Movatterモバイル変換


[0]ホーム

URL:


CN104176861B - A kind of offshore platform domestic sewage processing method - Google Patents

A kind of offshore platform domestic sewage processing method
Download PDF

Info

Publication number
CN104176861B
CN104176861BCN201410407386.8ACN201410407386ACN104176861BCN 104176861 BCN104176861 BCN 104176861BCN 201410407386 ACN201410407386 ACN 201410407386ACN 104176861 BCN104176861 BCN 104176861B
Authority
CN
China
Prior art keywords
sewage
sterilization pool
sterilization
sterilized water
tank
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active
Application number
CN201410407386.8A
Other languages
Chinese (zh)
Other versions
CN104176861A (en
Inventor
张保华
李波
王亮
孔祥军
刘艳武
雷岗星
付胜楠
王静
张楠
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Co Ltd Of Hai Youzong Energy-Saving And Emission-Reduction Monitoring Center
CNOOC Energy Technology and Services Ltd
Original Assignee
Co Ltd Of Hai Youzong Energy-Saving And Emission-Reduction Monitoring Center
China National Offshore Oil Corp CNOOC
CNOOC Energy Technology and Services Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Co Ltd Of Hai Youzong Energy-Saving And Emission-Reduction Monitoring Center, China National Offshore Oil Corp CNOOC, CNOOC Energy Technology and Services LtdfiledCriticalCo Ltd Of Hai Youzong Energy-Saving And Emission-Reduction Monitoring Center
Priority to CN201410407386.8ApriorityCriticalpatent/CN104176861B/en
Publication of CN104176861ApublicationCriticalpatent/CN104176861A/en
Application grantedgrantedCritical
Publication of CN104176861BpublicationCriticalpatent/CN104176861B/en
Activelegal-statusCriticalCurrent
Anticipated expirationlegal-statusCritical

Links

Landscapes

Abstract

The invention discloses a kind of offshore platform domestic sewage processing method, it comprises the following steps: (1) sends into equalizing tank after kitchen drainage is removed oil slick by oil trap, mix with excrement and urine waste and other drainings in equalizing tank, then pump in sterilization pool by sewage output tube; (2), after seawater is softening by softening installation, pump in brine tank, in brine tank, add solid sodium chloride, pump into electrolyzer after preparation strong brine and generate the sterilized water containing clorox, then sterilized water is pumped in sterilization pool; (3) sewage and sterilized water mixing in sterilization pool, and use agitator rapid stirring, realize the elimination to bacterium in sewage; (4) sewage after flocculation, sterilization flows in settling tank automatically, and after leaving standstill, supernatant liquid directly arranges sea after reaching emission standard.Adopt present method by electrolysis after seawater salt adding, heighten electrolytic efficiency.Avoid the damage of the organism in sewage to electrode, improve the work-ing life of electrode.

