CN207546187U - A kind of ship flue gas desulfurization removes nitre device - Google Patents
A kind of ship flue gas desulfurization removes nitre device Download PDFInfo
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- CN207546187U CN207546187U CN201721390834.3U CN201721390834U CN207546187U CN 207546187 U CN207546187 U CN 207546187U CN 201721390834 U CN201721390834 U CN 201721390834U CN 207546187 U CN207546187 U CN 207546187U
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- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
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Abstract
The utility model is that a kind of ship flue gas desulfurization removes nitre device and technique.The utility model device includes spray column and coupled flue, flue is disposed with flue air inlet, ozone injector, first jet along smoke movement direction, the direction of motion of spray column principal space axial direction along the flue gas is disposed with rectification porous plate, second nozzle, third nozzle, gas cooler, demisting layer, spray column gas outlet, the bottom of spray column is inverted cone, and is provided centrally with spray column wastewater outlet in inverted cone.Present apparatus combination ozonation technology and spray-absorption technology handle ship flue gas, with ozone oxidation lower nitrogen oxides and sulfur dioxide, its pollutant are made to be conducive to absorb efficiently removal by subsequent circulated sprinkling three times.Technique setting is reasonable, and installation area is small, build or reconstruct on ship all easily, construction cost it is low.
Description
Technical field
The utility model is related to atmospheric environment protection fields, and nitre device is removed especially with regard to a kind of ship flue gas desulfurization.
Background technology
With the development of Shipping industry, ship machine exhaust pollution increasingly sharpens, and the pollutant of discharge includes nitrogen oxides
(NOx), oxysulfide (SOx), carbon monoxide (CO), hydrocarbon (HC) and particulate matter (PM) etc., and with mobility
Greatly, the features such as diffusivity is big, the duration is long.It is shown according to International Maritime Organization (IMO) statistical data in 2014, ship discharge
SOx, NOx account for about the 13% and 15% of Global emissions total amount respectively.The statistics display of Chinese environmental protection portion motor vehicle blowdown monitoring center,
National ship SO2 discharge capacitys account for about the 8.4% of national total emission volumn within 2013, and NOx discharge accounts for 11.3%, by Pollution From Ships shadow
Ring maximum is port city, secondly rivers bank city.Ship machine exhaust pollution has become after tail gas pollution of motor-driven vehicle, industry
After enterprise's exhaust emission, the third-largest atmosphere pollution source in China has caused the strong interest of the whole society.
Chinese transportation Department of Transportation proposes《Ship and port pollution prevention special campaigns embodiment (2015-2020
Year)》, explicitly point out, to the year two thousand twenty, Pearl River Delta, the Yangtze River Delta, Circum-Bohai Sea (Jing-jin-ji region) waters ship oxysulfide, nitrogen oxides,
Particulate matter declined 65%, 20%, 30% respectively compared with 2015.Therefore, the ship machine exhaust pollution control policy in current China
It is broadly divided into three aspects：First, realize the control of SO2 by strictly controlling the fuel oil that ship uses；Second is that it is marked by discharging
Standard limits the discharge of CO, HC, NOx and PM etc.；Third, by actively promoting the use of bank electricity, the tail during ship reaches port is reduced
Gas discharges, and makes at " green harbour ".Marine exhaust is administered extremely urgent.
Research and development currently for the treatment technology of ship tail gas are still at an early stage.206397567 U of CN disclose ship
Oceangoing ship exhaust gas denitration system, Benitration reactor mainly include Urea Evaporation room, mixer and reative cell, which is equipped with
Urea liquid spray gun, the mixer connect the Urea Evaporation room and the reative cell, and exhaust gas is de- into this through the exhaust gas denitration pipeline
Behind the Urea Evaporation room of nitre reactor, mix with urea and enter after the reative cell carries out denitration through the mixer and discharge.CN
104326604 B disclose it is a kind of based on the marine exhaust desulfurization washing water treatment technology and its processing system of alkaline process is received, mainly
It is to introduce marine exhaust desulfurization washings to neutralize oxidation integral pool, air is blasted by sulphite into pond by Aeration fan
Sulfate is oxidized to, the pH value of the marine exhaust desulfurization washings added in sodium hydroxide solution adjusting neutralization oxidation integral pool reaches
To discharge standard, and using aeration disturbance neutralize it is quenched.Common marine exhaust treatment technology has SCR, EGR, washer
Etc. technologies, these technical principles it is different, respectively have its scope of application and feature, advantage and disadvantage.Therefore, still lacking one kind in the market can
Meet emission request, take up little area, is efficient, safeguarding at ship denitrating flue gas that is simple, adapting to marine special natural environment waterborne
Reason system.
