U.S. patent application number 11/537124 was filed with the patent office on 2007-01-25 for apparatus for mixing two fluids or keeping them separate.
This patent application is currently assigned to Acrison, Inc.. Invention is credited to Marc S. Landry, Ronald J. Ricciardi.
Application Number | 20070017581 11/537124 |
Document ID | / |
Family ID | 29717850 |
Filed Date | 2007-01-25 |
United States Patent
Application |
20070017581 |
Kind Code |
A1 |
Ricciardi; Ronald J. ; et
al. |
January 25, 2007 |
Apparatus For Mixing Two Fluids Or Keeping Them Separate
Abstract
A mixing apparatus for mixing two fluids immediately following
contact with each other is disclosed. The mixing apparatus includes
a spring-loaded ball valve separating a first fluid from a second
fluid. The ball valve closes as a result of at least spring force.
The ball valve opens as a result of hydraulic pressure of one of
the fluids operating against the spring force. Mixing is
accomplished instantaneously by dispersing one fluid in a thin
pattern around the open ball valve into a stream of the other
fluid.
Inventors: |
Ricciardi; Ronald J.;
(Woodcliff Lake, NJ) ; Landry; Marc S.; (Vernon,
NJ) |
Correspondence
Address: |
Richard P. Ferrara;FISH & RICHARDSON P.C.
P.O. BOX 1022
MINNEAPOLIS
MN
55440-1022
US
|
Assignee: |
Acrison, Inc.
Moonachie
NJ
|
Family ID: |
29717850 |
Appl. No.: |
11/537124 |
Filed: |
September 29, 2006 |
Related U.S. Patent Documents
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Application
Number |
Filing Date |
Patent Number |
|
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11189205 |
Jul 25, 2005 |
7114523 |
|
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11537124 |
Sep 29, 2006 |
|
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|
10176901 |
Jun 21, 2002 |
6926030 |
|
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11189205 |
Jul 25, 2005 |
|
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Current U.S.
Class: |
137/605 |
Current CPC
Class: |
B01F 15/0201 20130101;
Y10T 137/87676 20150401; Y10T 137/87652 20150401; B01F 2215/0052
20130101; B01F 15/026 20130101; Y10T 137/8766 20150401; B01F 5/0077
20130101; B01F 15/0429 20130101; B01F 3/0865 20130101 |
Class at
Publication: |
137/605 |
International
Class: |
F16K 11/02 20060101
F16K011/02 |
Claims
1.-9. (canceled)
10. A method of forming a mixture of an aqueous fluid and a
reactive polymer composition comprising: passing an aqueous fluid
into a mixing assembly through a first inlet port in a first
direction; passing a reactive polymer composition into the mixing
assembly through a second inlet port in a second direction, the
second direction being orthogonal to the first direction, with a
force sufficient to open a pressure-actuated valve located at an
intersection of the first inlet port and the second inlet port;
forming a mixture of the aqueous fluid and the reactive polymer
composition at the intersection without forming a coagulation on
the pressure-actuated valve; and passing the mixture out of the
mixing assembly through an outlet port axially aligned with the
first inlet port.
11. The method of claim 10, wherein the first direction is
substantially horizontal and the second direction is substantially
vertical.
12. The method of claim 10, wherein the reactive polymer
composition flows at a rate in the range of from about a fraction
of a gallon per hour to about several hundred gallons per hour.
13. The method of claim 10, wherein the aqueous fluid flows at a
rate in the range of from about a fraction of a gallon per minute
to about several hundred gallons per minute.
14. The method of claim 10, wherein a pressure of about 30 pounds
per square inch is applied to the pressure-actuated valve.
15. The method of claim 11, wherein the reactive polymer
composition flows at a rate in the range of from about a fraction
of a gallon per hour to about several hundred gallons per hour.
16. The method of claim 11, wherein the aqueous fluid flows at a
rate in the range of from about a fraction of a gallon per minute
to about several hundred gallons per minute.
