US1647273A - Apparatus for extracting volatile matter - Google Patents

Apparatus for extracting volatile matter Download PDF

Info

Publication number
US1647273A
US1647273A US111712A US11171226A US1647273A US 1647273 A US1647273 A US 1647273A US 111712 A US111712 A US 111712A US 11171226 A US11171226 A US 11171226A US 1647273 A US1647273 A US 1647273A
Authority
US
United States
Prior art keywords
cylinder
tumbler
volatile matter
vanes
extracting volatile
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
US111712A
Inventor
Clayton-Kennedy Kenneth Edgar
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.)
AMERICAN HYDROCARBON Co Inc
Original Assignee
AMERICAN HYDROCARBON CO Inc
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 AMERICAN HYDROCARBON CO Inc filed Critical AMERICAN HYDROCARBON CO Inc
Priority to US111712A priority Critical patent/US1647273A/en
Application granted granted Critical
Publication of US1647273A publication Critical patent/US1647273A/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
    • C10G1/00Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
    • C10G1/02Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal by distillation

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Wood Science & Technology (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Crushing And Pulverization Processes (AREA)
  • Carbon And Carbon Compounds (AREA)

Description

Nov. 1,1927. v ,6 7,273
K. E. CLAYTON-KENNEDY APPARATUS FOR EXTRACTING VOLATILE MATTER Filed May 26, 1926 ATTORNEYS Patented Nov l, I
UNITED STATES,
PATENT OFFICE.
KENNETH EDGAR CLAYTON-KEE'NEDY, OF NEW YORK, N. Y., ASSIGNOR '10 AMERICAN HYDROCARBON CO. INC., A CORPORATION OF DELAWARE.
APPARATUS FOR EXTRACTING VOLATILE MATTER.
Application filed May 26,
machine utilized in accomplishing the re- 1o sults above mentioned.
It is the purpose of my invention to prevent caking caused by heating the particles of finely divided coal or other material used thereby assuring a more even and uniform heating of the'material than heretofore obtained and create a. machine of greater capacity and efiiciency. Other objects will be apparent from the development of the construction and description.
In accordance with my invention I place in the heated cylinder containing the carbonaceous material a tumbler or agitator which will agitate and disturb, as well as fall upon and break up any agglomerated lumps of material. The advantages of such a device will be obvious when it is .considered that heretofore only disturbing baffles-or fins secured to the cylinder have been used.
Further features of my invention will appear from the following description taken in consideration with the drawings and the appended claims:
Figure 1 is a side elevation of a machine embodying my invention.
Figure 2 is a sectional view taken along 2'2 of Figure 1.
Figure 3 is a perspective view of the tumbler or agitator. I
I have illustrated my invention as applied to the conventional apparatus as indicated in Figural wherein 1 is the inclined rotating cylinderin which material to be treated is heated. The material is fed into the cylinder through the hopper 3 where it travels gradually down the length of the cylinder by the action of gravlty aided by rotation of the cylinder until the volatile substances have been driven out due to application of heat. The spent material passes through the discharge end 5 while the gases pass "out through discharge 11 by means of a pump 13, are condense 1n the condenser 15 and thereafter collected insultable containers.
vanes I have cut openings 31, 33 arranged regular contours suchas sharp teeth or the rial.
1926. Serial No. 111,712.
Heating may be accomplished through the medium of molten lead 7 which is'kept in a molten state by means of burners 9'or by any other suitable means. The usual drivmg motor is indicated at 17 for rotating cyllnder 1. It is understood of course that the cylinder and discharge ends are sealed agalnst entry of oxygen by, sealing the ends from the outside atmosphere.
The above brief description merely outlines the conventional apparatus and it has been found that there is a strong tendency for the particles of material to adhere, agglomerate and cake when heated in these machines thereby destroying the ideal condi- 7 tlons necessary to assure uniform and rapid heating of allthe particles of material.
To overcome this caking I find it-convenlent to place in the cylinder a tumbler or agltator 19. This tumbler is substantially 7 the same length as the cylinder but smallerm diameter so that it is capable of tumbling around in thecylinder. This tumbler is merely placed within the cylinder without securing -1t in any manner except to prevent the tumbler from sliding axially out of the cylinder by placing a spider 21 in the discharge end of the cylinder or by holding with a chain from the upper end.
As a preferred form I have shown this tumbler in Figure 3 as being formed of four vanes 23, 25, 27, 29, substantially at right angles to each other intersecting at and extending from a common axis. Within these in relatively staggered position for the purpose of allowin any material picked up by, the vanes to si' t through to the bottom of the cylinder.
The design of the tumbler may be varied to meet the demands of a particular material to be broken up, for instance, there may be three vanes or of star formation, or the edges of the respective vanes may have ir- 10o vanes may be formed of a corrugated mate- The tumbler is preferably of some heavy material such as iron or steel in order to'have sufficient mass to crush the carbonaceous material and also to withstand the operating temperatures.
In operation themachine functions inthe following manner. The cylinder containing the carbonaceous material and the tumbler is caused to rotate by means of motor 17 Due to the friction between the vanes, the material and the inner periphery of cylinder 1 tumbler 19 is carried up with the wall vthe rotating cylinder until a certain level is 5 reached whereupon the tumbler will dro upon the material and break up an oak portions. Duringthe movement of the tumler, the vanes will also carry some of the material u on their surfaces and this inaterial will si through openings .31, 33 and be re-distributed throughout the cylinder. Each time the tumbler reaches a certain level it 'will drop down upon the material and so the cycles will be re eated maintainin material in'a finely divided and distri state.
the uted intersecting in a common axis, said .vanes having openings therein arranged in staggered relationship,
In witness whereof, my signature.
KENNETH E. CLAYTON KENNEDY I hereunto subscribe
US111712A 1926-05-26 1926-05-26 Apparatus for extracting volatile matter Expired - Lifetime US1647273A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US111712A US1647273A (en) 1926-05-26 1926-05-26 Apparatus for extracting volatile matter

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US111712A US1647273A (en) 1926-05-26 1926-05-26 Apparatus for extracting volatile matter

Publications (1)

Publication Number Publication Date
US1647273A true US1647273A (en) 1927-11-01

Family

ID=22340051

Family Applications (1)

Application Number Title Priority Date Filing Date
US111712A Expired - Lifetime US1647273A (en) 1926-05-26 1926-05-26 Apparatus for extracting volatile matter

Country Status (1)

Country Link
US (1) US1647273A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5082534A (en) * 1990-03-14 1992-01-21 Wayne Technology, Inc. Pyrolytic conversion system
US5225044A (en) * 1990-03-14 1993-07-06 Wayne Technology, Inc. Pyrolytic conversion system
US5687092A (en) * 1995-05-05 1997-11-11 Nordson Corporation Method of compensating for changes in flow characteristics of a dispensed fluid
US6139903A (en) * 1989-06-16 2000-10-31 Nordson Corporation Method of compensating for non-linear characteristics in dispensing a coating material

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6139903A (en) * 1989-06-16 2000-10-31 Nordson Corporation Method of compensating for non-linear characteristics in dispensing a coating material
US5082534A (en) * 1990-03-14 1992-01-21 Wayne Technology, Inc. Pyrolytic conversion system
US5225044A (en) * 1990-03-14 1993-07-06 Wayne Technology, Inc. Pyrolytic conversion system
US5687092A (en) * 1995-05-05 1997-11-11 Nordson Corporation Method of compensating for changes in flow characteristics of a dispensed fluid
US5920829A (en) * 1995-05-05 1999-07-06 Nordson Corporation Method of compensating for changes in flow characteristics of a dispensed fluid
US5995909A (en) * 1995-05-05 1999-11-30 Nordson Corporation Method of compensating for changes in flow characteristics of a dispensed fluid

Similar Documents

Publication Publication Date Title
US3645659A (en) Extruding plastic
US2339932A (en) Chemical process
US1647273A (en) Apparatus for extracting volatile matter
US2470315A (en) Multiple stage pulverizing and dehydrating tube mill
US2098024A (en) Vacuum drier with centrifugal dust separator
US2452135A (en) Paper pulp machine
US2128848A (en) Process for treating raw clay materials
US2903400A (en) Apparatus for low temperature distillation of carbonaceous materials
US3221999A (en) Material refining machine
US2340456A (en) Attrition mill
US1276879A (en) Process of extracting hydrocarbon materials from shale and similar earthy material.
US2514616A (en) Pelleting magnesium dust
US2485128A (en) Pelleting magnesium dust
US3640849A (en) Spent shale retort with sonic oscillator clinker cutter
US1717786A (en) Apparatus for distilling oil shale
GB286739A (en) Improvements relating to centrifugal machines and the centrifugal separation of liquids from mixtures of liquids and solid particles
US2276589A (en) Drier
US2090177A (en) Method of and apparatus for drying special materials
US2201552A (en) Apparatus for treating pulverulent materials
US3221788A (en) Emulsifier
US3271018A (en) Rotary calcining kiln
US2258518A (en) Rotary kiln lining
US2587639A (en) Rotary kiln for the recovery of acid values
US1952647A (en) Extraction of asphalt
US1405183A (en) Process for the production of anhydrous aluminum chloride