CN204803151U - Boats and ships waste -gas desulfurization effluent treatment plant - Google Patents
Boats and ships waste -gas desulfurization effluent treatment plant Download PDFInfo
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- CN204803151U CN204803151U CN201520154526.5U CN201520154526U CN204803151U CN 204803151 U CN204803151 U CN 204803151U CN 201520154526 U CN201520154526 U CN 201520154526U CN 204803151 U CN204803151 U CN 204803151U
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Abstract
The utility model relates to a processing apparatus of boats and ships waste gas waste water especially relates to a boats and ships waste -gas desulfurization effluent treatment plant. Including desulfurization waste water storage tank, hydrocyclone separation unit, electric chemical treatment unit and collection storage tank, the cardinal principle is: desulfurization waste water passes through the pump and gets into the hydrocyclone separation unit, and the solid waste behind hydrocyclone separation is collected in the middle of the mud mortise. The upper solution of after -separating gets into special electric chemical treatment unit, and the positive pole adopts special metal oxide positive pole, and the negative pole adopts purpose -built porous graphite electrode to compressed air lets in near the negative pole. Utilize in pairs the electroxidation technique to produce H2O2 and carry out the deep oxidation processing with HClO to desulfurization waste water. Desired standard during desulfurization waste water after handling can satisfy the 8th regulation of IMO " boats and ships waste gas cleaning system guide rule (2009) " (MEPC. 184 (59).
Description
Technical field
The utility model relates to a kind for the treatment of unit of marine exhaust waste water, particularly relates to a kind of marine exhaust desulfurizing waste water processing device.
Background technology
When adopting Wet technique washing marine exhaust, oily substance imperfect combustion in marine exhaust, PAHs can enter in washing water.The emission standard of IMO " marine exhaust cleaning system directive/guide (2009) " (MEPC.184 (59)) the 8th article regulation PAHs.Investigate existing domestic and international marine exhaust desulfurizer, the research about the process of marine exhaust desulfurization wastewater is less, rarely has the detailed introduction of desulfuration waste water treatment process.Desulfurization wastewater is just by carrying out discharging or reuse after simple aerating oxidation or cyclonic separation process.COD value in desulfurization wastewater and turbidity value can only be reduced through the desulfurization wastewater of this operation process, can not polycyclic aromatic hydrocarbons (PAHs) in degradable removal desulfurization wastewater.The discharge index of washing water in IMO marine exhaust cleaning system can not be met.Therefore, must improve or develop new treatment technology to existing treatment technology and device.
Degraded for PAHs is removed, and method main both at home and abroad is at present absorption method and advanced oxidation processes.Absorption method utilizes that PAHs water solubility is low exactly and octanol-water system partition ratio is high, be easy to from aqueous phase, be assigned to the principle in settling and organic matter, utilize the PAHs in various Adsorbent For Removal of Heavy to remove, conventional sorbent material comprises gac, clay ore deposit (as zeolite, pyrrhosiderite, kaolinite, wilkinite etc.), bark, fiber, polyethylene etc.Advanced oxidation processes produces OH free radical by bringing out a series of radical chain reaction by different approaches exactly, attacks the various pollutents in water body, until be degraded to carbonic acid gas, water and other mineral salt, reaches the object of purifying water body.
The method of existing absorption method and advanced oxidation processes process PAHs has the following disadvantages:
1. absorption method: (1) treatment unit volume is large; (2) PAHs pollutent is adsorbed in after in sorbent material, needs to carry out secondary treatment to it, could really accomplish innoxious; (3) the desorption processing costs of sorbent material is high.
2. advanced oxidation processes: (1) reaction conditions requires harsh, easily generates secondary pollution material in reaction process; (2) entire system energy consumption is high, and treatment effect needs to be improved further.
Utility model content
The utility model, mainly for the PAHs in degraded desulfurization wastewater, adopts paired electrooxidation technology, utilizes the dual oxygenizement of negative electrode and anode to degrade to PAHs.Desulfurization wastewater through the process of particular electrical chemical treatment can meet the emission request of IMO to desulfurization wastewater, qualified discharge.
