GB1563586A - Separating device to separate two liquids of different specific gravity - Google Patents

Separating device to separate two liquids of different specific gravity Download PDF

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Publication number
GB1563586A
GB1563586A GB7002/77A GB700277A GB1563586A GB 1563586 A GB1563586 A GB 1563586A GB 7002/77 A GB7002/77 A GB 7002/77A GB 700277 A GB700277 A GB 700277A GB 1563586 A GB1563586 A GB 1563586A
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United Kingdom
Prior art keywords
plates
liquid
plate
flow
tank
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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.)
Expired
Application number
GB7002/77A
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JONG L DE
Original Assignee
JONG L DE
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Publication date
Application filed by JONG L DE filed Critical JONG L DE
Publication of GB1563586A publication Critical patent/GB1563586A/en
Expired legal-status Critical Current

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Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D17/00Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion
    • B01D17/02Separation of non-miscible liquids
    • B01D17/0208Separation of non-miscible liquids by sedimentation
    • B01D17/0211Separation of non-miscible liquids by sedimentation with baffles
    • 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
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A20/00Water conservation; Efficient water supply; Efficient water use
    • Y02A20/20Controlling water pollution; Waste water treatment
    • Y02A20/204Keeping clear the surface of open water from oil spills

Abstract

The apparatus serves in particular for the purification of a liquid by separating off oil of lower specific gravity contained therein. The apparatus has a separation unit (22) having inclined plates (10) arranged one above the other. These plates (10) have the shape of an inverted V in cross-section. In addition, upstream of the separation unit are provided upstream separation apparatuses (5, 6, 8) in which both the coarse fraction of the lighter liquid and relatively heavy solid particles are separated off from the heavier liquid. <IMAGE>

