CN206027734U - Automatic cycle recycle system of catalyst - Google Patents

Abstract

The utility model discloses an automatic cycle recycle system of catalyst, it includes module dust cleaning system, harmless circulation system, two dry activation system and the system of calcining of recycling of wasing of non -pressure in advance, module dust cleaning system in advance includes clean room, a transfer passage, high -pressure spraying and blowing organ and negative pressure wind blower, the harmless washing of non -pressure is recycled circulation system and is included clean water basin, fermentation vat, the harmless self - cleaning equipment of module non -pressure, is washd pond, sedimentation tank and pressure filter, two dry activation systems include high temperature fan, first drying chamber, secondary drying chamber, the 2nd transfer passage, the 3rd transfer passage, intake pipe, outlet duct, first connecting pipe, second connecting pipe and third connecting pipe, the system of calcining includes forge -cave and fourth transfer passage. The utility model discloses a regeneration of catalyst module, furthest's resources are saved can realize industrial waste water cycle recycle, a large amount of saving spaces moreover.

Description

Catalyst Automatic Cycle reutilization system

Technical field

This utility model belongs to catalyst regeneration techniques field, more particularly to a kind of catalyst Automatic Cycle recycles system System.

Background technology

China is coal-fired big country, can all discharge substantial amounts of nitrogen oxides every year, cause serious environmental pollution.It is dirty for reducing Dye, present coal-burning power plant of China is generally processed to flue gas using denitrating catalyst.And denitrating catalyst uses two in power plant Year or so, a large amount of dusts can be piled up in catalyst module surface and hole, long-time reaction causes catalyst activity to reduce, in flue gas The harmful substances such as the heavy metal of band are attached to catalyst surface, reduce the denitration efficiency of catalyst, cause power plant emission not up to standard. For meeting emission request, coal-burning power plant has to regularly replace new catalyst, and buying fresh catalyst needs to spend a large amount of money Gold, and the old catalyst for changing contains harmful substance, careless place is comprehended to environment.Therefore catalyst regenerates is Trend of the times, can reduce secondary pollution, can realize recycling for resource again.

Utility model content

This utility model is in order to solve the problems of the prior art, there is provided a kind of catalyst Automatic Cycle reutilization system, The regeneration of catalyst module is realized, is economized on resources to greatest extent, and industrial wastewater cycling and reutilization can be realized, Substantial amounts of saving space, its Environmental Safety, high working efficiency can be with substantial amounts of reduces cost.

For solving above-mentioned technical problem, this utility model is adopted the following technical scheme that：Catalyst Automatic Cycle recycles system System, it includes the pre- soot cleaning system of module, without pressing lossless cleaning to recycle blood circulation, double be dried activation system and calcination system；

The pre- soot cleaning system of module includes dirt pocket, the first transfer passage, high pressure blow smelting operation mechanism and negative pressure induced wind mechanism, first The dirt pocket is laid and passed through to transfer passage along the feedstock direction of dirt pocket, the first transfer passage portion inside dirt pocket It is divided into roller-way, roller-way is provided with gap by multiple carrying roller spread configurations between adjacent carrying roller；High pressure blow smelting operation mechanism includes injection master Pipe, is disposed with multiple injection arms on injection supervisor, is blown the lower section that arm is arranged in roller-way, each injection arm Arrangement arranges multiple opening up nozzles along its length for upper and carrying roller corresponding position；Negative pressure induced wind mechanism include with The discharge pipe connected at the top of dirt pocket, the gas outlet of discharge pipe are connected with air-introduced machine, spread configuration on the side wall of dirt pocket There is at least one air inlet, each air inlet is provided with unpowered fan；

Without press lossless cleaning recycle blood circulation include clear water reserviors, fermentation vat, module without press lossless automatic cleaning equipment, Service sink, sedimentation tank and pressure filter, the upper and lower of fermentation vat are corresponded to respectively and offer water inlet and outlet, service sink Upper and lower corresponds to respectively and offers water inlet and outlet；

Module is provided with whirlwind water conservancy diversion knot without the cylinder for pressing lossless automatic cleaning equipment to include vertical placement, inner barrel Structure, whirlwind flow-guiding structure include locating shaft and deflector, and locating shaft is arranged along the axis of cylinder, and the upper end of locating shaft with Cylinder is fixedly connected, and the deflector is around locating shaft spiral surrounding and is secured to connection, and cylinder top is provided with water inlet, cylinder Body bottom is provided with outlet with locating shaft corresponding position, and water outlet is connected with spray head；It is provided with below spray head Spray pond, the top of spray pond is set to open, is fixedly installed horizontal module setter plate, in module setter plate in spray pond Water-guiding hole is provided with, the bottom of spray pond is provided with discharge outlet；

The water inlet of fermentation vat, the water inlet of service sink and module are without the water inlet for pressing lossless automatic cleaning equipment middle cylinder body Connected with clear water reserviors by inlet channel and the first water pump being arranged on inlet channel, below the outlet of fermentation vat, module Sedimentation tank is correspondingly arranged on without pressing in lossless automatic cleaning equipment below the discharge outlet of spray pond and below the outlet of service sink；

The charging aperture of pressure filter is connected with sedimentation tank by feed pipe and the second water pump being arranged on feed pipe, is pressed The liquid outlet of filter is connected with clear water reserviors by water return pipeline；

