US1428159A - Oil-topping plant - Google Patents

Oil-topping plant Download PDF

Info

Publication number
US1428159A
US1428159A US310533A US31053319A US1428159A US 1428159 A US1428159 A US 1428159A US 310533 A US310533 A US 310533A US 31053319 A US31053319 A US 31053319A US 1428159 A US1428159 A US 1428159A
Authority
US
United States
Prior art keywords
oil
coils
receptacle
topping
plant
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
US310533A
Inventor
Gallsworthy Benjamin
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to US310533A priority Critical patent/US1428159A/en
Application granted granted Critical
Publication of US1428159A publication Critical patent/US1428159A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D3/00Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
    • B01D3/008Liquid distribution
    • 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

  • This-invention relates to new and useful improvements in'an oil topping. plant.
  • One object of the. invention is to provide a device of the character described which is primarily intended for topping.
  • crude petroleum that is, for extracting the lighter elements such as gasoline and kerosene there from, and in the process, ridding the oil of water, leavingv a residuum which is suitable for fuel oil (or which may be further treat ed in the process of refinmg'the same).
  • the water contained in the oil when heated,
  • Another object of the invention is to provide a device of the character described which is simple in construction, and which be cheaply and easily erected, and which,
  • Figure 1 is avertical sectional view of the device taken on the line 1-1 of Figure 2.
  • Figure 2 is a transverse sectional viewv principal part of the heat from the furnace and the main refining process takes place atv the bottom of the receptacle, where the oil j rises to submerge said coils.
  • the. numeral 1 refers-to a furnace and located adjacent thereto, there is the container 2.
  • the container 2 thereare a plurality of pipes 33, arranged in vertically extending coils, one. end of eachpipe communicating with the furnace, and the other ends communicating With the manifold, arranged abovethe furnace, and leading from this manifold, there is the outlet pipe 5, connectedto which is the suction fan 6, which induces a current of hot air from the furnace through the pipes 3.
  • the pipes 3 are arranged" in vertical coils, being composed of parallel sections arrangedone above the other, and connected at their respective ends to form a continuous conduit.
  • Each section .of each pipe is located within a hopper, said hoppers consisting of downwardly converging de-..c vflectors 7,7, formed of metallic plates which are anchored at their respective ends to the correspondlng ends of the receptacle 2, and spaced a suitabledistance from-the respectivecoils of pipe.
  • each coil there is an inlet pipe 8, said pipes havingtheirum dersides perforated, and the crude oil is admitte'd'tosaid pipes 8, from the manifold 9 into which the 011 is fed through the inlet pipelO.
  • sene are vaporized, and rise in the receptacle and passinto the domes 11,11, and thence out through the conduits 12, to the con-.
  • A'guage 15 is groyided at one end of the receptacle "cats the amount of oil therein and leading from the bottom of the receptacle,
  • neaehae heavier, aw eolllected in the receptacle may be drawn ed to he used as fuel or for further refiningas desired.
  • g I w I A device ofthe character] described, including a receptacle, a furnace arranged ad jacent thereto, an outlet manifold, flue pipes connected at one end directly into said furmace and arranged in vertical coils, in said receptacle and their other ends terminating in' said manifold, oil inlet-pipes arranged above the respective coils and whose under! sides are'proridedwith perforations through which crude oil may be discharged onto the re ective coils, downwardly. convex-gin baes arranged on opposite.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Description

