CN212657991U - Integral steam drum device and steam rotary dryer - Google Patents
Integral steam drum device and steam rotary dryer Download PDFInfo
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- CN212657991U CN212657991U CN202020505610.8U CN202020505610U CN212657991U CN 212657991 U CN212657991 U CN 212657991U CN 202020505610 U CN202020505610 U CN 202020505610U CN 212657991 U CN212657991 U CN 212657991U
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Abstract
The utility model relates to a whole steam pocket device for steam rotary dryer sets up at this steam rotary dryer's discharge end, contains: the steam chamber is communicated with the heat exchange device of the dryer, and the interior of the steam chamber is divided into a plurality of subareas by partition plates; the steam distribution device is respectively communicated with the steam pipeline of the dryer and the steam chamber; a lime set recovery unit, one end sets up in this steam chamber inside and has a plurality of lime set recovery mouths, the other end outwards extends and the lime set pipeline intercommunication of this desiccator, this lime set recovery unit and this subregion of this steam chamber are through this lime set recovery mouth intercommunication, when this steam chamber is rotatory along with this desiccator, lime set flows in this lime set recovery unit through this lime set recovery mouth under the action of gravity in at least this subregion. The utility model discloses still relate to a steam rotary dryer.
Description
Technical Field
The utility model relates to a desiccator technical field especially relates to a whole steam pocket device for steam rotary dryer to and contain the steam rotary dryer of this whole steam pocket device.
Background
In order to realize the urgent requirements of the pyrometallurgical industry on energy conservation and environmental protection, the high-temperature flue gas inevitably generated in the pyrometallurgical process is subjected to heat recovery, and the waste heat boiler becomes an effective means for recovering the heat contained in the waste heat boiler. As to how the high pressure steam generated by the waste heat boiler is utilized, power is currently generated from the high pressure steam in many smelting plants, however, another more economically feasible way is to apply the steam directly to the production of the plant in the form of heat energy. Therefore, the energy conversion link can be reduced, the energy utilization rate is improved, the storage and transportation of fuel are omitted, and the investment of power generation is avoided or reduced. Meanwhile, because fuel combustion is not needed, the generation of greenhouse gases and harmful gases is avoided, and the environment is protected.
In the above case, various steam rotary dryers are required to be used. However, the existing fixed steam rotary dryer has the defects of overheating at the bottom of a material bed, uneven heating and the like; the in-line tubular steam rotary dryer has the defects of easy wear of a heat exchange tube, inconvenient maintenance, small heat exchange area in the same ratio and the like; the split type steam rotary dryer with the circular pipe has the defects that the number of hoses in a steam drum is too large, the number of leakage points is too large, a rotary joint is easy to leak, and the like, and specifically, referring to fig. 8, the split type steam rotary dryer comprises 4 split type steam drum parts 1 ', each split type steam drum part 1 ' is communicated with the rotary joint 2 ' through a steam inlet hose 4 ' -1 and a water outlet hose 4 ' -2 respectively, and a fixing support 3 ' needs to be provided for fixing due to the fact that the split type steam drum parts 1 ', the steam inlet hoses 4 ' -1 and the water outlet hoses 4 ' -2 are large in number and complex in structure. When the steam boiler works, steam in the rotary joint 2 'is sent into the split steam drum part 1' through the steam inlet hose 4 '-1, and condensate obtained after heat exchange enters the rotary joint 2' from the split steam drum part 1 'through the water outlet hose 4' -2.
SUMMERY OF THE UTILITY MODEL
To above problem, the utility model aims to provide a whole steam pocket device, greatly reduced be used for the hose quantity and the contact point of connecting, simple structure, the leakage point is few. Another object of the utility model is to provide a steam rotary dryer has that heat transfer area is big, the heat exchange tube dismantles the advantage convenient, that the leakage point is few.
Therefore, the utility model provides an integral steam pocket device for steam rotary dryer sets up at this steam rotary dryer's discharge end, contains:
the steam chamber is communicated with the heat exchange device of the dryer, and the interior of the steam chamber is divided into a plurality of subareas by partition plates;
the steam distribution device is respectively communicated with the steam chamber and the steam pipeline of the dryer; and
a lime set recovery unit, one end sets up in this steam chamber inside and has a plurality of lime set recovery mouths, the other end outwards extends and the lime set pipeline intercommunication of this desiccator, this lime set recovery unit and this subregion of this steam chamber are through this lime set recovery mouth intercommunication, when this steam chamber is rotatory along with this desiccator, lime set flows in this lime set recovery unit through this lime set recovery mouth under the action of gravity in at least this subregion.