Utility model content
The purpose of this utility model is to provide a kind of can continually and steadily run, less energy consumption, take up little area, it is efficient,
Safeguard that a kind of ship flue gas desulfurization that is simple, adapting to marine special natural environment waterborne removes nitre device.
One purpose of the utility model is to disclose a kind of ship flue gas desulfurization except nitre device, to realize above-mentioned utility model
Purpose, the technical solution that the utility model is taken are as follows.
A kind of ship flue gas desulfurization removes nitre device, and including spray column and coupled flue, flue is along smoke movement side
To flue air inlet, ozone injector, first jet is disposed with, the ozone injector passes through pipeline and ozone generator
Connection；The connector of spray column and flue is spray column air inlet, and the pipeline before spray column air inlet is in certain slope to tower body
Direction tilts；Flue gas is entered by spray column air inlet in spray column, and the spray column principal space axial direction is along flue gas
The direction of motion is disposed with rectification porous plate, second nozzle, third nozzle, gas cooler, demisting layer, spray column outlet
Mouthful, the first jet, second nozzle, third nozzle are connect with slurry diversion device, the slurry diversion device and slurries
The water outlet connection of circulating pump, the water inlet of the slurry circulating pump go out with being set to the spray column slurries of the spray column lower part
Mouth connection.Slurry diversion device can supply the slurries of spray to the first jet, second nozzle, third nozzle simultaneously,
Slurries and flue gas are entered the prewashing tower after reacting, and enter the serum recycle by the spray column serum outlet
Pump forms the serum recycle of completion.
Preferably, the bottom of the spray column is inverted cone, waste liquid can be preferably collected, and in inverted cone
It is provided centrally with spray column wastewater outlet.
Preferably, further include the first sea water pump sequentially connected with the gas cooler, first filter；The cigarette
Gas Cooler is the coiled pipe heat-exchange device being spirally distributed, and seawater is by the first filter by first seawater
It is pumped into, enters the gas cooler from center, is exchanged with flue gas after heat from pipe other end discharge outboard.The flue gas cooling
Device can reduce flue-gas temperature, greatly reduce water content in flue gas, reduce water mist carrying amount.
Preferably, further include heat exchanger, the second sea water pump, the second filter；The heat exchanger is provided with hot friendship
Parallel operation sea intake, heat exchanger seawer outlet, heat exchanger slurry inlet, heat exchanger serum outlet；The heat exchanger
Sea intake is connect successively with second sea water pump, second filter, and the heat exchanger seawer outlet connects with outboard
Connect, the heat exchanger slurry inlet is connect with the slurry circulating pump water outlet, the heat exchanger serum outlet with it is described
Slurry diversion device connects.Slurries are entered by the heat exchanger slurry inlet in the heat exchanger, are handed over by the heat
Parallel operation serum outlet flows out, and the second sea water pump extracting seawater enters heat exchanger by the heat exchanger sea intake
It is interior, with seawater by being cooled down after heat exchange, outboard is then discharged by the heat exchanger seawer outlet.
Preferably, it further includes with coyote hole, medicament storage box, third sea water pump, third filter and is set to spray
The spray column injection point of tower side wall, it is described to be connect with coyote hole outlet with the spray column by spray column injection point；It is described
It is connect successively with third sea water pump, third filter with coyote hole first entrance, it is described to match coyote hole second entrance and medicament storage box
Connection.Seawater is pumped by the third filter by the third seawater, into interior of making up a prescription, with medicament storage box memory
The alkaline matter mixing of storage, is configured to the slurries.The alkaline matter is caustic alkali or magnesia.Caustic alkali is common
Alkali, cheap, alkalinity is high, easily uses, but corrosivity easy deliquescence by force, if spray liquid is configured using caustic alkali, is storing
When it is noted that anti-corrosion is moisture-proof, medicament storage box will do corresponding processing.Magnesia is common basic anhydride, in powdery, nothing
Poison is harmless, the consumption sprayed only has caustic alkali 1/4 is done, so required memory space is small.But its solubility in water is relatively low,
The spray liquid of configuration is in slurry, if spray liquid is configured using magnesia, circulated sprinkling pump should change the pump of energy transported slurry into.
