Longitudinal settler with flow separation

A continuous longitudinal settler with flow separation including an entry zone for the liquid to be treated, including a system for distribution of this liquid; a zone for homogenization of the flow, ensuring a dissipation of the entry energy and a constant velocity profile at the exit of this zone; a working zone for settling, exhibiting a homogeneous flow along the whole length of which a constant velocity profile is maintained, together with a high Froude number guaranteeing the stability of the liquid flow; and a zone for separation and for recovery of the flows, situated at the downstream end of the settler, the treated liquid being discharged at the surface and the settled matter via the bottom of the settler.

FIELD OF THE INVENTION 
The present invention relates generally to a device which makes it possible 
to separate continuously the immiscible matter contained in a liquid, in 
the form of an emulsion or suspension, and is aimed more particularly at a 
longitudinal settler with flow separation, which can be utilized, for 
example, in a water treatment plant (especially settling, clarification or 
oil separation). 
BACKGROUND OF THE INVENTION 
It is known that a continuous settler must be constructed so that: 
the flow regime should be homogeneous, with as little turbulence as 
possible and as stable as possible, so as to obtain horizontal and 
perfectly parallel fluid filaments over the whole length of the structure 
or at the very least over its major portion; 
the entry zone should be as small as possible and should make it possible 
to obtain a distribution which is as perfect as possible, of the raw 
liquid to be treated and a homogeneous flow regime; 
the recovery of the clarified liquid and that of the settled matter should 
be as uniform as possible, so as not to give rise to any significant 
perturbation of the homogeneous flow regime. 
When a longitudinal settler with horizontal flow is produced, the 
difficulty which is encountered is that of ensuring a good hydraulic 
distribution over a vertical plane, both at the entry of the structure and 
at its exit, and the problems which are encountered are those posed by the 
accumulation, the collection and the discharge of the settled matter, 
especially of sludge. 
In order to solve the abovementioned problems, attempts are made to obtain, 
as far as possible, a circulation that has the least possible turbulence 
throughout the settler, which is characterized by the lowest possible 
values of the Reynolds number. Furthermore, it is also known that the 
Froude number allows the stability of a flow regime to be assessed: the 
more stable the circulation, the more uniform is the distribution of the 
velocities over the whole section of the settling tank, stable 
circulations being characterized by high Froude numbers. 
Reference may be made on this topic to the "Memento Technique de l'Eau" 
"Water Technology Memorandum"!, 9th edition 1989, published by assignee, 
pages 158 to 166. 
The above considerations demonstrate the importance of the internal 
hydraulics of a settler, which is the overall result of the geometry of 
the settler, of the devices for the entry and exit of liquids and for 
recovery of the settled matter, especially of the sludge, and of the 
relative arrangement of these three devices. 
It is known that a zone of calm and unperturbed flow regime is needed to 
produce an optimum settling, this zone being defined as being the working 
zone of settling, in which the flow velocity profile is regular. A settler 
has proportionally better performance the greater the size of this working 
zone in relation to the overall dimensions of the structure. 
However, in most of the settlers constructed at present, the working zone 
of settling is greatly reduced as a result of the perturbations induced 
especially, on the one hand, by the liquid entry system which does not 
fulfil its function of energy dissipation and of distribution and, on the 
other hand, by the device for recovery of the treated liquid, which gives 
rise to inflow currents whose perturbing effect is felt in the major 
portion of the structure. 
The invention proposes to provide an improved horizontal settler which is 
noteworthy especially for outstanding internal hydraulics making it 
possible to obtain a very good efficiency. 
Consequently, this invention relates to a continuous longitudinal settler 
with flow separation, characterized in that it includes: 
an entry zone for the liquid to be treated, including a system for 
distribution of this liquid; 
a zone for homogenization of the flow regime, ensuring a dissipation of the 
entry energy and a regular and substantially flat velocity profile at the 
exit of this zone; 
a working zone of settling exhibiting a homogeneous flow regime, along the 
whole length of which a regular and substantially flat velocity profile is 
maintained, together with a high Froude number guaranteeing the stability 
of the liquid flow regime; and 
a zone for separation and for recovery of the flows, situated at the 
downstream end of the settler, the treated liquid being discharged at the 
surface and the settled matter via the bottom of the settler. 
According to the present invention, the zone for entry and distribution of 
the liquid to be treated may be produced in accordance with the 
characteristics defined co-pending patent application Ser. No. 08/621,510 
by the present assignee and entitled: "Improvements made to settlers". 
According to this preferred embodiment, this entry zone comprises a system 
for the distribution of liquid, which consists of a plurality of 
calibrated openings made in the partitions of the chamber for allowing the 
liquid to enter. These openings are fed with liquid from a feed channel so 
that each opening should receive a determined fraction of the flow of the 
liquid, the said openings being arranged according to at least two 
horizontal arrays. Reference may be made to this patent application, 
especially with regard to the technical effects and advantages provided by 
this preferred solution. 
According to the present invention the zone for separation and for recovery 
of the flows includes: 
in its upper portion a system of gutters for recovery of the treated 
liquid, these gutters being arranged preferably over the whole width of 
the structure, and 
in its lower portion, either a system of hoppers in which the settled 
matter is deposited, the latter being recovered from the hoppers by any 
conventional means, or a system for scraping and for recovery of the 
settled matter. 
According to another embodiment of the present invention, the zone for 
separation and for recovery of the flows includes: 
in the upper portion, means for recovery of the treated liquid, which may 
be produced in the form of gutters or of an immersed network of perforated 
pipes which are situated near the surface of the settler; 
in the lower portion, means for recovery of the settled matter, preferably 
produced in the form of an immersed network of perforated pipes positioned 
at the bottom of the settler. 
According to a preferred embodiment, the zone for separation and for 
recovery of the flows is provided with a system of sensors for the treated 
liquid--settled matter interface, enabling a regulation of the recovery of 
the settled matter to be obtained. 
According to the invention, and in the case where it is applied to the 
treatment of suspensions, the recovery of the floating matter is performed 
with the aid of transverse gutters which may be arranged either upstream 
of the structure, in the zone of entry of the liquid, or downstream, at 
the entry of the zone for separation and for recovery of the flows, or 
simultaneously in both these places. 
According to the invention, the settler is of the type with separate 
channels, optionally with communicating walls, each channel comprising the 
four zones defined above, the number of channels being chosen so as to 
obtain the desired Reynolds number. 
According to a preferred embodiment, a device for recovery of the settled 
matter is provided in the second and third zone, which may be produced 
conventionally in the form of a movable scraper bridge which may be 
provided with suction pipes that enable a recovery of the settled matter 
in these two zones to be carried out. 
According to another embodiment of the present invention, in the zone for 
separation and for recovery of the flows, the settler additionally 
comprises a laminar system in order to produce a refining of the settling.

DETAILED DESCRIPTION OF THE INVENTION 
Reference is made firstly to the diagram in FIG. 1, relating to the 
application of the invention to the treatment of suspensions, in which the 
other zones of a settler according to the invention have been marked out: 
Zone 1 is that through which the entry of the liquid to be treated takes 
place, for example a raw water containing matter in suspension, especially 
an industrial or urban waste water. This zone 1 comprises a system for 
distribution of the liquid to be treated and, in this example of preferred 
embodiment, this system includes a plurality of openings placed and 
designed so as to obtain a practically uniform dispersion of the jets of 
liquid in all directions, while occupying virtually all of the section 
offered to the flow regime. As explained above, this distribution system 
is preferably produced in accordance with the arrangements provided in 
co-pending application, mentioned above and to which the reader may refer. 
This system will therefore not be described again. 
Zone 2, which follows the liquid entry and distribution zone 1, forms a 
zone for homogenization of the flow regime. Its length is determined so as 
to obtain a natural dissipation of the entry energy and a flat velocity 
profile at its exit. 
Zone 3 is the working zone for the settling and it exhibits a homogeneous 
and unperturbed flow regime of the liquid throughout its length, this calm 
flow regime making it possible to maintain a regular velocity profile. As 
can be seen in this FIG. 1, the size of this zone 3 is large in relation 
to the general size of the settler, and this makes it possible to obtain 
an optimum efficiency of the latter. 
Zone 4 forms the exit zone for the settled matter and for the treated 
liquid, in which any distortion of the velocities in relation to the 
preceding zone must be avoided. The separation and the recovery of the 
flows: treated liquid/settled matter, are therefore carried out in this 
zone 4, the treated liquid being recovered at the surface and the settled 
matter via the bottom of the settler. In the example of embodiment 
illustrated in FIG. 1, which applies to the treatment of suspensions, the 
settled matter is collected in a system of hoppers which will be described 
in detail below. 
In the nonlimiting example of embodiment shown in this FIG. 1, this zone 4 
comprises, at its entry and over its whole width, a transverse gutter for 
recovery of the floating matter, referred to by reference 10. This 
recovery of the floating matter may also be carried out at the exit of the 
zone 1. It is obviously possible to envisage means for recovery of the 
floating matter at the exit of this zone 1 and at the entry of the zone 4. 
This recovery of the floating matter, performed at the beginning of the 
zone 4 and obtained with the aid of a transverse gutter arranged over the 
whole width of the settler, makes it possible to protect the exit of the 
treated liquid. A natural siphoning is thus produced over the width of the 
structure, and this contributes to making its construction easier. 
A device for recovery of the settled matter has also been shown, at 12, in 
this FIG. 1. This device may be produced conventionally in the form of a 
scraper bridge, optionally provided with suction pipes, as will be 
described below. 
Reference is now made to FIGS. 2 to 5, which show in detail a nonlimiting 
example of embodiment or the device of the invention in accordance with 
the diagram of FIG. 1. 
In these FIGS. 2 to 5 it is seen that the settler according to the present 
invention takes the conventional form of a tank referred to in its 
entirety by reference 14, partitioned into channels with the aid of 
separating walls, which may be communicating, as is clearly seen in FIG. 
3. This settling tank 14 comprises, at its entry in the zone corresponding 
to the zone 1 of FIG. 1, a device for allowing the entry of and for 
distributing the liquid to be treated, which is referred to in its 
entirety by reference 16, which may be, for example, of the type mentioned 
above and which, consequently, will not be described, it being possible 
for the reader to refer to the abovementioned co-pending application. 
Following the entry and distribution device 16, each channel of the 
settling tank comprises the zones 2 and 3 in accordance with FIG. 1. The 
description of these two zones will therefore not be repeated. 
As already seen, the zone 4 of this settler thus comprises means for 
simultaneous separation and recovery of the settled matter and of the 
treated liquid. These means are referred to in their entirety by reference 
18 (FIG. 2). 
In this example of application to the treatment of suspensions, the settled 
matter is collected in a system of hoppers such as 20, it being possible 
for each hopper 20 to be provided at its base with a discharge orifice 
emerging into a collecting pipe 22 (FIG. 5), from which the settled matter 
is delivered into collecting gutters such as 24, placed at the periphery 
of the structure (see FIG. 3), the recovery of the settled matter being 
carried out through the intermediacy of valves, for example of the 
telescopic type 26 (FIG. 5). 
This recovery of the settled matter may be performed by any appropriate 
means, for example with the aid of gravity suction pipes emerging into 
gutters arranged at the surface of the settler and in which the liquid 
level is lower than that in the settler, or else by any known means for 
pumping out, for example through the intermediacy of pipes provided with 
emulsion pumps, emerging into gutters arranged at the surface of the 
settler and in which the liquid level may be higher than that in the 
settler. 
This same zone 4 comprises the system of gutters which, according to the 
invention, ensures the recovery and the discharge of the treated liquid. 
In order to maintain an unperturbed flow regime in this zone 4 a recovery 
of the treated liquid is carried out over the whole surface of this zone, 
in contrast to the traditional arrangements in which the recovery of the 
treated water is performed through the intermediacy of side gutters, which 
gives rise to inflow currents whose effects are felt far upstream of this 
zone for discharge of the treated liquid, thus perturbing the flow regime 
in the settler. Thus, in this example of embodiment, the recovery of the 
treated liquid in the zone 4 is performed through the intermediacy of a 
network of transverse gutters such as 28, emerging into lengthwise gutters 
such as 30, the treated liquid being subsequently discharged through the 
intermediacy of a collector channel 32. 
As shown in FIGS. 2 and 5, the device according to the present invention 
may additionally comprise a system for laminar settling 33, placed in the 
zone 4, in order to further improve the settling. 
According to an alternative form of the invention the said system of 
gutters for recovery of the treated liquid may include a network of 
lengthwise gutters emerging into one or a number of transverse gutters, 
the treated liquid being discharged from this system of gutters through 
the intermediacy of the collector channel 32. 
It was seen above that, according to the invention, it was possible to 
provide a system for recovery of the settled matter, such as 12, arranged 
in the zones 2 and 3 of the settling tank. This system may be of a 
conventional "movable scraper bridge" type comprising scraper blades such 
as 34 (FIG. 4), and each scraper blade may be provided with a suction pipe 
such as 36. This alternative form of the invention makes it possible to 
produce a scraped settler with suction of the settled matter, which may be 
employed especially in a plant for clarification of liquids and especially 
of waste water, using activated sludge. However, this is merely an example 
of application and an embodiment, no limitation being implied thereby. 
FIG. 6 illustrates the application of a settler according to the invention 
to the treatment of emulsions. The four zones whose characteristics were 
defined in the preceding description are encountered again in this FIG. 6, 
only the zone 4 for separating the flows being produced differently. In 
this application the recovery of the treated liquid is performed in the 
upper portion of this zone, for example through the intermediacy either of 
gutters as specified above or of an immersed network of perforated pipes 
situated near the surface of the settler, and the recovery of the settled 
matter is performed with the aid of an immersed network of perforated 
pipes positioned at the bottom of the settler. 
In the alternative form of the invention, illustrated by FIG. 7, the 
recovery of the settled matter in the zone 4 is performed with the aid of 
a scraping system 35. 
As stated above, the settler according to the invention enables a 
practically constant velocity to be maintained over the whole length of 
its tank, and this allows an outstanding stability of the flow regime to 
be obtained. This result is due to the combined characteristics of the 
zone 1 for entry and distribution of the liquid to be treated, of the 
zones 2 and 3 which have a sufficient length in order to obtain and 
maintain the stability of the liquid flow regime, and of the zone 4 for 
separation and for recovery of the flows, the functioning of which has no 
detrimental effect on the stability of the upstream flow regime of the 
liquid to be treated. 
According to an alternative form of the invention a lamellar settler may 
also be provided in the zone 4, which makes it possible to improve the 
separation of the matter in suspension in the treated liquid and to 
collect nonhomogeneous matter, and this enables a refining of the settling 
to be produced. 
Means which make it possible to regulate the recovery of the settled matter 
as a function of the flow rate of the treated liquid may also be provided 
according to the invention. In fact, the settler according to the present 
invention is characterized by a very clean surface of separation of the 
flows at the entry of the zone 4, and this makes it possible, with the aid 
of sensors, to detect the position in height of this surface of treated 
liquid/settled matter separation and to produce a system for servo control 
of the recovery of the settled matter in the lower portion of the fourth 
zone, for example as a function of the flow rate. 
Among the advantages provided by the device according to the invention 
there may be mentioned, in particular: 
an outstanding efficiency of the settling resulting from the stability of 
the flow regime of the liquid over the whole length of the structure, due 
to the factors mentioned above, 
a simplification of the construction, resulting especially from the fact 
that, in contrast to the previous solutions, the recovery of the treated 
liquid is not performed by a system of side gutters but over the whole 
width of the structure, and this makes it easier to produce the roll 
surfaces for a scraper bridge, 
possibility of choosing the number of channels of the settler tank so as to 
preserve the desired Reynolds number, without reduction in the Froude 
number. 
The settler according to the invention can be applied to the separation of 
any immiscible matter present in a liquid, in the form of an emulsion or 
of a suspension, for example to settling, to clarification, to oil 
separation and the like. It will preferably be utilized, of course, in a 
water treatment plant for separating the matter in suspension which is 
present in industrial or urban waste water. The settler can also be 
utilized, as already mentioned, in a plant for clarification of waste 
water with sludge recirculation. 
It remains clearly understood that the present invention is not restricted 
to the examples of embodiment and of utilization which have been described 
and/or mentioned here, but that it includes all the alternative forms 
thereof.