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US1795495A - Centrifugal drier - Google Patents

Centrifugal drier Download PDF

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Publication number
US1795495A
US1795495A US316139A US31613928A US1795495A US 1795495 A US1795495 A US 1795495A US 316139 A US316139 A US 316139A US 31613928 A US31613928 A US 31613928A US 1795495 A US1795495 A US 1795495A
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Prior art keywords
drum
crystals
screen
same
shaft
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US316139A
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Charles O Lavett
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D33/00Filters with filtering elements which move during the filtering operation
    • B01D33/06Filters with filtering elements which move during the filtering operation with rotary cylindrical filtering surfaces, e.g. hollow drums
    • B01D33/11Filters with filtering elements which move during the filtering operation with rotary cylindrical filtering surfaces, e.g. hollow drums arranged for outward flow filtration
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D33/00Filters with filtering elements which move during the filtering operation
    • B01D33/44Regenerating the filter material in the filter

Definitions

  • This invention relates to a centrifugal drier, whereby the operation of drying crystal laden liquids may proceed continuously and has for its object the provision of a ma:
  • the drammg of the liquid from thesolids may not only be effected expeditiously but the crystals may be also throughly washed and heated, if required, during the operation of separating l the same from the liquid.
  • Figure 1 is a vertical longitudinal section of a centrifugal drier embodying my inven-' tion.
  • Figure 2 is a horizontalsection of the same.
  • Figure 3 is an end elevation of the machine.
  • Figure 4 is a vertical cross section of the same taken on line 44Fi re 1.
  • the numerals 10 and 11 represents standards-forming parts of the main frame of the -machine and which arearranged at the 'front' and-rear ends of the same, respectively.
  • Be- 5 tween these standards is arranged an enclosing casing 13 the upper part of which is provided with an outlet 14 for theescape of obnoxious or dangerous gases or vapors separated from the mother liquor and crystals, while the lower part of the casing contains a pan 15 which catches the liquid separated from the crystals and conducts them to a discharge pipe 16 leading to the exterior of the machine.
  • a separating drum Arranged within the casing and preferably turning about a'horizontal axisis a separating drum which in the particular form shown in the drawings comprises a cylin-. drical body 17, front and rear heads 18, 19
  • the body of the separating drum is made to serve as a screen for separating solid ;matter or crystals such as sodium sulphate,
  • this screen consists of inner and outer shells 24, 25 of perforated. sheet metal, and a filter cloth 26 of finer mesh interposed between said shells.
  • Each of the heads 18, 19 of the separating drum is of skeleton or openwork form to permit passa e of material through the same 'and each of t e trunnions 20, 21 is of tubular no
  • Rotation of the drum may be effected by any suitable means, for example, by the means shown in the drawings which comprise a horizontal driving shaft 27 journaled on 05 the rear part of the mainframe and having 1 a tight pulley 28 and a loose pulley 29, and a pair of intermeshing gear wheels 30, 31 secured, respectively, to the driving shaft and the rear trunnion of the drum.
  • the front head of the drum has a conical annular deflector or distributor 32 project-.
  • raw or .crystal laden mother liquor is introduced by a feed pipe 33 which receives it from a suitable source.
  • An annulartrough, channel or gutter 34 is arranged on the rear head of the separating drumand adapted to receive the crystals which have been dried or deprived of their so free moisture by the centrifugal action of the screen in passing lengthwise through the drum from the front to the rear end of the same.
  • the crystal or dried 5 material is removed from the rear or delivery channel byone or more scoops or doctors 35 which. are mounted on the rear part-of the .frame or casing and have their inner ends projecting into the rear channel and their outer ends projecting into delivery spots 36 on the exterlor of the machine.
  • scoops or doctors 35 which. are mounted on the rear part-of the .frame or casing and have their inner ends projecting into the rear channel and their outer ends projecting into delivery spots 36 on the exterlor of the machine.
  • Within the drum are arranged means for ropelling the material under treatment rom the front to the rear end of the screen and also washing the same and heating the same if this is desired.
