CN209501966U - A kind of wet-esp temperature rising integrated device - Google Patents

A kind of wet-esp temperature rising integrated device Download PDF

Info

Publication number
CN209501966U
CN209501966U CN201920165227.XU CN201920165227U CN209501966U CN 209501966 U CN209501966 U CN 209501966U CN 201920165227 U CN201920165227 U CN 201920165227U CN 209501966 U CN209501966 U CN 209501966U
Authority
CN
China
Prior art keywords
electric field
field region
layer electric
lower layer
upper layer
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.)
Active
Application number
CN201920165227.XU
Other languages
Chinese (zh)
Inventor
罗炜
蔡幼兰
黄明杰
寇向上
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.)
Fujian Longking Co Ltd.
Original Assignee
Fujian Longking 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 Fujian Longking Co Ltd. filed Critical Fujian Longking Co Ltd.
Priority to CN201920165227.XU priority Critical patent/CN209501966U/en
Application granted granted Critical
Publication of CN209501966U publication Critical patent/CN209501966U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Abstract

The utility model discloses a kind of wet-esp temperature rising integrated devices, including upper layer electric field region and lower layer electric field region, and the deflector for separating and flue gas is allowed to pass through upper layer and lower layer electric field region is equipped between the upper layer electric field region and lower layer electric field region;The upper layer electric field region and lower layer electric field region include cathode hanger, dust collecting electrode and cathode line, and the dust collecting electrode is equipped in the exhaust gases passes of honeycomb distribution on cross section, and the wall portion of each hexagon exhaust gases passes is formed by several remover of conductive glass steel tube permutation and combination;The remover of conductive glass steel tube is connected with steam pipework, heats up under working condition in dedusting, the remover of conductive glass steel tube of the upper layer electric field region is passed through steam, and the remover of conductive glass steel tube of the lower layer electric field region is not passed through steam.The device can be condensed and be heated in wet electrical dust precipitator operational process, while to flue gas, achieve the effect that reduce deduster follow-up equipment " except white ", substantially reduce cost of investment.

Description

A kind of wet-esp temperature rising integrated device
Technical field
The utility model relates to technical field of dust removal equipment, especially wet-esp temperature rising integrated device.
Background technique
Wet electrical dust precipitator is a kind of for handling the cleaner containing micro dust and microparticle, but can also be cooled down simultaneously Cooling gas and the humidity for increasing discharge gas, wet flue gas direct emission can generate " white haze ".
Currently, in order to solve " white haze " phenomenon, as shown in Figure 1, can wet electrical dust precipitator 1 ' afterwards installation condenser 2 ' and Low low-level (stack-gas) economizer system 3 ' (MGGH), after wet electrical dust precipitator 1 ', flue-gas temperature reduces flue gas, and humidity increases, and passes through Condenser 2 ' is by the condensate moisture in flue gas, while flue-gas temperature reduces 3-5 DEG C, and flue gas is using low low-level (stack-gas) economizer system later System 3 ', flue gas heating, then flue gas is discharged through chimney 4 ', reaches the requirement of the discharge " except white ".
But condenser and low low-level (stack-gas) economizer system are set on the subsequent emission path of wet electrical dust precipitator, not only Building block is more, the device is complicated, takes up a large area, moreover, cost of investment will also greatly increase.
Utility model content
The purpose of the utility model is to provide a kind of wet-esp temperature rising integrated devices.The device can be in wet type electricity In deduster operational process, while flue gas is condensed and heated, achieved the effect that " except white ", reduces that deduster is subsequent to be set It is standby, substantially reduce cost of investment.
To achieve the above object, the utility model provides a kind of wet-esp temperature rising integrated device, including upper layer electricity Place and lower layer electric field region are equipped between the upper layer electric field region and lower layer electric field region and upper layer and lower layer electric field region are separated and allowed The deflector that flue gas passes through;The upper layer electric field region and lower layer electric field region include cathode hanger, dust collecting electrode and cathode line, described Dust collecting electrode is equipped in the exhaust gases passes of honeycomb distribution on cross section, and the wall portion of each hexagon exhaust gases passes is by several conductions Glass reinforced plastic pipe permutation and combination is formed;The remover of conductive glass steel tube heats up under operating condition for being passed through steam in dedusting, the upper layer electricity The remover of conductive glass steel tube of place is in the state for being passed through steam, and the remover of conductive glass steel tube of the lower layer electric field region, which is in, is not passed through steaming The state of vapour.
Preferably, the deflector includes lower layer's deflector and upper layer deflector;Lower layer's deflector has crest portion Position and trough position, and be open at wave crest position equipped with flue gas;The upper layer deflector includes the shutter in inverted " v ", respectively The shutter be arranged in the flue gas overthe openings of lower layer's deflector and between lower layer's deflector there are Away to form the exhaust gases passes with dog leg path.
Preferably, front-rear direction of the deflector at the wave crest position and trough position for being parallel to lower layer's deflector Upper inclination arrangement.
Preferably, the inner walls sealing welding at the both ends of the deflector and the upper layer electric field region and lower layer electric field region Connection, the shell are equipped with rhone in the lowest part of the deflector.
Preferably, the length of the dust collecting electrode and cathode line of the lower layer electric field region is greater than the dust collecting electrode of the upper layer electric field region With the length of cathode line.
Preferably, in the case where upper layer electric field region sprays operating condition, the remover of conductive glass steel tube of the upper layer electric field region, which is in, not to be passed through The state of steam, the remover of conductive glass steel tube of the lower layer electric field region are in the state for being passed through steam.
Preferably, in the case where lower layer electric field region sprays operating condition, the remover of conductive glass steel tube of the upper layer electric field region, which is in, is passed through steaming The state of vapour, the remover of conductive glass steel tube of the lower layer electric field region are in the state for not being passed through steam.
Preferably, the remover of conductive glass steel tube is 2205 two-phase alloys pipes.
Preferably, the cathode hanger of the upper layer electric field region and lower layer electric field region is arranged in the side of its shell.
Preferably, the top of the upper layer electric field region is equipped with flue gas pooled portion, and cigarette is equipped in the flue gas pooled portion Gas outlet.
Increase the problem of many costs of investment for above-mentioned wet electrical dust precipitator follow-up equipment, the utility model devises one Kind of wet-esp temperature rising integrated device both can effectively solve low flue-gas temperature after wet electrical dust precipitator and subsequent flue, cigarette The problem of chimney low-temperature corrosion, and can solve " white haze " phenomenon that wet flue gas discharge generates, while not having in wet electrical dust precipitator The equipment such as condenser and MGGH are set afterwards, to substantially reduce cost of investment.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of wet electrical dust precipitator subsequent installation condenser and low low-level (stack-gas) economizer system;
Fig. 2 is a kind of structural representation of wet-esp temperature rising integrated device disclosed in the utility model embodiment Figure;
Fig. 3 is the partial enlarged view at the position A in Fig. 2;
Fig. 4 is the top view of single dust collecting electrode;
Fig. 5 is the structural schematic diagram that single hexagon exhaust gases passes are formed by remover of conductive glass steel tube permutation and combination;
In Fig. 1:
Low 3 ' the chimney 4 ' of low-level (stack-gas) economizer system of 1 ' condenser of wet electrical dust precipitator 2 '
Fig. 2 is into Fig. 4:
1. 2. lower layer electric field region of upper layer electric field region, 3. deflector, 31. lower layer's deflector, 32. upper layer deflector, 33. cigarette Gas opening 4. cathode hanger, 5. dust collecting electrode, 51. remover of conductive glass steel tube, 511. modular construction, 6. cathode line, 7. flue gas collects 8. exhanst gas outlet of portion
Specific embodiment
In order to make those skilled in the art better understand the scheme of the utility model, with reference to the accompanying drawing and specific implementation The utility model is described in further detail for mode.
Herein, the terms such as " front, rear, left and right " are positional relationships based on the figure and establishment, with reference to the accompanying drawings Difference, corresponding positional relationship is also possible to change therewith, therefore, can not be understood as to the exhausted of protection scope To restriction;Moreover, the relational terms of such as " first " and " second " or the like are used merely to one with another with identical The component of title distinguishes, without necessarily requiring or implying between these components there are any this actual relationship or Sequentially.
Referring to FIG. 2, Fig. 2 is a kind of wet-esp temperature rising integrated device disclosed in the utility model embodiment Structural schematic diagram.
As shown, in a specific embodiment, wet-esp heating integration provided by the utility model The inside of device is divided into upper layer electric field region 1 and lower layer electric field region 2, and upper layer electric field region 1 and lower layer electric field region 2 are mutually independent system System is arranged deflector 3 among upper layer and lower layer electric fields, upper layer and lower layer electric field system is separated, during flue gas is passed through through lower layer electric field region 2 Between deflector 3 toward upper layer electric field region 1 flow into.
Upper layer electric field region 1 and lower layer electric field region 2 include cathode hanger 4, dust collecting electrode 5 and cathode line 6, wherein cathode is hung It hangs 4 and is arranged in shell side.
The top of upper layer electric field region 1 is equipped with flue gas pooled portion 7, and exhanst gas outlet 8, lower layer are equipped in flue gas pooled portion 7 The dust collecting electrode 5 of electric field region 2 and the length of cathode line 6 are greater than the dust collecting electrode 5 of upper layer electric field region 1 and the length of cathode line 6.
Fig. 4, Fig. 5 are please referred to, Fig. 4 is the top view of single dust collecting electrode;Fig. 5 is single hexagon exhaust gases passes by conductive glass The structural schematic diagram that glass steel pipe permutation and combination is formed.
As shown, dust collecting electrode 5 is equipped in the exhaust gases passes of honeycomb distribution on cross section, except the part of edge For exhaust gases passes due to dividing except not formed complete hexagon, internal most of exhaust gases passes are the six of total side The wall portion of side shape exhaust gases passes, each hexagon exhaust gases passes is formed by several 51 permutation and combination of remover of conductive glass steel tube, on the whole Modular construction 511 is formed, the material of remover of conductive glass steel tube 51 is that 2205 two-phase alloys pipes have the advantages that thermal conductivity is high, can be straight Connect the residue steam of coal-burning power plant, steel plant, and performance of the 2205 two-phase alloys pipes in terms of antiplaque erosion and crevice corrosion It is more superior, it is suitble to wet electrical dust precipitator to use.
Referring to FIG. 3, Fig. 3 is the partial enlarged view at the position A in Fig. 2.
As shown, deflector 3 includes lower layer's deflector 31 and upper layer deflector 32;Lower layer's deflector 31 has crest portion Position and trough position, and flue gas opening 33 is equipped at wave crest position;Upper layer deflector includes the shutter in inverted " v ", each to hide Baffle is arranged in 33 top of flue gas opening of lower layer's deflector 31 and between lower layer deflector 31 there are appropriate spacing, with Form the exhaust gases passes with dog leg path.
When flue gas flows upwardly into upper layer electric field region 1 from lower layer electric field region 2, flue gas opening 33 is first travelled up to, then Upper layer deflector 32 block effect under, from flue gas opening 33 both sides flow downward, finally from the wave of lower layer's deflector 31 Valley position flows up, into upper layer electric field region 1.Since the exhaust gases passes of deflector 3 are dog leg path, even if upper layer is electric Condensed water is generated in place 1, will not enter lower layer electric field region 2, and deflector 3 had both been able to achieve flue gas and has passed through through lower layer electric field region 2 Intermediate deflector 3 is flowed into toward upper layer electric field region 1, and can guarantee infrastructure devices safe and stable operation.
In order to which the condensed water that may accumulate on deflector 3 is discharged, deflector 3 is in the wave crest for being parallel to its lower layer's deflector 31 The arrangement that has upwardly sloped front and rear sides at position and trough position, the both ends of deflector 3 and the shell of 1 lower layer electric field region 2 of upper layer electric field region Internal wall sealing welding connection, prevents water droplet from entering lower layer electric field region 2 from periphery fissure clearance flow, shell is set in the lowest part of deflector 3 There is rhone, water is directly flowed down from the rhone for being located at 3 lower of deflector along shell wallboard, so that it may avoid enter into lower layer Electric field region 2 avoids lower layer electric field region 2 that short circuit phenomenon occurs.
Deflector 3 shown in figure not only tilts in the longitudinal direction, but also is divided into symmetrical two parts, this two parts exists Also be in tilted layout on left and right directions, in the middle part of height be lower than the height on both sides, form deflector shape intermediate high, that both sides are low Formula.
In the process of running, the steam in the remover of conductive glass steel tube 51 of lower layer electric field region 2 is in off state, upper layer electric field region Steam is open state in 1 remover of conductive glass steel tube 51, and flue gas is when by lower layer electric field region 2, due to leading for lower layer electric field region 2 There is not steam in electric glass reinforced plastic pipe 51, the vapor in flue gas, which encounters cold remover of conductive glass steel tube 51, can be condensed into water;Work as heat When flue gas is by upper layer electric field region 1, due to being connected with steam in the remover of conductive glass steel tube 51 of upper layer electric field region 1, flue gas is by conductive 51 temperature of glass reinforced plastic pipe increases, to avoid the occurrence of " white haze " phenomenon.
In addition, only need to periodically be sprayed, not needed to remover of conductive glass steel tube 51 according to system operation situation when using Long-term water spray and overflow water.
When upper layer electric field region 1 is sprayed, the remover of conductive glass steel tube 51 of lower layer electric field region 2 is connected with steam, and flue gas passes through It is heated when the remover of conductive glass steel tube 51 of lower layer electric field region 2, and the obstructed steam of remover of conductive glass steel tube 51 of upper layer electric field region 1, cigarette Gas by upper layer electric field region 1 remover of conductive glass steel tube 51 when, condensation can be played to flue gas.Due in lower layer electric field region 2 Remover of conductive glass steel tube 51 is longer than upper layer electric field region 1, and the contact area of flue gas and remover of conductive glass steel tube 51 is bigger, therefore flue gas Temperature rise effect is bigger than flue gas condensing effect, and flue gas is overall or heats up.
When lower layer electric field region 2 is sprayed, the obstructed steam of remover of conductive glass steel tube 51 of lower layer electric field region 2, flue gas passes through When the remover of conductive glass steel tube 51 of lower layer electric field region 2, condensation can be played to flue gas, and the electroconductive frp of upper layer electric field region 1 Pipe 51 leads to steam, and flue gas is thus sustainable to heat up to flue gas by being heated when the electric field region 1 of upper layer, and then flue gas can It is directly arranged by flue to chimney, is also effectively solved the problems, such as " white haze ", and be conducive to the lifting of smoke height.
The remover of conductive glass steel tube 51 of dust collecting electrode 5 is connected with steam pipework, and steam is passed through conduction by these steam pipeworks Glass reinforced plastic pipe 51, steam can be discharged together after remover of conductive glass steel tube 51 with flue gas, or as condensed water along leading Flowing plate outflow.
Use above-mentioned wet-esp temperature rising integrated device, it may not be necessary to condenser is added after wet electrical dust precipitator Effect, cost of investment " except white ", which can be reached, with follow-up equipments such as MGGH to substantially reduce;It can effectively solve wet-esp Flue-gas temperature is low after device and subsequent flue, chimney low-temperature corrosion problem, and is conducive to the lifting of smoke height.
Above-described embodiment is only the preferred embodiment of the utility model, is specifically not limited thereto, on this basis can basis Actual needs is made having and targetedly be adjusted, to obtain different embodiments.For example, the shutter of upper layer deflector 32 In inverted " u "-shaped;Alternatively, the flue gas opening on lower layer's deflector 31 can be continuously, it is also possible to intermittent, etc..Due to Mode in the cards is more, just no longer illustrates one by one here.
Wet-esp temperature rising integrated device provided by the utility model is described in detail above.Herein Specific case is applied to be expounded the principles of the present invention and embodiment, the explanation of above example is only intended to Help understands the core concept of the utility model.It should be pointed out that for those skilled in the art, not taking off Under the premise of from the utility model principle, several improvements and modifications can be made to this utility model, these improvement and modification It also falls into the protection scope of the utility model claims.

Claims (10)

1. a kind of wet-esp temperature rising integrated device, which is characterized in that described including upper layer electric field region and lower layer electric field region The deflector that upper layer and lower layer electric field region is separated and flue gas is allowed to pass through is equipped between upper layer electric field region and lower layer electric field region;It is described Upper layer electric field region and lower layer electric field region include cathode hanger, dust collecting electrode and cathode line, and the dust collecting electrode is equipped on cross section In the exhaust gases passes that honeycomb is distributed, the wall portion of each hexagon exhaust gases passes is by several remover of conductive glass steel tube permutation and combination shapes At;The remover of conductive glass steel tube heats up under operating condition for being passed through steam in dedusting, the remover of conductive glass steel tube of the upper layer electric field region In the state for being passed through steam, the remover of conductive glass steel tube of the lower layer electric field region is in the state for not being passed through steam.
2. wet-esp temperature rising integrated device according to claim 1, which is characterized in that under the deflector includes Layer deflector and upper layer deflector;Lower layer's deflector has wave crest position and trough position, and is equipped with cigarette at wave crest position Gas opening;The upper layer deflector includes the shutter in inverted " v ", and each shutter is arranged in lower layer's water conservancy diversion The flue gas overthe openings of plate and between lower layer's deflector there are spacing, to form the exhaust gases passes with dog leg path.
3. wet-esp temperature rising integrated device according to claim 2, which is characterized in that the deflector is parallel In the wave crest position of lower layer's deflector and the arrangement that has upwardly sloped front and rear sides at trough position.
4. wet-esp temperature rising integrated device according to claim 3, which is characterized in that the both ends of the deflector It is connect with the inner walls sealing welding of the upper layer electric field region and lower layer electric field region, the shell is minimum the deflector Place is equipped with rhone.
5. wet-esp temperature rising integrated device according to claim 1, which is characterized in that the lower layer electric field region The length of dust collecting electrode and cathode line is greater than the dust collecting electrode of the upper layer electric field region and the length of cathode line.
6. wet-esp temperature rising integrated device according to claim 5, which is characterized in that sprayed in upper layer electric field region Under operating condition, the remover of conductive glass steel tube of the upper layer electric field region is in the state for not being passed through steam, the conduction of the lower layer electric field region Glass reinforced plastic pipe is in the state for being passed through steam.
7. wet-esp temperature rising integrated device according to claim 5, which is characterized in that sprayed in lower layer electric field region Under operating condition, the remover of conductive glass steel tube of the upper layer electric field region is in the state for being passed through steam, the conductive glass of the lower layer electric field region Glass steel pipe is in the state for not being passed through steam.
8. wet-esp temperature rising integrated device according to any one of claim 1 to 7, which is characterized in that described Remover of conductive glass steel tube is 2205 two-phase alloys pipes.
9. wet-esp temperature rising integrated device according to claim 8, which is characterized in that the upper layer electric field region and The cathode hanger of lower layer electric field region is arranged in the side of its shell.
10. wet-esp temperature rising integrated device according to claim 9, which is characterized in that the upper layer electric field region Top be equipped with flue gas pooled portion, and in the flue gas pooled portion be equipped with exhanst gas outlet.
CN201920165227.XU 2019-01-30 2019-01-30 A kind of wet-esp temperature rising integrated device Active CN209501966U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201920165227.XU CN209501966U (en) 2019-01-30 2019-01-30 A kind of wet-esp temperature rising integrated device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201920165227.XU CN209501966U (en) 2019-01-30 2019-01-30 A kind of wet-esp temperature rising integrated device

Publications (1)

Publication Number Publication Date
CN209501966U true CN209501966U (en) 2019-10-18

Family

ID=68203466

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201920165227.XU Active CN209501966U (en) 2019-01-30 2019-01-30 A kind of wet-esp temperature rising integrated device

Country Status (1)

Country Link
CN (1) CN209501966U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN117259011A (en) * 2023-11-03 2023-12-22 宣化冶金环保设备制造(安装)有限责任公司 Double-layer electric dust remover

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN117259011A (en) * 2023-11-03 2023-12-22 宣化冶金环保设备制造(安装)有限责任公司 Double-layer electric dust remover

Similar Documents

Publication Publication Date Title
CN106474860A (en) Wet desulfurization flue gas processing system and processing method
CN109395882A (en) A kind of dust-collecting and heat exchanging disappears white equipment and system
CN209501966U (en) A kind of wet-esp temperature rising integrated device
CN108546796B (en) Full-dry type cooling device for converter flue gas and cooling method thereof
CN110124347A (en) A kind of energy and water saving type flue gas purification device and method
CN206980987U (en) A kind of flue gas processing device
CN201028567Y (en) Heat pipe type air preheater
CN205048737U (en) Heat exchanger
CN111637481A (en) Tail gas purification system and method for recovering flue gas waste heat
CN208418777U (en) Phase-change heat exchange system
CN205825085U (en) A kind of New-type boiler flue gas waste heat recovery apparatus
CN204901732U (en) Modular waste heat of boiler flue gas recovery system
CN210980876U (en) Automatic air cooling island spraying and atomizing device of air exhaust
CN108151050A (en) A kind of dangerous waste burns wet method depickling flue gas and takes off white system and its application method
CN209386338U (en) A kind of electricity generation boiler tail flue gas based on high-temperature dust removal disappears white device
CN209371825U (en) A kind of high efficiency flue gas condensator
CN111744297A (en) Tail gas dust removal waste heat recovery system
CN206274230U (en) A kind of superconduction fluidised form heat exchanger
CN207527621U (en) A kind of eliminating white smoke integral system
CN206751452U (en) A kind of spraying system that desulfurization wastewater is concentrated using fume afterheat
CN218393031U (en) Dedusting smoke and white elimination system
CN215810247U (en) Sintering waste heat utilization system
CN108225083A (en) A kind of waste heat recovery furnace
CN210035563U (en) Vertical multi-flow countercurrent heat exchange flue gas condensation heat exchanger
CN204901733U (en) Novel composite boiler residual heat from flue gas system

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant