CN104230040B - A kind of ceramic industry waste hot gas effluent cycle utilizes treatment system - Google Patents

Abstract

The present invention relates to a kind of ceramic industry waste hot gas effluent cycle and utilize treatment system, its feature is that this system is made up of sewage collection equipment, water slag precipitation separation device, clear water and mud Automatic Extraction device, mud slag collector, slurry medicine rotational flow mixing device, pressure slag device, waste residue drying device, the automatically device such as slag unloading device, clear water collection and purification device. The present invention have effectively achieved the sewage to the generation of Production of Ceramics link, waste residue, waste hot gas effective recycling, reduce the processing cost of pottery enterprise sewage, waste residue, waste hot gas, for pottery, enterprise has saved a large amount of operational cost, but also improve pottery environmental protection of enterprise processing power, enterprise's ring is commented and reaches country's requirement.

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 be got rid of on base, and some are more tiny, subparticle suspended substance that particle diameter is between 0.02-30 micron, then more difficult get rid of quickly, it is necessary to 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, it becomes particularly important. At present, although sewage is also processed by Production of Ceramics producer, but 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 looks for local landfill substantially. And the mud without dehydration drying treatment, its water ratio height, Heavy Weight, transport very inconvenience, transportation cost height, and also in transportation, it is easy to unrestrained, seriously affect surrounding enviroment health. Further, second stage employ cannot also be carried out without the mud of dehydration drying treatment. But, along with the environmental requirement of country is more and more higher, and land resources is non-renewable, it is possible to landfill local fewer and feweri, how to enable sewage mud realize second stage employ and seems particularly important.

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

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

Summary of the invention

It is an object of the invention to solve the problem and deficiency, a kind of ceramic industry waste hot gas effluent cycle is provided to utilize treatment system, this treatment system can realize the sewage to the generation of Production of Ceramics link, waste residue carries out water slag separation, and the water after separation can be purified, reach the effect of recycle, with the slag material after being separated can be squeezed dry moisture content, and the waste hot gas that the slag material of the dry moisture content of squeezing utilizes Production of Ceramics link to produce is dried, so that transporting and recycling.

The 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, water slag precipitation separation device, clear water and mud Automatic Extraction device, mud slag collector, slurry medicine rotational flow mixing device, pressure slag device, waste residue drying device, automatically slag unloading device, clear water collection and purification device, wherein

Described sewage collection equipment is connected by sewage discharge place of pipeline with pottery workshop, enterprise production line, with the sewage centralized collection produced in pottery workshop, enterprise production line; Described sewage collection equipment comprises sewage collecting pool, sump pump, sewage input tube, medicine pond, Automatic Dosing mechanism, dispatch pipe, tail pipe, wherein said sewage input tube is connected with sewage collecting pool, described medicine pond is connected with sewage input tube by water pipe, and described Automatic Dosing mechanism is serially connected with on the water pipe between medicine pond and sewage input tube; One end of described tail pipe is connected with the input terminus of sump pump, and the other end of this tail pipe stretches in sewage collecting pool; Described dispatch pipe is connected to sewage delivery side of pump; Described sewage collection equipment is connected with water slag precipitation separation device by pipeline, carries out water slag separation to give water slag precipitation separation device by the sump pump that collection comes;

Clear water collection and purification device given by the fresh water pump that described water slag precipitation separation device is isolated, the slurry slag that described water slag precipitation separation device is isolated 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 mud slag collector;

Described mud slag collector will be collected scum pump and give slurry medicine rotational flow mixing device, pressure slag device is delivered to after the mixed medicine of slurry medicine rotational flow mixing device, described pressure slag device is connected with waste residue drying device, send into waste residue drying device with the slag material that squeezing is dry to dry, 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 pottery workshop, enterprise production line, described automatic slag unloading device is connected with waste residue drying device exit end, unloads to realize slag material automatic pouring.

