US1619977A - Process and apparatus for treating oils - Google Patents
Process and apparatus for treating oils Download PDFInfo
- Publication number
- US1619977A US1619977A US724077A US72407724A US1619977A US 1619977 A US1619977 A US 1619977A US 724077 A US724077 A US 724077A US 72407724 A US72407724 A US 72407724A US 1619977 A US1619977 A US 1619977A
- Authority
- US
- United States
- Prior art keywords
- oil
- streams
- heating zone
- coils
- heating
- 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
- 239000003921 oil Substances 0.000 title description 37
- 238000000034 method Methods 0.000 title description 8
- 238000010438 heat treatment Methods 0.000 description 15
- 229930195733 hydrocarbon Natural products 0.000 description 8
- 150000002430 hydrocarbons Chemical class 0.000 description 8
- 239000004215 Carbon black (E152) Substances 0.000 description 6
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 3
- 229910052799 carbon Inorganic materials 0.000 description 3
- 238000013459 approach Methods 0.000 description 2
- 238000002485 combustion reaction Methods 0.000 description 2
- 238000001556 precipitation Methods 0.000 description 2
- 241001527902 Aratus Species 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G9/00—Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
- C10G9/14—Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils in pipes or coils with or without auxiliary means, e.g. digesters, soaking drums, expansion means
- C10G9/18—Apparatus
- C10G9/20—Tube furnaces
Definitions
- the invention relates to a process and apparatus for treating hydrocarbon 011s, and refers more particularly to improvements designed to promote the production of a maximum yield of light hydrocarbons from heavy hydrocarbons.
- the inventlon is directed to improvements in the arrangement and position of the preheating coils within the furnace.
- the single figure 1 s a side elevational view, partly in section of the ap aratus.
- the 0 posite side of the bafile 7 are positione a plurality of sets of heating 0011s 9 and 10, arranged in this instance, parallel.
- oil may be charged thereto thrqigh the hue 11 on which is mounted pressure gauge 12 and in which is interposed valve 13, said line 11 communicating with the pump 14 drawing oil from any suitable source of storage or supply through inlet 15.
- the bank of tubes 10 may be charged through the line 16 in which is interposed the meter 17 pressure gauge 18 and valve 19, said line 16 communicating with the pump 14.
- a meter 17 may be interposed in line 11.
- the separate coils combining into one coil at the point 20 at the zone of highest temperature will assist in increasing the velocity of the oil as it approaches this hottest zone to prevent precipitation or dropping out of any carbon in the coil while at the same time maintaining the desirable effect of a single coil relative to this point.
- the spent gases of combustion passing through the flue chamber 2 may be passed out of the stack by opening the damper 4 and closing the damper 5, or they may be recirculated in any suitable manner by closing the damper 4 and opening the damper 5.
- a process of treating hydrocarbon oils consisting in forcing the oil under pressure in a plurality of independent streams through a furnace, Where'said oil is progressively heated, increasing the velocity of the oil approaching the point of highest heat by combining the oil streams into a less number of streams.
- a process for treating hydrocarbon oil consisting in placing the oil under pressure, in lowering the velocity of the oil during a preheating treatment by separating the oil into a plurality of independent streams in which streams the oil flows through that portion of a heating zone wherein the lowest temperature is maintained, in increasing the velocity of the oil prior to its passage through that portion of the heating zone wherein the maximum temperature is imparted to the oil by again uniting said streams.
- a process for treating hydrocarbon oil consisting in passing the oil in a plurality of streams through that portion of a heating zone maintained at the lowest temperature, in increasing the velocity of the oil to prevent precipitation of carbon when the oil is subjected to a decomposing temperature by uniting said streams prior to the passage of the oil through that portion of the heating zone wherein the maximum temperature is imparted to the oil.
- An apparatus for treating hydrocarbon oil comprising a heating zone, a plurality of preheating coils positioned in that portion of the heating zone wherein the lowest temperature is maintained, said plurality of preheating coils being united into a single elongated heating coil positioned in that portion of the heating zone wherein the maximum temperature is maintained and means for supplying oil under pressure to said preheating coils.
- a process for treating hydrocarbon oil consisting in passing the oil in a pluralit of streams during its initial flow throng a heating zone and while being subjected to preliminary heating therein, in thereafter increasing the velocity of the oil during a substantial portion of its flow through the heating zone by uniting said streams prior to the final heating of the oil in the heating zone.
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- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Description
March 8,1927.
L. C. HUFF PROCESS AND APPARATUS FOR TREATING OILS Filed July 3, 1924 I g a Patented Mar. 8, 1927.
UNITED STATES 1,619,977 PATENT OFFICE.
LYHAN C. RUFF, OF CHICAGO, ILLINOIS, ASSIGNOR TO UNIVERSAL OIL IIRODUCTS COMPANY, OF CHICAGO, ILLINOIS, A CORPORATION OF SOUTH DAKOTA.
PROCESS AND APPARATUS FOR TREATING. OILS.
Application filed July 3, 1924. Serial No. 724,077.
The invention relates to a process and apparatus for treating hydrocarbon 011s, and refers more particularly to improvements designed to promote the production of a maximum yield of light hydrocarbons from heavy hydrocarbons.
In its particular aspects the inventlon is directed to improvements in the arrangement and position of the preheating coils within the furnace.