Description

A kind of offshore platform domestic sewage processing method
Technical field
The present invention relates to sanitary sewage disposal, particularly relate to the treatment process of marine oil production vessel, drilling unit, floating type production, storage and offloading device (FPSO) and oceangoing vessel sanitary sewage.
Background technology
Offshore platform sanitary sewage refers to the sewage (being commonly called as Heisui River) containing excrement, urine that platform lavatory is discharged, the sewage containing washing composition that the kitchen in platform production facility district, toilet, washing place discharge and the sewage (being commonly called as buck) that consulting room is got rid of.
For protecting the marine environment; country comes into effect " offshore oil exploration and exploitation Pollutant emission concentration limit value " (GB4914-2008) standard on May 1st, 2009; regulation is made to the COD limit value that offshore oil exploration and exploitation is arranged in extra large sanitary sewage, has seen the following form.
Sanitary sewage emission concentration limit value unit: mg/L
Current offshore platform process sanitary sewage has two kinds of methods.One is biochemical process, the microorganism in active sludge is utilized to degrade to the pollutent in sanitary sewage, but offshore platform is due to away from land, in order to save Freshwater resources, platform all uses seawater flushing lavatory, cause saltiness in sewage to increase, microorganism active is declined or inactivation, and the treatment effect of practical application mesophytization method to sanitary sewage is unsatisfactory.Another kind is electrolytic process, the sanitary sewage being mixed with seawater is carried out electrolysis, and the clorox (NaClO) of generation is Strong oxdiative sterilizing agent, can contact with the bacterium of sewage fully, by sterilization, reach the object removing pollutent, but in actual use, because in seawater, saltiness only has about 3%, electrolytic process can waste a large amount of electric energy, and electrolytic process is that the organic pollutant in sewage very easily causes electrode damage, reduction of service life by electrolysis after seawater and sanitary sewage mixing.
Summary of the invention
The object of the invention is to the shortcoming overcoming prior art, a kind of power-saving, offshore platform sewage treatment unit that long service life, treatment effect are good is provided.
A kind of offshore platform domestic sewage processing method of the present invention, it comprises the following steps:
(1) send into equalizing tank after kitchen drainage being removed oil slick by oil trap, mix with excrement and urine waste and other drainings in equalizing tank, then pump in sterilization pool by sewage output tube;
(2) after the seawater on less than 5 meters, sea is softening by softening installation, pump in brine tank, solid sodium chloride is added in brine tank, be mixed with after massfraction is greater than the strong brine of 20%, electrolyzer is pumped into by salt water delivery pipe, in electrolyzer, generate the sterilized water containing clorox, then sterilized water is pumped in sterilization pool;
(3) sewage and sterilized water mixing in sterilization pool, and use agitator rapid stirring, realize the elimination to bacterium in sewage, in sterilization pool, be provided with some groups of iron-carbon galvanic cells can produce ferrous ion and carbon granules simultaneously, while realization sterilization, passes through throwing out, remove the suspended contamination in sewage,, between galvanic cell, there is electrochemical oxidation decomposition reaction, change the organism of more easily degrading in the organic compound simultaneously in sewage;
(4) sewage after flocculation, sterilization flows in settling tank automatically, and after leaving standstill, supernatant liquid directly arranges sea after reaching emission standard; Lower floor's mud enters in plate-and-frame filter press, and the dewatered sludge obtained transports land process back, after pressing filtering liquid is qualified after testing, directly arranges sea, if defective, in pressing filtering liquid recycle pump suction sterilization pool, continues process, until again arrange sea after qualified.
The present invention compared with prior art, has the following advantages:
(1) by electrolysis after seawater salt adding, heighten electrolytic efficiency, while producing the sterilized water higher containing clorox (NaClO), save electric energy.
(2) sewage directly enters sterilization pool, only carries out electrolysis to high density salt solution, avoid the damage of the organism in sewage to electrode, improve the work-ing life of electrode at electrolyzer.
(3) iron-carbon galvanic cell is used, the ferrous ion produced and carbon granules, play throwing out to the suspended substance in sewage, the electrochemical energy simultaneously produced further promotes organic decomposition in sewage, and galvanic cell has advantages such as cost is low, long service life, usage space are little.
(4) mud is after pressure filter compacting mummification, transports land process back, no longer directly arranges sea, reduce further the pollution to ocean.
Accompanying drawing explanation
Fig. 1 is the schema of a kind of offshore platform domestic sewage processing method of the present invention.
Embodiment
Below in conjunction with Fig. 1 and specific embodiment, the present invention is described in detail:
