CN214781445U - Sludge drying device - Google Patents

Abstract

The utility model discloses a sludge drying device, which comprises a drying rotary drum, wherein the drying rotary drum comprises an outer rotary drum and an inner rotor, the outer rotary drum is horizontally arranged, the inner rotor is arranged in the outer rotary drum, two ends of the drying rotary drum are respectively an inlet end and an outlet end, the inlet end is connected with an air inlet chamber for accessing hot flue gas, the outlet end is connected with an air outlet chamber for discharging low-temperature hot flue gas, the drying rotary drum is sequentially divided into a front section, a middle section and a rear section from the inlet end to the outlet end, the outer rotary drum and the inner rotor rotate in the same direction, a plurality of stirring rods are arranged on the inner rotor, and the stirring rods are arranged in a double-helix shape; an auxiliary crushing structure is arranged on the inner wall surface of the outer rotary drum. The utility model provides a sludge drying device, which directly dries high-temperature hot flue gas, and has high heat transfer efficiency and good drying effect; the specific surface area is fast to replace, and the drying efficiency is high; drying in a Brownian motion mode, and drying uniformly; the abrasion of equipment is reduced, and the service life of the equipment is prolonged; the mechanical energy consumption is reduced.

Description

Sludge drying device

Technical Field

The utility model belongs to the technical field of sludge treatment technique and specifically relates to a screw propulsion formula sludge drying device is related to.

Background

With the development of modern industry, a huge amount of various municipal domestic sludge and industrial sludge can be born all year round. The sludge drying technology is a common technology which can effectively reduce the water content of the sludge so as to facilitate the subsequent treatment of the sludge, and particularly is a process of heating the sludge in specially designed equipment and evaporating the water in the sludge. The method not only can effectively realize the effect of removing free water in the sludge, but also can quickly evaporate interstitial water, surface bound water and even internal bound water in the sludge, but also has long drying time. In addition, a centrifugal drying or electric heating method is adopted, the drying cost is low for centrifugal drying, but the reduction degree of the water content of the sludge is limited, and the water content of the sludge after centrifugal treatment is still high, so that the combustion requirement cannot be met; for electric heating, although the drying effect is good, extra energy is consumed, which results in higher cost. In addition, in the sludge drying process, the water content reaches 50% -55%, the sludge enters a sticky adhesive state, and drying equipment can generate great abrasion, so that the service life of the drying equipment is shortened. The utility model discloses a "rotation type sludge drying device" that chinese patent literature was disclosed, its publication No. CN208933214U, including the stoving case, the top movable mounting of stoving case has the agitator tank, the bottom intercommunication on agitator tank right side has the unloading pipe, the right side intercommunication at agitator tank top has the feeding funnel, the welding of the left bottom of agitator tank has the fixed plate, the first motor of top fixedly connected with of fixed plate, the output shaft of first motor passes through shaft joint fixedly connected with agitator pipe. The utility model discloses a first motor drives the agitator pipe and rotates, and the rethread air-blower carries dry wind to the inside of agitator pipe and the inside of agitator tank through double-deck drying mechanism and carries out double-deck drying, and rethread drive mechanism reciprocates the agitator tank and prevents that mud from blockking up in unloading pipe department, and although the device has improved drying efficiency to a certain extent, the device is difficult to carry out drying or discharge to the mud of bottom, and is difficult to guarantee even mummification.

SUMMERY OF THE UTILITY MODEL

The utility model provides a sludge drying device, which aims to overcome the problems of low drying efficiency, poor drying effect, uneven drying, larger abrasion in the installation process, influence on the service life of drying equipment and the like of the existing drying device, and has the advantages of high heat transfer efficiency and good drying effect; the specific surface area is fast to replace, and the drying efficiency is high; drying in a Brownian motion mode, and drying uniformly; the abrasion of equipment is reduced, and the service life of the equipment is prolonged; the mechanical energy consumption is reduced.