Double activation systems that are dried include high-temperature blower, the first hothouse, secondary drying chamber, the second transfer passage, the 3rd defeated Send passage, air inlet pipe, escape pipe, the first connecting tube, the second connecting tube and the 3rd connecting tube, second transfer passage is located at the One is dried interior, and the 3rd transfer passage is located in secondary drying chamber, and the high-temperature blower is connected with air inlet pipe, the first connecting tube To be connected at the top of the top of the first hothouse and secondary drying chamber, the second connecting tube is by the bottom of the first hothouse and second The bottom of hothouse is connected, and the air inlet pipe and escape pipe are connected with the first connecting tube, and the 3rd connecting tube is by Two connecting tubes are connected with escape pipe, and the first connecting tube between the air inlet pipe and the first hothouse is provided with the first valve, The first connecting tube between the air inlet pipe and escape pipe is provided with the second valve, the 3rd connecting tube and the first connecting tube it Between escape pipe be provided with the 3rd valve, the second connecting tube between the 3rd connecting tube and the first hothouse is provided with the 4th Valve, the 3rd connecting tube are provided with the 5th valve, the second connecting tube between the 3rd connecting tube and secondary drying chamber The 6th valve is provided with, and activating tank is provided between first hothouse and secondary drying chamber, is provided with catalyst mould in activating tank Block cleanout fluid；

Calcination system includes calcining kiln and the 4th transfer passage, and the 4th transfer passage is spread along the feedstock direction of calcining kiln And if passing through the calcining kiln.

The injection arm is be arranged in parallel with the roll body of the carrying roller；

The injection arm is arranged on the gap location arrange between adjacent carrying roller；

The first transfer passage part outside dirt pocket is ribbon conveyer, and ribbon conveyer docked with the roller-way Form first transfer passage；

The high pressure blow smelting operation mechanism and negative pressure induced wind mechanism are oppositely arranged on the both sides of dirt pocket.

Cleaner unit is provided between the discharge pipe and air-introduced machine, and the air inlet of cleaner unit is connected with the gas outlet of discharge pipe Logical, the air outlet of cleaner unit is connected with the air inlet of air-introduced machine；

The injection supervisor is provided with air door positioned on the body outside dirt pocket.

First water pump is the immersible pump being arranged in clear water reserviors；Second water pump is centrifugal pump.

It also includes centrifugal pump pond, and the centrifugal pump is arranged on the bottom of pond in centrifugal pump pond, the bottom of pond face in centrifugal pump pond and institute The bottom of pond face for stating sedimentation tank is in same plane.

Aspiration tube is provided with the fermentation vat and service sink, and a part of body of aspiration tube is located inside cell body, drum Another part body of trachea is located at outside cell body.

The bottom of the fermentation vat is set to the inverted cone-shaped structure that upper end is big, lower end is little, and the outlet of fermentation vat is arranged on The lower end center position of its inverted cone-shaped structure；

The bottom of the service sink is set to the inverted cone-shaped structure that upper end is big, lower end is little, and the outlet of service sink is arranged on The lower end center position of its inverted cone-shaped structure；

The spray pond is located at the position below module setter plate and is set to the inverted cone-shaped structure that upper end is big, lower end is little.

The water outlet of the outlet and service sink of the fermentation vat is provided with electrically operated valve；

Ribbon conveyer is provided with the solid outlet of the pressure filter；The water outlet of the fermentation vat is provided with vibration Sieve.

The bottom of pond face of the sedimentation tank by positioned at side bottom of pond horizontal plane and positioned at opposite side bottom of pond inclined-plane docking and Into, and bottom of pond horizontal plane is located at the bottom on bottom of pond inclined-plane；The connecting portion of the feed pipe and sedimentation tank is in the bottom of pond water Plane side；The bottom of pond face in the centrifugal pump pond is in same plane with the bottom of pond horizontal plane of the sedimentation tank.

The calcining kiln is natural gas kiln；Second transfer passage and the 3rd transfer passage are ribbon conveyer； Waste liquid collecting box is provided with below 3rd transfer passage；4th transfer passage is provided with many for transporting turning for catalyst module Fortune car.

The beneficial effects of the utility model are：

The workflow of catalyst Automatic Cycle reutilization system of the present utility model is as follows：Catalyst module after use Initially enter the pre- soot cleaning system of module, remove surface and hole interior part dust, afterwards using bridge crane by catalyst module Send into without pressing lossless cleaning to recycle blood circulation to carry out cleaning treatment, the catalyst module for cleaning up has large quantity of moisture, this When to be dried activation system and module is dried and activation processing by double.Eventually passing through calcination system carries out calcination processing, The activating and regenerating work of catalyst module is completed.

Cooperation of the pre- soot cleaning system of module by dirt pocket, roller-way, high pressure blow smelting operation mechanism and negative pressure induced wind mechanism, realizes To efficient, the environmentally friendly removing of dust can be piled up in catalyst module surface and hole.During work, the smoke inlet side of catalyst module To placing down, stop fixing after pushing in dedusting room by carrying roller, open air door, the pressure-air Jing in injection supervisor Injection arm nozzle spray, formed high pressure draught blow to catalyst module, in Modular surface and hole dust with high pressure draught to Upper flowing；Air-introduced machine is opened simultaneously, negative pressure is formed in dedusting room, and the airborne dust that high pressure blow smelting operation mechanism cleaning catalyst module is produced leads to Dirt pocket top discharge pipe is crossed into cleaner unit and is discharged.The catalyst module cleaned out is released, and a workflow is completed.

The first transfer passage inside dirt pocket is roller-way, and the first transfer passage outside dirt pocket is belt Conveyer, ribbon conveyer dock to form first transfer passage with the roller-way, and in said structure design, the first conveying is logical Road is docked and is formed by the roller-way and the ribbon conveyer outside dirt pocket inside dirt pocket, and which not only ensure that catalysis The conveying function of agent module, and do not affect injection dedusting of the high pressure blow smelting operation mechanism to catalyst module.

Cleaner unit is provided between the discharge pipe and air-introduced machine, and the air inlet of cleaner unit is connected with the gas outlet of discharge pipe Logical, the air outlet of cleaner unit is connected with the air inlet of air-introduced machine, and cleaner unit can be carried out at dedusting to the air that discharge pipe is discharged Reason, it is to avoid pollution environment.

Injection arm is be arranged in parallel with the roll body of the carrying roller, and the injection arm is arranged on what is arranged between adjacent carrying roller Gap location, improves action effect of the pressure-air to catalyst module.The injection supervisor is positioned at the body outside the dirt pocket On be provided with air door, be easy to control pressure-air injection.

The high pressure blow smelting operation mechanism and negative pressure induced wind mechanism are oppositely arranged on the both sides of dirt pocket, are easy to high pressure blow smelting operation mechanism Arrangement with negative pressure induced wind mechanism on dirt pocket is installed.

Clear water reserviors, fermentation vat, module are recycled in blood circulation without pressing lossless automatic cleaning equipment, clear without lossless cleaning is pressed The cooperation of wash pool, sedimentation tank and pressure filter and inlet channel, the first water pump, feed pipe and the second water pump, can not only be effective The impurity removed in catalyst module, realize the regeneration of catalyst module, economize on resources to greatest extent, and can Realize industrial wastewater cycling and reutilization, substantial amounts of saving space, its simple to operate, Environmental Safety, high working efficiency can be a large amount of Reduces cost.

Module is provided with whirlwind flow-guiding structure without the inner barrel for pressing lossless automatic cleaning equipment, and whirlwind flow-guiding structure includes Locating shaft and deflector, locating shaft are arranged along the axis of cylinder, and the upper end of locating shaft is fixedly connected with cylinder, described to lead Stream plate is around locating shaft spiral surrounding and is secured to connection, and cylinder top is provided with water inlet, and cylinder body bottom is corresponding with locating shaft Outlet is provided with position, and water outlet is connected with spray head, said structure design middle cylinder body and whirlwind flow-guiding structure and spray The collective effect of head is drenched, the current of stable and uniform are formed, then the spray head from the water outlet of cylinder sprays, to catalyst mould Block is cleaned.The current of stable and uniform not only can remove the impurity such as the flyash in catalyst module, and can protect The fragile part in catalyst module two ends is against damages.

Without spray pond is provided with below spray head in the lossless automatic cleaning equipment of pressure, the top of spray pond is set to module It is open, horizontal module setter plate is fixedly installed in spray pond, module setter plate is provided with water-guiding hole, and the bottom of spray pond sets Discharge outlet is equipped with, catalyst module is lifted in the module setter plate into spray pond during work, and spray head enters to catalyst module Water after row cleaning flows through water-guiding hole and discharges into spray pond bottom, and the discharge outlet of Jing spray ponds.Module setter plate plays right The supporting role of catalyst module.

First water pump is the immersible pump being arranged in clear water reserviors, is easy to inject the liquid in clear water reserviors by inlet channel To fermentation vat, service sink and module without in the cylinder for pressing lossless automatic cleaning equipment.Second water pump be centrifugal pump, be easy to by The mixing liquid with impurity in sedimentation tank is evacuated in pressure filter by feed pipe.Centrifugal pump is arranged on the pond in centrifugal pump pond Bottom, the bottom of pond face in centrifugal pump pond are in same plane with the bottom of pond face of the sedimentation tank, and the setting in centrifugal pump pond ensure that centrifugation Extraction effect of the pump to sedimentation tank, because centrifugal pump is before activation, it is necessary to make full of water in pump case and suction hose, centrifugal pump pond Bottom of pond face is in same plane with the bottom of pond face of the sedimentation tank, and in enabling sedimentation tank, liquid is flushed to pump case and water suction automatically In pipe.

Below the outlet of fermentation vat, module is without pressing in lossless automatic cleaning equipment the lower section of the discharge outlet of spray pond and clear The impurity such as sedimentation tank pond, the flyash in catalyst module passage are correspondingly arranged on below the outlet of wash pool as current are arranged Enter sedimentation tank.Bottom of pond inclined-plane docking of the bottom of pond face of sedimentation tank by the bottom of pond horizontal plane positioned at side and positioned at opposite side is formed, And bottom of pond horizontal plane is located at the bottom on bottom of pond inclined-plane, the above-mentioned setting in bottom of pond face can make the mixture in sedimentation tank to a lateral deviation Tiltedly, it is easy to follow-up cleaning.

The bottom of the fermentation vat or service sink is set to the inverted cone-shaped structure that upper end is big, lower end is little, the fermentation vat Outlet is arranged on the lower end center position of its inverted cone-shaped structure, above-mentioned design forming conflux effect, it is to avoid liquid is in immersion Residual in pond or service sink.The spray pond is located at the position below module setter plate and is set to the back taper that upper end is big, lower end is little Shape structure, it is to avoid liquid is remained in spray pond.

Aspiration tube is provided with the fermentation vat and service sink, and a part of body of aspiration tube is located inside cell body, drum Another part body of trachea is located at outside cell body, by using aspiration tube to the mode of injecting compressed air in water, makes immersion Water in pond and service sink forms rolling, so as to drive the impurity such as the flyash accumulated in catalyst module, is allowed to therefrom remove.

The water outlet of the outlet and service sink of fermentation vat is provided with electrically operated valve, is easy to control correspondence outlet Folding.

