CN109847508A - The main kiln linkage corollary equipment group of the drying kiln-of high efficiency drying - Google Patents
The main kiln linkage corollary equipment group of the drying kiln-of high efficiency drying Download PDFInfo
- Publication number
- CN109847508A CN109847508A CN201811387659.1A CN201811387659A CN109847508A CN 109847508 A CN109847508 A CN 109847508A CN 201811387659 A CN201811387659 A CN 201811387659A CN 109847508 A CN109847508 A CN 109847508A
- Authority
- CN
- China
- Prior art keywords
- kiln
- drying
- tail gas
- corollary equipment
- high efficiency
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- 238000001035 drying Methods 0.000 title claims abstract description 103
- 239000000428 dust Substances 0.000 claims abstract description 39
- 230000001877 deodorizing effect Effects 0.000 claims abstract description 16
- 239000000463 material Substances 0.000 claims abstract description 13
- 238000004332 deodorization Methods 0.000 claims abstract description 8
- 238000000034 method Methods 0.000 claims abstract description 7
- 238000004064 recycling Methods 0.000 claims abstract description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 11
- 238000002485 combustion reaction Methods 0.000 claims description 9
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 claims description 8
- 239000010802 sludge Substances 0.000 claims description 7
- 239000013049 sediment Substances 0.000 claims description 3
- 238000005265 energy consumption Methods 0.000 abstract description 7
- 238000002360 preparation method Methods 0.000 abstract description 7
- 239000007789 gas Substances 0.000 description 37
- 238000010586 diagram Methods 0.000 description 4
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 3
- QGJOPFRUJISHPQ-UHFFFAOYSA-N Carbon disulfide Chemical compound S=C=S QGJOPFRUJISHPQ-UHFFFAOYSA-N 0.000 description 3
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 3
- 238000010521 absorption reaction Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 239000002245 particle Substances 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 2
- LSDPWZHWYPCBBB-UHFFFAOYSA-N Methanethiol Chemical compound SC LSDPWZHWYPCBBB-UHFFFAOYSA-N 0.000 description 2
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 2
- 239000000919 ceramic Substances 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- WQOXQRCZOLPYPM-UHFFFAOYSA-N dimethyl disulfide Chemical compound CSSC WQOXQRCZOLPYPM-UHFFFAOYSA-N 0.000 description 2
- 229910000037 hydrogen sulfide Inorganic materials 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 238000005245 sintering Methods 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- GETQZCLCWQTVFV-UHFFFAOYSA-N trimethylamine Chemical compound CN(C)C GETQZCLCWQTVFV-UHFFFAOYSA-N 0.000 description 2
- QMMFVYPAHWMCMS-UHFFFAOYSA-N Dimethyl sulfide Chemical compound CSC QMMFVYPAHWMCMS-UHFFFAOYSA-N 0.000 description 1
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 description 1
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 description 1
- 239000005864 Sulphur Substances 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 239000000356 contaminant Substances 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 210000003298 dental enamel Anatomy 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 230000001788 irregular Effects 0.000 description 1
- 238000005065 mining Methods 0.000 description 1
- 230000000116 mitigating effect Effects 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 239000004570 mortar (masonry) Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000013618 particulate matter Substances 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 230000002035 prolonged effect Effects 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 150000003384 small molecules Chemical class 0.000 description 1
- -1 sulphur hydrogen Chemical class 0.000 description 1
- 239000002918 waste heat Substances 0.000 description 1
- 239000008096 xylene Substances 0.000 description 1
Landscapes
- Treating Waste Gases (AREA)
Abstract
The invention discloses a kind of main kiln linkage corollary equipment groups of the drying kiln-of high efficiency drying, belong to ceramsite preparation process technical field, it includes have: single-revolution kiln, for being sintered to haydite materials；One pre- cleaner, is connected with the offgas outlet of the rotary kiln, for carrying out preliminary dust removal to tail gas；At least one drying kiln is connected with the tail gas after preliminary dust removal, for carrying out drying and dewatering to pug；One deodorizing device is connected with the tail gas by the drying kiln, for carrying out deodorization to tail gas；Cleaner after one is connected with the tail gas after deodorization, for the dust removal process before exhaust emissions or recycling.The corollary equipment group improves the drying efficiency of drying kiln, has saved drying energy consumption, while also reducing the burden of rear cleaner, saves the human and material resources of exhaust-gas treatment.
