with screen element 44.If when the pollution treatment medicine added is more than a kind of, when needing again to add separately, multiple Automatic Dosing mechanism can be connected on sewage input tube, namely as shown in Figure 3.Add pollution treatment medicine in sewage input tube and, in flow process, can fully be mixed, reach the object exempting to stir.In addition, if when the amount of sewage disposal is many, sump pump also can install multiple stage as required.

As shown in Figure 4, described grain slag precipitation separation device 2 comprises slime water input tube 21, slime water imports buffer tube 22, grain slag precipitate and separate cylinder 23 and eddy flow slagging device 24, wherein said grain slag precipitate and separate cylinder 23 becomes the housing structure of the cylindrical shape in top, the tapered shape in bottom, the bottom of grain slag precipitate and separate cylinder 23 is become cone-shaped structure, is mainly beneficial to body refuse and discharges.The cylinder mouth inwall of grain slag precipitate and separate cylinder 23 is also provided with spilling water annular groove 231, the outer wall of grain slag precipitate and separate cylinder 23 is also provided with water shoot 25 accordingly that be connected with spilling water annular groove 231, this water shoot 25 is connected to clear water collection and purification device 9, carries out that purification is up to standard to be re-used to be delivered to by the clear water overflowed in clear water collection and purification device 9.Slag-drip opening 232 is also provided with in the bottom of grain slag precipitate and separate cylinder 23; Described slime water imports the pipe structure that buffer tube 22 becomes the cylindrical shape in top, bottom flare shape, the centre that this slime water importing buffer tube 22 is vertically installed in grain slag precipitate and separate cylinder 23 is set up, and the overhead height that this slime water imports buffer tube 22 will be arranged in the top margin higher than grain slag precipitate and separate cylinder 23, the top that described slime water input tube 21 and slime water import buffer tube 22 is connected.It is make the slime water entering into grain slag precipitate and separate cylinder 23 produce fluctuation that slime water imports the Main Function of buffer tube 22, thus the precipitation that can not have influence on grain slag be separated.Described eddy flow slagging device 24 is arranged on the grain slag precipitate and separate cylinder 23 be arranged in below slime water importing buffer tube 22, and this eddy flow slagging device 24 is provided with multiple slag charge enters mouth 241 and multiple slag charge relief outlet 242, together with each slag charge relief outlet 242 of described eddy flow slagging device 24 is connected with the slag-drip opening 232 of grain slag precipitate and separate cylinder 23.

In order to make that there is eddy flow slagging device 24 simple structure, practical feature, as shown in Figure 5, described eddy flow slagging device 24 by some the scum pipes 243 bending to circular shape from top to bottom in the shape of a spiral structure assemble, and the slag charge of each scum pipe 243 enters mouth 241 arranges in towards spiral center, together with the scum pipe 26 that the slag charge relief outlet 242 of each scum pipe 243 is provided with the slag-drip opening 232 of grain slag precipitate and separate cylinder 23 is respectively connected; Scum pipe 26 is also provided with residual cake valve 27.

The principle of work of this device is roughly as follows:

As shown in Figure 2, Figure 4 shows, described slime water input tube 21 is connected with the dispatch pipe 16 of sewage collection equipment 1, by the sewage sent here from sewage collection equipment 1, import buffer tube 22 by slime water and enter into grain slag precipitate and separate cylinder 23, and fluctuation can not be produced, to realize mud by the object of static for water slow precipitation by original water in diversion slag precipitate and separate cylinder 23.Under gravity, slag charge heavier-weight can sink to cylinder bottom, water can density less, upwards spill-over, through spilling water annular groove 231, by water shoot 25 flow to clear water collection and purification device 9 purify up to standard after, recycling.And the slag charge sunk, act on through eddy flow slagging device 24, produce eddy flow as shown by the arrows in Figure 5, discharge outside cylinder.And by this whirlwind-type deslagging mode, on the one hand, slag charge evenly and is stably discharged, can not larger fluctuation be drawn, be conducive to the precipitation of grain slag, purification and be separated; On the other hand, slag charge can not staticly lump, and causes slag-drip opening, has influence on normal deslagging.In addition, as shown in Figure 2, when needing sewage quantity to be processed more, multiple such grain slag precipitation separation device 2 can be set, distributed by a sewage divider 100 between each grain slag precipitation separation device 2, the slime water input tube 21 of each grain slag precipitation separation device 2 is directly connected with sewage divider 100, and sewage divider 100 is then connected with the dispatch pipe 16 of sewage collection equipment 1.