Ribbon conveyer is provided with the solid outlet of the pressure filter, the residue scrap obtained after pressure filter is separated It is transported in waste material conveying car by ribbon conveyer.The water outlet of the fermentation vat is provided with vibrosieve, fermentation vat conduct Accumulate the first order of impurity in removing catalyst module, larger impurity after removing, in fermentation vat, can be retained, used by oscillating screen is in mistake The larger impurity of filter granule.

Recycle the work flow of blood circulation as follows without lossless cleaning is pressed：

First, open the immersible pump in clear water reserviors, by inlet channel respectively to fermentation vat, without pressing lossless cleaning equipment, clear Injected clear water in wash pool.

2nd, catalyst module is lifted into fermentation vat, by using mode from aspiration tube to injecting compressed air in water, Make the water in fermentation vat form rolling, so as to drive the impurity such as the flyash accumulated in catalyst module, be allowed to therefrom remove.Powder The impurity such as coal ash lodge in fermentation vat bottom, periodically open the electric gate valve of bottom, while vibrosieve filters larger miscellaneous of granule Matter, remaining enters sedimentation tank.

3rd, catalyst module is lifted into spray pond after soaking, is utilized without the lossless cleaning equipment of pressure to catalyst module The mode of spray, will compare obstinate dust stratification and wash away and dispose, enter in sedimentation tank in catalyst module passage.Not only can The impurity such as the flyash in removal catalyst module, and stable spray protects the fragile portion in catalyst module two ends simultaneously Divide against damages.

4th, catalyst module is lifted into service sink after spraying, compression is injected in water again by using aspiration tube Air, makes the water in service sink form the mode of rolling, so as to remove the impurity such as flyash of remaining in catalyst module.Periodically The electric gate valve of service sink bottom is opened, is discharged it in sedimentation tank.

5th, when the waste material impurity in sedimentation tank reaches to a certain degree, start centrifugal pump in centrifugal pump pond by sedimentation tank In waste water be evacuated in pressure filter by feed pipe, pressure filter work by waste water processing be separated into residue scrap and clear water.

6th, the detached clear water in pressure filter is back in clear water reserviors by water return pipeline, and residue scrap passes through belt Conveyer is transported in waste material conveying car.Waste material conveying car is transported, and is processed.

Double activation systems that are dried are dried to catalyst module and activation processing, the effective secondary utilization energy of energy, are made Heat recycled for multiple times, reduce waste, it is cost-effective, and this system can either coordinated operation, again can be with independent operating, can Allocated according to the needs of production.Wherein the catalyst module flowed down from the 3rd transfer passage can be cleaned by waste liquid collecting box Liquid is collected, it is to avoid liquid waste penetrates into soil, and the soil of surrounding is polluted.

When calcination system is used, make calcining kiln in-furnace temperature reach pre-determined stability first, then will be equipped with catalyst module Transfer car(buggy) send into calcining kiln in calcined, complete calcining after, catalyst module is sent into calcining kiln, the calcination system Polylith module can be once calcined, high working efficiency realizes the effectively utilizes of the energy.

Description of the drawings

Fig. 1 is structural front view of the present utility model；

Fig. 2 is the front view of the pre- soot cleaning system of module；

Fig. 3 is the top view of the pre- soot cleaning system of module；

Fig. 4 is the rearview of the pre- soot cleaning system of module；

Fig. 5 is the left view of Fig. 4 mesohigh spraying and blowing organs；

Fig. 6 is the enlarged drawing at injection arm position in Fig. 5；

Fig. 7 is without the structural representation for pressing lossless cleaning to recycle blood circulation；

Fig. 8 is enlarged drawing of the module without the lossless automatic cleaning equipment of pressure in Fig. 7；

Fig. 9 is double front views for being dried activation system and calcination system.

Specific embodiment

Specific embodiment of the present utility model is elaborated below in conjunction with accompanying drawing.

As shown in figure 1, catalyst Automatic Cycle reutilization system of the present utility model, including being arranged in order in the horizontal direction The pre- soot cleaning system 91 of module of setting, without press it is lossless cleaning recycle blood circulation 92, it is double be dried activation system 93 and calcining system System 94.

The workflow of catalyst Automatic Cycle reutilization system is as follows：Catalyst module after use initially enters module Pre- soot cleaning system, removes surface and hole interior part dust, sends into catalyst module using bridge crane afterwards lossless without pressing Cleaning recycles blood circulation to carry out cleaning treatment, and the catalyst module for cleaning up has large quantity of moisture, at this moment will be by double dry Dry activation system is dried to module and activation processing, and eventually passing through calcination system carries out calcination processing, that is, complete catalyst The activating and regenerating work of module.

As shown in Figures 2 to 6, the pre- soot cleaning system 91 of module in this utility model, it includes that dirt pocket 83, first is conveyed Passage, high pressure blow smelting operation mechanism 84 and negative pressure induced wind mechanism, the first transfer passage are laid and are passed through along the feedstock direction of dirt pocket 83 The dirt pocket 83, the first transfer passage is by the roller-way 821 inside dirt pocket 83 and the belt outside dirt pocket 83 Conveyer docking 822 is formed, and roller-way 821 is made up of 89 spread configuration of multiple carrying rollers, is set between the adjacent carrying roller 89 at roller-way 821 It is equipped with gap；High pressure blow smelting operation mechanism 84 includes injection supervisor 841, is disposed with multiple injection arms on injection supervisor 841 842, the lower section that arm 842 is arranged in roller-way 821 is blown, injection arm 842 is be arranged in parallel with the roll body of carrying roller 89, and is sprayed Blow arm 842 and be arranged on the gap location arrange between adjacent carrying roller 89, with 89 corresponding position of carrying roller on each injection arm 842 Arrangement arranges multiple opening up nozzles 88 along its length.

Injection supervisor 841 is positioned at being provided with air door 87 on the body outside dirt pocket 83.

Negative pressure induced wind mechanism includes and the discharge pipe 85 being connected at the top of dirt pocket 83, the gas outlet connect setting of discharge pipe 85 There is air-introduced machine 810, on the 83 side wall of dirt pocket of the both sides of the first transfer passage 82, respectively arrange four air inlets 86, each air inlet Unpowered fan 861 is provided with 86.

Cleaner unit 811, air inlet and the discharge pipe 85 of cleaner unit 811 is provided between discharge pipe 85 and air-introduced machine 810 Gas outlet connects, and the air outlet of cleaner unit 811 is connected with the air inlet of air-introduced machine 810, and cleaner unit 811 can be to 85 row of discharge pipe The air for going out carries out dust removal process, it is to avoid pollution environment.The air outlet of air-introduced machine 810 is connected with open exhaust duct upward 812。

The high pressure blow smelting operation mechanism 84 and negative pressure induced wind mechanism are oppositely arranged on the both sides of dirt pocket 83.

During utility model works, the smoke inlet of catalyst module 5 is directed downward placement, by the first transfer passage 82 Stop fixing after pushing in dirt pocket 83, open air door 87, the pressure-air Jing injection arms 842 in injection supervisor 841 Nozzle 88 spray, formed high pressure draught blow to catalyst module 5, in Modular surface and hole dust with high pressure draught to upstream It is dynamic；Air-introduced machine 810 is opened simultaneously, negative pressure is formed in dirt pocket 83, and what the cleaning catalyst module 5 of high pressure blow smelting operation mechanism 84 was produced raises Dirt enters cleaner unit 811 by 83 top discharge pipe 85 of dirt pocket and Jing causes the exhaust duct 812 of the connection of machine 810 to discharge.Cleaning Clean catalyst module 1 is released.

The pre- soot cleaning system of module 91 realizes the removing to piling up dust in catalyst module surface and hole, and environmental protection peace Entirely, high working efficiency.

As shown in Figure 7 and Figure 8, in this utility model without press it is lossless cleaning recycle blood circulation 92, it includes clear water Pond 11, fermentation vat 3, module without pressing lossless automatic cleaning equipment 6, service sink 9, sedimentation tank 17 and pressure filter 1, fermentation vat 3 it is upper Portion and bottom correspond to respectively and offer water inlet and outlet, and the upper and lower of service sink 9 corresponds to respectively and offers water inlet And outlet, the outlet of fermentation vat 3, the water outlet of service sink 9 are correspondingly arranged on electrically operated valve 15,13.

Without the cylinder 61 for pressing lossless automatic cleaning equipment 6 to include vertical placement, the bottom of the cylinder 61 is set to module Upper end is big, the inverted cone-shaped structure that lower end is little.Cylinder 61 is internally provided with whirlwind flow-guiding structure, and whirlwind flow-guiding structure includes locating shaft 66 and deflector 67, locating shaft 66 is arranged along the axis of cylinder 61, and the upper end of locating shaft 66 is fixedly connected with cylinder 61, 6 plate 7 of the water conservancy diversion is around 66 spiral surrounding of locating shaft and is secured to connection, and 61 top of cylinder is provided with water inlet 68, cylinder 61 Bottom is provided with outlet 610 with 66 corresponding position of locating shaft, is connected with spray head 62 at outlet 610.Module is without pressure nothing The collective effect of the said structure design middle cylinder body 61 and whirlwind flow-guiding structure and spray head 62 of automatic cleaning equipment 6 is damaged, is formed The current of stable and uniform, then the spray head 62 from the outlet 68 of cylinder 61 spray, catalyst module is cleaned.Surely Fixed uniform current not only can remove the impurity such as the flyash in catalyst module, and can be with guard catalyst module two ends Fragile part is against damages.

The lower section of spray head 62 is provided with spray pond 64, and the top of spray pond 64 is set to open, fixation in spray pond 64 Horizontal module setter plate 611 is provided with, module setter plate 611 is provided with water-guiding hole, and the bottom of spray pond 64 is provided with draining Mouth 612.Water-guiding hole is sign in the accompanying drawings, the arrangement of water-guiding hole and is installed as the routine techniquess ability of those skilled in the art, The present embodiment is no longer described in detail.During work, catalyst module is lifted in the module setter plate 611 into spray pond 64, spray head 62 pairs Water after catalyst module is cleaned flows through water-guiding hole into 64 bottom of spray pond, and 612 row of discharge outlet of Jing spray ponds 64 Go out.Module setter plate 611 plays the supporting role to catalyst module.

The water inlet of fermentation vat 3, the water inlet of service sink 9 and module are without lossless 6 middle cylinder body 61 of automatic cleaning equipment of pressure Water inlet 68 is connected with clear water reserviors 11 by inlet channel 10 and the first water pump 12 being arranged on inlet channel 10, fermentation vat 3 Outlet below, module is without pressing in lossless automatic cleaning equipment 6 below the discharge outlet 612 of spray pond 64 and service sink 9 goes out Sedimentation tank 17 is correspondingly arranged on below the mouth of a river.

The bottom of pond face of sedimentation tank 17 is by the bottom of pond horizontal plane 171 positioned at side and positioned at 172 pairs, the bottom of pond inclined-plane of opposite side Connect and form, and bottom of pond horizontal plane 171 is located at the bottom on bottom of pond inclined-plane 172.

The charging aperture of pressure filter 1 passes through feed pipe 18 and the second water pump 19 being arranged on feed pipe 18 and sedimentation tank 17 connections, the liquid outlet of pressure filter 1 are connected with clear water reserviors 11 by water return pipeline 14.The company of feed pipe 18 and sedimentation tank 17 Socket part is located at 171 side of bottom of pond horizontal plane.