Description
Technical field
The present invention relates to ceramsite preparation process technical fields, link in particular to a kind of main kiln of drying kiln-of high efficiency drying
Corollary equipment group.
Background technique
Haydite is exactly as its name suggests the particle of ceramic.The external appearance characteristic of haydite is largely rounded or oval-shaped ball,
But it is not round or ellipse sphere there are also imitative rubble haydite, and is in irregular rubble shape, surface is one layer hard
Shell, this layer of shell are in ceramic or enamel, there is water proof to protect gas effect, and assign haydite higher intensity.Lightness is pottery
In many excellent performances of grain the most important and it heavy sandstone can be replaced to prepare light aggregate concrete, light mortar
The main reason for.
A kind of haydite as disclosed in the Chinese invention patent application No. is CN201110241100.X and preparation method thereof,
In the preparation process of existing haydite, enters mixing machine after pug drying kiln drying and pelletizer is entered back into rotary kiln and burnt
System, the tail gas of rotary kiln are discharged or are recycled after processing, and drying kiln drying pug reaches certain dehydration requirement and needs to consume
A large amount of energy consumption, drying cost is higher, meanwhile, the tail gas treatment device heavy load of rotary kiln needs continually to overhaul and unload
Material, the manpower and material resources cost of cost also remain high.
Summary of the invention
In view of the above technical problems, the main kiln linkage corollary equipment group of the drying kiln-of high efficiency drying of the present invention is used for
Sintering process in ceramsite preparation process, and rotary kiln exhaust gas is passed through baking after preliminary dust removal directly or after secondary combustion chamber
Dry kiln improves the drying efficiency of drying kiln, has saved drying energy consumption, while also reducing the burden of rear cleaner, section
The human and material resources of exhaust-gas treatment is saved.
To achieve the above object, the main kiln linkage corollary equipment group of the drying kiln-of a kind of high efficiency drying designed by the present invention,
Include:
Single-revolution kiln, for being sintered to haydite materials；
One pre- cleaner, is connected with the offgas outlet of the rotary kiln, for carrying out preliminary dust removal to tail gas；
At least one drying kiln is connected with the tail gas after preliminary dust removal, for carrying out drying and dewatering to pug；
One deodorizing device is connected with the tail gas by the drying kiln, for carrying out deodorization to tail gas；
Cleaner after one is connected with the tail gas after deodorization, for the dust removal process before exhaust emissions or recycling.
The heat source (such as hot-blast stove) that drying kiln used herein does not carry, only one kiln body will be still in height
The tail gas of warm (200 ~ 300 DEG C) state is passed through drying kiln, is capable of providing heat source, the waste heat of rotary kiln is utilized, saved drying
Cost, at the same the pug in drying kiln with moisture also can the remaining dust of absorbed portion, alleviate the negative of rear cleaner
Load.
As a preferred embodiment of the above technical solution, the pre- cleaner by cyclone dust collectors and bag filter series connection and
At.
The dust removal mechanism of cyclone dust collectors is that dust-contained airflow is made to rotate, by means of centrifugal force by grit from air-flow
Wall is separated and be trapped in, then so that grit is fallen into ash bucket by gravity, as the cleaner for contacting tail gas first, energy
Enough most dust removals, disadvantage is lower to the removal efficiency of micron-level particle size fine dusts below；For this purpose, immediately
Collocation use bag filter, by filtering sieve mechanism the dust in dusty gas is removed, in general,
After cyclone dust collectors and bag filter processing, dust removal efficiency is generally 99% or more, and house outlet gas dust content is in number
Ten mg/m3Within.
