[go: up one dir, main page]

CN203033861U - Vessel sewage integrated device - Google Patents

Vessel sewage integrated device Download PDF

Info

Publication number
CN203033861U
CN203033861U CN201320002472.1U CN201320002472U CN203033861U CN 203033861 U CN203033861 U CN 203033861U CN 201320002472 U CN201320002472 U CN 201320002472U CN 203033861 U CN203033861 U CN 203033861U
Authority
CN
China
Prior art keywords
tank
integrated device
membrane treatment
mbr membrane
sewage
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.)
Expired - Fee Related
Application number
CN201320002472.1U
Other languages
Chinese (zh)
Inventor
卢启友
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.)
YUEQING TENG XIANG MO TECHNOLOGY Co Ltd
Original Assignee
YUEQING TENG XIANG MO TECHNOLOGY Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by YUEQING TENG XIANG MO TECHNOLOGY Co Ltd filed Critical YUEQING TENG XIANG MO TECHNOLOGY Co Ltd
Priority to CN201320002472.1U priority Critical patent/CN203033861U/en
Application granted granted Critical
Publication of CN203033861U publication Critical patent/CN203033861U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Classifications

    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

Landscapes

  • Activated Sludge Processes (AREA)

Abstract

本实用新型涉及一种船舶污水一体式装置。一种船舶污水一体式装置,包括固液分离器、调节池、接触氧化池、MBR膜处理池、蓄水池和若干连接管道,固液分离器位于调节池中,调节池、接触氧化池、MBR膜处理池和蓄水池依次由连接管道相连接,还包括鼓风机,鼓风机通过第一通气管道与调节池相连接,所述第一通气管道旁通第二通气管道和第三通气管道,所述第二通气管道和第三通气管道分别与接触氧化池和MBR膜处理池相连接;所述MBR膜处理池通过回流管道连接调节池。该装置处理的污水处理的污水能够达到排放标准。

The utility model relates to a ship sewage integrated device. An integrated device for ship sewage, including a solid-liquid separator, a regulating tank, a contact oxidation tank, an MBR membrane treatment tank, a reservoir and several connecting pipes, the solid-liquid separator is located in the regulating tank, the regulating tank, the contact oxidation tank, The MBR membrane treatment tank and the storage tank are connected by connecting pipes in turn, and a blower is also included. The blower is connected with the regulating tank through the first ventilation pipe, and the first ventilation pipe bypasses the second ventilation pipe and the third ventilation pipe, so The second ventilation pipeline and the third ventilation pipeline are respectively connected with the contact oxidation tank and the MBR membrane treatment tank; the MBR membrane treatment tank is connected with the adjustment tank through the return pipeline. The sewage treated by the device can meet the discharge standard.

Description

一种船舶污水一体式装置A ship sewage integrated device

技术领域 technical field

本实用新型涉及污水处理领域,具体涉及一种船舶污水一体式装置。  The utility model relates to the field of sewage treatment, in particular to an integrated device for ship sewage. the

背景技术 Background technique

目前船舶上的污水处理装置,由于在调节池、氧化池和膜处理装置里反应过滤时不充分,致使处理的污水无法达到排放标准。  At present, the sewage treatment devices on the ship are not sufficient in the reaction and filtration in the regulating tank, oxidation tank and membrane treatment device, so that the treated sewage cannot meet the discharge standard. the

发明内容 Contents of the invention

根据现有技术的不足,本实用新型提供一种船舶污水一体式装置。该装置处理的污水能够达到排放标准。 According to the deficiencies of the prior art, the utility model provides an integrated device for ship sewage. The sewage treated by the device can meet the discharge standard.

根据现有技术的不足,本实用新型提供的技术方案为:一种船舶污水一体式装置,包括固液分离器、调节池、接触氧化池、MBR膜处理池、蓄水池和若干连接管道,固液分离器位于调节池中,调节池、接触氧化池、MBR膜处理池和蓄水池依次由连接管道相连接,还包括鼓风机,鼓风机通过第一通气管道与调节池相连接,所述第一通气管道旁通第二通气管道和第三通气管道,所述第二通气管道和第三通气管道分别与接触氧化池和MBR膜处理池相连接;所述MBR膜处理池通过回流管道连接调节池。 According to the deficiencies of the prior art, the technical solution provided by the utility model is: an integrated device for ship sewage, including a solid-liquid separator, a regulating tank, a contact oxidation tank, an MBR membrane treatment tank, a water storage tank and several connecting pipes, The solid-liquid separator is located in the adjustment tank, and the adjustment tank, the contact oxidation tank, the MBR membrane treatment tank and the storage tank are connected by connecting pipes in turn, and a blower is also included. The blower is connected to the adjustment tank through the first ventilation pipe. A ventilation pipeline bypasses the second ventilation pipeline and the third ventilation pipeline, and the second ventilation pipeline and the third ventilation pipeline are respectively connected with the contact oxidation tank and the MBR membrane treatment tank; the MBR membrane treatment tank is connected and regulated by a return pipeline pool.

