Method and apparatus for compensating for changes in viscosity in a two-component dispensing system

• US 5,271,521 A
• Filed: 11/23/1992
• Issued: 12/21/1993
• Est. Priority Date: 01/11/1991
• Status: Expired due to Fees

• Current Assignee: Nordson Corporation
• Original Assignee: Nordson Corporation
• Inventors: Schmitkons, James W., Price, Richard P., Noss, Jeffrey S.
• Primary Examiner(s): Bollinger, David H.
• Application Number:
  US07/980,543
• Time in Patent Office: 393 Days
• Field of Search: 222/135, 222/145, 222/129, 222/63, 222/55, 222/54, 222/52, 222/146.2, 222/146.5, 222/1
• US Class Current: 222/1
• CPC Class Codes: B01F 23/40 Mixing liquids with liquids; Emulsifying
• CPC Class Codes: B01F 25/43141 composed of consecutive sections of helical formed elements
• CPC Class Codes: B01F 35/1452 using fluids
• CPC Class Codes: B01F 35/2113 Pressure
• CPC Class Codes: B01F 35/2115 Temperature
• CPC Class Codes: B01F 35/882 using measuring chambers, e.g. volumetric pumps, for feeding the substances
• CPC Class Codes: B08B 7/02 by distortion, beating, or vibration of the surface to be cleaned B08B7/0007 takes precedence
• CPC Class Codes: B08B 9/08 Cleaning containers, e.g. tanks
• CPC Class Codes: B29B 7/325 Static mixers in general B01F25/42
• CPC Class Codes: B29B 7/726 Measuring properties of mixture, e.g. temperature or density B29B7/724 takes precedence
• CPC Class Codes: B29B 7/728 Measuring data of the driving system, e.g. torque, speed, power, vibration B29B7/724 takes precedence
• CPC Class Codes: B29B 7/7419 with static or injector mixer elements
• CPC Class Codes: B29B 7/7433 Plants
• CPC Class Codes: B29B 7/7605 having additional mixing arrangements B29B7/7673 takes precedence
• CPC Class Codes: B29B 7/7615 characterised by arrangements for controlling, measuring or regulating, e.g. for feeding or proportioning the components
• CPC Class Codes: B29B 7/826 Apparatus therefor
• CPC Class Codes: B29C 48/022 characterised by the choice of material
• CPC Class Codes: B29C 48/03 characterised by the shape of the extruded material at extrusion
• CPC Class Codes: B29K 2105/0097 Glues or adhesives, e.g. hot melts or thermofusible adhesives
• CPC Class Codes: G05D 11/132 by controlling the flow of the individual components G05D11/133 takes precedence

Abstract

A two-component mixing and dispensing system for mixing and dispensing two-component polymeric materials which react chemically with one another when combined to form a mixture includes a controller for adjusting the pressure at which at least one of the components is supplied to a dispenser dependent upon variations in the parameters which affect the cure time of the mixture.

Claims

1. A mixing and dispensing system for mixing and dispensing at least two different polymeric materials which react chemically with one another when combined, said system comprising:

a dispenser having a plurality of liquid flow inlets and an outlet;

first and second pump means for supplying a different liquid polymeric material under pressure to each of said liquid flow inlets of said dispenser, the liquid polymeric materials being combined with one another within said dispenser to form a mixture;

control means for adjusting the pressure at which at least one of said liquid polymeric materials is supplied to said inlets of said dispenser, when the flow of said materials through said dispenser is terminated, as a function of a change in the viscosity of the mixture of said liquid materials within said dispenser, said control means including a bypass flow path around at least one of said first and second pump means and an adjustable pressure regulator means for regulating the pressure in said bypass flow path.

2. The apparatus of claim 1 in which said first pump means includes a first pumping unit adapted to connect to a source of one liquid polymeric material and to one of said inlets of said dispenser, and said second pump means includes a second pumping unit adapted to connect to a source of a different liquid polymeric material and to another one of said inlets of said dispenser.

3. The apparatus of claim 2 in which said

adjustable pressure regulator means is connected between at least one of said first and second pumping units and said dispenser, for regulating the pressure at which at least one of said liquid polymeric materials is supplied to said dispenser;

means for adjusting said pressure regulator means to very the pressure at which said at least one liquid polymeric material is supplied to said dispenser dependent on changes in the viscosity of the mixture formed within said dispenser.

4. The apparatus of claim 3 in which said means for adjusting said pressure regulator means includes at least one of the following:

(i) means for determining the length of time during which flow of said liquid polymeric materials through said dispenser is terminated;

(ii) means for sensing changes in temperature of said mixture within said dispenser; and

(iii) means for determining the ratio of said liquid polymeric materials supplied to said dispenser.

5. The apparatus of claim 1 wherein said control means comprises:

a means for controlling the inlet pressure of each of said polymeric materials at said dispenser after the flow of materials through said dispenser is terminated so that said inlet pressures are a predetermined function of the pressure which was maintained at said dispenser when said materials were flowing through said dispenser.

6. The apparatus of claim 1 further comprising:

purge means, operatively connected to said control means, for purging the mixture of said liquid materials from said dispenser prior to resumption of flow of said liquid polymeric materials through said dispenser in the event the viscosity of the mixture exceeds a predetermined level.

7. The apparatus of claim 6 in which said purge means includes means for pulsing a flow of one of said liquid polymeric materials through said dispenser, while terminating the flow of the other liquid polymeric material, to force at least a partially cured mixture of such materials out of said dispenser.

8. The apparatus of claim 6 in which the mixture of liquid polymeric materials forms a cured layer along the internal walls of said dispenser, said purge means including means for heating said dispenser to reduce the shear strength with which said cured layer adheres to said internal walls, and means for introducing a flow of one of said liquid polymeric materials into said dispenser while terminating the flow of the other of said polymeric materials.

9. The apparatus of claim 6 in which said first pumping unit is adapted to connect to a source of one liquid polymeric material and to one of said inlets of said dispenser, and said second pumping unit is adapted to connect to a source of a different liquid polymeric material and to another one of said inlets of said dispenser.

10. The apparatus of claim 9 in which said

adjustable pressure regulator means is connected between at least one of said first and second pumping units and said dispenser, for regulating the pressure at which at least one of said liquid polymeric materials is supplied to said dispenser;

means for adjusting said pressure regulator means to vary the pressure at which said at least one liquid polymeric material is supplied to said dispenser dependent on changes in the viscosity of the mixture formed within said dispenser.

11. The apparatus of claim 10 in which said means for adjusting said pressure regulator means includes at least one of the following:

(i) means for determining the length of time during which flow of said liquid polymeric materials through said dispenser is terminated;

(ii) means for sensing changes in temperature of said mixture within dispenser; and

(iii) means for determining the ratio of said liquid polymeric materials supplied to said dispenser.

12. The method of mixing and dispensing at least two different polymeric materials which react chemically with one another when combined, comprising:

supplying different liquid polymeric materials, under pressure, from first and second pump means to a dispenser wherein said materials are combined to form a mixture which is emitted from the dispenser;

terminating the flow of the mixture from the dispenser;

adjusting the pressure at which at least one of the liquid polymeric materials is supplied to the dispenser, prior to resumption of the flow of the mixture from the dispenser, as a function of a change in viscosity of the mixture within the dispenser, said adjusting step performed via operation of an adjustable pressure regulator means adapted to regulate the pressure in a bypass flow path around at least one of said first and second pump means.

13. The method of claim 12 in which said step of adjusting the pressure comprises adjusting the pressure at which at least one of the liquid polymeric materials is supplied to the dispenser as a function of the time during which the mixture remains within the dispenser before flow of the mixture from the dispenser is resumed.

14. The method of claim 12 in which said step of adjusting the pressure comprises adjusting the pressure at which at least one of the liquid polymeric materials is supplied to the dispenser as a function of the ratio with which the liquid polymeric materials are supplied to the dispenser.

15. The method of claim 12 in which said step of adjusting the pressure comprises adjusting the pressure at which at least one of the liquid polymeric materials is supplied to the dispenser as a function of the temperature of the mixture within the dispenser.

16. A method of mixing and dispensing comprising the steps of:

a. intermittently dispensing a mixture of a first and second pressurized liquid polymeric material from an outlet of a dispenser, the first and second liquid polymeric materials supplied to the dispenser by first and second pump means, respectively;

b. determining a steady state inlet pressure for each liquid polymeric material supplied to the dispenser from said first and second pump means when said mixture is dispensing under steady state flow conditions;

c. determining and maintaining an off inlet pressure as a function of the respective steady state inlet pressures of each liquid polymeric material when said mixture is not being dispensed from the dispenser; and

d. adjusting the off inlet pressure prior to resumption of the flow of the mixture from the dispenser, as a function of a change in viscosity of the mixture within the dispenser, said adjusting step performed via operation of an adjustable pressure regulator means adapted to regulate the pressure in a bypass flow path around at least one of said first and second pump means.

17. The method of claim 16 wherein the off inlet pressure of each liquid polymeric material of step (c) is substantially equal to the respective steady state inlet pressure or is a multiple thereof;

and

wherein said step of adjusting the off inlet pressure comprises adjusting the pressure at which at least one of the first and second liquid polymeric materials is supplied to the dispenser as a function of at least one of the following;

(i) the time during which the mixture remains within the dispenser before flow of the mixture from the dispenser is resumed;

(ii) the ratio with which the liquid polymeric materials are supplied to the dispenser; and

(iii) the temperature of the mixture within the dispenser.