The useful effect of the present invention:

(1) basis is bright unifies collection by sewage collection equipment by the sewage of Production of Ceramics, and in collection process, add the dirty water decontamination handles medicine, then it is pumped into water slag precipitation separation device and carries out natural sedimentation purification, major part water 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, separation obtain slag slurry enter into again clear water carry out with mud Automatic Extraction device precipitation be separated with water slag, it is 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 be separated, through clear water, the scum pump obtained with mud Automatic Extraction device and deliver to mud slag collector and carry out unifying to collect, then, being pumped into pressure slag device more as required, to carry out moisture content squeezing dry, it is pumped in pressure slag device process in the process, starch medicine rotational flow mixing device by mud slag and slag material is mixed into medicine, to improve mud slag degree of purification, the slag material of dry moisture is squeezed through pressure slag device, it is sent to waste residue drying device to dry, so that the water ratio of mud slag drops under 10%, reach the requirement meeting and again returning utilization, and the hyperthermia drying hot gas that waste residue drying device is used, then being collected from Production of Ceramics link (the heat extraction mouth such as kiln) by pipeline, hyperthermia drying hot gas is dried through waste residue drying device after utilizing, and temperature significantly reduces, after being extremely beneficial to secondary-cleaned, the external world can be discharged out, from waste residue drying device every pallet slag material out, carry out after automatic slag dumping through automatic slag unloading device, obtain water ratio lower than 10% slag material, then can recycling, but, the water after clear water collection and purification device processes, then can pumped back production link, it is achieved water be cycled to repeat utilization.

(2) the present invention have effectively achieved the sewage to the generation of Production of Ceramics link, waste residue, waste hot gas effective recycling, reduce the processing cost of pottery enterprise sewage, waste residue, waste hot gas, for pottery, enterprise has saved a large amount of operational cost, but also improve pottery environmental protection of enterprise processing power, enterprise's ring is commented and reaches country's requirement.

Accompanying drawing explanation

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

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

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

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

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

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

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

Fig. 8 is the structural principle schematic diagram of the 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 the 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 the waste residue drying device of the present invention.

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

Figure 12 is the structural principle schematic diagram of the automatic slag unloading device of the present invention.

Figure 13 is the structural principle schematic diagram of the 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, water slag precipitation separation device 2, clear water and mud Automatic Extraction device 3, mud slag collector 4, slurry medicine rotational flow mixing device 5, pressure slag device 6, waste residue drying device 7, automatically slag unloading device 8, clear water collection and purification device 9, wherein

Described sewage collection equipment 1 is connected by sewage discharge place of pipeline with pottery workshop, enterprise production line, with the sewage centralized collection produced in pottery workshop, enterprise production line; Described sewage collection equipment 1 is connected with water slag precipitation separation device 2 by pipeline, carries out water slag separation to give water slag precipitation separation device 2 by the sump pump that collection comes;

Clear water collection and purification device 9 given by the fresh water pump that described water slag precipitation separation device 2 is isolated, the slurry slag that described water slag precipitation separation device 2 is isolated 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 mud slag collector 4;

Described mud slag 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, send into waste residue drying device 7 with the slag material that squeezing is dry to dry, 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 pottery workshop, enterprise production line, described automatic slag unloading device 8 is connected with waste residue drying device 7 exit end, unloads to realize slag material 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, pottery enterprise production line 10, such as, the sewage that polishing workshop produces unifies collection, and in collection process, add the dirty water decontamination handles medicine, then it is pumped into water slag precipitation separation device 2 and carries out natural sedimentation purification, major part water 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, separation obtain slag slurry enter into again clear water carry out with mud Automatic Extraction device 3 precipitation be separated with water slag, it is 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 be separated, through clear water, the scum pump obtained with mud Automatic Extraction device 3 and deliver to mud slag 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, it is pumped in pressure slag device 6 process in the process, by slurry medicine rotational flow mixing device 5, slag material is mixed into medicine, to improve mud slag degree of purification, the slag material of dry moisture is squeezed through pressure slag device 6, it is sent to waste residue drying device 7 to dry, so that the water ratio of mud slag drops under 10%, reach the requirement meeting and again returning 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 through waste residue drying device 7 after utilizing, temperature significantly reduces, after being extremely beneficial to secondary-cleaned, the external world can be discharged out, from waste residue drying device 7 every pallet slag material out, after automatic slag unloading device 8 carries out automatic slag dumping, obtain water ratio lower than 10% slag material, then can recycling, but, the water after clear water collection and purification device 9 processes, then can pumped back production link, it is achieved water be 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 14 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 14 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 water slag precipitation separation device 2, namely as shown in Figure 2. This device not only has the function 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 can fully be mixed, avoid stirring. Described Automatic Dosing mechanism 15 is made up of water pump, Flow-rate adjustment controller and control electric appliance unit. For the ease of equipment repair and maintenance, generally water pipe between Automatic Dosing mechanism 15 and medicine pond 14 is also serially connected with valve 18. In addition, in order to tail pipe 17 is blocked 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 incessantly a kind of, when needing to add separately again, it is possible to connect multiple Automatic Dosing mechanism on sewage input tube, namely as shown in Figure 3. Being added pollution treatment medicine in sewage input tube, in flow process, can fully be mixed, and reaches the object exempting to stir. In addition, if when the amount of sewage disposal is many, sump pump can also install multiple stage as required.

