US3620306A - Means for foam generation - Google Patents
Means for foam generation Download PDFInfo
- Publication number
- US3620306A US3620306A US791006A US3620306DA US3620306A US 3620306 A US3620306 A US 3620306A US 791006 A US791006 A US 791006A US 3620306D A US3620306D A US 3620306DA US 3620306 A US3620306 A US 3620306A
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- mesh
- pressure differential
- producing
- gas
- signal corresponding
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- A—HUMAN NECESSITIES
- A62—LIFE-SAVING; FIRE-FIGHTING
- A62C—FIRE-FIGHTING
- A62C5/00—Making of fire-extinguishing materials immediately before use
- A62C5/002—Apparatus for mixing extinguishants with water
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S261/00—Gas and liquid contact apparatus
- Y10S261/26—Foam
Definitions
- the invention relates to a method for generating high expansion foam and a foam generator for utilizing the method.
- a method of generating high expansion foam comprising the steps of controlling gas flow means to blow gas through a mesh, disposing on the mesh a solution of foam generating material, measuring the pressures on the upstream and downstream sides of the mesh and maintaining the pressure differential across the mesh substantially constant by controlling the gas flow means.
- a foam generator for generating high expansion foam comprising controllable gas flow means, a mesh so arranged as to have gas from the gas flow means blown through it, dispensing means for disposing on the mesh a solution of foam generating material and two pressure sensors, one on the upstream side and the other on the downstream side of the mesh, the arrangement being such that the gas flow means may be controlled so as to maintain the pressure differential across the mesh substantially constant.
- the rate of gas flow through the mesh should be within prescribed limits. Difficulties are encountered in situations where the back pressure against the foam generator is variable as, for example, when filling an enclosed space with foam for fire prevention or extinction. If the foam generator has sufficient capacity to generate foam against a high back pressure then there is a tendency for the gas velocity to be too high for efficient foam generation when there is little back pressure. Conversely, if the generator is of limited capacity so as to generate foam efficiently at low back pressures it will not operate efficiently at high back pressures The present invention allows efficient foam generation against a wide range of back pressures and is therefore particularly effective in filling enclosed spaces such as mines and tunnels with foam.
- control of the gas flow means is automatic, there being provided control means to which outputs from the two pressure sensors are applied and which gives an error signal output proportional to the divergence from a datum of the difference between the two pressures, and means for applying the error signal to control the gas flow means, the gas flow means being controlled so as to reduce the error signal to zero.
- the gas is usually air, although it may be carbon dioxide or some other gas.
- the gas flow means comprises a fan, axial or centrifugal which is controllable in speed and/or pitch to vary the gas flow rate.
- the control means may comprise controllable shutter means in the gas stream.
- a particular novel use of the invention is found in discharging oil from a seagoing tanker. lf there is a fire risk in such a tanker it is sometimes necessary to discharge oil rapidly.
- the present invention allows the discharge of oil to be effected by filling the tank with high expansion foam under pressure, the generation of foam being efficiently maintained despite changes in back pressure.
- a tank 1 in the tanker which holds oil 2.
- a high expansion foam generator 3 is sealed into the side of the tank near the top.
- the foam generator is activated to discharge foam 4 under pressure into the space above the oil and thereby eject the oil through a pipe 5 which has an inlet at the bottom of the tank and an outlet above the level of the tank.
- the foam generator comprises an expansion chamber 6 over the exit of which is arranged a mesh or net 7.
- a spray head 8 sprays a solution of a foaming agent in water on to the net.
- Air under pressure is ejected into chamber 6 from a nozzle 9 at the end of a conduit 10.
- the air may be derived from a fan 11 shown schematically in broken line as being driven by a motor 12.
- Conduit 10 includes throttle control means comprising an electrically operated shutter 13. This regulates the flow of air into the expansion chamber.
- a pressure transducer 14 is provided upstream of the net and a similar transducer 15 is provided downstream of the net. Signals therefrom respectively of the pressure upstream of the net and the pressure downstream of the net are applied to the inputs of a comparator 16. An output therefrom is given on line 17 representative of the difference between the pressures. This output is compared in a second comparator 18 with a reference datum signal derived from a reference datum generator 19. Any difference between the datum signal and the output from comparator 16 is given as an error signal from the output of comparator l8 and is applied to control shutter 13.
- a transducer such as 14 or 15 converts a mechanical (pressure) quantity into an electrical signal.
- the electrical signals from the two transducers are compared in comparator 16 which can be, for example, a differential amplifier or other similar well-known device.
