CN105481189B - Marine domestic sewage processing system - Google Patents
Marine domestic sewage processing system Download PDFInfo
- Publication number
- CN105481189B CN105481189B CN201610024557.8A CN201610024557A CN105481189B CN 105481189 B CN105481189 B CN 105481189B CN 201610024557 A CN201610024557 A CN 201610024557A CN 105481189 B CN105481189 B CN 105481189B
- Authority
- CN
- China
- Prior art keywords
- auxiliary material
- connecting rod
- sewage
- pond
- pump housing
- 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
Links
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/30—Wastewater or sewage treatment systems using renewable energies
- Y02W10/37—Wastewater or sewage treatment systems using renewable energies using solar energy
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
- Treatment Of Sludge (AREA)
Abstract
The present invention provides marine domestic sewage processing system, it includes regulating reservoir, anoxic pond, wherein, regulating reservoir is connected with hull drainage system, regulating reservoir top is provided with preliminary screen pack, regulating reservoir bottom is provided with first pump housing, first pump housing is connected with mechanical grille, mechanical grille outlet is connected by connecting tube with anoxic pond, anoxic pond bottom is provided with some mixture pipes, auxiliary material addition mechanism is provided with the top of anoxic pond, anoxic pond top side is provided with overflow launder, and it is connected by overflow launder with membrane biological reaction pond, film reaction mechanism is provided with membrane biological reaction pond, Blast mechanism is provided with above film reaction mechanism.This programme significantly reduces the use load of freshwater resources on ship, is effectively saved resource.
Description
Technical field
The present invention relates to technical field of ships, refers in particular to marine domestic sewage processing system.
Background technology
Sewage from Ships is primarily referred to as the excrement water of people, including from the sewage of the discharges such as urinal, water closet and useless
Thing；From the sewage and waste of ward, the washbasin in clinic, bathtub and these place tap discharges；And with above-mentioned sewage
The daily life water that waste mixes（Refer to face washing water, water for bathing, laundry water, kitchen water etc.）Water is used with other.To ship
For oceangoing ship sanitary sewage, main processing method, which has, is aboard ship mounted directly sewage treatment unit, installation sanitary sewage receipts
Acquisition means, after the first is processing up to standard, rivers are directly discharged into, second is to collect ashore to handle.At present, ship in the world
Sewage treatment unit mainly has HAMWORTHY companies of Britain, WelBen companies, Red-Pox companies of the U.S., Japan
The biochemical process processing unit of SASAKURA companies etc..Their handling process is mostly activated sludge process.Because hydraulic detention time
（HRT）Long, device volume is big, although meeting ship inspection standard, is not suitable for China's actual conditions and ship shipping economic development and effect
Benefit requires.The boat domestic sewage treatment device that the country occurs mainly has three kinds, ST types（Activated sludge process）, WCB types（It is active dirty
Mud and contact oxidation method）And CSWA series（Two-stage biological catalytic oxidation --- AB methods）.Though they are several improved, all because dress
Put volume and be unsuitable for the more combination vessel of number greatly.In addition, the treatment technology of Sewage from Ships remains in biography both at home and abroad
On the aerobic biological treatment process of system.The larger Sewage from Ships that is primarily due to of Aerobic biological process device volume is mostly lavatory
Excrement flushing water, there is higher BOD and SS than city domestic sewage, aerobic microbiological is higher due to being limited in for being supplied oxygen
Load is handled together, it is necessary to which longer time is come the organic matter in sewage of degrading.In order to shorten the biochemical treatment time, impact is reduced
The influence of load and exercise effect, the in recent years optimum organization of various biochemical processing methods are tested and applied.Wherein anaerobic process
More and more it is taken seriously.For installing Domestic sewage collecting device, principle is simple, but operating cost is higher, restricted application.
For marine domestic sewage processing, direction is still aboard ship mounted directly sewage treatment unit, and simply research has certainly
The equipment of main intellectual property, to reduce cost.Japan is in terms of the research of marine domestic sewage processor, in the leading of the world
Level, the SBT type series ship sewage treatment devices that they study, can realize steamer blowdown directly up to standard, but expensive, right
For most of shipowner in China, it is difficult to undertake.
