CN105254000A - Multitube gas stripping inner loop three-phase biological fluidized bed - Google Patents

Multitube gas stripping inner loop three-phase biological fluidized bed Download PDF

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Publication number
CN105254000A
CN105254000A CN201510808828.4A CN201510808828A CN105254000A CN 105254000 A CN105254000 A CN 105254000A CN 201510808828 A CN201510808828 A CN 201510808828A CN 105254000 A CN105254000 A CN 105254000A
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CN
China
Prior art keywords
fluidized bed
biological fluidized
pond body
tank body
phase biological
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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.)
Pending
Application number
CN201510808828.4A
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Chinese (zh)
Inventor
胡云开
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Wuxi Shanchuan Environmental Protection Machinery Co Ltd
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Wuxi Shanchuan Environmental Protection Machinery 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.)
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Publication date
Application filed by Wuxi Shanchuan Environmental Protection Machinery Co Ltd filed Critical Wuxi Shanchuan Environmental Protection Machinery Co Ltd
Priority to CN201510808828.4A priority Critical patent/CN105254000A/en
Publication of CN105254000A publication Critical patent/CN105254000A/en
Pending legal-status Critical Current

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    • 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

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  • Aeration Devices For Treatment Of Activated Polluted Sludge (AREA)

Abstract

The invention relates to an inner loop three-phase biological fluidized bed, in particular relates to a multitube gas stripping inner loop three-phase biological fluidized bed and belongs to the technical field of biological fluidized beds. The multitube gas stripping inner loop three-phase biological fluidized bed comprises a tank body, one gas distributing packet is arranged at each of the left side and the right side in the tank body, and the gas distributing packets at the left side and the right side in the tank body are connected into a whole by virtue of a plurality of aeration hoses; a main gas tube is arranged at each of the left side and the right side of the tank body, the gas outlet end of each main gas tube is connected with the gas distributing packet arranged at the bottom of the tank body by virtue of one branch gas tube; and one support is arranged at each of the front end and the rear end of the tank body, the inner side of each support is connected with a cross beam, the cross beams at the front end and the rear end of the tank body are connected into a whole by virtue of an eyeglass-like circle, the aeration hoses penetrate through the eyeglass-like circle, and the aeration hoses are supported and connected by virtue of the eyeglass-like circle. The multitube gas stripping inner loop three-phase biological fluidized bed is simple, compact and reasonable in structure, aeration efficiency is improved, operating cost is reduced, and equipment cost is saved.