- the output signal of the comparator 16 will have a magnitude and/or polarity which will be a representation of the difference between the upstream and downstream pressures.
- the signal from comparator 16 is applied to one input of a second comparator 18 which is, for example, another differential amplifier.
- the other input to the second comparator 18 is from a reference setting device 19 which can be, for example where a differential amplifier is used as the comparator 18, a suitable source of variable magnitude and/or polarity voltage.
- the signal from the device 19 is set to a level corresponding to a desired predetermined pressure difierential between the up stream and downstream pressures. As should be apparent, this can be with the upstream pressure greater than the downstream pressure, as is usually the case, or vice versa, or the differential being equal to zero.
- the error signal produced by the comparator 18 is an error signal which is used to drive the shutter 13 to control the flow rate of the gas produced by the fan 11 which reaches the net 15 and thereby the pressure differential.
- the error signal can be used to control the speed of the motor 12 driving fan 1 l or the pitch of the fan blades. Both of these actions will control the rate of gas flow.
- the control arrangement is such that the error signal always tends to be reduced to zero and this means that whatever the back pressure of foam 4, the pressure differential between transducers 14 and 15 is substantially constant, being determined by the setting of the datum generator 19.
- This pressure differential may be, for example, about 2 or 3 p.s.i. and may be maintained against a back pressure of 30 p.s.i. or
- the foam generator may be fixed in position in the side of the tank with a removable guard or cover such as is disclosed in British Pat. specification No. 1,051,850 for protecting the mesh from the oil and preventing ingress of the oil.
- a system for generating high expansion foam comprising an enclosure, means for producing a flow of gas within said enclosure, a mesh located to have the gas produced by the gas flow means blown onto said mesh, dispensing means for disposing on the mesh a solution of foam generating material which reacts with the gas blown onto the net to produce foam which is blown by the gas from the net, means for measuring the pressure differential of the system between the upstream and the downstream sides of the mesh, and means responsive to the measured pressure differential for controlling the rate of gas flow reaching said mesh to produce a substantially predetermined pressure differential.
- a system as in claim 1 further comprising means for comparing the measured pressure differential with a predetermined pressure differential and for producing an error signal representative of the difference between the two; and means responsive to the error signal for controlling the rate of gas flow reaching the mesh from said gas producing means in a manner to maintain said predetermined pressure differential.
- a system as in claim 1 in combination with a second container into which the foam is being expelled from the mesh, said pressure differential measuring means comprising first transducer means located within said first-mentioned container to measure the pressure upstream of said mesh and second transducer means located within said second container to measure the pressure therein.
- said means for measuring the pressure differential comprises first and second transducer means located respectively upstream and downstream of said mesh, each of said transducer means producing an electrical output signal corresponding to the pressure measured.
- said means for measuring the pressure difierential comprises first and second transducer means located respectively upstream and downstream of said mesh, each of said transducer means producing an electrical output signal corresponding to the pressure measured.
- said means for measuring the pressure differential comprises first and second transducer means located respectively upstream and downstream of said mesh, each of said transducer means producing an electrical output signal corresponding to the pressure measured.
- said means for measuring said pressure differential comprises first comparator means for producing a first signal corresponding to the difference in pressures measured by said two transducer means, means for producing a reference signal corresponding to a predetermined pressure differential, second comparator means for receiving said first and said reference signals and responsive thereto to produce an error signal corresponding to the difference between said measured pressure differential and said predetermined pressure differential, and means responsive to said error signal for controlling the rate of flow of the gas reaching said mesh.
- said means for measuring said pressure differential comprises first comparator means for producing a first signal corresponding to the difference in pressures measured by said two transducer means, means for producing a reference signal corresponding to a predetermined pressure differential, second comparator means for receiving said first and said reference signals and responsive thereto to produce an error signal corresponding to the difference between said measured pressure differential and said predetermined pressure differential, and means responsive to said error signal for controlling the rate of flow of the gas reaching said mesh.
- said means for controlling the flow rate of the gas reaching said mesh comprises a variable shutter located between said mesh and said gas producing means.
- a system as in claim 1 wherein said means for producing the gas flow comprises a fan and means for driving said fan, and said means for controlling the flow rate of the gas reaching said mesh comprises means for controlling the speed of said driving means.
- a system as in claim 1 wherein said means for producing the gas flow comprises a fan with at least one blade, and said means for controlling the flow rate of the gas reaching the mesh comprises means for varying the pitch angle of the fan blade.