First water pump 12 is the immersible pump being arranged in clear water reserviors 11；Second water pump 19 is centrifugal pump.Centrifugation Pump is arranged on the bottom of pond in centrifugal pump pond 21, and the bottom of pond face in centrifugal pump pond 21 is in the bottom of pond horizontal plane 171 of the sedimentation tank 17 Same plane.

Aspiration tube 4 is provided with fermentation vat 3, is provided with aspiration tube 8, a part of body position of aspiration tube 4,8 on service sink 9 Inside cell body, another part body of aspiration tube 4,8 is located at outside cell body, injects pressure by using aspiration tube 4,8 in water The mode of contracting air, makes the water formation rolling in fermentation vat 3 and service sink 9, so as to drive the fine coal accumulated in catalyst module The impurity such as ash, are allowed to therefrom remove.

The bottom of the fermentation vat 3 is set to the inverted cone-shaped structure that upper end is big, lower end is little, and the outlet of fermentation vat 3 is arranged In the lower end center position of its inverted cone-shaped structure.The bottom of the service sink 9 is set to the inverted cone knot that upper end is big, lower end is little Structure, the outlet of service sink 9 are arranged on the lower end center position of its inverted cone-shaped structure.The spray pond 64 is disposed positioned at module Position below plate is set to the inverted cone-shaped structure that upper end is big, lower end is little.Above-mentioned inverted cone-shaped structure is designed to form conflux Effect, it is to avoid liquid is remained in fermentation vat 3, service sink 9 or spray pond 64.

The water outlet of the fermentation vat 3 is provided with vibrosieve 16, and fermentation vat 3 accumulates miscellaneous as removing in catalyst module The first order of matter, can retain larger impurity in fermentation vat 3 after removing, vibrosieve 16 is used for filtering the larger impurity of granule.

Ribbon conveyer 2 is provided with the solid outlet of the pressure filter 1, and what is can obtained after pressure filter 1 is separated is residual Slag scrap is transported in waste material conveying car 22 by ribbon conveyer 2.

Recycle the work flow of blood circulation 92 as follows without lossless cleaning is pressed：

First, open clear water reserviors 11 in immersible pump, by inlet channel 10 respectively to fermentation vat 3, without press it is lossless cleaning set Standby 6, injected clear water in service sink 9.

2nd, catalyst module 5 is lifted into fermentation vat 3, by using side from aspiration tube 4 to injecting compressed air in water Formula, makes the water formation rolling in fermentation vat 3, so as to drive the impurity such as the flyash accumulated in catalyst module 5, is allowed to therefrom go Remove.The impurity such as flyash lodge in 3 bottom of fermentation vat, periodically open the electric gate valve 15 of bottom, while the filtration of vibrosieve 16 The larger impurity of grain, remaining enters sedimentation tank 17.

3rd, catalyst module 5 is lifted into spray pond 64 after soaking, using without pressing lossless cleaning equipment 6 to catalyst The mode of the spray of module 5, will compare obstinate dust stratification and wash away and dispose, enter in sedimentation tank 17 in 5 passage of catalyst module. The impurity such as flyash in catalyst module 5 not only can be removed, and stable spray protects 5 liang of catalyst module simultaneously The fragile part in end is against damages.

4th, catalyst module 5 is lifted into service sink 9 after spraying, pressure is injected in water again by using aspiration tube 8 Contracting air, makes the water in service sink 9 form the mode of rolling, so as to remove the impurity such as flyash of remaining in catalyst module 5. The electric gate valve 13 of 9 bottom of service sink is periodically opened, is discharged it in sedimentation tank 17.

5th, when the waste material impurity in sedimentation tank 17 reaches to a certain degree, the centrifugal pump 19 started in centrifugal pump pond 21 will Waste water in sedimentation tank 17 is evacuated in pressure filter 1 by feed pipe 18, and pressure filter 1 works and waste water processing is separated into residue and is given up Material block and clear water.

6th, the detached clear water in pressure filter 1 is back in clear water reserviors 11 by water return pipeline 14, and residue scrap passes through Ribbon conveyer 2 is transported in waste material conveying car 22.Waste material conveying car 22 is transported, and is processed.

Without pressing lossless cleaning to recycle blood circulation 92 effectively remove the impurity in catalyst module, realize The regeneration of catalyst module, is economized on resources to greatest extent, and can realize industrial wastewater cycling and reutilization, substantial amounts of Saving space, its simple to operate, Environmental Safety, high working efficiency can be with substantial amounts of reduces cost.

As shown in figure 9, it is double be dried activation system 93 include high-temperature blower 71, the first hothouse 72, secondary drying chamber 73, Two transfer passages 74, the 3rd transfer passage 75, air inlet pipe 76, escape pipe 77, the first connecting tube 78, the second connecting tube 79 and the 3rd Connecting tube 710, second transfer passage 74 are located in the first hothouse 72, and the 3rd transfer passage 75 is located at secondary drying chamber 73 Interior, the high-temperature blower 71 is connected with air inlet pipe 76, and the top of the first hothouse 72 and second are dried by the first connecting tube 78 The top of room 73 is connected, and the bottom of the first hothouse 72 is connected by the second connecting tube 79 with the bottom of secondary drying chamber 73, The air inlet pipe 76 and escape pipe 7 are connected with the first connecting tube 78, and the 3rd connecting tube 710 is by 79 He of the second connecting tube Escape pipe 77 is connected, and the first connecting tube 78 between the air inlet pipe 76 and the first hothouse 72 is provided with the first valve 711, In the first connecting tube between the air inlet pipe 76 and escape pipe 77,78 are provided with the second valve 712, the 3rd connecting tube 710 with Escape pipe 77 between first connecting tube 78 is provided with the 3rd valve 713, the 3rd connecting tube 710 and the first hothouse 72 it Between the second connecting tube 79 be provided with the 4th valve 714, the 3rd connecting tube 710 is provided with the 5th valve 715, the described 3rd The second connecting tube 79 between connecting tube 710 and secondary drying chamber 73 is provided with the 6th valve 716,72 He of the first hothouse Activating tank 717 is provided between secondary drying chamber 73, catalyst module cleanout fluid is provided with activating tank 717, and the 3rd conveying is logical The lower section in road 75 is provided with waste liquid collecting box 718.

