CN206793376U - A kind of cycle detection desulfuration spray tower - Google Patents
A kind of cycle detection desulfuration spray tower Download PDFInfo
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- CN206793376U CN206793376U CN201720491518.9U CN201720491518U CN206793376U CN 206793376 U CN206793376 U CN 206793376U CN 201720491518 U CN201720491518 U CN 201720491518U CN 206793376 U CN206793376 U CN 206793376U
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- layer
- gas
- spray tower
- cycle detection
- desulfurization
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Abstract
A kind of cycle detection desulfuration spray tower, built in gas tank have gas detecting instrument, and gas detecting instrument detects gas in air accumulator, if meeting discharge standard, are just discharged normal through air outlet outdoor；If discharge standard is not met, gas detecting instrument sends a signal to controller, controller opens valve, because valve and fan series connection, valve energization is opened aft-fan and also run simultaneously, gas in air accumulator is pumped to current-sharing module by pipeline 17, handled again again, until meeting gas discharge standard.
Description
Technical field
It the utility model is related to spray column, and in particular to the desulfuration spray tower recycled after a kind of detection.
Background technology
With the gradual enhancing of the environmental protection of the mankind, the mankind become more concerned with the quality of living environment around.Industry row
Contained hydrogen sulfide or sulfur dioxide gas, can not only cause the poisoning of pipeline and catalyst, cause work in the waste gas put
The corrosion of skill worsening condition, equipment, and quite serious environmental pollution can be caused, or even endanger human survival.Therefore, it is necessary to
The hydrogen sulfide or sulfur dioxide gas of discharge are administered.Hydrogen sulfide gas is a kind of air for increasingly causing the whole world to be paid attention to
Pollution nuisance, it is typical stench class gas, has that pollution range is very wide, far-reaching feature.And the process handled
The unnet waste gas of middle processing is easily together emitted into air with moisture in air, causes secondary pollution, caused in processes
Contain a large amount of impurity in waste water, it is very big to cause loss to equipment during water pump conveys, and treated
Cheng Zhong, air inlet waste gas is disorderly, greatly reduces treatment effeciency.Processing equipment in the market is in result without tight
Lattice control, there is very big probability to cause to handle imperfection, absorption is insufficient, so as to which the gas for causing to emit still contains
A small amount of harmful substance, the purpose of elimination can not be reached.
Utility model content
Technical problem to be solved in the utility model is to be directed to the above-mentioned state of the art, and providing one kind can preferably be handled
Sulphur-containing exhaust gas, and can preferably guarantee processing after gas meet discharge standard, prevent secondary pollution, caused waste water can
To focus on.Gas componant can be discharged by strict control, be then exhausted from after meeting discharge standard.
Technical scheme is used by the utility model solves above-mentioned technical problem：
A kind of cycle detection desulfuration spray tower, including air inlet and air outlet, it is characterised in that：The air inlet and air-out
Current-sharing module, the first desulfurization of pretreatment module layer, the second desulfurization layer, demisting layer and air accumulator are sequentially provided between mouthful；Described
One desulfurization layer and the second desulfurization layer inwall surrounding are equipped with spraying layer；It is all provided with the first desulfurization layer and the second desulfurization layer
There are multiple fillers；The spraying layer is connected on water pump by water pipe, water pump and pharmacy jar connection；It is suitable in the pretreatment module
Gas flow direction and be provided with multiple hollow-fibre membranes, and gas must be by that could enter the first desulfurization after hollow-fibre membrane
Layer；Collecting pit is provided with below the first desulfurization layer, the second desulfurization layer and demisting layer；The collecting pit connection has delivery port；Institute
Air accumulator is stated by pipeline with current-sharing module to couple；Fan is provided with the pipeline；The built in gas tank has gas detecting instrument；
The gas detecting instrument couples with controller；The pipe ends are equipped with valve；The controller couples with valve；The wind
Fan is connected with valve.
Further, the current-sharing module is provided with multiple airflow holes.
Further, the first desulfurization layer, the second desulfurization layer outside are equipped with observation window.
Further, it is a plurality of serpentine channel in the demisting layer.
Further, the hollow-fibre membrane is horizontal positioned along gas flow direction.
Further, the filler is spherical ceramic material.
Further, the pharmacy jar is built with sodium hydroxide.
Yet further, the spraying layer is made up of multiple atomizers.
The beneficial effects of the utility model are：Current-sharing module is provided with multiple apertures, before turbulent gas into devices,
Entering gas by current equalizer, aftertreatment device mobility is more stable, and reaction is more abundant, and then the best of it
Manage effect.Spherical ceramic packing specific area is big, and strong adsorption force, more for handling the waste gas such as benzene,toluene,xylene, stench
Secondary treatment by stages reaches processing highest standard, and guarantee reaches discharge standard.A plurality of serpentine channel is provided with demisting layer when aqueous
Gas gas enters inside demister, encounters wall in the serpentine channel of complications, vapor adhesion in being accumulated to constant weight above,
Bottom is flowed to along demisting dividing plate under gravity to be collected, and then the effect of demisting, it can equally reach
The effect of even air-flow.Provided with the first desulfurization layer and the second desulfurization layer, the further sulfide adsorbed in waste gas, pretreatment module
In be provided with multiple hollow-fibre membranes, waste gas can be prevented the advance filtration treatment of the impurity of big particle diameter thick by hollow-fibre membrane
Bulky grain is deposited in water, adds equipment loss during wastewater treatment.Collecting pit is provided with below equipment, can be by the molten of absorption
Liquid and water droplet are concentrated through delivery port discharge, and concentration is drained into sewage treatment equipment to be handled again.Observation window can facilitate
Staff checks filler state, can change and clear up in time after adsorption saturation.Built in gas tank has gas detecting instrument, gas
Gas in body detector detection air accumulator, if meeting discharge standard, just discharged normal through air outlet outdoor；If do not meet
Discharge standard, gas detecting instrument send a signal to controller, and controller opens valve, because valve and fan series connection, valve
The opening that is powered aft-fan is also run simultaneously, and the gas in air accumulator is pumped to current-sharing module by pipeline, entered again again
Row processing, until meeting gas discharge standard.
Brief description of the drawings
Fig. 1 is external structure schematic diagram of the present utility model；
Fig. 2 is pretreatment module perspective view.
Mark explanation：Air inlet 1, air outlet 2, the first desulfurization layer 3, the second desulfurization layer 4, demisting layer 5, spraying layer 6, flow
Module 7, pretreatment module 8, filler 9, observation window 10, collecting pit 11, delivery port 12, water pump 13, pharmacy jar 14, hollow-fibre membrane
15th, air accumulator 16, pipeline 17, fan 18.
Embodiment
Embodiment of the present utility model is described in further detail below in conjunction with accompanying drawing.
As depicted in figs. 1 and 2, waste gas is entered in equipment by air inlet 1, by current-sharing module 7, is set in current-sharing module 7
There are multiple airflow holes, before turbulent gas into devices, gas is entered aftertreatment device mobility by current equalizer
More stable, reaction is more abundant, and then optimization process effect.Waste gas enters pretreatment module after passing through current-sharing module 7
8, pretreatment module 8 is interior to be provided with multiple hollow-fibre membranes 15, and gas must be by that could enter first after hollow-fibre membrane 15
The material of big particle diameter is filtered, prevents big particle to be deposited in water, add wastewater treatment by desulfurization layer 3, hollow-fibre membrane 15
When equipment loss, subsequent waste gas enter after just considering in the first desulfurization layer 3, and water pump 13 is run, by the hydrogen in pharmacy jar 14
Sodium oxide molybdena, which is pumped to spraying layer 6, to be sprayed, and spraying layer 6 is made up of atomizer, by solution atomization, increase and the contact surface of waste gas
Product, reach the sulfurous gas maximized in absorption waste gas；Filler 9 is that spherical ceramic packing specific area is big, and strong adsorption force, is used
In waste gas such as processing benzene,toluene,xylene, stenches, then enter back into the second desulfurization layer 4 and handled again, repeatedly stage by stage
Processing reaches processing highest standard, and guarantee reaches discharge standard, and gas up to standard enters demisting layer 5, is a plurality of snakelike in demisting layer 5
Passage, encounter wall in the serpentine channel of complications, vapor adhesion in being accumulated to constant weight above, edge under gravity
Demisting dividing plate and flow to lower section pond and be collected, and then the effect of demisting can equally reach the effect of uniform air flow.
First desulfurization layer 3, the second desulfurization layer 4 and the lower section of demisting layer 5 UNICOM are to collecting pit 11, by the waste water after absorption and condensed
Water is delivered to sewage treatment equipment by the concentration of delivery port 12 and focused on, and saves batch processing link, reduces into
This expenditure.Gas detecting instrument is provided with air accumulator 16, gas detecting instrument detects gas in air accumulator 16, if meeting discharge mark
Standard, just discharge outdoor normal through air outlet 2；If not meeting discharge standard, gas detecting instrument sends a signal to controller, control
Device processed opens valve, because valve and fan 18 are connected, valve energization is opened aft-fan 18 and also run simultaneously, by air accumulator
Gas pumped by pipeline 17 to current-sharing module, handled again again, until meet gas discharge standard.