The content of the invention
Energy consumption is reduced it is an object of the invention to overcome the deficiencies of the prior art and provide one kind, is economized on resources, full automatic
Marine domestic sewage processing system.
To achieve the above object, technical scheme provided by the present invention is：Marine domestic sewage processing system, it includes
Regulating reservoir, anoxic pond, membrane biological reaction pond, secondary sedimentation tank, heat treatment mechanism, wherein, regulating reservoir and hull drainage system phase
Connection, regulating reservoir top are provided with preliminary screen pack, and regulating reservoir bottom is provided with first pump housing, and first pump housing is connected with mechanical grille
Connect, mechanical grille outlet is connected by connecting tube with anoxic pond, and anoxic pond bottom is provided with some mixture pipes, anoxic pond top
Portion is provided with auxiliary material addition mechanism, and anoxic pond top side is provided with overflow launder, and is connected by overflow launder with membrane biological reaction pond,
Film reaction mechanism is provided with membrane biological reaction pond, Blast mechanism is provided with above film reaction mechanism, the film positioned at overflow launder side is given birth to
Second pump housing is provided with thing reaction tank, the second pump housing outlet is extended in anoxic pond, and membrane biological reaction pond opposite side is provided with the 3rd
The pump housing, the 3rd pump housing outlet are connected with secondary sedimentation tank, and secondary sedimentation tank opposite side is provided with heat treatment mechanism, heat treatment mechanism
Exit connects provided with circulating water pipe, and heat treatment mechanism and circulating water pipe are provided with temperature-sensing valve between connecing；
Auxiliary material addition mechanism includes auxiliary material case, and auxiliary material upper box part is provided with auxiliary material storage bucket, auxiliary material storage bucket be it is square, it is auxiliary
Material storage bucket bottom is provided with inclined auxiliary material guide plate, and the relatively low one end side wall of auxiliary material guide plate is provided with auxiliary feed outlet, auxiliary feed outlet
Place is provided with auxiliary material controlling organization；Auxiliary material controlling organization includes ball float, controls connecting rod, connecting rod counterweight, wherein, in the middle part of controls connecting rod
By hinge in auxiliary material box cavity bottom, controls connecting rod one end is connected with ball float rope, and ball float rope bottom is provided with ball float, ball float
For three, the same one end of controls connecting rod is connected to by corresponding ball float rope respectively, the length of three ball float ropes differs；Control
The connecting rod other end is provided with connecting rod counterweight, is provided with separated time pulley in the auxiliary material case above connecting rod counterweight, the auxiliary material above separated time pulley
Storage bucket outer wall is provided with the first deflecting roller, and the first deflecting roller is two, auxiliary respectively on the outer wall of auxiliary material storage bucket both sides
The auxiliary material storage bucket outer wall of material outlet both sides is provided with the second deflecting roller, is set in the auxiliary material storage bucket side wall below the second deflecting roller
There is auxiliary material stopper slot；Activity is equipped with auxiliary material limit shaft in auxiliary material stopper slot, and auxiliary material control panel is provided with below auxiliary material limit shaft, auxiliary
Material control panel is engaged with auxiliary feed outlet, and the wherein side side wall of auxiliary material control panel is curved, and extrados is located at auxiliary material storage bucket
Inner chamber side；Auxiliary material limit shaft both ends are connected through auxiliary material stopper slot with control cord one end, and the control cord other end bypasses phase successively
It is connected after the second deflecting roller, the first deflecting roller and the separated time pulley answered with connecting rod counterweight；
Film reaction mechanism includes solarization air cell, membrane component, supporting plate, wherein, it is provided with supporting plate, supporting plate in the middle part of solarization air cell
Both sides are provided with membrane component, and membrane component is two pieces, is reserved respectively between supporting plate both sides, membrane component opposite side and supporting plate
Certain distance forms exhalant canal, aeration tube is provided with the solarization air cell below membrane component, aeration tube is two, respectively positioned at two
Below water inlet pipe；Aeration tube one end is connected through solarization air cell with Blast mechanism, and the aeration tube in solarization air cell is provided with some
Individual aeration nozzle, aeration nozzle are cylindrical shape, and the columnar cylinder lumen bottom is provided with up-small and down-big collecting chamber, on cylinder lumen
Portion is provided with spoiler of the outlet in spurting；Exhalant canal is connected with connecting tube, and connecting tube is connected with self priming pump, self priming pump
Outlet is connected with heat treatment mechanism；
Temperature-sensing valve includes valve body, temperature control spring, pushes up spring, check valve in advance, wherein, valve body one end and circulating water pipe are in succession
Connect, the other end is connected with heat treatment mechanism, body cavity one end be provided with it is stair-stepping spacing, it is spacing to connect one positioned at circulating water pipe
End, with spacing inconsistent, the other end is connected temperature control spring one end with pre- top spring one end, pre- to push up the spring other end and check valve
Inconsistent, the check valve other end is contradicted in valve body and the connecting portion of heat treatment mechanism.
