US1056043A - Process of separating mixed liquefied gases. - Google Patents

Process of separating mixed liquefied gases. Download PDF

Info

Publication number
US1056043A
US1056043A US69800112A US1912698001A US1056043A US 1056043 A US1056043 A US 1056043A US 69800112 A US69800112 A US 69800112A US 1912698001 A US1912698001 A US 1912698001A US 1056043 A US1056043 A US 1056043A
Authority
US
United States
Prior art keywords
liquefied gases
liquid
nitrogen
air
mixed liquefied
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
Application number
US69800112A
Inventor
Abraham Cressy Morrison
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to US69800112A priority Critical patent/US1056043A/en
Application granted granted Critical
Publication of US1056043A publication Critical patent/US1056043A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/48Treatment of water, waste water, or sewage with magnetic or electric fields
    • C02F1/481Treatment of water, waste water, or sewage with magnetic or electric fields using permanent magnets

Definitions

  • WITNESSES UNITED STATESPAETEN T OFFICE WITNESSES UNITED STATESPAETEN T OFFICE.
  • This process is especially designed for the production of gaseous oxygen and nitrogen from liquid air, and is based onthe facts that oxygen is a paramagnetic element and that its magnetic susceptibility is higher than that of nitrogen.
  • the process comprises the steps of placing the liquid air or other mixture of liquefied gases within a strong magnetic field, and then allowing the liquid to become V heated to a temperature slightly above the boiling-point of the nitrogen, or other more Volatile and less magnetic component, Whereuponthe nitrogen distils off, the oxygen, or other component, remaining by reason both of its relative involatility and of thetractive efiectof the magnetic field.
  • FIG. 1 Suitable apparatus for carrying out the process is shown in the accompanying drawing, in which the several figures are diagrammatic side elevations, showing a doublewalled vacuum vessel. containing the liquefied gas, and the poles of electromagnets in proximity thereto.
  • Figure 1 illustrates a vessel 1 having inner and outer concentric walls 2, 3, with "an intermediate space 4 from which the air has been exhausted.
  • a tap 5 extends from the lower end of the vessel.
  • the vessel is placed between the opposed pole-pieces 6, 7 of a powerfulelectromagnet 8.
  • the liquid air or other liquefied gas 91in the vessel is shown in the position whichit assumes in the magnetic field, and is indicated as haw ing a gradually-increasing density toward the bottom, by reason of the partial evaporation of the nitrogen and of the pull of the magnetic field. 4
  • the apparatus illustrated in Fig. 2 employs a pole-piece 10 of an electromagnet l1, placed directly beneath the base of the vessel. Means for creating a magnetic field at the. sides of or around the tube may also be used, such as the dotted lines.
  • the apparatus of Fig. 3 is identical with that of Fig. l, as to the vessel and electromagnet.
  • This means consists of a large number of small pieces of iron 12, supported and spaced apart in regular manner by intermediate pieces 13 of non-magnetic material, such as short copper wires.
  • the liquid air is placed in the vessel and the electromagnet or magnets are energized.
  • the oxygen is strongly attracted by the magnet poles, and the surface of the liquid assumes about the contour shown.
  • the nitrogen having the lower boiling-point and be ing less strongly attracted by the pole-pieces, distils ofi, while the less volatile and more pole-pieces indicated by .magnetic oxygen remains behind and is drawn off through the tap 5.
  • I claim p 1 The process of separating or fractionating mixed liquefied gases, which consists in-subjecting the liquid to a magnetic field while heated to a temperature above the boiling-point of the more volatile and less magnetic component.