所述调节池内设有液位计和提升泵。 A liquid level gauge and a lifting pump are arranged in the regulating pool.

所述蓄水池连接有外排泵。 The water storage tank is connected with an efflux pump.

本实用新型的有益效果是:首先采用固液分离,分离出固体物质,再经过调节池和接触氧化池的处理,污水实现均质,同时MBR膜处理池中的高浓度活性污泥定期回流到调节池中,鼓风机提供的空气对调节池、接触氧化池和MBR膜处理池进行搅拌,使污水中的有机悬浮物和大分子物质分解充分,实现污泥减量。 The beneficial effects of the utility model are as follows: firstly, solid-liquid separation is adopted to separate the solid matter, and then the sewage is homogenized through the treatment of the regulating tank and the contact oxidation tank, and at the same time, the high-concentration activated sludge in the MBR membrane treatment tank is periodically returned to the In the regulating tank, the air provided by the blower stirs the regulating tank, the contact oxidation tank and the MBR membrane treatment tank, so that the organic suspended solids and macromolecular substances in the sewage are fully decomposed, and the sludge volume is reduced.

附图说明 Description of drawings

附图1为本实用新型的实施例的装置流程图。 Accompanying drawing 1 is the device flowchart of the embodiment of the present utility model.

具体实施方式 Detailed ways

下面结合附图对本实用新型做进一步说明。 Below in conjunction with accompanying drawing, the utility model is further described.

如图1所示,一种船舶污水一体式装置,包括固液分离器1、调节池2、接触氧化池5、MBR膜处理池8、蓄水池12和若干连接管道,固液分离器1位于调节池2中,调节池2、接触氧化池5、MBR膜处理池8和蓄水池12依次由连接管道相连接,还包括鼓风机11,鼓风机11通过第一通气管道10与调节池2相连接,所述第一通气管道10旁通第二通气管道6和第三通气管道9,所述第二通气管道6和第三通气管道9分别与接触氧化池5和MBR膜处理池8相连接;所述MBR膜处理池8通过回流管道7连接调节池2。 As shown in Figure 1, a ship sewage integrated device includes a solid-liquid separator 1, a regulating tank 2, a contact oxidation tank 5, an MBR membrane treatment tank 8, a reservoir 12 and several connecting pipes, the solid-liquid separator 1 Located in the adjustment tank 2, the adjustment tank 2, the contact oxidation tank 5, the MBR membrane treatment tank 8 and the water storage tank 12 are connected successively by connecting pipes, and also includes a blower 11, which is connected to the adjustment tank 2 through the first ventilation pipe 10 connected, the first ventilation pipeline 10 bypasses the second ventilation pipeline 6 and the third ventilation pipeline 9, and the second ventilation pipeline 6 and the third ventilation pipeline 9 are connected with the contact oxidation tank 5 and the MBR membrane treatment tank 8 respectively ; The MBR membrane treatment tank 8 is connected to the regulating tank 2 through the return pipeline 7 .

所述调节池2内设有液位计3和提升泵4。 The regulating tank 2 is provided with a liquid level gauge 3 and a lifting pump 4 .

所述蓄水池12连接有外排泵13。 The water storage tank 12 is connected with an outflow pump 13 .

首先通过固液分离器对污水进行固液分离,分离出的固体物质通过人工处理,去掉废渣,同时污水进入到调节池中处理,污水实现均质,然后在调节池液位计的控制下,提升泵将调节池的污水送入到接触氧化池,在填料微生物的作用下,污水中的有机物质被微生物分解利用,出水进入到MBR膜处理池,在微滤膜的作用下实现泥水分离,同时MBR膜处理池中的高浓度活性污泥定期回流到调节池中,鼓风机提供的空气对调节池、接触氧化池和MBR膜处理池进行搅拌,使污水中的有机悬浮物和大分子物质分解充分,实现污泥减量。MBR出水经过紫外灭菌系统处理后排入蓄水池中,在外排泵的作用下将处理达标的污水排出船体。  First, the solid-liquid separation of the sewage is carried out through the solid-liquid separator. The separated solid matter is manually processed to remove the waste residue. At the same time, the sewage enters the regulating tank for treatment, and the sewage is homogeneous. The lift pump sends the sewage from the adjustment tank to the contact oxidation tank. Under the action of filler microorganisms, the organic matter in the sewage is decomposed and utilized by the microorganisms, and the effluent enters the MBR membrane treatment tank, where the mud and water are separated under the action of the microfiltration membrane. At the same time, the high-concentration activated sludge in the MBR membrane treatment tank is regularly returned to the regulating tank, and the air provided by the blower is used to stir the regulating tank, contact oxidation tank and MBR membrane treatment tank to decompose the organic suspended solids and macromolecular substances in the sewage. Fully realize sludge reduction. The MBR effluent is treated by the ultraviolet sterilizing system and then discharged into the reservoir. Under the action of the effluent pump, the sewage that meets the standard is discharged out of the hull. the

