CN206384876U - The humidifier of desulfurization wastewater spray evaporation device - Google Patents

The humidifier of desulfurization wastewater spray evaporation device Download PDF

Info

Publication number
CN206384876U
CN206384876U CN201621446497.0U CN201621446497U CN206384876U CN 206384876 U CN206384876 U CN 206384876U CN 201621446497 U CN201621446497 U CN 201621446497U CN 206384876 U CN206384876 U CN 206384876U
Authority
CN
China
Prior art keywords
kuppe
inlet pipe
humidifier
desulfurization wastewater
double
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.)
Expired - Fee Related
Application number
CN201621446497.0U
Other languages
Chinese (zh)
Inventor
杨丽杰
朱跃
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Yi Gong Chen (tianjin) Energy Saving Environmental Protection Technology Development Co Ltd
Original Assignee
Yi Gong Chen (tianjin) Energy Saving Environmental Protection Technology Development Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Yi Gong Chen (tianjin) Energy Saving Environmental Protection Technology Development Co Ltd filed Critical Yi Gong Chen (tianjin) Energy Saving Environmental Protection Technology Development Co Ltd
Priority to CN201621446497.0U priority Critical patent/CN206384876U/en
Application granted granted Critical
Publication of CN206384876U publication Critical patent/CN206384876U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Treating Waste Gases (AREA)

Abstract

The utility model discloses a kind of humidifier of desulfurization wastewater spray evaporation device, including, input pipe, it includes L-shaped water inlet pipe and the L-shaped air inlet pipe being co-axially located on the outside of described water inlet pipe, Double-fluid atomization nozzle, and it is fixedly installed on described input tube end and corresponding with described air inlet pipe and water inlet pipe turned on, kuppe, it is fixedly installed on described input pipe, is flowed from front to back with flue gas, and described Double-fluid atomization nozzle is arranged on described kuppe rear.The utility model uses Double-fluid atomization nozzle, it produces atomizing effect using the liquid collision of precession, the intake channel and spout of gas and liquid are all than larger, it effectively prevent the problem of outlet is blocked, and Double-fluid atomization nozzle spraying range is big, effectively improves atomization process effect, while setting kuppe at Double-fluid atomization nozzle rear portion, it is avoided that after atomization that liquid just converges without scattering with flue gas, improves atomization mixed effect.

Description

The humidifier of desulfurization wastewater spray evaporation device
Technical field
The utility model is related to fume treatment technical field, more particularly to a kind of spray of desulfurization wastewater spray evaporation device Mist mechanism.
Background technology
Lime stone-gypsum wet flue gas desulfurizing system is the desulphurization system being most widely used, and can be produced during the system operation Raw a certain amount of desulfurization wastewater.Desulfurization wastewater processing in the country's generally uses three header techniques at present, although three header techniques have Preferable treatment effect, technique relative maturity, but the system of three header techniques is complex, operating cost is higher, especially Can not effectively remove containing high concentration chlorion, and in order to ensure desulphurization system desulfurization normal table carry out, it is necessary to allow Chlorine ion concentration ensures that in below 20000ppm this, which allows for processing water outlet, can not carry out reuse, and the sludge produced is present Secondary pollution problems.
Effectively to remove chlorion, coal-burning power plant typically uses desulfurization wastewater spray evaporation device, passes through desulfurization wastewater Being capable of reuse, i.e., the flue sprayed into desulfurization wastewater between air preheater and electrostatic precipitator using atomizer after processing It is interior, evaporated by high-temperature flue gas and cause the pollutant in waste water and salinity crystallization and the removal in follow-up cleaner, evaporation Vapor in the desulfuration absorbing tower in downstream condensed entrance desulphurization absorption tower system, it is achieved thereby that recycling.
But, existing humidifier is easy to block, or even fouling, influences atomization process effect, then influences The normal operation of system.
Utility model content
The purpose of this utility model is to be directed to technological deficiency present in prior art, and provides a kind of desulfurization wastewater spraying The humidifier of vaporising device.
To realize that the technical scheme that the purpose of this utility model is used is:
A kind of humidifier of desulfurization wastewater spray evaporation device, including,
Input pipe, it includes L-shaped water inlet pipe and the L-shaped air inlet pipe being co-axially located on the outside of described water inlet pipe,
Double-fluid atomization nozzle, its be fixedly installed on described input tube end and with described air inlet pipe and water inlet pipe pair It should turn on,
Kuppe, it is fixedly installed on described input pipe, flowed from front to back with flue gas, described twin Shower nozzle is arranged on described kuppe rear.
Described kuppe includes the vertical baffle being fixedly connected with described input pipe, and is integrally formed in described erect Straight baffle plate periphery and side retaining ring horizontal-extending backward.
Described kuppe is semielliptical shape or half rugby shape.
Described kuppe is triangular pyramid or polygonal pyramid shape.
The front side root of described kuppe is provided with purge hole to purge kuppe windward in described air inlet pipe Face.
Described air inlet pipe is connected through the air pump flue anterior with preheater.
Compared with prior art, the beneficial effects of the utility model are:
The utility model uses Double-fluid atomization nozzle, its using precession liquid collision produce atomizing effect, gas and The intake channel and spout of liquid all than larger, effectively prevent the problem of outlet is blocked, and Double-fluid atomization nozzle sprays Spill scope big, effectively improve atomization process effect, while setting kuppe at Double-fluid atomization nozzle rear portion, be avoided that after atomization Liquid just converges without scattering with flue gas, increases the scope of dispersing of atomizing particle, improves atomization mixed effect.Meanwhile, utilize Kuppe it also avoid the right backward preceding fouling progressively extended of Double-fluid atomization nozzle, and reducing blocking may.
Brief description of the drawings
Fig. 1 show the structure of the first embodiment of the humidifier of desulfurization wastewater spray evaporation device of the present utility model Schematic diagram.
Fig. 2 show the structure of the second embodiment of the humidifier of desulfurization wastewater spray evaporation device of the present utility model Schematic diagram.
Embodiment
The utility model is described in further detail below in conjunction with the drawings and specific embodiments.It should be appreciated that this place The specific embodiment of description only to explain the utility model, is not used to limit the utility model.
As depicted in figs. 1 and 2, the humidifier of desulfurization wastewater spray evaporation device of the present utility model includes,
Input pipe 1, Double-fluid atomization nozzle 2 and kuppe 3, input pipe 1 include L-shaped water inlet pipe 11 and are co-axially located at institute The side wall and horizontal part of flue are run through with being axially parallel arranged in the L-shaped air inlet pipe 12 in the outside of water inlet pipe 11 stated, vertical portion In flue, Double-fluid atomization nozzle is arranged on horizontal part end, wherein, water inlet pipe and air inlet pipe are coaxially disposed, and inside is water inlet Passage, is inlet channel between water inlet pipe and air inlet pipe, air inlet pipe and compressed gas or to pass through air pump and preheater anterior Flue is connected, and the waste water after water inlet pipe and desulfurization, filtering is by the pipeline connection with the pump housing, using the structure of water in outer gas, Outside gas cooling can be heated to internal water in course of conveying, the drop temperature so after atomization and cigarette in flue Gas temperature-difference is little, it is easy to be combined into particle, lifts dust removing effects.
Double-fluid atomization nozzle 2 is fixedly installed on described input tube end and corresponding with described air inlet pipe and water inlet pipe Conducting, kuppe 3 is fixedly installed on described input pipe, is flowed from front to back with flue gas, then the spray of described twin Head is arranged on described kuppe rear.
The utility model uses Double-fluid atomization nozzle, its using precession liquid collision produce atomizing effect, gas and The intake channel of liquid all than larger, effectively prevent the problem of outlet is blocked, and Double-fluid atomization nozzle spraying range Greatly, effectively improve atomization process effect, while set kuppe at Double-fluid atomization nozzle rear portion, described water conservancy diversion cover opening to Afterwards and kuppe open side width flue width a quarter to 1/2nd, preferably 1/3rd, using kuppe, It is avoided that after atomization that liquid just converges without scattering with flue gas, increases the scope of dispersing of atomizing particle, improves atomization mixing effect Really.Meanwhile, the right backward preceding fouling progressively extended of Double-fluid atomization nozzle is it also avoid using kuppe, reducing blocking may.
As embodiment, as shown in figure 1, described kuppe is perpendicular including what is be fixedly connected with described input pipe Straight baffle plate, and it is integrally formed in described vertical baffle periphery and side retaining ring horizontal-extending backward, or as shown in Fig. 2 institute The kuppe stated is semielliptical or half rugby shape, and certainly described kuppe is alternatively other cavity structures, such as triangular pyramid or Polygonal pyramid shape, using cavate, hood configuration, the flue gas that should be purged to Double-fluid atomization nozzle rear portion is blocked into water conservancy diversion makes its point Dissipate, accelerate local velocity, the mixed effect of the atomized liquid sprayed with Double-fluid atomization nozzle is improved using its injection effect.
Further, to avoid the trailing flank of kuppe, i.e. windward side from dust stratification even fouling occur, in described air inlet pipe The front side root of described kuppe is provided with purge hole 4 to purge the windward side of kuppe, set in described purging orifice ring week Put and be blown to kuppe trailing flank in tangential direction, relatively rapid or clean purge gas can kuppe windward side structure Into similar air cushion Rotating fields, it is to avoid dirt accumulation, while also can effectively reduce stop of the kuppe to flue gas.
Described above is only preferred embodiment of the present utility model, it is noted that for the general of the art For logical technical staff, on the premise of the utility model principle is not departed from, some improvements and modifications can also be made, these change Enter and retouch and also should be regarded as protection domain of the present utility model.

