PH27030A - A method of de-inkins waste paper material - Google Patents

A method of de-inkins waste paper material Download PDF

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Publication number
PH27030A
PH27030A PH40180A PH40180A PH27030A PH 27030 A PH27030 A PH 27030A PH 40180 A PH40180 A PH 40180A PH 40180 A PH40180 A PH 40180A PH 27030 A PH27030 A PH 27030A
Authority
PH
Philippines
Prior art keywords
weight
substance
fibrous
inking
substance includes
Prior art date
Application number
PH40180A
Inventor
Stanley Blum
Original Assignee
Blumco Detergents Ltd
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 Blumco Detergents Ltd filed Critical Blumco Detergents Ltd
Publication of PH27030A publication Critical patent/PH27030A/en

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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
    • D21C5/00Other processes for obtaining cellulose, e.g. cooking cotton linters ; Processes characterised by the choice of cellulose-containing starting materials
    • D21C5/02Working-up waste paper
    • 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
    • D21C5/00Other processes for obtaining cellulose, e.g. cooking cotton linters ; Processes characterised by the choice of cellulose-containing starting materials
    • D21C5/02Working-up waste paper
    • D21C5/025De-inking
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/64Paper recycling

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  • Paper (AREA)
  • Treatment Of Sludge (AREA)

Description

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RB. . i R . :
Nv Py ro LI Fe ve i Sa ER Cae Coe fie SA
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A ww This invention relates to a method of Lo
Sh de—inking waste paper materials. - on In the paper and board industry, the use of secondary fibres derived from recycling waste 3
Tra a paper materials is well-known, and the dispersal an and separation of ink particles from waste paper
Ln materials and its secondary fibres is a necessary agli) step in the recycling of the ma terial, :
Hn : ‘particul arly in the production of paper for
Bee oq BS
Ey an? 10 newsprint, tissues, and fine paper. a “e.. In known re-cycling processes, the waste ‘ dass Lf - ' my : nA paper or "furnish" is usua lly placed in a o
BET “Lk i
SAREE : : pa - hydrapulper where it is mixed with water and the
EEL eb hls :
Tel Ee et ~ following chemicals: 3
Son He . CONE Co : at N | 19 ns (1) caustic soda or other de—inking Lo rash. | CU ait \ #2 -
AEE \ Ei chemical, :
Thad SRT (2) sodium metasilicate as a buffering
FEE i i.
FEET { / 8 Roa agent, and :
Bh i ~ \ SEE
Fe : 4 a tt
REGE aman (3) hydrogen peroxide or other bleaching ee LER : : so
EE : 20 opin, agent. os :
Ak : RN “ -
As Sh Cent In the hydrapulper, the ' furnish” is : ~ SH pe ' LL he N : aR ar : : “
Bey disintegrated into a fibrous pulp, which ia then etl) ate . :
HIE dE ! i
Jest de~inked and bleached by the added chemicals. rh 9 From the hydrapulper the fibrous pulp or. lushed 2 Ei 28 tibres, with a consistency of 18% (as in high
Leake Ce .
SE Li Longa [an ; piacedied SAN BERETA i
TERE ' Je = 2 = Co ceil TRE r to,
Yad Br bo oo . i
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—————————————— ee fg ST Ee Rr
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RRR 0 sc re DETR a= F030. aE h BARNEY £0: hi bg A COLAND . . ET
AE PR re iL TY 3 Fil ENA . ie : LT 3 L Ek )
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LG LT ee th
Theale SE : Te BONER wR ca Git
Pet SR For
We ie bn : . Coen hes Le . Coe rt : a - pa aL LY Be L - congistency pulping) or 85-47% (as in Mills not i :
Lo using high consistency pulping), is dumped into a
SL series of "dump" or storage chests where the oo
Arp :
AA - . whee “
En slushed fibres are diluted down to a consistency oo ww es an a of ‘around 1.9%. ar CE an SL The "stock" or diluted slushed fibres then / TE : pass to the de-inking mguipment, which either
Lo consists of flotation cells or washing screens or oT Pl :
Sora .. NEN . . :
Wo a combination of these, where the dispersed ink
A Sp - . aL 10 particles are removed from the sluehed fibres. ve Si In the method of utilising flotation cells, a 1. - le
Sh reoilector” soap is added to the “stock” prior to
Jape o RA i
A REFS Sh 1 entering the de-inking cell to agglomerate the
I un
He } dispersed ink particles which then float to the
Ee 18 surface of the cell ob air-bubbles which are
Bel i de soured at the base of the flotation cell and
IVE CE UR ) wh ARs B
Fan a
Sha whigh are then skimmed off.