When the steam rotary dryer works, steam enters the steam distribution device through the steam pipeline, then enters the steam chamber and finally enters the heat exchange device of the dryer; the condensate generated in the heat exchange process enters the steam chamber through the heat exchange device of the dryer, then enters the condensate recovery device through the condensate recovery port, and finally enters the condensate pipeline of the dryer.
In one embodiment, the integrated steam drum device further comprises a casing arranged between the dryer cylinder and the steam chamber, wherein a quick-insertion pressure-bearing hose is arranged in the casing, and the quick-insertion pressure-bearing hose is communicated with the heat exchange device and the steam chamber.
In one embodiment, the shell is further provided with a plurality of access holes.
In one embodiment, the number of partitions is more than 3.
In one embodiment, the steam chamber is formed by a space between an inner circular pipe and an outer circular pipe, both ends of which are sealed, the radial section of the steam chamber is in a ring shape, one end of the partition board is fixed on the outer wall of the inner circular pipe, and the other end of the partition board is fixed on the inner wall of the outer circular pipe.
In one embodiment, the condensate recovery device is disposed in the inner circular tube and is connected to the inner wall of the inner circular tube in a sealing manner, and the condensate recovery device is a condensate recovery screw.
In one embodiment, the dryer has a feed end higher than a discharge end.
Therefore, the utility model also provides a steam rotary dryer contains:
a feed box having a material inlet and a carrier gas outlet or inlet;
the discharging box is provided with a material outlet and a carrier gas inlet or a carrier gas outlet correspondingly;
a cylinder body, the exterior of which is provided with a supporting part for rotary supporting, and the interior of which is provided with a heat exchange tube group;
the integral steam drum device and the feeding box are respectively communicated with two ends of the cylinder body, and one end of the cylinder body, which is close to the integral steam drum device, is also communicated with the discharging box; and
the rotary joint is provided with a steam pipeline and a condensate pipeline;
wherein, this whole steam drum device contains:
the steam chamber is communicated with the heat exchange tube group, and the interior of the steam chamber is divided into a plurality of subareas by partition plates;
the steam distribution device is respectively communicated with the steam chamber and the steam pipeline; and
a lime set recovery unit, one end sets up in this steam chamber inside and has a plurality of lime set recovery mouths, and the other end outwards extends and this lime set pipeline intercommunication, and this lime set recovery unit and this subregion of this steam chamber are through this lime set recovery mouth intercommunication, and when this steam chamber was rotatory along with this desiccator, lime set was in at least this subregion and was flowed into this lime set recovery unit through this lime set recovery mouth under the action of gravity.
In one embodiment, the integral steam drum device further comprises a shell arranged between the cylinder and the steam chamber, and a quick-insertion pressure-bearing hose is arranged in the shell and is communicated with the heat exchange tube set and the steam chamber.
When the steam rotary dryer works, steam enters the steam distribution device through the steam pipeline of the rotary joint, then enters the heat exchange tube set through the fast inserted pressure-bearing hose, condensate generated in the heat exchange process flows back to each subarea of the steam chamber through the fast inserted pressure-bearing hose, finally flows into the condensate recovery device through the condensate recovery port under the action of gravity, and is discharged through the condensate pipeline; the material enters the cylinder body through the material inlet of the feeding box, meanwhile, the carrier gas enters the cylinder body through the carrier gas inlet of the discharging box, after the material is in countercurrent contact with the carrier gas, the material is discharged through the material outlet of the discharging box, and the carrier gas is discharged through the carrier gas outlet of the feeding box.
In one embodiment, the shell is further provided with a plurality of access holes.
In one embodiment, the number of partitions is more than 3.
In one embodiment, one end of the partition board is fixed on the inner wall of the steam chamber, and the other end of the partition board is fixed on the condensate recovery device.
In one embodiment, the condensate recovery device is arranged at the axis of the steam chamber, and the condensate recovery device is a condensate recovery screw.
In an embodiment, the rotary joint is a sleeve having an inner pipeline and an outer pipeline which are coaxial, the inner pipeline and the outer pipeline are the condensate pipeline and the steam pipeline respectively, the inner pipeline is connected to a condensate outlet, and the outer pipeline is connected to a steam inlet.
In one embodiment, the end of the cylinder communicating with the feed box is inclined higher than the other end.
In one embodiment, the heat exchange tube set is an arc-shaped heat exchange tube set, the arc-shaped heat exchange tube set comprises a plurality of arc-shaped heat exchange tubes and a plurality of straight tubes, the arc-shaped heat exchange tubes are arranged in a concentric circle mode in the radial direction of the cylinder body and are parallel to each other in the axial direction of the cylinder body, a plurality of circles of the arc-shaped heat exchange tubes are arranged in the radial direction of the cylinder body, each circle of the arc-shaped heat exchange tubes is divided into a plurality of parts in the radial direction of the cylinder body, and each part is composed of two straight tubes axially penetrating through the cylinder. Correspondingly, the arc-shaped heat exchange tubes are provided with a plurality of groups in the axial direction of the cylinder body, and the number of the groups can be adjusted according to the length of the cylinder body.
In one embodiment, the arc-shaped heat exchange tube is provided with 3-9 circles in the radial direction of the cylinder, and each circle of the arc-shaped heat exchange tube is divided into 3-8 parts in the radial direction of the cylinder.
In one embodiment, the curved heat exchange tube and/or the straight tube are secured by a tube support secured to the inner wall of the barrel.
In one embodiment, the quick-connect pressure-bearing hose is in communication with the straight tube.
In one embodiment, the arc-shaped heat exchange tube is a light pipe made of stainless steel or carbon steel.
In one embodiment, a discharge sealing part is arranged at the joint of the discharge box and the cylinder body.
In one embodiment, the discharge sealing part is a fish scale type sealing element or a square and V-shaped combined packing type sealing element, and an adjustable spring is contained in the fish scale type sealing element.
In one embodiment, the support includes a fixed end support and a free end support, the fixed end support being driven by the drive train.
The utility model has the advantages as follows:
(1) compare with current split type steam pocket structure, the utility model discloses a this whole steam pocket device integrates into a holistic steam pocket with the components of a whole that can function independently steam pocket, greatly reduced with the quantity of the hose that steam distribution device is connected, correspondingly greatly reduced the leakage point.
(2) The utility model discloses a desiccator, heat exchange tube group are connected with the steam chamber through inserting the pressure-bearing hose soon, and are equipped with the access hole on the casing, consequently the utility model discloses a steam rotary dryer examines and repair convenience, heat exchange tube group and dismantles convenient and fast. When the heat exchange tube set is overhauled, an operator can rapidly detach the quick-insertion pressure-bearing hose through the access hole and draw out the whole arc-shaped heat exchange tube from the flange of the cylinder.
(3) The utility model discloses a desiccator adopts annular heat exchange tube, has the big advantage of heat transfer area.
Drawings
Fig. 1 is a front view of the steam rotary dryer of the present invention.
Fig. 2 is a radial sectional view of the steam rotary dryer of the present invention.
Fig. 3 is a partial enlarged view of the feed end of the steam rotary dryer of the present invention.
Fig. 4 is a partial enlarged view of the discharge end of the steam rotary dryer of the present invention.
Fig. 5 is a schematic structural diagram of the integral drum device of the steam rotary dryer of the present invention.
Fig. 6 is a cross-sectional view taken along line a-a of fig. 5.
Fig. 7 is a sectional view of the rotary joint of the steam rotary dryer of the present invention.
Fig. 8 is a schematic perspective view of a split drum part of a conventional loop split steam rotary dryer.
Reference numerals
Prior Art
Split steam manifold 1'
Swivel joint 2'
Fixed support 3'
Steam inlet hose 4' -1
Water outlet hose 4' -2
The utility model discloses
Material and carrier gas inlet 1-1
Discharging box 5
A material outlet 5-1 and a carrier gas outlet 5-2
Rotary joint 6
Inner pipeline 6-1 and outer pipeline 6-2
Free end support 7
Transmission system 8
Fixed end support 9
Arc-shaped heat exchange tube 10
Pipe support 11
Quick-insertion pressure-bearing hose 13
Integral drum unit 14
Casing 14-1, steam chamber 14-2, steam distribution device 14-3
Socket 17
Condensate recovery port 19-1
Sealing surface 24
Arc heat exchange tube set 27
Detailed Description
In order to make the objects, technical solutions and advantages of the present invention more clearly understood, the present invention is further described in detail below with reference to the accompanying drawings and embodiments. It should be understood that the specific embodiments described herein are merely illustrative of the invention and are not intended to limit the invention. The present invention may repeat reference numerals and/or letters in the various examples. This repetition is for the purpose of simplicity and clarity and does not in itself dictate a relationship between the various embodiments and/or configurations discussed.
Referring to fig. 1, the steam rotary dryer provided in this embodiment includes an integral drum device, and specifically, the dryer includes: the feeding box 1, the barrel 3, the discharging box 5, the integral steam pocket device 14 and the rotary joint 6, wherein the feeding box 1 is provided with a material inlet 1-1 and a carrier gas inlet 5-1, the discharging box 5 is provided with a material outlet 5-1 and a carrier gas outlet 5-2, the barrel 3 is externally provided with a supporting part for rotating and supporting, the supporting part comprises a free end supporting part 7 and a fixed end supporting part 9, the fixed end supporting part 9 is driven by a transmission system 8, the inside of the barrel 3 is provided with a heat exchange tube group, two ends of the barrel 3 are respectively communicated with the feeding box 1 and the integral steam pocket device 14, one end of the barrel 3 close to the integral steam pocket device 14 is also communicated with the discharging box 5, and the discharging box 5.
In the above embodiment, the flow direction of the carrier gas is the same as that of the material, and the carrier gas and the material are in concurrent contact; in other embodiments, the feed box has a material inlet and a carrier gas outlet, the discharge box has a material outlet 5-1 and a carrier gas inlet 5-2, and the carrier gas is in counter-current contact with the material in a direction opposite to the flow direction of the material.
In the above embodiment, the fixed end supporting part 9 has four independent bearing seats, two by two of which are respectively supported by a metal riding wheel, and two spacing catch wheel assemblies arranged in front and back; the free end supporting part 7 is provided with four independent bearing seats, and a group of two independent bearing seats respectively supports a metal riding wheel; the transmission system 8 consists of a main motor, a hydraulic coupler, a main reduction gearbox and a driving gear.
Referring to fig. 2, the heat exchange tube group in the cylinder 3 is an arc heat exchange tube group 27, the arc heat exchange tube group 27 includes a plurality of arc heat exchange tubes 10 and a plurality of straight tubes 20, the arc heat exchange tubes 10 are arranged in a concentric circle manner in the radial direction of the cylinder 3 and are parallel to each other in the axial direction of the cylinder 3, 7 circles of arc heat exchange tubes 10 are arranged in the radial direction of the cylinder 3, each circle of arc heat exchange tubes 10 is divided into 5 parts in the radial direction of the cylinder 3, and each part is composed of two straight tubes 20 axially penetrating through the cylinder 3 and an arc heat exchange tube 10 connected between the two straight tubes 20. One end of the straight pipe 20 close to the discharge box 5 is connected with the pipe seats 17 of each branch of the steam chamber 14-2 through the quick-insertion pressure-bearing hose 13, and the arc-shaped heat exchange pipe 10 is welded between the two straight pipes 20 in parallel; each group of arc heat exchange tube groups 27 is supported by a tube supporting piece 11 fixed on the wall of the cylinder, the positions, corresponding to the straight tubes 10, on the tube supporting piece 11 are all designed into semicircular grooves, and the straight tubes 10 are fixed in the grooves.
With reference to fig. 1 and fig. 3, a feeding sealing part 2 is disposed at a connection part of the feeding box 1 and the cylinder 3, the feeding sealing part 2 is a fish scale type sealing member, and the fish scale type sealing member contains an adjustable spring. Similarly, please refer to fig. 1 and fig. 4, a discharge sealing portion 4 is disposed at a connection portion between the discharge box 5 and the cylinder 3, and the discharge sealing portion 4 and the feeding sealing portion 2 have similar structures and are not described again. In some embodiments, the feeding sealing part 2 is a square and V-shaped combined packing type sealing element, and similarly, the discharging sealing part 4 has a similar structure to the feeding sealing part 2 and is not described again; in some embodiments, the feeding box 1 and the discharging box 5 are respectively and directly connected with the cylinder 3 in a sealing manner, and the feeding sealing part 2 and the discharging sealing part 4 are not required to be arranged; in other embodiments, the infeed and outfeed seals 2, 4 may be replaced with sealing strips. Of course, the structures of the feed seal 2 and the discharge seal 4 may also be completely different in the same embodiment.
With continued reference to fig. 1 and 4, the drum 3 is connected with an integral steam drum device 14 through a drum flange 12, the integral steam drum device 14 is provided with a steam chamber 14-2 and a steam distribution device 14-3 which are communicated with each other, the integral steam drum device 14 is further provided with a shell 14-1 arranged between the steam chamber 14-2 and the drum 3, a quick-insertion pressure-bearing hose 13 is arranged in the shell 14-1, one end of the quick-insertion pressure-bearing hose 13 is communicated with a pipe seat 17 of each branch on the steam chamber 14-2, and the other end is communicated with a heat exchange pipe group. The integral drum device 14 in this embodiment is provided with a housing 14-1 and a quick-insertion pressure-bearing hose 13; in some other embodiments, the heat exchange tube bank may communicate directly with the tube seat 17 on the vapor chamber 14-2; in still other embodiments, the heat exchange tube set may be connected to the tube seat 17 of the steam chamber 14-2 by a common hose; in still other embodiments, the integral steam drum device 14 is provided with a shell 14-1 and a fast-inserting pressure-bearing hose 13, and the shell 14-1 is further provided with 5 access ports 21, and the access ports 21 are matched with the fast-inserting pressure-bearing hose 13, so that the heat exchange tube set can be rapidly assembled and disassembled by an operator during maintenance.
With reference to fig. 4, 5 and 6, the steam chamber 14-2 is formed by a space between an inner circular tube and an outer circular tube which are coaxial and both ends of which are sealed, the radial section of the steam chamber 14-2 is circular, one end of the partition 15 is fixed on the outer wall of the inner circular tube, and the other end is fixed on the inner wall of the outer circular tube, so that the steam chamber 14-2 is divided into 5 partitions 16 by 5 partitions 15, a condensate recovery device 19 which is connected with the inner wall of the inner circular tube in a sealing manner is arranged in the inner circular tube, a plurality of condensate recovery ports 19-1 are arranged on the condensate recovery device 19, and a condensate recovery port 19-1 is arranged on the condensate recovery device 19 corresponding to each partition 16. In this embodiment, the condensate recovery device 19 is a condensate recovery screw, but the present invention is not limited thereto.
Referring to fig. 4 and 5, one end of the condensate recovery device 19 is disposed in the inner circular pipe of the steam chamber 14-2, and the other end of the condensate recovery device extends outward through the axis of the steam distribution device 14-3 and is connected to the condensate line of the rotary joint 6, the rotary joint 6 is a sleeve having an inner line 6-1 and an outer line 6-2 which are coaxial, the inner line 6-1 and the outer line 6-2 are the condensate line and the steam line, respectively, the inner line 6-1 is connected to a condensate outlet 26, and the outer line 6-2 is connected to a steam inlet 25. The inner pipeline 6-1 is communicated with the steam chamber 14-2 through a condensate recovery device 19, and the outer pipeline 6-2 is communicated with the steam distribution device 14-3 through a pipeline opening 18. In addition, a partition plate 28 is arranged between the pipeline opening 18 and the condensate recovery device 19, one end of the partition plate 28 is connected with the inner wall of the outer pipeline 6-2, and the other end is connected with the outer wall of the inner pipeline 6-1, so that the outer pipeline 6-2 is separated from the inner pipeline 6-1.
As can be seen from the above, one end of the condensate recovery device 19 is communicated with each partition 16 through the condensate recovery port 19-1, and the other end is communicated with the inner pipeline 6-1 of the rotary joint 6, when the steam chamber 14-2 rotates along with the cylinder 3, the highest point of condensate in at least one partition 16 is higher than the condensate recovery port 19-1, and under the action of gravity, the condensate flows into the condensate recovery device 19 through the condensate recovery port 19-1 and then enters the inner pipeline 6-1 of the rotary joint 6, and finally is discharged through the condensate outlet 26.
In the embodiment, when the steam rotary dryer is applied, the flow rate of a steam inlet is preferably 10-20 m/s, the temperature of a heat exchange tube is preferably 110-280 ℃, the flow rate of a carrier gas in the cylinder 3 is preferably 1-3 m/s, the material handling capacity is preferably 30-400 t/h, the rotation speed of the cylinder 3 is preferably 0.5-4 rpm, one end of the cylinder 3, which is communicated with the feeding box 1, is higher than the other end of the cylinder and is obliquely arranged, and the inclination of the cylinder is preferably 1: 100-9: 100. Of course, in other embodiments, when the steam rotary dryer is used, it may be further preferable that: the flow rate of a steam inlet is 15m/s, the temperature of the heat exchange tube is 150-180 ℃, the flow rate of carrier gas in the cylinder 3 is 1.5-2 m/s, the material handling capacity is 50-150 t/h, and the inclination of the cylinder is 1: 100-4: 100.
When the steam rotary dryer provided by the embodiment works, steam enters the steam distribution device 14-3 and the steam chamber 14-2 from the outer pipeline 6-2 of the rotary joint 6, then enters the heat exchange tube group through the fast-insertion pressure-bearing hose 13 to provide heat required by material drying, and during heat exchange, condensate formed in the arc-shaped heat exchange tubes 10 flows from the higher end to the lower end due to the inclination of the dryer, flows back to each subarea 16 of the steam chamber 14-2 through the fast-insertion pressure-bearing hose 13, finally flows into the condensate recovery device 19 through the condensate recovery port 19-1 under the action of gravity, and is discharged through the condensate outlet 26 of the inner pipeline 6-1; the material and the carrier gas enter the cylinder 3 through the carrier gas and the material inlet 1-1 of the feeding box 1, the carrier gas carries the material to be lifted and sprayed by the arc-shaped heat exchange tube 10 along with the rotation of the cylinder 3, the material is dried by utilizing various heat exchange modes such as convection, conduction and radiation, namely the material is dehydrated under the dual actions of the carrier gas and the heat exchange tube group, and is moved from the higher end to the lower end by virtue of the inclination of the dryer, and finally is discharged from the material outlet 5-1 of the discharging box 5, and meanwhile, the carrier gas is discharged through the carrier gas outlet 1-2 of the feeding box 1 under the action of the fan.
When the steam rotary dryer provided by the embodiment is overhauled, an operator can rapidly remove the quick-insertion pressure-bearing hose 13 through the overhauling port 21 arranged on the shell 14-1 and draw out the whole arc-shaped heat exchange tube 10 from the barrel flange 12 at the front end of the barrel 3.
Referring to fig. 7, the embodiment is different from the above embodiment in that the rotary joint 6 has an inner tube 23, the inner tube 23 is a condensate line, two joints between 3 rings 22 are sleeved on the outer periphery of the inner tube 23, the 3 rings 22 are connected by a sealing member to form a steam inlet and a condensate outlet, three sealing surfaces 24 are formed between the sealing member and the rings 22, and a gas film or a liquid film formed between the sealing surfaces 24 is used for sealing. The ring 22 is made of cemented carbide, and the sealing member is made of graphite.
In some embodiments, the curved heat exchange tube 10 is a light pipe made of stainless steel. Of course, in other embodiments, the heat exchange pipe 10 may also be a light pipe made of carbon steel.
It should be noted that the above-mentioned preferred embodiments are only used for illustrating the present invention, but the present invention is not limited to the above-mentioned embodiments, and the variations and modifications made by those skilled in the art within the scope of the present invention are all within the protection scope of the present invention.
Claims (17)
1. The utility model provides an integral steam drum device for steam rotary dryer sets up the discharge end at this steam rotary dryer, its characterized in that contains:
the steam chamber is communicated with the heat exchange device in the dryer, and the interior of the steam chamber is divided into a plurality of subareas by partition plates;
the steam distribution device is respectively communicated with the steam chamber and the steam pipeline of the dryer; and
a lime set recovery unit, one end sets up in this steam chamber inside and has a plurality of lime set recovery mouths, and the other end outwards extends and the lime set pipeline intercommunication of this desiccator, and this lime set recovery unit and this subregion of this steam chamber are through this lime set recovery mouth intercommunication, and when this steam chamber was rotatory along with this desiccator, lime set flowed into this lime set recovery unit through this lime set recovery mouth under the action of gravity in at least this subregion.
2. The integrated steam drum device according to claim 1, further comprising a housing disposed between the dryer cylinder and the steam chamber, wherein a quick-insertion pressure-bearing hose is disposed in the housing, and the quick-insertion pressure-bearing hose communicates the heat exchange device and the steam chamber.
3. The integrated drum device according to claim 2, wherein the housing is further provided with a plurality of access ports.
4. The integrated drum device according to claim 1, wherein the number of partitions is more than 3.
5. The integrated drum device according to claim 1, wherein the steam chamber is formed by a space between an inner circular tube and an outer circular tube sealed at both ends, the radial section of the steam chamber has a circular ring shape, and the partition plate has one end fixed to an outer wall of the inner circular tube and the other end fixed to an inner wall of the outer circular tube.
6. The integrated steam drum device according to claim 5, wherein the condensate recovery device is disposed in the inner circular pipe and is connected with the inner wall of the inner circular pipe in a sealing manner, and the condensate recovery device is a condensate recovery screw.
7. The integrated drum installation according to claim 1, wherein the feed end of the dryer is higher than the discharge end.
8. A steam rotary dryer, comprising:
a feed box having a material inlet and a carrier gas outlet or inlet;
the discharging box is provided with a material outlet and a carrier gas inlet or a carrier gas outlet correspondingly;
a cylinder body, the exterior of which is provided with a supporting part for rotary supporting, and the interior of which is provided with a heat exchange tube group;
the integral steam drum device and the feeding box are respectively communicated with two ends of the cylinder body, and one end of the cylinder body, which is close to the integral steam drum device, is also communicated with the discharging box; and
the rotary joint is provided with a steam pipeline and a condensate pipeline;
wherein, this whole steam drum device contains:
the steam chamber is communicated with the heat exchange tube group, and the interior of the steam chamber is divided into a plurality of subareas by partition plates;
the steam distribution device is respectively communicated with the steam chamber and the steam pipeline; and
a lime set recovery unit, one end sets up in this steam chamber inside and has a plurality of lime set recovery mouths, and the other end outwards extends and this lime set pipeline intercommunication, and this lime set recovery unit and this subregion of this steam chamber are through this lime set recovery mouth intercommunication, and when this steam chamber was rotatory along with this desiccator, lime set was in at least this subregion and was flowed into this lime set recovery unit through this lime set recovery mouth under the action of gravity.
9. The steam rotary dryer of claim 8, wherein the rotary joint is a sleeve having an inner and an outer pipe which are coaxial, the inner and the outer pipe being the condensate and the steam respectively, the inner pipe being connected to a condensate outlet, the outer pipe being connected to a steam inlet.
10. The steam rotary dryer according to claim 8, wherein the heat exchange tube group is an arc heat exchange tube group comprising a plurality of arc heat exchange tubes arranged in a concentric circle in a radial direction of the drum and parallel to each other in an axial direction of the drum and a plurality of straight tubes, the arc heat exchange tubes being provided in a plurality of turns in the radial direction of the drum, each turn of the arc heat exchange tubes being divided into a plurality of portions in the radial direction of the drum, each portion being composed of two straight tubes axially penetrating the drum and an arc heat exchange tube connected between the two straight tubes.
11. The steam rotary dryer according to claim 10, wherein the curved heat exchange tube is provided with 3 to 9 turns in a radial direction of the drum, and each turn of the curved heat exchange tube is divided into 3 to 8 parts in the radial direction of the drum.
12. The steam rotary dryer of claim 10, wherein the arcuate heat exchange tube set is secured by a tube support member secured to an inner wall of the drum.
13. The steam rotary dryer of claim 10, wherein the straight pipe communicates with a fast spigot pressure-bearing hose disposed within the integral drum unit.
14. The steam rotary dryer of claim 10, wherein the arcuate heat exchange tubes are light pipes of stainless steel or carbon steel.
15. The steam rotary dryer of claim 8, wherein the junction of the discharge box and the drum is provided with a discharge seal, and the junction of the feed box and the drum is provided with a feed seal.
16. The steam rotary dryer of claim 15, wherein the discharge sealing part is a fish scale type sealing part or a square plus V type combined packing type sealing part, the feed sealing part is a fish scale type sealing part or a square plus V type combined packing type sealing part, and the fish scale type sealing part contains an adjustable spring.
17. The steam rotary dryer of claim 8, wherein the support includes a fixed end support and a free end support, the fixed end support being driven by a drive system.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202020505610.8U CN212657991U (en) | 2020-04-08 | 2020-04-08 | Integral steam drum device and steam rotary dryer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202020505610.8U CN212657991U (en) | 2020-04-08 | 2020-04-08 | Integral steam drum device and steam rotary dryer |
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| CN212657991U true CN212657991U (en) | 2021-03-05 |
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| CN202020505610.8U Active CN212657991U (en) | 2020-04-08 | 2020-04-08 | Integral steam drum device and steam rotary dryer |
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2020
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