As a preferred embodiment of the above technical solution, the drying kiln is the mud drying that drying and dewatering is carried out to riverway sludge
Kiln.
Riverway sludge itself contains large quantity of moisture, even if still remaining when entering in drying kiln after plate and frame filter press is handled
There are many moisture, this characteristic brings the effect of two aspects: 1. proposing higher want to the drying performance of drying kiln first
It asks, i.e. drying kiln needs to consume after more energy consumptions are dried or dried that moisture content is still higher, does not reach requirement, at this fashion
It is that drying kiln brings calorie source in the tail gas of high temperature, helps to promote the drying efficiency to riverway sludge, and saved drying
The energy consumption of kiln；2. the biggish pug of moisture content is easier to remaining dust in absorption tail gas, so that when tail gas passes through drying kiln in it
Dust removal rate promoted, and then alleviate it is subsequent after cleaner dedusting pressure and dedusting cost, dried through mud
After dry kiln absorption dedusting, the dust content in tail gas is further reduced.
As a preferred embodiment of the above technical solution, the deodorizing device is ozone deodorizing apparatus.
Ozone deodorizing apparatus irradiates foul gas using special high energy ozone and UV ultraviolet beam, cracks foul gas
Such as: ammonia, trimethylamine, hydrogen sulfide, first sulphur hydrogen, methyl mercaptan, methyl sulfide, methyl disulfide, carbon disulfide and styrene, sulfide H2S,
VOC class, the molecular link of benzene,toluene,xylene etc. make to be combined into small molecule in the contaminant molecule and ozone oxidation of free state
The compound of harmless or low evil, such as CO2、H2O etc..
As a preferred embodiment of the above technical solution, the rear cleaner is screen collector.
Screen collector belongs to a kind of cleaning equipment of wet type, is adequately collided with dust using water flow, utilizes water
Particulate matter and water mixing in pearl and dust, so that the dust particles of clean gas discharge and water reaction after being cleaned
Also it will directly stay in deduster and precipitate, the later period is cleared up.
As a preferred embodiment of the above technical solution, the water in the screen collector after dedusting is passed into vent gas treatment circulation
It is settled in pond, the upper layer clear water of the vent gas treatment circulatory pool is returned to reuse in the screen collector, lower layer's sedimentation
Object recycling is spare.
Lower layer's sediment can be delivered to by sludge pump at plate and frame filter press be dehydrated it is spare, can still do haydite materials.
After drying kiln or the absorption of mud drying kiln, the dredging period for the vent gas treatment circulatory pool that screen collector is connected
It is obviously prolonged, reduces the frequency of dredging, saved dredging cost.
As a preferred embodiment of the above technical solution, further include a secondary combustion chamber, be sintered for being undertaken in the rotary kiln
Haydite, tail gas after preliminary dust removal flows to drying after heat exchange by the secondary combustion chamber and sintered haydite again
Kiln, deodorizing device and rear cleaner.
After kiln tail tail gas is introduced secondary combustion chamber, exhaust temperature can be promoted to 400 ~ 500 degree, enter back into drying kiln just
It is to be directly entered drying kiln than former kiln tail tail gas to improve thermal energy, also improves the thermal efficiency.
Compared with prior art, the present invention have the following advantages that and the utility model has the advantages that
The main kiln linkage corollary equipment group of the drying kiln-of high efficiency drying of the present invention is for the agglomerant in ceramsite preparation process
Sequence, and rotary kiln exhaust gas is passed directly into drying kiln after preliminary dust removal, it is especially suitable for being passed through in the drying kiln of riverway sludge；
It improves the drying efficiency of drying kiln, pug can be made to reach the index of moisture content under the premise of less energy consumption, together
When also reduce the burden of rear cleaner, save the human and material resources of exhaust-gas treatment.
Detailed description of the invention
Fig. 1 is the main kiln linkage corollary equipment group schematic diagram of drying kiln-described in embodiment 1.
Fig. 2 is the main kiln linkage corollary equipment group schematic diagram of drying kiln-as described in example 2.
Fig. 3 is the main kiln linkage corollary equipment group schematic diagram of drying kiln-described in embodiment 3.
Fig. 4 is the main kiln linkage corollary equipment group schematic diagram of drying kiln-as described in example 4.
Gas circuit in Fig. 1 ~ Fig. 4, which is adopted, to be represented by dashed line.
In figure: mud drying kiln a-1.3, tail mud drying kiln a-2.2, rotary kiln c-1, cyclone dust collectors c-2, bag-type dust
Device c-3, deodorizing device c-4, rear cleaner c-5, vent gas treatment circulatory pool c-6, secondary combustion chamber c-8.
Specific embodiment
The present invention is described in further detail combined with specific embodiments below:
Embodiment is used to prepare sintering process and baking process in the ceramsite preparation process during haydite, in each embodiment institute
During stating play save drying kiln energy consumption and exhaust-gas treatment manpower and material resources, and reach drying moisture content index and
The technical effect of the burden of cleaner after mitigation.
Embodiment 1: Fig. 1, the main kiln linkage corollary equipment group of the drying kiln-of high efficiency drying, by rotary kiln c-1, whirlwind are referred to
Deduster c-2, bag filter c-3, tail mud drying kiln a-2.2, deodorizing device c-4 and rear cleaner c-5 are constituted, wherein
Tail mud drying kiln a-2.2 is used to carry out mining tail mud drying and processing, and deodorizing device c-4 is ozone deodorizing apparatus, rear cleaner
C-5 is screen collector；
Exhaust temperature in rotary kiln c-1 is up to 200 ~ 300 DEG C, successively through cyclone dust collectors c-2 and bag filter c-3 dedusting
Afterwards, temperature enters in tail mud drying kiln a-2.2 at 200 DEG C or more and provides heat as heat source, and drying material passes through simultaneously
Part residual dust is fallen by Adsorption, dust content further decreases, then into carrying out deodorization in ozone deodorizing apparatus, then
It is dusted by screen collector, the water in screen collector after dedusting, which is passed into vent gas treatment circulatory pool c-6, to be sunk
Drop, the upper layer clear water of the vent gas treatment circulatory pool c-6 are returned to reuse in the screen collector, and lower layer's sediment is through sludge
Pump conveying recycling still can be used for ceramisite sintered.
Embodiment 2: referring to Fig. 2, and the main kiln of the drying kiln-of high efficiency drying links corollary equipment group, it is different from embodiment 1 it
Be in: tail gas in rotary kiln c-1 time is passed into mud drying after cyclone dust collectors c-2 and bag filter c-3 dedusting
In kiln a-1.3.
Embodiment 3: referring to Fig. 3, and the main kiln of the drying kiln-of high efficiency drying links corollary equipment group, it is different from embodiment 2 it
It is in and after cyclone dust collectors c-2 and bag filter c-3 dedusting, is passed through tail mud drying kiln a-2.2 and silt in parallel in: tail gas
In mud drying kiln a-1.3, it is dusted then into carrying out deodorization in ozone deodorizing apparatus, then by screen collector.
Embodiment 4: referring to Fig. 4, and the main kiln of the drying kiln-of high efficiency drying links corollary equipment group, it is different from embodiment 1 it
Be in: the exhaust temperature in rotary kiln c-1 is up to 200 ~ 300 DEG C, and rotary kiln c-1 is delivered to the haydite of secondary combustion chamber c-8
Temperature is up to 800 ~ 1000 DEG C, and tail gas first passes around cyclone dust collectors c-2 and bag filter c-3 dedusting, then via rotary kiln
The secondary combustion chamber c-8 of the outlet c-1, temperature are promoted to 400 ~ 500 DEG C, enter back into tail mud drying kiln a-2.2 as heat source
Heat is provided, drying material is greatly improved the drying efficiency of material, while falling part residual dust, powder via Adsorption
Dust content further decreases.