The sewage water treatment method of the system, it includes following steps：
1st, caused sewage accesses regulating reservoir by drainpipe on ship,
2nd, impurity is tentatively filtered by preliminary screen pack into during regulating reservoir, is sent into and pressed by delivery pipe after filtering
Collected after the squeezing of crusher structure；
3rd, the sewage after filtering is pumped into mechanical grille by first pump housing and carries out impurity secondary filter, after secondary impurities filtering
Sewage enter anoxic pond in；
4th, auxiliary material is poured in auxiliary material storage bucket, and three ball floats are located at level height different in processing pond respectively, work as processing
When sewage in pond reaches bottom ball float position, the ball float of bottom is lifted up, and the balance of controls connecting rod is broken, to connecting rod
The inclined downward of counterweight one end, while drive control cord to decline, drive auxiliary material control panel to rise a spacing after being turned to by pulley
From opening auxiliary feed outlet bottom, auxiliary material fallen into processing pond from the indentation, there of opening；Example pushes away according to this, and sewage reaches second,
During three ball floats, drive auxiliary material control panel to rise by connecting rod counterweight and rise again, direct auxiliary feed outlet is opened completely, works as water level
During decline, ball float is vacantly fished, and connecting rod counterweight, which rises, blocks general who has surrendered's auxiliary feed outlet under auxiliary material control panel；
5th, Blast mechanism air feed after auxiliary material addition, mixture pipe spray bubble, are sufficiently mixed sewage and auxiliary material, decompose；
6th, mixed upper strata sewage is entered in membrane biological reaction pond by overflow launder and reacted, and reacted sewage has
Three kinds of processing modes, first, continuing to be pumped into anoxic pond secondary response by second pump housing, second, reacting by film reaction mechanism
After be directly accessed deodorizing sterilizing device carry out deodorizing sterilizing processing, third, by the 3rd pump housing be pumped into secondary sedimentation tank carry out again
Secondary precipitation, access deodorizing sterilizing device after precipitating again and carry out deodorizing sterilizing processing；
7th, the clear water after deodorizing sterilizing, which enters in heat treatment mechanism, is evaporated processing, and steam passes through at the top of heat treatment mechanism
Reduction cover be reduced into water and run in recycle by circulating water pipe.
The present invention after using such scheme, directly by solar energy system powered, and can substantially reduce energy consumption by the system,
Multistep treatment and finlling automatically are used simultaneously, completes full-automatic sewage processing, and the sewage after its high treating effect, processing reaches completely
To routine use requirement, the use load of freshwater resources on ship is significantly reduced, is effectively saved resource.
Brief description of the drawings
Fig. 1 is the overall structure diagram of the present invention.
The auxiliary material that Fig. 2 is the present invention adds structural scheme of mechanism.
Fig. 3 is the film reaction structural scheme of mechanism of the present invention.
Fig. 4 is the aeration tube structural representation of the present invention.
Fig. 5 is the temperature-sensing valve structural representation of the present invention.