Description

I A. O. MORRISON. PROCESS OF SBPARATING MIXED LIQUEFIED GASES.
APPLICATION FILED MAY 17, 1912.
Patented Mar. 18, 1913.
WITNESSES UNITED STATESPAETEN T OFFICE.
\/ ABRAHAM CRES-SY MORRISON, OF CHICAGO. ILLINOIS.
PROCESS OF SEPARATING MIXED LIQUEFIED GASE S.
Specification of Letters Patent. Patented B131, 18, 1913,
Application filed May 17, 1912. Serial No. 698,001.
i To all whom it may concern Be it known that I, ABRAHAM CREssY MORRISON, a citizen of the United States, residing atChicago, in the county of Cook and State of Illinois, have invented certain new and useful Improvements in Processes 0f- Separating Mixed Liquefied Gases, of which the following is a specification.
This process is especially designed for the production of gaseous oxygen and nitrogen from liquid air, and is based onthe facts that oxygen is a paramagnetic element and that its magnetic susceptibility is higher than that of nitrogen.
The process comprises the steps of placing the liquid air or other mixture of liquefied gases within a strong magnetic field, and then allowing the liquid to become V heated to a temperature slightly above the boiling-point of the nitrogen, or other more Volatile and less magnetic component, Whereuponthe nitrogen distils off, the oxygen, or other component, remaining by reason both of its relative involatility and of thetractive efiectof the magnetic field.
Suitable apparatus for carrying out the process is shown in the accompanying drawing, in which the several figures are diagrammatic side elevations, showing a doublewalled vacuum vessel. containing the liquefied gas, and the poles of electromagnets in proximity thereto.
Figure 1 illustrates a vessel 1 having inner and outer concentric walls 2, 3, with "an intermediate space 4 from which the air has been exhausted. A tap 5 extends from the lower end of the vessel. The vessel is placed between the opposed pole-pieces 6, 7 of a powerfulelectromagnet 8. The liquid air or other liquefied gas 91in the vessel is shown in the position whichit assumes in the magnetic field, and is indicated as haw ing a gradually-increasing density toward the bottom, by reason of the partial evaporation of the nitrogen and of the pull of the magnetic field. 4
The apparatus illustrated in Fig. 2 employs a pole-piece 10 of an electromagnet l1, placed directly beneath the base of the vessel. Means for creating a magnetic field at the. sides of or around the tube may also be used, such as the dotted lines.
The apparatus of Fig. 3 is identical with that of Fig. l, as to the vessel and electromagnet. In the lower end of the vessel and within the body of liquid air is placed means for carrying and diffusing the lines of magnetic flux passing between the pole-pieces 6, 7. This means consists of a large number of small pieces of iron 12, supported and spaced apart in regular manner by intermediate pieces 13 of non-magnetic material, such as short copper wires.
In using either type of apparatus illustrated, the liquid air is placed in the vessel and the electromagnet or magnets are energized. The oxygen is strongly attracted by the magnet poles, and the surface of the liquid assumes about the contour shown. As the liquid air becomes heated, the nitrogen, having the lower boiling-point and be ing less strongly attracted by the pole-pieces, distils ofi, while the less volatile and more pole-pieces indicated by .magnetic oxygen remains behind and is drawn off through the tap 5. While for the purpose ofdistinctness the portion evaporating has been termed nitrogen and' the portion remaining oxygen, in practice more or less of the oxygen will escape with the nitrogen and more or less of the nitrogen will remain with the oxygen, the process serving, however, to produce two fractions, one of' which has a'lower and the other a higher content of oxygen than air.'
I claim p 1. The process of separating or fractionating mixed liquefied gases, which consists in-subjecting the liquid to a magnetic field while heated to a temperature above the boiling-point of the more volatile and less magnetic component.
2. The process of separating liquefied air into portions of high and lower oxygencontent than air, which consists in subjecting the liquid to a magnetic field while heated to a temperature above the boilingpoint of nitrogen.
3. The process of separating orfractionating mixed liquefied gases, which consists in placing in the liquid a number of separate pieces of paramagnetic metal, and then subjecting the liquid to a magnetic field while heated to a temperature above the boiling-point of the more volatile and less magnetic component. I
4. The process of separating liquefied air into portions of higher and lower oxygencontent than air, which consists in placing in the liquid a number of separate pieces of paramagnetic metal, and then subjecting the liquid to a magnetic field while heated 10 to a temperature above the boiling-point of I nitrogen.
In testimon whereof I aflix my signature 'in presence 0 two witnesses.
US69800112A 1912-05-17 1912-05-17 Process of separating mixed liquefied gases. Expired - Lifetime US1056043A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US69800112A US1056043A (en) 1912-05-17 1912-05-17 Process of separating mixed liquefied gases.

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US69800112A US1056043A (en) 1912-05-17 1912-05-17 Process of separating mixed liquefied gases.

Publications (1)

Publication Number Publication Date
US1056043A true US1056043A (en) 1913-03-18

Family

ID=3124298

Family Applications (1)

Application Number Title Priority Date Filing Date
US69800112A Expired - Lifetime US1056043A (en) 1912-05-17 1912-05-17 Process of separating mixed liquefied gases.

