CN2442731Y - Combined sedimentation separator for oil containing waste water - Google Patents
Combined sedimentation separator for oil containing waste water Download PDFInfo
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- CN2442731Y CN2442731Y CN 00247977 CN00247977U CN2442731Y CN 2442731 Y CN2442731 Y CN 2442731Y CN 00247977 CN00247977 CN 00247977 CN 00247977 U CN00247977 U CN 00247977U CN 2442731 Y CN2442731 Y CN 2442731Y
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Abstract
The utility model relates to a combined type sedimentation separator for oil containing waste water. In the utility model, a left seal head 1, a right seal head 2 and a barrel body 3 form a horizontal pressure container, the inner part of the horizontal pressure container is divided into a left buffer space 14, a right buffer space 17, a downwards flowing space 15 and an upwards flowing space 16 by baffle plates 5, 12, 6 and contiguous spaces are communicated at the upper part or the lower part of the baffle plates. The downwards flowing space 15 and the upwards flowing space 16 are respectively provided with a downwards flowing inclined plate component 8 and an upwards flowing inclined plate component 11, and two contiguous inclined plates are crossed according to contrary angles. An oil discharging package 23 and a mud discharging package 21 are respectively arranged below and above the barrel body. The utility model overcomes the defects of unchanged cross section load, cross flow and short circuit and enhances the water quality.
Description
The utility model is the treatment facility of oil-polluted water.
Though the effluent quality of existing cross-current coalescence degreaser has reached predetermined index, but also there are some shortcomings, the one, its gravity type rectangular bar of steel structure can't be made tun, and maximum gauge can only be accomplished 4m after making the pressure type cylinder tank into, because the load of cross-current coalescence degreaser is by the sectional area decision of cylinder, and area of section is immutable, so will change surface loading, in parallel jar number can only be increased, equipment investment must be increased like this.As the length that prolongs jar, can only increase the time of staying of sewage in jar, load still can fall; The 2nd, the top of cross-current coalescence degreaser filler must be provided with oil-collecting oil extraction space, the bottom must be provided with collection mud spoil disposal space, and the filler in the device is big to the resistance of current, makes oil-collecting, collection mud space that channelling and short circuit very easily take place, cause the effluent quality instability, effluent quality is poor.
The purpose of this utility model is a kind of oil-polluted water combined type settlement separator of design, and it can solve the cross section immutable problem of loading, and can reduce load effectively, reduces the time of staying of sewage in jar; It can eliminate oil-collecting, channelling and short circuit problem take place in collection mud space, makes stable effluent quality, water quality meet standard.
The utility model comprises left end socket 1, right end socket 2, cylindrical shell 3, median septum 12, left clapboard 5, right clapboard 6, down to stream type sloping plate component 8, upward flow type sloping plate component 11, cylindrical shell 3 left and right end portions become complete horizontal cylinder pressure vessel by left end socket 1 and 2 sealings of right end socket, left clapboard 5, median septum 12, right clapboard 6 is divided into left cushion space 14 with internal tank, down to fluid space 15, upward flow space 16 right cushion spaces 17, left side cushion space 14 communicates to the top of fluid space 15 at left clapboard 5 with following, communicate with the bottom of upward flow space 16 to fluid space 15 down at median septum 12, upward flow space 16 communicates on the top of right clapboard 6 with right cushion space 17, is being separately installed with down to stream type sloping plate component 8 and upward flow type sloping plate component 11 to the middle part of fluid space 15 with upward flow space 16 down.The water of this mechanism is entered from left cushion space 14 by water inlet pipe 18, flow to from left clapboard 5 tops down again to fluid space 15, flow through down to stream type sloping plate component 8, adopt big following in gap to be beneficial to oil slick come-up and silt particle sedimentation here, avoid producing and stop up to stream type sloping plate component 8; Water flows to upward flow space 16 from the bottom of median septum 12, the upward flow type sloping plate component 11 of flowing through, adopt the little upward flow type sloping plate component 11 in gap here, it can make tiny silt particle do not taken away by water, also can further remove oil slick, water flows to right cushion space 17 from the top of right clapboard 6 again, is flowed out by outlet pipe 19 at last.
The utility model has overcome the cross section immutable shortcoming of loading, and has effectively reduced load, has reduced the time of staying of sewage in separator; It has eliminated oil-collecting, channelling and short circuit phenomenon take place in collection mud space, makes stable effluent quality, and water quality meets standard.It is suitable for the processing of low concentration ternary sewage.
Fig. 1 is an external structure schematic diagram of the present utility model, Fig. 2 is an internal structure schematic diagram of the present utility model, Fig. 3 is type sloping plate component 8 and type sloping plate component 11 first swash plate scheme of installation from left number, Fig. 4 be type sloping plate component 8 and type sloping plate component 11 from a left side several second swash plate scheme of installation, Fig. 5 is the A-A cutaway view of Fig. 2.
Embodiment: present embodiment is by left end socket 1, right end socket 2, cylindrical shell 3, saddle 4, median septum 12 left clapboards 5, right clapboard 6, last water distribution expanded metal lath 7, down to stream type sloping plate component 8, left side supporting steel plate screen component 9, right supporting steel plate screen component 10, upward flow type sloping plate component 11, expanded metal lath 13, water inlet pipe 18, outlet pipe 19, blow-down pipe 20, spoil disposal bag 21, blast pipe 22, oil extraction bag 23 is formed, cylindrical shell 3 left and right end portions become complete horizontal cylinder pressure vessel by left end socket 1 and 2 sealings of right end socket, left clapboard 5, median septum 12, right clapboard 6 is divided into left cushion space 14 with internal tank, down to fluid space 15, upward flow space 16, right cushion space 17, left side cushion space 14 communicates to the top of fluid space 15 at left clapboard 5 with following, communicate with the bottom of upward flow space 16 at median septum 12 to fluid space 15 down, upward flow space 16 communicates on the top of right clapboard 6 with right cushion space 17.Being equipped with down to stream type sloping plate component 8 down to the middle part of fluid space 15, above stream type sloping plate component 8, be provided with water distribution expanded metal lath 7 down, down to flow type sloping plate component 8 below be provided with left supporting steel plate screen component 9; At the middle part in upward flow space 16 upward flow type sloping plate component 11 is installed, be provided with expanded metal lath 13 above the upward flow type sloping plate component 11, be provided with right supporting steel plate screen component 10 below the upward flow type sloping plate component 11, upward flow type sloping plate component 8 is pressed opposite angle skewed crossing with following first swash plate and second swash plate to stream type sloping plate component 11, the 3rd swash plate and later swash plate intersect successively, and it is made up of a series of oblique triangle 26 staggered type sloping plate components that constitute.Be equipped with water inlet pipe 18 and outlet pipe 19 on left end socket 1, left clapboard 5 is passed in the bottom of outlet pipe 19 in cylindrical shell 3, right clapboard 6 extends to the right cushion space 17; Water inlet pipe 18 extends in the left cushion space 14.Bottom in cylindrical shell 3 outsides is connected with saddle 4, below cylindrical shell 3, be connected with cylindrical shell 3 in the blow-down pipe 20 and the spoil disposal bag 21 that communicate, the top of cylindrical shell 3 be connected with cylindrical shell 3 in the blast pipe 22 and the oil extraction bag 23 that communicate, on right end socket 2, be provided with hand-hole 24.
This structure type sloping plate component can make current be the broken line speed change to flow and to cause the intersection current, be beneficial to oil droplet, tiny silt particle collision and the coalescence on microcosmic, improve treatment effect; Whole swash plate district can be full of filler fully and avoid with the angle trigonum at invalid dead angle up and down during fabric swatch in the same way; Down, there are not channelling and short circulation road from top to bottom to fluid space 15 and upward flow space 16 water distribution or from bottom to top; Because the water distribution uniformity of expanded metal lath and the resistance of swash plate inside have guaranteed that water distribution is even up and down; When design,, can change the surface loading of equipment, be equivalent to change the treating capacity or the effluent quality of equipment along the length of cylindrical shell axially-extending type sloping plate component; Water inlet pipe 18 inserts in the left cushion space 14, has played the current stabilization effect, and avoiding into, water flings down to the stream type sloping plate component; Inlet tube and outlet tube is connected on a side can set up a pump house nearby, is convenient to the north of china in winter pipe insulation; Right cushion space can further be removed the oil that current are taken out of, guarantees that outlet pipe is not oily toward tyre, has improved the quality of water outlet.
