CN215049589U - Drying and granulating device - Google Patents

Abstract

The utility model discloses a dry granulation device, dry granulation device includes the extruder, the extruder includes first shell and establishes the squeeze roll group in the first cavity of first shell, be equipped with first heat source import on the first shell, squeeze roll group includes a plurality of squeeze rolls of arranging along first horizontal direction, two adjacent squeeze rolls cooperation of squeeze roll group, wherein a plurality of at least a part of squeeze roll rotatably sets up, is equipped with a plurality of holding tanks on a plurality of the outer peripheral surfaces of at least a part of squeeze roll; and the dryer comprises a second shell and a first heating plate arranged in a second cavity of the second shell, and the second cavity is communicated with the first cavity. According to the utility model discloses dry prilling granulator has not produced the dust, non-staining environment, simple process, equipment investment low, running cost low grade advantage.

Description

Drying and granulating device

Technical Field

The utility model relates to a sludge treatment field specifically, relates to dry prilling granulator.

Background

Wastewater treatment produces large amounts of sludge. Currently, there are many ways of disposing of sludge, such as directly applying sludge to the ground, drying sludge, incinerating sludge, and the like. No matter what treatment method is adopted for the sludge, strict requirements are imposed on the water content of the sludge. For example, the sludge water content of mixed landfill sludge in municipal wastewater treatment plant (GBT23485-2009) is required to be less than 60%; sludge for landscaping in sludge treatment of urban sewage treatment plants (GBT23486-2009) requires that the water content of the sludge is less than 40 percent; sludge for separate incineration of sludge disposal in urban sewage treatment plants (GBT24602-2009) requires that the water content of sludge subjected to self-sustaining incineration is less than 50%, and the low-temperature heat value is greater than 5000 kJ/kg; the sludge for brick making by sludge treatment in urban sewage treatment plants (GBT23485-2009) requires that the water content of the sludge is less than 40 percent.

After the sludge is dehydrated and dried, the volume is greatly reduced, the residual substances of the dried sludge are relatively stable, the malodorous and pathogenic organisms are greatly removed, and the heat value and the nutrient content of the sludge are reserved. Therefore, it can be said that sludge drying is the prerequisite and key of sludge treatment and disposal technology.

However, the existing sludge drying technology generally has the defect of large dust amount, and the dried product is powdery, so that the utilization approach is limited.

SUMMERY OF THE UTILITY MODEL

The present invention aims at solving at least one of the technical problems in the related art to a certain extent. Therefore, the utility model provides a dry prilling granulator.

According to the utility model discloses a dry granulation device includes: the extrusion machine comprises a first outer shell and an extrusion roller group arranged in a first cavity of the first outer shell, wherein a first heat source inlet is formed in the first outer shell, the extrusion roller group comprises a plurality of extrusion rollers arranged along a first horizontal direction, two adjacent extrusion rollers of the extrusion roller group are matched, at least one part of the extrusion rollers is rotatably arranged, and a plurality of accommodating grooves are formed in the outer peripheral surface of at least one part of the extrusion rollers; and the dryer comprises a second shell and a first heating plate arranged in a second cavity of the second shell, the second cavity is communicated with the first cavity, and the dryer is positioned below the extruding machine.

According to the utility model discloses a dry prilling granulator has the advantage that does not produce the dust, non-staining environment, processing technology is simple, equipment investment is low, running cost is low.

Optionally, at least one of the squeezing rollers has a first heating cavity, and a rotary joint is arranged on the squeezing roller and is matched with the first heating cavity so as to provide a heat source into the first heating cavity.

Optionally, each of the squeeze rollers is rotatably disposed, and the accommodating groove is disposed on an outer circumferential surface of each of the squeeze rollers, wherein the rotation directions of each of the squeeze rollers are opposite, and a difference between rotation rates of two adjacent squeeze rollers of the squeeze roller set is greater than or equal to a first preset value, or the rotation directions of two adjacent squeeze rollers of the squeeze roller set are the same.

Optionally, the accommodating grooves are dovetail grooves, and the accommodating grooves of two adjacent squeeze rollers of the squeeze roller group are alternately arranged along the axial direction of the squeeze rollers.

Optionally, the width of the groove bottom of the accommodating groove is greater than the width of the notch of the accommodating groove, and the distance between the notches of the accommodating grooves of two adjacent pressing rollers of the pressing roller group in the axial direction of the pressing rollers is less than or equal to a second preset value.

Optionally, the plurality of the extrusion roller sets are arranged at intervals in the up-down direction, the extruder further includes a plurality of first flow field plates and a plurality of second flow field plates provided in the first chamber, each of the first flow field plates and each of the second flow field plates are arranged obliquely, the extrusion roller sets are located between the plurality of first flow field plates and the plurality of second flow field plates in the first horizontal direction, and the plurality of first flow field plates and the plurality of second flow field plates are arranged alternately in the up-down direction.

Optionally, the receiving groove extends along the entire circumference of the pressure roller, and the press further comprises a cleaning member, at least a portion of which protrudes into the receiving groove.

Optionally, the drying and granulating device further comprises a sludge buffer bin, the sludge buffer bin is provided with a storage cavity, the storage cavity is communicated with the first cavity, a stirring shaft is arranged in the storage cavity, and a plurality of rake blades are arranged on the stirring shaft.

Optionally, the first housing includes a plurality of sub-housings, the plurality of sub-housings are detachably connected in sequence, and the plurality of squeeze roller sets are disposed on the plurality of sub-housings in a one-to-one correspondence.

