US2390871A - Apparatus for mixing and dispensing fluids of different densities - Google Patents
Apparatus for mixing and dispensing fluids of different densities Download PDFInfo
- Publication number
- US2390871A US2390871A US526222A US52622244A US2390871A US 2390871 A US2390871 A US 2390871A US 526222 A US526222 A US 526222A US 52622244 A US52622244 A US 52622244A US 2390871 A US2390871 A US 2390871A
- Authority
- US
- United States
- Prior art keywords
- cylinder
- tube
- branch
- mixture
- inlet
- Prior art date
- Legal status (The legal status 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 status listed.)
- Expired - Lifetime
Links
- 239000012530 fluid Substances 0.000 title description 13
- 239000007788 liquid Substances 0.000 description 22
- 239000000203 mixture Substances 0.000 description 19
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 16
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 description 16
- 239000001294 propane Substances 0.000 description 8
- 239000000446 fuel Substances 0.000 description 4
- 238000009835 boiling Methods 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- 230000001174 ascending effect Effects 0.000 description 1
- 238000005452 bending Methods 0.000 description 1
- 238000005219 brazing Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000008240 homogeneous mixture Substances 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 238000005476 soldering Methods 0.000 description 1
- 238000003466 welding Methods 0.000 description 1
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B67—OPENING, CLOSING OR CLEANING BOTTLES, JARS OR SIMILAR CONTAINERS; LIQUID HANDLING
- B67D—DISPENSING, DELIVERING OR TRANSFERRING LIQUIDS, NOT OTHERWISE PROVIDED FOR
- B67D7/00—Apparatus or devices for transferring liquids from bulk storage containers or reservoirs into vehicles or into portable containers, e.g. for retail sale purposes
- B67D7/06—Details or accessories
- B67D7/74—Devices for mixing two or more different liquids to be transferred
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/20—Mixing gases with liquids
- B01F23/23—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C13/00—Details of vessels or of the filling or discharging of vessels
- F17C13/002—Details of vessels or of the filling or discharging of vessels for vessels under pressure
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2265/00—Effects achieved by gas storage or gas handling
- F17C2265/02—Mixing fluids
- F17C2265/025—Mixing fluids different fluids
-
- 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
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T137/00—Fluid handling
- Y10T137/2931—Diverse fluid containing pressure systems
- Y10T137/3115—Gas pressure storage over or displacement of liquid
- Y10T137/3127—With gas maintenance or application
- Y10T137/313—Gas carried by or evolved from liquid
Definitions
- This invention relates generally to an apparatus for obtaining a definite proportional mixture of two fluids differing in density and boiling points and for continuously dispensing the deflnite proportional mixture thus obtained for use in the industrial arts.
- the invention relates to an apparatus including a tank or cylinder wherein -two fluids, capable of being admixed for use in metal operations (such as welding, cutting and the like) but differing in respect to their densities and boiling points, may be mixed in definite proportions and delivered continuously in such proportions to the point of use until the contents of the cylinder shall have been exhausted.
- my invention contemplates an apparatus of the character described wherein the fluid fuels consist of propane and ether, the propane being charged into the cylinder under a pressure of approximately 100-410 pounds per square inch whereby it will be largely converted into a liquid and, in such form, will be admixed with the ether of higher density in the bottom of th cylinder and, by means of a tube leading from the bottom of the cylinder, a mixture of these liquids will be delivered through the customary valve in the top of the cylinder.
- the fluid fuels consist of propane and ether
- Fig. 1 represents a view, partly in section and partly in elevation, of a cylinder having liquids of different densities therein and provided with a mixing and dispensing tube constructed in accordance with my invention
- Fig. 2 an enlarged detail in section taken on the line 2--2 of Fig. 1 looking in the direction of the arrows;
- Fig. 3 an enlarged detail in elevation, taken on the line 3-3 of Fig. 1 and lboking in the direction of the arrows;
- Fig. 4 an enlarged detail in section of the upper portion of the mixing and dispensing tube;
- Fig.5 an enlarged detail in sectional elevation of the lower end of the dispensing tube.
- l0 denotes a cylinder which is provided with a neck H within which there is threaded the lower end of a valve body l2 of the type usually providedfor cylinders suchas are'em-I The ployed for dispensing gases under pressure.
- threaded lower end l3 of the valve body is provided with a chamber M from which a-port l5 leads to the usual valve seat (not shown) and with which the usual valve (notshown), having an operating handle l6, cooperates.
- the valve body' is provided with an elbow IT to which a dise pensing pipe I8 is connected.
- l9 denotes the delivery branch of a tube, the upper end of which is connected, as by soldering or brazing, with the bottom of a tubular connector 20, the upperend of said connector being shown as threaded into the threaded lower end l3 of the valve body. It will be noted that this construction provides an expansion chamber between the delivery and of the branch l9 and the valve seat.
- the tube is bent upon itself to provide a close return bend or loop-adjacent to the bottom of the cylinder, with-the delivery branch extending upwardly therefrom to the connector.
- is shown as closed and an inlet opening 22 ,is provided therein adjacent to the closed end thereof.
- 23 denotes an inlet opening slightly above the bottom of the looped lower end of the tube and located substantially axially beneath the portion of the branch is extending thereabove.
- An inlet opening 24 is provided in the delivery branch [9 above the level of the liquid and approximately in the same horizontal plane as the center of the inlet opening 22.
- the inlet opening 24 serves to balance the pressure between the gaseous or vaporous atmosphere in the tank and the mixture within the tube.
- the size of the inlet openings for the admission of liquid and vapor into the tube will vary with the cross sectional area of the tube employed and, while satisfactory results have been obtained by the use, in the particular apparatus described herein, of an inlet opening of the size made by a #30 drill in the branch 2
- the opening 24 may be omitted.
- An apparatus for the purpose specified including a cylinder for dispensing under pressure a mixture of liquids differing widely in volatility and at least one of which exists normally in a gaseous condition, the said cylinder being provided at its top with a delivery valve body, a tube comprising a delivery branch connected to and extending downwardly from the said valve body to a point in close proximity to the bottom of the cylinder and a branch connected with the former branch and extending upwardly from the latter to a point above the liquid level of a normally full charge of liquids within the cylinder, the delivery branch being provided with an inlet in the bottom thereof arranged for deliverin liquid substantially axially into the said delivery branch and. being provided with an inlet of substantially the same size above the said level and the opposite branch of the tube being provided with a relatively large inlet also located above the said level.
- An apparatus for the purpose specified including a cylinder for dispensing under pressure a mixture of liquids difiering widely in volatility and at least one of which exists normally in a aseous condition, the said cylinder being provided at its top with a delivery valve body, a tube comprising a delivery branch connected to and extending downwardly from the said valve body to a point in close proximity to the bottom of the cylinder and a branch connected with the former branch and extending upwardly from the latter to a point above the liquid level of a normally in claim 1, wherein, with a tube of the order of 3/16 inch internal diameter, the inlet in the bottom of the delivery branch has a cross-sectional area of approximately the size of a hole made by a #69 drill, the inlet in the other branch having a cross-sectional area not materially less than that of a hole made by a #30 drill and the inlet in the portion of the delivery branch which is above the said liquid level having a cross-sectional area of approximately the size made by utilizing a drill withinthe range of from
- An apparatus for the purpose specified including a cylinder for dispensing under pressure a mixture of fluid elements differing widely in volatility, one of said elements existing normally in a gaseous condition, the said cylinder being provided at its top with a delivery valve body, a tube comprising a delivery branch connected to and extending downwardly from the said valve body to a point in close proximity to the bottom of the cylinder and a branch connected with the former branch and extending upwardly from the latter to a point above the liquid level of a full charge of fluids within the cylinder, the delivery branch being provided with an inlet in the bottom thereof arranged for delivering liquid substantially axially into the said delivery branch and the opposite branch of the tube being provided with a relatively large inlet located above the said liquid level, thefirst-mentioned inlet, in a tube wherein the delivery branch is approximately 3/16 inch internal diameter, having a cross sectional area of approximately the size of a hole made by a #69 drill.
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Containers And Packaging Bodies Having A Special Means To Remove Contents (AREA)
Description
Dec. 11, 1945. D. J; CONWAY APPARATUS FOR MIXING AND DISPENSING FLUIDS OF DIFFERENT DENSITIES.
I Filed March 13, 1944 IN VEN TOR.
Patented Dec. 11, 1945 I APPARATUS FOR MIXING AND DISPENSING I FLUIDS OF DIFFERENT DENSITIES Donald J. Conway,'Cleveland, Ohio, assignor to American Utilities Corporation,
Cleveland,
Ohio, a corporation of Delaware Application March 13, 1944, Serial No. 526,222
- 6 Claims. (Cl. 62-1) This invention relates generally to an apparatus for obtaining a definite proportional mixture of two fluids differing in density and boiling points and for continuously dispensing the deflnite proportional mixture thus obtained for use in the industrial arts.
More particularly, the invention relates to an apparatus including a tank or cylinder wherein -two fluids, capable of being admixed for use in metal operations (such as welding, cutting and the like) but differing in respect to their densities and boiling points, may be mixed in definite proportions and delivered continuously in such proportions to the point of use until the contents of the cylinder shall have been exhausted.
Still more limitedly, my invention contemplates an apparatus of the character described wherein the fluid fuels consist of propane and ether, the propane being charged into the cylinder under a pressure of approximately 100-410 pounds per square inch whereby it will be largely converted into a liquid and, in such form, will be admixed with the ether of higher density in the bottom of th cylinder and, by means of a tube leading from the bottom of the cylinder, a mixture of these liquids will be delivered through the customary valve in the top of the cylinder.
Attempts have been made heretofore to dispense from cylinders a mixture of predetermined proportions of these fluids and to maintain such predetermined proportions throughout the entire range of operation until the contents of the cylinders should be exhausted, utilizing for this purpose tubes communicating'with the bottoms ,of the cylinders and the valves in the tops of the same, but all such attempts with which I am familiar have resulted in failure. This failure has been due to the physical properties of the propane which, as the pressure within the cylinders containing the same is reduced, tends increasingly to assume a gaseous or vaporous form as the mixture is withdrawn from-the cylinders, with the result that a relatively large proportion of ether remains in the cylinders after the exhaustion of the propane.
Due to the construction of the tube which communicates with the cylinder valve 'and to the manner in which the vaporous andliquid fuel elements are admitted thereinto. I am enabled to obtain a mixture of definite predetermined proportions of the fluid fuel ingredients and to insure that this definite mixing and proportioning shall be automatically maintained so long as the pressure of the atmosphere within the tank-is capable of delivering mixture through the said tube.
I accomplish these objects by means of the apparatus shown in the accompanying drawing,
wherein Fig. 1 represents a view, partly in section and partly in elevation, of a cylinder having liquids of different densities therein and provided with a mixing and dispensing tube constructed in accordance with my invention; Fig.
2 an enlarged detail in section taken on the line 2--2 of Fig. 1 looking in the direction of the arrows; Fig. 3 an enlarged detail in elevation, taken on the line 3-3 of Fig. 1 and lboking in the direction of the arrows; Fig. 4 an enlarged detail in section of the upper portion of the mixing and dispensing tube; and Fig.5 an enlarged detail in sectional elevation of the lower end of the dispensing tube.
Describing the various parts by reference characters, l0 denotes a cylinder which is provided with a neck H within which there is threaded the lower end of a valve body l2 of the type usually providedfor cylinders suchas are'em-I The ployed for dispensing gases under pressure. threaded lower end l3 of the valve body is provided with a chamber M from which a-port l5 leads to the usual valve seat (not shown) and with which the usual valve (notshown), having an operating handle l6, cooperates. The valve body'is provided with an elbow IT to which a dise pensing pipe I8 is connected.
l9 denotes the delivery branch of a tube, the upper end of which is connected, as by soldering or brazing, with the bottom of a tubular connector 20, the upperend of said connector being shown as threaded into the threaded lower end l3 of the valve body. It will be noted that this construction provides an expansion chamber between the delivery and of the branch l9 and the valve seat. The tube is bent upon itself to provide a close return bend or loop-adjacent to the bottom of the cylinder, with-the delivery branch extending upwardly therefrom to the connector.
:of which the tube is composed more ductile and less liable tocrystallize and break'otl within the cylinder. under rough usage. This mannero! bending the tube also enables the latter to be inserted through the neck of the cylinder, when the valve is screwed thereinto.
The upper end of the branch 2| is shown as closed and an inlet opening 22 ,is provided therein adjacent to the closed end thereof. 23 denotes an inlet opening slightly above the bottom of the looped lower end of the tube and located substantially axially beneath the portion of the branch is extending thereabove. An inlet opening 24 is provided in the delivery branch [9 above the level of the liquid and approximately in the same horizontal plane as the center of the inlet opening 22.
In utilizing the apparatus thus described for dispensing a mixture of ether and propane, with an initial pressure in the cylinder of approximately 100 to 110 pounds at 70 F. atmospheric temperature and with the dispensing tube inch internal diameter and the inlet openings 23 and 24 made with a #69 drill and the inlet opening 22 of larger cross sectional area than the inlet openings 23 and 24, employing a cylinder 38 inches high by 12 inches intemal diameter having therein a charge of up to '7 pounds of ether and 50 pounds of propane, I have been able to produce and to deliver through the cylinder valve a uniform mixture of predetermined definite proportions of either and propane until the level of the liquid falls below the inlet opening 23. Satisfactory results have been obtained where the inlet opening 22 has been of a size such as made by a #30 drill and also where it has been equal to'the cross sectional area of the interior of the tube.
It is believed that when the cylinder valve is opened the liquid in the bottom of the cylinder is delivered in a jet into the ascending branch IQ of the tube and that in so doing it is admixed with the vaporous contents of the cylinder entering the descending branch of the tube through the inlet opening 22, the liquid delivered through the inlet opening 23 exercising an aspirating or ejector action upon the vapor. I have found that the inlet opening 24 serves to balance the pressure between the gaseous or vaporous atmosphere in the tank and the mixture within the tube. When the valve I6 is opened slightly, so as todeliver the mixture slowly through the branch IS, a back pressure will be created within the tube which will be balanced by the pressure of the atmosphere above the liquid level transmitted through the inlet opening 24. However, when the valve is opened wide and the mixture is being withdrawn rapidly from the tube, the pressure in the tube is reduced and the inlet opening 24 serves to admit atmosphere from the cylinder into the portion cf the tubular branch [9 thereabove, the net result being that the apparatus described herein delivers at all times a homogeneous mixture of the two fuels, admixed in constant, definite proportions; and this delivery of such definite proportions persists until the level of liquid within the cylinder falls below the inlet opening 23. Furthermore, with the parts constructed and arranged as described, the pressure within the cylinder falls very slowly, as compared with the-conditions which exist in cylinders in which it has been attempted heretofore to obtain a satisfactory operation of producing and delivering a constant definitely proportioned mixture of propane and ether.
Quite satisfactory results have also been obtained where, with a tube of the same diameter as that shown and described herein and with the inlet openings 22 and 23 of the respective sizes previously stated, the size of the inlet opening 24 has been increased by forming the same with a #62 drill and with a #54 drill. When, due to the operation' of dispensing the mixture, the
pressure within the cylinder was insufiicient to effect any 'further delivery therefrom, only 4 pound of ether remained therein in the former case and approximately 1 pound of ether remained in the latter case.
Obviously the size of the inlet openings for the admission of liquid and vapor into the tube will vary with the cross sectional area of the tube employed and, while satisfactory results have been obtained by the use, in the particular apparatus described herein, of an inlet opening of the size made by a #30 drill in the branch 2| of I the tube, the size of this opening may be reduced considerably but without preventing the constant delivery of a satisfactory mixture of the vaporous and liquid contents of the cylinder and, therefore, without avoiding the spirit of my invention.
Where one of the fluids within the cylinder remains in a liquid condition throughout the entire operation of producing and delivering a mixture of fluids and the other fluid remains in a gaseous condition throughout such entire operation, the opening 24 may be omitted.
Having thus described my invention, what I claim is:
1. An apparatus for the purpose specified including a cylinder for dispensing under pressure a mixture of liquids differing widely in volatility and at least one of which exists normally in a gaseous condition, the said cylinder being provided at its top with a delivery valve body, a tube comprising a delivery branch connected to and extending downwardly from the said valve body to a point in close proximity to the bottom of the cylinder and a branch connected with the former branch and extending upwardly from the latter to a point above the liquid level of a normally full charge of liquids within the cylinder, the delivery branch being provided with an inlet in the bottom thereof arranged for deliverin liquid substantially axially into the said delivery branch and. being provided with an inlet of substantially the same size above the said level and the opposite branch of the tube being provided with a relatively large inlet also located above the said level.
2. An apparatus for the purpose specified including a cylinder for dispensing under pressure a mixture of liquids difiering widely in volatility and at least one of which exists normally in a aseous condition, the said cylinder being provided at its top with a delivery valve body, a tube comprising a delivery branch connected to and extending downwardly from the said valve body to a point in close proximity to the bottom of the cylinder and a branch connected with the former branch and extending upwardly from the latter to a point above the liquid level of a normally in claim 1, wherein, with a tube of the order of 3/16 inch internal diameter, the inlet in the bottom of the delivery branch has a cross-sectional area of approximately the size of a hole made by a #69 drill, the inlet in the other branch having a cross-sectional area not materially less than that of a hole made by a #30 drill and the inlet in the portion of the delivery branch which is above the said liquid level having a cross-sectional area of approximately the size made by utilizing a drill withinthe range of from #54 to #69.
4. A dispensing apparatus of the type set forth in claim 1, wherein, with a tube of the order of inch internal diameter, the inlets in the delivery branch each have a cross-sectional area of approximately the size of a hole made by a #69 drill and the inlet in the other branch has a cross-sectional area not materially less than that of a hole made by a #30 drill.
,5. A dispensing apparatus of the type set forth in claim 2, wherein, with a tube of the order of inch internal diameter, the inlets in the delivery branch each have a cross-sectional area of approximately the size of a hole made by a #69 drill and the inlet in the other branch has a cross sectional area not materially less than that of a hole made by a #30 drill.
6. An apparatus for the purpose specified including a cylinder for dispensing under pressure a mixture of fluid elements differing widely in volatility, one of said elements existing normally in a gaseous condition, the said cylinder being provided at its top with a delivery valve body, a tube comprising a delivery branch connected to and extending downwardly from the said valve body to a point in close proximity to the bottom of the cylinder and a branch connected with the former branch and extending upwardly from the latter to a point above the liquid level of a full charge of fluids within the cylinder, the delivery branch being provided with an inlet in the bottom thereof arranged for delivering liquid substantially axially into the said delivery branch and the opposite branch of the tube being provided with a relatively large inlet located above the said liquid level, thefirst-mentioned inlet, in a tube wherein the delivery branch is approximately 3/16 inch internal diameter, having a cross sectional area of approximately the size of a hole made by a #69 drill.
DONALD J. CONWAY.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US526222A US2390871A (en) | 1944-03-13 | 1944-03-13 | Apparatus for mixing and dispensing fluids of different densities |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US526222A US2390871A (en) | 1944-03-13 | 1944-03-13 | Apparatus for mixing and dispensing fluids of different densities |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US2390871A true US2390871A (en) | 1945-12-11 |
Family
ID=24096438
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US526222A Expired - Lifetime US2390871A (en) | 1944-03-13 | 1944-03-13 | Apparatus for mixing and dispensing fluids of different densities |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US2390871A (en) |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2494219A (en) * | 1946-08-15 | 1950-01-10 | Samuel H White | Gaseous fuel mixture |
| US2582262A (en) * | 1947-11-10 | 1952-01-15 | Bridgeport Brass Co | Dispensing apparatus |
| US3069098A (en) * | 1960-06-20 | 1962-12-18 | Revlon | Aerosol sprayer |
| US3194450A (en) * | 1963-11-15 | 1965-07-13 | Scovill Manufacturing Co | Aerosol dispenser |
| US4356941A (en) * | 1980-05-19 | 1982-11-02 | Republic Tool & Manufacturing Corporation | Squeeze-type dispenser for powdered materials |
| DE102022203689A1 (en) | 2022-04-12 | 2023-10-12 | Jahn Gmbh Umform- Und Zerspanungstechnik | pressure vessel |
| US20250074688A1 (en) * | 2023-09-01 | 2025-03-06 | Jahn Gmbh Umform- Und Zerspanungstechnik | Pressure container |
-
1944
- 1944-03-13 US US526222A patent/US2390871A/en not_active Expired - Lifetime
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2494219A (en) * | 1946-08-15 | 1950-01-10 | Samuel H White | Gaseous fuel mixture |
| US2582262A (en) * | 1947-11-10 | 1952-01-15 | Bridgeport Brass Co | Dispensing apparatus |
| US3069098A (en) * | 1960-06-20 | 1962-12-18 | Revlon | Aerosol sprayer |
| US3194450A (en) * | 1963-11-15 | 1965-07-13 | Scovill Manufacturing Co | Aerosol dispenser |
| US4356941A (en) * | 1980-05-19 | 1982-11-02 | Republic Tool & Manufacturing Corporation | Squeeze-type dispenser for powdered materials |
| DE102022203689A1 (en) | 2022-04-12 | 2023-10-12 | Jahn Gmbh Umform- Und Zerspanungstechnik | pressure vessel |
| EP4260946A1 (en) * | 2022-04-12 | 2023-10-18 | Jahn GmbH Umform- und Zerspanungstechnik | Pressure vessel |
| DE102022203689B4 (en) * | 2022-04-12 | 2025-10-16 | Jahn Gmbh Umform- Und Zerspanungstechnik | pressure vessel |
| EP4685080A2 (en) | 2022-04-12 | 2026-01-28 | Jahn GmbH Umform- und Zerspanungstechnik | Pressure vessel |
| US20250074688A1 (en) * | 2023-09-01 | 2025-03-06 | Jahn Gmbh Umform- Und Zerspanungstechnik | Pressure container |
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