Description

(54) A SEPARATING DEVICE TO SEPARATE TWO LIQUIDS OF DIFFERENT SPECIFIC GRAVITY (71) I, LEENDERT WILLEM COR NELIS DE JONG, a Dutch citizen, of Westkade 27, Hellevoitsluis, The Netherlands, do hereby declare the invention, for which I pray that a patent may be granted to us, and the method by which it is to be performed, to be particularly described in and by the following statement: The invention relates to a separating device for separating liquid constituents of different specific gravity of a flow of liquid, for example, to clean a liquid by separating from its oil lighter than the liquid to be cleaned. Separators of this type are known which comprise a vessel with a separator unit having flow ways for the liquid spaced one above another and formed by a set of spaced, inclined plates of inverted-Vsection, the liquid entering the flow ways at the extremities of the plates.
According to the present invention, a separator for separating liquid constituents of a flow of liquid of different specific gravities, comprises a tank with an inlet for the flow of liquid, an outlet for a separated heavier liquid constituent, means for withdrawing from the tank a separated lighter liquid constituent floating on the top of the liquid in the tank and a separating unit mounted in the tank between the inlet and the outlet and comprising a set of spaced plates of inverted-V-shaped cross section whose ridge lines lie in a common vertical plane and are upwardly inclined, each plate having a pointed upper end portion whose profile is convergent in plan, its edges intersecting at a point in the ridge line of the plate, and the pointed upper end portion of each plate (except the uppermost) projecting forwardly beyond the corresponding end portion of the plate next above it, the plates defining between them a set of upwardlyinclined flow ways of inverted-V-shaped cross section arranged one above another through which the flow of liquid from the inlet passes, the arrangement being such that the liquid flow from the inlet enters the flow ways between the lower ends of the plates and the separated constituents leave the flow ways between the pointed upper end portions of the plates so that the separated lighter constituent rises to float on the top of the liquid in the tank for withdrawal by the said means.
In such a separator, the separated lighter liquid constituent is guided towards the liquid surface by the forwardly-projecting pointed end portions of the plates, and the heavier liquid constituent leaving the flow ways may flow away downwards at both sides of the pointed ends of the plates through the triangular gaps formed between the convergent edges of the pointed end portions of the plates and the side walls of the tank. By this a better separation may be achieved.
The invention may be carried into practice in various ways, but one specific embodiment thereof, comprising a device for cleaning a liquid by separating from it oil lighter than the liquid to be cleaned, in this case water, will now be described by way of example only and with reference to the accompanying drawings, in which: Figure 1 is a longitudinal section of a separating device; and Figure 2 is a section on the line II-II in Figure 1.
The oil separating device illustrated comprises a tank 1 with an oil separator unit 2.
The tank is provided with an inlet 3 for the liquid to be cleaned and a discharge tube 4 for the cleaned liquid.
The liquid entering the tank 1 through the inlet 3 first flows under an inclined baffle 5 and then flows into a space between the baffle 5 and a second baffle 6 which is formed in such a way that its lower portion is substantially parallel to the baffle 5 and its upper portion diverges away to form a larger space 7, so that the velocity of the flow of the upwardly flowing liquid to be cleaned decreases as it passes through the space 7. As a result the heavier particles such as sand and the like suspended in the liquid flow will descend, and the free easyto-separate constituents such as light oil will tend to float upwardy in space. The resultant floating layer of light oil is withdrawn by means of a skimmer 8.
This skimmer 8 is adjusted in such a way that during removal of the oil the thickness of the oil layer remains constant. This can only be done when the viscosity of the oil is not too high. If it is, the oil skimmer 8 has to be turned manually.
After this first separation the now less soiled water flows slowly downwardly between the baffle 6 and a baffle 9 to the entrance of the separator unit proper 2, after which it will flow upwardly between the parallel inclined separator plates 10.
These plates 10, the upper of which is indicated at 11 and the lower of which is indicated at 12, are of inverted-V-shape in section as shown in Figure 2 with pointed upper ends. Thus the uppermost end portion 10A of the length of each plate is of convergent form, terminating in a point on the ridge line of the plate, and moreover the convergent end portion 10A of each plate 10, 12 projects forwardly beyond the tip of the corresponding end portion of the plate next above it, as is seen clearly in Figure 1.
At the entry into the separator unit 2 of the soiled liquid the smaller droplets of oil will collect as a mist under the slanting sides of each plate 10, the longitudinal edges of the plates 10 lying close to the opposite side walls of the tank 1 as shown in Figure 2.
At a certain stage an oil film will be formed by this continuous mist deposit.
The continuous growing oil film will become thicker and will go in a V-shaped movement towards the ridge line or crosssectional apex of each plate 10 as the result of the inverted-V-shape of the plates and the angle of about 15 degrees with the horizontal at which the ridge lines of the plates are inclined.
Towards the upper end of each inverted V-shaped plate 10. the oil films collecting under both sides of the plate 10 will be joined to form a stream. At the pointed ends of the convergent portions 10A of the V-shaped plates 10 the oil will leave the plates in the shape of big drops. These big drops will rise easily to the surface because of their size.
These drops then again form an oil layer at the surface which is removed bv a second skimmer 13.
The water leaving the separating unit 2 travels down under a driving baffle 14 and then up and out through an adjustable overflow 15, with a great degree of cleanness.
The number of plates 10 and the selected distance between the plates determine the capacity.
The plates may be pushed inwards by means of cams provided on the side walls of the tank so that all plates above the bottom V-shaped plate 12 are removable.
The two skimmers 8 and 13 are connected with each other along a side wall by means of a duct so that only one outlet tube for the oil is necessary.
The levels of both skimmers 8 and 13 are adjustable by means of tube couplings at both ends of the skimmers.
The water overflow 15 is adjustable by turning a tube coupling (not shown) provided around the tube 4 after the bend.
It is easy to form the plates 10 into a V-shape.
The baffle 9 is mounted slanting between the side walls.
WHAT WE CLAIM IS: 1. A separator for separating liquid constituents of a flow of liquid of different specific gravities, which comprises a tank with an inlet for the flow of liquid, an outlet for a separated heavier liquid constituent, means for withdrawing from the tank a separated lighter liquid constituent floating on the top of the liquid in the tank and a separating unit mounted in the tank between the inlet and the outlet and comprising a set of spaced plates of inverted-Vshaped cross section whose ridge lines lie in a common vertical plane and are upwardly inclined, each plate having a pointed upper end portion whose profile is convergent in plan, its edges intersecting at a point in the ridge line of the plate, and the pointed upper end portion of each plate (except the uppermost) projecting forwardly beyond the corresponding end portion of the plate next above it, the plates defining between them a set of upwardly-inclined flow ways of inverted-V-shaped cross section arranged one above another through which the flow of liquid from the inlet passes the arrangement being such that the liquid flow from the inlet enters the flow ways between the lower ends of the plates and the separated constituents leave the flow ways between the pointed upper end portions of the plates so that the separated lighter constituent rises to float on the top of the liquid in the tank for withdrawal by the said means.
2. A separator as claimed in Claim 1 in which a baffle plate is mounted in the tank downstream of the separating unit and extends downwardly through the liquid surface. and an overflow weir is provided in the tank downstream of the baffle plate, the separated heavier liquid constituent after leaving the flow ways being caused to flow
**WARNING** end of DESC field may overlap start of CLMS **.