In the drawing, the single figure 1s a side elevational view, partly in section of the ap aratus.
fieferring in detail to the drawing, 1
designates a furnace having the flue passage 2,, stack 3, controlled by damper 4, said flue passage beiniguprovided with auxiliary damper 5. The rnace is of the side fired type being heated by means of the burners 6 and having the centrally positloned baflie 7 to form the combustion chamber 8. On
the 0 posite side of the bafile 7 are positione a plurality of sets of heating 0011s 9 and 10, arranged in this instance, parallel.
Referring to the bank of heating coils 9, oil may be charged thereto thrqigh the hue 11 on which is mounted pressure gauge 12 and in which is interposed valve 13, said line 11 communicating with the pump 14 drawing oil from any suitable source of storage or supply through inlet 15. The bank of tubes 10 may be charged through the line 16 in which is interposed the meter 17 pressure gauge 18 and valve 19, said line 16 communicating with the pump 14. At a point referably above the center of the horizontal banks of tubes, of which there may be any number, they. combine into one coil as shown at 20 having the outlet 21. A meter 17 may be interposed in line 11.
Referring now to the operation of the invention, and the reason for the particular construction shown, it has always been a problem to minimize the friction encountered in passing oil through a continuous coil. It has been found that when oil is passed through a continuous coil of say 3500 linear feet of three to four inch pipe mounted in the furnace it encounters a frictional 0 position of upwards of 100 pounds. I have discovered that by so arranging the coils in separate banks or sets that the same number of linear feet can be utilized, and the frictional resistance will be cut down very materially, less than 50 pounds. The
advantage of this from the standpoint of )umping the oil will be at once apparent. n addition, the separate coils combining into one coil at the point 20 at the zone of highest temperature will assist in increasing the velocity of the oil as it approaches this hottest zone to prevent precipitation or dropping out of any carbon in the coil while at the same time maintaining the desirable effect of a single coil relative to this point.
In addition, by increasing thevelocity of the oil as it approaches the point of critical temperature after having been previously subjected to a soakingheating in the parallel coils will result in any carbon which may be precipitated being washed along and carried by the oil under the increased ve locity. Thus the tube friction is materially decreased through a bank of tubes, thus elim inating costly pumping and high friction pressure. The oil flowing in parallel tubes will be heated to approximately the same temperature in the parallel coils, The. line 21 may lead to any suitable reaction chamber Where vaporization occurs.
The spent gases of combustion passing through the flue chamber 2 may be passed out of the stack by opening the damper 4 and closing the damper 5, or they may be recirculated in any suitable manner by closing the damper 4 and opening the damper 5.
I claim as my invention:
1. A process of treating hydrocarbon oils, consisting in forcing the oil under pressure in a plurality of independent streams through a furnace, Where'said oil is progressively heated, increasing the velocity of the oil approaching the point of highest heat by combining the oil streams into a less number of streams.
2. A process for treating hydrocarbon oil, consisting in placing the oil under pressure, in lowering the velocity of the oil during a preheating treatment by separating the oil into a plurality of independent streams in which streams the oil flows through that portion of a heating zone wherein the lowest temperature is maintained, in increasing the velocity of the oil prior to its passage through that portion of the heating zone wherein the maximum temperature is imparted to the oil by again uniting said streams.
3. A process for treating hydrocarbon oil, consisting in passing the oil in a plurality of streams through that portion of a heating zone maintained at the lowest temperature, in increasing the velocity of the oil to prevent precipitation of carbon when the oil is subjected to a decomposing temperature by uniting said streams prior to the passage of the oil through that portion of the heating zone wherein the maximum temperature is imparted to the oil.
4. An apparatus for treating hydrocarbon oil, comprising a heating zone, a plurality of preheating coils positioned in that portion of the heating zone wherein the lowest temperature is maintained, said plurality of preheating coils being united into a single elongated heating coil positioned in that portion of the heating zone wherein the maximum temperature is maintained and means for supplying oil under pressure to said preheating coils.
5. A process for treating hydrocarbon oil consisting in passing the oil in a pluralit of streams during its initial flow throng a heating zone and while being subjected to preliminary heating therein, in thereafter increasing the velocity of the oil during a substantial portion of its flow through the heating zone by uniting said streams prior to the final heating of the oil in the heating zone.
LYMAN C. HUFF.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US724077A US1619977A (en) | 1924-07-03 | 1924-07-03 | Process and apparatus for treating oils |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US724077A US1619977A (en) | 1924-07-03 | 1924-07-03 | Process and apparatus for treating oils |
Publications (1)
Publication Number | Publication Date |
---|---|
US1619977A true US1619977A (en) | 1927-03-08 |
Family
ID=24908879
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US724077A Expired - Lifetime US1619977A (en) | 1924-07-03 | 1924-07-03 | Process and apparatus for treating oils |
Country Status (1)
Country | Link |
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US (1) | US1619977A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2514535A (en) * | 1946-06-14 | 1950-07-11 | Shell Dev | Process for heating liquids in tube furnaces |
-
1924
- 1924-07-03 US US724077A patent/US1619977A/en not_active Expired - Lifetime
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2514535A (en) * | 1946-06-14 | 1950-07-11 | Shell Dev | Process for heating liquids in tube furnaces |
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