U.S. patent number 3,763,014 [Application Number 05/195,361] was granted by the patent office on 1973-10-02 for multi-stage flash evaporator.
This patent grant is currently assigned to Societa Italiana Resine S.p.A.. Invention is credited to Diego Barba, Giuseppe Liuzzo, Giovanni Tagliaferri.
United States Patent |
3,763,014 |
Barba , et al. |
October 2, 1973 |
MULTI-STAGE FLASH EVAPORATOR
Abstract
An improved multi-stage flash evaporator for distilling sea
water, which, in transverse profile, is symmetrical about a
vertical central axis. The evaporator construction includes a
horizontally disposed, longitudinally extending, continuous,
tubular casing, whose profile, on each side of the axis, is
substantially of the shape of an ellipse which is truncated towards
one end by this axis; and an inverted U-shaped shell within the
casing and extending along the length thereof. The lower edges of
the shell are sealingly connected to the floor of the casing, While
the top of the shell sealingly contacts the upper junction
connecting the elliptically shaped zones of the casing. A plurality
of vertical, spaced apart, transversely extending, apertured
partitions subdivide the shell into a number of serially connected
chambers, for the raw sea water to flow therethrough and evaporate
therein. The outer casing and the inner shall define separate,
condensation chambers which are positioned laterally on each side
of the serially connected evaporation chambers, the distillate
vapor flowing from the evaporation to the condensation chambers
through droplet-separating filters housed in the top of the
shell.
Inventors: |
Barba; Diego (Rome,
IT), Liuzzo; Giuseppe (Rome, IT),
Tagliaferri; Giovanni (Rome, IT) |
Assignee: |
Societa Italiana Resine S.p.A.
(Milan, IT)
|
Family
ID: |
11234130 |
Appl.
No.: |
05/195,361 |
Filed: |
November 3, 1971 |
Foreign Application Priority Data
|
|
|
|
|
Nov 12, 1970 [IT] |
|
|
31629 A/70 |
|
Current U.S.
Class: |
202/173; 159/2.3;
203/11 |
Current CPC
Class: |
C02F
1/06 (20130101); B01D 3/065 (20130101); Y02A
20/128 (20180101); Y02A 20/124 (20180101) |
Current International
Class: |
C02F
1/06 (20060101); B01D 3/00 (20060101); B01D
3/06 (20060101); B01d 003/00 (); B01d 001/28 ();
B01d 003/02 (); B01d 003/10 () |
Field of
Search: |
;159/2,2MS,15,22,18
;202/173,234,174 ;203/10,11 |
References Cited
[Referenced By]
U.S. Patent Documents
Primary Examiner: Yudkoff; Norman
Assistant Examiner: Sofer; J.
Claims
Having thus described the invention, what is desired to be secured
by Letters Patent and hereby claimed is:
1. A flash evaporator for distilling sea water and the like in a
plurality of multi-stage, generally horizontally disposed, serially
connected, adjacent evaporation chambers, wherein feed water to be
evaporated flows continuously through successive stages in which
progressively lower pressure exists in adjacent stages, the
evaporator comprising:
a continuous, elongated, generally horizontally disposed tubular
casing which in transverse profile is symmetrical about a vertical
central axis, the part of the profile on each side of the central
axis being generally of the shape of an ellipse whose major axis is
at right angles to such central axis and which is truncated towards
one end by such central axis, the profile deviating from elliptical
curvature in a zone extending on the lower side of the casing from
a point located approximately below the centre of the ellipse to
the central axis, the curvature in this zone being circular;
an elongated, inverted U-shaped shell, positioned within an
extending along the length of the casing, the lower edges of the
shell being sealingly connected to the casing, the shell thus
having as its floor a central portion of the casing, this shell
consisting of two vertical side walls and a top which is generally
flat in its central portion and curved at the edges joining said
side walls, the top meeting the casing sealingly at the junction
connecting the elliptically shaped zones of the casing;
a plurality of transverse partition walls positioned vertically
within the casing and spaced apart from each other, said partition
walls dividing the shell into said plurality of evaporation
chambers, each chamber having inlet and outlet means for the
feedwater to be evaporated, such means including passageways formed
in the bottoms of the partition walls serving as the feedwater
outlet means for one chamber and feed water inlet means for the
adjacent, lower pressure evaporation chamber; the inner surface of
the casing and the outer surface of the shell defining a plurality
of separate condensation chambers extending along said evaporation
chambers;
droplet-separating filter means housed in the top of the shell, for
permitting the flow of vapour from each of said evaporation
chambers to both of the condensation chambers laterally connected
thereto;
a pair of heat exchangers, one each positioned within and extending
along the length of each condensation chambers.
2. A flash evaporator as claimed in claim 1, wherein the ratio
between the major and the minor axis of each ellipse ranges from
1.4/1 to 1.6/1.
3. A flash evaporator as claimed in claim 1, wherein the angle
subtending said circular curvature ranges from 13.degree. to
18.degree..
4. A flash evaporator as claimed in claim 1, further comprising a
plurality of dams positioned vertically within said shell on the
floor thereof, each of said dams extending transversally of said
shell and each positioned within an evaporation chamber
approximately midway between said transverse partition walls, the
upper edge of said dams being positioned at a height greater than
the height of the upper edge of the passageways in said transverse
partition walls to maintain the liquid level above the upper edge
of said passageways.
Description
BACKGROUND OF THE INVENTION
1. Field of the Invention
The present invention relates to a multi-stage flash evaporator
particularly suitable for desalting sea water. More specifically,
the present invention relates to an evaporator wherein feed water
to be evaporated flows continuously through a plurality of serially
connected, evaporation chambers in which successively lower
internal pressures exist in adjacent chambers with each evaporation
chamber being connected to two separate condensation chambers.
2. The Prior Art
There have recently been disclosed a number of multi-stage flash
evaporators for distilling sea water, brack water and the like.
For instance, U.S. Pat. No. 3,146,177 (to Chalmers et al.)
discloses a multi-stage evaporator comprising a plurality of
evaporation chambers in series and side condensation chambers. Raw
sea water to be preheated, is subdivided into parallel streams
flowing through heat exchangers arranged within the condensation
chambers, the direction of flow of the sea water through the
exchangers being opposite to that of the flow of water being
evaporated through the evaporation chambers.
In accordance with Chalmers et al., each evaporation chamber is
subdivided into two half chambers, with each half chamber being
connected with one condensation chamber only, so that a single
evaporation chamber does not communicate with both of the laterally
positioned condensation chambers. Such a construction possesses
several major disadvantages, since it does not uniformly distribute
the vapor evolved at the evaporation zone; besides, the complexity
of such construction and the presence of several sharp corners and
dead zones result in an inefficient operation and, ultimately, an
impure distillate.
SUMMARY OF THE INVENTION
In general terms, the multi-stage flash evaporator construction for
distilling sea water and the like in accordance with the present
invention, may be stated as substantially comprising an outer,
continuous, generally horizontally disposed, longitudinally
extending casing which is specially shaped in the manner that will
be fully explained in detail below, and an inverted U-shaped shell
which is positioned within and extends along the length of the
casing. A plurality of vertical, spaced-apart, transverse partition
walls having passages therethrough adjacent the bottom of the
shell, subdivide the shell into a plurality of serially connected
chambers. At the opposite ends of the shell, inlet and outlet means
are provided for the continuous flow through the evaporation
chambers of the pre-heated liquid (e.g. sea water) to be
evaporated. Successively lower internal pressures exist in adjacent
chambers. Therefore, the inner shell defines the feedwater
receiving zone and the evaporation zone of the evaporator in
accordance with the invention. The outer walls of the shell and the
inner walls of the casing define a number of separate condensation
chambers positioned laterally on each side of the central
evaporation zone, the condensation chambers extending along the
length of the casing. In the generally flat top surface of the
shell, openings are provided for accommodating filtering means
which are horizontally positioned over the evaporation chambers and
which permit the flow of vapor from the evaporation chambers to the
condensation chambers. Two heat exchangers, extending along the
length of the casing, are positioned within the condensation
chambers to cause condensation of the vapor while partially
pre-heating the raw sea water, the flow of the raw sea water
through the heat exchangers being in a direciton opposite that of
the flow of the sea water being evaporated in the evaporation
chambers.
