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 PDFInfo
- 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
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- 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
Links
- 239000007789 gas Substances 0.000 title description 14
- 238000006243 chemical reaction Methods 0.000 description 41
- 238000010438 heat treatment Methods 0.000 description 9
- 238000004891 communication Methods 0.000 description 6
- 239000000463 material Substances 0.000 description 4
- 239000007788 liquid Substances 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000005485 electric heating Methods 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 1
- 241000283077 Trichechus manatus Species 0.000 description 1
- 150000007824 aliphatic compounds Chemical class 0.000 description 1
- 150000001491 aromatic compounds Chemical class 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000003345 natural gas Substances 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 230000008439 repair process Effects 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J3/00—Processes of utilising sub-atmospheric or super-atmospheric pressure to effect chemical or physical change of matter; Apparatus therefor
- B01J3/04—Pressure vessels, e.g. autoclaves
- B01J3/046—Pressure-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.
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- 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.
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)
| 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) |
-
1917
- 1917-04-26 US US16471217A patent/US1286135A/en not_active Expired - Lifetime
Cited By (25)
| 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) |
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