USRE17233E - de bajligethy - Google Patents

de bajligethy Download PDF

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Publication number
USRE17233E
USRE17233E US17233DE USRE17233E US RE17233 E USRE17233 E US RE17233E US 17233D E US17233D E US 17233DE US RE17233 E USRE17233 E US RE17233E
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United States
Prior art keywords
shell
drum
line
furnace
fluid
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Expired
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    • 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
    • C10G7/00Distillation of hydrocarbon oils

Definitions

  • i' elements may-,bg separitedfmm thi@ heavier jfelenints thrbff nd by theirs@ ⁇ Of Whiclizthe Mislfof" explsinf dliringthe distilling prof ⁇ i essfwillfbergra'tly 'ls/Selle@ l f l V Arlfherobieib of the invention@ t9 IPT@- yide'fiin apparatus Ofyfheliafacigen described f s ff illimite@ Shelli andlfhef'e @minfin-heat i "i retaining 4coating which ingame caghs, would prev-emmen being deposited on fthefborwm.
  • the hydro-carbon Will be delivered into the reaction drum7 at a high.temperature and underhigh pressure.
  • the valvelO may be closed until t-he required pressure in the reaction drum 7 isobtained and 'then slightly 'opened so as to permit the continual dis,-
  • the hydro-carbon Within the outer shell y1 Will be of somewhat lower temperature and lower pressure than that of the hydro-carbon in the re-action drum 7 and the vapors evolved by the release of the hydro-carbon through the nozzle 9 from higher pressure to a lower pressure Will operate 'to releasethe lighter elements or vapors from the fluid of higher pressure and t-he released vapors Will be of very high temperature and Will be distributedv through the fluid inthe outer shell and will keep such fluid in a state of constant turbulence resultingin a greater yyield of lighter elements than would be otherwise obtainable.
  • ThishousingI consists of an enlarged tube which surrounds the coil 5, in thefurnace, andis spaced therefrom.
  • the upper turn ⁇ of the housing y coil carries a container 17, and a fused metal is poured into' said container and fills the housing 15, and is kept in circulation by means of a vpump 18 VWhich is connected into a circulating 1ine'19, which is connected atV one end into the bottom turn of the housing coil, and at its other end into the container 17.
  • This fused metal is thus ⁇ kept in circulatio'n about' the coil 5 Within the housing 15, and its chief purpose is to'keepsaid housing from becoming too hot, and burned out and at the same time to permit the proper heat-ing of the coil 5.
  • AThe fused metal may be composed of lead and bismuth o ⁇ r a combination ofv other metals having a low melting point and a boilingpoint not lovver than (00 degrees F.
  • the line 20 is provided with a trap 22 in which the fused metal carried by the discharging hydrocarbon vivill collec-t and it Will drain back into the container 17 y through Vthe drain pipe 23.
  • Y y l lnstead ofthe fused metal anyother liquid bat-h for the coil 5 may beused Which may be found to bepralctical.
  • a still including Aan outer shell, anrinle't 'line entering said shell,l a furnace, said inlet Vline passing through'said'furnace, a housing surrounding the line vWithin the furnace and forming a circulating chamber therearound,
  • s n '6.A' still including anvouter shell, ⁇ a high pressure reaction druni located Wholly within in :said line outside of they shell, an outlet I leading from'saidldrum into the shell, a Valve operable from Withoutthe shell land controlfv i ling said outlet, nieansconnected tothe inlet line through which ⁇ fluid inthe druin may be i maintained at a higher pressure than the fluid surrounding the drum within the shell, said i valve controlling said outlet being effective to permit the escape'- of the high pressure fluid in the drum :troin said drum to distrib utc the samethroughout the low pressure n pressure reaction drum located Wholly Within the ⁇ shell, a furnace,y an inlet line passing through said furnace, said line entering the shell and terminating in saidv drum, a valve m rin :said line ⁇ outside ofthe shell, an outlet leading from said drum into the shell, a Valve ineans connected vto the inlet line through which fluid in the drum may

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  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)

