CN206138975U - Energy -conserving tower that vulcanizes of steel mill - Google Patents
Energy -conserving tower that vulcanizes of steel mill Download PDFInfo
- Publication number
- CN206138975U CN206138975U CN201620871194.7U CN201620871194U CN206138975U CN 206138975 U CN206138975 U CN 206138975U CN 201620871194 U CN201620871194 U CN 201620871194U CN 206138975 U CN206138975 U CN 206138975U
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- flue gas
- absorption tower
- connection
- pipe
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Abstract
The utility model discloses an energy -conserving tower that vulcanizes of steel mill belongs to the exhaust -gas treatment field, aims at solving the problem that current vulcanization tower vulcanizing effect is low, the energy consumption is big, processing apparatus, flue gas after treatment system, air transportation manage b behind absorbent supply system, absorption tower, flue gas conveyer pipe, water supply system, gypsum slurry, absorbent supply system, flue gas conveyer pipe, water supply system, gypsum slurry after processing apparatus, flue gas after treatment system, air transportation pipe b communicate with the absorption tower respectively.
Description
Technical field
The utility model is related to a kind of fume treatment field, is specifically a kind of steel mill energy-saving vulcanizing tower.
Background technology
Desulfurization, refer to the methods such as the element sulphur calcium base in coal are fixed become solid prevent burning when generate SO2.At present
Sulfur method typically have burn in burning before burning after three classes such as desulfurization.
By the dry and wet state of absorbent and desulfurization product in sweetening process again can by desulfurization technology be divided into wet method, dry method and
It is half-dried（It is semi-moist）Method.Wet FGD technology is that desulfurization and process desulfurization are produced under wet condition with the solution containing absorbent or slurries
Thing, the method has the advantages that desulphurization reaction speed is fast, equipment is simple, desulfuration efficiency is high, but generally existing seriously corroded, operation dimension
Shield is costly and easily causes secondary pollution problems.
The desulfurization absorption of dry method FGD technology and product are processed to be carried out under dry state, and the method has without sewage spent acid row
Go out, equipment corrosion lesser extent, flue gas in purification process without cigarette temperature after significant hypothermal, purification it is high, spread beneficial to chimney exhaust,
The advantages of secondary pollution is few, but it is low to there is desulfuration efficiency, reaction speed compared with it is slow, equipment is huge the problems such as.
So finding a kind of mode for combining dry and wet desulfurization method, simultaneously reducing energy consumption amount is led to exhaust-gas treatment
Domain will be significant.
Utility model content
The purpose of this utility model is：For above-mentioned problem, there is provided a kind of steel mill energy-saving vulcanizing tower, pass through
Water evaporation is condensed to form water smoke, water smoke and flue gas mixing after carry out flue gas desulfurization with the mode of reactive desulfurizing agent again, not only into
This reduction, desulfurized effect have also obtained the raising of higher degree.
The technical solution adopted in the utility model is as follows：
The utility model discloses a kind of steel mill energy-saving vulcanizing tower, including absorbent supplying system, absorption tower, flue gas are defeated
Send pipe, water system, gypsum slurries after-treatment device, flue gas after-treatment system, air delivery pipe b；
Locate after described absorbent supplying system, flue gas delivery pipe, water system, gypsum slurries after-treatment device, flue gas
Reason system, air delivery pipe b are connected respectively with absorption tower；
Used as improvement, described absorbent supplying system includes batcher, nitrator, holding vessel, air delivery pipe a, institute
The batcher stated is connected with transport vehicle and digester, and nitrator and holding vessel connect, and holding vessel is connected with absorption tower, described sky
Letter shoot a connects and holding vessel（103）And absorption tower（2）Between pipeline on.
Used as improvement, described water system includes water pipe, heat exchanger, water pipe and heat exchanger connection, heat exchanger and absorption
Tower connects.
Used as improvement, described flue gas after-treatment system includes the top of demister, heater, demister connection and absorption tower
Portion, heater is located at the downstream of demister.