More specifically stated, the evaporator construction in accordance
with the present invention, comprises:
a continuous, elongated, generally horizontally disposed, tubular
casing which in transverse profile is symmetrical about a vertical
central longitudinal plane, the part of the profile on each side of
the central plane being generally of the shape of an ellipse whose
major plane is at right angles to such central plane and which is
truncated towards one end by such central plane, the profile
deviating from elliptical curvature in a zone extending on the
lower side of the casing from a point located approximately below
the centre of the ellipse to the central plane, the curvature in
this zone being circular;
an elongated, inverted U-shaped shell, positioned within and
extending along the length of the casing, the lower edges of the
shell being sealingly connected to the casing, the shell thus
having as its floor a central portion of the casing, this shell
consisting of two vertical side walls and a top which is generally
flat in its central portion and curved at the edges joining said
side walls, the top meeting the casing sealingly at the junction
connecting the elliptically shaped zones of the casing;
a plurality of transverse partition walls positioned vertically
within the casing and spaced apart from each other, said partition
walls dividing the shell into said plurality of evaporation
chambers, each chamber having inlet and outlet means for the
feedwater to be evaporated, such means including passages formed in
the partition walls serving as the feedwater outlet means for one
chamber and feedwater inlet means for the adjacent, lower pressure
evaporation chamber; the inner surface of the casing and the outer
surface of the shell defining two separate condensation chambers
extending along said evaporation chambers;
droplet-separating filter means housed in the top of the shell, for
permitting the flow of vapour from each of said evaporation
chambers to both of the condensation chambers connected
thereto.
a heat exchanger positioned within and extending along the length
of each of the condensation chambers.
The evaporator in accordance with the invention appears more
suitable than prior evaporators to obtain high output capacities,
such as 500 m.sup.3 /hour of distillate product or even more. A
remarkable decrease in the evaporator weight and overall dimensions
is achieved. Furthermore, the special arrangement of the present
construction results in the lessening of the corrosion phenomens,
since the formation of stagnation zones of products which cannot be
condensed is hindered and no sharp corners are present. The highly
symmetrical arrangement also allows a better strain distribution,
with attendant stress decrease.
BRIEF DESCRIPTION OF THE DRAWINGS
In the drawings:
FIG. 1 is a perspective, partly cut-away view of a multi-stage
flash evaporator in accordance with the present invention:
FIG. 2 is a transverse sectional view taken along line II--II of
FIG. 1;
FIG. 3 is an enlarged, somewhat schematic, view of a portion of
FIG. 2;
FIG. 4 is a fragmentary longitudinal sectional view, taken along
line IV--IV of FIG. 2.
DESCRIPTION OF THE PREFERRED EMBODIMENT
Construction
As shown in the drawings, the flash evaporator construction of the
present invention is, in transverse profile, symmetrical about a
vertical central axis A. The evaporator includes a continuous,
generally horizontal, longitudinally extending, tubular casing 1,
which is supported on a plane surface by conventional supporting
means (not shown). As shown in detail in FIG.3, the profile of the
casing 1 on each side of the axis A is generally of the shape of an
ellipse which is truncated towards one end by the central axis A.
The ratio between the major axis M of the ellipse and its minor
axis m preferably ranges from 1.4/1 to 1.6/1. The profile of the
casing 1 deviates from elliptical curvature in a zone B extending
on the underside of casing 1, from a point C located below the
centre of the ellipse to a point D on the central axis A. Zone B is
generally circular and, preferably, the angle .alpha. subtending
the arc CD ranges from 13.degree. to 18.degree..