17. The method of claim 11, wherein a pressure of about 30 pounds
per square inch is applied to the pressure-actuated valve.
18. The method of claim 10, wherein the reactive polymer
composition flows at a rate in the range of from about a fraction
of a gallon per hour to about several hundred gallons per hour, the
aqueous fluid flows at a rate in the range of from about a fraction
of a gallon per minute to about several hundred gallons per minute
and a pressure of about 30 pounds per square inch is applied to the
pressure-actuated valve.
19. The method of claim 18, wherein the first direction is
substantially horizontal and the second direction is substantially
vertical.
Description
BACKGROUND OF THE INVENTION
[0001] This invention relates to an apparatus that can perform dual
functions of isolating and mixing two different fluids. The
apparatus can be used to dilute or pre-mix one fluid with another
and, when not in operation, completely isolates the two starting
fluids from each other.
[0002] Many processes require mixing two different fluids or
diluting one fluid with another. For example, liquid
polyelectrolytes (polymers) used in various water treatment and
wastewater treatment processes must be diluted with water to create
solutions having small concentrations, say, up to approximately 10%
polymer, by weight or volume. Due to the large amount of water
required to achieve this level of dilution, it is usually more cost
effective to transport the polymer ingredient to the site and to
dilute it with water already available at the site.
[0003] The polymers to be diluted can be compositions such as
polyelectrolytes, for example. Proper mixing of liquid polymers
with water is not always easy. Most polymers can activate very
quickly once they come into contact with water or aqueous
compositions, and can form a highly viscous and sticky
agglomeration if not promptly and thoroughly mixed with an
appropriate amount of water. A positive means of mixing must be
implemented to dilute the polymer effectively. The viscosity of a
particular solution can vary in direct proportion to the percentage
of polymer in the solution. In other words, as the percentage of
polymer in the solution is increased, the viscosity of the solution
is also increased, and vice versa. Inadequate or slow mixing of the
liquid polymer with the water can result in excessive and
undesirable coagulation of the mixture and consequent clogging or
obstruction of system piping and components. Clogging can be so
significant that a system might be rendered inoperable until it is
cleaned and the obstruction is cleared.
SUMMARY OF THE INVENTION
[0004] The apparatus of the invention provides a positive seal to
avoid completely any possibility of polymer leakage into any part
of a water or aqueous solution line whenever the polymer metering
pump is not pumping or the system is otherwise idle. As has been
noted above, to allow liquid polymer to come into contact with
water or an aqueous solution when such is not desired will activate
the polymer and thus cause extensive coagulation of the polymer,
which will thus foul and clog the components and piping of the
apparatus.
[0005] The present invention provides apparatus and a technique for
blending and/or isolating two fluids. Although this technique has
wide application to a number of mixing protocols, it is
particularly useful for mixing liquid polymers and water to create
solutions commonly used in water treatment and wastewater treatment
processes.
[0006] According to an aspect of the invention, when in use, water
can be continuously directed into one end of a mixing assembly. In
the central section of the mixing assembly, liquid polymer enters
the water stream by the exertion of hydraulic pressure in the
polymer supply line that overcomes the seal formed by a
spring-loaded ball. The polymer supply line pressure, generated by
a polymer feed pump, overcomes the force holding the ball in
sealing engagement with a valve seat and forces the ball off the
valve seat, thus allowing the polymer to flow between the valve
seat and the ball in the shape of a thin, cone-shaped stream as it
begins passing around the ball. The polymer will then disperse
rapidly into the vigorously flowing water stream which is passing
tangentially through the vicinity of the valve. This technique
produces easy and instantaneous blending of the liquid polymer and
water, allowing the thusly formed mixture to exit the mixing
assembly as a "pre-blended solution."
[0007] The mixing assembly of the invention improves the overall
polymer dilution process by providing a pre-blended solution of
polymer and water, sufficient to avoid unwanted coagulation, before
the mixture thus formed enters a downstream primary mixing or
activation mechanism for more thorough mixing. The mixing assembly
of the invention thus provides immediate "pre-blending" or
"pre-mixing" of the two fluids as soon as they come into contact
with each other. This immediate pre-mixing is important in
applications where the fluids react with each other rapidly to
produce highly viscous solutions.
[0008] Equally important, during periods of time when the system is
idle, the mixing assembly of the invention completely seals off one
fluid from the other fluid, thus preventing any leakage and
inadvertent contact that could result in coagulation and system
clogging or fouling.
[0009] In a typical system, a metering pump controls the amount and
flow of polymer delivered to the mixing assembly and a water
regulator or pump typically controls the flow of water into the
mixing assembly, as measured, for example, by a rotameter or a flow
meter. Thus, the desired ratio of polymer to water can be easily
maintained by controlling the polymer metering pump and the water
supply, either manually or automatically, in known ways.
[0010] The details of one or more embodiments of the invention are
set forth in the accompanying drawings and the description below.
Other features, objects, and advantages of the invention will be
apparent from the description, drawings and claims.
BRIEF DESCRIPTION OF THE DRAWINGS
[0011] FIG. 1 is a schematic representation of a mixing system
according to the invention.
[0012] FIG. 2 is a sectional elevation view of a mixing assembly
according to the invention.
DETAILED DESCRIPTION
[0013] In the particular system of FIG. 1, water regulator or pump
10 supplies water from water source 22 at a constant, but
adjustable rate. The water flows through rotameter or flow meter
12, throttling valve 11 for flow control, and then into water inlet
port 104 of mixing assembly 100. The rotameter or flow meter 12
measures the water flow rate and the throttling valve 11 permits
flow control of the water source 22 either manually or
automatically, in ways known to those of ordinary skill in the art.
Polymer metering pump 14 pumps, under pressure, a predetermined
quantity of liquid polymer from liquid polymer source 16 to polymer
inlet port 102 of mixing assembly 100. The liquid polymer is
injected with force into a turbulent water stream, thus forming a
pre-blended solution of the fluids in mixing assembly 100. This
polymer/water mixture then moves toward mixture (or polymer
solution) outlet port 106 from the vicinity of ball 108 (FIG. 2).
Further mixing occurs here due to the flow turbulence of the water
stream. The liquid polymer/water mixture exits mixing assembly 100
through mixture outlet port 106. The mixture then flows into
primary mixing device 20 downstream of mixing assembly 100 where
thorough mixing and final polymer activation occurs.
[0014] Referring to FIG. 2, water flows into mixing assembly 100 at
water inlet port 104. As shown, liquid polymer can enter the mixing
assembly at the polymer inlet port 102 and around ball 108 when the
device is in operation. When the device is not in operation, ball
108 mates with valve seat 112 as a result of at least the seating
force imparted by spring 110. Spring 110 is situated between ball
108 and recessed area 128 on the inside surface of injector housing
114. Ball 108 provides a liquid tight seal against valve seat 112
when they are mated. Polymer metering pump 14 is designed to
provide a polymer pressure great enough to overcome the force of
spring 110. This pressure forces ball 108 off valve seat 112, thus
allowing liquid polymer to flow around ball 108 and disperse into
the flowing water passing by ball 108 in a fine, thin conical
stream. This liquid polymer stream instantaneously blends with the
water flowing past ball 108 toward mixture outlet port 106. The
mixture then exits the mixing assembly 100 through the mixture
outlet port 106.
[0015] Valve-securing member 116 holds valve seat 112 in place.
Securing hardware 118 attaches valve-securing member 116 to
injector housing 114. In the drawing, pipe-mating member 130 is
integral with valve-securing member 116. Pipe-mating member 130 has
threads which co-act with threads on union 120 to allow easy
connection of mixing assembly 100 to polymer supply line 134.