Country Status (1)

Country Link
US (1) US1056043A (en)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2486684A (en) * 1946-04-10 1949-11-01 Socony Vacuum Oil Co Inc Distillation process using radiofrequency heating
US3174294A (en) * 1958-12-19 1965-03-23 Air Reduction Oxygen dispensing
US4027494A (en) * 1975-09-12 1977-06-07 Nasa Low gravity phase separator
US4049398A (en) * 1976-05-28 1977-09-20 Vaseen Vesper A Separating oxygen from the air by means of dissolving air in a nonmagnetic, inert liquid and then paramagnetically collecting the oxygen from the liquid
US4203740A (en) * 1978-09-11 1980-05-20 Vesper Albert Vaseen Oxygen production by paramagnetic removal of magnetized oxygen from liquid air
US6159271A (en) * 1998-09-11 2000-12-12 The Boeing Company Method and system for orienting diamagnetic liquid with respect to a gas in a low gravity environment
US20170241708A1 (en) * 2016-02-24 2017-08-24 Hatem I. Zeine System and a method to extract oxygen from air
DE102021109146B4 (en) 2021-04-13 2023-03-30 Institut für Luft- und Kältetechnik gemeinnützige Gesellschaft mbH Magnet module and device for magnet-based separation of an oxygen-containing mixed fluid and method for producing an oxygen-enriched useful gas by the device

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2486684A (en) * 1946-04-10 1949-11-01 Socony Vacuum Oil Co Inc Distillation process using radiofrequency heating
US3174294A (en) * 1958-12-19 1965-03-23 Air Reduction Oxygen dispensing
US4027494A (en) * 1975-09-12 1977-06-07 Nasa Low gravity phase separator
US4049398A (en) * 1976-05-28 1977-09-20 Vaseen Vesper A Separating oxygen from the air by means of dissolving air in a nonmagnetic, inert liquid and then paramagnetically collecting the oxygen from the liquid
US4203740A (en) * 1978-09-11 1980-05-20 Vesper Albert Vaseen Oxygen production by paramagnetic removal of magnetized oxygen from liquid air
US6159271A (en) * 1998-09-11 2000-12-12 The Boeing Company Method and system for orienting diamagnetic liquid with respect to a gas in a low gravity environment
US20170241708A1 (en) * 2016-02-24 2017-08-24 Hatem I. Zeine System and a method to extract oxygen from air
US11009292B2 (en) * 2016-02-24 2021-05-18 Zeine, Inc. Systems for extracting oxygen from a liquid
US20210231368A1 (en) * 2016-02-24 2021-07-29 Zeine, Inc. Systems For Extracting Oxygen From A Fluid
DE102021109146B4 (en) 2021-04-13 2023-03-30 Institut für Luft- und Kältetechnik gemeinnützige Gesellschaft mbH Magnet module and device for magnet-based separation of an oxygen-containing mixed fluid and method for producing an oxygen-enriched useful gas by the device

Similar Documents

Publication Publication Date Title
Bitter On inhomogeneities in the magnetization of ferromagnetic materials
US1056043A (en) Process of separating mixed liquefied gases.
Shibayama et al. Disordered magnetism at the metal-insulator threshold in nano-graphite-based carbon materials
KR890013968A (en) Particle Sources for Reactive Ion Beam Etching or Plasma Attachments
Constant The magnetic properties of certain Pt-Co and Pd-Co alloys
US4110222A (en) Apparatus for separating magnetizable particles from a fluid
GB814269A (en) Method and device for increasing the combustion efficiency of liquid fuels
Nakatani et al. Iron-nitride magnetic fluids prepared by plasma CVD technique and their magnetic properties
JP3794535B2 (en) Ferromagnetic force field generating coil for material levitation or magnetic separation
US1812505A (en) Means for conveying magnetic material
GB191229383A (en) Process of Separating Mixed Liquefied Gases.
US1273929A (en) Method of treating gases.
Edwards The magnetic properties of evaporated nickel and iron films
US1364136A (en) Process of and apparatus for treating mixed gases
Young et al. Purity of Helium Permeating through Quartz into a Vacuum System
US1937216A (en) Electromagnet
JPS60106966A (en) Confronting target type sputtering apparatus
GB685920A (en) Improvements in the measurement of the proportion of a paramagnetic gas, in particular oxygen, contained in a gaseous mixture
GB307044A (en) Improvements in ironless induction furnaces
GB303065A (en) Electrodynamic movement of fluid metals particularly for refrigerating machines
JPS648624A (en) Plasma apparatus
US2000025A (en) Vibrator
SU895515A1 (en) Apparatus for magnetic separation of materials
RU2131165C1 (en) Magnetic levitation device
JPS5613055A (en) Magnetic separator