In order to achieve the above purpose, the utility model adopts the following technical scheme:

a sludge drying device comprises a drying rotary drum, wherein the drying rotary drum comprises an outer rotary drum and an inner rotor, the outer rotary drum is horizontally arranged, the inner rotor is arranged in the outer rotary drum, two ends of the drying rotary drum are respectively provided with an inlet end and an outlet end, the inlet end is connected with an air inlet chamber used for connecting hot flue gas, the outlet end is connected with an air outlet chamber used for discharging low-temperature hot flue gas, the drying rotary drum is sequentially divided into a front section, a middle section and a rear section from the inlet end to the outlet end, the outer rotary drum and the inner rotor rotate in the same direction, a plurality of stirring rods are arranged on the inner rotor, and the stirring rods are arranged in a double-helix shape; an auxiliary crushing structure is arranged on the inner wall surface of the outer rotating cylinder, and a secondary wind shield is arranged on the middle section of the outer rotating cylinder. In the technical scheme, wet materials enter a drying rotary drum from an inlet end to be dried, the wet materials gradually move towards an outlet end under the combined action of the co-rotation of an outer rotary drum and an inner rotor and hot smoke, a stirring rod and an auxiliary crushing structure are used for crushing the materials, namely when the wet materials enter the drying rotary drum, the outer rotary drum rotates to drive the wet materials at the bottom of the outer rotary drum to the top of the outer rotary drum and throw the wet materials downwards, the stirring rod crushes large materials into small materials with wet surfaces, the small materials in a supermarket are quickly faced after contacting high-temperature hot air introduced into an air inlet chamber, the small materials are crushed into particles under the action of the stirring rod, and the particle materials move towards the outlet end under the action of high-temperature air flow of the air inlet chamber, wherein the auxiliary crushing structure is used for assisting the outer rotary drum to drive the wet materials to the top to be crushed by the auxiliary stirring rod, in the moving process, the dried particles can be bonded with the particles with high humidity, the particles are separated again after reaching a certain dryness and slowly move to an outlet and are finally discharged from the outlet end, a Brownian motion mode is formed, the uniform drying effect is achieved, and after the whole sludge is dried to a certain degree, when the water content of the sludge reaches 50% -55%, the material is in a fine boiling particle shape and is not in a bonding state, the problem that the sludge is viscous in a region is effectively solved, the equipment abrasion is reduced, and the service life of the equipment is greatly prolonged. In addition, the stirring rod is arranged in a double-spiral manner, so that the material can be conveniently crushed and forwards pushed to move, and the drying efficiency is improved. In addition, the second-level wind shield is used for blocking hot air flow, under the condition that the flow of the hot air flow is not changed, the area of the air flow is changed, the speed of the air flow is further changed, the speed of the air flow is increased, the materials can be pushed more conveniently, most of the materials in the middle section are small materials and granular materials with dry surfaces, in addition, the hot air is sealed in the rotary drum by the second-level wind shield, and turbulent flow is formed under the action of the internal components of the drying rotary drum, so that heat is fully used for drying the materials.

Preferably, the auxiliary crushing structure comprises a lifting plate arranged on the inner wall surface of the outer rotary drum, and the lifting plate is arranged in an arc-shaped structure. The lifting plate is arranged to be beneficial to driving the material to the top from the bottom of the outer rotary drum and throwing the material, so that the material is contacted with the stirring rod and is crushed by the stirring rod, the contact area between the material and hot air is increased, and the drying of the material is facilitated.

Preferably, the auxiliary crushing structure comprises a chain and a lifting plate which are arranged on the inner wall surface of the outer rotary drum, the chain is detachably connected to the inner wall surface of the outer rotary drum at the front section, and the lifting plate is arranged on the outer rotary drums at the middle section and the rear section. At the anterior segment of mummification rotary drum, the material is massive wet material, and being provided with of chain does benefit to and prevents the adhesion of wet material, has the effect of broken wet material simultaneously, and chain detachable connection is on outer rotary drum, and this dismouting change that has just realized the chain still is convenient for confirm the thickness of chain according to material nature, improves the commonality of mummification device. In addition, the chain is convenient for drive the wet material of bottom to the top, makes the material shed from the top, and then supplementary puddler carries out the mummification. And at the middle section and the back end of the drying rotary drum, wet materials form small blocks and surface-dried materials or granular materials which are not easy to bond, so that the materials are lifted to a high place by using the lifting plate to slide and shed, and the materials are convenient to crush and dry.