B. GALLSWORTHY.
OIL TOPPING PLANT.
APPLICATION FILED JULY 14. 19w.
Patented Sept. 5, 1922.
2 SHEETSSHEET 1.
B. GALLSWORTHY.
OIL TOPPING PLANT.
APPLICATION FILED JULY 14. I919.
1 428, 1 5 9 Patented Sept. 5, 1922,
2 SHEETSSHEET 2.
ammo/whoa mum of expansion and. foaming of the oil lighter elements such as gasoline and keroview.
BENJAMIN eannswon'rnr; or rear amnion, rnxas.
' 'orn-rorrme Application filed my 14;
" it may concem I Be it known that I, BENJAMIN GALLswon'rmr, a subject 'of'the King o f Great Britain, residing at Port Arthur, 1n the county of J elferson and State of'Texas, have invented certain new and useful Improve-. 'mentsin an Oil-Topping. Plant, of which the following is a specification.
This-invention relates to new and useful improvements in'an oil topping. plant.
One object of the. invention is to provide a device of the character described which is primarily intended for topping. crude petroleum, that is, for extracting the lighter elements such as gasoline and kerosene there from, and in the process, ridding the oil of water, leavingv a residuum which is suitable for fuel oil (or which may be further treat ed in the process of refinmg'the same). In refining crude petroleum; particularly heavy petroleum byi stills now in common use, the water contained in the oil, when heated,
often causes an expansion and foaming of the oil to such a degree that the still runs over, causing a waste of the oil and retard ing the refining process; It is the objectof this invention to provide a device of the.
character described whereby the water may be wholly or partially extracted from the oil during a preliminarystage of-refinement, and in such a manner, there will be a miniincident to the evaporation of the water the result that the succeeding or final process will not be retarded or interfered with.
- Another object of the invention is to provide a device of the character described which is simple in construction, and which be cheaply and easily erected, and which,
' coils of pipe. For this-reason, the deflecmay is eficient for the purpose intended. With the above and other objects in view,
the invention has particular relation to cer f tainnovel features of constructlon, operation and arrangement of parts, an example of which is given in this specification and illustrated in the accompanying drawings,
wherein:
Figure 1, is avertical sectional view of the device taken on the line 1-1 of Figure 2. 3
Figure 2, is a transverse sectional viewv principal part of the heat from the furnace and the main refining process takes place atv the bottom of the receptacle, where the oil j rises to submerge said coils. "Consequently,
taken on t e line 2-2 of Figure 1, and I Figure is an enlarged fragmentaryend Beferring now more particularly toQ the a i. T.
191a. aerial no. 310,538.
ra gs wherein likenumerals of refer-- ence designate similar parts in each of the Y figures, the. numeral 1, refers-to a furnace and located adjacent thereto, there is the container 2. Within this container, thereare a plurality of pipes 33, arranged in vertically extending coils, one. end of eachpipe communicating with the furnace, and the other ends communicating With the manifold, arranged abovethe furnace, and leading from this manifold, there is the outlet pipe 5, connectedto which is the suction fan 6, which induces a current of hot air from the furnace through the pipes 3.
As above stated, the pipes 3 are arranged" in vertical coils, being composed of parallel sections arrangedone above the other, and connected at their respective ends to form a continuous conduit. Each section .of each pipe is located within a hopper, said hoppers consisting of downwardly converging de-..c vflectors 7,7, formed of metallic plates which are anchored at their respective ends to the correspondlng ends of the receptacle 2, and spaced a suitabledistance from-the respectivecoils of pipe. A'bove each coil, there is an inlet pipe 8, said pipes havingtheirum dersides perforated, and the crude oil is admitte'd'tosaid pipes 8, from the manifold 9 into which the 011 is fed through the inlet pipelO. C-
When the oil strikes the heated coils, the
sene are vaporized, and rise in the receptacle and passinto the domes 11,11, and thence out through the conduits 12, to the con-.
pended incident to evaporation, causing a oaming or ebullition ofthe oil aroundthe tors 7, 7, have been. providedtoconfine the oil, and direct itonto thecoils" underneath.
The oil' thus gradually finds its way down over the succeeding coilsto the bottom of quired' degree to cause it to give off the point. These submerged coils absorb the 'the unsuhmerged coils have a much lower temperature than they wouldotherwise have, and are not sufficiently heated to cause-car- I hon to form on them.
As above stated, the lower turns or'se ctions of the coils which are submerged in the oil collecting at the bottom of the receptacle, perform part of the refining I recess, in
heatin the oil collecting in sai receptac e to a high temperature, causing itto giveofi any mov by the unsubmerged coils, necessary lighter elements.
If the receptacle is not insulated, there will be a certain amount of condensation on the inner walls of the receptacle 2, and this 1 will trickle down into'the, trough at 3, carried by the inner wall of the receptacle near the bottom'thereof, and may be led ofl out through the outlet conduits 1t, 1t. A'guage 15 is groyided at one end of the receptacle "cats the amount of oil therein and leading from the bottom of the receptacle,
' there is a drain pipe 16, from which the asoline, water or kerosene, not re,
neaehae heavier, aw eolllected in the receptacle may be drawn ed to he used as fuel or for further refiningas desired.
tll.claimis: g I w I A device ofthe character] described, including a receptacle, a furnace arranged ad jacent thereto, an outlet manifold, flue pipes connected at one end directly into said furmace and arranged in vertical coils, in said receptacle and their other ends terminating in' said manifold, oil inlet-pipes arranged above the respective coils and whose under! sides are'proridedwith perforations through which crude oil may be discharged onto the re ective coils, downwardly. convex-gin baes arranged on opposite. sides of eac of the respective turns of the coils and having their lower edges spaced apart throughout their length, and provided to direct the oil passing over each turn down onto the turn underneath, and an outlet leading from the receptacle above the lower coils In testimony whereof I have'signed my name to this specification the presence of two subscribingwitnesses. Y
. BENJAMIN GALLSWURTHY.
Witnseses: I I v ENV. HanowAr,
llnnnn Balms.
US310533A 1919-07-14 1919-07-14 Oil-topping plant Expired - Lifetime US1428159A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US310533A US1428159A (en) 1919-07-14 1919-07-14 Oil-topping plant

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US310533A US1428159A (en) 1919-07-14 1919-07-14 Oil-topping plant

Publications (1)

Publication Number Publication Date
US1428159A true US1428159A (en) 1922-09-05

Family

ID=23202934

Family Applications (1)

Application Number Title Priority Date Filing Date
US310533A Expired - Lifetime US1428159A (en) 1919-07-14 1919-07-14 Oil-topping plant

Country Status (1)

Country Link
US (1) US1428159A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4904345A (en) * 1986-12-03 1990-02-27 Mccants Malcolm Method and apparatus for cleaning petroleum emulsion
WO1996037740A1 (en) * 1995-05-25 1996-11-28 American Standard Inc. Falling film evaporator with refrigerant distribution system
WO1996037741A1 (en) * 1995-05-25 1996-11-28 American Standard Inc. Falling film evaporator with vapor-liquid separator
CN103890523A (en) * 2011-09-09 2014-06-25 三井海洋开发株式会社 Falling liquid film heat exchanger, absorption refrigeration system, ship, offshore structure, and underwater structure

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4904345A (en) * 1986-12-03 1990-02-27 Mccants Malcolm Method and apparatus for cleaning petroleum emulsion
WO1996037740A1 (en) * 1995-05-25 1996-11-28 American Standard Inc. Falling film evaporator with refrigerant distribution system
WO1996037741A1 (en) * 1995-05-25 1996-11-28 American Standard Inc. Falling film evaporator with vapor-liquid separator
GB2313903A (en) * 1995-05-25 1997-12-10 American Standard Inc Falling film evaporator with refrigerant distribution system
GB2315849A (en) * 1995-05-25 1998-02-11 American Standard Inc Falling film evaporator with vapor-liquid separator
GB2313903B (en) * 1995-05-25 1999-08-25 American Standard Inc Evaporator with refrigerant distributor
GB2315849B (en) * 1995-05-25 1999-10-27 American Standard Inc Evaporator with falling film and flooded evaporator portions
CN103890523A (en) * 2011-09-09 2014-06-25 三井海洋开发株式会社 Falling liquid film heat exchanger, absorption refrigeration system, ship, offshore structure, and underwater structure
CN103890523B (en) * 2011-09-09 2016-05-04 三井海洋开发株式会社 Fallig film heat exchanger, absorption chiller system and boats and ships, oceanic tectonic thing, underwater structures thing
US10222127B2 (en) 2011-09-09 2019-03-05 Modec, Inc. Falling film heat exchanger, absorption refrigerator system, ship, offshore structure and underwater offshore structure

Similar Documents

Publication Publication Date Title
US1428159A (en) Oil-topping plant
EP2134812A1 (en) High-performance chamber mixer for catalytic oil suspensions
US1870193A (en) Method of and apparatus for distillation of hydrocarbon oils
US1428458A (en) Process and apparatus for recovery of hydrocarbons from oil shale
US1490213A (en) Process for treating oil shale
US1547993A (en) Pressure still
US1886621A (en) Cracking still and process
US2140276A (en) Continuous coking of hydrocarbon oils
US1490576A (en) Oil saver
US1765159A (en) Smoke condenser
US1783697A (en) Method and apparatus for cracking oil
US728257A (en) Apparatus for continuously distilling petroleum.
US2286329A (en) Water heater
US1958267A (en) Process for treating hydrocarbon oils
US1562690A (en) Still
US1561758A (en) Apparatus for distilling oil
US1646448A (en) Oil-distilling apparatus and method
US1296244A (en) Process of refining, fractionating, and reducing oils.
US1921603A (en) Method and apparatus for cracking oils
US2749289A (en) Apparatus for treating petroleum
US1561169A (en) Hydrocarbon distillation
US1685476A (en) of chicago
US1893907A (en) Fractionating method
US1671423A (en) Apparatus for the treatment of hydrocarbon compounds
US1741510A (en) Process of cracking oil