The utility model is intended adopting paired electrooxidation technology to carry out degradation treatment to the PAHs in desulfurization wastewater.Paired electrooxidation technology refers to the dual oxygenizement utilizing negative electrode and anode, the H that the HClO namely utilizing anode to produce and negative electrode produce
2o
2the organic technology of oxidative degradation, becomes the CO of environmental sound by PAHs oxygenolysis
2and H
2o, enables the PAHs in desulfurization wastewater meet the emission standard of IMO.Anode adopts and analyses chlorine ruthenium series metal oxide of good performance anode, and negative electrode adopts porous graphite electrode, and blasts O near negative electrode
2.Its cathode and anode process is as follows:
Negative electrode:
Anode:
A kind of marine exhaust desulfurizing waste water processing device is provided for this reason, comprises desulfurization wastewater storage tank, cyclonic separation unit, electrochemical processing cell and collection storage tank;
Be provided with desulfurization wastewater import above described desulfurization wastewater storage tank, inside is provided with liquidometer, and described liquidometer is provided with high liquid level warning point from top to bottom, high liquid level start-up point, low liquid level arrests; Described desulfurization wastewater storage tank side connects the first water pump, and the first water pump the other end is connected with cyclonic separation unit;
Described cyclonic separation unit comprises cyclone separator and sludge sump, and be provided with sewage draining exit to be opened/closed below described cyclone separator, sewage draining exit is connected with sludge sump; Described cyclone separator side is provided with leakage fluid dram, and leakage fluid dram connects the second water pump, and the second water pump the other end is connected with electrochemical processing cell;
Described electrochemical processing cell comprises the whipping appts being installed on inside, and metal oxide anode and porous graphite negative electrode, be provided with compressed air inlet near negative electrode; Described electrochemical processing cell side is provided with wastewater outlet, is connected with the 3rd water pump, and the 3rd water pump the other end is connected with collection storage tank;
Described collection tank inside is provided with liquidometer, and described liquidometer is provided with high liquid level warning point from top to bottom, high liquid level start-up point, low liquid level arrests; Described collection storage tank side is provided with discharge outlet, is connected with ship side external environment.
Further, described whipping appts is 80-150mA/cm in current density
2condition under open.
A kind of marine exhaust method for treating desulfurized wastewater, is made up of following steps:
(1) desulfurization wastewater is collected in desulfurization wastewater storage tank from slurry pool, and the reference mark of liquidometer carrys out Controlling System by three liquid level switches be fixed in desulfurization wastewater storage tank automatically to run according to program; When liquid level rises to the high liquid level start-up point of liquidometer, system starts to start; First water pump by when in desulfurization wastewater storage tank, waste water is evacuated to low liquid level arrests gradually, system closing; Under normal circumstances, system is run between these two Liquid level points.
Desulfurization wastewater is extracted out by (2) first water pumps from desulfurization wastewater storage tank, is transferred to cyclonic separation unit, removes the particulate matter in waste water by gravity centrifugal settling effect, reduces the turbidity value of waste water, reaches the object of solid-liquid separation; Sewage draining exit is opened, in the middle of the sludge sump below being collected by the solid slag obtained after cyclonic separation.
(3) liquid after cyclonic separation enters electrochemical processing cell by leakage fluid dram and the second water pump.Electrochemical processing cell anode adopts and analyses chlorine ruthenium series metal oxide of good performance anode, and negative electrode adopts porous graphite electrode.It is large that porous graphite electrode has specific surface area, absorption O
2the feature that ability is strong, is more conducive to H
2o
2generation.Whipping appts is installed in electrochemical cell inside, before beginning electrolysis, opens whipping appts, and blast pressurized air near negative electrode.Setting current density is 80-150mA/cm
2, pass into electric current and start electrolysis.Utilize HClO and H that anode and negative electrode produce
2o
2to the NO in desulfurization wastewater
x -oxidative degradation process is carried out with PAHs.
(4) desulfurization wastewater through electrochemical processing cell process enters in collection storage tank, leaves standstill and stops 20-30min.Collecting the liquid level detection system that in storage tank, installation is identical with desulfurization wastewater storage tank, according to the keying of the signal control valve of detection system feedback, by the liquid discharge after process to outside ship side.
Further, once there is the situations such as water pump damages, open-close on-off quits work, when liquid level rises to the high liquid level warning point of liquidometer, high liquid level warning switch is reported to the police by the high liquid level warning lamp started on switchboard.By the liquid level automatic checkout system of desulfurization wastewater storage tank, thus realize the startup of Waste Water Treatment, closedown and warning function.
The utility model adopts " cyclonic separation+electrooxidation in pairs ", and technology processes boats and ships desulfurization wastewater, and anode adopts and analyses chlorine ruthenium series metal oxide of good performance anode, and negative electrode adopts porous graphite electrode.Through desulfurization wastewater process verification experimental verification, compared with prior art, there is following unusual effect:
1., compared with the simple aerating oxidation adopted with current boats and ships desulfurization wastewater or cyclonic separation treatment technology, the utility model device fully can reduce suspended substance, the turbidity value of waste water.
2. can reach depth degradation process for the PAHs in desulfurization wastewater, reduce further the COD value of waste water.
3. electrochemical processing cell negative electrode adopts porous graphite electrode, has very large specific surface area, absorption O
2ability strengthen, be more conducive to H
2o
2generation.
4. system integration is high, takies volume little, and fully solving boats and ships can the limited shortcoming of usage space.
5. processing parameter reduces greatly, and entire system energy consumption significantly reduces, and final obvious processing effect improves.
Through the boats and ships desulfurization wastewater of this process technical finesse, specific targets all reach standard required in the regulation of IMO " marine exhaust cleaning system directive/guide (2009) " (MEPC.184 (59)) the 8th article.Specific targets are in table 1.
Index before and after the process of table 1. desulfurization wastewater
| Discharge index | IMO MEPC.184 (59) standard | Desulfurization wastewater after process |
| COD | ≦125mg/L | 80mg/L |
| pH | 6-8.5 | 7.1 |
| PAHs | ≦50ug/L | 10ug/L |
| NO X - | ≦60mg/L | 23mg/L |
Accompanying drawing explanation
In order to be illustrated more clearly in the utility model embodiment or technical scheme of the prior art, be briefly described to the accompanying drawing used required in embodiment or description of the prior art below, apparently, accompanying drawing in the following describes is embodiments more of the present utility model, for those of ordinary skill in the art, under the prerequisite not paying creative work, other accompanying drawing can also be obtained according to these accompanying drawings.
Fig. 1 is structural representation of the present utility model;
1 desulfurization wastewater storage tank in figure, 11 desulfurization wastewater imports, 2 cyclonic separation unit, 21 cyclone separators, 22 sludge sumps, 3 electrochemical processing cell, 31 whipping apptss, 32 anodes, 33 negative electrodes, 34 compressed air inlet, 4 collect storage tank, 5 liquidometers, 6 first water pumps, 7 second water pumps, 8 the 3rd water pumps.
Embodiment
For making the object of the utility model embodiment, technical scheme and advantage clearly, below in conjunction with the accompanying drawing in the utility model embodiment, technical scheme in the utility model embodiment is clearly and completely described, obviously, described embodiment is the utility model part embodiment, instead of whole embodiments.Based on the embodiment in the utility model, those of ordinary skill in the art are not making the every other embodiment obtained under creative work prerequisite, all belong to the scope of the utility model protection.
A kind of marine exhaust desulfurizing waste water processing device, comprises desulfurization wastewater storage tank 1, cyclonic separation unit 2, electrochemical processing cell 3 and collection storage tank 4;
Be provided with desulfurization wastewater import 11 above described desulfurization wastewater storage tank 1, inside is provided with liquidometer 5, and described liquidometer 5 is provided with high liquid level warning point from top to bottom, high liquid level start-up point, low liquid level arrests; Described desulfurization wastewater storage tank 1 side connects first water pump 6, first water pump 6 the other end and is connected with cyclonic separation unit 2;
Described cyclonic separation unit 2 comprises cyclone separator 21 and sludge sump 22, and be provided with sewage draining exit to be opened/closed below described cyclone separator 21, sewage draining exit is connected with sludge sump 22; Described cyclone separator 21 side is provided with leakage fluid dram, and leakage fluid dram connects second water pump 7, second water pump 7 the other end and is connected with electrochemical processing cell 3;
Described electrochemical processing cell 3 comprises the whipping appts 31 being installed on inside, and the anode 32 of ruthenium series metal oxide and the negative electrode 33 of porous graphite, be provided with compressed air inlet 34 near negative electrode 33; Described electrochemical processing cell 3 side is provided with wastewater outlet, is connected with the 3rd water pump 8, and the 3rd water pump 8 the other end is connected with collection storage tank 4;
Described collection storage tank 4 inside is provided with liquidometer 5, and described liquidometer 5 is provided with high liquid level warning point from top to bottom, high liquid level start-up point, low liquid level arrests; Described collection storage tank 4 side is provided with discharge outlet, is connected with ship side external environment.
Described whipping appts 31 is 120mA/cm in current density
2condition under open.
A kind of marine exhaust method for treating desulfurized wastewater, is made up of following steps:
(1) desulfurization wastewater is collected in desulfurization wastewater storage tank 1 from slurry pool, and the reference mark of liquidometer carrys out Controlling System by three liquid level switches be fixed in desulfurization wastewater storage tank 1 automatically to run according to program; When liquid level rises to the high liquid level start-up point of liquidometer 5, system starts to start; First water pump 6 by when in desulfurization wastewater storage tank 1, waste water is evacuated to low liquid level arrests gradually, system closing; Under normal circumstances, system is run between these two Liquid level points.
Desulfurization wastewater is extracted out by (2) first water pumps 6 from desulfurization wastewater storage tank 1, is transferred to cyclonic separation unit 2, removes the particulate matter in waste water by gravity centrifugal settling effect, reduces the turbidity value of waste water, reaches the object of solid-liquid separation; Sewage draining exit is opened, in the middle of the sludge sump 22 below being collected into by the solid slag obtained after cyclonic separation.