Calcination system 94 includes natural gas kiln 722（Its model WM-SSY-1600）, the natural gas kiln 722 The 4th transfer passage 720 of transport catalyst is equipped with the ground of lower section, and the 4th transfer passage 720 is along natural gas kiln The natural gas kiln 722 is laid and passed through to 722 feedstock direction, has parked many transfer car(buggy)s on the 4th transfer passage 720 721。

It is first turned on high-temperature blower 71 during use, opens the first valve 711, high-temperature hot-air is blown into into the by air inlet pipe 76 One connecting tube 78 simultaneously enters into the first hothouse 72, opens the 4th valve 714 and the 6th valve 716, while by the 5th valve 715 Close, high-temperature hot-air enters into secondary drying chamber 73 by the second connecting tube 79, close the second valve 712, open the 3rd valve The first connecting tube of 713, high-temperature hot-air Jing 78 and escape pipe 77 are discharged.

When the temperature of the first hothouse 72 and the 3rd hothouse 73 reaches 60 DEG C -70 DEG C, will be without the lossless cleaning of pressure again The first hothouse 72 is sent into using the catalyst module 5 that blood circulation 92 was cleaned by the second transfer passage 74 to be done for the first time It is dry；After first drying is completed, catalyst module 5 is sent by the second transfer passage 74, then by lifting machine by catalyst module 5 hang in activating tank 17, carry out cleaning activation using the catalyst module cleanout fluid in activating tank to catalyst module 5；So Catalyst module 5 is hung in on the 3rd transfer passage 75 using lifting machine afterwards, the harm for now remaining on catalyst module 5 is molten Liquid is flow in waste liquid collecting box 718, in order to finally do unified process, prevents from polluting environment, last 3rd transfer passage 75 Catalyst module 5 is delivered to carries out redrying process in secondary drying chamber 73, redrying processes the 3rd conveying after completing Catalyst module 5 is sent secondary drying chamber 73 by passage 75, when temperature reaches 7600 DEG C in the natural gas kiln 722,

73 dried catalyst module 5 of Jing secondary drying chambers enters natural by the 4th transfer passages 720 of 721 Jing of transfer car(buggy) Gas kiln 722, catalyst module 5 is unloaded from transfer car(buggy) 721 and is calcined, after calcination operation terminates, by catalyst mould Block 5 is reinstalled transfer car(buggy) 721 and transports natural gas kiln 722, and so far a workflow is completed, that is, complete catalyst mould The activating and regenerating work of block.

Above example is only to illustrative and not limiting the technical solution of the utility model, although reference above-described embodiment pair This utility model has been described in detail, it will be understood by those within the art that：Still this utility model can be entered Row modification or equivalent, without deviating from any modification or partial replacement of spirit and scope of the present utility model, which all should Cover in the middle of right of the present utility model.

Claims (10)

1. catalyst Automatic Cycle reutilization system, it is characterised in that：It include the pre- soot cleaning system of module, without press it is lossless cleaning again Using blood circulation, double it is dried activation system and calcination system；

The pre- soot cleaning system of module includes dirt pocket, the first transfer passage, high pressure blow smelting operation mechanism and negative pressure induced wind mechanism, the first conveying The dirt pocket is laid and passed through to passage along the feedstock direction of dirt pocket, and the first transfer passage part inside dirt pocket is Roller-way, roller-way are provided with gap by multiple carrying roller spread configurations between adjacent carrying roller；High pressure blow smelting operation mechanism includes injection supervisor, Multiple injection arms are disposed with injection supervisor, the lower section that arm is arranged in roller-way is blown, on each injection arm Arrangement arranges multiple opening up nozzles along its length with carrying roller corresponding position；Negative pressure induced wind mechanism includes and removes The discharge pipe of dirt ceiling portion connection, the gas outlet of discharge pipe is connected with air-introduced machine, is disposed with the side wall of dirt pocket At least one air inlet, each air inlet are provided with unpowered fan；

Blood circulation is recycled to include clear water reserviors, fermentation vat, module without the lossless automatic cleaning equipment of pressure, cleaning without lossless cleaning is pressed Pond, sedimentation tank and pressure filter, the upper and lower of fermentation vat are corresponded to respectively and offer water inlet and outlet, the top of service sink Corresponded to bottom respectively and offer water inlet and outlet；

Module is provided with whirlwind flow-guiding structure, revolves without the cylinder for pressing lossless automatic cleaning equipment to include vertical placement, inner barrel Wind flow-guiding structure includes locating shaft and deflector, and locating shaft is arranged along the axis of cylinder, and upper end and the cylinder of locating shaft It is fixedly connected, the deflector is around locating shaft spiral surrounding and is secured to connection, and cylinder top is provided with water inlet, cylinder bottom Portion is provided with outlet with locating shaft corresponding position, and water outlet is connected with spray head；Spray is provided with below spray head Pond, the top of spray pond is set to open, is fixedly installed horizontal module setter plate in spray pond, and module setter plate is provided with Water-guiding hole, the bottom of spray pond are provided with discharge outlet；

