WO1990014152A1 - Improved mixing nozzle apparatus and method of use - Google Patents

Improved mixing nozzle apparatus and method of use Download PDF

Info

Publication number
WO1990014152A1
WO1990014152A1 PCT/US1990/002645 US9002645W WO9014152A1 WO 1990014152 A1 WO1990014152 A1 WO 1990014152A1 US 9002645 W US9002645 W US 9002645W WO 9014152 A1 WO9014152 A1 WO 9014152A1
Authority
WO
WIPO (PCT)
Prior art keywords
constituents
film forming
forming chamber
inlets
pump means
Prior art date
Application number
PCT/US1990/002645
Other languages
French (fr)
Inventor
John Orava
Original Assignee
John Orava
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by John Orava filed Critical John Orava
Publication of WO1990014152A1 publication Critical patent/WO1990014152A1/en

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F33/00Other mixers; Mixing plants; Combinations of mixers
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/40Static mixers
    • B01F25/46Homogenising or emulsifying nozzles

Definitions

  • This invention relates generally to mixing nozzle apparatus and methods of
  • under pressure are regulated either by a variable orifice or a selective orifice with
  • variable pumping velocities at the inlets In that foam making equipment, the
  • ratio of the chemical constituents is accordingly controlled by selective adjustment
  • variable orifices or by control of the pumping rate.
  • pumping rate An example of such
  • prior mixing apparatus includes a mixing chamber into which the chemical constituents are sprayed under high pressure. Within the chamber the streams are
  • a nozzle assembly including an outer cylindrical
  • selection member openings may be selectively aligned with the casing
  • the internal portion of the cylindrical selection member functions as a film
  • Air under pressure is periodically injected through a first inlet to clear
  • Methods of use include programming the pumping control to change the ratio of chemical constituents in response to encountered conditions.
  • the foaming reaction can be timed to occur only
  • the density may be varied over time or in response to mold conditions to give a desired
  • Figure 1 is a front view of the preferred embodiment of the present invention
  • Figure 2 is a front view of the disassembled nozzle apparatus of Figure 1
  • Figure 3 depicts the movement of a chemical constituent pumped through an
  • FIGS. 4a-4d represent a sequential operation of the nozzle apparatus
  • present invention is shown having multiple inlets 14, 16, 18, 20 and 21 with
  • the computer may comprise well known microprocessor technology which is programmable to provide timed pulses on data output ports.
  • pulses may be amplified and used to drive the pumps. Air and chemical
  • the nozzle is formed of a hollow cylindrical casing member 32 having an
  • internal inlet selection member 36 is provided within the casing and is generally
  • a threaded coupling 40 is arranged at its other extremity to mate with the
  • air is provided to this inlet and this inlet may be selected in conjunction with other
  • openings and the selection member to slideably provide the selection.
  • pressurized air is injected to scrub out the chemicals, cleaning the chamber,
  • the number of pulses and frequency is controlled by a programmable
  • the injected stream then circulates within the chamber to form a film
  • nozzle is kept free of reacting chemicals and difficult cleaning is avoided.
  • the chemical constituents are pumped by computer controlled digital pumps. Pumps of this type are described in my co-
  • Foam producing chemicals typically involve two or more components, the ratio
  • time can be controlled in a dynamic fashion, changing during operation under computer control in response to programming.
  • the controlling computer controls the mold to produce a skinned foam product.
  • the characteristics of the resulting product varies with the mold conditions and the mixture of chemical constituents.
  • the foam is used as insulation.
  • Wall cavities are typically filled by drilling holes spaced along the vertical dimension of the wall. Starting from the bottom, the
  • foam is injected through the holes, progressing from the bottom to the top.
  • the computer is programmed to vary the signals to the pumps and

Abstract

Generally there is provided a nozzle assembly (12) including an outer cylindrical casing member (32) and an inner cylindrical selection member (36). Inlets (14, 16, 18, 20, 21) are provided along the casing (32) and corresponding openings (50, 52, 54, 56, 57) are provided in the selection member (36) such that they may be selectively aligned with the casing inlets (14, 16, 18, 20, 21). The internal portion of the cylindrical selection member (36) functions as a film forming chamber where films (82, 86) are developed on the surface for mixing contact. Programmable pulsing pumps connected to the inlets (14, 16, 18, 20, 21) are sequentially operated to inject constituents into the mixing chamber in the desired order and quantity. Air pressure is periodically injected to clear the chamber of mixed constituents. With this programmable apparatus foam density and reaction time are variable during operation.