Description

Multi-pipe aerobic internal circulation three-phase biological fluidized bed
Technical field
The present invention relates to a kind of inner loop three phase fluidized bed reactor, specifically a kind of Multi-pipe aerobic internal circulation three-phase biological fluidized bed, belong to biological fluidized bed technical field.
Background technology
Biological fluidized bed refers to the processing efficiency into improving biomembrance process, filler is made and as biofilm carrier using sand (or hard coal, gac etc.), the bottom-up casting bed that flows through of waste water makes carrier layer be flow state, thus strengthen microbial film with the contact area of waste water and abundant oxygen supply in the unit time, and filler boiling state is utilized to strengthen the structures of biological wastewater treatment process.Biological fluidized bed process efficiency is high, take up an area less, reduced investment, beautiful, Deng state is nitrated for sewage, the process of denitrogenation even depth and sewage second-level process and other are containing the Industrial Wastewater Treatment such as phenol, pharmacy.
Inner loop three phase fluidized bed reactor is that of in recent years growing up on the basis of traditional biological fluidized-bed innovates technologies, and application is gradually extensive at present, and existing many cover production equipments are in operation at home.Inner loop three phase fluidized bed reactor by distinguishing up-flow district and Jiang Liu district in bed, utilize the density difference between two regions, circulating of propelling fluid band mobile carrier, finally carrying out being separated of carrier and water outlet in settling region, top, is a kind of biological fluidized bed of improvement.Its advantage is that mixing mass transfer condition is good, not easily carrier demixing phenomenon occurs; Relatively low to the requirement of fluid distributor, be easy to accomplish that fluid well-distributing distributes; In addition, also there is the features such as relatively simple, the shock-resistant ability of structure is strong, sludge output is few.Although biological fluidized bed has above-mentioned plurality of advantages, its popularity is far away from activated sludge process, biological contact oxidation process and biological filter.Major cause is due to fluidization itself, make the design of biological fluidized-bed reactor and the requirement of running management to technology higher.Until today, people are still comparatively superficial to the understanding of fluidisation phenomenon inherent laws, and the design of a large amount of engineering mainly relies on micro-judgment.In investment and working cost, the investment of biological fluidized bed and floor space are only equivalent to 70% and 50% of traditional active sludge aeration tank respectively, but working cost is relatively high, mainly because of the power consumption of fluidisation.
Summary of the invention
The object of the invention is to overcome above-mentioned weak point, thus a kind of Multi-pipe aerobic internal circulation three-phase biological fluidized bed is provided, improve aeration efficiency, reduce working cost, save equipment cost.
According to technical scheme provided by the invention, Multi-pipe aerobic internal circulation three-phase biological fluidized bed comprises pond body, it is characterized in that: the Ti Nei left and right sides, pond is respectively equipped with a point of gas bag, and a point gas bag for the left and right sides is linked into an integrated entity by several aeration flexible pipes; The body left and right sides, pond is respectively equipped with a main tracheae, and the outlet side of each main tracheae connects point gas bag be positioned at bottom the body of pond by a segmental bronchus; Body front and back end, pond is respectively equipped with a support, connecting cross beam inside each support, is linked into an integrated entity between the crossbeam of body front and back end, pond by glasses circle, and aeration flexible pipe, through glasses circle, forms support and connection by glasses circle to aeration flexible pipe; Aeration flexible pipe upper end arranges fluidized-bed gas hood, and fluidized-bed gas hood upper end connects multiple corrugated tube.
Further, segmental bronchus is provided with valve.
Further, fixed angles brandreth in the middle part of the body of pond, corrugated tube is fixed on angle-iron frame by anchor ear.
Compared with the prior art the present invention has the following advantages:
Structure of the present invention is simple, compact, reasonable, improves aeration efficiency, reduces working cost, save equipment cost.
Accompanying drawing explanation
Fig. 1 is front view of the present invention.
Fig. 2 is vertical view of the present invention.
Fig. 3 is A-A sectional view in Fig. 2.
The main tracheae of description of reference numerals: 1-, 2-valve, 3-segmental bronchus, 4-divide gas bag, 5-corrugated tube, 6-fluidized-bed gas hood, 7-pond body, 8-aeration flexible pipe, 9-support, 10-crossbeam, 11-glasses circle, 12-angle-iron frame, 13-anchor ear.
Embodiment
Embodiment in is by reference to the accompanying drawings further described by the present invention below:
As shown in Fig. 1 ~ 3, the present invention mainly comprises pond body 7, and in pond body 7, the left and right sides is respectively equipped with a point of gas bag 4, and a point gas bag 4 for the left and right sides is linked into an integrated entity by several aeration flexible pipes 8.
Pond body 7 left and right sides is respectively equipped with a main tracheae 1, and the outlet side of each main tracheae 1 connects point gas bag 4 be positioned at bottom pond body 7 by a segmental bronchus 3.
Described segmental bronchus 3 is provided with valve 2, is controlled the opening and closing of segmental bronchus 3 by valve 2.
Pond body 7 front and back end is respectively equipped with a support 9, connecting cross beam 10 inside each support 9, is linked into an integrated entity between the crossbeam 10 of pond body 7 front and back end by glasses circle 11.Aeration flexible pipe 8, through glasses circle 11, forms support and connection by glasses circle 11 pairs of aeration flexible pipes 8.
Aeration flexible pipe 8 upper end arranges fluidized-bed gas hood 6, and fluidized-bed gas hood 6 upper end connects multiple corrugated tube 5.Aeration flexible pipe 8 carries the collection and confinement of gases come up to enter corrugated tube 5 by fluidized-bed gas hood 6.
Fixed angles brandreth 12 in the middle part of pond body 7, corrugated tube 5 is fixed on angle-iron frame 12 by anchor ear 13.
Principle of work of the present invention is: during work, and during main tracheae, blower fan is the principal passage to fluidized-bed air feed, and the gas carried by main tracheae by segmental bronchus sends into point gas bag bottom the body of pond respectively, segmental bronchus arranges valve to regulate and control each bronchial displacement.Two relative point of gas bags are connected by aeration flexible pipe, and aeration flexible pipe passes from glasses circle, thus plays the effect of immobilized film flexible pipe.Aeration flexible pipe carries the collection and confinement of gases come up to enter corrugated tube by fluidized-bed gas hood.