As shown in Figure 4, described water slag precipitation separation device 2 comprises slime water input tube 21, slime water imports buffer tube 22, water slag precipitate and separate cylinder 23 and eddy flow slagging device 24, wherein said water slag precipitate and separate cylinder 23 becomes the cylinder body structure of top cylindrical form, the tapered shape in bottom, the bottom of water slag precipitate and separate cylinder 23 is become cone-shaped structure, is mainly beneficial to mud slag and discharges. The cylinder mouth inwall of water slag precipitate and separate cylinder 23 is also provided with excessive water annular groove 231, the outer wall of water slag precipitate and separate cylinder 23 is also provided with accordingly and the water shoot 25 that excessive water annular groove 231 is connected, this water shoot 25 is connected to clear water collection and purification device 9, carries out purifying up to standard re-using to be delivered to by the clear water overflowed in clear water collection and purification device 9. Slag-drip opening 232 also it is provided with in the bottom of water slag precipitate and separate cylinder 23; Described slime water imports the pipe structure that buffer tube 22 becomes top cylindrical form, bottom flare shape, this slime water imports buffer tube 22 and erects in the center position being installed in water slag precipitate and separate cylinder 23, and the overhead height of this slime water importing buffer tube 22 to be arranged in the limit, top higher than water slag precipitate and separate cylinder 23, the top that described slime water input tube 21 imports buffer tube 22 with slime water is connected. Slime water imports the main effect of buffer tube 22, makes the slime water entering into water slag precipitate and separate cylinder 23 can not produce fluctuation, thus the precipitation that can not have influence on water slag be separated. Described eddy flow slagging device 24 is arranged on the water slag precipitate and separate cylinder 23 being arranged in below slime water importing buffer tube 22, and this eddy flow slagging device 24 is provided with multiple slag material and enters mouth 241 and multiple slag material relief outlet 242, together with each slag material relief outlet 242 of described eddy flow slagging device 24 is connected with the slag-drip opening 232 of water 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 material of each scum pipe 243 enters mouth 241 and arranges in towards spiral center, together with the scum pipe 26 that the slag material relief outlet 242 of each scum pipe 243 is provided with the slag-drip opening 232 of water slag precipitate and separate cylinder 23 respectively is 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, the sewage will sent here from sewage collection equipment 1, import buffer tube 22 by slime water and enter into water slag precipitate and separate cylinder 23, and diversion slag precipitate and separate cylinder 23 can not produce fluctuation by original water, to realize the object of mud by static for water slow precipitation. Under gravity, slag material heavier-weight can sink to cylinder bottom, water can density less, upwards spill-over, through overflow 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 material 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 kind of whirlwind-type row's slag mode, on the one hand, slag material is evenly discharged stablely, larger fluctuation can not be drawn, be conducive to the precipitation of water slag, purification and it be separated; On the other hand, slag material can not static lump, and causes slag-drip opening, has influence on and normally arranges slag. In addition, as shown in Figure 2, when needing sewage quantity to be processed more, multiple such water slag precipitation separation device 2 can be set, distribute by a sewage divider 100 between each water slag precipitation separation device 2, the slime water input tube 21 of each water 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 water slag settling tank 31, water 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 that is installed on ball float frame 310, this is automatically taken out clear water mechanism 38 and is arranged in water slag settling tank 31 by ball float frame 310, and namely described clear water mechanism 38 of automatically taking out is on the water surface floated in water 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, the clear water being conducive to extracting like this, and the thing that forms sediment is few, meanwhile, can ensure again water pump can not lack of water and damage. 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 that is installed on ball float frame 310, and this automatic slag pumper structure 35 is arranged in water slag settling tank 31 by ball float frame 310, with reason, is on the water surface floated in water 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 mud slag collector 4. The output port of described water slag feed-pipe 32 is connected with water slag settling tank 31, and the input port of described water slag feed-pipe 32 is connected with the scum pipe 26 of water slag precipitation separation device 2.

In order to avoid bigger 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. With reason, 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 that is 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 screw rod 512 being arranged in shell 511 and the flange 513 that 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, flow process completes fully mixing of medicine and slime water.

In actual applications, it is possible to according to the slime water amount of flow of sewer line 54 or medicine usefulness, add the number of applications of this device on demand. Simultaneously scheme shown in Fig. 7 starches medicine rotational flow mixing device by two to input medicine to sewer line 54. 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 mud slag 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, the 2nd belt 63, belt wheel load slag mechanism 64, upper tensioning belt pulley 65, lower tensioning belt pulley 66, upper tensioning adjusting cylinders 67, lower tensioning adjusting cylinders 68, belt install around peripheral wheels 69, feeding mouth forms belt pulley 610, the top of wherein said frame 61 also is provided with support 611, this inclination support 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 inclination support 611, and described upper tensioning belt pulley 65 is installed on tensioning adjusting cylinders 67. The lower side position being positioned at support 611 upper end in frame 61 is also provided with secondary support 612, and this pair support 612 is also the feeding mouth structure forming ecto-entad tilt to coordinate, and described feeding mouth forms belt pulley 610 and is installed on the top of this pair support 612. Described lower tensioning adjusting cylinders 68 is arranged on and is positioned in the frame 61 below secondary support 612, and described lower tensioning belt pulley 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 letter " S " arrangements. The quantity of described medium size belt pulley 642, small size belt pulley 643, it is possible to press dry situation according to slag material and carry out designing and adopting, quantity is not particularly limited.

In order to make the first belt 62 can comparatively reasonably be installed in frame 1, as shown in Figure 8, described belt installs around peripheral wheels 69 and is made up of upper belt pulley 691, left leather belt wheel 692, bottom pulley 693, right leather belt wheel 694, wherein upper belt pulley 691 is installed on the lower end of support 611, described left leather belt wheel 692 is installed on the face, left side of frame 61, described right leather belt wheel 694 is installed on the face, right side of frame 61, and described bottom pulley 693 is installed on the bottom of frame 61. described first belt 62 is along upper tensioning belt pulley 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 2nd 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 tensioning belt pulley 66 install around in frame 61, and forming the first belt 62 between belt pulley 610 at upper tensioning belt pulley 65 and feeding mouth and between the 2nd belt 63, be also formed with the feeding mouth 620 of ecto-entad inclination, and taking turns the first belt 62 between 694 at lower tensioning belt pulley 66 and right leather belt and be also formed with discharge port 630 between the 2nd belt 63.

Described upper tensioning adjusting cylinders 67, lower tensioning adjusting cylinders 68 are mainly used in regulating the tensioning degree of the first belt 62, the 2nd belt 63, press dry rate to obtain relatively high-moisture.

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

As shown in Figure 8, above inclination support 611, a transfer lime 640 is set, this transfer lime 640 is connected with the sewer line 54 of slurry medicine rotational flow mixing device 5, the slag material that water content is bigger drops on the first belt 62 on support 611 by transfer lime 640, first belt 62 and the same direction motion of the 2nd belt 63, slag material is made to enter into after belt wheel load slag mechanism 64 squeezes one time from feeding mouth 620, from discharge port 630 out, namely obtain having squeezed dry slag material, moisture content then falls below belt wheel load slag mechanism 64, it is achieved water and slag are separated. In addition, as shown in Figure 2, from the slag material conveyer belt mechanism 200 of the discharge port 630 of this pressure slag device 6 slag material out through being arranged between this discharge port 630 and waste residue drying device 7, deliver in waste residue drying device 7 and dry, to reduce the water ratio of slag material further.

Such 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 that is arranged in this Rack Body 711, described oven dry entrance roller tables 74 is arranged at the inlet end drying body of heater 71, described outlet roller tables 75 of drying is arranged at the exit end 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, it is provided with moisture outlet port 714 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 drying body of heater 71 and sends on mouth 713 by hot air duct 715, the input terminus taking out calorifier 72 is then connected to hot gas offer source by an other segment pipe. the input terminus of described dehumidifier blower fan 73 is connected on the moisture outlet port 714 drying body of heater 1 by dehumidifier pipeline 716, after the output terminal of dehumidifier blower fan 73 then outputs to other predetermined device processes by an other segment pipe, then discharges the external world.

The drying efficiency drying body of heater 71 to improve, as shown in Figure 9 and Figure 10, being 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 drying entrance roller tables 74, the inlet end that platform 76 is sent in this lifting is then connected with conveying pipeline, automatically to be conveyed on each layer Roller way conveyor structure 712 drying body of heater 71 by slag material. Described lifting is sent platform 77 and is arranged at the exit end 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 material of slag 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 not being described in detail.

When oven dry body of heater 1 adopts some layers of Roller way conveyor structure 712 for structure, 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 some take-off pipes 730, the position corresponding to every layer of Roller way conveyor structure 712 on the two side faces of described oven dry body of heater 71 front end is respectively equipped with hot blast feeding 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. With reason, 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 some take-off pipes 730, the position corresponding to every layer of Roller way conveyor structure 712 on the two side faces of described oven dry body of heater 71 rear end 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 becoming side by side by some roller rods of a kind of slow formula rotation, and by motor-driven transfer mechanism, so that slag material transmits 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 and automatic slag unloading device 8, an automatic Zhuan Zha mechanism 300 that separately adds, and in conjunction with a streamline conveying belt or rollgang 400, one can be formed there is automatic charge, automatically discharging and the flow production line of automatic drying function.

As shown in figure 12, described automatic slag unloading device 8 comprises pallet batch turning mechanism 81, pallet resetting mechanism 82, first conveyer belt mechanism 83, the 2nd conveyer belt mechanism 84, the 3rd conveyer belt mechanism 85, wherein said pallet batch turning mechanism 81 is arranged between the first conveyer belt mechanism 83 and the 2nd conveyer belt mechanism 84, and this pallet batch turning mechanism 81 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 2nd 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, when this device works, first conveyer belt mechanism 83, the 2nd conveyer belt mechanism 84, the 3rd conveyer belt mechanism 85 first move forward as motor drives in driving source, the pallet 88 being loaded with slag material being carried on the first conveyer belt mechanism 83 is made to enter into the tray rack 87 on the right of pallet batch turning mechanism 81, 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 81 left side, and pallet 88 forward direction in pallet resetting mechanism 82 left side tray rack 87 is moved out originally; Now, the first conveyer belt mechanism 83, the 2nd 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, it is achieved batch turning, reset etc. is action. Substantially, the first conveyer belt mechanism 83, the 2nd conveyer belt mechanism 84, the 3rd conveyer belt mechanism 85 and carry out alternately action repeatedly between pallet batch turning mechanism 81, pallet resetting mechanism 82 exactly, with the object realizing batch turning and pallet resets for this device.

In addition, just as previously mentioned, in the specific implementation, this automatically slag unloading device 8 and waste residue drying device 7, an automatic Zhuan Zha mechanism 300 that separately adds, and in conjunction with a streamline conveying belt or rollgang 400, when can form the flow production line that has automatic charge, automatically discharging and drying function automatically, first conveyer belt mechanism 83 of this slag unloading device 8 automatically can be incorporated in streamline conveying belt or rollgang 400 with the 3rd conveyer belt mechanism 85 together with operate.

As shown in figure 13, described clear water collection and purification device 9 comprises the first pond 91, the 2nd pond 92, the 3rd pond 93, the 4th pond 94, water collector 95, water pump 96,

It is provided with overflow port 97 between wherein said first pond 91 and the 2nd pond 92, between described 2nd pond 92 and the 3rd pond 93, also it is provided with overflow port 97, 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 entering into the water in each pond is eliminated substantially, it is 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 that the subparticle suspended substance in pretreated water obtains effectively precipitating 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 entering into the water in 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, design requirements according to pond specification, other 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 is gathered by water pipe respectively 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 extracting by slag particle, affects the life-span of water pump.

In order to make each isocon 98 can extend in the first pond 1 near the pool wall in the first pond 91, 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 reduce the fluctuation to 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 connected on water collector 95, when decreasing draining, water is to the impact of throw out, fluctuation can not be caused, or make fluctuation less, the water in the first pond 91 flows into precipitation purification in the 2nd 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 and is cycled to repeat utilization.

Claims (17)

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

Described sewage collection equipment (1) is connected by sewage discharge place of pipeline with pottery workshop, enterprise production line, with the sewage centralized collection produced in pottery workshop, enterprise production line; 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 (14) 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 (14) 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); Described sewage collection equipment (1) is connected with water slag precipitation separation device (2) by pipeline, carries out water slag separation to give water slag precipitation separation device (2) by the sump pump that collection comes;

Clear water collection and purification device (9) given by the fresh water pump that described water slag precipitation separation device (2) is isolated, the slurry slag that described water slag precipitation separation device (2) is isolated 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 mud slag collector (4);

Described mud slag collector (4) will be collected scum pump and be given 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), send into waste residue drying device (7) with the slag material that squeezing is dry to dry, 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 pottery workshop, enterprise production line, described automatic slag unloading device (8) is connected with waste residue drying device (7) exit end, unload to realize slag material automatic pouring.

2. ceramic industry waste hot gas effluent cycle utilizes treatment system according to claim 1, 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 electric appliance unit, water pipe between Automatic Dosing mechanism (15) and medicine pond (14) is also serially connected with valve (18), the other end port of described tail pipe (17) is also set with screen element (44).

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

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

Described slime water imports the pipe structure that buffer tube (22) becomes top cylindrical form, bottom flare shape, this slime water imports buffer tube (22) and erects in the center position being installed in water slag precipitate and separate cylinder (23), and the overhead height of this slime water importing buffer tube (22) to be arranged in the limit, top higher than water slag precipitate and separate cylinder (23), the top that described slime water input tube (21) imports buffer tube (22) with slime water is connected;

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

4. ceramic industry waste hot gas effluent cycle utilizes treatment system according to claim 3, 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 material of each scum pipe (243) enter mouth (241) in towards spiral center arrange, together with the scum pipe (26) that slag material relief outlet (242) of each scum pipe (243) is provided with the slag-drip opening (232) of water slag precipitate and separate cylinder (23) respectively is connected; Scum pipe (26) is also provided with residual cake valve (27).

5. 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 water slag settling tank (31), water 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) that is installed on ball float frame (310), this is automatically taken out clear water mechanism (38) and is arranged in water 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) that is installed on ball float frame (310), this automatic slag pumper structure (35) is arranged in water 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 water slag feed-pipe (32) is connected with water slag settling tank (31).

6. ceramic industry waste hot gas effluent cycle utilizes treatment system according to claim 5, 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) being 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).

7. 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), the screw rod (512) being arranged 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).

8. 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 2nd belt (63), belt wheel load slag mechanism (64), upper tensioning belt pulley (65), lower tensioning belt pulley (66), upper tensioning adjusting cylinders (67), lower tensioning adjusting cylinders (68), belt install around peripheral wheels (69), feeding mouth forms belt pulley (610), wherein

The top of described frame (61) also is provided with support (611), and described upper tensioning adjusting cylinders (67) is installed on the upper end of this inclination support (611), and described upper tensioning belt pulley (65) is installed on tensioning adjusting cylinders (67); The lower side position being positioned at support (611) upper end in frame (61) is also provided with secondary support (612), and described feeding mouth forms belt pulley (610) and is installed on the top of this pair support (612); Described lower tensioning adjusting cylinders (68) is arranged in the frame (61) being positioned at secondary support (612) lower section, and described lower tensioning belt pulley (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) in letter " S " arrangements;

Described belt installs around peripheral wheels (69) and is made up of upper belt pulley (691), left leather belt wheel (692), bottom pulley (693), right leather belt wheel (694), wherein upper belt pulley (691) is installed on the lower end of support (611), described left leather belt wheel (692) is installed on the face, left side of frame (61), described right leather belt wheel (694) is installed on the face, right side of frame (61), and described bottom pulley (693) is installed on the bottom of frame (61);

Described first belt (62) is along upper tensioning belt pulley (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 2nd 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 tensioning belt pulley (66) install around in frame (61), and tensioning belt pulley (65) and feeding mouth form the first belt (62) between belt pulley (610) and are also formed with the feeding mouth (620) of ecto-entad inclination between the 2nd belt (63) on being positioned at, and also it is formed with discharge port (630) between the first belt (62) being positioned between lower tensioning belt pulley (66) and right leather belt wheel (694) and the 2nd belt (63).

9. 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) 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

Described oven dry body of heater (71) is made up of enclosed Rack Body (711) and the Roller way conveyor structure (712) that is arranged in this Rack Body (711), described oven dry entrance roller tables (74) is arranged at the inlet end 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), it is provided with moisture outlet port (714) 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 drying body of heater (71) and sends on mouth (713) by hot air duct (715), the input terminus of described dehumidifier blower fan (73) is connected on the moisture outlet port (714) drying body of heater (71) by dehumidifier pipeline (716).

10. ceramic industry waste hot gas effluent cycle utilizes treatment system according to claim 9, 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.

11. according to claim 10 ceramic industry waste hot gas effluent cycle utilize treatment system, 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 drying entrance roller tables (74), and described lifting is sent platform (77) and is arranged at the exit end drying outlet roller tables (75).

12. utilize treatment system according to ceramic industry waste hot gas effluent cycle described in claim 11, it is characterised 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.

13. according to claim 10 ceramic industry waste hot gas effluent cycle utilize treatment system, it is characterized in that: described in take out on calorifier (72) the end of hot air duct (715) be provided with some take-off pipes (730), the position corresponding to every layer of Roller way conveyor structure (712) on the two side faces of described oven dry body of heater (71) front end is respectively equipped with hot blast feeding 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.

14. according to claim 10 ceramic industry waste hot gas effluent cycle utilize treatment system, it is characterized in that: the end of the dehumidifier pipeline (716) on described dehumidifier blower fan (73) is provided with some take-off pipes (730), the position corresponding to every layer of Roller way conveyor structure (712) on the two side faces of described oven dry body of heater (71) rear end 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.

15. according to claim 1 ceramic industry waste hot gas effluent cycle utilize treatment system, it is characterized in that: described automatic slag unloading device (8) comprises pallet batch turning mechanism (81), pallet resetting mechanism (82), first conveyer belt mechanism (83), 2nd conveyer belt mechanism (84), 3rd conveyer belt mechanism (85), wherein said pallet batch turning mechanism (81) is arranged between the first conveyer belt mechanism (83) and the 2nd conveyer belt mechanism (84), this pallet batch turning mechanism (81) 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 2nd 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.

16. 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 2nd pond (92), the 3rd pond (93), the 4th pond (94), water collector (95), water pump (96), wherein

It is provided with overflow port (97) between described first pond (91) and the 2nd pond (92), also it is provided with overflow port (97) between described 2nd pond (92) and the 3rd pond (93), between described 3rd pond (93) and the 4th pond (94), also it is 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).

17. utilize treatment system according to ceramic industry waste hot gas effluent cycle described in claim 16, 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), respectively inputting water pipe (910) stretches in the 4th pond (94) respectively, the output terminal of each water pump (96) is gathered by water pipe respectively and is connected on a main discharge pipe (940).