Technical solution of the present invention and beneficial effect is described in detail in embodiment described above, it should be understood that
Above is only a specific embodiment of the present invention, it is not intended to restrict the invention, it is all to be done in spirit of the invention
Any modification, supplementary, and equivalent replacement etc., should all be included in the protection scope of the present invention.
Claims (7)
- The corollary equipment group 1. the main kiln of the drying kiln-of high efficiency drying links, which is characterized in that include:Single-revolution kiln (c-1), for being sintered to haydite materials；One pre- cleaner is connected with the offgas outlet of the rotary kiln (c-1), for carrying out preliminary dust removal to tail gas；At least one drying kiln is connected with the tail gas after preliminary dust removal, for carrying out drying and dewatering to pug；One deodorizing device (c-4) is connected with the tail gas by the drying kiln, for carrying out deodorization to tail gas；Cleaner (c-5) after one, is connected with the tail gas after deodorization, for the dust removal process before exhaust emissions or recycling.
- The corollary equipment group 2. the main kiln of the drying kiln-of high efficiency drying according to claim 1 links, it is characterised in that: described Pre- cleaner is connected in series by cyclone dust collectors (c-2) and bag filter (c-3).
- The corollary equipment group 3. the main kiln of the drying kiln-of high efficiency drying according to claim 1 links, it is characterised in that: described Drying kiln is the mud drying kiln (a-1.3) that drying and dewatering is carried out to riverway sludge.
- The corollary equipment group 4. the main kiln of the drying kiln-of high efficiency drying according to claim 1 links, it is characterised in that: described Deodorizing device (c-4) is ozone deodorizing apparatus.
- The corollary equipment group 5. the main kiln of the drying kiln-of high efficiency drying according to claim 1 links, it is characterised in that: described Cleaner (c-5) is screen collector afterwards.
- The corollary equipment group 6. the main kiln of the drying kiln-of high efficiency drying according to claim 5 links, it is characterised in that: described Water in screen collector after dedusting is passed into vent gas treatment circulatory pool (c-6) and is settled, the vent gas treatment circulation The upper layer clear water in pond is returned to reuse in the screen collector, and the recycling of lower layer's sediment is spare.
- The corollary equipment group 7. the main kiln of the drying kiln-of high efficiency drying according to claim 1 links, it is characterised in that: also wrap A secondary combustion chamber (c-8) is included, the tail gas for being undertaken on the haydite being sintered in the rotary kiln (c-1), after preliminary dust removal Flowed to again after heat exchange by the secondary combustion chamber (c-8) and sintered haydite drying kiln, deodorizing device (c-4) and after Cleaner (c-5).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811387659.1A CN109847508A (en) | 2018-11-21 | 2018-11-21 | The main kiln linkage corollary equipment group of the drying kiln-of high efficiency drying |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811387659.1A CN109847508A (en) | 2018-11-21 | 2018-11-21 | The main kiln linkage corollary equipment group of the drying kiln-of high efficiency drying |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN109847508A true CN109847508A (en) | 2019-06-07 |
Family
ID=66890109
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201811387659.1A Pending CN109847508A (en) | 2018-11-21 | 2018-11-21 | The main kiln linkage corollary equipment group of the drying kiln-of high efficiency drying |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN109847508A (en) |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102200394A (en) * | 2011-05-12 | 2011-09-28 | 浙江方远建材科技有限公司 | Method and device for utilizing exhaust gas of haydite rotary kiln |
| CN203208857U (en) * | 2013-04-23 | 2013-09-25 | 焦作市华岩实业有限公司 | System for removing dust in tail gas of rotary kilns |
| CN203907621U (en) * | 2014-05-22 | 2014-10-29 | 林清其 | Renewable thermal oxidizer for solid waste incineration |
| CN204574833U (en) * | 2015-02-09 | 2015-08-19 | 孝义市鑫腾矿业有限公司 | A kind of rotary kiln waste gas recycle device |
| CN105090993A (en) * | 2014-07-11 | 2015-11-25 | 浙江三联环保机械设备有限公司 | Built-in comprehensive drying and incinerating system for sludge and drying and incinerating method for sludge |
| CN209392948U (en) * | 2018-11-21 | 2019-09-17 | 浙江大东吴集团建设有限公司 | The main kiln linkage corollary equipment group of the drying kiln-of high efficiency drying |
-
2018
- 2018-11-21 CN CN201811387659.1A patent/CN109847508A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102200394A (en) * | 2011-05-12 | 2011-09-28 | 浙江方远建材科技有限公司 | Method and device for utilizing exhaust gas of haydite rotary kiln |
| CN203208857U (en) * | 2013-04-23 | 2013-09-25 | 焦作市华岩实业有限公司 | System for removing dust in tail gas of rotary kilns |
| CN203907621U (en) * | 2014-05-22 | 2014-10-29 | 林清其 | Renewable thermal oxidizer for solid waste incineration |
| CN105090993A (en) * | 2014-07-11 | 2015-11-25 | 浙江三联环保机械设备有限公司 | Built-in comprehensive drying and incinerating system for sludge and drying and incinerating method for sludge |
| CN204574833U (en) * | 2015-02-09 | 2015-08-19 | 孝义市鑫腾矿业有限公司 | A kind of rotary kiln waste gas recycle device |
| CN209392948U (en) * | 2018-11-21 | 2019-09-17 | 浙江大东吴集团建设有限公司 | The main kiln linkage corollary equipment group of the drying kiln-of high efficiency drying |
Non-Patent Citations (1)
| Title |
|---|
| 茹至刚编著: "《废水治理工程技术》", 31 January 1989, 中国环境科学出版社出版, pages: 268 - 271 * |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN106180169B (en) | A kind of soil thermal desorption renovation technique and equipment | |
| CN108479237A (en) | A kind of high gravity dedusting system and its application method | |
| CN103736604B (en) | A kind of cyclone wet type electrostatic dust collector | |
| CN209392948U (en) | The main kiln linkage corollary equipment group of the drying kiln-of high efficiency drying | |
| CN203437026U (en) | Fume purification system for garbage burning | |
| CN209665786U (en) | The haydite of high efficiency drying prepares production line | |
| CN109648700A (en) | The haydite of high efficiency drying prepares production line | |
| CN201231120Y (en) | Composite fertilizer drying tail-gas dust removing device | |
| CN201143409Y (en) | Asphaltum smoke purification system | |
| CN109847508A (en) | The main kiln linkage corollary equipment group of the drying kiln-of high efficiency drying | |
| CN206168118U (en) | Concrete mixing plant storehouse top dust collecting equipment | |
| CN2508123Y (en) | Impact water bath and active carbon filter combined three-stage high-efficiency dusting purifying device | |
| CN207324459U (en) | A kind of pitch dust pelletizing system | |
| CN206325362U (en) | Print waste gas recovery governing system | |
| CN103071352A (en) | Dust removing and waste gas removing apparatus | |
| CN109675399A (en) | A kind of ore processing dust collecting process | |
| CN206381749U (en) | A kind of multi-point dust separation system of coke production line | |
| CN206372641U (en) | The dust pelletizing system of flue gas produced by sludge high temperature processing | |
| CN2507548Y (en) | Venturi and active carbon filter combined three-stage high-efficiency dusting purifying device | |
| CN114832606A (en) | Sludge carbonization tail gas treatment and de-whitening process | |
| CN113634083A (en) | Combined type dust removal device and method for nickel-iron alloy smelting plant | |
| CN209783252U (en) | Integrated solid waste drying treatment system | |
| CN106247809A (en) | A kind of ceramic kiln exhaust waste heat recovery device | |
| CN209568015U (en) | A kind of Dredged bed mud prepares the device of light ceramic | |
| CN202030670U (en) | Vertical type powder grinding and drying device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination |