[go: up one dir, main page]

US1286135A - Apparatus for subjecting gases to the action of heat and pressure. - Google Patents

Apparatus for subjecting gases to the action of heat and pressure. Download PDF

Info

Publication number
US1286135A
US1286135A US16471217A US16471217A US1286135A US 1286135 A US1286135 A US 1286135A US 16471217 A US16471217 A US 16471217A US 16471217 A US16471217 A US 16471217A US 1286135 A US1286135 A US 1286135A
Authority
US
United States
Prior art keywords
pressure
chamber
reaction
gases
heat
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
US16471217A
Inventor
Edward E Somermeier
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 US16471217A priority Critical patent/US1286135A/en
Application granted granted Critical
Publication of US1286135A publication Critical patent/US1286135A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J3/00Processes of utilising sub-atmospheric or super-atmospheric pressure to effect chemical or physical change of matter; Apparatus therefor
    • B01J3/04Pressure vessels, e.g. autoclaves
    • B01J3/046Pressure-balanced vessels

Definitions

  • My invention relates to a process and apparatus for subjecting gases, vapors or vaporized liquid simultaneously to the action of heat and pressure.
  • I provide for efiecting the primary heating within a reaction chamber exposed both interiorly and exteriorly to the pressure at which it is desired that the reaction take place, surrounding said reaction chamber by a further chamber adapted to withstand interiorly the high pressures used.
  • This I efi'ect by inclosing the heated reaction chamber within a strong pressure chamber with the interior Specification of Letters Patent.
  • My invention is illustrated by the accom panying drawing, in which 1 indicates a strong steel or other metal chamber provided with a suitable cover 2 attached removably thereto in suitable pressure resisting manner, as for example, by bolts 3 assing through flanges 4 and 5 of the b0 y of the chamber and of its top respectively and the interposed gaskets 7.
  • I inclose the heating chamber proper, which in the form illustrated is constructed of side members 8, bottom member 9 and top member 10 and supported therein by any suitable means, as, for example, the standards 30.
  • Each of these members forming the interior reaction chamber may be suitably constructed of refractory mateh'ial, which may be supported or reinforced by an external armor 12 and fitted together in any suitable manner, as for example, by the chamfered edges 13 and bolts 14 passing through the flanges 15 of the external armor of the elements of the chamber.
  • the interior of the chamber is provided in the case illustrated with suitable electric heating means 16, to which leads 17, 17 pass from without the external pressure chamber.
  • An inlet pipe 18 provided with a suitable valve 19 passes through the external pressure chamber into the inclosed heating chamber for the admission thereinto of the gases or vapors which are to be subjected to the reaction heat and pressure.
  • An outlet pipe 20 provided with a suitable pressure valve 21 leads from within the internal heating chamber out of the external "pressure chamber to any suitable condenser or receiving device (not shown).
  • the outlet pipe 20 is provided without the chamber, but within the pressure chamber with an opening 22,
  • a suitable pressure valve 26 for the "outlet of fluids which may condense within the ressure chamber.
  • the temperature of. the lieating chamber may be observed by means of a suitable pyrometer 27, and the pressure prevailing in the device may be measured by a suitable manometer 28 commumcating through pipe 29 with the interior of the .outer chamber.
  • the gases or fluids. which are to be treated are forced through pipe 18 into the interior of the internal heated chamber. Here they are subjected to the heating effect of the heating elements 16, whereby, in
  • a temperature as high as 1200 to 1400 degrees C. may be produced. It is obvious that, if desired, higher temperatures than this may be attained by the use of other suitable heating means. While undergoing this high temperature the gases or vapors are simultaneously subjected to high pressure, which may be that produced by the action of the heat on the gases or va ors themselves, or may be produced by orcing reaction products, inert gases, or the like into the external reaction chamber. By reason of the free communication between the internal and external chambers through the opening 22 the pressure within the two chambers remains identical. The heating, however, is confined to the interior of the heated reaction chamber,
  • This pressure may obviously be a ove the limits of safe operation of other devices previously known, and may be from 300 to 400 pounds per square inch to many times this pressure, being limited only by the pressures which the external pressure chamber may be built to withstand.
  • An apparatus for effecting reactions under heat and pressure comprising a reaction chamber, means for heating said chamber interiorly, a pressure chamber surrounding the same, means whereby free communication is established between the interiors of said reaction chamber and of said pressure chamber, means for maintaining the desired pressure within the pressure chamber and means for supplying material to be treated to the interior of said reaction chamber and for withdrawing products of reaction from the reaction and pressur chamber.
  • An apparatus for effecting reactions 100 under heat and pressure comprising a metallic pressure chamber, a refractory reaction chamber supported therein, heating-means Within said reaction chamber, means for supplying material to be treated to said reaction chamber and means for establishing free communication between the interiors of the reaction and pressure chambers.
  • An apparatus for eifecting reactions under heat and pressure comprising a metallic pressure chamber, a refractory reaction chamber supported therein, electric heating means within said reaction chamber, means for supplying material to be treated to the interior of said reaction chamber, an outlet pipe from the reaction chamber to the exterior of the pressure chamber, said pipe being provided within the pressure chamber with an opening whereby free communication is established between the interiors of the rewithin said reaction chamber, means for sup- In testimony whereof, I have signed this plying material to be treated to said reacspecification in the presence of two subscribtion chamber and for withdrawing products ing witnesses.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)

Description

E. E. SOMERMEIER.
APPARATUS FOR SUBJECTING GASES TO THE ACTION 0F HEAT AND PRESSURE. APPLICATION HLED APR. 26. 191;.
1 ,286, 1 35. Patented Nov. 26, 1918.
IIIIIIIIIIIlI/I 1/11 ///////////11// 1/0/1101 IIIIIII IIIIIIIIII I IIlllIIlI/IIII 7 llIlII/I l/lII/I/IIII Ill/IIIII g Ill/Illl/II/ll/l/l/IIII III I [III/11 114174 5v I UNITED STATES PATENT OFFICE.
EDWARD E. SOMERMEIER, 0F EN GLEWOOD, FLORIDA.
APPARATUS FOR SUBJEC'IING GASES TO THE ACTION OF HEAT AND IERESSURTIT Application filed April 26, 1917.
To all whom-it may concern:
Be' it known that I, EDWARD E. SOMER- MEIER, of Englewood, in'the county of Manatee and State of Florida, have invented certain new and useful Improvements in Apparatus for Subjecting Gases to the Action of Heat and Pressure; and I do hereby declare the following to be a full, clear, and exact description of the invention, such as will enable others skilled in the art to which it appertains to make and use the same.
My invention relates to a process and apparatus for subjecting gases, vapors or vaporized liquid simultaneously to the action of heat and pressure.
In many reactions of modern industrial and research chemistry it is necessary or desirable to subject gases, vapors or vaporized liquids simultaneously to a high temperature and to a high pressure, as for example, in the treatment of crude petroleum or high boiling point hydrocarbons for the purpose of cracking the same into aliphatic or aromatic compounds, for the treatment of natural gas, the production of reactions between nitrogen and oxygen or their compounds, for determining the efiects' of catalytic reagents in such reactions as those above mentioned, and for many other chemical reactions.
Research in these and similar reactions, and the industrial application of such reactions has hitherto been greatly restricted by reason of the difficulties arising in the construction of furnaces which will withstand the effects of the extremely high temperatures and pressures involved, and will at the same time be simple in construction, easily operated, and readily taken apart and repaired. The subject of the present invention is a mode of operation and a construc- 7 tion whereby these features will be attained.
In accordance with my invention I provide for efiecting the primary heating within a reaction chamber exposed both interiorly and exteriorly to the pressure at which it is desired that the reaction take place, surrounding said reaction chamber by a further chamber adapted to withstand interiorly the high pressures used. This I efi'ect by inclosing the heated reaction chamber within a strong pressure chamber with the interior Specification of Letters Patent.
Patented Nov. 26, 1918.
Serial No. 164,712.
- inclosing pressure chamber are identical.
My invention is illustrated by the accom panying drawing, in which 1 indicates a strong steel or other metal chamber provided with a suitable cover 2 attached removably thereto in suitable pressure resisting manner, as for example, by bolts 3 assing through flanges 4 and 5 of the b0 y of the chamber and of its top respectively and the interposed gaskets 7. Within this chamber, which forms the external, pressure rcsisting chamber, I inclose the heating chamber proper, which in the form illustrated is constructed of side members 8, bottom member 9 and top member 10 and supported therein by any suitable means, as, for example, the standards 30. Each of these members forming the interior reaction chamber may be suitably constructed of refractory mateh'ial, which may be supported or reinforced by an external armor 12 and fitted together in any suitable manner, as for example, by the chamfered edges 13 and bolts 14 passing through the flanges 15 of the external armor of the elements of the chamber. The interior of the chamber is provided in the case illustrated with suitable electric heating means 16, to which leads 17, 17 pass from without the external pressure chamber. An inlet pipe 18 provided with a suitable valve 19 passes through the external pressure chamber into the inclosed heating chamber for the admission thereinto of the gases or vapors which are to be subjected to the reaction heat and pressure. An outlet pipe 20 provided with a suitable pressure valve 21 leads from within the internal heating chamber out of the external "pressure chamber to any suitable condenser or receiving device (not shown). The outlet pipe 20 is provided without the chamber, but within the pressure chamber with an opening 22,
whereby free communication is established 'a suitable pressure valve 26 for the "outlet of fluids which may condense within the ressure chamber. The temperature of. the lieating chamber may be observed by means of a suitable pyrometer 27, and the pressure prevailing in the device may be measured by a suitable manometer 28 commumcating through pipe 29 with the interior of the .outer chamber. l v
In operation the gases or fluids. which are to be treated are forced through pipe 18 into the interior of the internal heated chamber. Here they are subjected to the heating effect of the heating elements 16, whereby, in
the case of resistance coils, a temperature as high as 1200 to 1400 degrees C. may be produced. It is obvious that, if desired, higher temperatures than this may be attained by the use of other suitable heating means. While undergoing this high temperature the gases or vapors are simultaneously subjected to high pressure, which may be that produced by the action of the heat on the gases or va ors themselves, or may be produced by orcing reaction products, inert gases, or the like into the external reaction chamber. By reason of the free communication between the internal and external chambers through the opening 22 the pressure within the two chambers remains identical. The heating, however, is confined to the interior of the heated reaction chamber,
into which all of the gases treated are forced reaction cham er, being comparatively cool,
but may be cooled by contact with the air or, if desired, may even be water cooled. The desired pressure is maintained within the system by suitable adjustment of the pressure valves of the various outlet pipes.
The gases or va ors enterin the heated reaction chamber t rough the inlet pipe 18 for the greater. part pass out through the main outlet pipe 20, after having been subj ected to the reaction temperature and pressure. That portion of the gases and vapors which, after having passed through the re-' action chamber, passes into the external pressure chamber and aid there in maintaining the pressure in the system, escape as gases through the outlet ipe 23, or as condensed liquids, through the outlet ipe 25. This pressure may obviously be a ove the limits of safe operation of other devices previously known, and may be from 300 to 400 pounds per square inch to many times this pressure, being limited only by the pressures which the external pressure chamber may be built to withstand. As this chamber is not required'to withstand the high heat prevailing in the internal reaction chamber, it is obvious that the pressure strains which it will withstand are much greater than would be the case if it were also subjected to the high heat of the reaction. Furthermore it is obvious that the inner chamber, which is subjected to the extreme heat of the reaction, is not subject to the pressure strains, and is consequently less liable to deterioration and will require fewer repairs than would be the case were it also-subjected thereto. It is also apparent that the device is constructed so that the parts thereof are readily accessible and may be easily removed and repaired. 1
It is apparent that thedetails of structure, proportions, shape, etc., of the device may be varied to adapt the same to the reactions for which it is to be used without departing from my invention, and within the scope of the claims hereunto appended, such changes being within the skill of one expert inthe art.
I claim: I
1. An apparatus for effecting reactions under heat and pressure comprising a reaction chamber, means for heating said chamber interiorly, a pressure chamber surrounding the same, means whereby free communication is established between the interiors of said reaction chamber and of said pressure chamber, means for maintaining the desired pressure within the pressure chamber and means for supplying material to be treated to the interior of said reaction chamber and for withdrawing products of reaction from the reaction and pressur chamber.
2. An apparatus for effecting reactions 100 under heat and pressure comprising a metallic pressure chamber, a refractory reaction chamber supported therein, heating-means Within said reaction chamber, means for supplying material to be treated to said reaction chamber and means for establishing free communication between the interiors of the reaction and pressure chambers.
3. An apparatus for eifecting reactions under heat and pressure comprising a metallic pressure chamber, a refractory reaction chamber supported therein, electric heating means within said reaction chamber, means for supplying material to be treated to the interior of said reaction chamber, an outlet pipe from the reaction chamber to the exterior of the pressure chamber, said pipe being provided within the pressure chamber with an opening whereby free communication is established between the interiors of the rewithin said reaction chamber, means for sup- In testimony whereof, I have signed this plying material to be treated to said reacspecification in the presence of two subscribtion chamber and for withdrawing products ing witnesses.
of reaction from the reaction and pressure EDWARD E. SOMERMEIER. 6 chambers, and means for establishing free Witnesses:
communication between the interiors of the GILEs W. CHAPMAN,
reaction and pressure chambers. FLORENCE E. BUCH'AN.
US16471217A 1917-04-26 1917-04-26 Apparatus for subjecting gases to the action of heat and pressure. Expired - Lifetime US1286135A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US16471217A US1286135A (en) 1917-04-26 1917-04-26 Apparatus for subjecting gases to the action of heat and pressure.

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US16471217A US1286135A (en) 1917-04-26 1917-04-26 Apparatus for subjecting gases to the action of heat and pressure.

Publications (1)

Publication Number Publication Date
US1286135A true US1286135A (en) 1918-11-26

Family

ID=3353707

Family Applications (1)

Application Number Title Priority Date Filing Date
US16471217A Expired - Lifetime US1286135A (en) 1917-04-26 1917-04-26 Apparatus for subjecting gases to the action of heat and pressure.

Country Status (1)

Country Link
US (1) US1286135A (en)

Cited By (25)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2509921A (en) * 1945-11-30 1950-05-30 Benjamin Clayton Manufacture of sponge iron
US2519481A (en) * 1945-05-02 1950-08-22 Benjamin Clayton Temperature control of chemical reactions
US2538059A (en) * 1945-02-05 1951-01-16 Phillips Petroleum Co Internal insulation of vessels
US2545384A (en) * 1944-08-05 1951-03-13 Phillips Petroleum Co Insulation of catalyst chambers
US2551160A (en) * 1945-02-05 1951-05-01 Phillips Petroleum Co Internal insulation of vessels
US2551361A (en) * 1948-02-12 1951-05-01 Michelin Caoutchouc Apparatus permitting a thermal transformation, particularly for isomerization of pinene into dipentene
US2606270A (en) * 1950-10-28 1952-08-05 Gen Electric Condensation nuclei generator
US2621105A (en) * 1949-10-28 1952-12-09 Phillips Petroleum Co High-temperature solid material-fluid contact apparatus and method of operation
US2664348A (en) * 1949-08-05 1953-12-29 Phillips Petroleum Co High pressure and temperature reaction chamber
US2686048A (en) * 1950-06-07 1954-08-10 Westinghouse Electric Corp Electric heating means
US2717915A (en) * 1952-11-13 1955-09-13 Zalman M Shapiro Apparatus for production of purified metals
US2890990A (en) * 1955-10-20 1959-06-16 Exxon Research Engineering Co Method for conducting photochemical reactions
US2925636A (en) * 1956-07-17 1960-02-23 Crucible Steel Co America Skull type furnace
US2937923A (en) * 1957-10-18 1960-05-24 Hercules Powder Co Ltd Process for treatment of fluid reactants
US2946670A (en) * 1957-03-11 1960-07-26 Texaco Development Corp Manufacture of synthesis gas
US2992907A (en) * 1961-07-18 Manufacture of synthesis gas
US3025145A (en) * 1958-07-28 1962-03-13 Gen Electric Retort for an ammonia dissociator and the like
US3039857A (en) * 1960-07-26 1962-06-19 Condit Ralph Howell Apparatus for growing pure crystals
US3056664A (en) * 1959-03-12 1962-10-02 Standard Oil Co Apparatus for handling corrosive materials at high pressures and temperatures
US3282733A (en) * 1961-03-30 1966-11-01 Leesona Corp Process of operating a fuel cell utilizing inert gas to maintain pressure differental
US3396865A (en) * 1964-04-08 1968-08-13 Ici Ltd Synthesis pressure vessel
US3469624A (en) * 1966-10-20 1969-09-30 Basf Ag Cooling system for the shell of a reactor
US4078899A (en) * 1975-09-26 1978-03-14 Friedrich Uhde Gmbh Reaction vessel heated by helium
US4235841A (en) * 1979-02-21 1980-11-25 Autoclave Engineers, Inc. Double chambered high pressure furnace
US20100171506A1 (en) * 2008-11-26 2010-07-08 James Norgaard Explosion-proof detector assembly for a flame ionization detector (FID)

Cited By (25)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2992907A (en) * 1961-07-18 Manufacture of synthesis gas
US2545384A (en) * 1944-08-05 1951-03-13 Phillips Petroleum Co Insulation of catalyst chambers
US2538059A (en) * 1945-02-05 1951-01-16 Phillips Petroleum Co Internal insulation of vessels
US2551160A (en) * 1945-02-05 1951-05-01 Phillips Petroleum Co Internal insulation of vessels
US2519481A (en) * 1945-05-02 1950-08-22 Benjamin Clayton Temperature control of chemical reactions
US2509921A (en) * 1945-11-30 1950-05-30 Benjamin Clayton Manufacture of sponge iron
US2551361A (en) * 1948-02-12 1951-05-01 Michelin Caoutchouc Apparatus permitting a thermal transformation, particularly for isomerization of pinene into dipentene
US2664348A (en) * 1949-08-05 1953-12-29 Phillips Petroleum Co High pressure and temperature reaction chamber
US2621105A (en) * 1949-10-28 1952-12-09 Phillips Petroleum Co High-temperature solid material-fluid contact apparatus and method of operation
US2686048A (en) * 1950-06-07 1954-08-10 Westinghouse Electric Corp Electric heating means
US2606270A (en) * 1950-10-28 1952-08-05 Gen Electric Condensation nuclei generator
US2717915A (en) * 1952-11-13 1955-09-13 Zalman M Shapiro Apparatus for production of purified metals
US2890990A (en) * 1955-10-20 1959-06-16 Exxon Research Engineering Co Method for conducting photochemical reactions
US2925636A (en) * 1956-07-17 1960-02-23 Crucible Steel Co America Skull type furnace
US2946670A (en) * 1957-03-11 1960-07-26 Texaco Development Corp Manufacture of synthesis gas
US2937923A (en) * 1957-10-18 1960-05-24 Hercules Powder Co Ltd Process for treatment of fluid reactants
US3025145A (en) * 1958-07-28 1962-03-13 Gen Electric Retort for an ammonia dissociator and the like
US3056664A (en) * 1959-03-12 1962-10-02 Standard Oil Co Apparatus for handling corrosive materials at high pressures and temperatures
US3039857A (en) * 1960-07-26 1962-06-19 Condit Ralph Howell Apparatus for growing pure crystals
US3282733A (en) * 1961-03-30 1966-11-01 Leesona Corp Process of operating a fuel cell utilizing inert gas to maintain pressure differental
US3396865A (en) * 1964-04-08 1968-08-13 Ici Ltd Synthesis pressure vessel
US3469624A (en) * 1966-10-20 1969-09-30 Basf Ag Cooling system for the shell of a reactor
US4078899A (en) * 1975-09-26 1978-03-14 Friedrich Uhde Gmbh Reaction vessel heated by helium
US4235841A (en) * 1979-02-21 1980-11-25 Autoclave Engineers, Inc. Double chambered high pressure furnace
US20100171506A1 (en) * 2008-11-26 2010-07-08 James Norgaard Explosion-proof detector assembly for a flame ionization detector (FID)

Similar Documents

Publication Publication Date Title
US1286135A (en) Apparatus for subjecting gases to the action of heat and pressure.
US3025145A (en) Retort for an ammonia dissociator and the like
US1203312A (en) Process of treating hydrocarbons and products derived therefrom.
US731758A (en) Apparatus for making sulfuric anhydrid.
US1941271A (en) Treatment of reaction process apparatus
US1744750A (en) Calorimetric bomb for the catalysis of ammonia
DE567327C (en) Method of heating pressure vessels
US166862A (en) Improvement in apparatus for the manufacture of salicylic acid
US187162A (en) William momueteie
US1138266A (en) Process of treating hydrocarbon oils.
US1307362A (en) Xfesation-chambeb f fob making nitsogen
GB364043A (en) Improvements in and relating to the catalytic treatment of hydrocarbons at high temperatures
US1705180A (en) Process for the catalytic treatment of hydrocarbon oil
US1933845A (en) Conversion of hydrocarbon gases
US1825977A (en) Process of cracking mineral oil
US1478559A (en) Process of treating hydrocarbons
US130540A (en) Improvement in apparatus for converting iron into steel by means of hydrocarbon
US1502895A (en) Apparatus for treating gases
US1805628A (en) Process and apparatus for cracking oil
US736479A (en) Process of deodorizing or purifying petroleum.
US1055747A (en) Apparatus for refining petroleum.
US1806284A (en) Process of and apparatus for converting heavy into lighter hydrocarbons
US1803964A (en) Process of desulphurizing cracked hydrocarbons
US1526907A (en) Process of making gasoline from crude mineral oil
US774430A (en) Gas-manufacturing apparatus.