Preferably, the pitch between adjacent agitator bars increases from the inlet end to the outlet end. The puddler demonstrates from entrance point to the exit end by close to dredging the setting, and this material that is favorable to the anterior segment is smashed fast and is piled up backward, avoids wet material to pile up in a large number at the anterior segment, simultaneously along with the mummification of material, the reduction of volume, need increase dwell time at middle section and back end, reduces the translation speed.

Preferably, the stirring rod of the front section is of a semi-cylindrical structure, the plane of the stirring rod faces the inlet end side, and the semi-circular arc face faces the outlet end side. Such setting is favorable to impeling the material to remove to the exit end, guarantees that the material moves to the export direction as far as possible, reduces the probability that the material splashes to the import direction.

Preferably, the stirring rod is provided with a crushing piece, and the crushing piece is arranged as a crushing rod arranged perpendicular to the stirring rod. The contact area between the stirring rod and the wet material is favorably increased due to the arrangement of the crushing rod, the auxiliary stirring rod can conveniently crush the material into particles, and the specific surface area is rapidly changed, so that the drying efficiency is improved, the moisture evaporation is accelerated, and the temperature of hot smoke is rapidly reduced.

Preferably, a hot air guide plate is arranged on one side of the inner rotor close to the inlet end, the hot air guide plate is a circular plate, and a plurality of air guide holes arranged along the circle center of the circular plate in an annular array are arranged on the hot air guide plate; and a discharge wind shield is arranged on one side of the inner rotor close to the air outlet end, the discharge wind shield is a circular plate, and a gap K exists between the discharge wind shield and the inner wall surface. The hot air guide plate is used for guiding hot air, so that the hot air is more reasonably dispersed, heat is effectively transferred to the material at a higher speed, the drying efficiency is improved, meanwhile, the hot air can be quickly cooled in a very short time, and the condition that dioxin is not generated again is avoided, thereby being beneficial to environmental protection; the arrangement of the discharging wind shield is beneficial to avoiding inconvenience caused by the fact that dust in the drying drum is discharged along with hot air, and the arrangement of the distance H is convenient for the hot air to be concentrated at the gap between the discharging wind shield and the inner wall surface to be discharged, so that a drying product is brought out conveniently.

Preferably, the two ends of the outer rotating cylinder are provided with material blocking rings, the material blocking rings are arranged on the inner surface, a material selecting plate is arranged on the material blocking ring close to the outlet end, and the material selecting plate is fixed on the material blocking rings in a lifting mode. The setting of retaining ring is favorable to preventing that the material of not mummification from falling out from outer rotary drum, and the water content and the particle size of the drying product of highly being convenient for control through adjusting the select board.

Preferably, the secondary wind deflector is arranged in an annular structure, the inner diameter of the secondary wind deflector is larger than the diameter of the inner rotor, and a distance H generated by the diameter difference exists between the secondary wind deflector and the inner rotor. The second-level wind shield is of an annular structure, namely, the materials and the air flow only pass through the space H, so that small materials can be blocked, the granular materials can pass through the space along with hot air, and the drying quality is improved.

Preferably, a second-stage wind shield is arranged on the middle section of the outer rotating cylinder and comprises an inner ring and an outer ring, a plurality of connecting plates which are uniformly arranged are arranged between the inner ring and the outer ring, a vent is arranged between every two adjacent connecting plates, the connecting plates are of telescopic plate structures and comprise outer plates fixed on the outer ring and inner plates fixed on the outer plates in a telescopic mode, one ends of the inner plates are inserted into the outer plates, the other ends of the inner plates are arranged in arc-shaped sleeve sleeves sleeved outside the inner ring, the telescopic structures are arranged between the inner plates and the outer plates, the inner ring is arranged to be bent to form a circular elastic rod, one end of the elastic rod is provided with a slot, and the other end of the elastic rod is inserted into the slot to form a closed circular shape. The hot air flow passes through from the wind screen opening, because the connecting plate has reduced the area of passing through, the air current speed grow more is favorable to advancing the material, and the expansion plate controls the area of passing through of air current and then high limit air current speed through control inner ring diameter. Wherein extending structure control inner panel is flexible, and then makes elastic rod one end slide in the slot of the other end, and then takes place deformation for the size of inner ring changes, and connecting plate length change has still changed the diameter of blow vent simultaneously, further changes air velocity.