MYL Sige :
Ee a -
Es) “In the washing method of de—inking the Lo
Ho LEE Cn
FR dimparsed ink particles are washed out of. the ig
Cel ny :
SEE SERIE =
EN 20 system by passing the stock onto a rotary decker, _ aft dp Te =
Lo Ly ; See . Rk '
Al a sidemill screen, a screw press, or similar’ re he TH | -
BL equipment, using large volumes of water. RE
Ekg .. Lie - weld oo he Sh Lo
Lo 3 Sd, Sex Lo
TRE fyiThese known methods of de-inking thus require
AEN SHE LL ay o = . . ” der | - Laie .
PERE a 5 ab the addition of a number of different de—inking : [AF ei i SR
Fas 25 chemicals. Some chemicals are also only effective i wf. Cl Ee rs I 7
BER cL SU
SER el int tu vo . CE 2 Et Sheat = 3 = Te = ~ . ek : : 01 Lo 0 ie -
PRLROgL Lo. RO LT eke oR r GIN AL dD 0 af “1: BAD OR dD. ed # : te! wo
Ie Eo . Ce Nae a
ANE BARA FA
FEA SE Co Ln pe » sy Cn Vil vo ee :
FripL SA HT
———— ET ——————————————er eS EE —
L
Whee en 5 has ; rd [50 Tver or THR Se dey a: ET re SU eae “ : {nai
We. SE : 43080 TR
Bent if =n Fh ede Tat Ce LE orn Ta oo ! Co Ei
EA i She oh i : . : i he wh : { - - s Jw : tl Pe
ST for one of the two different methods, i.e.
J } i Cu flotation and washing methods, and cannot be used hy
Te
So in the other method. Furthermore, caustic soda, YN . which is most commonly used in relatively large ‘ a amounts as a de-inking chemical, can attack the gE fibres and may not be regarded as being Co 2X b Lv an . i
EEE environmentally safe when emptied from the mill -
Co vo into external water sources. it is therefore an object of the present
Co 10 invention to provide Aa method of de-inking waste : paper materials which substantially removes the es above-mentioned problems asaspciated with known Sl
AE methods, : ie
SEE Coy Te
CEST Accordingly, the present invention consists Ch
Lh v nT ol - ia in a method of de—inking waste paper materials ST
Hae Vi rg. comprising the steps afs-- ER
Fir J diol plilping the paper material to form a fibrous sda Ca . $a ae ee mL stock of a slush-like consistency) :
Tali a Sha . ' :
SR adding a substance to the fibrous stock to } o
SE 20 disperse ink particles from the stocky . "a 8 Ll Ea ; 0
FOE Cg oo
Tak : and removing the dispersed ink particles from : pL . Cle : .
Be Sy co pn ] the fibrous stock} - gas . characterised in that the substance used to
Cashel en disperse ink particles consists of a mixture of DEE ee 25 phosphated and carbonated sodium salts. wn, aE. = =
HE ev SL nt oo Ca Le aay | So - 4 =
Cede fg
CET a
LEE ! I :
SNE ; No
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HE Li ORGINA- Re bo uo FI BAv TE
PE A Nan” - bh Le Sy i Sl
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L
. Ro STC | vs le : Lo men
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ER ee CT Gi) oo Pe LT pA as i a
SyHbg Co
FL } i : : iY . ; :
Preferably, the substance consists of 1 to oC
Co . 75% weight in weight of sodium carbonate and 23 to . \ Ce * * 99% weight in weight of sodium phosphate. ) eS \ } i \ The substance may also include 1 to 2% weight 8 in weight of metasilicates and/or 0.3 to 2% weight oo
Es oo in weight of caustic soda. dey The substance may also include hygroscopic pe se ' SE : oo salts, together with a non-caustic booster, and ara may include a sanitiser.