Of the present invention a kind of offshore platform domestic sewage processing method as shown in Figure 1, it comprises the following steps: (1) sends into equalizing tank 7 after kitchen drainage is removed oil slick by oil trap 4, mix with excrement and urine waste and other drainings in equalizing tank, then pump in sterilization pool by sewage output tube; (2) after the seawater on less than 5 meters, sea is softening by softening installation, pump in brine tank 11, solid sodium chloride is added in brine tank, be mixed with after massfraction is greater than the strong brine of 20%, electrolyzer 14 is pumped into by salt water delivery pipe, in electrolyzer, generate the sterilized water containing clorox, then sterilized water is pumped in sterilization pool 17; (3) sewage and sterilized water mixing in sterilization pool, and with agitator 19 rapid stirring, realize the elimination to bacterium in sewage, some groups of iron-carbon galvanic cells are installed in sterilization pool simultaneously, ferrous ion and carbon granules can be produced, while realization sterilization, also by throwing out, remove the suspended contamination in sewage, the organic compound simultaneously in sewage, between galvanic cell, there is electrochemical oxidation decomposition reaction, change the organism of more easily degrading into; (4) sewage after flocculation, sterilization flows in settling tank automatically, and after leaving standstill, supernatant liquid directly arranges sea (COD≤300mg/L) after reaching emission standard; Lower floor's mud enters in plate-and-frame filter press 22, and the dewatered sludge obtained transports land process back, and pressing filtering liquid is qualified rear (COD≤300mg/L) after testing, directly row sea, if defective, in pressing filtering liquid recycle pump suction sterilization pool, continue process, until again arrange sea after qualified.
As the device realizing the inventive method, it comprises equalizing tank 7, and there are oil trap 4 and liquidometer 6 in inside, is imported by kitchen drainage 2 in oil trap 4, after removing oil slick, mixes, pump in sterilization pool 17 through sewage output tube 13 with excrement and urine waste and other drainings 1.Oil slick recovery port 5 and emergency overflow mouth 3 is offered in equalizing tank 7.
After seawater 9 is softening by softening installation 10, pump in brine tank 11, be provided with in brine tank 11 and throw salt mouth, add solid sodium chloride by throwing salt mouth 8, be mixed with after massfraction is greater than the dense salt solution of 20%, brine tank 11 is connected with electrolyzer 14 by salt water delivery pipe 12, electrolyzer 14 is connected by pipeline with sterilization pool 17, dense salt solution pumps into electrolyzer 14, generates the sterilized water containing clorox (NaClO), then pumped in sterilization pool 17 by sterilized water in electrolyzer 14.Electrolyzer 14 offers hydrogen discharge mouth 15, carries out voltage-regulation by electrolyzer control panel 16.
Sewage and sterilized water mixing in sterilization pool 17, and with agitator 19 rapid stirring, realize the elimination to bacterium in sewage, some groups of iron-carbon galvanic cells 18 are installed in sterilization pool 17 simultaneously, ferrous ion and carbon granules can be produced, remove the suspended contamination in sewage by throwing out.
Sewage after flocculation, sterilization flows in settling tank 20 automatically, and after leaving standstill 45min, the Sewage outlet 21 of supernatant liquid through being arranged on settling tank 20 top arranges sea; Lower floor's mud is through manually entering in plate-and-frame filter press 22, and the dewatered sludge obtained transports land process back, after pressing filtering liquid detection is qualified, directly sea is arranged, if defective, in pressing filtering liquid recycle pump 24 suction sterilization pool 17 through pressing filtering liquid discharge outlet 23, continue process, until again arrange sea after qualified.
Embodiment 1
(1) send into equalizing tank after kitchen drainage being removed oil slick by oil trap, mix with excrement and urine waste and other drainings in equalizing tank, then pass through sewage output tube with 1.5m3the flow of/h pumps in sterilization pool;
(2) after the seawater on less than 5 meters, sea is softening by softening installation, pump in brine tank, in brine tank, add solid sodium chloride, be mixed with after massfraction is greater than the strong brine of 20%, by salt water delivery pipe pump with 0.5m3the flow of/h pumps into electrolyzer, generates the sterilized water containing clorox, then pump in sterilization pool by sterilized water in electrolyzer;
(3) sewage and sterilized water mixing in sterilization pool, and use agitator rapid stirring, realize the elimination to bacterium in sewage, some groups of iron-carbon galvanic cells are installed in sterilization pool simultaneously, ferrous ion and carbon granules can be produced, while realization sterilization, also by throwing out, remove the suspended contamination in sewage, the organic compound simultaneously in sewage, between galvanic cell, there is electrochemical oxidation decomposition reaction, change the organism of more easily degrading into;
(4) sewage after flocculation, sterilization flows in settling tank automatically, and after 45min leaves standstill, supernatant liquid directly arranges sea after reaching emission standard; Lower floor's mud enters in plate-and-frame filter press, and the dewatered sludge obtained transports land process back, after pressing filtering liquid is qualified after testing, directly arranges sea, if defective, in pressing filtering liquid recycle pump suction sterilization pool, continues process, until again arrange sea after qualified.
The effect of employing present method is: the method is applied in certain offshore production platform, it is (70-125) mg/L that COD arranges extra large numerical value, meet the limit value of COD≤300mg/L in " offshore oil exploration and exploitation Pollutant emission concentration limit value " (GB4914-2008) completely, suspended substance is arranged extra large concentration and is less than 35mg/L, respond well.

Claims (1)

CN201410407386.8A2014-08-182014-08-18A kind of offshore platform domestic sewage processing methodActiveCN104176861B (en)

Priority Applications (1)

Application NumberPriority DateFiling DateTitle
CN201410407386.8ACN104176861B (en)2014-08-182014-08-18A kind of offshore platform domestic sewage processing method

Applications Claiming Priority (1)

Application NumberPriority DateFiling DateTitle
CN201410407386.8ACN104176861B (en)2014-08-182014-08-18A kind of offshore platform domestic sewage processing method

Publications (2)

Publication NumberPublication Date
CN104176861A CN104176861A (en)2014-12-03
CN104176861Btrue CN104176861B (en)2016-03-30

Family

ID=51958251

Family Applications (1)

Application NumberTitlePriority DateFiling Date
CN201410407386.8AActiveCN104176861B (en)2014-08-182014-08-18A kind of offshore platform domestic sewage processing method

Country Status (1)

CountryLink
CN (1)CN104176861B (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication numberPriority datePublication dateAssigneeTitle
BE1029516B1 (en)*2021-06-212023-01-23Noah Water Solutions bvba METHOD FOR TREATMENT OF BLACK WATER

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication numberPriority datePublication dateAssigneeTitle
CN108083520A (en)*2017-12-292018-05-29苏州东大仁智能科技有限公司A kind of marine domestic sewage processing method
CN108911284A (en)*2018-05-312018-11-30中海油能源发展股份有限公司A kind of offshore platform sanitary sewage disposal electrolytic method
US11453603B2 (en)*2019-06-282022-09-27Crystal Lagoons Technologies, Inc.Low cost and sanitary efficient method that creates two different treatment zones in large water bodies to facilitate direct contact recreational activities

Citations (5)

* Cited by examiner, † Cited by third party
Publication numberPriority datePublication dateAssigneeTitle
CN102120661A (en)*2010-12-062011-07-13青岛双瑞海洋环境工程有限公司Equipment and method for treating ship domestic sewage through electrolytic process
CN102167472A (en)*2011-03-072011-08-31天津亿利科能源科技发展股份有限公司Combined type MBR (membrane bioreactor) sewage treating and recycling device for offshore platform
CN202193681U (en)*2011-08-102012-04-18上海赛一水处理科技有限公司 Integrated automatic drinking water disinfection device
CN102515398A (en)*2011-11-302012-06-27青岛双瑞海洋环境工程股份有限公司Method for treating domestic sewage of compound ship
CN103755105A (en)*2014-01-292014-04-30中国海洋石油总公司Treatment system and treatment method for marine domestic sewage

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication numberPriority datePublication dateAssigneeTitle
JP2011056345A (en)*2009-09-072011-03-24Toshiba CorpDesalination system
JP2013027840A (en)*2011-07-292013-02-07Kyowa Kako KkSystem for clarifying seawater