Preferably, further include wastewater treatment equipment sequentially connected with the spray column wastewater outlet, sewage collecting box,
Sludge treatment equipment connects.Waste water can be directly handled on hull, saves forms space protection environment.
Preferably, the porous board diameter of rectification is identical with inner diameter of tower, multiple circles are opened on the rectification porous plate
Aperture, percent opening 50-80%, preferred value 58% can preferably smooth air-flow.
Preferably, the demisting layer is corrosion-resistant folded plate demister, the steam carried secretly in flue gas is removed.
Preferably, further include pH meter and liquid level gauge, the pH meter and liquid level gauge are arranged at the inverted cone of tower body bottom
In body.
Another purpose of the utility model is to disclose a kind of ship flue gas desulfurization technique of nitrate removal according to above device,
Including following processing step：
(1) ship flue gas enters flue by flue air inlet, and ozone generator generates ozone and is delivered to ozone injector,
Ozone injector is to flue gas contrainjection ozone, ozone energy oxidizing lower nitrogen oxides and sulfide, such as nitric oxide (NO)
It is oxidized to nitrogen dioxide (NO2), sulfur dioxide (SO2) it is oxidized to sulfur trioxide (SO3)；
(2) cycle for the first time occurs with the slurries that first jet sprays by the ship flue gas that step (1) is handled to wash, it is high
Valency nitrogen oxides and sulfur trioxide can be reacted to acid compared to low oxide with water, and then slurries neutral and alkali substance and acid are sent out
Raw acid-base neutralization reaction desulfurization is absorbed except nitre, nitrogen oxides and sulfide, and the slurries that first jet sprays enter stack base,
Spray column is entered by the inclined pipeline of stack base, serum recycle is returned to by the spray column serum outlet for spraying tower bottom
Pump forms complete cycle；
(3) the ship flue gas handled by step (2) is entered by spray column air inlet in spray column, porous by rectification
The smooth air-flow of plate occurs to recycle washing twice with second nozzle and third nozzle, further absorbing NOx and vulcanization in succession
The slurries that object, second nozzle and third nozzle spray enter prewashing tower bottom, pass through the spray column serum outlet of prewashing tower bottom
Slurry circulating pump is returned to, forms complete cycle；
(4) the ship flue gas handled by step (3), passes sequentially through gas cooler cooling, demister dehumidifying, and seawater leads to
It crosses the first filter to be pumped by first seawater, enters the gas cooler from center, after heat is exchanged with flue gas
Outboard is discharged from the pipe other end, flue-gas temperature can be reduced, greatly reduces water content in flue gas, water mist carrying amount is reduced, then, removes
Day with fog is corrosion-resistant folded plate demister, removes the steam carried secretly in flue gas, is gone out by purified flue gas up to standard by spray column
Gas port is discharged；
(5) judge tower body liquid level and pH value by being set to pH meter and liquid level gauge in the inverted cone of tower body bottom, if
Liquid level is higher than setting value, opens the spray column wastewater outlet of tower body bottom, waste water flow into wastewater treatment equipment, sewage collecting box,
It in sludge treatment equipment, is handled, if pH value is less than setting value, adds in spray column injection point input slurries, slurries exist
Indoor completion of making up a prescription is configured；With coyote hole by the seawater after third sea water pump and the input filtering of third filter, deposited by medicament
Storage tank inputs alkaline matter, is then mixedly configured into the slurries.If spray liquid is configured using caustic alkali, to be noted in storage
Anti-corrosion of anticipating is moisture-proof, and medicament storage box will do corresponding processing.If using magnesia, since solubility is relatively low in its water, configuration
Spray liquid in slurry, if being configured spray liquid using magnesia, circulated sprinkling pump should change into can transported slurry pump；
When serum recycle pump work, heat exchanger, the second sea water pump, the second filter are opened；Slurries pass through the heat
Exchanger slurry inlet enters in the heat exchanger, is flowed out by the heat exchanger serum outlet, second sea water pump
Extracting seawater is entered by the heat exchanger sea intake in heat exchanger, with seawater by being cooled down after heat exchange,
Then outboard is discharged by the heat exchanger seawer outlet, slurries neutral and alkali substance and acid occur acid-base neutralization reaction desulfurization and removes
Nitre is exothermic reaction, reduce loop slurry temperature, can significantly more efficient desulfurization remove nitre.