Embodiment
With reference to all accompanying drawings, the invention will be further described, and presently preferred embodiments of the present invention is：Referring to accompanying drawing 1 to
Accompanying drawing 5, the marine domestic sewage processing system described in the present embodiment include regulating reservoir 1, anoxic pond 2, membrane biological reaction pond 3,
Secondary sedimentation tank 4, heat treatment mechanism 5, wherein, regulating reservoir 1 is connected with hull drainage system, and the top of regulating reservoir 1 is provided with preliminary
Screen pack 6, the bottom of regulating reservoir 1 are provided with first pump housing 7, and first pump housing 7 is connected with mechanical grille 8, and the outlet of mechanical grille 8 passes through
Connecting tube is connected with anoxic pond 2, and the bottom of anoxic pond 2 is provided with some mixture pipes 9, and the top of anoxic pond 2 is provided with auxiliary material and added
Mechanism 10, the top side of anoxic pond 2 is provided with overflow launder 11, and is connected by overflow launder 11 with membrane biological reaction pond 3, film biology
Film reaction mechanism 12 is provided with reaction tank 3, the top of film reaction mechanism 12 is provided with Blast mechanism 13, the film positioned at the side of overflow launder 11
Second pump housing 14 is provided with biological reaction pool 3, the outlet of second pump housing 14 is extended in anoxic pond 2, the opposite side of membrane biological reaction pond 3
Provided with the 3rd pump housing 15, the outlet of the 3rd pump housing 15 is connected with secondary sedimentation tank 4, and the opposite side of secondary sedimentation tank 4 is provided with heat treatment
Mechanism 5, the exit of heat treatment mechanism 5 connect 16 provided with circulating water pipe, and heat treatment mechanism 5 and circulating water pipe are provided with temperature control between connecing 16
Valve 19；
Auxiliary material addition mechanism 10 includes auxiliary material case A1, and auxiliary material case A1 tops are provided with auxiliary material storage bucket A4, auxiliary material storage bucket
A4 is square, and auxiliary material storage bucket A4 bottoms are provided with inclined auxiliary material guide plate A5, and one end side wall relatively low auxiliary material guide plate A5 is provided with
Auxiliary material controlling organization is provided with auxiliary feed outlet A6, auxiliary feed outlet A6；Auxiliary material controlling organization include ball float A7, controls connecting rod A8,
Connecting rod counterweight A9, wherein, connected in the middle part of controls connecting rod A8 by hinge in auxiliary material case A1 inner chambers bottom, controls connecting rod A8 one end
Ball float rope A10 is connected to, ball float rope A10 bottoms are provided with ball float A7, and ball float A7 is three, is connected respectively by corresponding ball float rope A10
The same one end of controls connecting rod A8 is connected on, three ball float rope A10 length differs；The controls connecting rod A8 other ends are provided with connecting rod counterweight
Separated time pulley A11 is provided with auxiliary material case A1 above A9, connecting rod counterweight A9, outside the auxiliary material storage bucket A4 above separated time pulley A11
It is two that wall, which is provided with the first deflecting roller A12, the first deflecting roller A12, auxiliary respectively on the outer wall of auxiliary material storage bucket A4 both sides
The auxiliary material storage bucket A4 outer walls of material outlet A6 both sides are provided with the auxiliary material storage below the second deflecting roller A13, the second deflecting roller A13
Bucket A4 side walls are provided with auxiliary material stopper slot A14；Activity is equipped with auxiliary material limit shaft A15, auxiliary material limit shaft in auxiliary material stopper slot A14
It is engaged below A15 provided with auxiliary material control panel A3, auxiliary material control panel A3 with auxiliary feed outlet A6, auxiliary material control panel A3 wherein side
Side wall is curved, and extrados is located at auxiliary material storage bucket A4 inner chambers side；Auxiliary material limit shaft A15 both ends pass through auxiliary material stopper slot A14
Be connected with control cord A2 one end, the control cord A2 other ends successively around corresponding second deflecting roller A13, the first deflecting roller A12 and
It is connected after separated time pulley A11 with connecting rod counterweight A9；
Film reaction mechanism 12 includes solarization air cell B1, membrane component B4, supporting plate B3, wherein, branch is provided with the middle part of solarization air cell B1
Fagging B3, supporting plate B3 both sides are provided with membrane component B4, and membrane component B4 is two pieces, and one is reserved between membrane component B4 and supporting plate B3
Aeration tube B6 is provided with solarization air cell B1 below set a distance formation exhalant canal B5, membrane component B4, aeration tube B6 is two, respectively
Below two water inlet pipe B2；Aeration tube B6 one end is connected through solarization air cell B1 with Blast mechanism 13, in solarization air cell B1
Aeration tube B6 provided with several aeration nozzles B7, aeration nozzle B7 be cylindrical shape, the columnar cylinder lumen bottom is provided with upper
Small lower big collecting chamber, cylinder lumen top are provided with spoiler B8 of the outlet in spurting；Exhalant canal B5 and the phase of connecting tube 17
Connection, connecting tube 17 are connected with self priming pump 18, and the outlet of self priming pump 18 is connected with heat treatment mechanism 5；
Temperature-sensing valve 19 includes valve body C12, temperature control spring C13, pre- top spring C14, check valve C15, wherein, valve body C12
One end connects 16 with circulating water pipe and is connected, and the other end is connected with heat treatment mechanism 5, and valve body C12 inner chambers one end is provided with stair-stepping limit
Position, spacing to connect 16 one end positioned at circulating water pipe, temperature control spring C13 one end is with spacing inconsistent, the other end and pre- top spring C14 mono-
End is connected, and pre- the top spring C14 other ends and check valve C15 are inconsistent, and the check valve C15 other ends are contradicted in valve body C12 and heat
The connecting portion of processing mechanism 5.
