US1950900A - Process and means for producing asphalt - Google Patents
Process and means for producing asphalt Download PDFInfo
- Publication number
- US1950900A US1950900A US551972A US55197231A US1950900A US 1950900 A US1950900 A US 1950900A US 551972 A US551972 A US 551972A US 55197231 A US55197231 A US 55197231A US 1950900 A US1950900 A US 1950900A
- Authority
- US
- United States
- Prior art keywords
- diaphragm
- asphalt
- container
- residuum
- supplying
- 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
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10C—WORKING-UP PITCH, ASPHALT, BITUMEN, TAR; PYROLIGNEOUS ACID
- C10C3/00—Working-up pitch, asphalt, bitumen
- C10C3/02—Working-up pitch, asphalt, bitumen by chemical means reaction
- C10C3/04—Working-up pitch, asphalt, bitumen by chemical means reaction by blowing or oxidising, e.g. air, ozone
-
- Y—GENERAL 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
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S48/00—Gas: heating and illuminating
- Y10S48/05—Diffusion membrane for gas reaction or separation
Definitions
- the invention comprises the features hereinafter fully described, and particularly pointed out in the claims, thefollowing description and the annexed drawing setting forth in detail certain illustrative embodiments of the invention, these being indicative, however, of but a few of the various ways in which the principle 9 of the invention may be employed.
- Fig. l is a vertical sectional semi-diagrammatic view showing apparatus contemplated in the-invention; Figs. 2 and 3 are fragmentary section and plan views of details; and Fig. 4 is a similar sectional detail of' another form.
- a container or tank 1 having a covering or lagging of heat-insulating material 2,
- a gaspervious diaphragm 6 is provided in the lower portion of the tank and conveniently this may take the form of a false-floor or partition. Beneath the diaphragm 6 is an inlet 1 for oxygen-supplying gas. Preferably, this may have several openings 8, to provide distribution, particularly if the tank be on a large scale.
- the oxygen pipe I may connect with a source of supply, which may be a connection 9 to a source of compressed-oxygen if desired, or teen air-compressor 10.
- the detail construction of the diaphragm 6 may vary somewhat, in accordance with circumstances, and may comprise plural-mesh metal, 50 or stamped metal in which openings are provided on a very fine scale, for instance such as off-set punchings 11 (Figs. 2 and 3) in plate'12, the offsets being scored and spaced just sufiiciently to provide fine pass-ways 13 ,for gas, without opening up free channels for the asphalt material.
- porous materials such as fabricated aluminum oxide plates, porous porcelain or other ceramic material 14 (Fig. 4), in which a porous structure may be-had to desired extent in accordance with sizes of grain material initially entering into the make-up of the plates or tiles.
- hot petroleum residuum for instance as coming from a still, is 6 introduced into the container 1' through the inlet 3.
- the temperature of the material may range for example, from 400 to 700 F.
- Oxygen is also supplied from the source 9, dr air from the pump 10, and passing through the pervious diaphragm 6 is thereby broken up into very finely divided state and thus fed into the body of residuum thereover.
- An advantage of the employment of oxygen is that all of the gas passed through the diaphragm is actively available, and no dilute inert gas, as in the case'df the nitrogen of the air, has to be handled.
- the gas as supplied to the pipe 7 may be subjected further to a tem-- perature control in the conditioner 15.
- the gas may be heated there, and its temperature gauged to maintain effective action in the tank even with relatively low temperature petroleum material.
- the gas may be cooled in the conditioner 15. In such manner, the operation in the tank may lie-controlled quite precisely in accordance with any particular temperature requirements.
- the waste gases escape through the outlet 5, and may be passed through a condenser system if desired, or wash-towers, to catch any possible constituents which are not to be discharged directly to the atmosphere.
- the final asphalt product may be drawn off by the outlet 16.
- heat may be introduced for melting such material and freeing the surfaces of obstruction, by means of a suitable heating; element, for instance a steam coil-1'7. If filesired, asimilar coil 18 may be provided also below the diaphragm.
- a method of making asphalt which comprises supplying a body of hot petroleum reside uum at one side of a porous diaphragm, and sup: plying air at a greater pressure at the other side to capillarily divide and permeate into the petroleum residuum.
- a method of making asphalt which comprises supplying a body of hot petroleum residuum against a gas-pervious diaphragm, supplying air at the other side, and forcing the air through to permeate the petroleum residuum in capillary division, while guarding the residuum against heat-loss exteriorly.
- Apparatus for making asphalt which comprises a container, means for supplying petroleum residuum thereto, means for guarding said container against heat-loss exteriorly, a porous ceramic diaphragm in the lower portion of said container, and means for supplying gaseousoxygen through said diaphragm.
- Apparatus for making asphalt which comprises a container, means for supplying petroleum residuum thereto, a diaphragm of porous aluminum oxide blocks in the lower portion of said container, indirect heat exchange means for heating the diaphragm, and means for supplying gaseous oxygen through said diaphragm.
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- Chemical & Material Sciences (AREA)
- General Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Civil Engineering (AREA)
- Structural Engineering (AREA)
- Materials Engineering (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Working-Up Tar And Pitch (AREA)
Description
Patented Mar. 13, 1934 UNITED STATES PROCESS AND MEANS FOR PRODUCING ASPHALT Elliott B. McConnell, Cleveland Heights, Ohio, asslgnor to The Standard Oil Company, Cleveland, Ohio, a corporation of Ohio 7 Application .luly 20,1931, Serial No. 551,972
11 Claims. (01. 196-44) In the customary preparation of asphalt by heating petroleum residuum and blowing air therethrough, among other dimculties encountered-is the baking of the material on the still surfaces. In accordance with the present invention, the difllculties and draw-backs concomitant with furnace-heating in asphalt-making may be eliminated, and an easily controllable procedure may be had, with a high capacity through-put. Other objects and'advantages will appear as the description proceeds.
To the accomplishment of the foregoing and related ends, the invention, then, comprises the features hereinafter fully described, and particularly pointed out in the claims, thefollowing description and the annexed drawing setting forth in detail certain illustrative embodiments of the invention, these being indicative, however, of but a few of the various ways in which the principle 9 of the invention may be employed.
In said annexed drawing:-
Fig. l is a vertical sectional semi-diagrammatic view showing apparatus contemplated in the-invention; Figs. 2 and 3 are fragmentary section and plan views of details; and Fig. 4 is a similar sectional detail of' another form.
Referring more particularly to the drawing, there is shown a container or tank 1 having a covering or lagging of heat-insulating material 2,
and provided with an inlet connection 3 forpetroleum residuum, as forwarded from any suitable source, for instance from a reducing still or pipe still through a pump 4. A vent outlet 5 at the upper portion of the container or tank may lead to the atmosphere, through'a condenser if de sired. In the lower portion of the tank, a gaspervious diaphragm 6 is provided and conveniently this may take the form of a false-floor or partition. Beneath the diaphragm 6 is an inlet 1 for oxygen-supplying gas. Preferably, this may have several openings 8, to provide distribution, particularly if the tank be on a large scale. The oxygen pipe I may connect with a source of supply, which may be a connection 9 to a source of compressed-oxygen if desired, or teen air-compressor 10. r
The detail construction of the diaphragm 6 may vary somewhat, in accordance with circumstances, and may comprise plural-mesh metal, 50 or stamped metal in which openings are provided on a very fine scale, for instance such as off-set punchings 11 (Figs. 2 and 3) in plate'12, the offsets being scored and spaced just sufiiciently to provide fine pass-ways 13 ,for gas, without opening up free channels for the asphalt material.
'be in the form of porous materials such as fabricated aluminum oxide plates, porous porcelain or other ceramic material 14 (Fig. 4), in which a porous structure may be-had to desired extent in accordance with sizes of grain material initially entering into the make-up of the plates or tiles.
For the production of asphalt, hot petroleum residuum, for instance as coming from a still, is 6 introduced into the container 1' through the inlet 3. The temperature of the material may range for example, from 400 to 700 F. Oxygen is also supplied from the source 9, dr air from the pump 10, and passing through the pervious diaphragm 6 is thereby broken up into very finely divided state and thus fed into the body of residuum thereover. An advantage of the employment of oxygen is that all of the gas passed through the diaphragm is actively available, and no dilute inert gas, as in the case'df the nitrogen of the air, has to be handled. On the other hand, by employment of air, a cheap and readily available source of oxygen is had, even though requiring a greater through-put on account of the 39 diluent nitrogen contained. The gas as supplied to the pipe 7 may be subjected further to a tem-- perature control in the conditioner 15. For instance, the gas may be heated there, and its temperature gauged to maintain effective action in the tank even with relatively low temperature petroleum material. On the other hand, if the temperature of the latter is already unnecessarily 1 high, the gas may be cooled in the conditioner 15. In such manner, the operation in the tank may lie-controlled quite precisely in accordance with any particular temperature requirements. The waste gases escape through the outlet 5, and may be passed through a condenser system if desired, or wash-towers, to catch any possible constituents which are not to be discharged directly to the atmosphere. The final asphalt product may be drawn off by the outlet 16.
In cases of shut-down, etc., and a freezing or solidification of the asphalt material on the diaphragm surfaces, heat may be introduced for melting such material and freeing the surfaces of obstruction, by means of a suitable heating; element, for instance a steam coil-1'7. If filesired, asimilar coil 18 may be provided also below the diaphragm.
Other modes of applying the principle of the invention may be employed, change being made as regards the details described, provided the pervious diaphragm, and iorcing the gaseous oxygen in.capillarily-'divided form into the petroleum residuum. g 3. A method of making asphalt, which comprises supplying a body of hot petroleum reside uum at one side of a porous diaphragm, and sup: plying air at a greater pressure at the other side to capillarily divide and permeate into the petroleum residuum. v
4. A method of making asphalt, which comprises supplying a body of hot petroleum residuum against a gas-pervious diaphragm, supplying air at the other side, and forcing the air through to permeate the petroleum residuum in capillary division, while guarding the residuum against heat-loss exteriorly.
' devious fine passages, and forcing air through in minute division into the petroleum residuum, while guarding the residuum against heat loss exteriorly. a
introducing gaseous oxygen through said diaphragm into the container, and indirect heat exchange means for heating the diaphragm.
9. Apparatus for making asphalt, which comprises a container, means for supplying petroleum residuum thereto, means for guarding said container against heat-loss exteriorly, a porous ceramic diaphragm in the lower portion of said container, and means for supplying gaseousoxygen through said diaphragm.
10. Apparatus for making asphalt, which comprises a container, means for supplying petroleum residuum thereto, a diaphragm of porous aluminum oxide blocks in the lower portion of said container, indirect heat exchange means for heating the diaphragm, and means for supplying gaseous oxygen through said diaphragm.
11. Apparatus for making asphalt, which comprises a container, means for supplying petroleum residuum thereto, means for guarding said container against heat loss exteriorly,=a porous ceramic diaphragm in the lower portion of said container, indirect heat exchange means for heating the diaphragm, and means for supplying gaseous oxygen through said diaphragm.
- ELLIO'I'I 2B. McCONNEIL.
lac
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US551972A US1950900A (en) | 1931-07-20 | 1931-07-20 | Process and means for producing asphalt |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US551972A US1950900A (en) | 1931-07-20 | 1931-07-20 | Process and means for producing asphalt |
Publications (1)
Publication Number | Publication Date |
---|---|
US1950900A true US1950900A (en) | 1934-03-13 |
Family
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US551972A Expired - Lifetime US1950900A (en) | 1931-07-20 | 1931-07-20 | Process and means for producing asphalt |
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US (1) | US1950900A (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2607671A (en) * | 1945-11-01 | 1952-08-19 | Hartford Nat Bank & Trust Co | Generator for producing a combustible oil gas |
US2694042A (en) * | 1951-08-25 | 1954-11-09 | Chicago Pump Co | Method of humidifying an aeriform body supplied to diffusion media |
US2738313A (en) * | 1952-07-30 | 1956-03-13 | Miller James | Method and apparatus for producing asphalt |
US4004302A (en) * | 1975-05-23 | 1977-01-25 | Sanji Hori | Air-foam generating apparatus for bath |
US4281423A (en) * | 1979-04-27 | 1981-08-04 | Matsushita Electric Industrial Co., Ltd. | Foam bathing apparatus |
-
1931
- 1931-07-20 US US551972A patent/US1950900A/en not_active Expired - Lifetime
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2607671A (en) * | 1945-11-01 | 1952-08-19 | Hartford Nat Bank & Trust Co | Generator for producing a combustible oil gas |
US2694042A (en) * | 1951-08-25 | 1954-11-09 | Chicago Pump Co | Method of humidifying an aeriform body supplied to diffusion media |
US2738313A (en) * | 1952-07-30 | 1956-03-13 | Miller James | Method and apparatus for producing asphalt |
US4004302A (en) * | 1975-05-23 | 1977-01-25 | Sanji Hori | Air-foam generating apparatus for bath |
US4281423A (en) * | 1979-04-27 | 1981-08-04 | Matsushita Electric Industrial Co., Ltd. | Foam bathing apparatus |
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