Relative to the prior art, the utility model achieves beneficial technique effect：
1. present apparatus combination ozonation technology and spray-absorption technology handle ship flue gas, with ozone oxidation at a low price
Nitrogen oxides and sulfur dioxide make its pollutant be conducive to absorb efficiently removal by subsequent circulated sprinkling three times.
2. the waste water handled can recycle sludgeization processing, environment-friendly high-efficiency；
3. technique setting is reasonable, installation area is small, simple in structure, easy maintenance, builds or reconstructs all on ship
Easily, construction cost is low, can not only improve the utilization ratio of device, and reduces the complexity of technique.
Description of the drawings
Fig. 1 device technique flow diagrams；
Fig. 2 gas cooler partial enlarged views；
Fig. 3 rectification porous plate partial enlarged views.
Reference numeral：Spray column 1, flue 2, flue air inlet 3, ozone injector 4, ozone generator 5, first jet
6th, spray column air inlet 7, rectification porous plate 8, second nozzle 9, third nozzle 10, gas cooler 11, demisting layer 12, spray column
Gas outlet 13, the first sea water pump 14, first filter 15, heat exchanger 16, heat exchanger sea intake 161, heat exchanger sea
Water out 162, heat exchanger slurry inlet 163, heat exchanger serum outlet 164, the second sea water pump 17, the second filter 18,
Slurry circulating pump 19, with coyote hole 20, third sea water pump 21, third filter 22, medicament storage box 23, sludge treatment equipment 24,
Sewage collecting box 25, wastewater treatment equipment 26, spray column wastewater outlet 27, spray column serum outlet 28, spray column injection point
29th, slurry circulating pump water outlet 30, slurry diversion device 31.
Specific embodiment
Specific embodiment of the present utility model is described further below in conjunction with the accompanying drawings：
Embodiment
A kind of ship flue gas desulfurization removes nitre device, as shown in Figure 1, its agent structure is spray column 1 and coupled cigarette
Road 2, the connector of spray column 1 and flue 2 are spray column air inlet 7, and the channel before spray column air inlet 7 is in certain slope to tower
Body direction tilts, to prevent liquid product in flue.2 one end of flue is provided with flue air inlet 3, along smoke movement direction successively
Ozone injector 4, first jet 6 are provided with, the ozone injector 4 is connect by pipeline with ozone generator 5.Ozone occurs
Device 4 generate ozone, by ozone injector 4 in flue 2 to flue gas contrainjection ozone, ozone energy oxidizing lower nitrogen oxides
With part sulfur dioxide, removed convenient for follow-up spray-absorption.Entered by the flue gas that ozone treatment is crossed by spray column air inlet 7
In spray column 1, the direction of motion of spray column 1 principal space axial direction along the kiln gas be disposed with rectification porous plate 8,
It is sprayed in second nozzle 9, third nozzle 10, gas cooler 11, demisting layer 12, spray column gas outlet 13, flue gas and nozzle
Slurries occur chemical action and then are handled, and are discharged by spray column gas outlet 13.
The first jet 6, second nozzle 9 and third nozzle 10 are connect with slurry diversion device 31, slurry diversion device
31 connect with slurry circulating pump water outlet 30, and 1 bottom of spray column is provided with spray column serum outlet 28, spray column serum outlet 28
It is connect with 19 water inlet of slurry circulating pump, slurries form a serum recycle in spray column.
The bottom of spray column 1 is inverted cone, can preferably collect slurries, inverted cone is provided centrally with spray column
Wastewater outlet 27, spray column wastewater outlet 27 are connect by pipeline with wastewater treatment equipment 26, wastewater treatment equipment 26 and waste water
Collecting box 25 connects, and sewage collecting box 25 is connect with sludge treatment equipment 24.
