US1751730A - Apparatus for cracking oil - Google Patents

Apparatus for cracking oil Download PDF

Info

Publication number
US1751730A
US1751730A US444234A US44423421A US1751730A US 1751730 A US1751730 A US 1751730A US 444234 A US444234 A US 444234A US 44423421 A US44423421 A US 44423421A US 1751730 A US1751730 A US 1751730A
Authority
US
United States
Prior art keywords
oil
pipe
air
dephlegmator
chamber
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
US444234A
Inventor
Egloff Gustav
Harry P Benner
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.)
Universal Oil Products Co
Original Assignee
Universal Oil Products Co
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 Universal Oil Products Co filed Critical Universal Oil Products Co
Priority to US444234A priority Critical patent/US1751730A/en
Application granted granted Critical
Publication of US1751730A publication Critical patent/US1751730A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING 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
    • C10G9/00Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
    • C10G9/14Thermal 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

Definitions

  • This invention relates to improvements in apparatus for cracking oil and refers more particularly to that type of process and apparatus in which the oil is first passed through a relatively closed coil or heating chamber and then delivered in substantially liquid form to an enlarged expansion chamber. Vapors are taken oif from such expansion' chamber and subject to dephlegmation
  • the particular feature of the present invention lies more especially in the novel means for controlling the temperature of the dephlegmator and at.,the same time obtaining the highest heat efliciency from the fuel used for initially heating the'oil in the cracking zone.
  • the single figure is a view, partly in vertical section, and partly in side elevation, of improved apparatus for carrying out our process.
  • 1 designates a furnace, provided with the burner 2, stack 3, and combustion chamber 4.
  • the heating coil 5 which may take the form of a continuous coil of 3 pipe formed by interconnected tubes.
  • the inlet side of the coil is connected to inlet line 6 leading to charging pump 7
  • the outlet side of the coil is connected to the transfer line 8 leading to the elongated expansion chamber 9.
  • This expansion chamer is provided with manhole plate 10, 5residue drawofi' pipe 11 and vapor outlet pipe 12.
  • the last named pipe extends into the lower end of the dephle mator 13, A. s aced cap member 14 is rovided above the pipe 12 to prevent the re ux condensate from falling back into the expansion chamber.
  • the dephlegmator consists of the upper and 0 lower drums 15 and 16 connected by the tubes 17, surrounded by the annular heat enclosing shell 18.
  • the drum 16 is. provided with the reflux return pipe 19 leading to feed line 6. Its lower side is provided with the branch pipe 20 whereby the refiux condensate may be led elsewhere if desired.
  • the upper chamber 15 is provided with the vapor pipe 21 leading to the condenser coil 22 seated in condenser box 23.
  • the lower end of the coil is connected by pipe 24 with the top of receiver 25.
  • This receiver 25 has pressure gauge 26, liquid-level gauge 27, gas outlet pipe 28 and distillate drawoif pipe 29.
  • Various parts of the system are provided with the throttle valves 30, as shown in the drawing, whereby vapor pressures may be maintained on all or part of the system or diflerential pressures maintained.
  • an air blower 31 which is adapted to deliver regulated quantities of cool air to the dephlegmator so as to definitel and accurately control the temperatureo the dephle ator.
  • the air passes around the tubes of the de hlegrnator, it, of course, serves to cool the oil and itself becomes heated.
  • the heat units thus transferred instead of being wasted, are saved and utilized by causin them to pass throu h the insulated hot air pipe 32 connected to t e upper end of the shell 18 at one end and at its other end leading back to the burner whereby the hot air may be utilized in con-- nection with the air supply of the burner and l thus get a more" efficient combustion than would be the case where cool air was used, the pipe being preferably provided with a art 33 for connecting the same with the urner.
  • the construction seems simple but 8 it is to be borne in mind that in the cracking of petroleum oil, one of the major expenses 7 is the fuel required for heating the oil to be cracked. As a matter of fact, in the commercial operation of cracking processes, large amounts of fuel oil are consumed in heating the oil to be treated, which fuel oil might itself be cracked and thus tend to serve to conserve the fuel supply of the country.

Description

March 25, 1930. G. EGLOFF ET AL APPARATUS FOR CRACKING OIL Original Filed Feb. 11. 1921 Fatented Mar 25,
GUSTAV EGLOFF AND HARRY P. IBENNER, OF CHICAGO, ILLINOIS, ASSIGNORS T UNI- VERSAL OIL PRODUCTS COMPANY, OF CHICAGO, ILLINOIS, ACORPORATION 0F SOUTH DAKOTA,
APPARATUS FOR CRACKING OIL Application filed February 11, 1921, Serial No. 444,234. Renewed February 21, 1929.
This invention relates to improvements in apparatus for cracking oil and refers more particularly to that type of process and apparatus in which the oil is first passed through a relatively closed coil or heating chamber and then delivered in substantially liquid form to an enlarged expansion chamber. Vapors are taken oif from such expansion' chamber and subject to dephlegmation The particular feature of the present invention lies more especially in the novel means for controlling the temperature of the dephlegmator and at.,the same time obtaining the highest heat efliciency from the fuel used for initially heating the'oil in the cracking zone.
In the drawing, the single figure is a view, partly in vertical section, and partly in side elevation, of improved apparatus for carrying out our process.
Refeiring in detail to the drawing, 1 designates a furnace, provided with the burner 2, stack 3, and combustion chamber 4. In the combustion chamber is mounted the heating coil 5 which may take the form of a continuous coil of 3 pipe formed by interconnected tubes. The inlet side of the coil is connected to inlet line 6 leading to charging pump 7 The outlet side of the coil is connected to the transfer line 8 leading to the elongated expansion chamber 9. This expansion chamer is provided with manhole plate 10, 5residue drawofi' pipe 11 and vapor outlet pipe 12. The last named pipe extends into the lower end of the dephle mator 13, A. s aced cap member 14 is rovided above the pipe 12 to prevent the re ux condensate from falling back into the expansion chamber. The dephlegmator consists of the upper and 0 lower drums 15 and 16 connected by the tubes 17, surrounded by the annular heat enclosing shell 18. The drum 16 is. provided with the reflux return pipe 19 leading to feed line 6. Its lower side is provided with the branch pipe 20 whereby the refiux condensate may be led elsewhere if desired. The upper chamber 15 is provided with the vapor pipe 21 leading to the condenser coil 22 seated in condenser box 23. The lower end of the coil is connected by pipe 24 with the top of receiver 25. This receiver 25 has pressure gauge 26, liquid-level gauge 27, gas outlet pipe 28 and distillate drawoif pipe 29. Various parts of the system are provided with the throttle valves 30, as shown in the drawing, whereby vapor pressures may be maintained on all or part of the system or diflerential pressures maintained.
Referring now more particularly to the novel feature of the invention, to the lower end of the shell 18 is connected an air blower 31, which is adapted to deliver regulated quantities of cool air to the dephlegmator so as to definitel and accurately control the temperatureo the dephle ator. As the air passes around the tubes of the de hlegrnator, it, of course, serves to cool the oil and itself becomes heated. The heat units thus transferred, instead of being wasted, are saved and utilized by causin them to pass throu h the insulated hot air pipe 32 connected to t e upper end of the shell 18 at one end and at its other end leading back to the burner whereby the hot air may be utilized in con-- nection with the air supply of the burner and l thus get a more" efficient combustion than would be the case where cool air was used, the pipe being preferably provided with a art 33 for connecting the same with the urner. The construction: seems simple but 8 it is to be borne in mind that in the cracking of petroleum oil, one of the major expenses 7 is the fuel required for heating the oil to be cracked. As a matter of fact, in the commercial operation of cracking processes, large amounts of fuel oil are consumed in heating the oil to be treated, which fuel oil might itself be cracked and thus tend to serve to conserve the fuel supply of the country.
' We claim as our invention:
1. In an ap aratus for cracking oil, the combination with a still mounted in a furnace, of a dephlegmator connected to the vapor space thereof, and a closed air chamber within the interior of said dephlegmator, means connected to said de hlegmator for forcing cool air thereto an means for removing the air heated by the dephlegmator and delivering it to the furnace of the still.
2. In an apparatus for cracking oil, the
combination with a heating coil mounted in a furnace, a reaction zone communicating therewith where substantial vaporization takes lace, a dephlegmator communicating with the vapor space of said reaction zone, a closed air chamber within the interior of said dephlegmator, means communicating with said closed chamber in the dephlegmator for forcing cool air thereto, and means for re moving said air after passage through the closed air chamber which has been heated by the dephle mator, and means for delivering said heate air to the furnace.
GUSTAV EGLOFF. HARRY Pv BENNER.
US444234A 1921-02-11 1921-02-11 Apparatus for cracking oil Expired - Lifetime US1751730A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US444234A US1751730A (en) 1921-02-11 1921-02-11 Apparatus for cracking oil

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US444234A US1751730A (en) 1921-02-11 1921-02-11 Apparatus for cracking oil

Publications (1)

Publication Number Publication Date
US1751730A true US1751730A (en) 1930-03-25

Family

ID=23764039

Family Applications (1)

Application Number Title Priority Date Filing Date
US444234A Expired - Lifetime US1751730A (en) 1921-02-11 1921-02-11 Apparatus for cracking oil

Country Status (1)

Country Link
US (1) US1751730A (en)

Similar Documents

Publication Publication Date Title
US1751730A (en) Apparatus for cracking oil
US1805614A (en) Apparatus for cracking oil
US1674827A (en) Process and apparatus for cracking oil
US1751729A (en) Apparatus for treating hydrocarbons
US1806618A (en) op chicago
US1598368A (en) Apparatus for cracking oil
US1619921A (en) Process of cracking petroleum oil
US1725067A (en) Method for cooling the heating coils of an oil-cracking apparatus
US1715643A (en) Apparatus for treating hydrocarbons
US1791617A (en) Apparatus for cracking oil
US1357276A (en) Apparatus for the treatment of hydrocarbon oils
US1649102A (en) Process of treating emulsified oils
US1526907A (en) Process of making gasoline from crude mineral oil
US1549352A (en) Process for cracking oil
US1839049A (en) Process and apparatus for treating oils
US1685476A (en) of chicago
US1965335A (en) Process and apparatus for cracking hydrocarbon oils
US1670105A (en) Apparatus for treating hydrocarbons
US1638115A (en) Process of and apparatus for cracking oil
US1703617A (en) Process for cracking oil
US1851429A (en) Preparing and cracking hydrocarbon materials
US1541553A (en) Apparatus for treating oil
US1799530A (en) Process for cracking oil
US1733651A (en) Apparatus for treating petroleum oils
US1835809A (en) Process and apparatus for cracking oil