NE) 10 if desire, a bleaching chemical may be added,
Cit Loy ' . hE for example 0.25 to &% weight in weight of
Ln hydrogen. peroxide or any other suitable hleaching
SER Ln
MOREL alee ng agent. }
Wp CL che .
Ln The invention will now be further described
Ceo ia by way:of example with reference to the } an accompanying drawing, which illustrates : Ce
Hh schematically one embodiment of the present
EAT : rel SI
Tw Pe invention. Re Co
A A Co ‘Referring now to the drawing, there is shown
A Tari “ . A )
EAE ON A Hv
EE Age :
Ee 20 a flow diagram of a washing method of de—inking,
ABR : AEE Lo on
LR © rom——r Op ——n ’ :
EEE the steps of which are well-known to those skilled
Sa dE ERE BS
Adit cer in tha’art, except for the replacement of known ns
Fi A : Cs oo on ve Br yk oo Le in Sa co : : wo a Ca de-inking substances by the substance as used in lL : A : TEL . : Sr
PARES LL J Co RG ; ee A accordance with the present invention. Seb tile . 2% Inthe illustrated method, waste paper is fed co
Cin hime, Cae : Lo eR : Fen fol SEE
REE as i m= 8 = ; ns
RA a Co fg 4 , dD Re
LAE we, . Coe :
Cp LE INAL a
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REE BS ALE i ode ) > :
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SER li. EMER ; nde i iw
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AER Cr i LEE
SEESRESE Ne Sat pe
LE J
Hal i -
Tein No. oo Co
Ea into a hydrapulper 1, in which it is disintegrated win - ven into a fibrous pulp or fibrous stock of a slushed
So consistency. Water is added to the stock,
Ry together with a substance to disperse ink
HA a particles from the stock. From there, the stock
HE and dispersed ink particles pass into Aa LL '
Tn + 4 Co
SEE centrifugal cleaner 2 to remove grit, pins, clips,
EEA ei hh ete; and through a screen I to remove overeslzed inl particles.
BREN \_ 10 The stock then passes to a first washing
I fir
Geil stage 4 consisting of a thickener 3 and a fine
ME ER :
Ce hy Co .
SRE deflaker or disperser &, which produces a well >
SCEYIYAL ST : Lo wl Co ro
Eke LT defibered stock, which is reasonably «clean and wh AT Toon =
TE he :
HRY free from ink specks but still contains very small
Tore ae .
AT 1a ink. particles. From there, the stock passes to Lo iin FAL CORN ST fades . Lanse Sa .
Ey } secdnd and third washing stages 7 and 8 GL on
EX RE respectively, pach including a vertical screen 9 5
AANA Ph Sp : Cae sl OL
SREhaaEA Ae no RE tig ei SU and:in which dilution water is added to the ‘stock. go
Edd Nr LL EEE So a pa 7 :
We A:fourth washing stage 10 consists of. wanother
Sreiely OA Lo : : Sree gl 2 dl 20 thickener 11, and the clean stock iz then ‘passed we
ATA Rl ! - fas. ra
SFT SO SAE EARS .