Abstract
A method and means of generating high expansion foam by spraying foaming agent onto a mesh through which gas (usually air) is blown. Pressure sensors on either side of the mesh sense the pressure differential across the mesh and through control means ensure a constant pressure differential despite changes in back pressure.
Description
United States Patent [111 3,620,306
[72] Inventor Denis Shepherd [56] References Cited 3' "arrow, 5118181"! UNITED STATES PATENTS [21] P 7 2,992,542 7/1961 Arthur 62/140X [22] Filed Jan. 14, 1969 3,004,399 10/1961 Keller 62/l40 [45] Patented Nov. 16, 1971 186 490 6 1965 J l 1 9 [73] Assignee Walter Kldde 8: Company Inc. ammo" eta 6 l5 3,368,629 2/l968 Joerren 169/15 Belleville, NJ.
Primary Examiner-Lloyd L. King M AttorneyDarby & Darby [54] MEANS FOR FOAM GENERATION 11 Claims 1 Drawing ABSTRACT: A method and means of generating high expan- [52] U.S.Cl 169/15, sion foam by spraying foaming agent onto a mesh through 26l/DlG. 26 which gas (usually air) is blown. Pressure sensors on either [51] lnl.Cl A62c 35/00 side of the mesh sense the pressure differential across the [50] Field of Search 26l/DIG. mesh and through control means ensure a constant pressure 26; 62/204; [69/14, 15 differential despite changes in back pressure.
MEANS FOR FOAM GENERATION The invention relates to a method for generating high expansion foam and a foam generator for utilizing the method.
According to one aspect of the invention there is provided a method of generating high expansion foam comprising the steps of controlling gas flow means to blow gas through a mesh, disposing on the mesh a solution of foam generating material, measuring the pressures on the upstream and downstream sides of the mesh and maintaining the pressure differential across the mesh substantially constant by controlling the gas flow means.
According to another aspect of the invention there is provided a foam generator for generating high expansion foam comprising controllable gas flow means, a mesh so arranged as to have gas from the gas flow means blown through it, dispensing means for disposing on the mesh a solution of foam generating material and two pressure sensors, one on the upstream side and the other on the downstream side of the mesh, the arrangement being such that the gas flow means may be controlled so as to maintain the pressure differential across the mesh substantially constant.
For efficient foam generation at a given rate of supply of foam generating material the rate of gas flow through the mesh should be within prescribed limits. Difficulties are encountered in situations where the back pressure against the foam generator is variable as, for example, when filling an enclosed space with foam for fire prevention or extinction. If the foam generator has sufficient capacity to generate foam against a high back pressure then there is a tendency for the gas velocity to be too high for efficient foam generation when there is little back pressure. Conversely, if the generator is of limited capacity so as to generate foam efficiently at low back pressures it will not operate efficiently at high back pressures The present invention allows efficient foam generation against a wide range of back pressures and is therefore particularly effective in filling enclosed spaces such as mines and tunnels with foam.
Preferably the control of the gas flow means is automatic, there being provided control means to which outputs from the two pressure sensors are applied and which gives an error signal output proportional to the divergence from a datum of the difference between the two pressures, and means for applying the error signal to control the gas flow means, the gas flow means being controlled so as to reduce the error signal to zero.
The gas is usually air, although it may be carbon dioxide or some other gas.
Conveniently the gas flow means comprises a fan, axial or centrifugal which is controllable in speed and/or pitch to vary the gas flow rate. Alternatively, or in addition, the control means may comprise controllable shutter means in the gas stream.
A particular novel use of the invention is found in discharging oil from a seagoing tanker. lf there is a fire risk in such a tanker it is sometimes necessary to discharge oil rapidly. The present invention allows the discharge of oil to be effected by filling the tank with high expansion foam under pressure, the generation of foam being efficiently maintained despite changes in back pressure.
The invention will further be described with reference to the accompanying drawing, which is a diagram illustrating an embodiment of the invention as used to discharge oil from a tanker.
Referring to the drawing there is shown a tank 1 in the tanker which holds oil 2. A high expansion foam generator 3 is sealed into the side of the tank near the top. In order to discharge the oil in an emergency the foam generator is activated to discharge foam 4 under pressure into the space above the oil and thereby eject the oil through a pipe 5 which has an inlet at the bottom of the tank and an outlet above the level of the tank. Thus, as the level of the oil in the tank falls the back pressure required in foam 4 to eject the oil rises.