Therefore, the utility model discloses following beneficial effect has: the high-temperature hot flue gas is directly dried, so that the heat transfer efficiency is high and the drying effect is good; the specific surface area is fast to replace, and the drying efficiency is high; drying in a Brownian motion mode, and drying uniformly; the abrasion of equipment is reduced, and the service life of the equipment is prolonged; the mechanical energy consumption is reduced; the air flow speed is changed through the secondary wind shield, so that the air flow is changed, and the drying quality is improved.

Drawings

FIG. 1 is a schematic structural view of a sludge drying apparatus of the present invention;

FIG. 2 is a schematic representation of the construction of a drying drum;

FIG. 3 is a side view of the inlet end of the drying drum;

FIG. 4 is a side view of the exit end of the drying drum;

FIG. 5 is a schematic view of a first configuration of the desiccant drum at a secondary wind deflector;

FIG. 6 is a schematic view of a second configuration of the desiccant drum at a secondary wind deflector;

FIG. 7 is a cross-sectional view of the inner ring of FIG. 6;

in the figure: 1. the drying device comprises a frame 2, a drying rotary drum 201, an outer rotary drum 202, an inner rotor 3, a stirring rod 4, a crushing piece 5, an air inlet chamber 6, an air outlet chamber 7, a sealing device 8, a lifting plate 9, a feed inlet 10, a discharge outlet 11, an inlet end 12, an outlet end 13, a hot air guide plate 1301, an air guide hole 14, a discharge wind shield 15, a material selecting plate 16, a material blocking ring 17, an outer rotary motor 18, a gear 19, a retaining device 20, a retaining ring 21, a chain fixing plate 22, a chain 23, a secondary wind shield 24, a guide plate 25, an outer ring 26, an inner ring 2601, a first limiting convex edge 2602, a second limiting convex edge 2603, a slot 27, a connecting plate 2701, an inner plate 2702, an outer plate 28 and an air vent.

Detailed Description

The present invention will be further described with reference to the accompanying drawings and the detailed description.

Example 1:

in the embodiment 1 shown in fig. 1 and fig. 2, a sludge drying device comprises a drying drum 2, the drying drum 2 comprises an outer drum 201 arranged horizontally and an inner rotor 202 arranged in the outer drum 201, the outer drum 201 and the inner rotor 202 are in the same direction, a plurality of stirring rods 3 are arranged on the inner rotor 202, the stirring rods 3 are arranged in a double-helix shape, an auxiliary crushing structure is arranged on the inner wall surface of the outer rotary drum 201, the two ends of the drying rotary drum 2 are respectively provided with an inlet end 11 and an outlet end 12, the inlet end 11 is connected with an air inlet chamber 5 for connecting hot flue gas, the outlet end 12 is connected with an air outlet chamber 6 for discharging low-temperature hot flue gas, the bottom of the inlet end 11 is also provided with a feed inlet 9, the bottom of the outlet end 12 is provided with a discharge outlet 10, the drying rotary drum 2 is sequentially divided into a front section, a middle section and a rear section from the inlet end 11 to the outlet end 12, and the screw pitches between the stirring rods 3 are arranged from the inlet end 11 to the outlet end 12 from dense to sparse.