Description

IMPROVED MIXING NOZZLE APPARATUS AND METHOD OF USE
BACKGROUND OF THE INVENTION
Field of the Invention
This invention relates generally to mixing nozzle apparatus and methods of
use; and particularly to such nozzle apparatus for use with equipment in the
manufacture of foam. A typical application of such equipment being in the
insulation and packaging fields.
Description of the Prior Art
Chemical mixing for the foam machine industry has previously been accomplished by use of well known variable orifice valves used to control flow
rate in combination with mechanical mixing techniques. In such systems chemicals
under pressure are regulated either by a variable orifice or a selective orifice with
variable pumping velocities at the inlets. In that foam making equipment, the
ratio of the chemical constituents is accordingly controlled by selective adjustment
of the variable orifices or by control of the pumping rate. An example of such
prior mixing apparatus includes a mixing chamber into which the chemical constituents are sprayed under high pressure. Within the chamber the streams are
caused to impinge on obstructions to cause mixing, or in an alternative system a
mechanical device stirs the chemicals to cause the mixing. These devices result
in nozzle apparatus which is difficult to clean and within which reacted constituents collect to clog the nozzle. In addition to the high maintenance required, these devices generally require high pumping pressure to operate efficiently, and this pressure is dangerous and expensive to generate.
SUMMARY OF THE INVENTION
It is therefore a principal objective of the present invention to provide a
mixing apparatus which yields increased accuracy, increased control and improved mixing efficiency.
It is a further object to provide a mixing apparatus which is easy to clean and maintain, and to provide apparatus that is operable at a safe low pressure.
It is yet a further object of the present invention to provide a mixing
apparatus that is computer controllable, and which provides improved methods
of use with foam construction techniques.
Generally there is provided a nozzle assembly including an outer cylindrical
casing member and an inner cylindrical selection member. Inlets are provided along the casing and corresponding openings are provided in the selection member
such that the selection member openings may be selectively aligned with the casing
inlets. The internal portion of the cylindrical selection member functions as a film
forming chamber where films are developed on the inner surface for mixing
contact. Programmable pulsing pumps connected to the inlets are sequentially
operated to inject constituents into the mixing chamber in the desired order and
quantity. Air under pressure is periodically injected through a first inlet to clear
the chamber of the constituents. Methods of use include programming the pumping control to change the ratio of chemical constituents in response to encountered conditions. When used to
produce a foam product the programming would control the component ratios to
vary the density of the finished product or the time required for the chemicals to
react to create the foam. In use, the foaming reaction can be timed to occur only
after the chemicals are ejected and in the desired location. Moreover, the density may be varied over time or in response to mold conditions to give a desired
surface skin on a molded foam product.
BRIEF DESCRIPTION OF THE DRAWINGS
Figure 1 is a front view of the preferred embodiment of the present invention
showing the nozzle apparatus having a plurality of inlets for air and chemicals with
pulsing pumps connected thereto.
Figure 2 is a front view of the disassembled nozzle apparatus of Figure 1
showing the internal selection member.
Figure 3 depicts the movement of a chemical constituent pumped through an
inlet into the chamber. Figures 4a-4d represent a sequential operation of the nozzle apparatus
whereby first and second films are developed within the chamber and then
scrubbed out by an air jet.
While the invention will be described in connection with a preferred
embodiment, it will be understood that I do not intend to limit the invention to
that embodiment. On the contrary, I intend to cover all alternatives,
modifications, and equivalents as may be included within the spirit and scope of
the invention as defined by the appended claims.
DESCRIPTION OF THE PREFERRED EMBODIMENT
Turning first to Figure 1, the nozzle apparatus 12 in accordance with the
present invention is shown having multiple inlets 14, 16, 18, 20 and 21 with
computer controlled pulsing pumps 22, 24, 26, 28 and 29 coupled thereto,
respectively. The computer (not shown) may comprise well known microprocessor technology which is programmable to provide timed pulses on data output ports.
These pulses may be amplified and used to drive the pumps. Air and chemical
constituents (see Figure 4a-4b) are injected into these inlets and the resultant
mixed product is ejected from the nozzle outlet 30.
The nozzle is formed of a hollow cylindrical casing member 32 having an
external thread attachment 34 at one end thereof. Its other extremity is generally
closed with the outlet 30 provided therethrough. In the preferred embodiment an
internal inlet selection member 36 is provided within the casing and is generally
of a hollow cylindrical design open at one extremity 38 to correspond to the nozzle
outlet. A threaded coupling 40 is arranged at its other extremity to mate with the
threaded end 34 of the casing to provide a tight seal thereto. The selection
member functions principally to seal the inlets when the inlet (or the entire
nozzle) is not in use. In the broad application of this nozzle, the basic function
is obtained with the casing alone, the inlets being controlled by the pumps.
Along the selection member there is provided patterns of inlet openings
arranged in series and circumferentially distributed around the selection member. In the location surrounding the selection member at the first inlet there is
provided a first series 50 of openings. In the preferred embodiment, air is provided to this inlet and this inlet may be selected in conjunction with other
combinations of inlets, or alone, by aligning the selection member to allow flow
from the selected inlets and closing off all others. Similarly, at the location on the
selection member corresponding to the second inlet, there is provided a second
series 52 of one or more openings. Third, fourth and fifth circumferentally
arranged series of openings 54, 56 and 57 are provided to control the third, fourth
and fifth inlets in the same manner. While the selection member is arranged to
rotatively provide selection, it is within the scope of the invention to arrange the
openings and the selection member to slideably provide the selection.
Operation of the nozzle apparatus of the present invention is illustrated in
Figure 3 and Figures 4a-4d. When a chemical constituent 60 is pumped through
an inlet 62 it passes through the opening 64 in the selection member 66 and
circulates within the cylindrical cavity 70. During the circulation a thin film is
caused to develop on the interior surface. Subsequent injection of a second
chemical constituent creates a second overlying thin film and thereby yielding a
high surface contact between the chemicals. Similarly, additional constituents may
be injected and layered in the chamber. Once the films have been developed, pressurized air is injected to scrub out the chemicals, cleaning the chamber,
ejecting the chemicals and causing further mixing of the constituents.
The operational process is depicted in Figures 4a-4d. Figure 4a shows the
chamber being scrubbed with air injected through the first opening 14. This air
stream is forced into the chamber by a selectively operated (programmable)
pulsing pump and the stream is caused to impinge on the chamber wall to set up
a turbulent flow which propagates down the tube to the exit orifice. In Figure 4b the first of the chemical constituents 80 is injected to the film forming chamber. The stream of chemical is selectively forced through the opening by a pulsing
pump. (The number of pulses and frequency is controlled by a programmable
computer.) The injected stream then circulates within the chamber to form a film
82 on the interior surface. Turning to Figure 4c the second chemical constituent
84 is similarly injected to form a second overlying film 86. Following the
development of the second film, additional films may likewise be developed by
injection through the remaining openings. When all required constituents have been injected, an air burst (Figure 4d) is again directed into opening 14 to expel
the films and to cause further intermixing. In this fashion, the interior of the
nozzle is kept free of reacting chemicals and difficult cleaning is avoided.
In the preferred embodiment the chemical constituents are pumped by computer controlled digital pumps. Pumps of this type are described in my co-
pending application, Serial No. 273,590. Under computer control, pump selection and pumping rate is selectively controllable, allowing an operator to program the
desired sequence and quantity of chemical constituents delivered.
Foam producing chemicals typically involve two or more components, the ratio
of which vary the density of the foam product and the time required for the
reaction that produces the foam product. Accordingly, the density and foaming
time can be controlled in a dynamic fashion, changing during operation under computer control in response to programming.
This programmability has been used in two major innovative methods.
Previously it has been the practice to inject a foam producing mixture into a cold
mold to produce a skinned foam product. In such system, the characteristics of the resulting product varies with the mold conditions and the mixture of chemical constituents. In accordance with the present invention, the controlling computer
is programmed to vary the chemical ratios during operation to affect the density.
Initially a mixture is used which generates a higher density foam. When this is
injected it covers the mold surface to form the skin. After a sufficient quantity
is injected the computer alters the ratio to produce a lower density foam for the
interior. This change is accomplished by varying the computer controlled pulse
signals to the pumps during the mold filling process.
Another appplication has been developed in the construction industry where
the foam is used as insulation. Wall cavities are typically filled by drilling holes spaced along the vertical dimension of the wall. Starting from the bottom, the
foam is injected through the holes, progressing from the bottom to the top. With the apparatus of the present invention only one top hole is drilled (and only one
hole needs to be patched) and the foam is injected into the cavity through this
hole. The computer is programmed to vary the signals to the pumps and
therefore the chemical ratios to control the time required for the foam to react
and set. This allows the mixture of chemicals time to flow to the bottom of the
cavity at the beginning; but during the injection process, the mixture is changed
to gradually shorten the setup time as the cavity is filled. From the foregoing description, it will be apparent that modifications can be made to the apparatus and method for using same without departing from the teachings of the present invention. Accordingly, the scope of the invention is only
to be limited as necessitated by the accompanying claims.

