US1861184A - Method for converting liquid paper pulp into a consistent mass suitable for storage, etc., or into bales for shipment - Google Patents

Method for converting liquid paper pulp into a consistent mass suitable for storage, etc., or into bales for shipment Download PDF

Info

Publication number
US1861184A
US1861184A US406786A US40678629A US1861184A US 1861184 A US1861184 A US 1861184A US 406786 A US406786 A US 406786A US 40678629 A US40678629 A US 40678629A US 1861184 A US1861184 A US 1861184A
Authority
US
United States
Prior art keywords
pulp
storage
bales
shipment
screw
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
US406786A
Inventor
Richard T Lang
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 Voith Contact Co
Original Assignee
American Voith Contact 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 US165774A external-priority patent/US1829563A/en
Application filed by American Voith Contact Co filed Critical American Voith Contact Co
Priority to US406786A priority Critical patent/US1861184A/en
Application granted granted Critical
Publication of US1861184A publication Critical patent/US1861184A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21CPRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
    • D21C9/00After-treatment of cellulose pulp, e.g. of wood pulp, or cotton linters ; Treatment of dilute or dewatered pulp or process improvement taking place after obtaining the raw cellulosic material and not provided for elsewhere
    • D21C9/18De-watering; Elimination of cooking or pulp-treating liquors from the pulp

Definitions

  • bales for shipment Serial 165,7 74, filed b me on February 4,
  • baling press which generally is of the same type as the hydraulic dewatering ress,on1y of somewhat lighterconstru'ction.
  • the feeding equipment may comprise a trough, a hopper, a screw feeder in the cylinder part of the noun) runs runr a coxsrsrnm" mm sorranna' together require much manual work and an expensive installation, occupying an enorof the trou h.
  • the end of the cylindrical part of the trough. into which the feeding screw does not pass, is of conical shape, having its larger end towards the pressure chamber and its smaller end towards the screw.
  • the stock forced through this conical art into the pressure room is sub-- 'ect on e screw side to the pressure produced the action of the screw, on the pressure 0 amber side it is under the pressure prevailing in the air pipe connected to the pressure chamber.
  • Suitable equipment may also consist in t e arrangement, at the one end of the shaft of the screw towards the pressure chamber of a knife-like tool which scrapes small articles in even quantities from the pulp fe into the pressure chamber. These loosened particles are carried away by the compressed air passing through the pressure chamber and are transported through the adjoining piping to the distribution storage bin, baling press, hopper etc.
  • the pressure chamber is referably arranged in sucha manner that t e knife itself is almost fully out of the path of the compressed air current and only the pulp to be transported is in this path of the stream of air.
  • iig. 2 shows a lon 'tudinal section of the special pulp feeding evice 6 in larger scale.
  • 1 is the screen in which the pulp to be dewatered is freed from coarse particles, etc.
  • the fgood pulp leaves the screen in a dilution 0 1 part 0 solid matter to about 300 parts of water, which latter is partly removed in the decker 2 to a consistency of from 2 to 8% of the pulp.
  • the pulp thus redewatered is collected in a chest 3 and ows from there to the screw press 4, where the final dewatering is taking place.
  • the ressure piping 12 To the pressure chamber 7 is connected the ressure piping 12,'through which the pul ed into t e pressure chamber is blown by t e compressed air to either the storage 13, or to the cyclone 14 on the roof of the bahng department. From the cyclone in which the air is se arated fromthe ulp the latter drops into t e bin 15 and is fed om there into the hopper 16 of the baling ress 17.
  • the baling press delivers the pul in bales 18-to aconveyor or the like 19, on w ch the bales are gevices 6. The compressed acked for shi mentif necessary and whic carries them 'rectly into the I light or e warehouse for storage in case no direct shi ment is intended.
  • Fi 2 which shows the. feedin device 6 with t e pressure chamber 7 of i 1 in larger scale, 21 desi ates the troug with hopper 22 into whic the ulp is delivered from the screw press 4 of ig. 1.

Landscapes

  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Wood Science & Technology (AREA)
  • Paper (AREA)

Description

May 31, 1932'. R. T. LANG METHOD FOR CONVERTING LIQUID PAPER PULP INTO A CONSISTENT MASS SUITABLE FOR STORAGE, ETC. 0R INTO BALES FOR SHIPMENT Original Fiied Feb. 4. 1927 ATTORNEY Patent ed May 31, 1932 or EEIDBNHEIM-ON-TEE-BREHZ, sum, Assmnoa'ro .umaryorrncomac-r comranr rncoaronarnn, orgjnzw You, H. z, a coaronm.
,gron sronacn, are, 03. Intro nnmsron.
fon'i atbn aat faiea February 4, 1927, Bfiflll No. 105,774,, manta aim; application ma November 18, 1928.
1 toa method for convertingliquid paper pulp or the like into a consistent suitable for storage, etc., or
into bales for shipment.
i"II1;lthiSllpp1iC8 tlbn I have shown anddescribed apparatus shown in my copending'applicationj-for convertingnli uid paper P P into aconsistent 'suitab e for stor-,
,etc.', or into; bales for shipment, Serial 165,7 74, filed b me on February 4,
ing through the new-manufacturing method, in the present application the claims are directed to my new niethodsteps which are capable of being -carried out by any suitable apparatusfor in any convenient manner.
The particular object of my invention to eliminate the" wet presses, hydrauhc. presses, carts, etc., as well as the enormous manual work involved with the present system forobtainiiig a pulp of consistent form such as would be suitable for storage or for producing bales from the liquid stock. a
With the old system of using the said wet machines so called laps are produced containing about -75% of water. These laps the water pressed out fromthe laps in the hydraulic presses, have then be removed from the laps whereupon thejlatter,after,lf having been reassembled, are sent to the storage or are packed into bales for shipment,
on the baling press which generally is of the same type as the hydraulic dewatering ress,on1y of somewhat lighterconstru'ction.
e wet presses used in that old pulp treat-- ing system, requires new wires and felts rather frequently, which means high maintenance and upkeeping costs; Further the frequent insertion of fresh felt or other of which this app 'cation' forms a Whereasinthe parent application referred? to I have claimed-the apparatus for carry-'2 Serial No. 408,188,
mous floor space.
Accordingto the method of my invention I avoid all these disadvantages by predewaterly into baling presses of the hay press type,
which inturnsurrender the finished bale on a bale conveyor leading to the store house or to the railway car or other shipping contrivance.
' Where-the pulp storage or baling department is at a location distant from the other parts of thepulp manufacturing plant, then the pneumatic handling of the pulp leaving the screw press is of considerable advantage. Therefore'it is further an essential part of my invention, to have the pulp manufacturing plants adapted to such new and improved working conditions. When using my new method of pulp handling, I may connect a special feeding device between the screw press and the air pressure pipe line through whichthe pulp is blown to the storage or baling department. The compressed air is delivered to this piping from a compressor, and 'only a relatively low air pressure of 30 to. 40 'lbs. is required for blowing the pulp over a distance of half a mile and more.
carrying-out my method steps in my new manufacturing plant the feeding equipment may comprise a trough, a hopper, a screw feeder in the cylinder part of the noun) runs runr a coxsrsrnm" mm sorranna' together require much manual work and an expensive installation, occupying an enorof the trou h.
trough, and a pressure chamber into which the screw feeds the moist pulp. The end of the cylindrical part of the trough. into which the feeding screw does not pass, is of conical shape, having its larger end towards the pressure chamber and its smaller end towards the screw. The stock forced through this conical art into the pressure room is sub-- 'ect on e screw side to the pressure produced the action of the screw, on the pressure 0 amber side it is under the pressure prevailing in the air pipe connected to the pressure chamber. The stock forms in the conical art a kind of plug which prevents the stock rom being blown back into the screw room Suitable equipment may also consist in t e arrangement, at the one end of the shaft of the screw towards the pressure chamber of a knife-like tool which scrapes small articles in even quantities from the pulp fe into the pressure chamber. These loosened particles are carried away by the compressed air passing through the pressure chamber and are transported through the adjoining piping to the distribution storage bin, baling press, hopper etc. Thereby the pressure chamber is referably arranged in sucha manner that t e knife itself is almost fully out of the path of the compressed air current and only the pulp to be transported is in this path of the stream of air.
It is further a. part of my invention to counteract a variation in moisture of the pulp to be blown to which purpose the distance between the end of the feeding screw and the knife may be varied; for pulp containing less moisture, the distance is shorter, whereas pulp with a higher moisture content requires a larger distance between the end of screw and the knife, in order to prevent the pressure in the ressure chamber from blowin the stock in t e wron way through the fee g screw instead of bIowing it through the piping.
A mode of carrying out the present invention is shown by way-of example in the accompanying drawings, in whic Figure 1 is a diagrammatic cross section of a pulp treating plant suitable for carryin out my new method; and
iig. 2 shows a lon 'tudinal section of the special pulp feeding evice 6 in larger scale.
In the apparatus illustrated by -way of example in Figure 1, 1 is the screen in which the pulp to be dewatered is freed from coarse particles, etc. The fgood pulp leaves the screen in a dilution 0 1 part 0 solid matter to about 300 parts of water, which latter is partly removed in the decker 2 to a consistency of from 2 to 8% of the pulp. The pulp thus redewatered is collected in a chest 3 and ows from there to the screw press 4, where the final dewatering is taking place. The pulp leaves the screw press 4 with a consistency of 30 to containing to u 45% water, and falls into the special feeding device 6 which leads it into its ressure chamber 7 into which com'presse air is blown through a piping 8, which is connected to the air tank 9. If more than one screw press is bein used then the pulp leaving the presses is co lected in a conveyor 5 and carried by it to the feedinegi air is produc the com resso'r 10, which 18' connected to t e air ta 9 by means of piping 11. To the pressure chamber 7 is connected the ressure piping 12,'through which the pul ed into t e pressure chamber is blown by t e compressed air to either the storage 13, or to the cyclone 14 on the roof of the bahng department. From the cyclone in which the air is se arated fromthe ulp the latter drops into t e bin 15 and is fed om there into the hopper 16 of the baling ress 17. The baling press delivers the pul in bales 18-to aconveyor or the like 19, on w ch the bales are gevices 6. The compressed acked for shi mentif necessary and whic carries them 'rectly into the I frei or e warehouse for storage in case no direct shi ment is intended.
Fi 2 which shows the. feedin device 6 with t e pressure chamber 7 of i 1 in larger scale, 21 desi ates the troug with hopper 22 into whic the ulp is delivered from the screw press 4 of ig. 1.
23 is the feedm screw in the cylindrical part of the trou 24 is the shaft of the screw carried on t e hopper side in a bearing 25 and driven on its free-end through a pulley 26. 27 is the conical part of the trough in which the ulp forms the sealing plug, 28 is the knife astened to the shaft on the ressure chamber side. 29 is the ressure c amber with openings 30 and 31 in it, to which the pi e 8 from the air tank 9 and the pipe 12 ltea1 ing to the storage or cyclone are connec e ht car 20 or, other shipping contrivance Instead of a feeder of the screw type, any
other typeof feeding device such as a piston feeder, etc., and instead of air handling any other system for conveying the pulp can be used without departing from the spirit of my invention.
It is to be understood that I do not limit myself to the precise method steps employed except as indicated in my claims, and it will be obvious to those skilled in the art to which my invention appertains that many forms of apparatus and kinds of equipment may be used to carry out the manufacturing method hereinbefore explained.
I claim:
1. In a method of treating paper pulp stock, first denuding loose paper stock of the greater part of its moisture content, then disintegrating the denuded pulp stock and finally subjecting particles of the pulp. stock at the point of disintegration to the action-of compressed air and conveying the same while in air suspension to a remote point for further treatment.
2. In a method of treating paper pulp hereto.
RICHARD T. LANG.
that I claim the foregoing
US406786A 1927-02-04 1929-11-13 Method for converting liquid paper pulp into a consistent mass suitable for storage, etc., or into bales for shipment Expired - Lifetime US1861184A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US406786A US1861184A (en) 1927-02-04 1929-11-13 Method for converting liquid paper pulp into a consistent mass suitable for storage, etc., or into bales for shipment

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US165774A US1829563A (en) 1927-02-04 1927-02-04 Conveying device for paper pulp
US406786A US1861184A (en) 1927-02-04 1929-11-13 Method for converting liquid paper pulp into a consistent mass suitable for storage, etc., or into bales for shipment

Publications (1)

Publication Number Publication Date
US1861184A true US1861184A (en) 1932-05-31

Family

ID=26861694

Family Applications (1)

Application Number Title Priority Date Filing Date
US406786A Expired - Lifetime US1861184A (en) 1927-02-04 1929-11-13 Method for converting liquid paper pulp into a consistent mass suitable for storage, etc., or into bales for shipment

Country Status (1)

Country Link
US (1) US1861184A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2532660A (en) * 1944-05-11 1950-12-05 Arthur J P Care Apparatus for producing fiber staples
US3055795A (en) * 1957-09-09 1962-09-25 Bauer Bros Co Handling of paper pulp
US3316141A (en) * 1963-10-05 1967-04-25 Svenska Cellulosa Ab Process of dewatering sulphate pulp to contain less shives therein

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2532660A (en) * 1944-05-11 1950-12-05 Arthur J P Care Apparatus for producing fiber staples
US3055795A (en) * 1957-09-09 1962-09-25 Bauer Bros Co Handling of paper pulp
US3316141A (en) * 1963-10-05 1967-04-25 Svenska Cellulosa Ab Process of dewatering sulphate pulp to contain less shives therein

Similar Documents

Publication Publication Date Title
US2323194A (en) Apparatus for the production of pulp from cellulosic material
US2675304A (en) Briquetting
US1861184A (en) Method for converting liquid paper pulp into a consistent mass suitable for storage, etc., or into bales for shipment
FI62366C (en) REFERENCE TO A VIDEO FILLING MATERIAL AV FIBERMASSA LINOCELLULOSAHALTIGT MATERIAL
JPS5829896A (en) Method of preparing combustible classified matter to briquette home garbage and apparatus for carrying out method
US3680796A (en) Defiberation apparatus for separating cellulosic fibrous material from refuse
US3047453A (en) Pulp handling system, method and apparatus
US5471921A (en) Apparatus for dewatering and lossening raw biopulp
US3907630A (en) Method of fiber board article production employing predrying of the ligno-cellulosic material prior to liquid suspension and article formation, and employing water recirculation
US3670968A (en) System and process for recovery of cellulosic fibrous material from refuse
US3316141A (en) Process of dewatering sulphate pulp to contain less shives therein
US3697324A (en) Apparatus for removing liquid from fibrous materials
US3055795A (en) Handling of paper pulp
SU1752451A1 (en) Technological complex for dry air concentration of loose materials
FI62235B (en) INMATNINGSANORDNING FOER STRAOLKVARN
US3694308A (en) Bagasse fiber product and process
CA1136912A (en) Method and apparatus for efficiently producing cellulosic pulp by the thermo mechanical pulping method
US2884147A (en) Method of shipping celulose pulp in bulk
GB486738A (en) Process and apparatus for the extraction and treatment of medulla from plants
GB1367508A (en) Process and apparatus for extracting soluble substances from fibrous materials
CN207203579U (en) A kind of high pressure belt starches air cushioning case
US1542559A (en) Composition board and method for making the same
RU2771393C1 (en) Installation for the production of briquetted oil sorbent
FI58171C (en) FOERFARANDE FOER AVSKILJNING AV AONGA UR MASSA SOM KOMMER UT FRAON EN UNDER TRYCK VARANDE SKIVRAFFINOERS UTLOPPSSIDA SAMT ANORDNING FOER GENOMFOERANDE AV FOERFARANDET
US2907685A (en) Compressed starch grits