The water inlet of fermentation vat, the water inlet of service sink and module pass through without the water inlet for pressing lossless automatic cleaning equipment middle cylinder body Inlet channel and the first water pump being arranged on inlet channel are connected with clear water reserviors, and below the outlet of fermentation vat, module is without pressure Sedimentation tank is correspondingly arranged on below the discharge outlet of spray pond and below the outlet of service sink in lossless automatic cleaning equipment；

The charging aperture of pressure filter is connected with sedimentation tank by feed pipe and the second water pump being arranged on feed pipe, pressure filter Liquid outlet connected with clear water reserviors by water return pipeline；

Double activation systems that are dried include that high-temperature blower, the first hothouse, secondary drying chamber, the second transfer passage, the 3rd conveying are logical Road, air inlet pipe, escape pipe, the first connecting tube, the second connecting tube and the 3rd connecting tube, second transfer passage are dry positioned at first Dry interior, the 3rd transfer passage are located in secondary drying chamber, and the high-temperature blower is connected with air inlet pipe, and the first connecting tube is by the The top of one hothouse be connected at the top of secondary drying chamber, the second connecting tube by the bottom of the first hothouse and second be dried The bottom of room is connected, and the air inlet pipe and escape pipe are connected with the first connecting tube, and the 3rd connecting tube connects second Adapter is connected with escape pipe, and the first connecting tube between the air inlet pipe and the first hothouse is provided with the first valve, described The first connecting tube between air inlet pipe and escape pipe is provided with the second valve, between the 3rd connecting tube and the first connecting tube Escape pipe is provided with the 3rd valve, and the second connecting tube between the 3rd connecting tube and the first hothouse is provided with the 4th valve Door, the 3rd connecting tube is provided with the 5th valve, in the second connecting tube between the 3rd connecting tube and secondary drying chamber The 6th valve is provided with, and activating tank is provided between first hothouse and secondary drying chamber, is provided with catalyst module in activating tank Cleanout fluid；

Calcination system includes calcining kiln and the 4th transfer passage, and the 4th transfer passage is laid simultaneously along the feedstock direction of calcining kiln Through the calcining kiln.

2. catalyst Automatic Cycle reutilization system according to claim 1, it is characterised in that：The injection arm and institute The roll body for stating carrying roller be arranged in parallel；

The injection arm is arranged on the gap location arrange between adjacent carrying roller；

The first transfer passage part outside dirt pocket is ribbon conveyer, and ribbon conveyer docks to be formed with the roller-way First transfer passage；

The high pressure blow smelting operation mechanism and negative pressure induced wind mechanism are oppositely arranged on the both sides of dirt pocket.

3. catalyst Automatic Cycle reutilization system according to claim 1, it is characterised in that：The discharge pipe and air inducing Cleaner unit is provided between machine, the air inlet of cleaner unit is connected with the gas outlet of discharge pipe, the air outlet and air-introduced machine of cleaner unit Air inlet connection；

The injection supervisor is provided with air door positioned on the body outside dirt pocket.

4. catalyst Automatic Cycle reutilization system according to claim 1, it is characterised in that：First water pump is to set Put the immersible pump in clear water reserviors；Second water pump is centrifugal pump.

5. catalyst Automatic Cycle reutilization system according to claim 4, it is characterised in that：It also includes centrifugal pump Pond, the centrifugal pump are arranged on the bottom of pond in centrifugal pump pond, and the bottom of pond face in centrifugal pump pond is with the bottom of pond face of the sedimentation tank in same One plane.

6. the catalyst Automatic Cycle reutilization system according to claim 1 or 4 or 5, it is characterised in that：The fermentation vat Be provided with aspiration tube on service sink, a part of body of aspiration tube is located inside cell body, another part body of aspiration tube Outside cell body.

7. catalyst Automatic Cycle reutilization system according to claim 6, it is characterised in that：The bottom of the fermentation vat The inverted cone-shaped structure that upper end is big, lower end is little is set to, the outlet of fermentation vat is arranged on the lower end centre bit of its inverted cone-shaped structure Put place；

The bottom of the service sink is set to the inverted cone-shaped structure that upper end is big, lower end is little, and the outlet of service sink is arranged on which and falls The lower end center position of pyramidal structure；

The spray pond is located at the position below module setter plate and is set to the inverted cone-shaped structure that upper end is big, lower end is little.

8. catalyst Automatic Cycle reutilization system according to claim 7, it is characterised in that：The water outlet of the fermentation vat The water outlet of mouth and service sink is provided with electrically operated valve；

Ribbon conveyer is provided with the solid outlet of the pressure filter；The water outlet of the fermentation vat is provided with vibrosieve.

9. catalyst Automatic Cycle reutilization system according to claim 5, it is characterised in that：The bottom of pond of the sedimentation tank Bottom of pond inclined-plane docking of the face by the bottom of pond horizontal plane positioned at side and positioned at opposite side is formed, and bottom of pond horizontal plane is oblique positioned at bottom of pond The bottom in face；The connecting portion of the feed pipe and sedimentation tank is in the bottom of pond horizontal plane side；The pond in the centrifugal pump pond Bottom surface is in same plane with the bottom of pond horizontal plane of the sedimentation tank.

10. catalyst Automatic Cycle reutilization system according to claim 1, it is characterised in that：The calcining kiln is Natural gas kiln；Second transfer passage and the 3rd transfer passage are ribbon conveyer；It is provided with below 3rd transfer passage Waste liquid collecting box；4th transfer passage is provided with many transfer car(buggy)s for transporting catalyst module.