US86248A - Improvement in the manufacture of oxygen-gas - Google Patents

Improvement in the manufacture of oxygen-gas Download PDF

Info

Publication number
US86248A
US86248A US86248DA US86248A US 86248 A US86248 A US 86248A US 86248D A US86248D A US 86248DA US 86248 A US86248 A US 86248A
Authority
US
United States
Prior art keywords
steam
oxygen
retorts
pipe
gas
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
Publication date
Application granted granted Critical
Publication of US86248A publication Critical patent/US86248A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • C01B3/02Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
    • C01B3/06Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents
    • C01B3/068Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents the hydrogen being generated from the water as a result of a cyclus of reactions, not covered by groups C01B3/063 or C01B3/105
    • 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
    • Y02E60/36Hydrogen production from non-carbon containing sources, e.g. by water electrolysis

Definitions

  • Figure 2 is a plan or top view thereof.
  • Figure 3 is a detached section of the exhauster, which may be used in carrying cut'my invention.
  • the mangauate of soda is heated in a nest of retorts, steam is passed through these retorts from a steam-boiler, then the steam is shut olf,and currents of air are passed through the retorts, by a suitable air-pump or fanfblower.
  • the partial vacuum in the retorts is produced by jets of steam, on the principle of Giiiards injector, and the steam requisite or this purpose is steam-jets, both the steam-supply and the suctionpipes being connected by a three-way cock, so that, by the simple act of closing the steam-supply pipe, the suction-pipe is opened, and vice persa, and thereby the operation ofthe apparatus is materially facilitated.
  • the letter A represents a steam-boiler, which connects, by a pipe, B, with the three-way cock C, 4from which branch ofi' the steam-supply pipe I? and the suc tion or exhaust-pipe E, as clearly shown .in fig. 1.
  • the steani-supply pipe D connects, by branch-pipes a, with the several retorts F, and from the upper parts of the retcrts extend branch-pipes b, which connect with the suction-pipe E.
  • Suitable check-valves o1' vacuum-yalves e admit the external air into the retorts, as soon as the pressure in the same has been reduc-cd below the atmospheric pl'GSSlfll'C.
  • the oxygen-gas when disengaged from the manganate of soda in the retort-s F, passes oli" with the steam through the pipe G, which leads to the condenser H, and in this condenser the steam is condensed, and the oxygen-gas passes through the pipe I into the gasholdcr or receiver J.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Health & Medical Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Inorganic Chemistry (AREA)
  • Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)

Description

@time @sie Lette/rs Patent No. 86,248,
dated January 26, 1869.
IMPROVEMENT IN THE MANUFACTURE OIE' OXYGEN-GAS.
The Schedule referred to in these Letters Patent and making part of the. name.
To all whom l'it mayI concern Be it known that I, OnvILLE M. PHILLIPS, of the city, county, and State of N ew York, have invented a new and useful Improvement in the Manufacture of Oxygen-Gas; and I do hereby declare the followingto he a full, clear, and exact description thereof, which will enable those skilled in the art to make and use the same, reference being had to the accompanying drawing, forming part of this specification, in which drawing- Figure 1 represents a sides view of this invention.
Figure 2 is a plan or top view thereof.
Figure 3 is a detached section of the exhauster, which may be used in carrying cut'my invention.
Similar letters indicate corresponding parts` his invention is intended an improvement on the process and apparatus of Motay and lNIai-echal for producing oxygen-gas from alkaline manganates.
This process, which has only quite recently been in trodnced in the 'United States, has originated in the ascertaining of two facts:
First, that if a current of ster-nn over an nllfa line manganatc, by preiinencc, manganate oi' sollst, it will abstract and carry aways considerable portion of the oxygen, which can afterwards be sepa-rated and secured by the simple condensation of the steam; and
Second, that il' a current of air is passed over the partially-deoxidized compound, said compound will recover from the air the oxygen it had lost. lhen this is done, a new current of steam may be employed to take off a second portion of inrygen, to be followed by a new current of air to restore it again; and so ou in definitely.
In carrying out this process, the mangauate of soda is heated in a nest of retorts, steam is passed through these retorts from a steam-boiler, then the steam is shut olf,and currents of air are passed through the retorts, by a suitable air-pump or fanfblower.
This operation is attended with certain disadvantages, which I have sought to overcome by my invention.
In the first place, .the shutting o" of the current of steam, and the subsequent starting of the air-forcing apparatus, and'then the stopping of the air-forcing apparatus, and the letting on of the current of steam, require constant attention of an 'experienced mechanic.
Secondly, the steam, which still fills the upper parts of the retorts, when the currents of cold air are admitted, condenses at least in part, and' the wat-er of condensation accumulates in said retorts, and obstructs the operation.-
These difficulties I have overcome by creatingr and maintaining in the retorts, after -the steam has been shut off, a partial vacuum, whereby the steam still rctained in said retorts is caused to pass ofi' through the suctionpipes, and, at the Sametime, the requisite currents of air are caused to pass through said retorts by suction.
Furthermore, the partial vacuum in the retorts is produced by jets of steam, on the principle of Giiiards injector, and the steam requisite or this purpose is steam-jets, both the steam-supply and the suctionpipes being connected by a three-way cock, so that, by the simple act of closing the steam-supply pipe, the suction-pipe is opened, and vice persa, and thereby the operation ofthe apparatus is materially facilitated.
In the accompanying 'drawing- The letter A represents a steam-boiler, which connects, by a pipe, B, with the three-way cock C, 4from which branch ofi' the steam-supply pipe I? and the suc tion or exhaust-pipe E, as clearly shown .in fig. 1.
The steani-supply pipe D connects, by branch-pipes a, with the several retorts F, and from the upper parts of the retcrts extend branch-pipes b, which connect with the suction-pipe E.
In the interior of this suction-pipe, I place thc con- .ical nozzles c and spout-s d, (see iig. 3,) so that-the steam, in passing through said pipe, will create a partial vacuum in each of the retorts.
Suitable check-valves o1' vacuum-yalves e admit the external air into the retorts, as soon as the pressure in the same has been reduc-cd below the atmospheric pl'GSSlfll'C.
The oxygen-gas, when disengaged from the manganate of soda in the retort-s F, passes oli" with the steam through the pipe G, which leads to the condenser H, and in this condenser the steam is condensed, and the oxygen-gas passes through the pipe I into the gasholdcr or receiver J.
' After the steam has acted a sufficient length of time on the manganate of soda in the retorts, the th1ee-\vay A cock O is turned, and thereby the supply-pipe D is shut oli, and the suction-pipe E is opened.
By the steam passing through this pipe, a partial vacuum is created in each retort, the steam still retained in suchretorts is sucked out, and the external air enters through the vacuum-valves e, so as to restore the oxygen previously abstracted from the manga-nate in the retorts.
By these means, the apparatus required for the manufacture of oxygen, and the operation of the same, are simplified, and, by exhausting the steam still remaining in the retorts after the steam-pipe has been shut oli, a decided advantage is obtained over the old process, in regard to the yield of oxygen.
I distinctly disclaim everything shown and described in the process of Motay and Marechal; but having thus described my invention,
tVhat I claim as new, and ters Patent, is-
1. The within-described process of facilitating the manufacture of oxygen-gas, by creating in the retorts containing the alkaline manganates, or other material from which the oxygen is extracted, at certain intervals, a partial vacuum, substantial-ly in the manner described.
2. The arrangement of a suction-pipe, E, in combination with the steam-pipe D and retorts F, substantially as and for the purpose set forth.
ORVILLE M. PHILLIPS.
desire to secure by Let- Witnesses W. HAUFF,
taken fromthe same steam-boilerewhich supplies the ERNEST F. KAsrnNnnnEn.
US86248D Improvement in the manufacture of oxygen-gas Expired - Lifetime US86248A (en)

Publications (1)

Publication Number Publication Date
US86248A true US86248A (en) 1869-01-26

Family

ID=2155737

Family Applications (1)

Application Number Title Priority Date Filing Date
US86248D Expired - Lifetime US86248A (en) Improvement in the manufacture of oxygen-gas

Country Status (1)

Country Link
US (1) US86248A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4089938A (en) * 1977-07-15 1978-05-16 Hudson Engineering Corporation Process for recovering oxygen from air

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4089938A (en) * 1977-07-15 1978-05-16 Hudson Engineering Corporation Process for recovering oxygen from air

Similar Documents

Publication Publication Date Title
US86248A (en) Improvement in the manufacture of oxygen-gas
TWI727972B (en) Process and plant for separating a gas mixture
US489147A (en) Evaporating apparatus
JP2898741B2 (en) Treatment method of exhaust gas containing organic vapor
NO161315B (en) PROCEDURE FOR MANUFACTURING UREA.
US835886A (en) Process of making potable and aerated water.
JPH0542287B2 (en)
US1922682A (en) Method of converting potassium chloride into potassium sulphate
AU2009225953B2 (en) Method of concentrating a Bayer process liquor
US85174A (en) The extract of bark for tanning
US94969A (en) Improved method op purifying- nitric acid
US12616A (en) Of white lead by precipitation
US219411A (en) Improvement in processes and apparatus for granulating and desiccating milk, sugar
US818858A (en) Ammonia-still.
US129114A (en) Improvement in treating sugars
US313177A (en) Manufacture of tanning extract
US918997A (en) Process for producing, from straw, a liquid suitable for the production of alcohol.
CN220237773U (en) Paramydehyde continuous film distillation plant
US254916A (en) Process
US746850A (en) Turpentine-still.
US101035A (en) Improved apparatus for purifying water for the manufacture of ice
US375622A (en) Vinegar apparatus
US88222A (en) Improved apparatus and process for extracting oil from vegetable and other matter
Seth The activation of pancreatic juice by enterokinase
US441621A (en) Apparatus for concentrating solutions and extracting solids therefrom