O-ring 126 is provided to prevent liquid polymer from leaking where
polymer supply line 134 meets mixing assembly 100. O-ring 124 is
also provided to prevent leakage of liquid polymer between valve
seat 112 and valve-securing member 116. Another O-ring 122 is
provided to prevent leakage of liquid polymer between injector
housing 114 and valve seat 112. Alternates to the O-rings and
securing hardware 118 can, of course, be implemented in place of
the specific features described above, as will be readily apparent
to those of ordinary skill in the art.
[0016] Mixing assembly 100 can generally, but need not, be
configured as shown in FIG. 1 and FIG. 2, with the liquid polymer
entering mixing assembly 100 from below. Such a configuration is
desirable because gravity would then assist spring 110 with seating
ball 108 on valve seat 112. Other orientations or configurations
can, of course, be used as alternatives without departing from the
spirit and scope of the invention.
[0017] In a typical system, polymer metering pump 14 is capable of
producing a pressure ranging from approximately 50 to approximately
150 pounds per square inch and the ball 108 and spring 110
arrangement is designed to unseat at a liquid polymer pressure of
approximately 30 pounds per square inch. This unseating pressure
can be adjusted by using alternative pumps and/or springs having
different physical and operational characteristics, as will be
readily apparent to those of ordinary skill.
[0018] Because certain liquid polymers have been found to be
somewhat corrosive, spring 110 is made of various metallic
materials and then coated with a protective material to enhance its
ability to resist corrosion. Such protective materials can
typically be plastic, rubber or other synthetic or synergistic type
coatings. Ball 108 can be made of various metallic materials,
ceramic, or synthetic materials. If made of stainless steel, ball
108 can be coated with a protective material to enhance its
resistance to corrosion. Such protective materials can typically be
plastic, rubber or other synthetic or synergistic type coatings.
Valve seat 112 can be made of, or can comprise, a more pliable
synthetic material than ball 108 comprises. The combination of a
harder ball 108 with a softer, more pliable valve seat 112 provides
an excellent seal for preventing inadvertent leakage of liquid
polymer into the water stream, or vice versa. This excellent seal
is achieved because a more pliable valve seat 112 can conform to
ball 108. Of course, as will be readily appreciated by one of
ordinary skill, ball 108 can comprise the more pliable material,
with valve seat 112 being made of a harder material to provide
excellent sealing capability.
[0019] Other parts of the mixing assembly 100 may be constructed
using synthetic materials, such as acrylic, polycarbonate and
polyvinylchloride (PVC), as well as stainless steel. Various
components such as injector housing 114 and valve-securing member
116 may be made of transparent or translucent material, if desired,
to allow visual observation of the operation of mixing assembly
100.
[0020] Mixing assembly 100 can be designed for handling a wide
range of water flow rates typically from a fraction of a gallon per
minute up to several hundred gallons per minute. Mixing assembly
100 can also be designed to handle a wide range of polymer flow
rates ranging typically from a fraction of a gallon per hour, up to
several hundred gallons per hour. In a typical system, a rotameter
or flow meter 12 is used to measure the water flow rate and a
metering pump 14 is used to set the liquid polymer flow rate.
Adjusting these parameters sets the desired ratio of polymer to
water. This can be done either manually or automatically, as will
be readily apparent to one of ordinary skill. Useful solutions of
liquid polymers in various water treatment or wastewater treatment
processes can have concentrations, say, from approximately 0.25%
polymer by weight or volume up to, say, approximately 10% polymer
by weight or volume. As will be appreciated, these percentages can
vary beyond the stated amounts.
[0021] A number of embodiments and variations of the invention have
been described. Nevertheless, it will be understood that various
modifications can be made without departing from the spirit and
scope of the invention. For example, the techniques disclosed
herein can be used to mix fluids other than those specifically
disclosed herein. Additionally, other materials may be used to form
the different components described herein. Accordingly, other
embodiments are within the scope and spirit of the invention and
the following claims.
* * * * *