Description

March `lz, 1929.
gld
` lppl:BAJLIGETHL,FHUSTDM MEMS. 'l
"DISTILLING Ammiims.
i' elements may-,bg separitedfmm thi@ heavier jfelenints thrbff nd by theirs@` Of Whiclizthe Mislfof" explsinf dliringthe distilling prof` i essfwillfbergra'tly 'ls/Selle@ l f l V Arlfherobieib of the invention@ t9 IPT@- yide'fiin apparatus Ofyfheliafacigen described f s ff illimite@ Shelli andlfhef'e @minfin-heat i "i retaining 4coating which ingame caghs, would prev-emmen being deposited on fthefborwm.
@at Wit-l1; M1 l'lsidrnr conducting pipe i.
ind .an Qlifsiidf or' @mailing pif@ which purgidypfithe 'furnace in: has@ the inner cpi; Should `burst "thus fp'rventfng the dicharg 'niinv nu@ @15d comprenais@ novel "Cf furnace, CaSe Qftlh b'iirsii'igf Qi j th `inner C011, 'i1-ndiv avoiding an expljsio'n geinnt of parts, an Example gli? Iiin this speiflcziton and lllugtr ed' in fthe n 'cconipanyiigf drawings,
` i i .i i l. 111 the? drawlngs, thenumeml l designates A further feature of; the ,lnvientiqn residesL th l 'c' r Shelloifontaini under Whifchfthe bdrm-*SMH Q51: contain@ is filled Gr partly pres ,of constmciin, @pril container. The sediment and heavy elements will settle tothe bottom of the reaction drum thus preventing their collection on the bottom of the outer shell. The bottom of the outer shell being thus kept .clean Willnot burn out and permit the discharge of its contents into the furnace which, if it happens, causes an explosion. The re-action drum 7 also relieves the shell 1 of part of lthe pressure :to
which the hydro-carbon is subjected by the pump 4, the pressure in said reaction ,drum being much higher than the pressurein the outer shell around said reaction drum;r The lighter elements given off in the cracking process pass through the line '11"leading through the top of the 'shell to the conventional condenser as 12.'v The heavy oil may be drained from t-he shell 1 through the outlet pipe'13controllable by a Vsuitable valve- 14. In case ythe reaction drum shouldburst the pressure in the outer shell may 'falso be relieved through said pipe 13. At intervals the re-action drum`7 maybe. cleaned 'out by rermovingl one eind thereof for that purpose.
The hydro-carbon Will be delivered into the reaction drum7 at a high.temperature and underhigh pressure. The valvelO may be closed until t-he required pressure in the reaction drum 7 isobtained and 'then slightly 'opened so as to permit the continual dis,-
charge through the'nozz'le 9 but to maint-ain thepressure in the re-action 'drum 7. The hydro-carbon Within the outer shell y1 Will be of somewhat lower temperature and lower pressure than that of the hydro-carbon in the re-action drum 7 and the vapors evolved by the release of the hydro-carbon through the nozzle 9 from higher pressure to a lower pressure Will operate 'to releasethe lighter elements or vapors from the fluid of higher pressure and t-he released vapors Will be of very high temperature and Will be distributedv through the fluid inthe outer shell and will keep such fluid in a state of constant turbulence resultingin a greater yyield of lighter elements than would be otherwise obtainable.
It often happens that `the coilbursts, on account -of the pressure Within it, and the oil in said coil, in such event is drained into the furnace causing an explosion.' To kprevent this the surrounding housing 15 has` been provided. ThishousingI consists of an enlarged tube which surrounds the coil 5, in thefurnace, andis spaced therefrom. The pipe 3, of which' the coil formed, fitted through the glands 1,6, 16,011 opposite sides of thev furnace, which close thelends of said housing.` The upper turn `of the housing y coil carries a container 17, and a fused metal is poured into' said container and fills the housing 15, and is kept in circulation by means of a vpump 18 VWhich is connected into a circulating 1ine'19, which is connected atV one end into the bottom turn of the housing coil, and at its other end into the container 17. This fused metal is thus `kept in circulatio'n about' the coil 5 Within the housing 15, and its chief purpose is to'keepsaid housing from becoming too hot, and burned out and at the same time to permit the proper heat-ing of the coil 5. AThe fused metal may be composed of lead and bismuth o`r a combination ofv other metals having a low melting point and a boilingpoint not lovver than (00 degrees F.