Optionally, a gas inlet communicated with the first chamber is arranged at the lower part of the first housing, and a gas outlet communicated with the first chamber is arranged at the upper part of the first housing.

Optionally, the dryer includes a plurality of first heating plates and a plurality of second heating plates, each first heating plate is annular, each second heating plate is annular, wherein a plurality of first heating plates and a plurality of second heating plates are arranged in an up-down direction in an alternating manner, each outer edge of the second heating plate is located at an outer side of each outer edge of the first heating plate, and each inner edge of the first heating plate is located at an inner side of each inner edge of the second heating plate.

Optionally, the dryer further comprises: a shaft passing through the plurality of first heating plates and the plurality of second heating plates in an up-down direction; a plurality of first mounting members and a plurality of second mounting members, which are alternately provided on the shaft in an up-down direction, wherein the plurality of first mounting members are located above the plurality of first heating plates in a one-to-one correspondence, and the plurality of second mounting members are located above the plurality of second heating plates in a one-to-one correspondence; the first toggle pieces are arranged on the first mounting pieces in a one-to-one corresponding mode, and each first toggle piece is in an outer spiral shape; and the second toggle pieces are arranged on the second mounting pieces in a one-to-one correspondence mode, and each second toggle piece is in an inner spiral shape.

Optionally, a lower edge of each of the first toggle pieces is adjacent to the upper surface of the corresponding first heating plate in the up-down direction, and a lower edge of each of the second toggle pieces is adjacent to the upper surface of the corresponding second heating plate in the up-down direction.

Optionally, each of the first heating plate and the second heating plate comprises: the tray body is provided with a second heating cavity, and the second heating cavity is provided with a steam inlet and a steam outlet; and a plurality of first partitions and a plurality of second partitions alternately and spacedly provided in the second heating chamber in a circumferential direction of the tray body, an outer end surface of each of the first partitions being connected to an outer circumferential wall surface of the second heating chamber, an inner end surface of each of the first partitions being spacedly provided in a radial direction of the tray body from the inner circumferential wall surface of the second heating chamber, an inner end surface of one of the second partitions being connected to the inner circumferential wall surface of the second heating chamber, an outer end surface of one of the second partitions being connected to the outer circumferential wall surface of the second heating chamber, remaining inner end surfaces of the second partitions being connected to the inner circumferential wall surface of the second heating chamber, remaining outer end surfaces of the second partitions being spacedly provided in the radial direction of the tray body from the outer circumferential wall surface of the second heating chamber, one of the second partition plates is located between the steam inlet and the steam outlet in a circumferential direction of the disk body.

Optionally, each of the first heating plate and the second heating plate comprises a plate body, the plate body comprises a plurality of sub plate bodies connected in sequence, each sub plate body is in a fan ring shape, each sub plate body is provided with a second heating cavity, and the second heating cavity is provided with a steam inlet and a steam outlet.

Optionally, a plurality of first partition plates and a plurality of second partition plates are arranged in each second heating cavity, the plurality of first partition plates and the plurality of second partition plates are alternately and separately arranged between the steam inlet and the steam outlet in the circumferential direction of the disc body, each second partition plate is located between two adjacent first partition plates in the circumferential direction of the disc body, wherein the outer end surface of each first partition plate is connected to the outer side wall surface of the second heating chamber, the inner end surface of each first partition plate is spaced apart from the inner side wall surface of the second heating chamber in the radial direction of the tray body, the inner end surface of each second partition plate is connected to the inner side wall surface of the second heating chamber, and the outer end surface of each second partition plate is spaced apart from the outer side wall surface of the second heating chamber in the radial direction of the tray body.

Drawings

Fig. 1 is a schematic structural diagram of a drying and granulating apparatus according to an embodiment of the present invention;

fig. 2 is a schematic structural diagram of a squeezing roller of a dry granulation device according to an embodiment of the present invention;

fig. 3 is a schematic structural diagram of a first heating plate (a second heating plate) of a dry granulation apparatus according to an embodiment of the present invention;

fig. 4 is a schematic structural diagram of a first heating plate (a second heating plate) of a dry granulation apparatus according to an embodiment of the present invention;

fig. 5 is a schematic structural diagram of a sub-tray body of a first heating tray (a second heating tray) of the drying and granulating device according to an embodiment of the present invention;

fig. 6 is a schematic structural diagram of a sludge drying system according to an embodiment of the present invention.

Detailed Description

Reference will now be made in detail to embodiments of the present invention, examples of which are illustrated in the accompanying drawings. The embodiments described below with reference to the drawings are exemplary and intended to be used for explaining the present invention, and should not be construed as limiting the present invention.

A dry granulation apparatus 100 according to an embodiment of the present invention is described below with reference to the drawings. As shown in fig. 1 to 5, a dry granulation apparatus 100 according to an embodiment of the present invention includes an extruder 1 and a dryer 2.

The extruder 1 comprises a first housing 11 and a set of extrusion rollers 12, the first housing 11 having a first chamber 111, the set of extrusion rollers 12 being provided in the first chamber 111. The first housing 11 is provided with a first heat source inlet so that a heat source is introduced into the first chamber 111 through the first heat source inlet. The squeeze roller group 12 includes a plurality of squeeze rollers 121 arranged in the first horizontal direction, and adjacent two squeeze rollers 121 of the squeeze roller group 12 are engaged. At least a part of the pressing rollers 121 is rotatably disposed, and a plurality of receiving grooves 1212 are formed on an outer circumferential surface 1211 of at least a part of the pressing rollers 121.