The sewage water treatment method of the system includes following steps：
1st, caused sewage accesses regulating reservoir by drainpipe on ship,
2nd, impurity is tentatively filtered by preliminary screen pack into during regulating reservoir, is sent into and pressed by delivery pipe after filtering
Collected after the squeezing of crusher structure；
3rd, the sewage after filtering is pumped into mechanical grille by first pump housing and carries out impurity secondary filter, after secondary impurities filtering
Sewage enter anoxic pond in；
4th, auxiliary material is poured in auxiliary material storage bucket, and three ball floats are located at level height different in processing pond respectively, work as processing
When sewage in pond reaches bottom ball float position, the ball float of bottom is lifted up, and the balance of controls connecting rod is broken, to connecting rod
The inclined downward of counterweight one end, while drive control cord to decline, drive auxiliary material control panel to rise a spacing after being turned to by pulley
From opening auxiliary feed outlet bottom, auxiliary material fallen into processing pond from the indentation, there of opening；Example pushes away according to this, and sewage reaches second,
During three ball floats, drive auxiliary material control panel to rise by connecting rod counterweight and rise again, direct auxiliary feed outlet is opened completely, works as water level
During decline, ball float is vacantly fished, and connecting rod counterweight, which rises, blocks general who has surrendered's auxiliary feed outlet under auxiliary material control panel；
5th, Blast mechanism air feed after auxiliary material addition, mixture pipe spray bubble, are sufficiently mixed sewage and auxiliary material, decompose；
6th, mixed upper strata sewage is entered in membrane biological reaction pond by overflow launder and reacted, and reacted sewage has
Three kinds of processing modes, first, continuing to be pumped into anoxic pond secondary response by second pump housing, second, reacting by film reaction mechanism
After be directly accessed deodorizing sterilizing device carry out deodorizing sterilizing processing, third, by the 3rd pump housing be pumped into secondary sedimentation tank carry out again
Secondary precipitation, access deodorizing sterilizing device after precipitating again and carry out deodorizing sterilizing processing；
7th, the clear water after deodorizing sterilizing, which enters in heat treatment mechanism, is evaporated processing, and steam passes through at the top of heat treatment mechanism
Reduction cover be reduced into water and run in recycle by circulating water pipe.
The present embodiment is directly powered by solar energy system, can substantially reduce energy consumption, while using multistep treatment and certainly
Dynamic filling, full-automatic sewage processing is completed, routine use requirement is fully achieved in the sewage after its high treating effect, processing, significantly
The use load of freshwater resources on ship is alleviated, is effectively saved resource.
Embodiment described above is only the preferred embodiments of the invention, and the practical range of the present invention is not limited with this,
Therefore the change that all shape, principles according to the present invention are made, it all should cover within the scope of the present invention.
Claims (2)
1. marine domestic sewage processing system, it is characterised in that：It includes regulating reservoir（1）, anoxic pond（2）, membrane biological reaction
Pond（3）, secondary sedimentation tank（4）, heat treatment mechanism（5）, wherein, regulating reservoir（1）It is connected with hull drainage system, regulating reservoir
（1）Top is provided with preliminary screen pack（6）, regulating reservoir（1）Bottom is provided with first pump housing（7）, first pump housing（7）With mechanical grille
（8）It is connected, mechanical grille（8）Outlet passes through connecting tube and anoxic pond（2）It is connected, anoxic pond（2）Bottom is provided with some
Mixture pipe（9）, anoxic pond（2）Top is provided with auxiliary material addition mechanism（10）, anoxic pond（2）Top side is provided with overflow launder
（11）, and pass through overflow launder（11）With membrane biological reaction pond（3）It is connected, membrane biological reaction pond（3）It is interior to be provided with film reaction mechanism
（12）, film reaction mechanism（12）Top is provided with Blast mechanism（13）, positioned at overflow launder（11）The membrane biological reaction pond of side（3）It is interior
Provided with second pump housing（14）, second pump housing（14）Outlet extends to anoxic pond（2）It is interior, membrane biological reaction pond（3）Opposite side is provided with
3rd pump housing（15）, the 3rd pump housing（15）Outlet and secondary sedimentation tank（4）It is connected, secondary sedimentation tank（4）Opposite side is provided with heat
Processing mechanism（5）, heat treatment mechanism（5）Exit connects provided with circulating water pipe（16）, heat treatment mechanism（5）Connect with circulating water pipe
（16）Between be provided with temperature-sensing valve（19）；
Auxiliary material adds mechanism（10）Include auxiliary material case（A1）, auxiliary material case（A1）Top is provided with auxiliary material storage bucket（A4）, auxiliary material storage
Deposit bucket（A4）To be square, auxiliary material storage bucket（A4）Bottom is provided with inclined auxiliary material guide plate（A5）, auxiliary material guide plate（A5）Relatively low one
Side wall is provided with auxiliary feed outlet（A6）, auxiliary feed outlet（A6）Place is provided with auxiliary material controlling organization；Auxiliary material controlling organization includes floating
Ball（A7）, controls connecting rod（A8）, connecting rod counterweight（A9）, wherein, controls connecting rod（A8）Middle part is by hinge in auxiliary material case
（A1）Inner chamber bottom, controls connecting rod（A8）One end is connected with ball float rope（A10）, ball float rope（A10）Bottom is provided with ball float（A7）, float
Ball（A7）For three, pass through corresponding ball float rope respectively（A10）It is connected to controls connecting rod（A8）Same one end, three ball float ropes
（A10）Length differ；Controls connecting rod（A8）The other end is provided with connecting rod counterweight（A9）, connecting rod counterweight（A9）The auxiliary material of top
Case（A1）It is interior to be provided with separated time pulley（A11）, separated time pulley（A11）The auxiliary material storage bucket of top（A4）Outer wall is provided with first and turned to
Wheel（A12）, the first deflecting roller（A12）For two, respectively positioned at auxiliary material storage bucket（A4）On the outer wall of both sides, auxiliary feed outlet（A6）
The auxiliary material storage bucket of both sides（A4）Outer wall is provided with the second deflecting roller（A13）, the second deflecting roller（A13）The auxiliary material storage bucket of lower section
（A4）Side wall is provided with auxiliary material stopper slot（A14）；Auxiliary material stopper slot（A14）Interior activity is equipped with auxiliary material limit shaft（A15）, auxiliary material
Limit shaft（A15）Lower section is provided with auxiliary material control panel（A3）, auxiliary material control panel（A3）With auxiliary feed outlet（A6）It is engaged, auxiliary material control
Plate（A3）Wherein side side wall it is curved, extrados is located at auxiliary material storage bucket（A4）Inner chamber side；Auxiliary material limit shaft（A15）Two
Hold through auxiliary material stopper slot（A14）With control cord（A2）One end connects, control cord（A2）The other end bypasses corresponding second successively
Deflecting roller（A13）, the first deflecting roller（A12）With separated time pulley（A11）Afterwards with connecting rod counterweight（A9）It is connected；