Claims (6)

**WARNING** start of CLMS field may overlap end of DESC **. larger space 7, so that the velocity of the flow of the upwardly flowing liquid to be cleaned decreases as it passes through the space 7. As a result the heavier particles such as sand and the like suspended in the liquid flow will descend, and the free easyto-separate constituents such as light oil will tend to float upwardy in space. The resultant floating layer of light oil is withdrawn by means of a skimmer 8. This skimmer 8 is adjusted in such a way that during removal of the oil the thickness of the oil layer remains constant. This can only be done when the viscosity of the oil is not too high. If it is, the oil skimmer 8 has to be turned manually. After this first separation the now less soiled water flows slowly downwardly between the baffle 6 and a baffle 9 to the entrance of the separator unit proper 2, after which it will flow upwardly between the parallel inclined separator plates 10. These plates 10, the upper of which is indicated at 11 and the lower of which is indicated at 12, are of inverted-V-shape in section as shown in Figure 2 with pointed upper ends. Thus the uppermost end portion 10A of the length of each plate is of convergent form, terminating in a point on the ridge line of the plate, and moreover the convergent end portion 10A of each plate 10, 12 projects forwardly beyond the tip of the corresponding end portion of the plate next above it, as is seen clearly in Figure 1. At the entry into the separator unit 2 of the soiled liquid the smaller droplets of oil will collect as a mist under the slanting sides of each plate 10, the longitudinal edges of the plates 10 lying close to the opposite side walls of the tank 1 as shown in Figure 2. At a certain stage an oil film will be formed by this continuous mist deposit. The continuous growing oil film will become thicker and will go in a V-shaped movement towards the ridge line or crosssectional apex of each plate 10 as the result of the inverted-V-shape of the plates and the angle of about 15 degrees with the horizontal at which the ridge lines of the plates are inclined. Towards the upper end of each inverted V-shaped plate 10. the oil films collecting under both sides of the plate 10 will be joined to form a stream. At the pointed ends of the convergent portions 10A of the V-shaped plates 10 the oil will leave the plates in the shape of big drops. These big drops will rise easily to the surface because of their size. These drops then again form an oil layer at the surface which is removed bv a second skimmer 13. The water leaving the separating unit 2 travels down under a driving baffle 14 and then up and out through an adjustable overflow 15, with a great degree of cleanness. The number of plates 10 and the selected distance between the plates determine the capacity. The plates may be pushed inwards by means of cams provided on the side walls of the tank so that all plates above the bottom V-shaped plate 12 are removable. The two skimmers 8 and 13 are connected with each other along a side wall by means of a duct so that only one outlet tube for the oil is necessary. The levels of both skimmers 8 and 13 are adjustable by means of tube couplings at both ends of the skimmers. The water overflow 15 is adjustable by turning a tube coupling (not shown) provided around the tube 4 after the bend. It is easy to form the plates 10 into a V-shape. The baffle 9 is mounted slanting between the side walls. WHAT WE CLAIM IS:
1. A separator for separating liquid constituents of a flow of liquid of different specific gravities, which comprises a tank with an inlet for the flow of liquid, an outlet for a separated heavier liquid constituent, means for withdrawing from the tank a separated lighter liquid constituent floating on the top of the liquid in the tank and a separating unit mounted in the tank between the inlet and the outlet and comprising a set of spaced plates of inverted-Vshaped cross section whose ridge lines lie in a common vertical plane and are upwardly inclined, each plate having a pointed upper end portion whose profile is convergent in plan, its edges intersecting at a point in the ridge line of the plate, and the pointed upper end portion of each plate (except the uppermost) projecting forwardly beyond the corresponding end portion of the plate next above it, the plates defining between them a set of upwardly-inclined flow ways of inverted-V-shaped cross section arranged one above another through which the flow of liquid from the inlet passes the arrangement being such that the liquid flow from the inlet enters the flow ways between the lower ends of the plates and the separated constituents leave the flow ways between the pointed upper end portions of the plates so that the separated lighter constituent rises to float on the top of the liquid in the tank for withdrawal by the said means.
2. A separator as claimed in Claim 1 in which a baffle plate is mounted in the tank downstream of the separating unit and extends downwardly through the liquid surface. and an overflow weir is provided in the tank downstream of the baffle plate, the separated heavier liquid constituent after leaving the flow ways being caused to flow
beneath the baffle plate and then over the weir to the outlet, and the means for withdrawing the separated lighter liquid constituent being located between the baffle plate and the inlet.
3. A separator as claimed in Claim 1 or Claim 2 including a preliminary separating device of baffle type providing an upwardlydivergent flow passage and being disposed in the path of the liquid flow in the tank upstream of the separating unit.
4. A separator as claimed in Claim 3 including a deflector plate mounted in the tank and extending downwardly through the liquid surface towards the uppermost plate of the separating unit, in a position to deflect the liquid flow leaving the preliminary separating device into the flow ways between the lower ends of the inclined plates.
5. A separator as claimed in Claim 4 in which the longitudinal edges of the plates of the separating unit lie close to the opposite side walls of the tank.
6. A separator substantially as specifically described herein with reference to the accompanying drawings.
GB7002/77A 1976-02-19 1977-02-18 Separating device to separate two liquids of different specific gravity Expired GB1563586A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
NL7601702A NL7601702A (en) 1976-02-19 1976-02-19 SEPARATION DEVICE FOR SEPARATING TWO LIQUIDS OF DIFFERENT TYPES OF WEIGHT.