Claims (3)

1. a Multi-pipe aerobic internal circulation three-phase biological fluidized bed, comprises pond body (7), it is characterized in that: pond body (7) the interior left and right sides is respectively equipped with a point of gas bag (4), and a point gas bag (4) for the left and right sides is linked into an integrated entity by several aeration flexible pipes (8); Pond body (7) left and right sides is respectively equipped with a main tracheae (1), and the outlet side of each main tracheae (1) is by being positioned at point gas bag (4) of pond body (7) bottom the connection of a segmental bronchus (3); Pond body (7) front and back end is respectively equipped with a support (9), each support (9) inner side connecting cross beam (10), linked into an integrated entity by glasses circle (11) between the crossbeam (10) of pond body (7) front and back end, aeration flexible pipe (8), through glasses circle (11), forms support and connection by glasses circle (11) to aeration flexible pipe (8); Aeration flexible pipe (8) upper end arranges fluidized-bed gas hood (6), and fluidized-bed gas hood (6) upper end connects multiple corrugated tube (5).
2. Multi-pipe aerobic internal circulation three-phase biological fluidized bed as claimed in claim 1, is characterized in that: described segmental bronchus (3) is provided with valve (2).
3. Multi-pipe aerobic internal circulation three-phase biological fluidized bed as claimed in claim 1, is characterized in that: middle part fixed angles brandreth, described pond body (7) (12), corrugated tube (5) is fixed on angle-iron frame (12) by anchor ear (13).
CN201510808828.4A 2015-11-20 2015-11-20 Multitube gas stripping inner loop three-phase biological fluidized bed Pending CN105254000A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201510808828.4A CN105254000A (en) 2015-11-20 2015-11-20 Multitube gas stripping inner loop three-phase biological fluidized bed

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201510808828.4A CN105254000A (en) 2015-11-20 2015-11-20 Multitube gas stripping inner loop three-phase biological fluidized bed

Publications (1)

Publication Number Publication Date
CN105254000A true CN105254000A (en) 2016-01-20

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CN201510808828.4A Pending CN105254000A (en) 2015-11-20 2015-11-20 Multitube gas stripping inner loop three-phase biological fluidized bed

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CN (1) CN105254000A (en)

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN2500675Y (en) * 2001-09-28 2002-07-17 胡建东 Multi-pipe aerobic internal circulation three-phase biological fluidized bed
CN204281405U (en) * 2014-11-24 2015-04-22 胡云开 Membrane bioreactor is to upper reaches No clean system
CN104961303A (en) * 2015-07-10 2015-10-07 青岛小川环保设备有限公司 Pump-free integrated wastewater deep treatment equipment
CN205151885U (en) * 2015-11-20 2016-04-13 无锡山川环保机械有限公司 Multi -pipe aerobic internal circulation three -phase biological fluidized bed

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN2500675Y (en) * 2001-09-28 2002-07-17 胡建东 Multi-pipe aerobic internal circulation three-phase biological fluidized bed
CN204281405U (en) * 2014-11-24 2015-04-22 胡云开 Membrane bioreactor is to upper reaches No clean system
CN104961303A (en) * 2015-07-10 2015-10-07 青岛小川环保设备有限公司 Pump-free integrated wastewater deep treatment equipment
CN205151885U (en) * 2015-11-20 2016-04-13 无锡山川环保机械有限公司 Multi -pipe aerobic internal circulation three -phase biological fluidized bed

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Application publication date: 20160120

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