Film reaction mechanism（12）Include solarization air cell（B1）, membrane component（B4）, supporting plate（B3）, wherein, solarization air cell（B1）Middle part
Provided with supporting plate（B3）, supporting plate（B3）Both sides are provided with membrane component（B4）, membrane component（B4）For two pieces, respectively positioned at supporting plate
（B3）Both sides, membrane component（B4）Opposite side and supporting plate（B3）Between reserve certain distance formed exhalant canal（B5）, membrane component
（B4）The solarization air cell of lower section（B1）It is interior to be provided with aeration tube（B6）, aeration tube（B6）For two, respectively positioned at two water inlet pipes（B2）
Lower section；Aeration tube（B6）One end passes through solarization air cell（B1）With Blast mechanism（13）Connection, positioned at solarization air cell（B1）Interior aeration tube
（B6）It is provided with several aeration nozzles（B7）, aeration nozzle（B7）For cylindrical shape, the columnar cylinder lumen bottom is provided with upper small
Big collecting chamber down, cylinder lumen top are provided with spoiler of the outlet in spurting（B8）；Exhalant canal（B5）With connecting tube
（17）It is connected, connecting tube（17）With self priming pump（18）It is connected, self priming pump（18）Outlet and heat treatment mechanism（5）It is connected；
Temperature-sensing valve（19）Include valve body（C12）, temperature control spring（C13）, push up spring in advance（C14）, check valve（C15）, wherein, valve
Body（C12）One end connects with circulating water pipe（16）Connection, the other end and heat treatment mechanism（5）Connection, valve body（C12）Inner chamber one end is set
Have it is stair-stepping spacing, it is spacing to be connect positioned at circulating water pipe（16）One end, temperature control spring（C13）One end is another with spacing inconsistent
End and pre- top spring（C14）One end is connected, and pushes up spring in advance（C14）The other end and check valve（C15）It is inconsistent, check valve
（C15）The other end is contradicted in valve body（C12）With heat treatment mechanism（5）Connecting portion.
2. the sewage water treatment method of system described in claim 1, it is characterised in that：It includes following steps：
1）, caused sewage accesses regulating reservoir by drainpipe on ship,
2）, into during regulating reservoir impurity is tentatively filtered by preliminary screen pack, pass through delivery pipe after filtering and be sent into squeezing
Collected after mechanism squeezing；
3）, the sewage after filtering mechanical grille is pumped into by first pump housing and carries out impurity secondary filter, after secondary impurities filtering
Sewage enters in anoxic pond；
4）, auxiliary material be poured in auxiliary material storage bucket, three ball floats level height different in the processing pond respectively, when in processing pond
Sewage when reaching bottom ball float position, the ball float of bottom is lifted up, and the balance of controls connecting rod is broken, to connecting rod counterweight
The inclined downward of one end, while drive control cord to decline, drive auxiliary material control panel to rise certain distance after being turned to by pulley, make
Auxiliary feed outlet bottom is opened, and auxiliary material is fallen into processing pond from the indentation, there of opening；Example pushes away according to this, and sewage reaches second, third
During ball float, drive auxiliary material control panel to rise by connecting rod counterweight and rise again, direct auxiliary feed outlet is opened completely, works as water level decreasing
When, ball float is vacantly fished, and connecting rod counterweight, which rises, blocks general who has surrendered's auxiliary feed outlet under auxiliary material control panel；
5）, auxiliary material addition after Blast mechanism air feed, mixture pipe spray bubble, be sufficiently mixed sewage and auxiliary material, decompose；
6）, mixed upper strata sewage entered by overflow launder in membrane biological reaction pond and reacted, reacted sewage has three
Kind processing mode, first, continuing to be pumped into anoxic pond secondary response by second pump housing, second, after reacting by film reaction mechanism
It is directly accessed deodorizing sterilizing device and carries out deodorizing sterilizing processing, is carried out again third, being pumped into secondary sedimentation tank by the 3rd pump housing
