CN205838848U - Powder lime suspension calcining production line - Google Patents
Powder lime suspension calcining production line Download PDFInfo
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- CN205838848U CN205838848U CN201620532920.2U CN201620532920U CN205838848U CN 205838848 U CN205838848 U CN 205838848U CN 201620532920 U CN201620532920 U CN 201620532920U CN 205838848 U CN205838848 U CN 205838848U
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P40/00—Technologies relating to the processing of minerals
- Y02P40/40—Production or processing of lime, e.g. limestone regeneration of lime in pulp and sugar mills
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Abstract
This utility model relates to a kind of powder lime suspension calcining production line, and it includes that rubble lime stone stores device, agstone preparation facilities, drawing-in device, suspension calcining chiller, fuel supply system, sieve material device, finished product storage device, emission-control equipment.Suspension calcining chiller includes heating bucket, dore furnace and the cooling bucket of three grades of Pyatyi, respectively heating send the inverted U-shaped airduct connection at pipe, whirlwind return pipe, material pipe and dore furnace top to form air channel by whirlwind between bucket, dore furnace, cooling bucket, utilize the fuel gas supply end of this air channel connecting fan and fuel supply system, thus in dore furnace, form suspension calcining, the temperature of suspension calcining is 850～1000 DEG C, calcination time is 10 seconds in, finally by the material pipe discharging of final stage cooling bucket, after sieve material device sieve material, obtain finished powder Calx.This utility model whole production process is closed, more environmental protection, improves the heat utilization efficiency of suspension calcining, thus ensures production efficiency and the quality of production.
Description
Technical field
This utility model relates to lime generation equipment, is a kind of powder lime suspension calcining production line.
Background technology
Traditional pulverized limestone mode of production is mostly by oarse-grained limestone block is carried out calcination reaction, then by bulk
Calx break into pieces after obtain pulverized limestone.It is inefficient that this mode not only produces Calx, and calcination reaction cannot ensure block Calx
The abundant decomposition of stone, the problem that often there is burning or underburnt, cause final pulverized limestone yield the highest, quality defect.Except this
In addition, traditional lime production, not only efficiency is low, and heat utilization is low, and there is substantial amounts of dust and waste residue, easily causes environment dirty
Dye.In order to solve these problems, prior art discloses some and has used suspension calcining technique to prepare powder lime, and i.e. limestone is first
Carry out pulverizing and form agstone, enter back into suspension calcining equipment and carry out suspension calcining and prepare powder lime, life is not only greatly improved
Produce efficiency, and heat utilization efficiency is high, reduces energy consumption, the problem improving environmental pollution.But existing suspension calcining equipment is at fuel
Still suffering from problem to aspect altogether, mainly fuel is not fully combined with air, abundant before causing burning, thus causes suspension calcining
Equipment overall thermal utilizes and service behaviour is not good enough.To this end, need existing equipment is improved.
Summary of the invention
For overcoming above-mentioned deficiency, a kind of powder lime suspension calcining production line of this utility model design so that it is solve existing same
Class powder lime produces production efficiency of equipment and the technical problem of quality defect.It adopts the following technical scheme that realization.