Claims (6)

1. a kind of humidifier of desulfurization wastewater spray evaporation device, it is characterised in that including,
Input pipe, it includes L-shaped water inlet pipe and the L-shaped air inlet pipe being co-axially located on the outside of described water inlet pipe,
Double-fluid atomization nozzle, it is fixedly installed on described input tube end and corresponding with described air inlet pipe and water inlet pipe led It is logical,
Kuppe, it is fixedly installed on described input pipe, flowed from front to back with flue gas, described Double-fluid atomization nozzle It is arranged on described kuppe rear.
2. the humidifier of desulfurization wastewater spray evaporation device as claimed in claim 1, it is characterised in that described kuppe Including the vertical baffle being fixedly connected with described input pipe, and it is integrally formed in described vertical baffle periphery and backward level The side retaining ring of extension.
3. the humidifier of desulfurization wastewater spray evaporation device as claimed in claim 1, it is characterised in that described kuppe For semielliptical shape or half rugby shape.
4. the humidifier of desulfurization wastewater spray evaporation device as claimed in claim 1, it is characterised in that described kuppe For triangular pyramid or polygonal pyramid shape.
5. the humidifier of desulfurization wastewater spray evaporation device as claimed in claim 1, it is characterised in that in described air inlet The front side root of kuppe described in Guan Yu is provided with purge hole to purge the windward side of kuppe.
6. the humidifier of desulfurization wastewater spray evaporation device as claimed in claim 1, it is characterised in that described air inlet pipe Connected through the air pump flue anterior with preheater.
CN201621446497.0U 2016-12-27 2016-12-27 The humidifier of desulfurization wastewater spray evaporation device Expired - Fee Related CN206384876U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201621446497.0U CN206384876U (en) 2016-12-27 2016-12-27 The humidifier of desulfurization wastewater spray evaporation device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201621446497.0U CN206384876U (en) 2016-12-27 2016-12-27 The humidifier of desulfurization wastewater spray evaporation device

Publications (1)

Publication Number Publication Date
CN206384876U true CN206384876U (en) 2017-08-08

Family

ID=59490986

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201621446497.0U Expired - Fee Related CN206384876U (en) 2016-12-27 2016-12-27 The humidifier of desulfurization wastewater spray evaporation device

Country Status (1)

Country Link
CN (1) CN206384876U (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110015798A (en) * 2019-04-08 2019-07-16 上海电力学院 Desulfurizing waste water processing device applied to coal-burning power plant
CN114956239A (en) * 2022-06-21 2022-08-30 国家电投集团重庆合川发电有限公司 Desulfurization wastewater treatment device

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110015798A (en) * 2019-04-08 2019-07-16 上海电力学院 Desulfurizing waste water processing device applied to coal-burning power plant
CN114956239A (en) * 2022-06-21 2022-08-30 国家电投集团重庆合川发电有限公司 Desulfurization wastewater treatment device
CN114956239B (en) * 2022-06-21 2024-01-26 国家电投集团重庆合川发电有限公司 Desulfurization waste water treatment device

Similar Documents

Publication Publication Date Title
CN206285660U (en) The tower desulfurization wastewater spray evaporation device of drying and flue gas processing device
CN208008493U (en) A kind of equipment that flue residue heat is used for Waste Water From Fire Power Plant zero discharge treatment
CN106512456B (en) A kind of four sections of method vaporising devices and method of desulfurization wastewater
CN106348373A (en) Wastewater evaporation equipment and wastewater treatment method and device
CN107140777A (en) A kind of desulfurization wastewater zero discharge treatment device and its processing method
CN206384876U (en) The humidifier of desulfurization wastewater spray evaporation device
CN105597483A (en) Device and method for removing vapor dissolved particles by virtue of wet desulphurization exhaust gas cooling method
CN202902317U (en) Single-body multi-stage cremator tail gas purifying device
CN109133234A (en) A kind of desulfurization wastewater Zero discharging system
CN208574404U (en) A kind of industrial fumes cleaning equipment
CN104801165A (en) Three-stage dust removal and desulphurization device
CN104841256B (en) A kind of boiler smoke treatment zero draining system and method
CN206375693U (en) The humidifier and flue spray evaporation device of good antiscale property
CN108706671A (en) A kind of desulfurization wastewater self-preheating type evaporation technology using sintering machine high-temperature flue gas
CN205340545U (en) Smoke and dust deacidification dust removal processing apparatus
CN206285659U (en) Outer processing formula desulfurization wastewater spray evaporation device
CN207918472U (en) A kind of waste water from power plant device
CN110455090A (en) A kind of efficient swirling flow atomizing desulfurization and dust-removal method
CN106693511A (en) Power plant flue gas treatment device
CN205659522U (en) Desorption acid gas's cooling tower
CN206103607U (en) Split type energy -saving SOx/NOx control dust collecting equipment
CN206508663U (en) Power-plant flue gas processing unit
CN209952568U (en) Wet flue desulfurization waste water flue sprays evaporation zero release processing system
CN206872600U (en) A kind of desulfurization wastewater zero discharge treatment device
CN107803125B (en) Combined gas-liquid fusion device of serial venturi tube

Legal Events

Date Code Title Description
GR01 Patent grant
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: 20170808

Termination date: 20181227