Precipitation, access deodorizing sterilizing device after precipitating again and carry out deodorizing sterilizing processing；
7）, the clear water after deodorizing sterilizing enter in heat treatment mechanism and be evaporated processing, steam by heat treatment mechanism at the top of
Reduction cover is reduced into water and runs in recycle by circulating water pipe.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610024557.8A CN105481189B (en) | 2016-01-15 | 2016-01-15 | Marine domestic sewage processing system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610024557.8A CN105481189B (en) | 2016-01-15 | 2016-01-15 | Marine domestic sewage processing system |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN105481189A CN105481189A (en) | 2016-04-13 |
| CN105481189B true CN105481189B (en) | 2018-03-23 |
Family
ID=55668523
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610024557.8A Active CN105481189B (en) | 2016-01-15 | 2016-01-15 | Marine domestic sewage processing system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN105481189B (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107381929A (en) * | 2016-05-16 | 2017-11-24 | 福建双环能源科技股份有限公司 | A kind of vehicle-mounted water processing system |
| CN109323740B (en) * | 2017-08-01 | 2024-02-27 | 司米厨柜有限公司 | High-precision weighing rechecking system |
| IL287695B (en) * | 2019-04-29 | 2022-09-01 | Zero Discharge Llc | Zero discharge water treatment apparatus and method |
| CN112229874B (en) * | 2020-10-19 | 2023-08-01 | 重庆电子工程职业学院 | Liquid-saving reversing device for biosensor equipment |
Family Cites Families (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2680655Y (en) * | 2004-03-05 | 2005-02-23 | 陈秋竹 | Continental river ship sewage treating equipment |
| CN100337928C (en) * | 2005-07-09 | 2007-09-19 | 蒋遂安 | Method for nonmud purifying treating of ship sewage and its equipment |
| KR101138003B1 (en) * | 2010-04-05 | 2012-04-20 | 주식회사 엔케이 | Apparatus for multi-processing of wasted water in a ship |
| CN103910471A (en) * | 2014-04-09 | 2014-07-09 | 上海华业水处理工程有限公司 | Integrative composite structure of marine internal and external circulation three-phase biological fluidized beds |
| CN205387526U (en) * | 2016-01-15 | 2016-07-20 | 沅江精一科技机械制造有限公司 | Marine sewage treatment system |
-
2016
- 2016-01-15 CN CN201610024557.8A patent/CN105481189B/en active Active
Also Published As
| Publication number | Publication date |
|---|---|
| CN105481189A (en) | 2016-04-13 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN105481189B (en) | Marine domestic sewage processing system | |
| CN206014509U (en) | A kind of two-phase laminated flow inner-outer circulation anaerobic reactor | |
| CN103011404B (en) | Internal-mixing anaerobic reaction tank | |
| CN205387526U (en) | Marine sewage treatment system | |
| CN202379803U (en) | Staggered flow type aeration, sediment and filter device | |
| CN209853873U (en) | Integrated high-efficiency water purifying device | |
| CN205528252U (en) | Take sewage treatment plant of auxiliary material automatic control function | |
| CN203007037U (en) | Internal mixing anaerobic reactor | |
| CN205740499U (en) | A kind of reaction tower | |
| CN111777178B (en) | Vertical oxidation ditch micro-power water treatment system | |
| CN108862571A (en) | A kind of integral bio Air Exposure equipment | |
| CN201932945U (en) | Catalytic oxidation fluidization bed | |
| CN205473204U (en) | Split type treatment of domestic sewage ware of passenger traffic ship | |
| CN208829499U (en) | Miniature sanitary sewage integrated treatment tank | |
| CN205528251U (en) | Passenger traffic ship treatment of domestic sewage ware | |
| CN207596550U (en) | A kind of bio-aeration pool | |
| CN206970303U (en) | A kind of levitation device focused on for aquatic building sanitary sewage | |
| CN205473203U (en) | Marine multi -functional sewage treatment system of passenger traffic | |
| CN101857322A (en) | Removable trash transfer station sewage disposal device | |
| CN207671767U (en) | A kind of anaerobism Impulsive tank for wastewater treatment | |
| CN207294326U (en) | A kind of upflow anaerobic sludge blanket reactor of belt stirrer | |
| CN111056632A (en) | Anaerobic external tubular ultrafiltration membrane bioreactor | |
| CN204824547U (en) | Float formula river course purifier | |
| CN205635275U (en) | High -efficient sewage treatment unit of integration | |
| CN201424410Y (en) | Movable sewage purification treatment device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant |