US3525228A - Nonboiling liquid target for a high-energy particle beam - Google Patents

Nonboiling liquid target for a high-energy particle beam Download PDF

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US3525228A
US3525228A US796350A US3525228DA US3525228A US 3525228 A US3525228 A US 3525228A US 796350 A US796350 A US 796350A US 3525228D A US3525228D A US 3525228DA US 3525228 A US3525228 A US 3525228A
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target
liquid
cell
coolant
particle beam
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Robert L Anderson
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS 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
    • F17C13/00Details of vessels or of the filling or discharging of vessels
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS 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
    • F17C2201/00Vessel construction, in particular geometry, arrangement or size
    • F17C2201/01Shape
    • F17C2201/0104Shape cylindrical
    • F17C2201/0119Shape cylindrical with flat end-piece
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS 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
    • F17C2203/00Vessel construction, in particular walls or details thereof
    • F17C2203/03Thermal insulations
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS 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
    • F17C2203/00Vessel construction, in particular walls or details thereof
    • F17C2203/03Thermal insulations
    • F17C2203/0391Thermal insulations by vacuum
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS 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
    • F17C2203/00Vessel construction, in particular walls or details thereof
    • F17C2203/06Materials for walls or layers thereof; Properties or structures of walls or their materials
    • F17C2203/0602Wall structures; Special features thereof
    • F17C2203/0612Wall structures
    • F17C2203/0626Multiple walls
    • F17C2203/0629Two walls
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS 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
    • F17C2221/00Handled fluid, in particular type of fluid
    • F17C2221/01Pure fluids
    • F17C2221/012Hydrogen
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS 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
    • F17C2221/00Handled fluid, in particular type of fluid
    • F17C2221/03Mixtures
    • F17C2221/038Refrigerants
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS 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
    • F17C2223/00Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel
    • F17C2223/01Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel characterised by the phase
    • F17C2223/0146Two-phase
    • F17C2223/0153Liquefied gas, e.g. LPG, GPL
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS 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
    • F17C2223/00Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel
    • F17C2223/01Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel characterised by the phase
    • F17C2223/0146Two-phase
    • F17C2223/0153Liquefied gas, e.g. LPG, GPL
    • F17C2223/0161Liquefied gas, e.g. LPG, GPL cryogenic, e.g. LNG, GNL, PLNG
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/32Hydrogen storage

Definitions

  • a differentially pressurized target system in which heat in a pressurized liquid hydrogen target is transferred by rapid convection currents to one side of a heat exchanger for dissipation on the other side in a liquid hydrogen reservoir that is maintained at atmospheric pressure.
  • the rapid convection currents and the diiference in pressures in the target and reservoir permits cooling of the target by the liquid hydrogen in the reservoir to a temperature below the boiling point of the liquid target, thus inhibiting boiling of the target liquid upon impingement of a particle beam.
  • the present invention relates to nonboiling liquid targets for high-energy particle beams, and more particularly, it relates to a convectively cooled liquid target that is pressurized to raise its boiling temperature significantly above its operating temperature.
  • the present invention pertains to a liquid target that may be positioned in the path of a high-energy particle beam of predetermined energy and intensity without boiling the target liquid.
  • the target is comprised of a target cell filled with a target liquid maintained under pressure to raise its boiling point.
  • the cell is shaped to contain a large total volume of target liquid, relative to the volume traversed by the beam, to provide sufiicient space for the creation of temperature differentials that will sustain convection currents upon heating the target liquid with the beam.
  • a heat exchanger is exposed to the convection currents for transferring heat from the cell to a reservoir of coolant.
  • the coolant is maintained at a pressure such that it boils at a temperature less than the boiling point of the target liquid, thereby maintaining the target liquid in a nonboiling state.
  • Another object is to dissipate beam energy deposited in a liquid target by pressurizing the target to raise its boiling point to a temperature level that is significantly above that of a coolant that is permitted to boil to dissipate the energy.
  • Another object is to transfer heat from a liquid target for a high-energy particle beam to a heat exchanger by means of convection currents.
  • Another object is todetect the liquid level of a liquid target for a high-energy particle beam with a constant volume source of pressurized gas.
  • FIG. 1 is a diagram with portions broken away of a liquid target for a high-energy particle beam and a target cooling system, according to the invention.
  • a target system including a target 12 comprised of a cell 13 filled with a target liquid such as liquid hydrogen. Hydrogen is often used as a target because it has a relatively simple nucleus that yields easily interpreted results.
  • the cell 13 is suitably attached to one end of a reservoir 15 that is partially filled with a coolant 16 such as liquid hydrogen.
  • a heat exchanger 17 is mounted between the reservoir 15 and the target 12 with fins 18 exposed to the coolant 16 and fins 18 exposed to the target liquid.
  • the reservoir 15 may be filled with liquid coolant through a line 20 connected to a coolant supply (not shown).
  • the coolant in the reservoir 15 may conveniently be held at atmospheric pressure through a vent line 22 to atmosphere.
  • the target liquid in the cell 13 is held under pressure by means of a pressurized target gas supply 24 connected to the cell 13 over a line 26 which is passed through the coolant 16 for precooling the gas.
  • the target 12 and reservoir 15 are enclosed in a vacuum environment for thermal isolation by means of a scattering chamber 28 and a tank 30.
  • the target 12 and the reservoir 15 may be moved relative to the tank 30 and scattering chamber 28 by means of a bellows 32 through which the lines 20, 22 and 26 extend; these lines may be flexibly connected by conventional means to their sources to permit movement of the target and reservoir.
  • the target system may be connected to the end of an accelerator 34 in which a high-energy particle beam 35 is developed.
  • the target 12 may be centrally located in the path of the beam to enable collisions between the beam particles and the particles of the target 3 liquid for development of subatomic particles which then pass through a thin window 36 in the scattering chamber for detection with a particle detector (not shown) such as a Geiger counter, spectrometer, bubble chamber or spark chamber.
  • Impingement of the beam in the target 12 generates a large amount of heat in the liquid in the path of the particle beam.
  • the cell 13 is arranged to have a relatively large total volume as compared to the volume of the target liquid traversed by the beam 35, typically 60 to l with the heat exchanger spaced on the order of four beam diameters from the beam path. This permits a substantial temperature gradient to be set up between the heated volume in the beam path and cooler outer regions of the cell.
  • the target liquid in the region of the fins 18' is held substantially at the temperature of the coolant 16 by means of the heat exchanger 17.
  • Convection currents 38 are generated thereby to carry heat from the region of the particle beam 35 to the fins 18' for transfer through the exchanger 17 to the fins 18 for dissipation in the coolant 16. Since the coolant 16 is held at atmospheric pressure, the added heat causes the coolant to boil to dissipate the heat.
  • the vaporized liquid hydrogen is vented to atmosphere through the vent line 22, while additional liquid coolant may be automatically supplied through line 20 under control of conventional liquid level sensing means (not shown).
  • the cell 13 may be filled with target liquid directly from the pressurized target gas supply 24 whereby the gas in the cell immediately condenses on the fins 18' upon entering the cell 13.
  • the cell 13 could be filled by temporarily switching the line 26 to a liquid hydrogen supply to avoid delay in cooling the target.
  • a dummy cell 42 may be suitably mounted on the lower end of the cell 13 and may be selectively raised into the path of the beam 35.
  • a vacuum is provided within the cell 42 so that when it is in the beam path, the effect of the beam on the cell walls may be determined with particle detectors and taken into account when interpreting the results obtained with the cell 13 in the path of the beam.
  • the dummy cell 42 may be used as a second target cell and filled with hydrogen or deuterium, using the target liquid in the cell 13 as a coolant to condense gas supplied to the cell 42.
  • the target liquid in the cell 13 as a coolant to condense gas supplied to the cell 42.
  • a system exemplifying the invention was constructed in which the volume of the reservoir 15 was approximately liters, the coolant 16 was liquid hydrogen at a temperature of 20.4 K. at standard pressure, the
  • target liquid was liquid hydrogen held at 15 p.s.i. above atmospheric by the supply 24 so that its boiling point was 23 K.
  • This system was successfully operated in conjunction with an electron beam having a maximum average intensity of about 15 microamps and a crosssectional area of 0.1 cm.
  • the beam was estimated to deposit approximately watts in the target liquid.
  • the beam had a maximum repetition rate of 360 p.p.s.
  • the heat exchanger 17 was made of solid copper.
  • a variety of target cells were made of 2 mil thick aluminum or nickel plated stainless steel, ranging up to 40 inches long for a horizontal rectangular cell and up to 12 inches in diameter for a large vertical cell. Convection currents on the order of 10 to 20 cm./sec. were generated with a beam having a horizontal dimension of 1 cm.
  • a target cell filled with a target liquid for positioning in the path of said beam said cell having a large total volume relative to the volume of liquid traversed by said beam to permit the occurrence of temperature differentials that will sustain convection currents;
  • heat transfer means for receiving heat from said convection currents for transfer from said target liquid to said coolant
  • said predetermined pressure applying means includes a constant closed volume supply reservoir for supplying the gaseous form of said target liquid to said target cell, and means responsive to the pressure in said supply reservoir for indicating the predetermined pressure at which said cell is filled with said target liquid.
  • said heat transfer means is comprised of a first heat conduction surface extending into contact with said target liquid, and a second heat conduction surface thermally connected to said first surface and extending into contact with said coolant.

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Particle Accelerators (AREA)

Description

Aug. 25, 1970 R. ANDERSON 3,525,228
NONBOILING LIQUID TARGET FOR A HIGH-ENERGY PARTICLE BEAM Filed Feb. 4, 1969 VENT TO ATMOSPHERE FROM LIQUID COOLANT SUPPLY PRESSURIZED TARGET GAS SUPPLY 34 BEAM 35 INVENTOR. ROBQRT LANDERSON ATTORNEY United States Patent O 3,525,228 NONBOILIN G LIQUID TARGET FOR A HIGH- ENERGY PARTICLE BEAM Robert L. Anderson, Palo Alto, Calif., assignor to the United States of America as represented by the United States Atomic Energy Commission Filed Feb. 4, 1969, Ser. No. 796,350 Int. Cl. F17c 13/00; F25b 19/00 US. Cl. 62-54 6 Claims ABSTRACT OF THE DISCLOSURE A differentially pressurized target system in which heat in a pressurized liquid hydrogen target is transferred by rapid convection currents to one side of a heat exchanger for dissipation on the other side in a liquid hydrogen reservoir that is maintained at atmospheric pressure. The rapid convection currents and the diiference in pressures in the target and reservoir permits cooling of the target by the liquid hydrogen in the reservoir to a temperature below the boiling point of the liquid target, thus inhibiting boiling of the target liquid upon impingement of a particle beam.
The invention disclosed herein was made under, or in, the course of Contract No. AT(04-3)-40O with the United States Atomic Energy Commission.
BACKGROUND OF THE INVENTION The present invention relates to nonboiling liquid targets for high-energy particle beams, and more particularly, it relates to a convectively cooled liquid target that is pressurized to raise its boiling temperature significantly above its operating temperature.
It is found desirable in high-energy physics research that is carried out in connection with high-energy particle accelerators, to bombard liquid targets with an accelerator beam to produce subatomic particles. The advantage of a liquid target is that it results in a greater number of interesting events than is obtained with the same target substance in a gaseous state. This is due to the greater density of a substance in its liquid state over its density in its gaseous state. It is necessary, however, for correct interpretation of detected actions of subatomic particles, to know the precise amount of target substance that the beam traverses. Thus, when using a liquid target, should the target boil, the amount of target liquid traversed by the beam is difficult to determine. For accurate interpretation of results, it is necessary, therefore, to maintain a liquid target in a nonboiling state in order to preserve the known density of the liquid. This is preferably accomplished without resort to complex and expensive cooling arrangements.
SUMMARY OF THE INVENTION In brief, the present invention pertains to a liquid target that may be positioned in the path of a high-energy particle beam of predetermined energy and intensity without boiling the target liquid. The target is comprised of a target cell filled with a target liquid maintained under pressure to raise its boiling point. The cell is shaped to contain a large total volume of target liquid, relative to the volume traversed by the beam, to provide sufiicient space for the creation of temperature differentials that will sustain convection currents upon heating the target liquid with the beam. A heat exchanger is exposed to the convection currents for transferring heat from the cell to a reservoir of coolant. The coolant is maintained at a pressure such that it boils at a temperature less than the boiling point of the target liquid, thereby maintaining the target liquid in a nonboiling state.
It is an object of the invention to simply, effectively, and economically inhibit boiling of a liquid target for a high-energy particle beam.
Another object is to dissipate beam energy deposited in a liquid target by pressurizing the target to raise its boiling point to a temperature level that is significantly above that of a coolant that is permitted to boil to dissipate the energy.
Another object is to transfer heat from a liquid target for a high-energy particle beam to a heat exchanger by means of convection currents.
Another object is todetect the liquid level of a liquid target for a high-energy particle beam with a constant volume source of pressurized gas.
Other objects and advantageous features of the invention will be apparent in a description of a specific embodiment thereof, given by way of example only, to enable one skilled in the art to readily practice the invention, and described hereinafter with reference to the accompanying drawing.
BRIEF DESCRIPTION OF THE DRAWING The figure is a diagram with portions broken away of a liquid target for a high-energy particle beam and a target cooling system, according to the invention.
DESCRIPTION OF AN EMBODIMENT Referring to the figure there is shown a target system including a target 12 comprised of a cell 13 filled with a target liquid such as liquid hydrogen. Hydrogen is often used as a target because it has a relatively simple nucleus that yields easily interpreted results. The cell 13 is suitably attached to one end of a reservoir 15 that is partially filled with a coolant 16 such as liquid hydrogen. A heat exchanger 17 is mounted between the reservoir 15 and the target 12 with fins 18 exposed to the coolant 16 and fins 18 exposed to the target liquid. The reservoir 15 may be filled with liquid coolant through a line 20 connected to a coolant supply (not shown). The coolant in the reservoir 15 may conveniently be held at atmospheric pressure through a vent line 22 to atmosphere. The target liquid in the cell 13 is held under pressure by means of a pressurized target gas supply 24 connected to the cell 13 over a line 26 which is passed through the coolant 16 for precooling the gas.
The target 12 and reservoir 15 are enclosed in a vacuum environment for thermal isolation by means of a scattering chamber 28 and a tank 30. The target 12 and the reservoir 15 may be moved relative to the tank 30 and scattering chamber 28 by means of a bellows 32 through which the lines 20, 22 and 26 extend; these lines may be flexibly connected by conventional means to their sources to permit movement of the target and reservoir.
In operation, the target system may be connected to the end of an accelerator 34 in which a high-energy particle beam 35 is developed. The target 12 may be centrally located in the path of the beam to enable collisions between the beam particles and the particles of the target 3 liquid for development of subatomic particles which then pass through a thin window 36 in the scattering chamber for detection with a particle detector (not shown) such as a Geiger counter, spectrometer, bubble chamber or spark chamber.