Publications (1)

Publication Number Publication Date
GB1563586A true GB1563586A (en) 1980-03-26

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ID=19825651

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GB7002/77A Expired GB1563586A (en) 1976-02-19 1977-02-18 Separating device to separate two liquids of different specific gravity

Country Status (8)

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AT (1) AT366289B (en)
BE (1) BE851522A (en)
CH (1) CH618886A5 (en)
DE (1) DE2706642C3 (en)
FR (1) FR2341345A1 (en)
GB (1) GB1563586A (en)
IT (1) IT1082466B (en)
NL (1) NL7601702A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2469948A1 (en) * 1979-11-20 1981-05-29 Nordstjernan Rederi Ab METHOD AND DEVICE FOR INTRODUCING AND DISPENSING COMPOSITE LIQUIDS IN A LAMINARY SEPARATION APPARATUS
GB2275210A (en) * 1993-02-17 1994-08-24 Oekologia Beteiligungs Handels Regenerating of degreasing liquid
GB2276561A (en) * 1993-04-02 1994-10-05 Squid Systems Pty Ltd Continuous separation of immiscible liquids
WO1998001395A1 (en) * 1995-06-26 1998-01-15 Terje Johan Myrhaug Oil/grease separator
CN115502064A (en) * 2022-09-19 2022-12-23 浙江嘉柯新材料科技有限公司 Antifouling type waterborne synthetic leather and production facility thereof