(3) liquid after cyclonic separation enters electrochemical processing cell 3 by leakage fluid dram and the second water pump 7, and whipping appts is installed in electrochemical cell inside, and anode adopts and analyses chlorine ruthenium series metal oxide of good performance anode, and negative electrode adopts porous graphite electrode.It is large that porous graphite electrode has specific surface area, absorption O
2ability strengthen feature, in electrolytic process, be more conducive to H
2o
2generation; Near negative electrode, pass into pressurized air, utilize paired electrooxidation technology to produce H
2o
2with HClO, oxidative degradation process is carried out to NOX-and PAHs in desulfurization wastewater.
(4) desulfurization wastewater processed through electrochemical processing cell 3 enters to be collected in storage tank 4, collecting the liquid level detection system that in storage tank 4, installation is identical with desulfurization wastewater storage tank 1, leaving standstill after stopping 25min and being disposed to outside ship side.
Once there is the situations such as water pump damages, open-close on-off quits work, when liquid level rises to the high liquid level warning point of liquidometer 5, high liquid level warning switch is reported to the police by the high liquid level warning lamp started on switchboard.By the liquid level automatic checkout system of desulfurization wastewater storage tank 1, thus realize the startup of Waste Water Treatment, closedown and warning function.
According to the method described above, boats and ships desulfurization wastewater is processed.According to the detection method specified in China Classification Society (CCS) marine exhaust cleaning system test load-efficiency guide to COD, pH, PAHs, the NO before and after desulfurization wastewater process
x -detect, detected result sees the following form 2:
Discharge index contrast before and after the process of table 2. desulfurization wastewater
| Discharge index | Before desulfurization wastewater process | After desulfurization wastewater process |
| COD | 267mg/L | 80mg/L |
| pH | 6.5 | 7.1 |
| PAHs | 513ug/L | 10ug/L |
| NO X - | 62mg/L | 23mg/L |
Claims (2)
1. a marine exhaust desulfurizing waste water processing device, is characterized in that: comprise desulfurization wastewater storage tank (1), cyclonic separation unit (2), electrochemical processing cell (3) and collection storage tank (4);
Described desulfurization wastewater storage tank (1) top is provided with desulfurization wastewater import (11), inside is provided with liquidometer (5), and described liquidometer (5) is provided with high liquid level warning point from top to bottom, high liquid level start-up point, low liquid level arrests; Described desulfurization wastewater storage tank (1) side connects the first water pump (6), and the first water pump (6) the other end is connected with cyclonic separation unit (2);
Described cyclonic separation unit (2) comprises cyclone separator (21) and sludge sump (22), described cyclone separator (21) below is provided with sewage draining exit to be opened/closed, and sewage draining exit is connected with sludge sump (22); Described cyclone separator (21) side is provided with leakage fluid dram, and leakage fluid dram connects the second water pump (7), and the second water pump (7) the other end is connected with electrochemical processing cell (3);
Described electrochemical processing cell (3) comprises the whipping appts (31) being installed on inside, the anode (32) of ruthenium series metal oxide and the negative electrode (33) of porous graphite, be provided with compressed air inlet (34) near negative electrode (33); Described electrochemical processing cell (3) side is provided with wastewater outlet, is connected with the 3rd water pump (8), and the 3rd water pump (8) the other end is connected with collection storage tank (4);
Described collection storage tank (4) inside is provided with liquidometer (5), and described liquidometer (5) is provided with high liquid level warning point from top to bottom, high liquid level start-up point, low liquid level arrests; Described collection storage tank (4) side is provided with discharge outlet, is connected with ship side external environment.
2. a kind of marine exhaust desulfurizing waste water processing device as claimed in claim 1, is characterized in that: described whipping appts (31) is 80-150mA/cm in current density
2condition under open.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520154526.5U CN204803151U (en) | 2015-03-18 | 2015-03-18 | Boats and ships waste -gas desulfurization effluent treatment plant |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520154526.5U CN204803151U (en) | 2015-03-18 | 2015-03-18 | Boats and ships waste -gas desulfurization effluent treatment plant |
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|---|---|
| CN204803151U true CN204803151U (en) | 2015-11-25 |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104761086A (en) * | 2015-03-18 | 2015-07-08 | 青岛双瑞海洋环境工程股份有限公司 | Ship waste gas desulfurization waste water treatment apparatus and method thereof |
-
2015
- 2015-03-18 CN CN201520154526.5U patent/CN204803151U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104761086A (en) * | 2015-03-18 | 2015-07-08 | 青岛双瑞海洋环境工程股份有限公司 | Ship waste gas desulfurization waste water treatment apparatus and method thereof |
| CN104761086B (en) * | 2015-03-18 | 2017-01-11 | 青岛双瑞海洋环境工程股份有限公司 | Ship waste gas desulfurization waste water treatment apparatus and method thereof |
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