  • this propelling washing and heating means comprise a hollow conveyor shaft 37 arranged lengthwise on the drum and concentrically therewith and provided at its front and rear ends with tubular or hollow trunnions 38, 39 which turn" in bearings formed by the front and rear trunnions of the separating drums and extend to the exterior of the machine.
  • Rotary motion is imparted to this hollow shaft by means consisting preferably of intermeshing gear wheels 40, 41, secured, respectively, to the driving shaft and'the rear trunnion of the hollo shaft, as shown in Fig. 1.
  • propelling means Arranged close to or engaging with the bore of thescreen of the drum are means for propelling the crystals or solid material from the front to the rear end of the drum which means rotate with the hollow shaft.
  • these propelling means consist .of two longitudinal rows of propeller blades or paddles 42 arranged close to or engaging with the inner side of said screen and each blade being of helical form or inclined lentgthwise of the axis of the conveyor shaft an also preferably inclined circumferentially forward relative to a radial line, as
  • FIG. 4 The blades of each row are connected by reduced supporting arms 43 with a longitudinal bar 44 mounted on the ad acent part of the hollow shaft.
  • the crystals or solid materials can be readily scraped from the screen, even though the same has the form of a thin layer, and pass over the inner edge of the blade and readjust itself before being acted upon by the nextfollowing blade due to the fact that the narrow. blade arms intermittently interrupt the conveying action on the crystals, thereby permitting of thorough washing of the crystals and more complete extraction of the excess moisture therefrom before the crystals leave the machine.
  • the inclination of the blades is such that upon moving the hollow shaft and the drum I relatively to one another, circumferentially the blades will cause the material on the inner side to be gradually shifted lengthwise of the screen from the front end thereof to the rear outlet end of the same, whereby the screen is lengthwise of the screen and separating them, and discharging the liquid and crystals separately proceeds continuously instead ofef- .fecting this work in batches.
  • the hollow shaft carrying the blades and the drum carrying the screen are turned in the same direction but the drum turns somewhat faster than the hollow shaft due to the relative size of the pairs of gear wheels which transmit motion from the driving shaft to the drum and the conveyor which in this instance consists in making the gear wheel 30 larger than the gear wheel 31, and making the gear wheel 40 smaller than the gear wheel 41, as shown in Fig. 1.
  • this organization of gearing may be reversed so that the drum turns slower than the conveyor in which case the inclination of the conveyor bladesor paddles must also be reversed for causing the material on the screen to flow in the proper direction.
  • a diaphragm or partition 45 is arranged across the interior of the hollow conveyor shaft so as to divide the interior of the same into a front wash chamber 46 and a rear heating chamber 47, and the central part of this shaft is provided in front of this partition with a plurality of radial perforations 48 and in rear ingthe liquid from the crystals it is desired.
  • such heating may be effected by introducing steam, hot water or other heating agent into the rear chamber 47 through the hollow rear trunnion of the conveyor shaft and discharging the same through the perforations 49 against the crystals or solid material at a distance from the rear v end of screenso that the crystals will be heated and therefore yield more readily to the cleansing or other treatment to which they are subjected, before escaping from the rear end of the machine.
  • this machine By the use of this machine it is possible to dry or drain to separate'the crystals hndlike matter from liquids containing the same by a hollow shaft having trunnions journaled in the trunnions of said screen and provided with an inlet in one of its trunnions for a cleansing fluid, an inlet in its other trunnion for a heating agent, a partition in said shaft and perforations on opposite sides of said partitions for discharging said cleansing fluid and heating agent toward said screen, and conveyor blades mounted on said shaft and arranged adjacent to said screen.
  • centrifugal force continuously and expeditiously, and also subject the same during such separation to a washing as well as a heating action as best suits the particular material in hand.
  • this machine is comparatively simple and compact in construction, the same is strong and durable and not liableto get out of order, and all of the parts are readily accessible for inspection, repairs and cleaning.
  • a centrifugal drier comprising a rotary drum having a cylindrical screen body, open work heads and trunnions arranged on said heads and j ournaled; in bearings, means for supplying laden liquid to said screen,

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)

Description

March 10,1931; c. o. LAVETT 1,795,495
'CENTRIFUGAL DRIER Fi le i'oct. 31, 1928 I 2 Sheets-Sheet 1 mum Mal-ch10, 1931. lo, LAVETT I 1,795,495
7 CENTRIFUGAL DRIER Filed Oct. 51, I928 2 Sheets-Sheet 2 Patented Mar. 10, 1931.
UNITED STATES crimes 0. mvmr, or'nmuo, new You CENTBIEUGAL DRIER Application filed October a1, 1928; Serial No. 316,139.
This invention relates to a centrifugal drier, whereby the operation of drying crystal laden liquids may proceed continuously and has for its object the provision of a ma:
chine for this purpose whereby the drammg of the liquid from thesolids may not only be effected expeditiously but the crystals may be also throughly washed and heated, if required, during the operation of separating l the same from the liquid.
In the accompanying drawings w Figure 1 is a vertical longitudinal section of a centrifugal drier embodying my inven-' tion. Figure 2 is a horizontalsection of the same. Figure 3 is an end elevation of the machine. Figure 4 is a vertical cross section of the same taken on line 44Fi re 1.
In the following description similar characters of reference indicate like parts in the several figures of the drawings.
The numerals 10 and 11 represents standards-forming parts of the main frame of the -machine and which arearranged at the 'front' and-rear ends of the same, respectively. Be- 5 tween these standards is arranged an enclosing casing 13 the upper part of which is provided with an outlet 14 for theescape of obnoxious or dangerous gases or vapors separated from the mother liquor and crystals, while the lower part of the casing contains a pan 15 which catches the liquid separated from the crystals and conducts them to a discharge pipe 16 leading to the exterior of the machine.
Arranged within the casing and preferably turning about a'horizontal axisis a separating drum which in the particular form shown in the drawings comprises a cylin-. drical body 17, front and rear heads 18, 19
mounted on the front and rear ends of the body, and front and reartrunnions 20, 21
extending forwardly and rearwardly from the front and rear heads and journaled, respective'ly, in bearings 22, 23 on the front and rear standards of the frame, as shown in Figure 1.'
The body of the separating drum is made to serve as a screen for separating solid ;matter or crystals such as sodium sulphate,
sodium chlorid, sugar and salt,from the mother liquid.- In itspreferred form this screen consists of inner and outer shells 24, 25 of perforated. sheet metal, and a filter cloth 26 of finer mesh interposed between said shells.
Each of the heads 18, 19 of the separating drum is of skeleton or openwork form to permit passa e of material through the same 'and each of t e trunnions 20, 21 is of tubular no Rotation of the drum may be effected by any suitable means, for example, by the means shown in the drawings which comprise a horizontal driving shaft 27 journaled on 05 the rear part of the mainframe and having 1 a tight pulley 28 and a loose pulley 29, and a pair of intermeshing gear wheels 30, 31 secured, respectively, to the driving shaft and the rear trunnion of the drum.
The front head of the drum has a conical annular deflector or distributor 32 project-.
ing forwardly therefrom into which the full,
raw or .crystal laden mother liquor is introduced by a feed pipe 33 which receives it from a suitable source. An annulartrough, channel or gutter 34 is arranged on the rear head of the separating drumand adapted to receive the crystals which have been dried or deprived of their so free moisture by the centrifugal action of the screen in passing lengthwise through the drum from the front to the rear end of the same.
As the drum rotates the crystal or dried 5 material is removed from the rear or delivery channel byone or more scoops or doctors 35 which. are mounted on the rear part-of the .frame or casing and have their inner ends projecting into the rear channel and their outer ends projecting into delivery spots 36 on the exterlor of the machine. Within the drum are arranged means for ropelling the material under treatment rom the front to the rear end of the screen and also washing the same and heating the same if this is desired. In the preferred form this propelling washing and heating means comprise a hollow conveyor shaft 37 arranged lengthwise on the drum and concentrically therewith and provided at its front and rear ends with tubular or hollow trunnions 38, 39 which turn" in bearings formed by the front and rear trunnions of the separating drums and extend to the exterior of the machine. Rotary motion is imparted to this hollow shaft by means consisting preferably of intermeshing gear wheels 40, 41, secured, respectively, to the driving shaft and'the rear trunnion of the hollo shaft, as shown in Fig. 1.
. Arranged close to or engaging with the bore of thescreen of the drum are means for propelling the crystals or solid material from the front to the rear end of the drum which means rotate with the hollow shaft. In their preferred form these propelling means consist .of two longitudinal rows of propeller blades or paddles 42 arranged close to or engaging with the inner side of said screen and each blade being of helical form or inclined lentgthwise of the axis of the conveyor shaft an also preferably inclined circumferentially forward relative to a radial line, as
shown in Fig. 4. The blades of each row are connected by reduced supporting arms 43 with a longitudinal bar 44 mounted on the ad acent part of the hollow shaft.
By thus making the blade wide and short and connecting the same by narrow arms with the narrow support the crystals or solid materials can be readily scraped from the screen, even though the same has the form of a thin layer, and pass over the inner edge of the blade and readjust itself before being acted upon by the nextfollowing blade due to the fact that the narrow. blade arms intermittently interrupt the conveying action on the crystals, thereby permitting of thorough washing of the crystals and more complete extraction of the excess moisture therefrom before the crystals leave the machine.
The inclination of the blades is such that upon moving the hollow shaft and the drum I relatively to one another, circumferentially the blades will cause the material on the inner side to be gradually shifted lengthwise of the screen from the front end thereof to the rear outlet end of the same, whereby the screen is lengthwise of the screen and separating them, and discharging the liquid and crystals separately proceeds continuously instead ofef- .fecting this work in batches.
In the preferred manner of operating the machine the hollow shaft carrying the blades and the drum carrying the screen are turned in the same direction but the drum turns somewhat faster than the hollow shaft due to the relative size of the pairs of gear wheels which transmit motion from the driving shaft to the drum and the conveyor which in this instance consists in making the gear wheel 30 larger than the gear wheel 31, and making the gear wheel 40 smaller than the gear wheel 41, as shown in Fig. 1. If desired this organization of gearing may be reversed so that the drum turns slower than the conveyor in which case the inclination of the conveyor bladesor paddles must also be reversed for causing the material on the screen to flow in the proper direction.
Obviously the same results can be secured by turning the drum and conveyor in opposite directions by a suitable driving mechanism and inclining the blades in the appropriate manner for causing the trend of the material under treatment to be lengthwise from the front to the rear of the machine.
It sometimes is necessary or desirable to wash the crystals or solid materials during the draining operation, and at times the character of the materials necessitate the application of heat to get the best results. To accomplish this in the present machine a diaphragm or partition 45 is arranged across the interior of the hollow conveyor shaft so as to divide the interior of the same into a front wash chamber 46 and a rear heating chamber 47, and the central part of this shaft is provided in front of this partition with a plurality of radial perforations 48 and in rear ingthe liquid from the crystals it is desired.
to add water thereto for cleaning them, or to add some other liquid thereto for producing some particular result, this can be done by introducing such wash water or other liquid to the front chamber 46 through the front hollow trunnion of the conveyor shaft whereby this auxiliary liquid is supplied to the crystals after the latter have been Fartially or wholly drained of liquid on the rout end partition with a plurality of perforauid supply chamber of the conveyor shaft with perforations, thereby enabling the screen to either wholly dry or partially dry the crystals before adding further liquid thereto.
If for any reason it is desirable to heat the material under treatment, as for example, when impurities will separate therefrom and escape with the wash water, such heating may be effected by introducing steam, hot water or other heating agent into the rear chamber 47 through the hollow rear trunnion of the conveyor shaft and discharging the same through the perforations 49 against the crystals or solid material at a distance from the rear v end of screenso that the crystals will be heated and therefore yield more readily to the cleansing or other treatment to which they are subjected, before escaping from the rear end of the machine.
This action of the heating medium is possible by providing only the front part of the chamber 47 with perforations 49 leaving the rear part of the same imperforate, as shown in Figs. 1 and 2.
By the use of this machine it is possible to dry or drain to separate'the crystals hndlike matter from liquids containing the same by a hollow shaft having trunnions journaled in the trunnions of said screen and provided with an inlet in one of its trunnions for a cleansing fluid, an inlet in its other trunnion for a heating agent, a partition in said shaft and perforations on opposite sides of said partitions for discharging said cleansing fluid and heating agent toward said screen, and conveyor blades mounted on said shaft and arranged adjacent to said screen.
In testimony whereof I hereby afiix my signature.
' CHARLES O. LAVETT.
centrifugal force continuously and expeditiously, and also subject the same during such separation to a washing as well as a heating action as best suits the particular material in hand.
Moreover, this machine is comparatively simple and compact in construction, the same is strong and durable and not liableto get out of order, and all of the parts are readily accessible for inspection, repairs and cleaning.
Furthermore when the crystal laden liquid is introduced by the feed pipe into the conical distributor the same is quickly spread out by this distributor to the screen and brought under the influence of the blades so that the drying operation begins immediately and permits a larger amount of material to be handled by the expenditure of a smaller amount of power.
I- claim as iny invention 1. A centrifugal drier comprising a rotary drum having a cylindrical screen body, open work heads and trunnions arranged on said heads and j ournaled; in bearings, means for supplying laden liquid to said screen,
and means for propelling the material
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Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2426126A (en) * 1944-03-16 1947-08-19 Western States Machine Co Method and apparatus for affining sugar
US3371426A (en) * 1965-07-19 1968-03-05 Egg Vi Tein Company Dehydrating drum
US3388733A (en) * 1963-06-17 1968-06-18 Jackering Gunter Process and apparatus for the separation of suspensions
US3396088A (en) * 1964-04-01 1968-08-06 Rene G Levaux Rotary multi-compartment distillation drum having radially adjustable outlet to varythickness of liquid layer
US3932284A (en) * 1975-01-06 1976-01-13 Cominco Ltd. Barrel shaped mercury separator with spoked agitator
US4493768A (en) * 1982-09-06 1985-01-15 Sulzer-Escher Wyss Ltd. Twin pusher centrifuge including rotatable pusher
EP0207340A3 (en) * 1985-07-05 1987-06-24 Chr. Wandel GmbH + Co. Screening apparatus, particularly for screening pulp suspensions for paper making
DE4124337A1 (en) * 1991-07-23 1993-01-28 Rudolf Pelzer THICK FILM EVAPORATOR
US6156193A (en) * 1999-01-25 2000-12-05 Caterpillar Inc. Centrifugal oil filter with particle retention

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2426126A (en) * 1944-03-16 1947-08-19 Western States Machine Co Method and apparatus for affining sugar
US3388733A (en) * 1963-06-17 1968-06-18 Jackering Gunter Process and apparatus for the separation of suspensions
US3396088A (en) * 1964-04-01 1968-08-06 Rene G Levaux Rotary multi-compartment distillation drum having radially adjustable outlet to varythickness of liquid layer
US3371426A (en) * 1965-07-19 1968-03-05 Egg Vi Tein Company Dehydrating drum
US3932284A (en) * 1975-01-06 1976-01-13 Cominco Ltd. Barrel shaped mercury separator with spoked agitator
US4493768A (en) * 1982-09-06 1985-01-15 Sulzer-Escher Wyss Ltd. Twin pusher centrifuge including rotatable pusher
EP0207340A3 (en) * 1985-07-05 1987-06-24 Chr. Wandel GmbH + Co. Screening apparatus, particularly for screening pulp suspensions for paper making
DE4124337A1 (en) * 1991-07-23 1993-01-28 Rudolf Pelzer THICK FILM EVAPORATOR
US5256250A (en) * 1991-07-23 1993-10-26 Rudolf Pelzer Thin film evaporator
US6156193A (en) * 1999-01-25 2000-12-05 Caterpillar Inc. Centrifugal oil filter with particle retention

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