The foam generator comprises an expansion chamber 6 over the exit of which is arranged a mesh or net 7. A spray head 8 sprays a solution of a foaming agent in water on to the net. Air under pressure is ejected into chamber 6 from a nozzle 9 at the end of a conduit 10. The air may be derived from a fan 11 shown schematically in broken line as being driven by a motor 12.Conduit 10 includes throttle control means comprising an electrically operated shutter 13. This regulates the flow of air into the expansion chamber.
A pressure transducer 14 is provided upstream of the net and a similar transducer 15 is provided downstream of the net. Signals therefrom respectively of the pressure upstream of the net and the pressure downstream of the net are applied to the inputs of a comparator 16. An output therefrom is given on line 17 representative of the difference between the pressures. This output is compared in a second comparator 18 with a reference datum signal derived from a reference datum generator 19. Any difference between the datum signal and the output from comparator 16 is given as an error signal from the output of comparator l8 and is applied to control shutter 13.
As is well known, a transducer such as 14 or 15 converts a mechanical (pressure) quantity into an electrical signal. The electrical signals from the two transducers are compared in comparator 16 which can be, for example, a differential amplifier or other similar well-known device. The output signal of the comparator 16 will have a magnitude and/or polarity which will be a representation of the difference between the upstream and downstream pressures. The signal from comparator 16 is applied to one input of a second comparator 18 which is, for example, another differential amplifier. The other input to the second comparator 18 is from a reference setting device 19 which can be, for example where a differential amplifier is used as the comparator 18, a suitable source of variable magnitude and/or polarity voltage. The signal from the device 19 is set to a level corresponding to a desired predetermined pressure difierential between the up stream and downstream pressures. As should be apparent, this can be with the upstream pressure greater than the downstream pressure, as is usually the case, or vice versa, or the differential being equal to zero. The error signal produced by the comparator 18 is an error signal which is used to drive the shutter 13 to control the flow rate of the gas produced by the fan 11 which reaches the net 15 and thereby the pressure differential. As alternatives, the error signal can be used to control the speed of the motor 12 driving fan 1 l or the pitch of the fan blades. Both of these actions will control the rate of gas flow.
The control arrangement is such that the error signal always tends to be reduced to zero and this means that whatever the back pressure of foam 4, the pressure differential between transducers 14 and 15 is substantially constant, being determined by the setting of the datum generator 19. Thus, the optimum pressure differential for efficient foam generation is maintained despite large variations in back pressure. This pressure differential may be, for example, about 2 or 3 p.s.i. and may be maintained against a back pressure of 30 p.s.i. or
The foam generator may be fixed in position in the side of the tank with a removable guard or cover such as is disclosed in British Pat. specification No. 1,051,850 for protecting the mesh from the oil and preventing ingress of the oil.
We claim:
1. A system for generating high expansion foam comprising an enclosure, means for producing a flow of gas within said enclosure, a mesh located to have the gas produced by the gas flow means blown onto said mesh, dispensing means for disposing on the mesh a solution of foam generating material which reacts with the gas blown onto the net to produce foam which is blown by the gas from the net, means for measuring the pressure differential of the system between the upstream and the downstream sides of the mesh, and means responsive to the measured pressure differential for controlling the rate of gas flow reaching said mesh to produce a substantially predetermined pressure differential.
2. A system as in claim 1 further comprising means for comparing the measured pressure differential with a predetermined pressure differential and for producing an error signal representative of the difference between the two; and means responsive to the error signal for controlling the rate of gas flow reaching the mesh from said gas producing means in a manner to maintain said predetermined pressure differential.
3. A system as in claim 1 in combination with a second container into which the foam is being expelled from the mesh, said pressure differential measuring means comprising first transducer means located within said first-mentioned container to measure the pressure upstream of said mesh and second transducer means located within said second container to measure the pressure therein.
4. A system as in claim 1 wherein said means for measuring the pressure differential comprises first and second transducer means located respectively upstream and downstream of said mesh, each of said transducer means producing an electrical output signal corresponding to the pressure measured.
5. A system as in claim 2 wherein said means for measuring the pressure difierential comprises first and second transducer means located respectively upstream and downstream of said mesh, each of said transducer means producing an electrical output signal corresponding to the pressure measured.
6. A system as in claim 3 wherein said means for measuring the pressure differential comprises first and second transducer means located respectively upstream and downstream of said mesh, each of said transducer means producing an electrical output signal corresponding to the pressure measured.
7. A system as in claim 5 wherein said means for measuring said pressure differential comprises first comparator means for producing a first signal corresponding to the difference in pressures measured by said two transducer means, means for producing a reference signal corresponding to a predetermined pressure differential, second comparator means for receiving said first and said reference signals and responsive thereto to produce an error signal corresponding to the difference between said measured pressure differential and said predetermined pressure differential, and means responsive to said error signal for controlling the rate of flow of the gas reaching said mesh.
8. A system as in claim 6, wherein said means for measuring said pressure differential comprises first comparator means for producing a first signal corresponding to the difference in pressures measured by said two transducer means, means for producing a reference signal corresponding to a predetermined pressure differential, second comparator means for receiving said first and said reference signals and responsive thereto to produce an error signal corresponding to the difference between said measured pressure differential and said predetermined pressure differential, and means responsive to said error signal for controlling the rate of flow of the gas reaching said mesh.
9. A system as in claim 1, wherein said means for controlling the flow rate of the gas reaching said mesh comprises a variable shutter located between said mesh and said gas producing means.
'10. A system as in claim 1 wherein said means for producing the gas flow comprises a fan and means for driving said fan, and said means for controlling the flow rate of the gas reaching said mesh comprises means for controlling the speed of said driving means.
11. A system as in claim 1 wherein said means for producing the gas flow comprises a fan with at least one blade, and said means for controlling the flow rate of the gas reaching the mesh comprises means for varying the pitch angle of the fan blade.
t t i t i
Claims (10)
- 2. A system as in claim 1 further comprising means for comparing the measured pressure differential with a predetermined pressure differential and for producing an error signal representative of the difference between the two; and means responsive to the error signal for controlling the rate of gas flow reaching the mesh from said gas producing means in a manner to maintain said predetermined pressure differential.
- 3. A system as in claim 1 in combination with a second container into which the foam is being expelled from the mesh, said pressure differential measuring means comprising first transducer means located within said first-mentioned container to measure the pressure upstream of said mesh and second transducer means located within said second container to measure the pressure therein.
- 4. A system as in claim 1 wherein said means for measuring the pressure differential comprises first and second transducer means located respectively upstream and downstream of said mesh, each of said transducer means producing an electrical output signal corresponding to the pressure measured.
- 5. A system as in claim 2 wherein said means for measuring the pressure differential comprises first and second transducer means located respectively upstream and downstream of said mesh, each of said transducer means producing an electrical output signal corresponding to the pressure measured.
- 6. A system as in claim 3 wherein said means for measuring the pressure differential comprises first and second transducer means located respectively upstream and downstream of said mesh, each of said transducer means producing an electrical output signal corresponding to the pressure measured.
- 7. A system as in claim 5 wherein said means for measuring said pressure differential comprises first comparator means for producing a first signal corresponding to the difference in pressures measured by said two transducer means, means for producing a reference signal corresponding to a predetermined pressure differential, second comparator means for receiving said first and said reference signals and responsive thereto to produce an error signal corresponding to the difference between said measured pressure differential and said predetermined pressure differential, and means responsive to said error signal for controlling the rate of flow of the gas reaching said mesh.
- 8. A system as in claim 6, wherein said means for measuring said pressure differential comprises first comparator means for producing a first signal corresponding to the difference in pressures measured by said two transducer means, means for producing a reference signal corresponding to a predetermined pressure differential, second comparator means for receiving said first and said reference signals and responsive thereto to produce an error signal corresponding to the difference between said measured pressure differential and said predetermined pressure differential, and means responsive to said error signal for controlling the rate of flow of the gas reaching said mesh.
- 9. A system as in claim 1, wherein said means for controlling the flow rate of the gas reaching said mesh comprises a variable shutter located between said mesh and said gas producing means.
- 10. A system as in claim 1 wherein said means for producing the gas flow comprises a fan and means for driving said fan, and said means for controlling the flow rate of the gas reaching said mesh comprises means for controlling the speed of said driving means.
- 11. A system as in claim 1 wherein said means for producing the gas flow comprises a fan with at least one blade, and said means for controlling the flow rate of the gas reaching the mesh comprises means for varying the pitch angle of the fan blade.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US79100669A | 1969-01-14 | 1969-01-14 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US3620306A true US3620306A (en) | 1971-11-16 |
Family
ID=25152375
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US791006A Expired - Lifetime US3620306A (en) | 1969-01-14 | 1969-01-14 | Means for foam generation |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US3620306A (en) |
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3749378A (en) * | 1971-05-28 | 1973-07-31 | Gen Foods Ltd | Producing a foamed liquid |
| US3811660A (en) * | 1970-11-20 | 1974-05-21 | H Cole | Equipment for making foam for dust suppression and other purposes |
| US3846515A (en) * | 1971-08-11 | 1974-11-05 | Chemetron Corp | Mechanical foam generating method and system |
| US4027993A (en) * | 1973-10-01 | 1977-06-07 | Polaroid Corporation | Method and apparatus for compressing vaporous or gaseous fluids isothermally |
| US4060572A (en) * | 1974-07-31 | 1977-11-29 | Borden Products Limited | Foaming apparatus |
| US4323474A (en) * | 1975-10-16 | 1982-04-06 | P. Campen Maskinfabrik A/S | Method of producing foam material and apparatus therefor |
| US4446923A (en) * | 1979-04-30 | 1984-05-08 | Walter Kidde & Co., Inc. | Removal of explosive or combustible gas or vapors from tanks and other enclosed spaces |
| US4653591A (en) * | 1983-09-06 | 1987-03-31 | Marshall James S | Method of producing foam and foam generator |
| US4732181A (en) * | 1985-02-22 | 1988-03-22 | Stefan Sollander | Vehicle carried system for camouflage with foam |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2992542A (en) * | 1956-10-23 | 1961-07-18 | Garrett Corp | Ice formation control for air conditioning systems |
| US3004399A (en) * | 1958-12-01 | 1961-10-17 | Gen Controls Co | Automatic defrost control for refrigerators or heat pump systems |
| US3186490A (en) * | 1961-08-08 | 1965-06-01 | Specialties Dev Corp | Fire-fighting method employing high expansion foam |
| US3368629A (en) * | 1965-08-12 | 1968-02-13 | Specialties Dev Corp | Protective closure for fire-fighting foam generator |
-
1969
- 1969-01-14 US US791006A patent/US3620306A/en not_active Expired - Lifetime
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2992542A (en) * | 1956-10-23 | 1961-07-18 | Garrett Corp | Ice formation control for air conditioning systems |
| US3004399A (en) * | 1958-12-01 | 1961-10-17 | Gen Controls Co | Automatic defrost control for refrigerators or heat pump systems |
| US3186490A (en) * | 1961-08-08 | 1965-06-01 | Specialties Dev Corp | Fire-fighting method employing high expansion foam |
| US3368629A (en) * | 1965-08-12 | 1968-02-13 | Specialties Dev Corp | Protective closure for fire-fighting foam generator |
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3811660A (en) * | 1970-11-20 | 1974-05-21 | H Cole | Equipment for making foam for dust suppression and other purposes |
| US3749378A (en) * | 1971-05-28 | 1973-07-31 | Gen Foods Ltd | Producing a foamed liquid |
| US3846515A (en) * | 1971-08-11 | 1974-11-05 | Chemetron Corp | Mechanical foam generating method and system |
| US4027993A (en) * | 1973-10-01 | 1977-06-07 | Polaroid Corporation | Method and apparatus for compressing vaporous or gaseous fluids isothermally |
| US4060572A (en) * | 1974-07-31 | 1977-11-29 | Borden Products Limited | Foaming apparatus |
| US4323474A (en) * | 1975-10-16 | 1982-04-06 | P. Campen Maskinfabrik A/S | Method of producing foam material and apparatus therefor |
| US4446923A (en) * | 1979-04-30 | 1984-05-08 | Walter Kidde & Co., Inc. | Removal of explosive or combustible gas or vapors from tanks and other enclosed spaces |
| US4653591A (en) * | 1983-09-06 | 1987-03-31 | Marshall James S | Method of producing foam and foam generator |
| US4732181A (en) * | 1985-02-22 | 1988-03-22 | Stefan Sollander | Vehicle carried system for camouflage with foam |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| AS | Assignment |
Owner name: KIDDE, INC. Free format text: MERGER;ASSIGNORS:HIMP-2 INC.;HIMP-2 INC. (CHANGED TO);REEL/FRAME:005046/0017 Effective date: 19880331 Owner name: WALTER KIDDE FIRE SUPRESSION, INC., A DE CORP., NO Free format text: ASSIGNMENT OF ASSIGNORS INTEREST.;ASSIGNOR:KIDDIE, INC. (KC), A DE CORP.;REEL/FRAME:005006/0495 Effective date: 19880402 |
|
| AS | Assignment |
Owner name: BLOOM-1 INC., A CORP. OF DE Free format text: MERGER;ASSIGNOR:KIDDE INC.;REEL/FRAME:005359/0391 Effective date: 19880331 |