In the above technical solution, the drying drum 2 is used for drying wet materials, the wet materials enter the drying drum 2 from the inlet end 11 for drying, the wet materials gradually move to the outlet end 12 under the combined action of the co-rotation of the outer drum 201 and the inner rotor 202 and the hot flue gas, the stirring rod 3 and the auxiliary crushing structure are used for crushing the materials, that is, when the wet materials enter the drying drum 2, the outer drum 201 rotates to drive the wet materials at the bottom of the outer drum 201 to the top of the outer drum 201 and throw the wet materials downwards, the stirring rod 3 crushes large block materials into small block materials with wet surfaces, the small block materials in the supermarket are quickly dried after contacting the high-temperature hot air introduced into the air inlet chamber 5, the small block materials are crushed into granules again under the action of the stirring rod 3, and the materials under the action of the high-temperature air flow of the granular air inlet chamber 5 move to the outlet end 12, wherein the auxiliary crushing structure is used for assisting the outer drum to crush the wet materials 3 at the driving part of the wet materials to crush the wet material driving part to the auxiliary stirring rod 201 In the moving process, the dried particles can be bonded with the particles with high humidity, the particles are separated again after reaching a certain dryness and slowly move to the outlet and are finally discharged from the outlet end 12, a Brownian motion mode is formed, the uniform drying effect is achieved, and after the whole sludge is dried to a certain degree, when the water content of the sludge reaches 50% -55%, the material is in a fine boiling particle shape and is not in a bonding state, the problem of a sludge viscous area is effectively solved, the equipment abrasion is reduced, and the service life of the equipment is greatly prolonged. In addition, puddler 3 is that double helix form arranges the comminuted and the forward propulsion of being convenient for removes, improves mummification efficiency, and puddler 3 demonstrates from entrance point 11 to exit end 12 and is set up by closely getting loose, and this material that is favorable to the anterior segment is smashed fast and is piled up backward, avoids wet material to pile up in a large number at the anterior segment, simultaneously along with the mummification of material, the reduction of volume, need increase dwell time at middle section and back end, reduces the translation rate, improves the mummification quality. The air inlet chamber 5 is used for accessing and distributing hot flue gas, the upper limit of the inlet air temperature provided by the inlet end 11 of the air inlet chamber 5 is 600-700 ℃, and high-temperature air enters the rotor drier to contact with the crushed small blocky wet materials to quickly dry the wet materials, so that the drying effect is improved, and the tail gas treatment capacity is reduced; the temperature of the outlet of the drying rotary drum 22 is 150-200 ℃, the low-temperature hot flue gas is collected and discharged by the gas outlet chamber 6, and the low-temperature flue gas, the dried material and a very small amount of dust are settled and separated. In the whole drying process, the temperature of the sludge in the high-temperature gas is slowly raised in a Brownian motion mode, the temperature of the sludge is inconvenient to maintain at 60-80 ℃, the decomposition of organic matters is reduced, the generation of odor in the drying process is reduced, and the tail gas treatment cost is reduced.

Further, in the case where the auxiliary crushing structure includes the lifting plate 8 provided on the inner wall surface of the outer drum 201, the lifting plate 8 is provided in an arc-shaped structure. The lifting plate 8 is arranged to be beneficial to driving the material to the top from the bottom of the outer rotary drum 201 and throwing the material, so that the material is contacted with the stirring rod 3 and is crushed by the stirring rod 3, the contact area between the material and hot air is increased, and the drying of the material is facilitated.

Further, a crushing member 4 is provided on the stirring rod 3, and the crushing member 4 is provided as a crushing rod provided perpendicularly to the stirring rod 3. The crushing rod is arranged to increase the contact area between the stirring rod 3 and the wet material, so that the auxiliary stirring rod 3 can crush the material into particles, the specific surface area can be changed rapidly, the drying efficiency can be improved, the water evaporation can be accelerated, and the temperature of hot smoke can be reduced rapidly.

Further, be provided with second grade deep bead 23 on the middle section of outer rotary drum 201, the setting of second grade deep bead 23 is used for blockking hot air current, under the unchangeable condition of hot air current's flow, the area that changes the air current and then the speed of changing the air current, make the air current speed grow, be more favorable to impel the material, the material of middle section is the fritter material and the granular material of surface drying mostly, second grade deep bead 23 still seals hot-blast in the rotary drum in addition, form turbulent flow state under the effect of 2 internal component in mummification rotary drum and make the heat fully be used for the mummification material.

