[go: up one dir, main page]

US1832970A - Apparatus for cracking oil - Google Patents

Apparatus for cracking oil Download PDF

Info

Publication number
US1832970A
US1832970A US330182A US33018229A US1832970A US 1832970 A US1832970 A US 1832970A US 330182 A US330182 A US 330182A US 33018229 A US33018229 A US 33018229A US 1832970 A US1832970 A US 1832970A
Authority
US
United States
Prior art keywords
gas
header
receiver
cracking oil
battery
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
US330182A
Inventor
Egloff Gustav
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
Priority claimed from US430870A external-priority patent/US1703617A/en
Application filed by Universal Oil Products Co filed Critical Universal Oil Products Co
Priority to US330182A priority Critical patent/US1832970A/en
Application granted granted Critical
Publication of US1832970A publication Critical patent/US1832970A/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 .i
  • the gas from each receiver goes to a common gas header, and is prevented fromv flowing back to the receiver, but instead is conveyed to a suitable reservoir where it is compressed and returned to the heatinI tubes.
  • the slngle ligure designates a view, partly in side elevation and partly in vertical section, of a battery of stills, constructed in accordance with the present invention.
  • FIG. 1 designates the various furnaces, in each o which is mounted a heatin -coil 2, as for example, a continuous 'A coil of our-inch pipe several hundred feet in length.
  • Each coil 2 is connected bytrans- 1920, Serial No. 430,870. Divided and this application illed January 4, 1929. Serial No. 330.182.
  • each rece1ver is also provided at its upper end w with a gas outlet pipe 23, having throttle valve 24, which pipes 23 lead to a common gas header 25.
  • the header 25 is connected to a compresser pump 27, which ut is prevented at all.
  • This 'receiver 29 is connected by a feed line 30, having main throttle valve 31.
  • the feed .line 30 in turn is connected by branch lines 32 having throttle valves 33 to the inlet side of the heating' coils 2.
  • the process may be o erated as follows:
  • vvOil as for example, Iansas fuel oil, may
  • Each vapor chamber 5N is provided with a lresidue drawoif pipe 7, controlled by throt.-
  • each dephlegmator is provid with suitable bailles 14', and at its upper end with a vapor outlet pipe 15, leading to condenser coil 16, seated in condenser' y box 17. The lower end of each coil 16 is connected to each corresponding receiver 18,
  • the gen,-u erated vapors pass through the dephlegma structed exactiy alike and maintains its own pressure over its own generated vapors and is not subjected to any back pressure from the gas header on the receivers. In other words, 5 the incondensable as is prevented from flowing backwardly t rough the system at all times.
  • a battery of stills each having its own condenser and receiver, of a common incon'densable gaa header connected to leach receiver, a gas reservoir connected with said header, means for compressing the inconvdensable .gas in the reservoir, 'a return header connected with said gasreservoir, and valved branches leading from said return header for ,diverting-f the returned gas to any still of lthe battery, means located inthe lines connecting each receiver with the common gas header for preventing the return of incondensable gas from the .common gas header into the receiver of any still of the battery.
  • each a having its own condenser and receiver, of al common incondensable gas header connected to each receiver, a. gas reservoir connected with said header, means for compressing the 30 incondensable gask in the reservoir, a return header connected with said gas reservoir, and valved branches leading from said return header fordiverting the returned gas to any still of the battery, means comprising a check valve opening outwardly located in the lines connecting each receiver with they common gas header for preventing the return of incondensable gas from the common gas header into the receiver of any still of the battery.

Landscapes

  • 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)
  • Pipeline Systems (AREA)

Description

NOV. 24, 1931. (g,q EGLQFF APPARATUS FOR CRACKING OIL Original Filed Deo. 15, 1920 Patented Nov. -249 17931 UNITED STATES PATENT OFFICE GUSTAV EGLOFF, OF CHICAGO, ILLINOIS, ASSIGNOR TO UNIVERSAL OIL PRODUCTS COM- PANY, OF CHICAGO, ILLINOIS, CORPORATION F SOUTH DAKOTA APPARATUS FORl CRACKING OIL Original application illedleoember 15,
I application filed'by me-Serial No. 430,870
on December th, 1920; which has matured into Patent #1,703,617.
This inventionrelates to improvements in apparatus for cracking oil, and refers more .i
particularly to meansy for utilizing and con trollin the incondensable as formed as an inevita le result of the crac 'ng process, and more particularly to the utilization of the* incondensable gas formed bythe process itself, by passing it back through the heating tubes. In the present invention, the gas from each receiver goes to a common gas header, and is prevented fromv flowing back to the receiver, but instead is conveyed to a suitable reservoir where it is compressed and returned to the heatinI tubes.
In the drawing, the slngle ligure designates a view, partly in side elevation and partly in vertical section, of a battery of stills, constructed in accordance with the present invention. 1
Referring to the drawin 1 designates the various furnaces, in each o which is mounted a heatin -coil 2, as for example, a continuous 'A coil of our-inch pipe several hundred feet in length. Each coil 2 is connected bytrans- 1920, Serial No. 430,870. Divided and this application illed January 4, 1929. Serial No. 330.182.
which receiver has liquid drawof pipe 19, controlled by throttle valve 20 and pressure gauge 21 and liquidlevel gauge 22. Each rece1ver is also provided at its upper end w with a gas outlet pipe 23, having throttle valve 24, which pipes 23 lead to a common gas header 25. In each pipe 23 is interposed valve. The header 25 is connected to a compresser pump 27, which ut is prevented at all.
Shown is -only for the purpose of illustration.
This 'receiver 29 is connected by a feed line 30, having main throttle valve 31. The feed .line 30 in turn is connected by branch lines 32 having throttle valves 33 to the inlet side of the heating' coils 2. The process may be o erated as follows:
vvOil, as for example, Iansas fuel oil, may
fer line 3, having throttle valve 4, to its ex- ,be continuously fed through the various ply. Each vapor chamber 5Nis provided with a lresidue drawoif pipe 7, controlled by throt.-
' tle valve 8,and is also provided with a vapor outlet pipe 9, extending into the upper end of a dephlegmator 10, and provided ,with a spaced cap member 11, the arrangement being such as to permit the vapors to enter the dephlegmator 10, While preventing the reflux L condensate from falling back into the expansion chamber. Instead, the reflux condensate is drawn off through the line 12, having throttle valve 13, and leading back to thecorrespondin feed pump. Each dephlegmator is provid with suitable bailles 14', and at its upper end with a vapor outlet pipe 15, leading to condenser coil 16, seated in condenser' y box 17. The lower end of each coil 16 is connected to each corresponding receiver 18,
stills, and `there subjected to a pressure o fsb say 135 pounds and a temperature of 7 50 de'- f ees F. While still in liquid phase the oil 1s delivered to the expansion chambers 5, where vaporization takes place.
tors, where they are subjected to reflux condensation, and the reflux condensate returns to the heating tube for further treatment.
The gen,-u erated vapors pass through the dephlegma structed exactiy alike and maintains its own pressure over its own generated vapors and is not subjected to any back pressure from the gas header on the receivers. In other words, 5 the incondensable as is prevented from flowing backwardly t rough the system at all times.
I claim as my invention: i l. In an apparatus for cracking oil, the combination with a battery of stills, each having its own condenser and receiver, of a common incon'densable gaa header connected to leach receiver, a gas reservoir connected with said header, means for compressing the inconvdensable .gas in the reservoir, 'a return header connected with said gasreservoir, and valved branches leading from said return header for ,diverting-f the returned gas to any still of lthe battery, means located inthe lines connecting each receiver with the common gas header for preventing the return of incondensable gas from the .common gas header into the receiver of any still of the battery.
2. In an apparatus for cracking oil, the combination with a battery of stills, each a having its own condenser and receiver, of al common incondensable gas header connected to each receiver, a. gas reservoir connected with said header, means for compressing the 30 incondensable gask in the reservoir, a return header connected with said gas reservoir, and valved branches leading from said return header fordiverting the returned gas to any still of the battery, means comprising a check valve opening outwardly located in the lines connecting each receiver with they common gas header for preventing the return of incondensable gas from the common gas header into the receiver of any still of the battery. 4 In testimony whereof I aiiix my signature. GSTAV EGLOFF.
US330182A 1920-12-15 1929-01-04 Apparatus for cracking oil Expired - Lifetime US1832970A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US330182A US1832970A (en) 1920-12-15 1929-01-04 Apparatus for cracking oil

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US430870A US1703617A (en) 1920-12-15 1920-12-15 Process for cracking oil
US330182A US1832970A (en) 1920-12-15 1929-01-04 Apparatus for cracking oil

Publications (1)

Publication Number Publication Date
US1832970A true US1832970A (en) 1931-11-24

Family

ID=26987152

Family Applications (1)

Application Number Title Priority Date Filing Date
US330182A Expired - Lifetime US1832970A (en) 1920-12-15 1929-01-04 Apparatus for cracking oil

Country Status (1)

Country Link
US (1) US1832970A (en)

Similar Documents

Publication Publication Date Title
US1832970A (en) Apparatus for cracking oil
US1821750A (en) Process of cracking oil
US1703617A (en) Process for cracking oil
US1674827A (en) Process and apparatus for cracking oil
US1887039A (en) Apparatus for converting hydrocarbons
US1537593A (en) Process for cracking oil
US1806619A (en) A cobpobation op
US1852748A (en) Process and apparatus for treating hydrocarbons
US1535725A (en) Process for treating hydrocarbons
US1638093A (en) Process for cracking oil
US1821747A (en) Process for cracking oil
US1347544A (en) Method of treating hydrocarbons
US1356208A (en) Apparatus for cracking petroleum
US1839017A (en) Process of cracking oils
US1820057A (en) Process for converting hydrocarbons
US1783228A (en) Process for cracking petroleum oil
US1965334A (en) Apparatus for cracking oil
US1751729A (en) Apparatus for treating hydrocarbons
US1806618A (en) op chicago
US1850869A (en) Process of treating petroleum oil
US1716306A (en) Process and apparatus for treating oil
US1766986A (en) Apparatus for cracking oil
US1619921A (en) Process of cracking petroleum oil
US1766331A (en) Process and apparatus for cracking oil
US1638115A (en) Process of and apparatus for cracking oil