Claims (6)
1, oil-polluted water combined type settlement separator, it comprises left end socket (1), right end socket (2), cylindrical shell (3), median septum (12), left clapboard (5), right clapboard (6), down to stream type sloping plate component (8), upward flow type sloping plate component (11), cylindrical shell (3) left and right end portions is by left end socket (1) and the complete horizontal cylinder pressure vessel of right end socket (2) sealing becoming, it is characterized in that left clapboard (5), median septum (12), right clapboard (6) is divided into left cushion space (14) with internal tank, down to fluid space (15), upward flow space (16), right cushion space (17), left side cushion space (14) communicates to the top of fluid space (15) at left clapboard (5) with following, communicate with upward flow space (16) bottom to fluid space (15) down at median septum (12), upward flow space (16) communicates with the top of right cushion space (17) at right clapboard (6), is being separately installed with down to stream type sloping plate component (8) and upward flow type sloping plate component (11) to the middle part of fluid space (15) with upward flow space (16) down.
2, according to claim 1,2 described oil-polluted water combined type settlement separators, it is characterized in that above stream type sloping plate component (8), being provided with water distribution expanded metal lath (7) down, below stream type sloping plate component (8), be provided with left supporting steel plate screen component (9) down.
3, according to claim 1,2 described oil-polluted water combined type settlement separators, it is characterized in that upward flow type sloping plate component (11) above be provided with expanded metal lath (13), be provided with right supporting steel plate screen component (10) below the upward flow type sloping plate component (11).
4, according to claim 1,2 described oil-polluted water combined type settlement separators, it is characterized in that upward flow type sloping plate component (8) and press first swash plate from opposite angle skewed crossing to stream type sloping plate component (11) and second swash plate down, the 3rd swash plate and later swash plate intersect successively, and it is made up of the staggered type sloping plate component that constitutes of a series of oblique triangles (26).
5, according to claim 1,2 described oil-polluted water combined type settlement separators, it is characterized in that the bottom of cylindrical shell (3) be connected with cylindrical shell (3) in the spoil disposal bag (21) that communicates, the top of cylindrical shell (3) be connected with cylindrical shell (3) in the oil extraction bag (23) that communicates.
6, according to claim 1,2 described oil-polluted water combined type settlement separators, it is characterized in that on left end socket (1), being equipped with water inlet pipe (18) and outlet pipe (19), outlet pipe (19) passes left clapboard (5) from the bottom in the cylindrical shell (3), right clapboard (6) extends to the right cushion space (17), and water inlet pipe (18) extends in the left cushion space (14).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 00247977 CN2442731Y (en) | 2000-08-31 | 2000-08-31 | Combined sedimentation separator for oil containing waste water |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 00247977 CN2442731Y (en) | 2000-08-31 | 2000-08-31 | Combined sedimentation separator for oil containing waste water |
Publications (1)
Publication Number | Publication Date |
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CN2442731Y true CN2442731Y (en) | 2001-08-15 |
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN 00247977 Expired - Fee Related CN2442731Y (en) | 2000-08-31 | 2000-08-31 | Combined sedimentation separator for oil containing waste water |
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN100443581C (en) * | 2001-08-31 | 2008-12-17 | 拜耳医药保健股份公司 | A unit and a process for carrying out high cell density fermentation |
CN104787844A (en) * | 2014-01-16 | 2015-07-22 | 中国石化工程建设有限公司 | Oil-containing wastewater treatment apparatus and oil-containing wastewater treatment method |
-
2000
- 2000-08-31 CN CN 00247977 patent/CN2442731Y/en not_active Expired - Fee Related
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN100443581C (en) * | 2001-08-31 | 2008-12-17 | 拜耳医药保健股份公司 | A unit and a process for carrying out high cell density fermentation |
CN104787844A (en) * | 2014-01-16 | 2015-07-22 | 中国石化工程建设有限公司 | Oil-containing wastewater treatment apparatus and oil-containing wastewater treatment method |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C17 | Cessation of patent right | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20010815 |