[0001] The present invention relates to a static emulsifier for the production of stable
mixtures of water, coal and oil.
[0002] In the present state of the art, no static emulsifiers exist for use for mixtures
of coal and oil.
[0003] It is however known an emulsifying device suitable to produce stable emulsions of
water in fuel oil.
[0004] For the description of such a device we avail ourselves of hereto attached fig. 1.
[0005] Such a device is constituted by a convergent conical duct (1), followed by a short
length of constant-section duct (2) ending into a plenum chamber (3) of cylindrical
section in communication with a discharge duct (4).
[0006] The mixture to be emulsified (5) delivered under pressure to the convergent duct
runs, at high speed,through the short duct of constant section and enters then the
plenum chamber; inside this chamber the emulsifying of the mixture occurs, the emulsified
mixture leaving (6) the device through the discharge duct.
[0007] The device operates on the basis of the superimposition of a plurality of physical
phenomena whose effect is of notably reducing the size of water drops, thus originating
a homogeneous emulsion.
[0008] Said device is poorly suitable to stabilize mixtures of coal, fuel oil and water.
[0009] A static equipment suitable to homogenize above all mixtures of coal, oil and water
has been found, which allows a stable mixture to be obtained.
[0010] The equipment which is the object of the present invention comprises a feeding duct
in communication with a duct of convergent cone-frustum shape, which continues into
a duct of constant section, leading to a chamber [chamber (a)] whose transversal dimensions
are greater than those of the constant-section duct, wherein the chamber (a) has a
volume which can be varied as requir ed by means of a movable adjustable bottom and
is provided in its lateral wall with a set of holes, said holes placing the chamber
(a) in communication with a discharge chamber [chamber (b)3 annular and coaxial with
the chamber (a).
[0011] The angle between the greater base and the lateral surface of the cone-frustum shaped
duct is preferably comprised between 50° and 70° and more preferably is in the region
of 60°.
[0012] The chamber (a), plenum chamber, is preferably of cylindrical shape.
[0013] The feeding duct, the convergent cone-frustum shaped duct and the constant-section
duct can be provided in a single metal block or in two or more metal blocks.
[0014] The diameter of the chamber (a) and the diameter of the constant-section-duct are
so selected as to obtain between the inlet of the constant-section duct and the chamber
(a) a drop of mixture pressure greater then 3 bar, more preferably of about 5 bar.
[0015] For simpleness' sake in equipment construction, it can be preferable to select the
diameter of the plenum chamber equal to the diameter of the feeding duct.
[0016] The equipment being the object of the present invention shall be now illustrated
with reference to hereto attached fig. 2 which represents an embodiment thereof, which
is not to be considered as a limitation of the invention.
[0017] The mixture of coal, oil and water (1) enters, delivered under pressure, the equipment,
runs through the feed ign duct (2), then through the convergent cone-frustum shaped
duct (3), subsequently at high speed through the duct of constant section (4), and
penetrates then into the chamber (5) [chamber (a)], called plenum chamber, of cylindrical
shape with movable adjustable bottom (6), go ing to collide with the same bottom of
said chamber.
[0018] Because of the collision of the mixture with the bottom of the chamber a fine suddivision
occurs of the components of the mixture, the homogenizing of the same mixture being
thus obtained. The mixture, after having been homogenized, passes from the plenum
chamber through a plurality of holes (7) uniformly distributed in the later al wall
(8) of said chamber into the discharge chamber (9) annular and coaxial to the said
plenum chamber and leaves (10) the device.
[0019] The discharge chamber is bounded by the outer wall of the plenum chamber and by a
cylindrical manifold (11). The feeding duct, the cone-frustum shaped duct and the
duct of constant section are made in two blocks (12) and (13).
[0020] The movable adjustable bottom allows the length and obviously the volume of the plenum
chamber to be varied above all on the basis of the flow rate and of the composition
of the mixture.
[0021] There is schematically shown with (14) a nut for the locking of the movable bottom
of the plenum chamDer, with (15) the angle comprised between the major base and the
lateral wall of the cone-frustum shaped duct.
[0022] An example is now reported having the purpose of illustrating the use of the equipment
which is the object of the invention.

[0023] The ground coal has been mixed first with an amount of water of about 22.2% by weight
relatively to the coal and then with heavy fuel oil; the mixture formed has been homogenized
by stabilization in the equipment described in fig. 2.
[0024] The most representative dimensions of the equipment are:

angle between the major base and the lateral wall of the cone-frustum shaped duct
60°
[0025] The diameter of the plenum chamber and the diameter of the constant-section duct
have been so selected, as to obtain a 5 bar drop in mixture pressure between the inlet
of the constant-section duct and the plenum chamber.
[0026] A stable mixture with the following composition has been obtained:

1. Static equipment for stabilizing mixtures of coal, oil and water, characterized
in that it comprises a feeding duct in communication with a duct of convergent cone-frustum
shape, which continues into a duct of consant section, leading to a chamber [chamber
(a)] whose transversal dimensions are greater than those of the constant-section duct,
wherein the chamber (a) has a volume which can be varied as required by means of a
movable adjustable bottom and is provided in its side wall with a set of holes, said
holes placing the chamber (a) in communication with a discharge chamber [chamber (b)]
annular and coaxial with the chamber (a).
2. Equipment according to claim 1, wherein the chamber (a) is a cylindrical chamber.
3. Equipment according to claim 1, wherein the feeding duct, the convergent cone-frustum
shaped duct and the constant-section duct are provided in a single metal block.
4. Equipment according to claim 1, wherein the feeding duct, the convergent cone-frustum
shaped duct and the constant-section duct are provided in two or more metal blocks.
5. Equipment according to claim 1, wherein the angle between the greater base of the
cone-frustum shaped duct and the lateral surface of said duct is comprised within
the range of from 50° and 70°.
6. Equipment according to claim 5, wherein the angle is in the region of 60°.
7. Equipment according to claim 2, wherein the diameter of the cylindrical chamber
(a) is equal to the diameter of the feeding duct.
8. Equipment as disclosed and represented.