In case thepressru'e in the coil 5 should cause the same to burst the hydrocarbon will be retainedin the. housing 15 and Will vbe forced up into the container 17 through the fused metal and'will pass out through the relief line 20, which is cont-rolled by the relief valve 21, and conducted a sufficient distance from the thereof. 4 V
The line 20 is provided with a trap 22 in which the fused metal carried by the discharging hydrocarbon vivill collec-t and it Will drain back into the container 17 y through Vthe drain pipe 23. Y y l lnstead ofthe fused metal anyother liquid bat-h for the coil 5 may beused Which may be found to bepralctical. Y y
lVhile I lhave described only'one-form4 of still to prevent an'eXplosion vthe invention itis apparent that mechanical changes may be made 1ny the embodiment thereof andA equivalents substituted for the parts shown Without departing from 'the principle of Vthe'invention and-I hereby reserve the rightto make such changes as may be found to be 'practical,or-expedientr so long as the principle embodied Within the append-` 2. A still including an outer shell, an inlet line entering said shell, a furnace, said inlet line passingv through said furnace, a housing surroundingthe line Within the furnace and 4forming a circulating chamber therearound, means for circulating a fluid through said chamber said circulating means including an outlet line leading out from said chaniber and ra trap incorporated into said outlet line.
3. A still including Aan outer shell, anrinle't 'line entering said shell,l a furnace, said inlet Vline passing through'said'furnace, a housing surrounding the line vWithin the furnace and forming a circulating chamber therearound,
means for circulating a fluid through said Cil".A
, outside of the shelllfor1ning`a circulatingv f fluid in the shell yand to maintain the luid drum in the shell into which the inlet line is y"connected, a furnace, said inlet line passing through said furnace, a'housingsurrounding fthe line Within theiu'rnace and forming a anoutlet line leading from said chamber, and .f
a trap incorporatedinto said" outlet line;
In 7a still an outer' shell, an. inlet line for thefoute'r shell, a housing around said line chamber around the line, means' for circulating a luidthrough said chamber, said circu y j lating means includingr a relief line. leading from saidchanibferand' a trap associated withv therelief line; v n
5. still includingan outer shell, an inlet line entering said shell, an enlargedfreaction l circulating chamber therearound, means for` l "the shell,l afurnace, an inlet line passing` `through said furnace, said line entering the i `shell and terminating in said drum, a valve 30 t circulating a fused met-al through said ch'annr ber,1fneans' for `forcing fluid under pressure through saidk inletline intosaid drinn, said circulating ineansincluding an outlet line leading :troni saidchainber, and a trap asso` ciated' Withthe outlet line. s n '6.A' still including anvouter shell,` a high pressure reaction druni located Wholly within in :said line outside of they shell, an outlet I leading from'saidldrum into the shell, a Valve operable from Withoutthe shell land controlfv i ling said outlet, nieansconnected tothe inlet line through which `fluid inthe druin may be i maintained at a higher pressure than the fluid surrounding the drum within the shell, said i valve controlling said outlet being effective to permit the escape'- of the high pressure fluid in the drum :troin said drum to distrib utc the samethroughout the low pressure n pressure reaction drum located Wholly Within the` shell, a furnace,y an inlet line passing through said furnace, said line entering the shell and terminating in saidv drum, a valve m rin :said line` outside ofthe shell, an outlet leading from said drum into the shell, a Valve ineans connected vto the inlet line through which fluid in the drum may befmaintained ata higher pressure than the fluid surrounding the drum Within the shell, said Valve controllingsaid outlet being effective to permit the escape of the high pressure fluid in the drum from said drum todistribute the same throughout the loW pressure .fluid inthe shell and to maintain the luid in the drum under a the shell; 4 l' In testimony. vwhereof I have signed"` Iny name to the specification.
LMAX F. DE BAJLIGETHY.
vhigher pressurexthan the fluid inthe shell, d
and alvaporline for relieving theA vapor from 50 s located Within the shell and operable from yWithout the shell and ycontrolling said outlet,
US17233D de bajligethy Expired USRE17233E (en)

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