In addition, as shown in fig. 3 and 4, a hot air guide plate 2413 is arranged on one side of the inner rotor 202 close to the inlet end 11, the hot air guide plate 2413 is a circular plate, a plurality of air guide holes 1301 arranged along the circular center of the circular plate in an annular array are arranged on the hot air guide plate 2413, and the hot air guide plate 2413 is used for guiding hot air, so that the hot air is dispersed more reasonably, heat is effectively transferred to the material at a higher speed, the drying efficiency is improved, meanwhile, the hot air can be quickly cooled in a very short time, so that no condition for regenerating dioxin is generated, and the environment protection is facilitated; one side that interior rotor 202 is close to the gas outlet end is provided with ejection of compact deep bead 14, and ejection of compact deep bead 14 sets up to the plectane, has interval K between ejection of compact deep bead 14 and the internal face, and the setting of ejection of compact deep bead 14 does benefit to and avoids the dust in mummification rotary drum 2 along with hot-blast discharge, causes the inconvenience, and interval K's setting is convenient for concentrate hot-blast clearance department between ejection of compact deep bead 14 and the internal face and discharges, and then also is convenient for take the mummification product out.

Further, both ends of the outer rotating cylinder 201 are provided with material blocking rings 16, the material blocking rings 16 are arranged on the inner surface, a material selecting plate 15 is arranged on the material blocking ring 16 close to the outlet end 12, the material selecting plate 15 is fixed on the material blocking rings 16 in a lifting mode, and a space K exists between the material selecting plate and a discharging wind shield for facilitating discharging. The arrangement of the material blocking ring 16 is favorable for preventing the non-dried material from falling out of the outer rotary drum 201, and the water content and the particle size of the dried product can be conveniently controlled by adjusting the height of the material selecting plate 15.

In addition, the sludge drying device further comprises a frame 1, the frame 1 is used for supporting the whole drying device, a drying rotary drum 2 is horizontally arranged on the frame 1, sealing devices 7 are arranged at two ends of the drying rotary drum 2, namely the sealing devices 7 are arranged between the outer rotary drum 201 and the air inlet chamber 5, the sealing devices 7 are also arranged between the outer rotary drum 201 and the air outlet chamber 6, and the drying device which is effectively placed by the sealing devices 7 is polluted due to air leakage during operation. In addition, a gear 18 and a retainer ring 20 are further arranged outside the outer rotary drum 201, an outer rotary motor 17 and a retainer device 19 are arranged on the rack 1, the outer rotary motor 17 is connected with the gear 18 to provide power for rotation of the outer rotary drum 201 and drive the outer rotary drum 201 to rotate, the outer rotary drum 201 is connected with the retainer device 19 through the retainer ring 20, and the retainer device 19 is arranged to facilitate rotation of the outer rotary drum 201 and enable the outer rotary drum 201 to generate large transverse displacement during operation.

Example 2:

as shown in fig. 2, the embodiment 2 is basically the same as the embodiment 1, except that: the auxiliary crushing structure comprises a chain 22 and a lifting plate 8 which are arranged on the inner wall surface of the outer rotary drum 201, a chain fixing plate 21 is arranged on the front section of the inner wall surface of the outer rotary drum 201, the chain 22 is fixed on the chain fixing plate 21, and the lifting plate 8 is arranged on the outer rotary drum 201 on the middle section and the rear section. At the anterior segment of mummification rotary drum 2, the material is massive wet material, and being provided with of chain 22 does benefit to and prevents the adhesion of wet material, has the effect of broken wet material simultaneously, and chain 22 detachable connection is on outer rotary drum 201, and this dismouting change that has just realized chain 22 is convenient for still confirm the thickness of chain 22 according to material nature, improves the commonality of mummification device. In addition, the chain 22 is convenient for driving the wet material at the bottom to the top, so that the material is thrown from the top, and the drying of the stirring rod 3 is assisted. And at the middle section and the rear section of the drying rotary drum 2, wet materials form small blocks and surface-dried materials or granular materials which are not easy to bond, so that the materials are lifted to a high place by the lifting plate 8 to slide and shed, and the materials are convenient to crush and dry.

Example 3:

the embodiment 3 is basically the same as the embodiment 1, except that: the puddler 3 of anterior segment is half cylindrical structure, and the plane of puddler 3 is towards entrance point 11 one side, and the semicircle face is towards exit end 12 one side. Such an arrangement is beneficial to propelling the material to move towards the outlet end 12, ensures that the material moves towards the outlet direction as much as possible, and reduces the probability of splashing of the material towards the inlet direction.

Example 4:

as shown in fig. 5, the embodiment 4 is basically the same as the embodiment 1, except that: the secondary wind deflector 23 is arranged in an annular structure, the inner diameter of the secondary wind deflector 23 is larger than the diameter of the inner rotor 202, and a distance H generated by the diameter difference exists between the secondary wind deflector 23 and the inner rotor 202. The material and the air current only pass through from interval H, are favorable to blockking the fritter material, and make the granular material pass through along with hot-blast, have reached the selection by winnowing purpose of mummification material, and then make the moisture content and the particle diameter of mummification product more even, and the quality is better.

Further, a guide plate 24 is provided on the secondary wind deflector 23, and the guide plate 24 is used for guiding the hot air flow to flow out from the gap H.

Example 5:

as shown in fig. 6 and 7, the embodiment 5 is basically the same as the embodiment 4, except that: be equipped with second grade deep bead 23 on outer rotary drum 201's middle section, second grade deep bead 23 includes inner ring 26 and outer loop 25, be provided with a plurality of evenly arranged's connecting plate 27 between inner ring 26 and the outer loop 25, be provided with blow vent 28 between the adjacent connecting plate 27, connecting plate 27 sets up to the extending plate structure, connecting plate 27 is including fixing planking 2702 on outer loop 25 and the telescopic inner panel 2701 of fixing on planking 2702, the one end of inner panel 2701 is pegged graft in planking 2702, the other end of inner panel 2701 sets up to the arc sleeve pipe cover and establishes outside inner ring 26, be provided with extending structure between planking 2701 and planking 2702, inner ring 26 sets up to the circular elastic rod of crooked formation, elastic rod one end is equipped with slot 2603, the other end is pegged graft and is formed circularly in slot 2603. The hot air flow passes through the wind shielding opening, the passing area is reduced by the connecting plate 27, the air flow speed is increased, the material can be pushed, and the passing area of the air flow is controlled by the expansion plate through controlling the diameter of the inner ring 26, so that the air flow speed is high. Wherein the inner panel 2701 is flexible in the extending structure control, and then makes elastic rod one end slide in the slot 2603 of the other end, and then takes place deformation for the size of inner ring 26 changes, and connecting plate 27 length change has still changed the diameter of blow vent 28 simultaneously, further changes the air velocity.

Further, the end face of one end of the inner ring 26 inserted into the slot 2603 is provided with a first limiting convex edge 2601, the opening of the slot 2603 is provided with a second limiting convex edge 2602, and the arrangement of the first limiting convex edge 2601 and the second limiting convex edge 2602 prevents one end of the inner ring 26 from being disengaged from the slot 2603, which causes inconvenience.

Example 7:

the embodiment 7 is basically the same as the embodiment 1, except that: the inner rotor 202 is disposed obliquely, and the side of the inner rotor 202 near the inlet end 11 is higher than the side near the outlet end 12. The outer drum 201 is horizontally arranged, so that the sludge at the bottom of the outer drum 201 is prevented from flowing in the outer drum 201, the inner rotor 202 is obliquely arranged, and when the outer drum 201 and the inner rotor 202 rotate simultaneously, the sludge in the drying drum 2 is pushed from the inlet end 11 to the outlet end 12 along with the rotation of the inner rotor 202, so that the efficiency is improved, the air volume can be reduced, and the mechanical loss is reduced.

Example 8:

the embodiment 8 is basically the same as the embodiment 1, except that: the inner rotor 202 and the outer rotor eccentric shaft are arranged, namely the axes of the inner rotor 202 and the outer rotor are not coincident but parallel, the arrangement is convenient for reducing the required size of the stirring rod 3, and the requirement on the rigidity of the stirring rod 3 is lower, so that the manufacturing process of the stirring rod 3 is simplified, and the cost is reduced.

It should be noted that the technical solutions in the above embodiments can be freely combined, and the words "front", "back", "left", "right", "upper" and "lower" used in the above description refer to the directions in the drawings, and the words "inner" and "outer" refer to the directions toward or away from the geometric center of a specific component, respectively.

The above examples are only for illustrating the present invention and are not intended to limit the scope of the present invention. Various other modifications and changes may be made by those skilled in the art based on the above-described technical solutions and concepts, and all such modifications and changes are intended to fall within the scope of the claims.