Families Citing this family (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE3024681A1 (en) * 1980-06-30 1982-01-28 Schloemann-Siemag AG, 4000 Düsseldorf Rolling mill spent oil purifier - based on sedimentation and flotation in sectionalised reservoir
DE3043254A1 (en) * 1980-11-15 1982-07-08 Robert Bosch Gmbh, 7000 Stuttgart METHOD FOR CLEANING NEUTRALIZED INDUSTRIAL WASTEWATER AND DEVICE FOR IMPLEMENTING THE METHOD
NL8100955A (en) * 1981-02-27 1982-09-16 Pielkenrood Vinitex Bv MULTI-PHASE SEPARATOR.
SE445710B (en) * 1984-11-01 1986-07-14 Hyosong M Lee DEVICE FOR CONTINUOUS SEPARATION OF A LIQUID MIXTURE, INCLUDING A LIGHTER AND A Lighter Phase
FR2654950B1 (en) * 1989-11-29 1992-03-06 Saint Dizier Ste Cale COALESCENCE OIL-WATER SEPARATOR.
DE4231790B4 (en) * 1992-09-23 2006-10-05 Fariwar-Mohseni, Ursula Apparatus for the treatment of waste water
FR2726482B1 (en) * 1994-11-09 1997-01-31 Prefaest Sa HIGH SEPARATION LIQUID SEPARATOR
DE19850320C2 (en) * 1998-11-02 2002-09-26 Hans Huber Ag Masch & Anlagenb Compact system for the mechanical treatment of waste water
FR2855070B1 (en) * 2003-05-21 2006-09-01 Eparco Assainissement DECANTER, IN PARTICULAR FOR THE PRIMARY TREATMENT OF DOMESTIC EFFLUENTS OR THE LIKE
DE102013114380B4 (en) * 2013-12-18 2021-12-30 Endress+Hauser (Deutschland) Gmbh+Co. Kg Device for the detection of a non-conductive liquid in water

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2613811A (en) * 1948-12-09 1952-10-14 Standard Oil Dev Co Continuous settling apparatus
US3558482A (en) * 1968-07-31 1971-01-26 Smith Ind Inc Water purification
AT300687B (en) * 1970-07-13 1972-08-10 Internat Pollution Control Sys Device for the separation of oil from oily liquids, in particular ship bilges of pleasure boats or the like.

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2469948A1 (en) * 1979-11-20 1981-05-29 Nordstjernan Rederi Ab METHOD AND DEVICE FOR INTRODUCING AND DISPENSING COMPOSITE LIQUIDS IN A LAMINARY SEPARATION APPARATUS
GB2275210A (en) * 1993-02-17 1994-08-24 Oekologia Beteiligungs Handels Regenerating of degreasing liquid
GB2276561A (en) * 1993-04-02 1994-10-05 Squid Systems Pty Ltd Continuous separation of immiscible liquids
WO1998001395A1 (en) * 1995-06-26 1998-01-15 Terje Johan Myrhaug Oil/grease separator
CN115502064A (en) * 2022-09-19 2022-12-23 浙江嘉柯新材料科技有限公司 Antifouling type waterborne synthetic leather and production facility thereof
CN115502064B (en) * 2022-09-19 2023-06-09 浙江嘉柯新材料科技有限公司 Antifouling type waterborne synthetic leather and production equipment thereof

Also Published As

Publication number Publication date
ATA110877A (en) 1981-08-15
DE2706642B2 (en) 1981-07-02
FR2341345A1 (en) 1977-09-16
CH618886A5 (en) 1980-08-29
IT1082466B (en) 1985-05-21
DE2706642C3 (en) 1982-09-09
DE2706642A1 (en) 1977-09-01
AT366289B (en) 1982-03-25
BE851522A (en) 1977-08-17
NL7601702A (en) 1977-08-23

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Legal Events

Date Code Title Description
PS Patent sealed [section 19, patents act 1949]
PCNP Patent ceased through non-payment of renewal fee