It the above is only preferred embodiment of the present utility model, the scope of protection of the utility model is not limited merely to above-mentioned
Embodiment, all technical schemes belonged under the utility model thinking belong to the scope of protection of the utility model.It should be pointed out that pair
For those skilled in the art, some improvements and modifications under the premise of the utility model principle is not departed from,
It should be regarded as the scope of protection of the utility model.
Claims (8)
1. a kind of cycle detection desulfuration spray tower, including air inlet（1）And air outlet（2）, it is characterised in that：The air inlet
（1）And air outlet（2）Between be sequentially provided with current-sharing module（7）, pretreatment module（8）First desulfurization layer（3）, the second desulfurization layer
（4）, demisting layer（5）And air accumulator（16）；The first desulfurization layer（3）With the second desulfurization layer（4）Inwall surrounding is equipped with spray
Layer（6）；The first desulfurization layer（3）With the second desulfurization layer（4）Inside it is equipped with multiple fillers（9）；The spraying layer（6）Pass through water
Pipe is connected in water pump（13）On, water pump（13）And pharmacy jar（14）Connection；The pretreatment module（8）It is interior along gas flowing side
To provided with multiple hollow-fibre membranes（15）, and gas must pass through hollow-fibre membrane（15）After could enter the first desulfurization layer（3）；
The first desulfurization layer（3）, the second desulfurization layer（4）With demisting layer（5）Lower section is provided with collecting pit（11）；The collecting pit（11）Connection
It is connected to delivery port（12）；The air accumulator（16）Pass through pipeline（17）With current-sharing module（7）Connection；The pipeline（17）Inside it is provided with
Fan（18）；The air accumulator（16）It is interior to be provided with gas detecting instrument；The gas detecting instrument couples with controller；The pipeline
（17）Both ends are equipped with valve；The controller couples with valve；The fan（18）Connected with valve.
A kind of 2. cycle detection desulfuration spray tower as claimed in claim 1, it is characterised in that：The current-sharing module（7）On set
There are multiple airflow holes.
A kind of 3. cycle detection desulfuration spray tower as claimed in claim 1, it is characterised in that：The first desulfurization layer（3）,
Two desulfurization layers（4）Outside is equipped with observation window（10）.
A kind of 4. cycle detection desulfuration spray tower as claimed in claim 1, it is characterised in that：The demisting layer（5）Interior is more
Bar serpentine channel.
A kind of 5. cycle detection desulfuration spray tower as claimed in claim 1, it is characterised in that：The hollow-fibre membrane（15）It is suitable
It is horizontal positioned gas flow direction.
A kind of 6. cycle detection desulfuration spray tower as claimed in claim 1, it is characterised in that：The filler（9）For spherical pottery
Porcelain material.
A kind of 7. cycle detection desulfuration spray tower as claimed in claim 1, it is characterised in that：The pharmacy jar（14）Built with
Sodium hydroxide.
A kind of 8. cycle detection desulfuration spray tower as claimed in claim 1, it is characterised in that：The spraying layer（6）By multiple
Atomizer is formed.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720491518.9U CN206793376U (en) | 2017-05-05 | 2017-05-05 | A kind of cycle detection desulfuration spray tower |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720491518.9U CN206793376U (en) | 2017-05-05 | 2017-05-05 | A kind of cycle detection desulfuration spray tower |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206793376U true CN206793376U (en) | 2017-12-26 |
Family
ID=60738274
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720491518.9U Expired - Fee Related CN206793376U (en) | 2017-05-05 | 2017-05-05 | A kind of cycle detection desulfuration spray tower |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206793376U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109364727A (en) * | 2018-11-29 | 2019-02-22 | 黄冬艳 | Hazardous chemical production gas sampling processing unit |
| CN110102164A (en) * | 2019-04-22 | 2019-08-09 | 攀枝花市蓝鼎环保科技有限公司 | Wet desulfurizing process for high sulfur concentration flue gas |
| CN113578013A (en) * | 2021-07-30 | 2021-11-02 | 汪雯雯 | Environment-friendly industrial waste gas purifies uses low temperature plasma SOx/NOx control device |
-
2017
- 2017-05-05 CN CN201720491518.9U patent/CN206793376U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109364727A (en) * | 2018-11-29 | 2019-02-22 | 黄冬艳 | Hazardous chemical production gas sampling processing unit |
| CN110102164A (en) * | 2019-04-22 | 2019-08-09 | 攀枝花市蓝鼎环保科技有限公司 | Wet desulfurizing process for high sulfur concentration flue gas |
| CN113578013A (en) * | 2021-07-30 | 2021-11-02 | 汪雯雯 | Environment-friendly industrial waste gas purifies uses low temperature plasma SOx/NOx control device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20171226 Termination date: 20210505 |