The dryer 2 includes a second housing 21 and a first heating plate 22, the second housing 21 having a second chamber 211, the second chamber 211 communicating with the first chamber 111. The first heating plate 22 is provided in the second chamber 211. A second heat source inlet is provided on the second housing 21 so that the heat source enters the first heating pan 22 through the second heat source inlet. The dryer 2 is located below the extruder 1.

A process of treating sludge using the dry granulation apparatus 100 according to an embodiment of the present invention will be described with reference to fig. 1 to 5.

The sludge entered into the first chamber 111 may fall between adjacent two squeeze rollers 121, and the adjacent two squeeze rollers 121 cooperate to squeeze the sludge into the plurality of receiving grooves 1212. The heat source entering into the first chamber 111 may dry the sludge in the holding tank 1212 so as to dry the sludge in the holding tank 1212 into sludge particles. Subsequently, the sludge particles come out of the holding tank 1212 and enter the first heating pan 22 in the second chamber 211. The first heating plate 22 heats the sludge particles to further dry the sludge particles, and finally, finished particles are obtained. The solid content of the finished product particles can reach 60-98%. That is, the ratio of the weight of solids in the finished granules to the weight of the finished granules is (0.6-0.98): 1, the ratio of the weight of water in the finished granules to the weight of the finished granules is (0.02-0.4): 1.

the sludge treatment method in the related technology is to firstly dry the sludge into powdery semi-finished products and then granulate the semi-finished products so as to realize the reutilization of the sludge. Therefore, the sludge treatment mode in the related technology has the defects of large dust amount, complex treatment process, high equipment investment and high operation cost.

According to the utility model discloses dry prilling granulator 100 is through setting up a plurality of holding tanks 1212 on the outer peripheral face 1211 of squeeze roller 121 to can become the fritter mud of packing in holding tank 1212 with mud separation, and dry this fritter mud so that obtain the mud granule. Therefore, according to the utility model discloses dry dehydration and granulation can be accomplished simultaneously to dry prilling granulator 100 to can obtain the finished product granule and need not to output pulverous mud.

Therefore, the drying and granulating device 100 according to the embodiment of the present invention has the advantages of no dust generation, no environmental pollution, simple treatment process, low equipment investment, low operation cost, etc.

The utility model also provides a sludge drying system 1000. As shown in fig. 1 to 6, a sludge drying system 1000 according to an embodiment of the present invention includes a sludge bin 800, an extruder 1, and a dryer 2.

The extruder 1 comprises a first housing 11 and a set of extrusion rollers 12, the first housing 11 having a first chamber 111, the set of extrusion rollers 12 being provided in the first chamber 111. The first chamber 111 is communicated with the discharge hole of the sludge bin 800, so that the sludge in the sludge bin 800 can enter the first chamber 111. The first housing 11 is provided with a first heat source inlet so that a heat source is introduced into the first chamber 111 through the first heat source inlet. The squeeze roller group 12 includes a plurality of squeeze rollers 121 arranged in the first horizontal direction, and adjacent two squeeze rollers 121 of the squeeze roller group 12 are engaged. At least a part of the pressing rollers 121 is rotatably disposed, and a plurality of receiving grooves 1212 are formed on an outer circumferential surface 1211 of at least a part of the pressing rollers 121.

The dryer 2 includes a second housing 21 and a first heating plate 22, the second housing 21 having a second chamber 211, the second chamber 211 communicating with the first chamber 111. The first heating plate 22 is provided in the second chamber 211. A second heat source inlet is provided on the second housing 21 so that the heat source enters the first heating pan 22 through the second heat source inlet.

Therefore, the sludge drying system 1000 according to the embodiment of the present invention has the advantages of no dust generation, no environmental pollution, simple treatment process, low equipment investment, low operation cost, etc.

As shown in fig. 1 to 6, the sludge drying system 1000 includes a sludge bin 800, a sludge pump 200, a sludge buffer bin 3, an extruder 1 and a dryer 2. The sludge drying system 1000 and the drying and granulating device 100 can be used for treating sludge with water content of about 80%.

For example, the sludge drying system 1000 and the drying and granulating apparatus 100 may be used to treat sludge having a water content of 85% or less. Optionally, the water content of the sludge is less than or equal to 80%. The particle size of the finished product particles is more than or equal to 6 mm and less than or equal to 8 mm. Optionally, the finished pellets have a moisture content of less than 40%.

The feed inlet of sludge pump 200 and the discharge gate intercommunication in sludge warehouse 800, the feed inlet of mud buffering storehouse 3 and the discharge gate intercommunication of sludge pump 200, the discharge gate and the first cavity 111 intercommunication in mud buffering storehouse 3.

The sludge buffer bin 3 is provided with a storage cavity 31, a stirring shaft 32 is arranged in the storage cavity 31, and a plurality of rake blades 33 are arranged on the stirring shaft 32. Therefore, the sludge in the storage cavity 31 can be stirred by the plurality of rake blades 33, so that the bridging phenomenon can be avoided, and the sludge can be favorably introduced into the first chamber 111. The holding cavity 31 is communicated with the first chamber 111 so that the sludge in the holding cavity 31 can enter the first chamber 111.

The extruder 1 comprises a first housing 11 and a plurality of extrusion roller sets 12, the first housing 11 having a first chamber 111, the extrusion roller sets 12 being provided in the first chamber 111.

As shown in fig. 1, the first housing 11 may alternatively include a plurality of sub-housings 112, the plurality of sub-housings 112 may be detachably connected in sequence, and the plurality of pressing roller groups 12 may be provided on the plurality of sub-housings 112 in a one-to-one correspondence. In other words, the number of the compression roller sets 12 may be equal to the number of the sub-housings 112, one compression roller set 12 per one sub-housing 112.