Claims

CLAIMSI claim:
1. A fluid mixing nozzle apparatus comprising: a cylindrical casing member having a plurality of inlets defined thereon, an
outlet defined on one end thereof, and a film forming chamber defined
therein; and
pump means for selectively providing bursts of fluid chemical constituents and
air under pressure into said inlets, such that said constituents form
juxtaposed thin film layers within said film forming chamber and said
air burst scrubs said juxtaposed layers of constituents from said film
forming chamber to produce bursts of mixed constituents.
2. The fluid mixing nozzle of Claim 1 wherein said pump means is controlled to
inject said chemical constituents sequentially into said film forming chamber
and to inject said air following said chemical injection to further mix and eject
said chemicals.
3. The fluid mixing nozzle of Claim 2 wherein said chemical constituents
comprise foam producing components and said pump means is programmable.
4. A method of mixing fluids comprising:
connecting a plurality of chemical constituents and an air supply to a plurality
of pulsing pump means; connecting each of said pulsing pump means to the inlets of a nozzle having
a plurality of inlets thereto, said nozzle having a film forming chamber therein and an outlet therefrom;
sequentially pumping bursts of said constituents into said film forming chamber
such that said constituents form juxtaposed thin film layers within said
film forming chamber; and
pumping bursts of air into said film forming chamber to scrub said juxtaposed
layers of constituents from said film forming chamber to produce bursts of mixed constituents.
5. The method of mixing fluids of Claim 4 wherein said chemical constituents
comprise foam producing components and said pump means is programmable.
PCT/US1990/002645 1989-05-15 1990-05-10 Improved mixing nozzle apparatus and method of use WO1990014152A1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US35148089A 1989-05-15 1989-05-15
US351,480 1989-05-15

Publications (1)

Publication Number Publication Date
WO1990014152A1 true WO1990014152A1 (en) 1990-11-29

Family

ID=23381108

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/US1990/002645 WO1990014152A1 (en) 1989-05-15 1990-05-10 Improved mixing nozzle apparatus and method of use

Country Status (3)

Country Link
AU (1) AU5631690A (en)
CA (1) CA2016722A1 (en)
WO (1) WO1990014152A1 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20110259971A1 (en) * 2007-12-20 2011-10-27 Askin Steven R Fluid injection assembly for nozzles
US20120205098A1 (en) * 2011-02-14 2012-08-16 TEC artec valves GmbH & Co., KG Equipment feeding polymers into a fluid flow
RU174710U1 (en) * 2017-04-20 2017-10-30 Федеральное государственное бюджетное образовательное учреждение высшего образования "Самарский государственный университет путей сообщения" (СамГУПС) Mixing device

Citations (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2962193A (en) * 1957-12-06 1960-11-29 Trilex Engineering Inc Liquid dispensing device
US3102004A (en) * 1959-08-05 1963-08-27 Grintz Joseph John Mixing and dispensing apparatus
US3377139A (en) * 1963-06-21 1968-04-09 Allied Chem Apparatus for preparing low density urea-formaldehyde foams
US3450388A (en) * 1968-03-12 1969-06-17 Gen Motors Corp Mixer with flushing valve in the outlet
US3541023A (en) * 1963-03-11 1970-11-17 Olin Corp Portable foaming system
US3892389A (en) * 1972-11-29 1975-07-01 Bekaert Sa Nv Device and method for injecting liquids into a mixing head
US4204612A (en) * 1978-05-11 1980-05-27 Foam Controls Inc. System for applying foam insulation
US4209258A (en) * 1978-02-14 1980-06-24 Oakes W Peter Automatic continuous mixer apparatus
US4213936A (en) * 1978-08-09 1980-07-22 Robert Lodrick Foam generating and spraying apparatus
US4260355A (en) * 1979-01-13 1981-04-07 Maschinenfabrik Hennecke Gmbh Device for the discontinuous production of block foam
US4341327A (en) * 1980-02-28 1982-07-27 Vernon Zeitz Digital proportional metering pumping system
US4438072A (en) * 1982-02-22 1984-03-20 Freeman Chemical Corporation Continuous stream mixer having variable dwell time chamber with auger
US4458827A (en) * 1980-05-13 1984-07-10 Gebruder Lodige Maschinenbau-Gesellschaft mit beschrankter Haftung Method to meter adhesive for adhesively coating chips, fibers and the like for the manufacture of composite panels, as well as apparatus to carry out the method
US4493286A (en) * 1983-07-25 1985-01-15 Koppers Company, Inc. Method and apparatus for applying a multi-component adhesive
US4647212A (en) * 1986-03-11 1987-03-03 Act Laboratories, Inc. Continuous, static mixing apparatus
US4691850A (en) * 1984-08-09 1987-09-08 Kirschmann John D Chemical dispensing system

Patent Citations (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2962193A (en) * 1957-12-06 1960-11-29 Trilex Engineering Inc Liquid dispensing device
US3102004A (en) * 1959-08-05 1963-08-27 Grintz Joseph John Mixing and dispensing apparatus
US3541023A (en) * 1963-03-11 1970-11-17 Olin Corp Portable foaming system
US3377139A (en) * 1963-06-21 1968-04-09 Allied Chem Apparatus for preparing low density urea-formaldehyde foams
US3450388A (en) * 1968-03-12 1969-06-17 Gen Motors Corp Mixer with flushing valve in the outlet
US3892389A (en) * 1972-11-29 1975-07-01 Bekaert Sa Nv Device and method for injecting liquids into a mixing head
US4209258A (en) * 1978-02-14 1980-06-24 Oakes W Peter Automatic continuous mixer apparatus
US4204612A (en) * 1978-05-11 1980-05-27 Foam Controls Inc. System for applying foam insulation
US4213936A (en) * 1978-08-09 1980-07-22 Robert Lodrick Foam generating and spraying apparatus
US4260355A (en) * 1979-01-13 1981-04-07 Maschinenfabrik Hennecke Gmbh Device for the discontinuous production of block foam
US4341327A (en) * 1980-02-28 1982-07-27 Vernon Zeitz Digital proportional metering pumping system
US4458827A (en) * 1980-05-13 1984-07-10 Gebruder Lodige Maschinenbau-Gesellschaft mit beschrankter Haftung Method to meter adhesive for adhesively coating chips, fibers and the like for the manufacture of composite panels, as well as apparatus to carry out the method
US4438072A (en) * 1982-02-22 1984-03-20 Freeman Chemical Corporation Continuous stream mixer having variable dwell time chamber with auger
US4493286A (en) * 1983-07-25 1985-01-15 Koppers Company, Inc. Method and apparatus for applying a multi-component adhesive
US4691850A (en) * 1984-08-09 1987-09-08 Kirschmann John D Chemical dispensing system
US4647212A (en) * 1986-03-11 1987-03-03 Act Laboratories, Inc. Continuous, static mixing apparatus

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20110259971A1 (en) * 2007-12-20 2011-10-27 Askin Steven R Fluid injection assembly for nozzles
US8568018B2 (en) * 2007-12-20 2013-10-29 Rave N.P., Inc. Fluid injection assembly for nozzles
US20120205098A1 (en) * 2011-02-14 2012-08-16 TEC artec valves GmbH & Co., KG Equipment feeding polymers into a fluid flow
RU174710U1 (en) * 2017-04-20 2017-10-30 Федеральное государственное бюджетное образовательное учреждение высшего образования "Самарский государственный университет путей сообщения" (СамГУПС) Mixing device

Also Published As

Publication number Publication date
AU5631690A (en) 1990-12-18
CA2016722A1 (en) 1990-11-15

Similar Documents

Publication Publication Date Title
US4749554A (en) Nozzle for mixing flowable reaction components
US4285446A (en) Automatic purging system having a pressure sensor and a timing mechanism
US4141470A (en) Mixing head for mixing at least two reactive components
US3892389A (en) Device and method for injecting liquids into a mixing head
US6264113B1 (en) Fluid spraying system
EP0740987B1 (en) Solvent flush reaction injection molding mixhead
US2857144A (en) Mixing device
US5887975A (en) Multiple component in-line paint mixing system
US4175874A (en) High pressure injection mixing head for multi-component plastics, particularly polyurethane
US6435854B1 (en) Apparatus for mixing and injection molding thermosetting polyurethane
EP0063707A1 (en) Plural component spray gun
WO1990014152A1 (en) Improved mixing nozzle apparatus and method of use
RU2374005C2 (en) Coaxial supply system
US7306119B2 (en) Dispensing material produced by a chemical reaction
US6814110B2 (en) Method of and apparatus for improved pressurized fluid dispensing for the guaranteed filling of cavities and/or the generating of guaranteed uniform gasket beads and the like
US6227228B1 (en) Purge process for sequential plural component mixing system
JP2709425B2 (en) Urethane foam resin mixing equipment
JP2009233631A (en) Mixing device of paint feeding device for multi-liquid coating
JP2004154643A (en) Multi-liquid mixing apparatus, and multi-liquid mixing method
JP5838014B2 (en) Fluid mixing device
JPS633727B2 (en)
SU549938A1 (en) Gun-mixer for manufacturing foam plastics
JPS582813B2 (en) Polyurethane foam
JPS63143930A (en) Adjustment of setting for mixing ratio of liquids, mixture discharge of ejection method and device thereof
CN117505112A (en) Dispenser with air mixing

Legal Events

Date Code Title Description
AK Designated states

Kind code of ref document: A1

Designated state(s): AT AU BB BG BR CH DE DK ES FI GB HU JP KP KR LK LU MC MG MW NL NO RO SD SE SU

AL Designated countries for regional patents

Kind code of ref document: A1

Designated state(s): AT BE BF BJ CF CG CH CM DE DK ES FR GA GB IT LU ML MR NL SE SN TD TG

REG Reference to national code

Ref country code: DE

Ref legal event code: 8642