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication numberPriority datePublication dateAssigneeTitle
CN102120661A (en)*2010-12-062011-07-13青岛双瑞海洋环境工程有限公司Equipment and method for treating ship domestic sewage through electrolytic process
CN102167472A (en)*2011-03-072011-08-31天津亿利科能源科技发展股份有限公司Combined type MBR (membrane bioreactor) sewage treating and recycling device for offshore platform
CN202193681U (en)*2011-08-102012-04-18上海赛一水处理科技有限公司 Integrated automatic drinking water disinfection device
CN102515398A (en)*2011-11-302012-06-27青岛双瑞海洋环境工程股份有限公司Method for treating domestic sewage of compound ship
CN103755105A (en)*2014-01-292014-04-30中国海洋石油总公司Treatment system and treatment method for marine domestic sewage

Cited By (1)

* Cited by examiner, † Cited by third party
Publication numberPriority datePublication dateAssigneeTitle
BE1029516B1 (en)*2021-06-212023-01-23Noah Water Solutions bvba METHOD FOR TREATMENT OF BLACK WATER

Also Published As

Publication numberPublication date
CN104176861A (en)2014-12-03

Similar Documents

PublicationPublication DateTitle
CN101928097B (en)Ecological community domestic sewage treatment system
CN101723548B (en)System for recycling and treating coking wastewater
WO2020238021A1 (en)Intensive modular combined aquaculture tail water treatment system
CN110240353B (en) A marine aquaculture tailwater treatment system
CN104176861B (en)A kind of offshore platform domestic sewage processing method
CN102351382B (en)Combined treatment method of leachate and excrement wastewater
CN104496008B (en)The Apparatus and method for of a kind of electrochemistry-biological coupling process organic waste water
CN105236685A (en)Zero-discharge treatment method for offshore-platform domestic sewage
CN106830450A (en)Surface water algae is in situ with the microkinetic of nutritive salt to collect separation integrated apparatus
CN109516641A (en)Method for treating high-salt high-concentration organic wastewater by electrocatalytic oxidation-biochemical coupling
CN102276111A (en)Optimally combined treating method for micro-polluted water sources
CN108773878A (en)A kind of landfill leachate bio-chemical effluent treatment reactor and method
CN105523624A (en)Method and system for processing domestic wastewater of offshore oil drilling platforms
CN109368746A (en)A kind of high COD, difficult biochemical waste water pretreatment unit pretreatment system and method
CN104310663B (en)Combined system for hydroxyl radical (.OH) strong oxidation treatment of high algae-laden water
CN201864641U (en)Housing estate domestic sewage ecological treatment system
CN203530076U (en)Sewage treatment system
CN101195501A (en)Fecal sewage decolorizing method and device
CN101665308B (en) A method for advanced treatment of landfill leachate
CN107337327A (en)A kind of integrated sewage treatment device
CN109970158B (en)Electrochemistry sewage treatment system
CN203360193U (en)Sewage treatment integration system
CN105540847B (en)A kind of continuous stream three sections of bio electric desalting apparatus and its application processes for the refinery produced-water treatment containing acetonitrile
CN210656513U (en)Domestic sewage treatment equipment
CN207175730U (en)A kind of integrated sewage treatment device

Legal Events

DateCodeTitleDescription
C06Publication
PB01Publication
C10Entry into substantive examination
SE01Entry into force of request for substantive examination
C14Grant of patent or utility model
GR01Patent grant
C41Transfer of patent application or patent right or utility model
TR01Transfer of patent right

Effective date of registration:20170301

Address after:100027 Beijing city Dongcheng District Dongzhimen Street No. 6

Patentee after:CNOOC Energy Development Co., Ltd.

Patentee after:Company limited of Hai Youzong energy-saving and emission-reduction monitoring center

Address before:100010 Dongcheng District, Chaoyangmen, North Street, No. 25, CNOOC building, mailbox,, 4705

Patentee before:China National Offshore Oil Corporation

Patentee before:CNOOC Energy Development Co., Ltd.

Patentee before:Company limited of Hai Youzong energy-saving and emission-reduction monitoring center


[8]ページ先頭

©2009-2025 Movatter.jp