Thereby, the number of the sub-housings 112 and the compression roller group 12 can be flexibly selected according to the sludge treatment amount, and the increase and decrease of the compression roller group 12 can be realized by installing and detaching the sub-housings 112 so as to meet the sludge treatment amount. For example, the plurality of press roller groups 12 are provided on the opposite side plates of the plurality of sub-housings 112 in a one-to-one correspondence.

The first housing 11 is provided with a first heat source inlet so that a heat source is introduced into the first chamber 111 through the first heat source inlet. The heat source may directly heat the sludge in the holding tank 1212, or may indirectly heat the sludge in the holding tank 1212 by heating the squeeze roller 121. The heat source may be steam or heat transfer oil, etc.

At least one of the pressing rollers 121 has a first heating cavity 1213, and the pressing roller 121 is provided with a rotary joint (not shown in the drawings) which cooperates with the first heating cavity 1213 to provide a heat source into the first heating cavity 1213. That is, the heat source may enter the first heating cavity 1213 through the rotary joint. In particular, a first heat source delivery tube may be connected to the rotary joint through the first heat source inlet, and the heat source may pass through the first heat source delivery tube and the rotary joint in that order into the first heating chamber 1213.

The rotary joint may have an entry passage through which the heat source enters the first heating chamber 1213 and an exit passage through which the heat source, having completed the heat exchange, exits the first heating chamber 1213 within the first heating chamber 1213. Alternatively, the pressing roller 121 is provided with two rotary joints, the heat source enters the first heating cavity 1213 through one rotary joint, and the heat source which completes heat exchange in the first heating cavity 1213 exits the first heating cavity 1213 through the other rotary joint.

The squeeze roller group 12 includes a plurality of squeeze rollers 121 arranged in the first horizontal direction, and adjacent two squeeze rollers 121 of the squeeze roller group 12 are engaged. The first horizontal direction is indicated by arrow a in fig. 1, and the vertical direction is indicated by arrow B in fig. 1. Each of the pressing rollers 121 is rotatably provided, and an accommodating groove 1212 is provided on an outer circumferential surface 1211 of each of the pressing rollers 121.

Alternatively, the rotation direction of each of the pressing rollers 121 is opposite, and the difference in the rotation rates of two adjacent pressing rollers 121 of the pressing roller group 12 is greater than or equal to a first preset value. Alternatively, the rotation directions of the adjacent two press rolls 121 of the press roll group 12 are the same. Whereby adjacent two squeeze rolls 121 of the set of squeeze rolls 12 can be operated at a differential speed to create relative motion between the crossovers so that the sludge can be pulled into fluffy small pieces of sludge to make the sludge particles easier to form.

As shown in fig. 2, the receiving slots 1212 are dovetail slots. Therefore, the small sludge in the holding tank 1212 is not easy to fall off, so that the residence time of the small sludge on the squeeze roller 121 can be prolonged, the effective heating area of the squeeze roller 121 can be increased, and the volumes of the extruder 1 and the drying and granulating device 100 can be further reduced.

Optionally, the width of the groove bottom of the receiving groove 1212 is greater than the width of the notch of the receiving groove 1212. Thereby, the residence time of the small sludge on the squeeze roller 121 can be further prolonged, so that the effective heating area of the squeeze roller 121 is further increased, and the volumes of the extruder 1 and the drying and granulating device 100 are further reduced. The width of the groove bottom of the accommodation groove 1212 refers to the dimension of the groove bottom of the accommodation groove 1212 in the axial direction of the pressing roller 121, and the width of the notch of the accommodation groove 1212 refers to the dimension of the notch of the accommodation groove 1212 in the axial direction of the pressing roller 121.

As shown in fig. 2, the accommodating grooves 1212 of the adjacent two press rolls 121 of the press roll group 12 are alternately arranged in the axial direction of the press rolls 121, which is indicated by an arrow C in fig. 2. This can improve the sludge treatment capacity of the drying and granulating apparatus 100.

Alternatively, the distance of the notches of the receiving grooves 1212 of the adjacent two pressing rolls 121 of the pressing roll group 12 in the axial direction of the pressing rolls 121 is less than or equal to a second preset value. This can improve the sludge treatment capacity of the drying and granulating apparatus 100.

As shown in fig. 1, the accommodating groove 1212 extends along the entire circumferential direction of the pressing roller 121. The extruder 1 further comprises a cleaning member 14, at least a portion of the cleaning member 14 extending into the receiving groove 1212. From this not only can utilize clearance piece 14 to make this mud granule after being heated break away from holding tank 1212 to be favorable to this mud granule after being heated to break away from holding tank 1212, can utilize the remaining mud in clearance piece 14 clearance holding tank 1212 in addition, so as to be favorable to new fritter mud to enter into in the holding tank 1212.

As shown in fig. 1, the plurality of press roller sets 12 are provided, and the plurality of press roller sets 12 are provided at intervals in the vertical direction. The extruder 1 further includes a plurality of first flow field plates 131 and a plurality of second flow field plates 132 provided in the first chamber 111, each of the first flow field plates 131 and each of the second flow field plates 132 being obliquely arranged.

The squeeze roller group 12 is located between the plurality of first flow field plates 131 and the plurality of second flow field plates 132 in the first horizontal direction, and the plurality of first flow field plates 131 and the plurality of second flow field plates 132 are alternately arranged in the vertical direction. The flow direction of the hot gas from the dryer 2 can thereby be changed by means of the first and second flow field plates 131, 132, i.e. the hot gas is changed from a substantially vertical flow to a substantially horizontal flow by means of the first and second flow field plates 131, 132, in order to deflect the hot gas, so that the sludge particles in the holding tank 1212 can be heated by the hot gas by means of lateral flushing.

In order to make the technical solution of the present application easier to understand, the technical solution of the present application will be further described below by taking the first horizontal direction as an example of being consistent with the left-right direction. The left-right direction is indicated by an arrow D in fig. 1. The plurality of first flow path plates 131 may be positioned at the left side of the plurality of compression roller sets 12, and the plurality of second flow path plates 132 may be positioned at the right side of the plurality of compression roller sets 12. The hot gas from the dryer 2 flows from left to right after being blocked by the first flow path plate 131; the hot air from the dryer 2 flows from right to left after being blocked by the second flow field plate 132.

As shown in fig. 1, the lower portion of the first housing 11 is provided with a gas inlet 113 communicating with the first chamber 111, and the upper portion of the first housing 11 is provided with a gas outlet 114 communicating with the first chamber 111. Thereby, a drying gas (preferably a dry hot gas) can be fed into the first chamber 111 through the gas inlet 113, the drying gas can carry away the evaporated water vapor in the first chamber 111 and leave the first chamber 111 through the gas outlet 114, i.e. the drying gas and the water vapor in the first chamber 111 leave the first chamber 111 through the gas outlet 114, thereby increasing the drying speed of the sludge.

As shown in fig. 1, the dryer 2 includes a second housing 21 and a first heating plate 22, the second housing 21 having a second chamber 211, the second chamber 211 communicating with the first chamber 111. The first chamber 111 may be located above the second chamber 211 so that the sludge particles enter the second chamber 211 by their own weight.

The first heating plate 22 is provided in the second chamber 211. A second heat source inlet is provided on the second housing 21 so that the heat source enters the first heating pan 22 through the second heat source inlet. The heat source can thus heat the sludge granules on the first heating plate 22, so that the finished granules can be obtained. The heat source may be water vapor or heat transfer oil, etc.

As shown in fig. 1, the dryer 2 includes a plurality of first heating plates 22 and a plurality of second heating plates 23, each of the first heating plates 22 being annular, and each of the second heating plates 23 being annular. Wherein, a plurality of first heating plates 22 and a plurality of second heating plates 23 are arranged alternately in the vertical direction, the outer edge of each second heating plate 23 is positioned at the outer side of the outer edge of each first heating plate 22, and the inner edge of each first heating plate 22 is positioned at the inner side of the inner edge of each second heating plate 23. Thereby, the sludge particles can be heated by the first heating plates 22 and the second heating plates 23, and the solid content of the finished product particles can be further improved.

As shown in fig. 1, the dryer 2 further includes a shaft 24, a plurality of first mounting members 251, a plurality of second mounting members 252, a plurality of first toggle members 261, and a plurality of second toggle members 262. The shaft 24 passes through the plurality of first heating plates 22 and the plurality of second heating plates 23 in the up-down direction, that is, the plurality of first heating plates 22 and the plurality of second heating plates 23 are sleeved on the shaft 24.

The plurality of first mounting members 251 and the plurality of second mounting members 252 are alternately provided on the shaft 24 in the up-down direction. The first mounting members 251 are located above the first heating plates 22 in a one-to-one correspondence, and the second mounting members 252 are located above the second heating plates 23 in a one-to-one correspondence. That is, the number of the first mounting members 251 may be equal to the number of the first heating plate 22, the number of the second mounting members 252 may be equal to the number of the second heating plate 23, one first mounting member 251 is provided above each first heating plate 22, and one second mounting member 252 is provided above each second heating plate 23.

The first toggle pieces 261 are correspondingly arranged on the first mounting pieces 251, and each first toggle piece 261 is in an external spiral shape. In other words, the number of the first toggle pieces 261 may be equal to the number of the first mounting parts 251, and one first toggle piece 261 is provided on each first mounting part 251. The second toggle members 262 are correspondingly disposed on the second mounting members 252, and each of the second toggle members 262 has an inner spiral shape. That is, the number of the second toggle members 262 may be equal to the number of the second mounting members 252, and one second toggle member 262 is provided on each of the second mounting members 252.

Since each first toggle member 261 has an outer spiral shape, the first toggle member 261 can toggle the sludge particles on the first heating plate 22 outwards. Since the outer edge of each second heating pan 23 is located outside the outer edge of each first heating pan 22, the sludge particles moving outward can fall onto the second heating pan 23 after leaving the first heating pan 22.

Since each of the second toggle members 262 has an internal spiral shape, the second toggle members 262 can toggle the sludge particles on the second heating pan 23 inwards. Since the inner edge of each first heating pan 22 is located inside the inner edge of each second heating pan 23, the sludge particles moving inward can fall onto the first heating pan 22 after leaving the second heating pan 23. Thereby, the sludge particles can be heated by the first heating plates 22 and the second heating plates 23, and the finished product particles can be obtained.

As shown in fig. 1, a lower edge of each of the first toggle members 261 is adjacent to an upper surface of the corresponding first heating pan 22 in the up-down direction, so that the first toggle member 261 can more effectively toggle the sludge particles on the first heating pan 22. The lower edge of each second toggle member 262 is adjacent to the upper surface of the corresponding second heating pan 23 in the up-down direction so that the second toggle member 262 can more effectively toggle the sludge particles on the second heating pan 23.

As shown in fig. 3, each of the first heating plate 22 and the second heating plate 23 includes a plate body 221, a plurality of first partition plates 222, and a plurality of second partition plates 223. The tray body 221 has a second heating cavity 2211, and the second heating cavity 2211 has a steam inlet 2212 and a steam outlet 2213. Specifically, a second heat source delivery pipe may be connected to the steam inlet 2212 through the second heat source inlet, and the heat source enters the second heating cavity 2211 through the second heat source delivery pipe and the steam inlet 2212 in sequence. The heat source in the second heating cavity 2211 exchanges heat with the sludge particles on the first heating plate 22 and the second heating plate 23, and then leaves the second heating cavity 2211 through the steam outlet 2213.

The plurality of first partition plates 222 and the plurality of second partition plates 223 are alternately and spacedly provided in the second heating cavity 2211 along the circumferential direction of the tray body 221. In other words, the plurality of first partition plates 222 and the plurality of second partition plates 223 are alternately provided in the second heating cavity 2211 in the circumferential direction of the tray body 221, and the plurality of first partition plates 222 and the plurality of second partition plates 223 are provided in the second heating cavity 2211 at intervals in the circumferential direction of the tray body 221.

An outer end surface of each first partition plate 222 is connected to the outer circumferential wall surface of the second heating chamber 2211, and an inner end surface of each first partition plate 222 is spaced apart from the inner circumferential wall surface of the second heating chamber 2211 in the radial direction of the tray body 221. An inner end surface of one second partition plate 223 is connected to the inner circumferential wall surface of the second heating chamber 2211, an outer end surface of the one second partition plate 223 is connected to the outer circumferential wall surface of the second heating chamber 2211, and the one second partition plate 223 is located between the steam inlet 2212 and the steam outlet 2213 in the circumferential direction of the tray body 221. The one second partition plate 223 may thus be used to separate the steam inlet 2212 from the steam outlet 2213, thereby avoiding entry of heat from the steam inlet 2212 to the heat source to directly exit the second heating cavity 2211 through the steam outlet 2213.

Inner end faces of the remaining second partition plates 223 are connected to the inner circumferential wall face of the second heating chamber 2211, and outer end faces of the remaining second partition plates 223 are spaced apart from the outer circumferential wall face of the second heating chamber 2211 in the radial direction of the tray body 221. Thereby, a flow path of the heat source in the second heating cavity 2211 can be greatly extended, so that the heat of the heat source can be sufficiently utilized.

As shown in fig. 4 and 5, each of the first heating pan 22 and the second heating pan 23 includes a tray 221, and the tray 221 includes a plurality of sub-trays 225 connected in series, each sub-tray 225 having a fan-ring shape. Wherein each sub-disc 225 has a second heating cavity 2211, and the second heating cavity 2211 has a steam inlet 2212 and a steam outlet 2213. This can reduce the difficulty in manufacturing the first heating plate 22 and the second heating plate 23.

As shown in fig. 4 and 5, a plurality of first partition plates 222 and a plurality of second partition plates 223 are provided in each second heating cavity 2211. The plurality of first partition plates 222 and the plurality of second partition plates 223 are alternately and intermittently provided between the steam inlet 2212 and the steam outlet 2213 in the circumferential direction of the disc body 221. Each second partition plate 223 is located between adjacent two first partition plates 222 in the circumferential direction of the disc body 221.

An outer end surface of each first partition plate 222 is connected to an outer side wall surface of the second heating chamber 2211, and an inner end surface of each first partition plate 222 is spaced apart from an inner side wall surface of the second heating chamber 2211 in the radial direction of the tray body 221. An inner end surface of each second partition plate 223 is connected to an inner side wall surface of the second heating chamber 2211, and an outer end surface of each second partition plate 223 is spaced apart from an outer side wall surface of the second heating chamber 2211 in the radial direction of the tray body 221. The structure of the sub-disc 225 can be made more rational.

As shown in fig. 6, the sludge drying system 1000 further includes a dry material bin 300 and a lifting machine 400, wherein the lifting machine 400 is disposed between the discharge port of the dryer 2 and the feed port of the dry material bin 300. The elevator 400 can thus transfer the finished pellets discharged from the inlet of the dry bin 300 into the dry bin 300.

As shown in fig. 6, the second housing 21 is provided with an inert gas inlet communicating with the second chamber 211, and the first housing 11 is provided with an inert gas outlet communicating with the first chamber 111. The sludge drying system further comprises a blower 500, and an air outlet of the blower 500 is communicated with the inert gas inlet. The blower 500 may deliver the inert gas into the second chamber 211, and then the inert gas flows from the second chamber 211 into the first chamber 111 and exits the first chamber 111 from the inert gas outlet. Therefore, the inert gas can take away the evaporated water vapor in the first chamber 111 and the second chamber 211, so that the drying speed of the sludge and the sludge particles can be increased.

As shown in fig. 6, the sludge drying system 1000 further includes a cooling spray tower 600 and a gas-water separator 700. The gas inlet of the cooling spray tower 600 is communicated with the inert gas outlet, and the gas inlet of the gas-water separator 700 is communicated with the gas outlet of the cooling spray tower 600.

The inert gas discharged from the inert gas outlet of the extruder 1 enters the cooling spray tower 600 at the bottom thereof and is brought into counter-current contact with the cooling spray water at the upper portion thereof in the cooling spray tower 600. The inert gas is washed and cooled and then enters the gas-water separator 700, and water at the bottom of the cooling spray tower 600 is pumped by circulating water for water removal treatment. Inside the gas-water separator 700, the moisture carried in the inert gas is separated, and the separated water enters the water treatment system. The inert gas after passing through the gas-water separator 700 is led out by a draught fan. The inert gas led out by the draught fan can enter an incineration system and can also be discharged after being treated.

The utility model discloses still provide the utilization according to the utility model discloses the sludge drying treatment process that the sludge drying system 1000 of above-mentioned embodiment implemented. According to the utility model discloses sludge drying treatment process includes following step:

conveying the sludge in the sludge bin into an extruder 1;

simultaneously granulating and dewatering the sludge in an extruder 1 to obtain sludge granules; and

the sludge granules are dewatered to obtain finished granules.

The sludge drying treatment process provided by the embodiment of the utility model has the advantages of no dust generation, no environmental pollution, simple treatment process, low equipment investment, low operation cost and the like.

According to the utility model discloses sludge drying treatment process can be used for handling the mud of moisture content about 80%. For example, the sludge drying treatment process according to the embodiment of the invention can be used for treating sludge with water content less than or equal to 85%. Optionally, the water content of the sludge is less than or equal to 80%. The particle size of the finished product particles is more than or equal to 6 mm and less than or equal to 8 mm. Optionally, the finished pellets have a moisture content of less than 40%.

In the description of the present invention, it is to be understood that the terms "center", "longitudinal", "lateral", "length", "width", "thickness", "upper", "lower", "front", "rear", "left", "right", "vertical", "horizontal", "top", "bottom", "inner", "outer", "clockwise", "counterclockwise", "axial", "radial", "circumferential", and the like, indicate the orientation or positional relationship indicated based on the drawings, and are only for convenience of description and simplicity of description, and do not indicate or imply that the device or element referred to must have a particular orientation, be constructed and operated in a particular orientation, and therefore, should not be construed as limiting the present invention.

Furthermore, the terms "first", "second" and "first" are used for descriptive purposes only and are not to be construed as indicating or implying relative importance or implicitly indicating the number of technical features indicated. Thus, a feature defined as "first" or "second" may explicitly or implicitly include at least one such feature. In the description of the present invention, "a plurality" means at least two, e.g., two, three, etc., unless specifically limited otherwise.

In the present invention, unless otherwise expressly stated or limited, the terms "mounted," "connected," and "fixed" are to be construed broadly and may, for example, be fixedly connected, detachably connected, or integrally formed; may be mechanically coupled, may be electrically coupled or may be in communication with each other; they may be directly connected or indirectly connected through intervening media, or they may be connected internally or in any other suitable relationship, unless expressly stated otherwise. The specific meaning of the above terms in the present invention can be understood according to specific situations by those skilled in the art.

In the present application, unless expressly stated or limited otherwise, the first feature may be directly on or directly under the second feature or indirectly via intermediate members. Also, a first feature "on," "over," and "above" a second feature may be directly or diagonally above the second feature, or may simply indicate that the first feature is at a higher level than the second feature. A first feature being "under," "below," and "beneath" a second feature may be directly under or obliquely under the first feature, or may simply mean that the first feature is at a lesser elevation than the second feature.

In the present disclosure, the terms "one embodiment," "some embodiments," "an example," "a specific example," or "some examples" or the like mean that a particular feature, structure, material, or characteristic described in connection with the embodiment or example is included in at least one embodiment or example of the present disclosure. In this specification, the schematic representations of the terms used above are not necessarily intended to refer to the same embodiment or example. Furthermore, the particular features, structures, materials, or characteristics described may be combined in any suitable manner in any one or more embodiments or examples. Furthermore, various embodiments or examples and features of different embodiments or examples described in this specification can be combined and combined by one skilled in the art without contradiction.

Although embodiments of the present invention have been shown and described, it is understood that the above embodiments are exemplary and should not be construed as limiting the present invention, and that variations, modifications, substitutions and alterations can be made to the above embodiments by those of ordinary skill in the art without departing from the scope of the present invention.

Claims (16)

1. A dry granulation apparatus, comprising:

the extrusion machine comprises a first outer shell and an extrusion roller group arranged in a first cavity of the first outer shell, wherein a first heat source inlet is formed in the first outer shell, the extrusion roller group comprises a plurality of extrusion rollers arranged along a first horizontal direction, two adjacent extrusion rollers of the extrusion roller group are matched, at least one part of the extrusion rollers is rotatably arranged, and a plurality of accommodating grooves are formed in the outer peripheral surface of at least one part of the extrusion rollers; and

the desiccator, the desiccator includes the second shell and establishes first heating plate in the second cavity of second shell, the second cavity with first cavity intercommunication, the desiccator is located the below of extruder.

2. A dry granulation apparatus as claimed in claim 1, wherein at least one of said squeeze rollers has a first heating chamber, and a rotary joint is provided on said squeeze roller, said rotary joint cooperating with said first heating chamber to provide a heat source into said first heating chamber.

3. The dry granulation apparatus as claimed in claim 1, wherein each of said pressing rollers is rotatably provided, and said accommodating groove is provided on an outer circumferential surface of each of said pressing rollers,

wherein the rotation directions of the extrusion rollers are opposite, the difference value of the rotation speeds of two adjacent extrusion rollers of the extrusion roller group is larger than or equal to a first preset value,

alternatively, the rotation directions of two adjacent press rolls of the press roll group are the same.

4. A dry granulation apparatus according to claim 1, wherein said receiving grooves are dovetail grooves, and said receiving grooves of adjacent two of said squeeze rollers of said squeeze roller group are alternately arranged in an axial direction of said squeeze rollers.

5. The dry granulation device according to claim 4, wherein the width of the groove bottom of the accommodating groove is larger than the width of the notch of the accommodating groove, wherein the distance between the notches of the accommodating grooves of two adjacent pressing rollers of the pressing roller group in the axial direction of the pressing rollers is equal to or smaller than a second preset value.

6. The dry granulation apparatus as claimed in claim 1, wherein the plurality of the press roller groups are provided in plurality, and a plurality of the press roller groups are provided at intervals in an up-down direction, the press further comprises a plurality of first flow field plates and a plurality of second flow field plates provided in the first chamber, each of the first flow field plates and each of the second flow field plates being provided obliquely, wherein the press roller groups are located between the plurality of the first flow field plates and the plurality of the second flow field plates in the first horizontal direction, and the plurality of the first flow field plates and the plurality of the second flow field plates are alternately provided in the up-down direction.

7. A dry granulation apparatus as claimed in claim 1, wherein said containing groove extends along the entire circumference of said extrusion roller, said extrusion machine further comprising a cleaning member, at least a portion of said cleaning member extending into said containing groove.

8. The drying and granulating apparatus of claim 1, further comprising a sludge buffer bin having a storage chamber, the storage chamber being in communication with the first chamber, wherein a stirring shaft is disposed in the storage chamber, and a plurality of blades are disposed on the stirring shaft.

9. The dry granulation apparatus as claimed in claim 1, wherein the first housing comprises a plurality of sub-housings, the plurality of sub-housings are detachably connected in sequence, and the plurality of the squeeze roller groups are provided on the plurality of sub-housings in one-to-one correspondence.

10. A dry granulation apparatus as claimed in claim 1, wherein the lower part of said first housing is provided with a gas inlet communicating with said first chamber, and the upper part of said first housing is provided with a gas outlet communicating with said first chamber.

11. The dry granulation apparatus as claimed in claim 1, wherein the dryer comprises a plurality of the first heating plates and a plurality of the second heating plates, each of the first heating plates is annular, each of the second heating plates is annular, wherein the plurality of the first heating plates and the plurality of the second heating plates are alternately arranged in the vertical direction, an outer edge of each of the second heating plates is located outside an outer edge of each of the first heating plates, and an inner edge of each of the first heating plates is located inside an inner edge of each of the second heating plates.

12. The dry granulation apparatus of claim 11, wherein the dryer further comprises:

a shaft passing through the plurality of first heating plates and the plurality of second heating plates in an up-down direction;

a plurality of first mounting members and a plurality of second mounting members, which are alternately provided on the shaft in an up-down direction, wherein the plurality of first mounting members are located above the plurality of first heating plates in a one-to-one correspondence, and the plurality of second mounting members are located above the plurality of second heating plates in a one-to-one correspondence;

the first toggle pieces are arranged on the first mounting pieces in a one-to-one corresponding mode, and each first toggle piece is in an outer spiral shape; and

the second stirring pieces are arranged on the second mounting pieces in a one-to-one corresponding mode, and each second stirring piece is of an inner spiral shape.

13. The dry granulation apparatus of claim 12, wherein a lower edge of each of the first toggle members is vertically adjacent to an upper surface of the corresponding first heating pan, and a lower edge of each of the second toggle members is vertically adjacent to an upper surface of the corresponding second heating pan.

14. The dry granulation apparatus of claim 11, wherein each of the first heating pan and the second heating pan comprises:

the tray body is provided with a second heating cavity, and the second heating cavity is provided with a steam inlet and a steam outlet; and

a plurality of first partitions and a plurality of second partitions, the plurality of first partitions and the plurality of second partitions being alternately and spacedly provided in the second heating chamber in a circumferential direction of the tray body, an outer end surface of each of the first partitions being connected to an outer peripheral wall surface of the second heating chamber, an inner end surface of each of the first partitions being spacedly provided from the inner peripheral wall surface of the second heating chamber in a radial direction of the tray body, an inner end surface of one of the second partitions being connected to the inner peripheral wall surface of the second heating chamber, an outer end surface of one of the second partitions being connected to the outer peripheral wall surface of the second heating chamber, remaining inner end surfaces of the second partitions being connected to the inner peripheral wall surface of the second heating chamber, remaining outer end surfaces of the second partitions being spacedly provided from the outer peripheral wall surface of the second heating chamber in the radial direction of the tray body, one of the second partition plates is located between the steam inlet and the steam outlet in a circumferential direction of the disk body.

15. The dry granulation apparatus of claim 11, wherein each of said first heating pan and said second heating pan comprises a tray body comprising a plurality of sub-tray bodies connected in series, each of said sub-tray bodies being in the shape of a fan ring, wherein each of said sub-tray bodies has a second heating cavity having a steam inlet and a steam outlet.

16. A dry granulation apparatus as claimed in claim 15, wherein a plurality of first partition plates and a plurality of second partition plates are provided in each of said second heating chambers, the plurality of first partition plates and the plurality of second partition plates being alternately and spaced apart in the circumferential direction of said tray body between said steam inlet and said steam outlet, each of said second partition plates being located between two adjacent first partition plates in the circumferential direction of said tray body, wherein the outer end surface of each first partition plate is connected to the outer side wall surface of the second heating chamber, the inner end surface of each first partition plate is spaced apart from the inner side wall surface of the second heating chamber in the radial direction of the tray body, the inner end surface of each second partition plate is connected to the inner side wall surface of the second heating chamber, and the outer end surface of each second partition plate is spaced apart from the outer side wall surface of the second heating chamber in the radial direction of the tray body.

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