The side wall of spray column 1 is provided with spray column injection point 29, and spray column injection point 29 with the outlet of coyote hole 20 with connecting
It connects, is connect successively with third sea water pump 21, third filter 22 with 20 first entrance of coyote hole, third filter 22 and seawater A connects
It is logical, connect with 20 second entrance of coyote hole with medicament storage box 23, medicament storage box 23 is stored with alkaline matter, such as caustic alkali or
Magnesia, 21 extracting seawater of third sea water pump enter with coyote hole 20, mix according to a certain percentage with coyote hole 20 mixing seawater with
Alkaline matter obtains the slurries, and the slurries are entered by spray column injection point 29 in spray column 1.
As preferred embodiment, heat exchanger 16 is further included, heat exchanger 16 is provided with heat exchanger sea intake
161st, heat exchanger seawer outlet 162, heat exchanger slurry inlet 163, heat exchanger serum outlet 164, heat exchanger slurries
Import 163 is connect with slurry circulating pump water outlet 30, and heat exchanger serum outlet 164 is connect with slurry diversion device 31, slurries
Part flow arrangement 31 connects to be connect with first jet 6, second nozzle 9 and third nozzle 10, slurries by heat exchanger slurries into
Mouth 163 enters in heat exchanger 16, is flowed out by heat exchanger serum outlet 164；Heat exchanger sea intake 161 successively with
Second sea water pump 17, the second filter 18 connect, the second filter 18 connection seawater A, heat exchanger seawer outlet 162 and outboard
B connections, 17 extracting seawater of the second sea water pump are entered in heat exchanger 16 by heat exchanger sea intake 161, passed through with seawater
Heat exchange is cooled down, and then discharges outboard by heat exchanger seawer outlet 162.
Gas cooler 11 is as shown in Fig. 2, gas cooler 11 connects successively with the first sea water pump 14, first filter 15
It connects, first filter 15 is connected with seawater A, and gas cooler 11 is the coiled pipe heat-exchange device being spirally distributed, seawater
It is pumped by first filter 15 by the first sea water pump 14, enters gas cooler 11 from center, exchanged with flue gas after heat from pipe
The other end discharges outboard, and gas cooler 11 can reduce flue-gas temperature, greatly reduces water content in flue gas, reduces water mist and carries
Amount.
As described in Figure 3,8 diameter of rectification porous plate is identical with inner diameter of tower, the rectification porous plate for rectification porous plate 8
Multiple circular apertures, percent opening 50-80%, preferred value 58% are opened on 8.The liquid that nozzle sprays is in mist, spray angle
More than 120 °, entire tower body inner section can be covered.The demisting layer 12 is corrosion-resistant folded plate demister, removes what is carried secretly in flue gas
Steam.
As preferred embodiment, pH meter and liquid level gauge are further included, the pH meter and liquid level gauge are arranged at tower body bottom
Inverted cone in.
A kind of ship flue gas desulfurization technique of nitrate removal, including following processing step：
(1) ship flue gas enters flue 2 by flue air inlet 3, and ozone generator 5 generates ozone and is delivered to ozone injection
Device 4, ozone injector 4 is to flue gas contrainjection ozone, ozone energy oxidizing lower nitrogen oxides and sulfide, such as nitric oxide
(NO) it is oxidized to nitrogen dioxide (NO2), sulfur dioxide (SO2) it is oxidized to sulfur trioxide (SO3)；
(2) cycle for the first time occurs with the slurries that first jet 6 sprays by the ship flue gas that step (1) is handled to wash,
Higher nitrogen oxides and sulfur trioxide can be reacted to acid compared to low oxide with water, then slurries neutral and alkali substance and acid
Acid-base neutralization reaction desulfurization occurs except nitre, nitrogen oxides and sulfide are absorbed, the slurries that first jet 5 sprays enter flue bottom
Portion flows into tower by the inclined pipeline of stack base, serum recycle is returned to by the spray column serum outlet 28 of 1 bottom of spray column
Pump 19 forms complete cycle；
(3) entered in spray column 1 by spray column air inlet 7 by the ship flue gas that step (2) is handled, it is more by rectification
8 smooth air-flow of orifice plate occurs to recycle washing twice with second nozzle 9 and third nozzle 10, further absorbing NOx in succession
And sulfide, the slurries that second nozzle 9 and third nozzle 10 spray enter 1 bottom of prewashing tower, pass through the spray of prewashing tower bottom
Tower serum outlet 28 returns to slurry circulating pump 19, forms complete cycle；
(4) the ship flue gas handled by step (3), passes sequentially through that gas cooler 11 cools down, demisting layer 12 dehumidifies, sea
Water is pumped by the first filter 14 by first sea water pump 15, enters the gas cooler 11 from center, with cigarette
Outboard is discharged from the pipe other end after gas exchange heat, flue-gas temperature can be reduced, greatly reduce water content in flue gas, water mist is reduced and carries
Amount, then, demister 12 are corrosion-resistant folded plate demister, the steam carried secretly in flue gas are removed, by purified flue gas up to standard
It is discharged by spray column gas outlet 13；
(5) judge tower body liquid level and pH value by being set to pH meter and liquid level gauge in the inverted cone of tower body bottom, if
Liquid level is higher than setting value, opens the spray column wastewater outlet 27 of tower body bottom, and waste water flows into wastewater treatment equipment 26, wastewater collection
It in case 25, sludge treatment equipment 24, is handled, if pH value is less than setting value, is inputted and starched by spray column injection point 29
Liquid, slurries are with completion configuration in coyote hole 20；After being filtered with coyote hole 20 by third sea water pump 21 and the input of third filter 22
Seawater, by medicament storage box 23 input alkaline matter, be then mixedly configured into the slurries.If it is configured using caustic alkali
Spray liquid, in storage it is noted that anti-corrosion is moisture-proof, medicament storage box will do corresponding processing.If using magnesia, due to it
Solubility is relatively low in water, and the spray liquid of configuration is in slurry, if spray liquid is configured using magnesia, circulated sprinkling pump should change into
The pump of energy transported slurry；
When slurry circulating pump 19 works, heat exchanger 16, the second sea water pump 17, the second filter 18 are opened；Slurries lead to
It crosses the heat exchanger slurry inlet 163 to enter in the heat exchanger 16, be flowed by the heat exchanger serum outlet 162
Go out, 17 extracting seawater of the second sea water pump is entered by the heat exchanger sea intake 161 in heat exchanger 16, with seawater
By being cooled down after heat exchange, outboard, slurries neutral and alkali substance are then discharged by the heat exchanger seawer outlet 162
Acid-base neutralization reaction desulfurization occurs except nitre is exothermic reaction with acid, reduces loop slurry temperature, can significantly more efficient desulfurization remove
Nitre.
According to the disclosure and teachings of the above specification, the utility model those skilled in the art can also be to above-mentioned reality
The mode of applying is changed and is changed.Therefore, the utility model is not limited to specific embodiment disclosed and described above, right
Some modifications and changes of utility model should also be as falling into the scope of the claims of the utility model.In addition, although
Some specific terms are used in this specification, but these terms are merely for convenience of description, not to the utility model structure
Into any restrictions.
Claims (9)
1. a kind of ship flue gas desulfurization removes nitre device, which is characterized in that including spray column and coupled flue, flue is along cigarette
The gas direction of motion is disposed with flue air inlet, ozone injector, first jet, the ozone injector by pipeline with it is smelly
Oxygen Generator connects；The connector of spray column and flue is spray column air inlet, and the pipeline before spray column air inlet is in certain slope
It spends to tower body direction and tilts；Flue gas is entered by spray column air inlet in spray column, and the spray column body interior is along flue gas
The direction of motion is disposed with rectification porous plate, second nozzle, third nozzle, gas cooler, demisting layer, spray column outlet
Mouthful, the first jet, second nozzle, third nozzle are connect with slurry diversion device, the slurry diversion device and slurries
The water outlet connection of circulating pump, the water inlet of the slurry circulating pump go out with being set to the spray column slurries of the spray column lower part
Mouth connection.
2. the apparatus according to claim 1, which is characterized in that the bottom of the spray column is inverted cone, and in rounding
Cone is provided centrally with spray column wastewater outlet.
3. the apparatus according to claim 1, which is characterized in that further include and the gas cooler sequentially connected first
Sea water pump, first filter；The gas cooler is the coiled pipe heat-exchange device being spirally distributed, and seawater passes through described
First filter is pumped by first seawater, enters the gas cooler from center, is exchanged with flue gas another from pipe after heat
Discharge outboard in one end.
4. the apparatus according to claim 1, which is characterized in that further include heat exchanger, the second sea water pump, the second filtering
Device；The heat exchanger is provided with heat exchanger sea intake, heat exchanger seawer outlet, heat exchanger slurry inlet, heat and hands over
Parallel operation serum outlet；The heat exchanger sea intake is connect successively with second sea water pump, second filter, described
Heat exchanger seawer outlet is connect with outboard, and the heat exchanger slurry inlet is connect with the slurry circulating pump water outlet, institute
It states heat exchanger serum outlet to connect with the slurry diversion device, slurries enter slurry diversion through over-heat-exchanger postcooling and fill
It puts.
5. the apparatus according to claim 1, which is characterized in that further include with coyote hole, medicament storage box, third sea water pump,
Third filter and the spray column injection point for being set to spray tower side wall, it is described to pass through with coyote hole outlet with the spray column
Spray column injection point connects；It is described to be connect successively with third sea water pump, third filter with coyote hole first entrance, it is described to make up a prescription
Room second entrance is connect with medicament storage box, and the medicament storage box is stored with alkaline matter, and the alkaline matter is caustic alkali
Or magnesia.
6. the apparatus of claim 2, which is characterized in that further include sequentially connected with the spray column wastewater outlet
Wastewater treatment equipment, sewage collecting box, sludge treatment equipment.
7. the apparatus of claim 2, which is characterized in that further include pH meter and liquid level gauge；The pH meter and liquid level gauge
It is arranged in the inverted cone of tower body bottom.
8. the apparatus according to claim 1, which is characterized in that the porous board diameter of rectification is identical with inner diameter of tower, institute
It states and multiple circular apertures is opened on rectification porous plate, percent opening 50-80%.
9. the apparatus according to claim 1, which is characterized in that the demisting layer is corrosion-resistant folded plate demister.
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| CN201721390834.3U CN207546187U (en) | 2017-10-25 | 2017-10-25 | A kind of ship flue gas desulfurization removes nitre device |
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| CN201721390834.3U CN207546187U (en) | 2017-10-25 | 2017-10-25 | A kind of ship flue gas desulfurization removes nitre device |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107583429A (en) * | 2017-10-25 | 2018-01-16 | 广东佳德环保科技有限公司 | A kind of ship flue gas desulfurization removes nitre device and technique |
| CN110385027A (en) * | 2019-07-04 | 2019-10-29 | 西安航天源动力工程有限公司 | A kind of ship tail gas pollutant collaboration processing unit |
| CN117357999A (en) * | 2023-12-04 | 2024-01-09 | 长春黄金研究院有限公司 | Instantaneous high-concentration nitrogen oxide flue gas treatment method |
| US12025040B2 (en) | 2019-09-10 | 2024-07-02 | Alfa Laval Corporate Ab | Exhaust gas cleaning system and method for cleaning exhaust gas and use of exhaust gas cleaning system |
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2017
- 2017-10-25 CN CN201721390834.3U patent/CN207546187U/en active Active
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107583429A (en) * | 2017-10-25 | 2018-01-16 | 广东佳德环保科技有限公司 | A kind of ship flue gas desulfurization removes nitre device and technique |
| CN110385027A (en) * | 2019-07-04 | 2019-10-29 | 西安航天源动力工程有限公司 | A kind of ship tail gas pollutant collaboration processing unit |
| CN110385027B (en) * | 2019-07-04 | 2024-05-28 | 西安航天源动力工程有限公司 | Ship tail gas pollutant cooperative treatment device |
| US12025040B2 (en) | 2019-09-10 | 2024-07-02 | Alfa Laval Corporate Ab | Exhaust gas cleaning system and method for cleaning exhaust gas and use of exhaust gas cleaning system |
| CN117357999A (en) * | 2023-12-04 | 2024-01-09 | 长春黄金研究院有限公司 | Instantaneous high-concentration nitrogen oxide flue gas treatment method |
| CN117357999B (en) * | 2023-12-04 | 2024-03-01 | 长春黄金研究院有限公司 | Instantaneous high-concentration nitrogen oxide flue gas treatment method |
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