US2068845A - Process of manufacturing hard bituminous materials - Google Patents
Process of manufacturing hard bituminous materials Download PDFInfo
- Publication number
- US2068845A US2068845A US692029A US69202933A US2068845A US 2068845 A US2068845 A US 2068845A US 692029 A US692029 A US 692029A US 69202933 A US69202933 A US 69202933A US 2068845 A US2068845 A US 2068845A
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- US
- United States
- Prior art keywords
- softening point
- bituminous
- materials
- cracking
- bituminous materials
- 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
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- 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
Definitions
- This invention relates to a process for manufacturing hard bituminous materials and particularly bituminous materials which are harder than similar materials of the same softening points.
- Bituminous materials are used in the construction of molded objects such as electric storage battery boxes.
- the bituminous materials that have heretofore been found suitable are the better grades of natural bituminous materials known as glance pitch, large quantities of which are imported into this country. These bituminous materials are acid-proof and have the necessary high softening points, hardness and toughness.
- Petroleum distillate oils are subjected to cracking temperatures and pressures to convert the high boiling compounds to lower boiling compounds such as gasoline. In cracking the petroleum distillate oils to gasolines, for best results care is taken that the conversion is not carried so far that coke deposits are produced in the cracked residue.
- the resulting residue is distilled either under vacuum or in the presence of steam, either batch or continuously, to remove the lower boiling point portions of the cracked residue and obtain a soft flux having a softening point of to F. Care is taken during the distillation that no further cracking takes place.
- the soft flux having a softening point of 80 to 90 F. is then oxidized by contacting with air or a gas containing free oxygen to a bituminous product having a softening point not materially below 280 F. and upwards of 300 F.
- Hard bituminous materials may be prepared by straight reduction under vacuum or in the presence of steam. These products do not have the same desirable physical characteristics as when an 80 to 90 F. softening point soft flux is oxidized.
- the sample is placed in a dish of standard size and immersed in a bath at the desired temperature for a period of time. The following measurements are generally made:
- a further improved product may be obtained by dissolving the above oxidized bituminous material in benzol, separating the insoluble material and recovering the refined product by evaporation of the solvent.
- the physical characteristics of this refined product are illustrated by the following analyses of the several products:
- a process of manufacturing a hard bituminous material from a tar obtained by cracking a petroleum distillate oil comprising subjecting the tar to vacuum distillation to reduce the tar to an to F. softening point material and contacting the said material with a gas containing free oxygen to produce a bituminous material having a softening point over 275 F.
- a process of manufacturing a hard bituminous material having a specific gravity of over 1, a softening point above 265 F., and a penetration of 0 at 135 F. using a gram weight for 5 seconds comprising subjecting a residuum oil obtained in cracking a petroleum distillate oil to vacuum distillation to reduce the residuum oil to an 80 to 90 F. softening point, contacting the reduced residuum oil with a gas containing free oxygen to obtain a bituminous material having a softening point over 275 F., dissolving the bituminous material in an asphalt dissolving solvent, such as benzol, separating the insoluble materials and evaporating the solvent from the dissolved bituminous material.
- an asphalt dissolving solvent such as benzol
- a process of manufacturing a bituminous material having a specific gravity of over 1, a softening point above 265 F., a penetration of 0 at F. using a 100 gram weight for 5 seconds and over 98% soluble in carbon disulfide comprising subjecting cracking coil tar obtained in the pressure cracking of petroleum distillate oil after the tar had been subjected to non-oxidizing distillation to give a residue having a softening point of 80 to 90 F. to oxidation by contacting the residue with a gas containing free oxygen to produce a 275 to 300 F. softening point bituminous material.
- a process of manufacturing a hard bituminous material from a residuum oil obtained in cracking a petroleum distillate oil comprising subjecting a residuum oil obtained in cracking a petroleum distillate oil, to vacuum distillation to reduce the residuum oil to an 80 to 90 F. softening point, contacting the reduced residuum oil with a gas containing free oxygen to obtain a bituminous material having a softening point over 275 F., dissolving the bituminous material in benzol, separating the insoluble materials and evaporating the solvent from the dissolved bituminous material.
Description
Patented Jan. 26, 1937 UNITED STATES PATENT OFFICE PROCESS OF MANUFACTURING HARD BITUltIINOUS MATERIALS ration of Delaware No Drawing. Application October 3, 1933, Serial No. 692,029
4 Claims.
This invention relates to a process for manufacturing hard bituminous materials and particularly bituminous materials which are harder than similar materials of the same softening points.
Bituminous materials are used in the construction of molded objects such as electric storage battery boxes. The bituminous materials that have heretofore been found suitable are the better grades of natural bituminous materials known as glance pitch, large quantities of which are imported into this country. These bituminous materials are acid-proof and have the necessary high softening points, hardness and toughness.
It has been discovered that residues, which are formed during the cracking of a petroleum distillate oil, may be treated according to a process hereafter disclosed to produce bituminous materials which have equal, if not superior, properties such as being acid-proof and also having the necessary hardness and toughness.
In accordance with the present invention, this may be accomplished in the following manner:
Petroleum distillate oils are subjected to cracking temperatures and pressures to convert the high boiling compounds to lower boiling compounds such as gasoline. In cracking the petroleum distillate oils to gasolines, for best results care is taken that the conversion is not carried so far that coke deposits are produced in the cracked residue. The resulting residue is distilled either under vacuum or in the presence of steam, either batch or continuously, to remove the lower boiling point portions of the cracked residue and obtain a soft flux having a softening point of to F. Care is taken during the distillation that no further cracking takes place. The soft flux having a softening point of 80 to 90 F. is then oxidized by contacting with air or a gas containing free oxygen to a bituminous product having a softening point not materially below 280 F. and upwards of 300 F.
Hard bituminous materials may be prepared by straight reduction under vacuum or in the presence of steam. These products do not have the same desirable physical characteristics as when an 80 to 90 F. softening point soft flux is oxidized.
The following table illustrates the physical characteristics of a hard bituminous material obtained by oxidizing an 80 F. melting point residuum obtained from cracking petroleum distillate oil, and Cuban glance pitch:
The determination of the distance a standard needle will penetrate the sample in a fixed time, in 1/100ths of a centimeter, is a measure of the softness of the asphalt and is known as the penetration test. The sample is placed in a dish of standard size and immersed in a bath at the desired temperature for a period of time. The following measurements are generally made:
Weight of Temper- Time for Method of ature F. g gfi t penetration designation 50 5 116] 50/ 5 77 100 5 77/100/5 32 200 so 32l200/60 A further improved product may be obtained by dissolving the above oxidized bituminous material in benzol, separating the insoluble material and recovering the refined product by evaporation of the solvent. The physical characteristics of this refined product are illustrated by the following analyses of the several products:
Cuban Hard bitug2 glance minous minous pitch material material Softening point (B. 8: R.) 277 F. 288 F. 265 F. Penetration F./100 g./5 sec. 11% 6 7 Soluble in benzol 97. 39% 81. 90% 95. 34%
This invention is not to be limited by any theory 'or the particulars given by way of illustration but only by the following claims in which it is my intention to claim all novelty inherent in the invention.
I claim:
1. A process of manufacturing a hard bituminous material from a tar obtained by cracking a petroleum distillate oil, comprising subjecting the tar to vacuum distillation to reduce the tar to an to F. softening point material and contacting the said material with a gas containing free oxygen to produce a bituminous material having a softening point over 275 F.
2. A process of manufacturing a hard bituminous material having a specific gravity of over 1, a softening point above 265 F., and a penetration of 0 at 135 F. using a gram weight for 5 seconds, comprising subjecting a residuum oil obtained in cracking a petroleum distillate oil to vacuum distillation to reduce the residuum oil to an 80 to 90 F. softening point, contacting the reduced residuum oil with a gas containing free oxygen to obtain a bituminous material having a softening point over 275 F., dissolving the bituminous material in an asphalt dissolving solvent, such as benzol, separating the insoluble materials and evaporating the solvent from the dissolved bituminous material.
3. A process of manufacturing a bituminous material having a specific gravity of over 1, a softening point above 265 F., a penetration of 0 at F. using a 100 gram weight for 5 seconds and over 98% soluble in carbon disulfide, comprising subjecting cracking coil tar obtained in the pressure cracking of petroleum distillate oil after the tar had been subjected to non-oxidizing distillation to give a residue having a softening point of 80 to 90 F. to oxidation by contacting the residue with a gas containing free oxygen to produce a 275 to 300 F. softening point bituminous material.
4. A process of manufacturing a hard bituminous material from a residuum oil obtained in cracking a petroleum distillate oil, comprising subjecting a residuum oil obtained in cracking a petroleum distillate oil, to vacuum distillation to reduce the residuum oil to an 80 to 90 F. softening point, contacting the reduced residuum oil with a gas containing free oxygen to obtain a bituminous material having a softening point over 275 F., dissolving the bituminous material in benzol, separating the insoluble materials and evaporating the solvent from the dissolved bituminous material.
JOHN OLIVER COLLINS.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US692029A US2068845A (en) | 1933-10-03 | 1933-10-03 | Process of manufacturing hard bituminous materials |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US692029A US2068845A (en) | 1933-10-03 | 1933-10-03 | Process of manufacturing hard bituminous materials |
Publications (1)
Publication Number | Publication Date |
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US2068845A true US2068845A (en) | 1937-01-26 |
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US692029A Expired - Lifetime US2068845A (en) | 1933-10-03 | 1933-10-03 | Process of manufacturing hard bituminous materials |
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2455709A (en) * | 1945-04-03 | 1948-12-07 | Socony Vacuum Oil Co Inc | Battery box asphalt and method of making the same |
US2768119A (en) * | 1952-12-31 | 1956-10-23 | Phillips Petroleum Co | Pitches from petroleum and process for producing same |
US2991241A (en) * | 1957-09-11 | 1961-07-04 | Sinclair Refining Co | Process for the production of pitch comprising heating and concurrently airblowing the bottoms of a distilled catalytically cracked gas oil |
-
1933
- 1933-10-03 US US692029A patent/US2068845A/en not_active Expired - Lifetime
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2455709A (en) * | 1945-04-03 | 1948-12-07 | Socony Vacuum Oil Co Inc | Battery box asphalt and method of making the same |
US2768119A (en) * | 1952-12-31 | 1956-10-23 | Phillips Petroleum Co | Pitches from petroleum and process for producing same |
US2991241A (en) * | 1957-09-11 | 1961-07-04 | Sinclair Refining Co | Process for the production of pitch comprising heating and concurrently airblowing the bottoms of a distilled catalytically cracked gas oil |
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