Claims (3)

1. vessel sewage integrated device, comprise solid-liquid separator, equalizing tank, contact-oxidation pool, MBR film treating pond, water reservoir and some connecting tubes, solid-liquid separator is arranged in equalizing tank, equalizing tank, contact-oxidation pool, MBR film treating pond is connected by connecting tube successively with water reservoir, it is characterized in that: also comprise gas blower, gas blower is connected with equalizing tank by first breather line, the described first breather line bypass, second breather line and the 3rd breather line, described second breather line is connected with MBR film treating pond with contact-oxidation pool respectively with the 3rd breather line; Described MBR film treating pond connects equalizing tank by reflux line.
2. a kind of vessel sewage integrated device according to claim 1 is characterized in that: be provided with liquidometer and lift pump in the described equalizing tank.
3. a kind of vessel sewage integrated device according to claim 1, it is characterized in that: described water reservoir is connected with efflux pump.
CN201320002472.1U 2013-01-05 2013-01-05 Vessel sewage integrated device Expired - Fee Related CN203033861U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201320002472.1U CN203033861U (en) 2013-01-05 2013-01-05 Vessel sewage integrated device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201320002472.1U CN203033861U (en) 2013-01-05 2013-01-05 Vessel sewage integrated device

Publications (1)

Publication Number Publication Date
CN203033861U true CN203033861U (en) 2013-07-03

Family

ID=48685998

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201320002472.1U Expired - Fee Related CN203033861U (en) 2013-01-05 2013-01-05 Vessel sewage integrated device

Country Status (1)

Country Link
CN (1) CN203033861U (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103304109A (en) * 2013-07-09 2013-09-18 天津中天海盛环保科技有限公司 Hospital wastewater treatment process equipment and hospital wastewater treatment method
CN105645689A (en) * 2016-01-31 2016-06-08 江苏韩通船舶重工有限公司 Treatment system for effluent discharged by ship

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103304109A (en) * 2013-07-09 2013-09-18 天津中天海盛环保科技有限公司 Hospital wastewater treatment process equipment and hospital wastewater treatment method
CN105645689A (en) * 2016-01-31 2016-06-08 江苏韩通船舶重工有限公司 Treatment system for effluent discharged by ship

Similar Documents

Publication Publication Date Title
CN104310554B (en) Micro-nano bubble flocculation-air floatation process
CN103523966A (en) A deep sewage treatment system and treatment method
CN104492265A (en) Ultrafiltration membrane device with on-line medicament backwashing and blowdown device
CN104193041B (en) A kind for the treatment of process of jade processing waste water
CN105541010B (en) A kind of sewage disposal system peculiar to vessel and its processing method
CN203033861U (en) Vessel sewage integrated device
CN203419823U (en) Combined oilfield produced water treatment device
CN203021379U (en) Surface water purifying device
CN106517495B (en) A continuous flow SBR sewage treatment device
CN105967441B (en) A kind of sewage disposal system and method
CN205133295U (en) But device of inorganic waste liquid in integrated treatment chemistry experiment room
CN203754540U (en) Industrial sewage treatment equipment
CN102616991B (en) Method and equipment for sewage treatment by means of biochemical pressurized dissolved air flotation
CN103723882A (en) Ship wastewater treatment method and device
JP6460935B2 (en) Anaerobic fermentation treatment method for waste water, microbial carrier for anaerobic fermentation treatment, and anaerobic fermentation treatment apparatus
CN102951775B (en) Integral sewage treatment method and device thereof
CN204310916U (en) Petrochemical wastewater advanced treatment system
CN104045206A (en) UV/O3+BAF combined advanced oxidation sewage treatment equipment
CN204550323U (en) A kind of percolate concentrates liquid processing device
CN203360193U (en) Sewage treatment integration system
CN103508629A (en) Wastewater treatment system for food industry
CN207792975U (en) A kind of processing system of quick biochemical treatment COD
WO2016174562A4 (en) Dissolved ozone floatation effluent treatment system
CN205328816U (en) Landfill leachate optimization processing system
CN205347130U (en) Handle high concentration organic waste water integrated device

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20130703

Termination date: 20150105

EXPY Termination of patent right or utility model