Claims (10)

1. The sludge drying device comprises a drying rotary drum (2), wherein the drying rotary drum (2) comprises an outer rotary drum (201) and an inner rotor (202) which is arranged in the outer rotary drum (201) in a horizontal arrangement mode, two ends of the drying rotary drum (2) are respectively provided with an inlet end (11) and an outlet end (12), the inlet end (11) is connected with an air inlet chamber (5) used for accessing hot flue gas, and the outlet end (12) is connected with an air outlet chamber (6) used for discharging low-temperature hot flue gas; an auxiliary crushing structure is arranged on the inner wall surface of the outer rotating cylinder (201), and a secondary wind shield (23) is arranged on the middle section of the outer rotating cylinder (201).

2. The sludge drying device as claimed in claim 1, wherein the auxiliary crushing structure comprises a lifting plate (8) arranged on the inner wall surface of the outer rotating drum (201), and the lifting plate (8) is arranged in an arc structure.

3. The sludge drying device as claimed in claim 1, wherein the auxiliary crushing structure comprises a chain (22) and a lifting plate (8) arranged on the inner wall surface of the outer rotating cylinder (201), the chain (22) is detachably connected to the inner wall surface of the outer rotating cylinder (201) at the front section, and the lifting plate (8) is arranged on the outer rotating cylinder (201) at the middle section and the rear section.

4. A sludge drying apparatus according to claim 1, wherein the pitch between adjacent stirring rods (3) is gradually increased from the inlet end (11) to the outlet end (12).

5. The sludge drying device as claimed in claim 1, wherein the front stirring rod (3) is a semi-cylindrical structure, and the plane of the stirring rod (3) faces to the inlet end (11) side, and the semi-circular arc faces to the outlet end (12) side.

6. A sludge drying device according to claim 1, wherein the stirring rod (3) is provided with a crushing member (4), and the crushing member (4) is arranged as a crushing rod arranged perpendicular to the stirring rod (3).

7. The sludge drying device as claimed in any one of claims 1 to 6, wherein a hot air guide plate (13) is disposed on one side of the inner rotor (202) close to the inlet end (11), the hot air guide plate (13) is configured as a circular plate, and a plurality of air guide holes (1301) are disposed on the hot air guide plate (13) and arranged in an annular array along the circle center of the circular plate; a discharging wind shield (14) is arranged on one side, close to the air outlet end, of the inner rotor (202), the discharging wind shield (14) is a circular plate, and a distance H exists between the discharging wind shield (14) and the inner wall surface.

8. The sludge drying device as claimed in any one of claims 1 to 6, wherein material blocking rings (16) are arranged at both ends of the outer rotating cylinder (201), the material blocking rings (16) are arranged on the inner surface, a material selecting plate (15) is arranged on the material blocking ring (16) close to the outlet end (12), and the material selecting plate (15) is fixed on the material blocking rings (16) in a lifting manner.

9. The sludge drying device as claimed in any one of claims 1 to 6, wherein the secondary wind deflector (23) is configured as an annular structure, the inner diameter of the secondary wind deflector (23) is larger than the diameter of the inner rotor (202), and a distance H generated by the diameter difference exists between the secondary wind deflector (23) and the inner rotor (202).

10. The sludge drying device as claimed in any one of claims 1 to 6, wherein a secondary wind shield (23) is arranged on the middle section of the outer barrel (201), the secondary wind shield (23) comprises an inner ring (26) and an outer ring (25), a plurality of uniformly arranged connecting plates (27) are arranged between the inner ring (26) and the outer ring (25), a vent (28) is arranged between adjacent connecting plates (27), the connecting plates (27) are arranged to be telescopic plate structures, the connecting plates (27) comprise an outer plate (2702) fixed on the outer ring (25) and an inner plate (2701) telescopically fixed on the outer plate (2702), one end of the inner plate (2701) is inserted into the outer plate (2702), the other end of the inner plate (2701) is arranged to be an arc-shaped sleeve to be sleeved outside the inner ring (26), and a telescopic structure is arranged between the inner plate (2701) and the outer plate (2702), the inner ring (26) is an elastic rod which is bent to form a circle, one end of the elastic rod is provided with a slot (2603), and the other end of the elastic rod is inserted into the slot (2603) to form a closed circle.

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