Used as improvement, described absorption tower bottom is provided with structure protruding upward and forms evaporation layer, sets in described evaporation layer
There is an evaporimeter, between described evaporation layer and the first volume structure on absorption tower the filter membrane that can filter out fixed dust is provided with；
The upper strata of evaporation layer is provided with condensate layer, and the condensation pipe of spatial networks is provided with the middle of described condensate layer, described
The cross section of condensation pipe is circle, and round diameter is 10mm-100mm, and described condensate layer is provided with and heat exchanger connection
Heat exchanger；
The upper strata of described condensate layer is provided with mixed layer, and mixed layer and flue gas delivery pipe connect, flue gas delivery pipe（3）Will refining
The water smoke mixing that the flue gas and condensate layer that steel mill produces is produced, described mixed layer is provided with can be sufficiently mixed flue gas and water smoke
Eddy mixer；
The upper strata of mixed layer is provided with absorbed layer, and described absorbed layer and absorbent supplying system connects.
Used as improvement, described heater and the heat exchanger of condensate layer connects, and the heat that can be absorbed condensate layer is passed
It is delivered to heater.
Used as improvement, described condensation pipe is made up of heat-conducting polymer material, and described heat-conducting polymer includes：High score
100 parts of sub- matrix resin, heat conducting fiber 20-50 part, coupling agent 0.5-5 parts, antioxidant 0.5-5 parts.
Preferably, including at least a kind of at least containing one kind in the synthesis material monomer of described macromolecule matrix resin
The monomer of hydrophobic grouping.
Preferably, described macromolecule matrix resin is PMMA, PS, one kind of nylon 6, described coupling agent be γ-
Aminopropyl triethoxysilane, γ-glycidyl ether oxygen propyl trimethoxy silicane, γ-methacryloxypropyl front three
TMOS, N- (β-aminoethyl)-γ-aminopropyltrimethoxysilane, N- β-（Aminoethyl）- γ-aminopropyltriethoxy dimethoxy
One kind of base silane.
Preferably, described heat conducting fiber is short silk carbon fiber, copper fiber, steel fibre, one kind of aluminum fiber, it is described
Antioxidant is one kind of diphenylamines, p-phenylenediamine and EEDQ.
In sum, as a result of above-mentioned technical proposal, the beneficial effects of the utility model are：
The utility model is adopted and is condensed into water smoke again simultaneously and flue gas, the method for desulphurizer mixing to hot water elder generation heating evaporation,
So that can be mutually mixed between each component, desulfurized effect is improved, reduced the cost.
In specific process choice, in the middle of the process heated to water, the utility model is by the way of distribution heating
Carry out, not only save fuel and reduce the heat time, and by the heating of the heat transmission of condensed absorbent to flue gas after-treatment system
Heat exchanger on device and water-supply-pipe, has saved fuel.
In the selection of condensed material, traditional metal has that heat transfer effect is high, low cost a little, but but not corrosion resistant
Erosion, service life is short, and the utility model strengthens the method for macromolecule resin using heat conducting fiber, using disclosed in the utility model
Not only heat-conducting effect is high, hydrophobicity is good, corrosion-resistant, long service life for the obtained heat-conducting polymer material of formula.
Description of the drawings
Fig. 1 is the utility model structural representation；
Mark in figure：1- absorbent supplying systems, 101- batchers, 102- nitrators, 103- holding vessels, 104- air is defeated
Pipe a, 2- absorption towers, 201- evaporimeters, 202- condensate layers, 203- mixed layers, 204- absorbed layers, 3- flue gas delivery pipes, 4- is sent to supply
Water system, 401- water pipes, 402- heat exchangers, 5- gypsum slurries processing meanss, 6- flue gas after-treatment systems, 601- demisters,
602- heaters, 7- air delivery pipe b.
Specific embodiment
Below in conjunction with the accompanying drawings, the utility model is described in detail.
In order that the purpose of this utility model, technical scheme and advantage become more apparent, below in conjunction with accompanying drawing and enforcement
Example, is further elaborated to the utility model.It should be appreciated that specific embodiment described herein is only to explain
The utility model, is not used to limit the utility model.