Impingement of the beam in the target 12 generates a large amount of heat in the liquid in the path of the particle beam. The cell 13 is arranged to have a relatively large total volume as compared to the volume of the target liquid traversed by the beam 35, typically 60 to l with the heat exchanger spaced on the order of four beam diameters from the beam path. This permits a substantial temperature gradient to be set up between the heated volume in the beam path and cooler outer regions of the cell. In particular, the target liquid in the region of the fins 18' is held substantially at the temperature of the coolant 16 by means of the heat exchanger 17. Convection currents 38 are generated thereby to carry heat from the region of the particle beam 35 to the fins 18' for transfer through the exchanger 17 to the fins 18 for dissipation in the coolant 16. Since the coolant 16 is held at atmospheric pressure, the added heat causes the coolant to boil to dissipate the heat. The vaporized liquid hydrogen is vented to atmosphere through the vent line 22, while additional liquid coolant may be automatically supplied through line 20 under control of conventional liquid level sensing means (not shown).
It has been found in practice that spreading the beam horizontally results in more effective target cooling and permits a substantial increase in maximum beam intensity; for example, an increase in the width of the beam by a factor of 2.2 permits the beam energy to be increased by a factor of ten.
The cell 13 may be filled with target liquid directly from the pressurized target gas supply 24 whereby the gas in the cell immediately condenses on the fins 18' upon entering the cell 13. Alternatively, the cell 13 could be filled by temporarily switching the line 26 to a liquid hydrogen supply to avoid delay in cooling the target.
When the cell 13 is filled from the gas supply 24, completion of filling may be detected with a pressure gauge 40. Since the volume of the cell 13 and the mass of gas in the supply 24 are easily determined, the drop in pressure due to the gas condensation necessary to fill the target may be calculated and the dropobserved on the gauge 40. Additionally, should the energy deposited by the beam in the target liquid rise above the capacity of the system to dissipate the energy and thereby cause the target liquid to boil, this condition will cause a rise in pressure in the gas supply that will be indicated on the gauge 40. Similarly, when the cell 13 is filled from a liquid supply and the gas supply 24 is subsequently switched to the line 26 to maintain the target liquid under pressure, any rise in pressure due to boiling of the target liquid also will be indicated on the gauge A dummy cell 42 may be suitably mounted on the lower end of the cell 13 and may be selectively raised into the path of the beam 35. A vacuum is provided within the cell 42 so that when it is in the beam path, the effect of the beam on the cell walls may be determined with particle detectors and taken into account when interpreting the results obtained with the cell 13 in the path of the beam.
Alternatively, the dummy cell 42 may be used as a second target cell and filled with hydrogen or deuterium, using the target liquid in the cell 13 as a coolant to condense gas supplied to the cell 42. Such an arrangement would be useful in an experiment requiring two different shaped target cells or for an experiment requiring a comparison between hydrogen and deuterium.
A system exemplifying the invention was constructed in which the volume of the reservoir 15 was approximately liters, the coolant 16 was liquid hydrogen at a temperature of 20.4 K. at standard pressure, the
target liquid was liquid hydrogen held at 15 p.s.i. above atmospheric by the supply 24 so that its boiling point was 23 K. This system was successfully operated in conjunction with an electron beam having a maximum average intensity of about 15 microamps and a crosssectional area of 0.1 cm. The beam was estimated to deposit approximately watts in the target liquid. The beam had a maximum repetition rate of 360 p.p.s. The heat exchanger 17 was made of solid copper. A variety of target cells were made of 2 mil thick aluminum or nickel plated stainless steel, ranging up to 40 inches long for a horizontal rectangular cell and up to 12 inches in diameter for a large vertical cell. Convection currents on the order of 10 to 20 cm./sec. were generated with a beam having a horizontal dimension of 1 cm.
With beam currents of 15 microamps and a horizontal dimension of 1 cm., calculations show that the change in the target liquid density is of the order of less than one percent.
While an embodiment of the invention has been shown and described, further embodiments or combinations of those described herein will be apparent to those skilled in the art without departing from the spirit of the invention or from the scope of the appended claims.
I claim:
1. In a nonboiling liquid target system in combination with a high-energy particle beam generating device, the combination of:
a target cell filled with a target liquid for positioning in the path of said beam said cell having a large total volume relative to the volume of liquid traversed by said beam to permit the occurrence of temperature differentials that will sustain convection currents;
means for applying a predetermined pressure to said target liquid for control of the temperature at which said target liquid boils;
a reservoir containing a liquid coolant for cooling said target liquid;
heat transfer means for receiving heat from said convection currents for transfer from said target liquid to said coolant; and
means for maintaining said coolant at a pressure that permits boiling of the coolant at a temperature that is less than the boiling point of said target liquid for dissipating the energy deposited by said beam in said target liquid.
2. The combination of claim 1 wherein said target liquid and said coolant have the same chemical composition, said coolant is maintained at atmospheric pressure, and said target liquid is maintained at a pressure higher than atmospheric pressure.
3. The combination of claim 1 wherein said predetermined pressure applying means includes a constant closed volume supply reservoir for supplying the gaseous form of said target liquid to said target cell, and means responsive to the pressure in said supply reservoir for indicating the predetermined pressure at which said cell is filled with said target liquid.
4. The combination of claim 1 wherein said heat transfer means is comprised of a first heat conduction surface extending into contact with said target liquid, and a second heat conduction surface thermally connected to said first surface and extending into contact with said coolant.
5. The combination of claim 1 wherein said coolant is liquid hydrogen and said target liquid is liquid hydrogen.
6. The combination of claim 1 further including means for thermally isolating said target system to permit heat transfer from said target liquid to said coolant only through said heat transfer means.
(References on following page) References Cited UNITED STATES PATENTS Sulfrian 6254 Reid 313-330 X Hanson 250-83.6 Zunick et a1. 313330 Leisegang 250-495 Salsig et a1 250-43 Ela et a1. 250-845 Justi 6248 X 6 OTHER REFERENCES A. W. DAVIS, JR, Assistant Examiner US. Cl. X.R.
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Cited By (9)

* Cited by examiner, † Cited by third party
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US4068495A (en) * 1976-03-31 1978-01-17 The United States Of America As Represented By The United States National Aeronautics And Space Administration Closed loop spray cooling apparatus
US4545218A (en) * 1984-09-17 1985-10-08 E. Reichert Optische Werke Ag Cryogenic fixation apparatus
US4737647A (en) * 1986-03-31 1988-04-12 Siemens Medical Laboratories, Inc. Target assembly for an electron linear accelerator
US4800060A (en) * 1982-08-03 1989-01-24 Yeda Research & Development Co., Ltd. Window assembly for positron emitter
US4955204A (en) * 1989-11-09 1990-09-11 The Regents Of The University Of California Cryostat including heater to heat a target
US5867546A (en) * 1993-10-04 1999-02-02 Hassal; Scott Bradley Method and apparatus for production of radioactive iodine
US6359968B1 (en) * 1999-02-12 2002-03-19 U.S. Philips Corporation X-ray tube capable of generating and focusing beam on a target
US20130187374A1 (en) * 2010-09-10 2013-07-25 Wartsila Finland Oy Arrangement for connecting a pipe to a lng tank
US10249398B2 (en) 2015-06-30 2019-04-02 General Electric Company Target assembly and isotope production system having a vibrating device

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US2821650A (en) * 1951-09-28 1958-01-28 Gen Electric Method of obtaining vacuum tightness in cast metal structures of thin section and resulting products
US2858444A (en) * 1954-07-14 1958-10-28 Siemens Ag Object-holding device for electron microscopes
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Cited By (11)

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US4068495A (en) * 1976-03-31 1978-01-17 The United States Of America As Represented By The United States National Aeronautics And Space Administration Closed loop spray cooling apparatus
US4141224A (en) * 1976-03-31 1979-02-27 The United States Of America As Represented By The Administrator Of The National Aeronautics And Space Administration Closed loop spray cooling apparatus
US4800060A (en) * 1982-08-03 1989-01-24 Yeda Research & Development Co., Ltd. Window assembly for positron emitter
US4545218A (en) * 1984-09-17 1985-10-08 E. Reichert Optische Werke Ag Cryogenic fixation apparatus
US4737647A (en) * 1986-03-31 1988-04-12 Siemens Medical Laboratories, Inc. Target assembly for an electron linear accelerator
US4955204A (en) * 1989-11-09 1990-09-11 The Regents Of The University Of California Cryostat including heater to heat a target
US5867546A (en) * 1993-10-04 1999-02-02 Hassal; Scott Bradley Method and apparatus for production of radioactive iodine
US6359968B1 (en) * 1999-02-12 2002-03-19 U.S. Philips Corporation X-ray tube capable of generating and focusing beam on a target
US20130187374A1 (en) * 2010-09-10 2013-07-25 Wartsila Finland Oy Arrangement for connecting a pipe to a lng tank
US9664317B2 (en) * 2010-09-10 2017-05-30 Wartsila Finland Oy Arrangement for connecting a pipe to a LNG tank
US10249398B2 (en) 2015-06-30 2019-04-02 General Electric Company Target assembly and isotope production system having a vibrating device

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