As shown in Figure 6, described clear water and mud Automatic Extraction device 3 comprise grain slag settling tank 31, grain slag feed-pipe 32, sludge discharge pipe 33, clear water vent pipe 34, automatically slag pumper structure 35, mud tail pipe 36, clear water tail pipe 37, automatically take out clear water mechanism 38, wherein said clear water mechanism 38 of automatically taking out is made up of ball float frame 310 and the water pump 320 be installed on ball float frame 310, this is automatically taken out clear water mechanism 38 and is arranged in grain slag settling tank 31 by ball float frame 310, and namely described clear water mechanism 38 of automatically taking out floats on the water surface in grain slag settling tank 31.Described clear water tail pipe 37 is connected to the water pump input terminus automatically taking out clear water mechanism 38, and the length of this clear water tail pipe 37 is general shorter, if mostly time just passable a little less than the water surface, be conducive to the clear water extracted like this, and shallow lake thing is few, meanwhile, can ensure again that water pump can not lack of water and damaging.Described clear water vent pipe 34 is connected with the water pump output terminal automatically taking out clear water mechanism 38, the other end of this clear water vent pipe 34 and clear water collection and purification device 9.

Described automatic slag pumper structure 35 is made up of ball float frame 310 and the water pump 320 be installed on ball float frame 310, and this automatic slag pumper structure 35 is arranged in grain slag settling tank 31 by ball float frame 310, in like manner, is float on the water surface in grain slag settling tank 31.Described mud tail pipe 6 is connected to the water pump input terminus of automatic slag pumper structure 35, and the length of this mud tail pipe 36 is general longer, can directly extend in the mud sediment thing at the bottom of pond, is drawn out by mud.Described sludge discharge pipe 33 is connected with the water pump output terminal of automatic slag pumper structure 35, and the other end of this sludge discharge pipe 33 is connected with Sludge Collector 4.The output port of described grain slag feed-pipe 32 is connected with grain slag settling tank 31, and the input port of described grain slag feed-pipe 32 is connected with the scum pipe 26 of grain slag precipitation separation device 2.

In order to avoid larger slag thing blocking pipe, as shown in Figure 6, the inhalation port of described clear water tail pipe 37 is also provided with screen element 44.In like manner, the inhalation port of described mud tail pipe 36 is yet provided with screen element 44.

In order to make automatic slag pumper structure 35 or automatically take out clear water mechanism 38, there is the effect that structure is simple, cost of manufacture is low, as shown in Figure 6, described automatic slag pumper structure 35 or the ball float frame 310 of automatically taking out clear water mechanism 38 are made up of two ball floats or keg float 330 and the connection bracket 340 be arranged between these two ball floats or keg float 330, and described automatic slag pumper structure 35 or the water pump 320 automatically taking out clear water mechanism 8 are arranged in connection bracket 340.

As shown in Figure 7, described slurry medicine rotational flow mixing device 5 comprises spiral medicine mixer 51, delivery tube 52, valve 53, wherein said spiral medicine mixer 51 is made up of shell 511, the flange 513 that is arranged at the screw rod 512 in shell 511 and is arranged at shell 511 2 end, described delivery tube 52 one end is connected on the sidewall of shell 511 input end, and described valve 53 is serially connected with on delivery tube 52.When applying in ceramic industry, as shown in Figure 7, by being provided with flange 513 on sewer line 54, the flange 513 on the shell 511 of this device is connected, and makes this device serial connection on sewer line 54.Under the effect of external pressure, slime water moves along screw rod 512, simultaneously, medicine refers generally to liquid also under the effect of external pressure, shell 511 is entered into by delivery tube 52, under the effect of screw rod 512, flow together with slime water, in flow process, complete fully mixing of medicine and slime water.

In actual applications, according to the slime water amount of flow of sewer line 54 or medicine usefulness, the number of applications of this device can be added on demand.Simultaneously scheme shown in Fig. 7 inputs medicine to sewer line 54 by two slurry medicine rotational flow mixing devices.The maximum feature of this device is that structure is simple, operation does not need power, zero energy consumption, installation application is convenient.

As shown in Figure 2, during application, the sewer line 54 being positioned at spiral medicine mixer 51 input terminus is connected with Sludge Collector 4 by a mortar pump, and the sewer line 54 being positioned at spiral medicine mixer 51 output terminal is connected to pressure slag device 6.

As shown in Figure 8, described pressure slag device 6 comprises frame 61, first belt 62, second belt 63, belt wheel load slag mechanism 64, upper idler 65, lower idler 66, upper tensioning adjusting cylinders 67, lower tensioning adjusting cylinders 68, belt installs around peripheral wheels 69, feeding mouth formation skin takes turns 610, the top of wherein said frame 61 is also provided with tilt stand 611, this tilt stand 611 is arranged to skewed, is the feeding mouth structure tilted to form ecto-entad.Described upper tensioning adjusting cylinders 67 is installed on the upper end of this tilt stand 611, and described upper idler 65 is installed on tensioning adjusting cylinders 67.The lower side position that frame 61 is positioned at tilt stand 611 upper end is also provided with assistant support 612, and this assistant support 612 is also that described feeding mouth forms belt pulley 610 and is installed on the top of this assistant support 612 in order to coordinate the feeding mouth structure forming ecto-entad and tilt.Described lower tensioning adjusting cylinders 68 is arranged in the frame 61 that is positioned at below assistant support 612, and described lower idler 66 is installed on lower tensioning adjusting cylinders 68.

Again as shown in Figure 8, described belt wheel load slag mechanism 64 is made up of large size belt pulley 641, medium size belt pulley 642, small size belt pulley 643, and wherein large size belt pulley 641, medium size belt pulley 642, small size belt pulley 643 are sequentially installed in frame 61 in alphabetical serpentine shape with arranging.The quantity of described medium size belt pulley 642, small size belt pulley 643, can press dry situation according to slag charge and carry out designing and adopting, quantitatively be not particularly limited.

Can comparatively reasonably be installed in frame 1 to make the first belt 62, as shown in Figure 8, described belt installs around peripheral wheels 69 and is taken turns 694 formed by upper belt pulley 691, left leather belt wheel 692, bottom pulley 693, right leather belt, wherein upper belt pulley 691 is installed on the lower end of tilt stand 611, described left leather belt wheel 692 is installed on the left surface of frame 61, described right leather belt wheel 694 is installed on the right flank of frame 61, and described bottom pulley 693 is installed on the bottom of frame 61.Described first belt 62 is along upper idler 65, large size belt pulley 641, medium size belt pulley 642, small size belt pulley 643 and belt install around peripheral wheels 69 and install around in frame 61, described second belt 63 forms belt pulley 610 along feeding mouth, large size belt pulley 641, medium size belt pulley 642, small size belt pulley 643 and lower idler 66 install around in frame 61, and between the first belt 62 formed at upper idler 65 and feeding mouth between belt pulley 610 and the second belt 63, be also formed with the feeding mouth 620 that ecto-entad tilts, and discharge port 630 is also formed between first belt 62 of taking turns at lower idler 66 and right leather belt between 694 and the second belt 63.

Described upper tensioning adjusting cylinders 67, lower tensioning adjusting cylinders 68 are mainly used in the rate of tension of adjustment first belt 61, second belt 62, press dry rate to obtain comparatively high-moisture.

The principle of work of this device is roughly as follows:

As shown in Figure 8, one transfer lime 640 is set above tilt stand 611, this transfer lime 640 is connected with the sewer line 54 of slurry medicine rotational flow mixing device 5, the slag charge that water content is larger drops on the first belt 62 on tilt stand 611 by transfer lime 640, move in first belt 62 and the second same direction of belt 63, make slag charge from feeding mouth 620 enter into belt wheel load slag mechanism 64 squeezing one time after, from discharge port 630 out, namely dry slag charge has been squeezed, moisture content then falls below belt wheel load slag mechanism 64, realizes water and slag is separated.In addition, as shown in Figure 2, from the discharge port 630 of this pressure slag device 6 slag charge out through being arranged on the slag charge conveyer belt mechanism 200 between this discharge port 630 and waste residue drying device 7, delivering in waste residue drying device 7 and drying, to reduce the water ratio of slag charge further.

As Fig. 9, shown in Figure 10 and Figure 11, described waste residue drying device 7 comprises dries body of heater 71, take out calorifier 72, dehumidifier blower fan 73, dry entrance roller tables 74 and dry outlet roller tables 75, wherein said oven dry body of heater 71 is made up of enclosed Rack Body 711 and the Roller way conveyor structure 712 be arranged in this Rack Body 711, described oven dry entrance roller tables 74 is arranged at the inlet end of drying body of heater 71, described outlet roller tables 75 of drying is arranged at the exit end of drying body of heater 71, and the front end of described oven dry body of heater 71 is provided with hot blast feeding mouth 713, moisture outlet port 714 is provided with in the rear end of this oven dry body of heater 71, the described output terminal taking out calorifier 72 is connected to the hot blast of drying body of heater 71 by hot air duct 715 and sends on mouth 713, the input terminus taking out calorifier 72 is then connected to hot gas providing source by an other segment pipe.The input terminus of described dehumidifier blower fan 73 be connected to by dehumidifier pipeline 716 dry body of heater 1 moisture outlet port 714 on, after the output terminal of dehumidifier blower fan 73 then outputs to other predetermined device processes by an other segment pipe, then discharge the external world.

In order to improve the drying efficiency of drying body of heater 71, as shown in Figure 9 and Figure 10, be provided with some layers of Roller way conveyor structure 712 in described oven dry body of heater 71, described oven dry entrance roller tables 74, oven dry outlet roller tables 75 become the roller tables mechanism with some layers of structure for conveying respectively accordingly.Simultaneously, in order to improve level of automation and the production efficiency of this device, as shown in Figure 9, this device also comprises lifting feeding platform 76 and sends platform 77 with lifting, wherein said lifting is sent into platform 76 and is arranged at the inlet end of drying entrance roller tables 74, the inlet end that platform 76 is sent in this lifting is then connected with conveying pipeline, to be automatically conveyed into by slag charge on each layer Roller way conveyor structure 712 of oven dry body of heater 71.Described lifting is sent platform 77 and is arranged at the exit end of drying outlet roller tables 75, and it is be connected with conveying pipeline that platform 77 output port is sent in this lifting, to be sent by the slag charge one by one after oven dry.

Again as shown in figure 11, described lifting is sent into platform 76 and is sent platform 77 with lifting and be made up of frame 78, motor 79, lifting gantry 710 and chain or belt 720 respectively.These mechanisms all belong to more conventional technology application, so be not described in detail.

When adopting some layers of Roller way conveyor structure 712 for structure in oven dry body of heater 1, in order to ensure the abundant spreadability of hot gas flow at each layer Roller way conveyor structure 712, as shown in Figure 9, the end of the described hot air duct 715 taken out on calorifier 72 is provided with several take-off pipes 730, the position described oven dry body of heater 71 front end two side faces corresponding to every layer of Roller way conveyor structure 712 is respectively equipped with hot blast and sends into mouth 713, and each take-off pipe 730 of described hot air duct 715 is sent into mouth 713 with each hot blast respectively and is connected.In like manner, in order to ensure that the steam that each layer produces can be taken away in time, as shown in Figure 10, the end of the dehumidifier pipeline 716 on described dehumidifier blower fan 73 is provided with several take-off pipes 730, the position described oven dry body of heater 71 rear end two side faces corresponding to every layer of Roller way conveyor structure 712 is respectively equipped with moisture outlet port 714, and the take-off pipe 730 of described dehumidifier pipeline 716 is connected with each moisture outlet port 714 respectively.In addition, described Roller way conveyor structure 712 is being formed side by side by some roller rods of a kind of slow formula rotation, and by motor-driven transfer mechanism, to make slag charge transmit once in oven dry body of heater 1, just can reach the requirement of oven dry.

In addition, as shown in Figure 2, in the specific implementation, this waste residue drying device 7 is with automatic clinker-removing device 8, separately add an automatic muck loader structure 300, and in conjunction with a streamline conveying belt or rollgang 400, the flow production line that has automatic charge, automatic discharging and auto-drying function can be formed.

As shown in figure 12, described automatic clinker-removing device 8 comprises pallet batch turning mechanism 81, pallet resetting mechanism 82, first conveyer belt mechanism 83, second conveyer belt mechanism 84, the 3rd conveyer belt mechanism 85, wherein said pallet batch turning mechanism 82 is arranged between the first conveyer belt mechanism 83 and the second conveyer belt mechanism 84, and this pallet batch turning mechanism 82 is made up of rotation axis 86 and the tray rack 87 that is arranged on rotation axis 86 in crosswise; Described pallet resetting mechanism 82 is arranged between the second conveyer belt mechanism 84 and the 3rd conveyer belt mechanism 85, and this pallet resetting mechanism 82 is made up of rotation axis 86 and the tray rack 87 that is arranged on rotation axis 86 in crosswise.In order to simply, effectively realize the effect of support pallet 88, as shown in figure 12, described tray rack 87 becomes the plate rail body in letter " U " shape.

The principle of work of this device is roughly as follows:

As shown in figure 12, during the work of this device, first conveyer belt mechanism 83, second conveyer belt mechanism 84, the 3rd conveyer belt mechanism 85 first travel forward as motor drives at drive source, the pallet 88 being loaded with slag charge be carried on the first conveyer belt mechanism 83 is made to enter into tray rack 87 on the right of pallet batch turning mechanism 82, originally the complete pallet 8 of batch turning enters into the tray rack 87 on the right of pallet resetting mechanism 82 from the tray rack 7 on pallet batch turning mechanism 2 left side, and pallet 88 forward direction originally in pallet resetting mechanism 82 left side tray rack 87 shifts out; Now, the first conveyer belt mechanism 83, second conveyer belt mechanism 84, the 3rd conveyer belt mechanism 85 brake and stop, and pallet batch turning mechanism 81, pallet resetting mechanism 82 stop after rotating counterclockwise 90 degree, and realizing batch turning, reset etc. is action.This device substantially, carries out alternate repetition ground action exactly between the first conveyer belt mechanism 83, second conveyer belt mechanism 84, the 3rd conveyer belt mechanism 85 and pallet batch turning mechanism 81, pallet resetting mechanism 82, to realize the object that batch turning and pallet reset.