Specific embodiment 1：As shown in figure 1, present embodiment discloses a kind of steel mill energy-saving vulcanizing tower, including absorbent is supplied
Answer system 1, absorption tower 2, flue gas delivery pipe 3, water system 4, gypsum slurries after-treatment device 5, flue gas after-treatment system 6, sky
Letter shoot b；
Described absorbent supplying system 1, flue gas delivery pipe 3, water system 4, gypsum slurries after-treatment device 5, flue gas
After-treatment system 6, air delivery pipe b are connected respectively with absorption tower 2；
Described absorbent supplying system 1 includes batcher 101, nitrator 102, holding vessel 103, air delivery pipe
A104, described batcher 101 is connected with transport vehicle and digester 102, and nitrator 102 and holding vessel 103 connect, holding vessel
103 are connected with absorption tower 2, in described air delivery pipe a104 connections and the pipeline between holding vessel 103 and absorption tower 2.
Described water system includes water pipe 401, heat exchanger 402, and water pipe 401 and heat exchanger 402 connect, heat exchanger 402
Connect with absorption tower 2.
Flue gas after-treatment system 6 includes the top of demister 601, heater 602, the connection of demister 601 and absorption tower 2,
Heater 602 is located at the downstream of demister 601.
The described bottom of absorption tower 2 is provided with structure protruding upward and forms evaporation layer, and in described evaporation layer evaporimeter is provided with
201, it is provided with the filter membrane that can filter out fixed dust between described evaporation layer and the first volume structure on absorption tower 2；
The upper strata of evaporation layer is provided with condensate layer 202, and the condensation pipe of spatial networks is provided with the middle of described condensate layer 202,
The cross section of described condensation pipe is circle, and round diameter is 10mm, and described condensate layer 202 is provided with and heat exchanger 402
The heat exchanger of connection；
The upper strata of described condensate layer 202 is provided with mixed layer 203, and mixed layer 203 and flue gas delivery pipe 3 connect, and flue gas is defeated
The flue gas that pipe 3 produces steel mill and the water smoke mixing that condensate layer is produced are sent, described mixed layer is provided with can be by flue gas and water
The well-mixed eddy mixer of mist；
The upper strata of mixed layer 203 is provided with absorbed layer 204, and described absorbed layer 204 and absorbent supplying system connects.
The heat exchanger connection of described heater 602 and condensate layer 202, the heat that can be absorbed condensate layer 202 is passed
It is delivered to heater 602.
Described condensation pipe is made up of heat-conducting polymer material, and described heat-conducting polymer includes：Macromolecule matrix tree
100 parts of fat, 20 parts of heat conducting fiber, 0.5 part of coupling agent, 0.5 part of antioxidant.
At least contain a kind of hydrophobic grouping including at least a kind of in the synthesis material monomer of described macromolecule matrix resin
Monomer.
Described macromolecule matrix resin is PMMA, and described coupling agent is gamma-aminopropyl-triethoxy-silane.
Described heat conducting fiber is short silk carbon fiber, and described antioxidant is diphenylamines, p-phenylenediamine and EEDQ
One kind.
Specific embodiment 2：As shown in figure 1, present embodiment discloses a kind of steel mill energy-saving vulcanizing tower, including absorbent is supplied
Answer system 1, absorption tower 2, flue gas delivery pipe 3, water system 4, gypsum slurries after-treatment device 5, flue gas after-treatment system 6, sky
Letter shoot b；
Described absorbent supplying system 1, flue gas delivery pipe 3, water system 4, gypsum slurries after-treatment device 5, flue gas
After-treatment system 6, air delivery pipe b are connected respectively with absorption tower 2；
Described absorbent supplying system 1 includes batcher 101, nitrator 102, holding vessel 103, air delivery pipe
A104, described batcher 101 is connected with transport vehicle and digester 102, and nitrator 102 and holding vessel 103 connect, holding vessel
103 are connected with absorption tower 2, in described air delivery pipe a104 connections and the pipeline between holding vessel 103 and absorption tower 2.
Described water system includes water pipe 401, heat exchanger 402, and water pipe 401 and heat exchanger 402 connect, heat exchanger 402
Connect with absorption tower 2.
Flue gas after-treatment system 6 includes the top of demister 601, heater 602, the connection of demister 601 and absorption tower 2,
Heater 602 is located at the downstream of demister 601.
The described bottom of absorption tower 2 is provided with structure protruding upward and forms evaporation layer, and in described evaporation layer evaporimeter is provided with
201, it is provided with the filter membrane that can filter out fixed dust between described evaporation layer and the first volume structure on absorption tower 2；
The upper strata of evaporation layer is provided with condensate layer 202, and the condensation pipe of spatial networks is provided with the middle of described condensate layer 202,
The cross section of described condensation pipe is circle, and round diameter is 100mm, and described condensate layer 202 is provided with and heat exchanger 402
The heat exchanger of connection；
The upper strata of described condensate layer 202 is provided with mixed layer 203, and mixed layer 203 and flue gas delivery pipe 3 connect, and flue gas is defeated
The flue gas that pipe 3 produces steel mill and the water smoke mixing that condensate layer is produced are sent, described mixed layer is provided with can be by flue gas and water
The well-mixed eddy mixer of mist；
The upper strata of mixed layer 203 is provided with absorbed layer 204, and described absorbed layer 204 and absorbent supplying system connects.
The heat exchanger connection of described heater 602 and condensate layer 202, the heat that can be absorbed condensate layer 202 is passed
It is delivered to heater 602.
Described condensation pipe is made up of heat-conducting polymer material, and described heat-conducting polymer includes：Macromolecule matrix tree
100 parts of fat, 50 parts of heat conducting fiber, 5 parts of coupling agent, 5 parts of antioxidant.
At least contain a kind of hydrophobic grouping including at least a kind of in the synthesis material monomer of described macromolecule matrix resin
Monomer.
Described macromolecule matrix resin is PS, and described coupling agent is γ-glycidyl ether oxygen propyl trimethoxy silicon
Alkane.
Described heat conducting fiber is copper fiber, and described antioxidant is p-phenylenediamine.
Specific embodiment 3：As shown in figure 1, present embodiment discloses a kind of steel mill energy-saving vulcanizing tower, including absorbent is supplied
Answer system 1, absorption tower 2, flue gas delivery pipe 3, water system 4, gypsum slurries after-treatment device 5, flue gas after-treatment system 6, sky
Letter shoot b；
Described absorbent supplying system 1, flue gas delivery pipe 3, water system 4, gypsum slurries after-treatment device 5, flue gas
After-treatment system 6, air delivery pipe b are connected respectively with absorption tower 2；
Described absorbent supplying system 1 includes batcher 101, nitrator 102, holding vessel 103, air delivery pipe
A104, described batcher 101 is connected with transport vehicle and digester 102, and nitrator 102 and holding vessel 103 connect, holding vessel
103 are connected with absorption tower 2, in described air delivery pipe a104 connections and the pipeline between holding vessel 103 and absorption tower 2.
Described water system includes water pipe 401, heat exchanger 402, and water pipe 401 and heat exchanger 402 connect, heat exchanger 402
Connect with absorption tower 2.
Flue gas after-treatment system 6 includes the top of demister 601, heater 602, the connection of demister 601 and absorption tower 2,
Heater 602 is located at the downstream of demister 601.
The described bottom of absorption tower 2 is provided with structure protruding upward and forms evaporation layer, and in described evaporation layer evaporimeter is provided with
201, it is provided with the filter membrane that can filter out fixed dust between described evaporation layer and the first volume structure on absorption tower 2；
The upper strata of evaporation layer is provided with condensate layer 202, and the condensation pipe of spatial networks is provided with the middle of described condensate layer 202,
The cross section of described condensation pipe is circle, and round diameter is 70mm, and described condensate layer 202 is provided with and heat exchanger 402
The heat exchanger of connection；
The upper strata of described condensate layer 202 is provided with mixed layer 203, and mixed layer 203 and flue gas delivery pipe 3 connect, and flue gas is defeated
The flue gas that pipe 3 produces steel mill and the water smoke mixing that condensate layer is produced are sent, described mixed layer is provided with can be by flue gas and water
The well-mixed eddy mixer of mist；
The upper strata of mixed layer 203 is provided with absorbed layer 204, and described absorbed layer 204 and absorbent supplying system connects.
The heat exchanger connection of described heater 602 and condensate layer 202, the heat that can be absorbed condensate layer 202 is passed
It is delivered to heater 602.
Described condensation pipe is made up of heat-conducting polymer material, and described heat-conducting polymer includes：Macromolecule matrix tree
100 parts of fat, 30 parts of heat conducting fiber, 1 part of coupling agent, 1 part of antioxidant.
At least contain a kind of hydrophobic grouping including at least a kind of in the synthesis material monomer of described macromolecule matrix resin
Monomer.
Described macromolecule matrix resin is nylon 6, and described coupling agent is γ-methacryloxypropyl trimethoxy
Base silane.
Described heat conducting fiber is aluminum fiber, and described antioxidant is diphenylamines.
Specific embodiment 4：As shown in figure 1, present embodiment discloses a kind of steel mill energy-saving vulcanizing tower, including absorbent is supplied
Answer system 1, absorption tower 2, flue gas delivery pipe 3, water system 4, gypsum slurries after-treatment device 5, flue gas after-treatment system 6, sky
Letter shoot b；
Described absorbent supplying system 1, flue gas delivery pipe 3, water system 4, gypsum slurries after-treatment device 5, flue gas
After-treatment system 6, air delivery pipe b are connected respectively with absorption tower 2；
Described absorbent supplying system 1 includes batcher 101, nitrator 102, holding vessel 103, air delivery pipe
A104, described batcher 101 is connected with transport vehicle and digester 102, and nitrator 102 and holding vessel 103 connect, holding vessel
103 are connected with absorption tower 2, in described air delivery pipe a104 connections and the pipeline between holding vessel 103 and absorption tower 2.
Described water system includes water pipe 401, heat exchanger 402, and water pipe 401 and heat exchanger 402 connect, heat exchanger 402
Connect with absorption tower 2.
Flue gas after-treatment system 6 includes the top of demister 601, heater 602, the connection of demister 601 and absorption tower 2,
Heater 602 is located at the downstream of demister 601.
The described bottom of absorption tower 2 is provided with structure protruding upward and forms evaporation layer, and in described evaporation layer evaporimeter is provided with
201, it is provided with the filter membrane that can filter out fixed dust between described evaporation layer and the first volume structure on absorption tower 2；
The upper strata of evaporation layer is provided with condensate layer 202, and the condensation pipe of spatial networks is provided with the middle of described condensate layer 202,
The cross section of described condensation pipe is circle, and round diameter is 10mm, and described condensate layer 202 is provided with and heat exchanger 402
The heat exchanger of connection；
The upper strata of described condensate layer 202 is provided with mixed layer 203, and mixed layer 203 and flue gas delivery pipe 3 connect, and flue gas is defeated
The flue gas that pipe 3 produces steel mill and the water smoke mixing that condensate layer is produced are sent, described mixed layer is provided with can be by flue gas and water
The well-mixed eddy mixer of mist；
The upper strata of mixed layer 203 is provided with absorbed layer 204, and described absorbed layer 204 and absorbent supplying system connects.
The heat exchanger connection of described heater 602 and condensate layer 202, the heat that can be absorbed condensate layer 202 is passed
It is delivered to heater 602.
Described condensation pipe is made up of heat-conducting polymer material, and described heat-conducting polymer includes：Macromolecule matrix tree
100 parts of fat, 50 parts of heat conducting fiber, 0.5 part of coupling agent, 5 parts of antioxidant.
At least contain a kind of hydrophobic grouping including at least a kind of in the synthesis material monomer of described macromolecule matrix resin
Monomer.
Described macromolecule matrix resin is PMMA, PS, one kind of nylon 6, described coupling agent be N- β-（Ammonia second
Base）One kind of-γ-aminopropyltriethoxy dimethoxysilane.
Described heat conducting fiber is aluminum fiber, and described antioxidant is EEDQ.
Specific embodiment 5：As shown in figure 1, present embodiment discloses a kind of steel mill energy-saving vulcanizing tower, including absorbent is supplied
Answer system 1, absorption tower 2, flue gas delivery pipe 3, water system 4, gypsum slurries after-treatment device 5, flue gas after-treatment system 6, sky
Letter shoot b；
Described absorbent supplying system 1, flue gas delivery pipe 3, water system 4, gypsum slurries after-treatment device 5, flue gas
After-treatment system 6, air delivery pipe b are connected respectively with absorption tower 2；
Described absorbent supplying system 1 includes batcher 101, nitrator 102, holding vessel 103, air delivery pipe
A104, described batcher 101 is connected with transport vehicle and digester 102, and nitrator 102 and holding vessel 103 connect, holding vessel
103 are connected with absorption tower 2, in described air delivery pipe a104 connections and the pipeline between holding vessel 103 and absorption tower 2.
Described water system includes water pipe 401, heat exchanger 402, and water pipe 401 and heat exchanger 402 connect, heat exchanger 402
Connect with absorption tower 2.
Flue gas after-treatment system 6 includes the top of demister 601, heater 602, the connection of demister 601 and absorption tower 2,
Heater 602 is located at the downstream of demister 601.
The described bottom of absorption tower 2 is provided with structure protruding upward and forms evaporation layer, and in described evaporation layer evaporimeter is provided with
201, it is provided with the filter membrane that can filter out fixed dust between described evaporation layer and the first volume structure on absorption tower 2；
The upper strata of evaporation layer is provided with condensate layer 202, and the condensation pipe of spatial networks is provided with the middle of described condensate layer 202,
The cross section of described condensation pipe is circle, and round diameter is 100mm, and described condensate layer 202 is provided with and heat exchanger 402
The heat exchanger of connection；
The upper strata of described condensate layer 202 is provided with mixed layer 203, and mixed layer 203 and flue gas delivery pipe 3 connect, and flue gas is defeated
The flue gas that pipe 3 produces steel mill and the water smoke mixing that condensate layer is produced are sent, described mixed layer is provided with can be by flue gas and water
The well-mixed eddy mixer of mist；
The upper strata of mixed layer 203 is provided with absorbed layer 204, and described absorbed layer 204 and absorbent supplying system connects.
The heat exchanger connection of described heater 602 and condensate layer 202, the heat that can be absorbed condensate layer 202 is passed
It is delivered to heater 602.
Described condensation pipe is made up of heat-conducting polymer material, and described heat-conducting polymer includes：Macromolecule matrix tree
100 parts of fat, 20 parts of heat conducting fiber, 5 parts of coupling agent, 0.5 part of antioxidant.
At least contain a kind of hydrophobic grouping including at least a kind of in the synthesis material monomer of described macromolecule matrix resin
Monomer.
Described macromolecule matrix resin is PMMA, described coupling agent be N- β-（Aminoethyl）- γ-aminopropyltriethoxy two
Methoxy silane.
Described heat conducting fiber is short silk carbon fiber, and described antioxidant is diphenylamines.
Relative to the desulfurizer enjoyed, the desulfurized effect of embodiment 1-3 improves more than 20%, cost reduce by 30% with
On.
Preferred embodiment of the present utility model is the foregoing is only, it is all at this not to limit the utility model
Any modification, equivalent and improvement made within the spirit and principle of utility model etc., should be included in the utility model
Protection domain within.
Claims (6)
1. a kind of steel mill energy-saving vulcanizing tower, it is characterised in that including absorbent supplying system（1）, absorption tower（2）, flue gas it is defeated
Send pipe（3）, water system（4）, gypsum slurries after-treatment device（5）, flue gas after-treatment system（6）, air delivery pipe b（7）；
Described absorbent supplying system（1）, flue gas delivery pipe（3）, water system（4）, gypsum slurries after-treatment device（5）、
Flue gas after-treatment system（6）, air delivery pipe b（7）Respectively and absorption tower（2）Connection.
2. steel mill energy-saving vulcanizing tower according to claim 1, it is characterised in that described absorbent supplying system（1）
Including batcher（101）, nitrator（102）, holding vessel（103）, air delivery pipe a（104）, described batcher（101）With
Transport vehicle and digester（102）Connection, nitrator（102）And holding vessel（103）Connection, holding vessel（103）With absorption tower（2）Even
Connect, described air delivery pipe a（104）Connection and holding vessel（103）And absorption tower（2）Between pipeline on.
3. steel mill energy-saving vulcanizing tower according to claim 2, it is characterised in that described water system includes water pipe
（401）, heat exchanger（402）, water pipe（401）And heat exchanger（402）Connection, heat exchanger（402）And absorption tower（2）Connection.
4. steel mill energy-saving vulcanizing tower according to claim 3, it is characterised in that described flue gas after-treatment system（6）
Including demister（601）, heater（602）, demister（601）It is connected to absorption tower（2）Top, heater（602）It is located at
Demister（601）Downstream.
5. steel mill energy-saving vulcanizing tower according to claim 4, it is characterised in that described absorption tower（2）Bottom is provided with
Structure protruding upward forms evaporation layer, and in described evaporation layer evaporimeter is provided with（201）, described evaporation layer and absorption tower（2）
Superstructure between be provided with the filter membrane that can filter out fixed dust；
The upper strata of evaporation layer is provided with condensate layer（202）, described condensate layer（202）Centre is provided with the condensation pipe of spatial networks,
The cross section of described condensation pipe is circle, and round diameter is 10mm-100mm, described condensate layer（202）It is provided with and changes
Hot device（402）The heat exchanger of connection；
Described condensate layer（202）Upper strata be provided with mixed layer（203）, mixed layer（203）And flue gas delivery pipe（3）Connection, cigarette
Letter shoot（3）The water smoke mixing that the flue gas that steel mill is produced and condensate layer are produced, described mixed layer is provided with can be by cigarette
Gas and the well-mixed eddy mixer of water smoke；
Mixed layer（203）Upper strata be provided with absorbed layer（204）, described absorbed layer（204）With absorbent supplying system connection.
6. steel mill energy-saving vulcanizing tower according to claim 5, it is characterised in that described heater（602）And condensation
Layer（202）Heat exchanger connection, can be by condensate layer（202）The heat transfer of absorption is to heater（602）.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620871194.7U CN206138975U (en) | 2016-08-12 | 2016-08-12 | Energy -conserving tower that vulcanizes of steel mill |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620871194.7U CN206138975U (en) | 2016-08-12 | 2016-08-12 | Energy -conserving tower that vulcanizes of steel mill |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206138975U true CN206138975U (en) | 2017-05-03 |
Family
ID=58628391
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620871194.7U Expired - Fee Related CN206138975U (en) | 2016-08-12 | 2016-08-12 | Energy -conserving tower that vulcanizes of steel mill |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206138975U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106076082A (en) * | 2016-08-12 | 2016-11-09 | 攀枝花市九鼎智远知识产权运营有限公司 | A kind of steel mill energy-saving vulcanizing tower |
-
2016
- 2016-08-12 CN CN201620871194.7U patent/CN206138975U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106076082A (en) * | 2016-08-12 | 2016-11-09 | 攀枝花市九鼎智远知识产权运营有限公司 | A kind of steel mill energy-saving vulcanizing tower |
| CN106076082B (en) * | 2016-08-12 | 2018-11-27 | 浙江国正安全技术有限公司 | A kind of steel mill energy-saving vulcanizing tower |
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