This powder lime suspension calcining production line includes suspension calcining chiller, fuel supply system, sieve material device, sieve material
Device is arranged at the discharge end of suspension calcining chiller, and fuel supply system includes coal dust supply side and fuel gas supply end；Its
Being characterised by that described suspension calcining chiller includes regenerator section, calcining part, cooling segment, regenerator section includes that one-level adds
Heat bucket, two grades of heating buckets, three grades of heating buckets, level Four heating bucket, Pyatyi heating buckets, calcining part is dore furnace, cooling end subpackage
Including one-level cooling bucket, two grades of cooling buckets, three grades of cooling buckets, the top of each heating bucket and cooling bucket is all connected with whirlwind and send pipe, respectively adds
The side of heat bucket and cooling bucket is all connected with whirlwind return pipe, and the bottom of each heating bucket and cooling bucket is all connected with material pipe, and described two grades add
The whirlwind of heat bucket send pipe as the feed end of suspension calcining chiller, and is connected to the whirlwind return pipe of described one-level heating bucket,
The whirlwind of one-level heating bucket send pipe to be connected to institute as the exhaust end of described suspension calcining chiller, the material pipe of one-level heating bucket
The whirlwind of the whirlwind return pipe and three grades of heating buckets of stating two grades of heating buckets send pipe, and the material pipe of two grades of heating buckets is connected to described three grades and adds
The whirlwind return pipe of heat bucket and the whirlwind of level Four heating bucket send pipe, and the material pipe of three grades of heating buckets is connected to the whirlwind of level Four heating bucket and returns
The whirlwind of pipe and Pyatyi heating bucket send pipe, the material pipe of level Four heating bucket to be connected in described dore furnace, and dore furnace top is by U
Shape airduct is connected with the whirlwind return pipe of described Pyatyi heating bucket, and the whirlwind connecting described one-level cooling bucket bottom dore furnace send pipe,
The material pipe of described Pyatyi heating bucket is connected to the whirlwind of described two grades of cooling buckets and send pipe and the whirlwind return pipe of one-level cooling bucket, one-level
The material pipe of cooling bucket is connected to the whirlwind of described three grades of cooling buckets and send pipe and the whirlwind return pipe of two grades of cooling buckets, two grades of cooling buckets
Material pipe is connected to the whirlwind return pipe of three grades of cooling buckets, and the whirlwind return pipe of three grades of cooling buckets is connected to blower fan discharge pipe and sieve material device
The first feed end, three grades cooling bucket material pipes be connected to described sieve material device the second feed end；Described fuel supply system
Coal dust supply side be connected directly in described dore furnace, described fuel gas supply end branch is connected to the rotation of described one-level cooling bucket
Wind return pipe, the whirlwind return pipe of described three grades of cooling buckets and described dore furnace.By said structure, the heating bucket of Pyatyi is utilized to realize
Preheating, thus improve heat utilization efficiency, the fuel gas supply end simultaneously supplying it to device passes to, in the pipeline that cooling struggles against, borrow in advance
Help air current flow to be sufficiently mixed, thus ensure that combustion gas can fully be burnt in entering dore furnace, improve the thermal efficiency and Calx
Stone powder decomposition efficiency, it is achieved energy-saving and emission-reduction.
In said structure, the whirlwind connected send pipe and whirlwind return pipe to be integral type pipe, facilitates structure processing and connects.Described
One-level heating bucket is double column structure, and i.e. two one-level heating buckets are set up in parallel.Double column structure is conducive to the most pre-to agstone
Heat.
This powder lime suspension calcining production line also includes rubble lime stone storage device, agstone preparation facilities, feeding dress
Put, finished product storage device, emission-control equipment, rubble lime stone storage device discharge end be connected to agstone preparation facilities
Feed end, the discharge end of agstone preparation facilities connects the feed end of drawing-in device, going out of drawing-in device by conveying mechanism
Material end is connected to the feed end of described suspension calcining chiller, and the discharge end of described sieve material device connects described finished product storing dress
Putting, described suspension calcining chiller, the respective exhaust end of agstone preparation facilities are connected to give up by the pipeline of band blower fan
The air inlet of Flash Gas Compression Skid System, the air vent of emission-control equipment is connected to exhaust chimney by the pipeline of band blower fan.By this
Structure, to realize the production in enormous quantities of powder lime, effectively controls waste gas discharge simultaneously, reduces environmental pollution, it is achieved environmental protection is raw
Produce.
Between exhaust end and the air inlet of described emission-control equipment of described suspension calcining chiller, powder mistake is set
Filter collection device.By this powder device for filtering and collecting, reduce while polluting, be conducive to suspension calcining chiller aerofluxus
The agstone reclaiming that end is discharged is produced, and reduces the wasting of resources, fully improves yield.
The pipeline of fans branch that the exhaust end of described suspension calcining chiller is connected is connected to described agstone system
The air inlet of standby device.Same, the agstone that beneficially suspension calcining chiller exhaust end is discharged is recycled to limestone
Powder preparation facilities reproduction.
This utility model changes the production structure of tradition powder lime, utilizes suspension calcining technique to produce powder lime, not only
Whole production process is closed, does not easily cause the suspension calcining cooling device after environmental pollution, and improvement, improves heat utilization efficiency,
Thus improve powder lime production efficiency and powder lime quality.
Accompanying drawing explanation
Fig. 1 is overall structure schematic diagram, and in figure, dotted line represents that airflow pipeline, arrow represent direction.
Sequence number and entitled in figure: 1, rubble lime stone storage device, 2, agstone preparation facilities, 3, drawing-in device, 4,
Suspension calcining chiller, 401, whirlwind send pipe, 402, whirlwind return pipe, 403, material pipe, 404, inverted U-shaped airduct, 405, dore furnace,
5, coal dust supply side, 6, fuel gas supply end, the 7, first feed end, the 8, second feed end, 9, blower fan discharge pipe, 10, finished product storing
Device, 11, powder device for filtering and collecting, 12, emission-control equipment, 13, exhaust chimney, C1, one-level heating bucket, C2, two grades add
Heat bucket, C3, three grades of heating buckets, C4, level Four heating bucket, C5, Pyatyi heating bucket, CL1, one-level cooling bucket, CL2, two grades of cooling buckets,
CL3, three grades of cooling buckets.
Detailed description of the invention
In conjunction with accompanying drawing, this utility model is described as follows.
This powder lime suspension calcining production line includes rubble lime stone storage device 1, agstone preparation facilities 2, feeding dress
Put 3, suspension calcining chiller 4, fuel supply system, sieve material device, finished product storage device 10, emission-control equipment 12, broken
The discharge end of limestone storage device 1 is connected to the feed end of agstone preparation facilities 2, going out of agstone preparation facilities 2
Material end connects the feed end of drawing-in device 3 by conveying mechanism, and the discharge end of drawing-in device 3 is connected to suspension calcining chiller
The feed end of 4.Sieve material device is arranged at the discharge end of suspension calcining chiller 4, and fuel supply system includes coal dust supply side 5
With fuel gas supply end 6, the discharge end of sieve material device connects finished product storage device 10.Suspension calcining chiller 4, agstone system
The respective exhaust end of standby device 2 is connected to the air inlet of emission-control equipment 12, emission-control equipment by the pipeline of band blower fan
The air vent of 12 is connected to exhaust chimney 13 by the pipeline of band blower fan, and the exhaust end of suspension calcining chiller 4 and waste gas
Arranging powder device for filtering and collecting 11 between the air inlet of processing means 12, the exhaust end of suspension calcining chiller 4 is connected
Pipeline of fans branch be connected to the air inlet of agstone preparation facilities 2.
Above-mentioned suspension calcining chiller 4 includes regenerator section, calcining part, cooling segment, and regenerator section is provided with one-level
Heating bucket C1, two grades of heating bucket C2, three grades of heating bucket C3, level Four heating bucket C4, Pyatyi heating bucket C5, calcining part is dore furnace
405, cooling segment is provided with one-level cooling bucket CL1, two grades of cooling bucket CL2, three grades of cooling bucket CL3, each heating bucket and cooling bucket
Top is all connected with whirlwind and send pipe 401, and the side of each heating bucket and cooling bucket is all connected with whirlwind return pipe 402, each heating bucket and cooling
Bucket bottom be all connected with expect pipe 403, two grades heating bucket C2 whirlwind send pipe 401 as the feed end of suspension calcining chiller 4,
And be connected to one-level heating bucket C1 whirlwind return pipe 402, one-level heating bucket C1 whirlwind send pipe 401 as suspension calcining cooling dress
Putting the exhaust end of 4, the material pipe 403 of one-level heating bucket C1 is connected to two grades of whirlwind return pipes 402 heating bucket C2 and three grades of heating buckets
The whirlwind of C3 send pipe 401, and the material pipe 403 of two grades of heating bucket C2 is connected to three grades of whirlwind return pipes 402 heating bucket C3 and level Four adds
The whirlwind of heat bucket C4 send pipe 401, the material pipe 403 of three grades of heating bucket C3 to be connected to the whirlwind return pipe 402 and five of level Four heating bucket C4
The whirlwind of level heating bucket C5 send pipe 401, the material pipe 403 of level Four heating bucket C4 to be connected in dore furnace 405, dore furnace 405 top
It is connected by the whirlwind return pipe 402 of inverted U-shaped airduct 404 with Pyatyi heating bucket C5, bottom dore furnace 405, connects one-level cooling bucket
The whirlwind of CL1 send pipe 401, the material pipe 403 of Pyatyi heating bucket C5 to be connected to the whirlwind of two grades of cooling bucket CL2 and send pipe 401 and one-level
The whirlwind return pipe 402 of cooling bucket CL1, the material pipe 403 of one-level cooling bucket CL1 is connected to the whirlwind of three grades of cooling bucket CL3 and send pipe 401
And the whirlwind return pipe 402 of two grades of cooling bucket CL2, the material pipe 403 of two grades of cooling bucket CL2 is connected to the whirlwind of three grades of cooling bucket CL3
Return pipe 402, the whirlwind return pipe 402 of three grades of cooling bucket CL3 is connected to blower fan discharge pipe 9 and sieves the first feed end 7 of material device, and three
The material pipe 403 of level cooling bucket CL3 is connected to the second feed end 8 of sieve material device；The coal dust supply side 5 of fuel supply system is direct
Being connected in dore furnace 405, fuel gas supply end 6 branch is connected to whirlwind return pipe 402, the three grades cooling bucket of one-level cooling bucket CL1
The whirlwind return pipe 402 of CL3 and dore furnace 405.The above-mentioned whirlwind connected send pipe 401 and whirlwind return pipe 402 also can design in one
Formula.Above-mentioned one-level heating bucket C1 is double column structure, and i.e. two one-level heating bucket C1 are set up in parallel, and are conducive to being fully warmed-up.
The technical process of this powder lime suspension calcining production line is: by the discharge end of rubble lime stone storage device 1 by rubble
Lime stone is delivered to agstone preparation facilities 2, carries out the preparation of agstone.The limestone that agstone preparation facilities 2 prepares
Powder is delivered to drawing-in device 3 by conveying mechanism, then by drawing-in device 3, agstone uniformly feeds suspension calcining chiller 4
Feed end, i.e. one-level heating bucket C1 whirlwind return pipe 402 in.By blower fan, suspension calcining chiller 4 is supplied, air-flow
From bottom to top pipe 401, whirlwind return pipe 402, material pipe 403 and inverted U-shaped airduct 404 is sent to connect suspension calcining cooling dress by each whirlwind
Put 4 respectively heat bucket, dore furnace 405, cooling bucket.Directly supplied in dore furnace 405 by the coal dust supply side 5 of fuel supply system
Answer coal dust, by the fuel gas supply end 6 of fuel supply system to whirlwind return pipe 402, the three grades cooling bucket CL3 of one-level cooling bucket CL1
Whirlwind return pipe 402 and dore furnace 405 supply combustion gas, combustion gas is sufficiently mixed with air-flow, and in dore furnace 405 burn.Suspend
The detailed process of calcining is: the agstone falling into one-level heating bucket C1 whirlwind return pipe 402 send pipe at two grades of heating bucket C2 whirlwind
Under the airflow function of 401, whirlwind return pipe 402 along one-level heating bucket C1 carries out Conveyance in sending into one-level heating bucket C1
Level preheating；Agstone after one-level preheating falls into two grades of whirlwind return pipes heating bucket C2 along the material pipe 403 of one-level heating bucket C1
402, three grades of heating bucket C3 whirlwind send the air-flow of pipe 401 to be sent into along the whirlwind return pipe 402 of two grades of heating bucket C2 by agstone
Conveyance two grades of preheatings are carried out in two grades of heating bucket C2；Agstone after two grades of preheatings is along the material pipe of two grades of heating bucket C2
The 403 whirlwind return pipes 402 falling into three grades of heating bucket C3, are sent the air-flow of pipe 401 by agstone edge by level Four heating bucket C4 whirlwind
The whirlwind return pipe 402 of three grades of heating bucket C3 carries out Conveyance three grades of preheatings in sending into three grades of heating bucket C3；After three grades of preheatings
Agstone along three grades heating bucket C3 material pipes 403 fall into level Four heating bucket C4 whirlwind return pipe 402, by Pyatyi heating bucket C5
The whirlwind return pipe 402 that whirlwind send the air-flow of pipe 401 that agstone heats the C4 that struggles against along level Four is carried out in sending into level Four heating bucket C4
Conveyance level Four preheating；Agstone after level Four preheating falls into dore furnace 405 along the material pipe 403 of level Four heating bucket C4
In, in control dore furnace 405, calcining heat is 850～1000 DEG C, and calcination time is 10 seconds in, and agstone calcining and decomposing is formed
Pulverized limestone, by air-flow in dore furnace 405 by the pulverized limestone in dore furnace 405 along the inverted U-shaped airduct 404 at dore furnace 405 top and
The whirlwind return pipe 402 of Pyatyi heating bucket C5 carries out Conveyance in sending into Pyatyi heating bucket C5 and keeps fully reaction.Pyatyi adds
Heat bucket C5 in pulverized limestone along Pyatyi heating bucket C5 material pipe 403 fall into one-level cooling bucket CL1 whirlwind return pipe 402, by two grades
Cooling bucket CL2 whirlwind send the air-flow of pipe 401 that the whirlwind return pipe 402 that pulverized limestone cools down bucket CL1 along one-level is sent into one-level cooling bucket
Conveyance one-level cooling is carried out in CL1；Pulverized limestone after one-level cooling falls into two along the material pipe 403 of one-level cooling bucket CL1
The whirlwind return pipe 402 of level cooling bucket CL2, is sent the air-flow of pipe 401 by pulverized limestone along two grades of cooling buckets by three grades of cooling bucket CL3 whirlwind
The whirlwind return pipe 402 of CL2 carries out Conveyance two grades of coolings in sending into two grades of cooling bucket CL2；Pulverized limestone after two grades of coolings
Along two grades cooling bucket CL2 material pipes 403 fall into three grades cooling bucket CL3 whirlwind return pipes 402, the undecomposed agstone of part or
Material then falls into the first feed end 7 of sieve material device；By the air-flow of blower fan discharge pipe 9 by three grades of cooling bucket CL3 whirlwind return pipes 402
Pulverized limestone along three grades cooling bucket CL3 whirlwind return pipes 402 send into three grades cooling bucket CL3 in carry out Conveyance and three grades cold
But, the pulverized limestone after three grades of coolings falls into the second feed end 8 of sieve material device.The material of first feed end the 7, second feed end 8
Obtaining finished powder Calx after sieve material device sieve material, finished powder Calx is delivered to finished product storage device 10 and stores.By Calx
The material that each exhaust end of stone powder preparation facilities 2 and suspension calcining chiller 4 is discharged, a part is through powder device for filtering and collecting
Being processed by emission-control equipment 12 after 11 sieves material and discharged waste gas by blowdown stack, another part is re-fed into via pipeline
Agstone preparation facilities 2 carries out Commercial cultivation again.More than it is whole technique stream prepared by this utility model powder lime
Journey.
Claims (6)
1. a powder lime suspension calcining production line, it includes that suspension calcining chiller (4), fuel supply system, sieve material fill
Putting, sieve material device is arranged at the discharge end of suspension calcining chiller (4), fuel supply system include coal dust supply side (5) and
Fuel gas supply end (6)；It is characterized in that described suspension calcining chiller (4) includes regenerator section, calcining part, cooling end
Point, regenerator section include one-level heating bucket (C1), two grades heating bucket (C2), three grades heating bucket (C3), level Four heating bucket (C4), five
Level heating bucket (C5), calcining part is dore furnace (405), and cooling segment includes one-level cooling bucket (CL1), two grades of cooling buckets
(CL2), three grades of coolings bucket (CL3), the top of each heating bucket and cooling bucket is all connected with whirlwind and send pipe (401), and each heating struggles against and cold
But the side struggled against is all connected with whirlwind return pipe (402), and each bottom heating bucket and cooling bucket is all connected with material and manages (403), described two grades
Heating bucket (C2) whirlwind send pipe (401) as the feed end of suspension calcining chiller (4), and be connected to described one-level heat
The whirlwind return pipe (402) of bucket (C1), the whirlwind of one-level heating bucket (C1) send pipe (401) as described suspension calcining chiller
(4) exhaust end, the material pipe (403) of one-level heating bucket (C1) is connected to the whirlwind return pipe (402) of described two grades of heating bucket (C2)
And the whirlwind of three grades of heating bucket (C3) send pipe (401), the material pipe (403) of two grades of heating bucket (C2) to be connected to described three grades of heating buckets
(C3) whirlwind return pipe (402) and the whirlwind of level Four heating bucket (C4) send pipe (401), the material pipe (403) of three grades of heating bucket (C3)
The whirlwind of the whirlwind return pipe (402) and Pyatyi heating bucket (C5) that are connected to level Four heating bucket (C4) send pipe (401), level Four heating bucket
(C4) material pipe (403) is connected in described dore furnace (405), and inverted U-shaped airduct (404) and institute are passed through in dore furnace (405) top
The whirlwind return pipe (402) stating Pyatyi heating bucket (C5) connects, and dore furnace (405) bottom connects described one-level cooling bucket (CL1)
The whirlwind that whirlwind send pipe (401), the material pipe (403) of described Pyatyi heating bucket (C5) to be connected to described two grades of coolings bucket (CL2) send
Pipe (401) and the whirlwind return pipe (402) of one-level cooling bucket (CL1), the material pipe (403) of one-level cooling bucket (CL1) is connected to described
The whirlwind of three grades of coolings bucket (CL3) send pipe (401) and the whirlwind return pipe (402) of two grades of coolings bucket (CL2), two grades of cooling buckets
(CL2) material pipe (403) is connected to the whirlwind return pipe (402) of three grades of coolings bucket (CL3), and the whirlwind of three grades of coolings bucket (CL3) returns
Pipe (402) is connected to blower fan discharge pipe (9) and first feed end (7) of sieve material device, the material pipe of three grades of coolings bucket (CL3)
(403) second feed end (8) of described sieve material device it is connected to；The coal dust supply side (5) of described fuel supply system directly connects
Being connected in described dore furnace (405), described fuel gas supply end (6) branch is connected to the whirlwind of described one-level cooling bucket (CL1) and returns
Pipe (402), the whirlwind return pipe (402) of described three grades of coolings bucket (CL3) and described dore furnace (405).
Powder lime suspension calcining production line the most according to claim 1, it is characterised in that described in the whirlwind that connects send pipe
(401) with whirlwind return pipe (402) be integral type pipe.
Powder lime whirlwind the most according to claim 1 calcining production line, it is characterised in that described one-level heating bucket (C1) is
Double column structure, i.e. two one-levels heating bucket (C1) are set up in parallel.
Powder lime suspension calcining production line the most according to claim 1, it is characterised in that this production line also includes rubble ash
Stone storage device (1), agstone preparation facilities (2), drawing-in device (3), finished product storage device (10), emission-control equipment
(12), the discharge end of rubble lime stone storage device (1) is connected to the feed end of agstone preparation facilities (2), agstone system
The discharge end of standby device (2) connects the feed end of drawing-in device (3) by conveying mechanism, and the discharge end of drawing-in device (3) connects
To the feed end of described suspension calcining chiller (4), the discharge end of described sieve material device connects described finished product storage device
(10), the respective exhaust end pipeline by band blower fan of described suspension calcining chiller (4), agstone preparation facilities (2)
Being connected to the air inlet of emission-control equipment (12), the air vent of emission-control equipment (12) is connected to by the pipeline of band blower fan
Exhaust chimney (13).
Powder lime suspension calcining production line the most according to claim 4, it is characterised in that described suspension calcining chiller
(4) between exhaust end and the air inlet of described emission-control equipment (12), powder device for filtering and collecting (11) is set.
Powder lime suspension calcining production line the most according to claim 4, it is characterised in that described suspension calcining chiller
(4) the pipeline of fans branch that exhaust end is connected is connected to the air inlet of described agstone preparation facilities (2).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620532920.2U CN205838848U (en) | 2016-06-02 | 2016-06-02 | Powder lime suspension calcining production line |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620532920.2U CN205838848U (en) | 2016-06-02 | 2016-06-02 | Powder lime suspension calcining production line |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205838848U true CN205838848U (en) | 2016-12-28 |
Family
ID=57623061
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620532920.2U Active CN205838848U (en) | 2016-06-02 | 2016-06-02 | Powder lime suspension calcining production line |
Country Status (1)
| Country | Link |
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| CN (1) | CN205838848U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105906223A (en) * | 2016-06-02 | 2016-08-31 | 浙江钙科机械设备有限公司 | Lime powder suspension calcining production line and suspension calcining process thereof |
| CN113860345A (en) * | 2021-10-08 | 2021-12-31 | 浙江钙科机械设备有限公司 | Automatic control system for calcium oxide classification suspension calcination process |
-
2016
- 2016-06-02 CN CN201620532920.2U patent/CN205838848U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105906223A (en) * | 2016-06-02 | 2016-08-31 | 浙江钙科机械设备有限公司 | Lime powder suspension calcining production line and suspension calcining process thereof |
| CN113860345A (en) * | 2021-10-08 | 2021-12-31 | 浙江钙科机械设备有限公司 | Automatic control system for calcium oxide classification suspension calcination process |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CP03 | Change of name, title or address | ||
| CP03 | Change of name, title or address |
Address after: 313000 Mianxian village, Meishan Town, Changxing County, Huzhou City, Zhejiang Province Patentee after: Zhejiang Caoke Technology Co.,Ltd. Address before: 313000 Visiting Xian Village, Baixian Township, Changxing County, Huzhou City, Zhejiang Province Patentee before: ZHEJIANG CALCIUM TECHNOLOGY MACHINERY CO.,LTD. |