In addition, just as previously mentioned, in the specific implementation, this automatic clinker-removing device 8 is with waste residue drying device 7, separately add an automatic muck loader structure 300, and in conjunction with a streamline conveying belt or rollgang 400, one can be formed when there is the flow production line of automatic charge, automatic discharging and auto-drying function, operate together with the first conveyer belt mechanism 83 and the 3rd conveyer belt mechanism 85 of this automatic clinker-removing device 8 can be incorporated in streamline conveying belt or rollgang 400.

As shown in figure 13, described clear water collection and purification device 9 comprises the first pond 92, pond 91, second, the 3rd pond 93, the 4th pond 94, water collector 95, water pump 96,

Be provided with overflow port 97 between wherein said first pond 91 and the second pond 92, be also provided with overflow port 97 between described second pond 92 and the 3rd pond 93, between described 3rd pond 93 and the 4th pond 94, be also provided with overflow port 97.By overflow port 97 structure between the first pond 91 to the 4th pond 94, the fluctuation of the water entering into each pond is eliminated substantially, be obtained for better static state deposition, and the water that overflow port 97 flows out is all limpid water after precipitation, thus also just ensure that the effect subparticle suspended substance in pretreated water being precipitated effectively removing.

Again as shown in figure 13, the output terminal of described water collector 95 is connected with some isocons 98, and the output terminal of each isocon 98 stretches in the first pond 91 respectively, and the input terminus of described water collector 95 is connected with some water inlet pipes 99.The pretreated water transported is collected by water, the structure design shunted is carried out again by each bar isocon, make the fluctuation of the water entering into the first pond less, thus be conducive to the static state deposition of water except grain process, promote the effect of precipitation purifying treatment.

As shown in figure 13, the input terminus of described water pump 96 is connected with input water pipe 910, and this input water pipe 910 stretches in the 4th pond 94, and the output terminal of described water pump 96 is also connected with water shoot 25, extracts the water sequentially purified through four ponds out application by water pump 96.In addition, according to the design requirements of pond specification, otherly in the side in the 4th pond 94 can be provided with some water pumps 96, the input terminus of each water pump 96 is connected to input water pipe 910, each input water pipe 910 stretches in the 4th pond 94 respectively, and the output terminal of each water pump 96 gathers respectively by water pipe and is connected on a main discharge pipe 940.In addition, the end of described input water pipe 910 is generally also provided with screen element 44, to prevent slag particle to extract, affects the life-span of water pump.

Can extend in the first pond 1 near the pool wall in the first pond 91 to make each isocon 98, as shown in figure 13, the output terminal of described each isocon 98 has also made heel 981 respectively, by the design of heel 981, each isocon 98 can be made can to extend in the first pond 91 near the pool wall in the first pond 91, and then the fluctuation reduced Chi Zhongshui, promote the effect of precipitation purification.

The principle of work of this device is roughly as follows: when pretreated clear water enters water collector 95 by water inlet pipe 99, water is discharged to the bottom in the first pond 91 by the isocon 98 that water collector 95 connects, when decreasing draining, water is to sedimentary impact, fluctuation can not be caused, or make fluctuation less, the water in the first pond 91 flows into precipitation purification in the second pond 92 by overflow port 97, overflow to the 3rd pond 93, through the precipitation in the 3rd pond 93, overflow to the 4th pond 94 again to precipitate, use is extracted the most again by water pump 96, the water extracted there is no suspended particle, reach standards for industrial water usage, thus the sewage produced in enterprise's production link is obtained be cycled to repeat utilization.

Claims (18)

1. a ceramic industry waste hot gas effluent cycle utilizes treatment system, it is characterized in that: comprise sewage collection equipment (1), grain slag precipitation separation device (2), clear water and mud Automatic Extraction device (3), Sludge Collector (4), slurry medicine rotational flow mixing device (5), pressure slag device (6), waste residue drying device (7), automatic clinker-removing device (8), clear water collection and purification device (9), wherein

Described sewage collection equipment (1) is connected by sewage discharge place of pipeline with workshop, Ceramics Enterprises production line, with the sewage centralized collection produced in workshop, Ceramics Enterprises production line; Described sewage collection equipment (1) is connected with grain slag precipitation separation device (2) by pipeline, gives grain slag precipitation separation device (2) carry out grain slag separation with sump pump collection come;

Clear water collection and purification device (9) given by the isolated fresh water pump of described grain slag precipitation separation device (2), the isolated screenings of described grain slag precipitation separation device (2) sends clear water and mud Automatic Extraction device (3) to by pipeline, clear water collection and purification device (9) given by the fresh water pump that described clear water and mud Automatic Extraction device (3) precipitate and isolate, and the scum pump that described clear water and mud Automatic Extraction device (3) precipitate and isolate gives Sludge Collector (4);

Described Sludge Collector (4) will be collected scum pump and give slurry medicine rotational flow mixing device (5), pressure slag device (6) is delivered to after the mixed medicine of slurry medicine rotational flow mixing device (5), described pressure slag device (6) is connected with waste residue drying device (7), dry so that slag charge dry for squeezing is sent into waste residue drying device (7), described waste residue drying device (7) is provided with high temperature hot gas input terminus, this high temperature hot gas input terminus is connected by the high-temperature exhaust emission pipe of pipeline with workshop, Ceramics Enterprises production line, described automatic clinker-removing device (8) is connected with waste residue drying device (7) exit end, unload to realize slag charge automatic pouring.

2. ceramic industry waste hot gas effluent cycle utilizes treatment system according to claim 1, it is characterized in that: described sewage collection equipment (1) comprises sewage collecting pool (11), sump pump (12), sewage input tube (13), medicine pond (14), Automatic Dosing mechanism (15), dispatch pipe (16), tail pipe (17), wherein said sewage input tube (13) is connected with sewage collecting pool (11), described medicine pond (13) is connected with sewage input tube (13) by water pipe, described Automatic Dosing mechanism (15) is serially connected with on the water pipe between medicine pond (13) and sewage input tube (13), one end of described tail pipe (17) is connected with the input terminus of sump pump (12), and the other end of this tail pipe (17) stretches in sewage collecting pool (11), described dispatch pipe (16) is connected to the output terminal of sump pump (12).

3. ceramic industry waste hot gas effluent cycle utilizes treatment system according to claim 2, it is characterized in that: the Automatic Dosing mechanism (15) of described sewage collection equipment (1) is made up of water pump, Flow-rate adjustment controller and control apparatus unit, water pipe between Automatic Dosing mechanism (15) and medicine pond (13) is also serially connected with valve (18), the other end port of described tail pipe (17) is also set with screen element (44).

4. ceramic industry waste hot gas effluent cycle utilizes treatment system according to claim 1, it is characterized in that: described grain slag precipitation separation device (2) comprises slime water input tube (21), slime water imports buffer tube (22), grain slag precipitate and separate cylinder (23) and eddy flow slagging device (24), wherein

Described grain slag precipitate and separate cylinder (23) becomes the housing structure of the cylindrical shape in top, the tapered shape in bottom, the cylinder mouth inwall of grain slag precipitate and separate cylinder (23) is also provided with spilling water annular groove (231), the outer wall of grain slag precipitate and separate cylinder (23) is also provided with water shoot (25) accordingly that be connected with spilling water annular groove (231), is also provided with slag-drip opening (232) in the bottom of grain slag precipitate and separate cylinder (23);

Described slime water imports the pipe structure that buffer tube (22) becomes the cylindrical shape in top, bottom flare shape, the centre that this slime water importing buffer tube (22) is vertically installed in grain slag precipitate and separate cylinder (23) is set up, and the overhead height that this slime water imports buffer tube (22) will be arranged in the top margin higher than grain slag precipitate and separate cylinder (23), the top that described slime water input tube (21) and slime water import buffer tube (22) is connected;

Described eddy flow slagging device (24) is arranged on and is arranged in the grain slag precipitate and separate cylinder (23) that slime water imports buffer tube (22) below, and this eddy flow slagging device (24) is provided with multiple slag charge enters mouth (241) and multiple slag charge relief outlet (242), together with each slag charge relief outlet (242) of described eddy flow slagging device (24) is connected with the slag-drip opening (232) of grain slag precipitate and separate cylinder (23).

5. ceramic industry waste hot gas effluent cycle utilizes treatment system according to claim 4, it is characterized in that: by some the scum pipes (243) bending to circular shape, from top to bottom structure assembles described eddy flow slagging device (24) in the shape of a spiral, and the slag charge of each scum pipe (243) enters mouth (241) arranges in towards spiral center, together with the scum pipe (26) that the slag charge relief outlet (242) of each scum pipe (243) is provided with the slag-drip opening (232) of grain slag precipitate and separate cylinder (23) is respectively connected; Scum pipe (26) is also provided with residual cake valve (27).

6. ceramic industry waste hot gas effluent cycle utilizes treatment system according to claim 1, it is characterized in that: described clear water and mud Automatic Extraction device (3) comprise grain slag settling tank (31), grain slag feed-pipe (32), sludge discharge pipe (33), clear water vent pipe (34), automatically slag pumper structure (35), mud tail pipe (36), clear water tail pipe (37), automatically take out clear water mechanism (38), wherein

Described clear water mechanism (38) of automatically taking out is made up of ball float frame (310) and the water pump (320) be installed on ball float frame (310), this is automatically taken out clear water mechanism (38) and is arranged in grain slag settling tank (31) by ball float frame (310), described clear water tail pipe (37) is connected to the water pump input terminus automatically taking out clear water mechanism (38), and described clear water vent pipe (34) is connected with the water pump output terminal automatically taking out clear water mechanism (38);

Described automatic slag pumper structure (35) is made up of ball float frame (310) and the water pump (320) be installed on ball float frame (310), this automatic slag pumper structure (35) is arranged in grain slag settling tank (31) by ball float frame (310), described mud tail pipe (36) is connected to the water pump input terminus of automatic slag pumper structure (35), and described sludge discharge pipe (33) is connected with the water pump output terminal of automatic slag pumper structure (35); The output port of described grain slag feed-pipe (32) is connected with grain slag settling tank (31).

7. ceramic industry waste hot gas effluent cycle utilizes treatment system according to claim 6, it is characterized in that: the inhalation port of described clear water tail pipe (37) is also provided with screen element (44), the inhalation port of described mud tail pipe (36) is also provided with screen element (44), described automatic slag pumper structure (35) or automatically take out clear water mechanism (38) ball float frame (310) by two ball floats or keg float (330), and the connection bracket (340) be arranged between these two ball floats or keg float (330) is formed, described automatic slag pumper structure (35) or the water pump (320) automatically taking out clear water mechanism (38) are arranged in connection bracket (340).

8. ceramic industry waste hot gas effluent cycle utilizes treatment system according to claim 1, it is characterized in that: described slurry medicine rotational flow mixing device (5) comprises spiral medicine mixer (51), delivery tube (52), valve (53), wherein said spiral medicine mixer (51) is by shell (511), be arranged at the screw rod (512) in shell (511), and the flange (513) being arranged at shell (511) two end is formed, described delivery tube (52) one end is connected on the sidewall of shell (511) input end, described valve (53) is serially connected with on delivery tube (52).

9. ceramic industry waste hot gas effluent cycle utilizes treatment system according to claim 1, it is characterized in that: described pressure slag device (6) comprises frame (61), the first belt (62), the second belt (63), belt wheel load slag mechanism (64), upper idler (65), lower idler (66), upper tensioning adjusting cylinders (67), lower tensioning adjusting cylinders (68), belt installs around peripheral wheels (69), feeding mouth forms skin wheel (610), wherein

The top of described frame (61) is also provided with tilt stand (611), and described upper tensioning adjusting cylinders (67) is installed on the upper end of this tilt stand (611), and described upper idler (65) is installed on tensioning adjusting cylinders (67); The lower side position that frame (61) is positioned at tilt stand (611) upper end is also provided with assistant support (612), and described feeding mouth forms belt pulley (610) and is installed on the top of this assistant support (612); Described lower tensioning adjusting cylinders (68) be arranged on be positioned at assistant support (612) below frame (61) on, described lower idler (66) is installed on lower tensioning adjusting cylinders (68);

Described belt wheel load slag mechanism (64) is made up of large size belt pulley (641), medium size belt pulley (642), small size belt pulley (643), and wherein large size belt pulley (641), medium size belt pulley (642), small size belt pulley (643) are sequentially installed in frame (61) with arranging in alphabetical serpentine shape;

Described belt installs around peripheral wheels (69) and is taken turns (694) formed by upper belt pulley (691), left leather belt wheel (692), bottom pulley (693), right leather belt, wherein upper belt pulley (691) is installed on the lower end of tilt stand (611), described left leather belt wheel (692) is installed on the left surface of frame (61), described right leather belt wheel (694) is installed on the right flank of frame (61), and described bottom pulley (693) is installed on the bottom of frame (61);

Described first belt (62) is along upper idler (65), large size belt pulley (641), medium size belt pulley (642), small size belt pulley (643) and belt install around peripheral wheels (69) and install around in frame (61), described second belt (63) forms belt pulley (610) along feeding mouth, large size belt pulley (641), medium size belt pulley (642), small size belt pulley (643) and lower idler (66) install around in frame (61), and idler (65) and feeding mouth form the feeding mouth (620) being also formed with ecto-entad between the first belt (62) between belt pulley (610) and the second belt (63) and tilting on being positioned at, and take turns between the first belt (62) between (694) and the second belt (63) and be also formed with discharge port (630) being positioned at lower idler (66) and right leather belt.

10. ceramic industry waste hot gas effluent cycle utilizes treatment system according to claim 1, it is characterized in that: described waste residue drying device (7) comprise dry body of heater (71), take out calorifier (72), dehumidifier blower fan (73), dry entrance roller tables (74) and dry outlet roller tables (75), wherein

Described oven dry body of heater (71) is made up of enclosed Rack Body (711) and the Roller way conveyor structure (712) be arranged in this Rack Body (711), described oven dry entrance roller tables (74) is arranged at the inlet end of drying body of heater (71), described oven dry exports the exit end that roller tables (75) is arranged at oven dry body of heater (71), and the front end of described oven dry body of heater (71) is provided with hot blast feeding mouth (713), moisture outlet port (714) is provided with in the rear end of this oven dry body of heater (71), the described output terminal taking out calorifier (72) is connected to the hot blast of drying body of heater (71) by hot air duct (715) and sends on mouth (713), the input terminus of described dehumidifier blower fan (73) is connected on the moisture outlet port (714) of oven dry body of heater (71) by dehumidifier pipeline (716).

11. according to claim 10 ceramic industry waste hot gas effluent cycle utilize treatment system, it is characterized in that: be provided with some layers of Roller way conveyor structure (712) in described oven dry body of heater (71), described oven dry entrance roller tables (74), oven dry outlet roller tables (75) become the roller tables mechanism with some layers of structure for conveying respectively accordingly.

12. utilize treatment system according to ceramic industry waste hot gas effluent cycle described in claim 11, it is characterized in that: also comprise lifting feeding platform (76) and send platform (77) with lifting, wherein said lifting is sent into platform (76) and is arranged at the inlet end of drying entrance roller tables (74), and described lifting is sent platform (77) and is arranged at the exit end of drying outlet roller tables (75).

13. utilize treatment system according to ceramic industry waste hot gas effluent cycle described in claim 12, it is characterized in that: described lifting feeding platform (76) is sent platform (77) with lifting and is made up of frame (78), motor (79), lifting gantry (710) and chain or belt (720) respectively.

14. utilize treatment system according to ceramic industry waste hot gas effluent cycle described in claim 11, it is characterized in that: described in the end of hot air duct (715) of taking out on calorifier (72) be provided with several take-off pipes (730), the position described oven dry body of heater (71) front end two side faces corresponding to every layer of Roller way conveyor structure (712) is respectively equipped with hot blast and sends into mouth (713), and each take-off pipe (730) of described hot air duct (715) is sent into mouth (713) respectively and is connected with each hot blast.

15. utilize treatment system according to ceramic industry waste hot gas effluent cycle described in claim 11, it is characterized in that: the end of the dehumidifier pipeline (716) on described dehumidifier blower fan (73) is provided with several take-off pipes (730), the position described oven dry body of heater (71) rear end two side faces corresponding to every layer of Roller way conveyor structure (712) is respectively equipped with moisture outlet port (714), and the take-off pipe (730) of described dehumidifier pipeline (716) is connected with each moisture outlet port (714) respectively.

16. according to claim 1 ceramic industry waste hot gas effluent cycle utilize treatment system, it is characterized in that: described automatic clinker-removing device (8) comprises pallet batch turning mechanism (81), pallet resetting mechanism (82), first conveyer belt mechanism (83), second conveyer belt mechanism (84), 3rd conveyer belt mechanism (85), wherein said pallet batch turning mechanism (82) is arranged between the first conveyer belt mechanism (83) and the second conveyer belt mechanism (84), this pallet batch turning mechanism (82) is made up of rotation axis (86) and the tray rack (87) that is arranged on rotation axis (86) in crosswise, described pallet resetting mechanism (82) is arranged between the second conveyer belt mechanism (84) and the 3rd conveyer belt mechanism (85), and this pallet resetting mechanism (82) is made up of rotation axis (86) and the tray rack (87) that is arranged on rotation axis (86) in crosswise.

17. according to claim 1 ceramic industry waste hot gas effluent cycle utilize treatment system, it is characterized in that: described clear water collection and purification device (9) comprises the first pond (91), the second pond (92), the 3rd pond (93), the 4th pond (94), water collector (95), water pump (96), wherein

Overflow port (97) is provided with between described first pond (91) and the second pond (92), also be provided with overflow port (97) between described second pond (92) and the 3rd pond (93), between described 3rd pond (93) and the 4th pond (94), be also provided with overflow port (97); The output terminal of described water collector (95) is connected with some isocons (98), and the output terminal of each isocon (98) stretches in the first pond (91) respectively, and the input terminus of described water collector (95) is connected with some water inlet pipes (99); The input terminus of described water pump (96) is connected with input water pipe (910), and this input water pipe (910) stretches in the 4th pond (94), and the output terminal of described water pump (96) is also connected with water shoot (25).

18. utilize treatment system according to ceramic industry waste hot gas effluent cycle described in claim 17, it is characterized in that: the output terminal of described each isocon (98) has also made heel (981) respectively, the end of described input water pipe (910) is also provided with screen element (44), the side in described 4th pond (94) is other is provided with some water pumps (96), the input terminus of each water pump (96) is connected to input water pipe (910), each input water pipe (910) stretches in the 4th pond (94) respectively, the output terminal of each water pump (96) gathers respectively by water pipe and is connected on a main discharge pipe (940).