As shown in FIGS. 1 and 2, within the casing 1 and extending along
its length is, an inverted U-shaped shell 2, consisting of side
walls 3 and 4 and a flat top 5, which is curved at the edges 6, 7
joining side walls 3 and 4, respectively. The bottom edges 8 and 9
of the side walls 3 and 4, are sealingly connected to the central
portion of the floor 10 of the casing 1, this portion forming the
floor of the shell 2. The top 5 of the shell 2 meets the casing 1
sealingly at the joint J connecting the elliptically shaped upper
zones 11 and 11' of the casing 1. Two vertical partitions 12 and
13, having passages 12a, 12b and 13a, 13b, respectively, and end
walls 17 and 18, subdivide the interior of the shell 2 into three
evaporator chambers 14, 15 and 16, each chamber forming a feed
water receiving stage and also an evaporation stage. Connected to
the shell 2 is a sea water heater, not shown. Connections between
this heater and a raw sea water inlet 19 on the end wall 17 are
also not shown. The end wall 18 has an outlet 20 for discharging
the raw sea water which has not evaporated while flowing through
the evaporation chambers 14, 15 and 16.
In each of the evaporation chambers 14, 15 and 16, a dam 21 is
positioned vertically and extends transversely of shell 2. As shown
in FIG.4, the upper edges 21' of the dams 21 lie above the upper
edges of the passages 12a, 12b, 13a and 13b, to maintain the sea
water in each chamber at least at a minimum level sufficient to
prevent vapor from being blown between adjacent chambers through
said passages, while still permitting flow of the sea water to be
evaporated.
In order to regulate the flow of the sea water to be evaporated
through the evaporation chambers, as well the level of the sea
water in said chambers, the passages 12a, 12b, 13a and 13b could be
equipped with selectively adjustable, constriction means (such as a
sluice-gate valve).
The top 5 of the shell 2 has longitudinally extending openings 22
accommodating horizontal droplet-separating filters 23 which allow
the flow of vapor, while the droplets entrained by the vapors are
captured by the filters and drip back in the evaporation chamber.
The outer wall surfaces of the shell 2 and the inner wall surfaces
of the casing 1 define six side condensation chambers 24, 24a, 24b
and 25, 25a and 25b.
Two heat exchangers 26 and 27 comprising a plurality of condensing
tubes 29 are positioned within and extend along the length of the
condensation chambers. Conventional distillate drain means (not
shown in the drawings) are connected to the condensation chambers,
for discharging distillate water therefrom.
Operation
Raw sea water enters the condensing tube inlet 30 of evaporation
chamber 16, which is maintained at the lowest pressure and
temperature. This sea water is pre-heated by forming the condensing
medium flowing through the condensing tubes 29, passing
progressively through each of the evaporation chambers 16, 15 and
14, to leave finally through the condensing tube outlet 31 of the
chamber 14, which has the highest temperature and pressure. The
partially pre-heated sea water then passes in the heater (not
shown), where the sea water is heated to the desired temperature.
This fully pre-heated sea water is then fed into the feed water
receiving section of the chamber 14, to begin the desalinization
process. In the evaporation chamber 14, a certain amount of water
flashes off into vapor, which rises and passes through the
droplet-separating filters 23 into condensation chambers 24 and 25,
as indicated by the arrows in FIG.2. The filters 23 capture
droplets of unvaporized sea water which drip back into the
evaporation chamber 14, thus preventing any contamination of the
condensed vapor 33 contained in the condensing chambers 24 and 25.
The elliptically shaped zones 11 an 11' at the top of the casing 1
prevent deposition of the distillate vapor on the upper part of the
casing 1. As distillate vapor contacts the heat exchangers 26 and
27 within the condensation chambers 24 and 25, it gives up a
certain amount of heat to the raw sea water in the condensing tubes
29 and the distilled vapor then condenses and collects at the lower
portion of condensation chambers 24 and 25. The raw sea water which
has not undergone distillation within the first evaporation chamber
14, flows continuously through the passages 12a and 12b into the
next adjacent evaporation chamber 15, thus flowing in the opposite
direction to the raw sea water being pre-heated within the
condensing tubes 29. In the evaporation chamber 15, the same
process as in the evaporation chamber 14 takes place. The sea water
entering evaporation chamber 15 is, however, at a lower temperature
than sea water in chamber 14 and the pressure in chamber 15 is also
correspondingly lower. The sea water, then, flows continuously
through the evaporation chambers 14, 15 and 16 at progressively
decreasing temperature and pressure, finally leaving from the
chamber at the lowest temperature and pressure. The distillate 33
is drained from the condensing chambers 24 and 25 through a known
distillate drain, not shown in the drawings.
* * * * *