Pres Ny wr ’ EN VL a Co from the thickener 11 to refiners and paper—-making E ; 24% AK yr ) 0 we . ik 3 : ie Po ne om. maSninery. i ps bok: efit Yo th SE yo - - } ara, fae Helo In accordance with an embodiment of the . . pc ect ROE FR : RE ’ Ra i
COREL Lo : : La AN | po co
KARR IL? FEAT - ; ne , - Le
CORRE ae prasant invention, the substance added to dimparse wo
SR Ca ro
PEGA Se 23 tHe ink particles consiets of a mixture of 1 to
PERCH : Trophies . ol pesado Ed tr hl RE eT EN
PLE Coe oo
FREE. CA Caglh fe Cider v (HEE Ae i" — le Te [le Lk Lt : wo =z &b = to +
ED EH SN . on ~ A i . ' " :
YA TB Y . Se . -
Tn gh . rh a 5 BAD ORIGINAL OF ey 3 Co : 7 AT 3, me TI . : . ay Ee - Lo
Pan Ye on
Ld gL . ad ch i: “
EEE : EELS Ma “a
ET fe ‘ RRA a o
Sat ee et mmm mmr r= ——— = £
RR pe mde a
BREN: oe . ae oo LY nl h 2 I OT A A Auden © i ’ . PLE Ta flan Sie aR
BRE 0 By tC Tn fi Oe : 29030 pi IRENE
BL FEEL Gl a aT CR : Lo Cn . CE NE
A EE Cl . VLE ATR gl ot Bo EE AE EE CRE TR
RRA RT - CATE ve CT LRT
MELROTP ELIE. Lo 0 os Ap CE lay aE hi Qui Al THE od : yd £23 URS Lh
BRE Bol rat RE a ER a Ne ipa, we : CI
FR cL Se Ce
SRE vo he ELE L ER:
EE pe v Grade 7 Fo TET
EN , nn Sh Cn ; Preah S Sn ! : py yo
FL pts VL J Le L
Dlr wet : . i -
Eh ’ 75% weight in weight of sodium carbonate and 25 to CL + i EN cl - ] : 99% weight in weight of sodium phosphate, with a
Jie "- . ’ : typical composition being 8% weight in weight of
A sodium carbonate and 92% weight in weight of ’
LL a sodium phosphate. eH The substance may also include small .
Le quantities of metasilicates (for example 1 to 2% ' hs Si ie weight in weight) and/or caustic soda (for example }
AE oH . . ,
Foo . 0.% to 2% weight in weight). The compasition may gy oo
Sa iC be further enhanced by using hygroscopic salts, .
ST N together with a non-caustic booster, and may on
El IE . include a sanitiser. A bleaching agent, for . Tea get . } example. ¢.2% to 8% hydrogen peroxide, may also be -
Ey added. "Tk = + al ie : : = Sed UE J
Se 1a Asan alternative to the above-described ol
Rs Sa - dn “ne i -
Sa washing method of de-inking, the substance may be
Se Ro co
CET I utilised to disperse ink particles in known REY Cl lL " Co Cn IE
LET - sg Ca ca) an flotation: methods. we i. .
AER Vike Da : ti EL . Lo CATE yy oh
Ra Lo Theiiuse of this substance in de—inking; My
A EE CA
Ade } . ? Ar on } wT ey 20 methods has advantages over the use of the So © Co fob Brig CR Se oe
ABER - Lh i. Sr
Belie Ca chemicals generally used as follows:-— co Co po are By a Son sn EE (1)F It is an effective ink dispersant in CL ae Lc Ca ans ant Lea fa nh sy both traditional methods of de—inking (i.e. Na {
Faia CIs ; [ERT CPR | Lies , ‘ raagthin & Geo LE ’ PE oo
ERS Fiotation and Washing) unlike other de-inking . Lo
POE fo da! ’ -r ae | CL Le
HORE: 0 a 23 products: which are only effective in one or other i
Broo Pua oo
Daas RAL J CL
SE INE :
RAS yl - or I
RARE LE . . i fe oa "oo orGNAL 0) pr . BAD ORI pe [7 Si ‘ J. 3 fhe) - - batho ard ST , Tot ! on oo peg kako A 3 iD .
SY He :
Re <7 ap
FR 4 Co. Re A Co a
J RE
5 . ee ase Yo ! Oo : pk eb: } Co, oO . - 3 gibi IN Lox ¢ hy Lo Ri 3 : 3
SEE, Lt dari -nk oe eT J :£
TRE Ar; a. L {- 8 , pletely vo. . . "%
Se ET Tp td
SRE: Th EE . CTE :
RG IGESL A, war Ce
SRC ‘ CU
ABER A Eo: LER : rsa . A SE :
FREE Due Cee 3 ey . “Te . hs SORARTE he :
Bs gh Lo ond co
AE ail - - Le
TERRY HE
SEAR A
LIRR Sa
Sromiay Si of the traditional methods but not both.
GRE al (2) By virtue of its formulation, it can be wR Jv umsed as a "one-shot" ink dispersant in the
EL hydrapulper, without the need for the addition of lg AREA Y ¢
Eh i
EEA a .
Cte § - buffering agent or any other chemical in the
Leni "
SEE hydrapulper.
PTET Col (3) It is effective as an ink dispersant at
Oa low temperatures (eg. 7 0), ant therefore saves 1, ash ie
RAE
» RL a Lad 4 a © the power requ ired to heat thn hydrapulper
NA oo 0 Oo.
FUNERAL oe 10 © contents to 50 60 C, as is necessary in hnown oe AT y Le
Segre 4d or
Slheiar Ce Sh } . } sey : methods using other de—inking chemica 1s.
Bed said Ea ,
Freer] - A (4) Unlike caustic soda, it does not attack
Galea Tyla? Los
FER da , .
Et WE ,
ERS i J . the fibres, and therefore gives a stronger paper
Bagi) . A
Fa . Lange
Sali iy “Siand product, and may be used as a caustic soda
SERS] : BERET 2 !
Ta : 15% EE replacement in the hydrapulper.
SYA se
Seedy Ro pl | SOR (5) As an ink dispersant, it does not
Fatt) Ae .
ERI REAR RE
Sgn Liilthecessarily require a collec tor soap in Flotation
SA Lowel We i, cide to ype so wa CANE “a.
CARS eT ales Rs & | dide—ink ing, nor the high tempera ture (60°C)
PEER) Lo SNE oe
FREER SI) SRR SL
Aga nr LATA :
SgiEdy a Co : JEonecessary when a collector scap is used, this
NER Coa Lo
Su . LER Is
FESR ! We Lo
Sal Co 20 2¥giving further ec onomies in use. . sail a: ie amd . LEE (6) It is safer to the envi renment, i.e. it
Steg . Sri .
Zags Cra rl 4 a - wit is much less toxic to aquatic wildlife, and has g Si So LE oe Be] : , Sia = it Co wit\lower and more acceptable Riolegical Oxygen Demand pg Sti
BAT a
Br . ai R.0.D.) and Chepical Oxygen Demand {(C.0.D.) when
RE ria EE
EE EE t
SE - 29 emptied from the mill into external water sources
SE aE
Chadd RL XG a | So le wy
Hashmi on be iad L
EEE ] kn = 3 = - spy ered CAFE
Sent HE .
CREEL Sate TE .
Ea lee, rr
Tag ‘ ER eal fi ant 9) re phos BAD ORI Z
Hadas Co nL
Epi i - SL baa
Fe Gag : ak BEd : . MOG
Na ed oe
Ean yh )
BARTLET vy
LllppPar st fa .
J TERE Ce
————————— EE ——————— —- mm
WERE a ry ’ TA
EE CR 27° 2 En
SEN PM - aa o Ce Bi a Ji FAR wa . te W ! mL a Co a
J Cu ‘.
CR J gem co Ce pod po
RE - . aga ~ :
SE | "
HE A, sc a be than other de—inking products at the present time
Cond e.g. caustic sada or bleach.
CA | (7) In mill trials, it has been found to or i. have excellent "former" properties in that it
Tg 5 ives a uniform distribution of fibres in the
Bo 9 we i finished paper which resuilts in a better quality aa end product.
Ee | Furthermore, mill machine runs and further ne aR experimental procedures utilising this substance
FL . Co. ,
GEES \ J 10 in de—inking methods have revealed the following :
SEES : eas vr )
Irae ‘© .
Ho additional advantagresi— no = ot ‘ a (a) striking increases in the strength of fled viet IS “ Lei = BA SM aE Lo Y the recycled products of between a8 to 30%,
LF Sr rar a Nuk,
SEERA - SAA brated " ‘depending on the waste mix in the furnish used}
TEL :
Fir Aa a
EE . 13 i (b) production of a better, less speckled
EE Co fa “product when used to de—-ink better arade, hind ad
EEE office-type waste paper, hitherto known as aie i” tL abd eo » y
HEE Cy shdifficult to de-ink rade (i.e. wood-free
HEN . 0h 9
Sale Ne wl ok waste); i]
BESS . Tul So
LEY Sd . . SE ln . 20 ry (c) successful attacks on laser print,
ATED = Py ky wh i qi
Ra : Lxerographic print, hitherto known as difficult to 3 = el oo a Lo remove" inks, and on the new FLOXO inks, as well
SEEN oo ck : wa am’ producing a higher brightness than standard ropa : TE : pEaEAl. Sa gary i Srde—-inking products and et 23 val i A ; Pa . £ na - . CNEL -
ETL . a . . ped Co 20 in (d) enabling up to 85% of "grtickies" or gums
Egan) : Ci : [rae Coe ny oo
El 7 - ORIGINAL © page 3 = BAD
Fp ot Le )
EEE . [i . '
Saad
Lisle Co iat
REA ;
FER Ce
FEY on
Pra CL anh) .
SNEED -
ene a Sm
EEA Ca , nl ha gall 4S a a hg . i - 4 ] 4, bo rh 2 i pil Dl Vit x er N i cal HF03 La pe i
ICRA] MEIRAER 7 af IY Tes a. - cat oo or Dae HLS ba 2 we I ptt ree Sha . : Cy CT El
LIE EEA al QO aE SERA SEs : PPR
RADNER AN tT sled : A Aaa " : Bry
HR oF rT ail Co GLE : 2
MEE SR : a TE
TAR Rk Ve BE iS oe ore Fa ov Ch Jan . a
Ee] AC Soa { -
TEE VT
CLIT . wh
Eas CA
HARES : ig }
TEE i g
SEE j SL Ce
NCR TEY co
FA : . " ge
PT to be passed out, thus removing the bulk of a : Lo major problem of the paper recycling industry,
Shan which can account for expensive "dowsn-time" of the
BCE i machines. £0 : iE fA . Whilst particular embodiments of the present
Ca Sinwvention have been described, various
Ca ‘ a A modifications will be envisaged wit hout departure
SAA
1 Fn [EN © nin from the scope of the Invention, as defined in the
Se . appended claims.
CHE -
Semel Co aaeiabs . Je se i
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EXCRETE Sh
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Boer eet ROE .

Claims (1)

  1. CMR A ut «Hah ME cg > 's RRR ROT 3, hi Gr Fe 2 EN Cad ' Soe At Cg CL BEERS : AN WE.
    Ci Fey : Lo BRR 320 LF 2703 + PIER RRC Sr: oy Als . Sd SER ER PTE BEI NL bo wl : pei lt CE Sa i BG RY ETN at Co te, ! Frid (Sr AE oo “ ; A | ‘ . IEC Veet JAE . x Stay co SRE i ET ESE RE i. in a method of de-inking waste paper } sme ARLE ih y “material comprising the steps of:- fe ce pulping the paper material to form a Salt ol : fibrous stock of a slush-like consistencyy a wh 0 - adding a substance to the fibrous stock = So thus formed to disperse ink particles from IS the fibrous stocks CA : and removing the ink particles thus al dispersed from the fibrous stocks SOEREITS 10 the improvement, which enables the method to . Li F r we Co Lo IN See be carvied out at ambien t temperatures, consists CR cl A nL “iat using a mixture of phospbated and carbonated Via . Cie EARLE RE Bhi : igodium salts as the substance for d isperasing the EEX RTE EE SEY] (apink particles from the fibrous stool.
    Feld Cole Saat LE HEE 195000 2. A method as claimed in claim 1, wherein rte Re Uh el Rr — pw CREST ¥the substance consists of 1 to 75% weight in SE Cweight of sodium carbona te and 25 to 99% weight in CSEEATA Cog i Za Swelght of sodium phospahte.
    So ea \ eed I.
    A method as claimed in claim 2; wherein Agr Nar i.
    CEES CSE . . . Loa CRA 20 ihe mubstance consists of 8% weight in weight of Si EL " Egan : SEU . . carat Saodium carbonate and 92% weight in weight of Ea si : pn . CRE Can RH oo Reise E BC : Lea rt nisodium phosphate. raps] | CLE i gmat Br 4. A method as claimed in claim 1, wherein Ags AT . amb TH ea be Wthe substance includes metasil icates. ft : 29 sp 5. A method as claimed in claim 4, wherein * LEE To CLA LR I : EAS wi EE or Na \ et x Fagan CE Eps | : Ge. = 11 = . a : | N Higa Hi I at a : - wil Y ’ seme Co by PRE PIDE - CAT ! 2 ERs eat, . Fale ; 5 ~~ NAL 0 aE dt) 4 : Pe § i ) I 100 Yn . Cage VE oo FALE WE Ell oo EET
    ——————— em Sree Sm r————— ae = = AR Las, YE Ge SR 2) AON PE, a ge Lon Co : ; - . Coed tml lec Ca . eld Ros age Co CU ae SNE fm pan I Lor igen : Te ER
    VEL. (Se . LL co CT aE Lo yr Sh ’ ¥ ERE : at ne Hh I Fans Saar BG | So RAE W Bm fe ir 3 Cr : oe EERIE erp bs 1 Go 5 - ro SA oy AR = . Sn heat Pt cil Bgl 55 . He : Tn iE 5 na . Le -
    Tr . the substance consists of 1 to 2% weight in weight Sie EE Co : go of metasilicates.
    1 4. A method as claimed in claim 1. wherein RN} on oe the substance includes caustic soda. ] Sh 8 7. A method as claimed in claim &, wherein : Shel . Spry - » , ‘ RH SRA the substance consists of 0.5 to 2% weight in ip SO ' fe weight of caustic soda. As : g. A method as claimed in claim 1. wherein . be the substance includes hygroscopic salts, together :
    a. J 10 with a non-caustic booster. sh 9. A method as claimed in claim 1, wherein we A | T- ELC 3 . . Shak the substance includes a sanitiser. . Sher Ih Ee - or . Sk 10. A method as claimed in claim 1, wherein : SBT the substance includes a bleaching agent. an At oS why ake — ir GEE 13 HL AN method as claimed in claim 10, wherein So HET LE co nfs Aa Lo . : Ln Way . LPH eto Sah, « : a He the “substance consists of 0.2% to 5% weight in: : wR IN , TERE EA “ fp weight of hydrogen peroxide. oo Cy age A So efron eo Tl Co abet dT To ERE When J . RE : Co ag ER Co Se Rt Da STANLEY ELUM . Co AR A ‘ Inventor Ci eg So - a SN nL i ali Ly | Co oh SR Lo Papas : SA ee Ct el . Ten . ARERR I Caer . AERA CR i LER Ee a : bho Cha h Cen A i ba ’ IE : 3 oT | - , I \ iol J Cou , . pega JC - id Ee AE = 12 = : aEm co # HG CRE ie A 7 HoT) : Le . \ 2 ne 0g En , . Cy 5 : EP 7 ee \ gr 0 aR : Hi INAL SF 45 Let : Te i \G . £8 frig Ds . . a . Bude CC & we POMEL. Tn Ar, SE ‘ iy nL : bs EA hE . ait NE Cor oe ee ameiineatyl }
PH40180A 1989-03-15 1990-03-13 A method of de-inkins waste paper material PH27030A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB8905942A GB8905942D0 (en) 1989-03-15 1989-03-15 A method of de-inking waste paper materials

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PH27030A true PH27030A (en) 1993-02-01

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KR (1) KR0151110B1 (en)
BG (1) BG95308A (en)
BR (1) BR9007224A (en)
CA (1) CA2048618C (en)
DE (1) DE69017205T2 (en)
FI (1) FI914276A0 (en)
GB (1) GB8905942D0 (en)
IN (1) IN174412B (en)
LT (1) LTIP1852A (en)
MC (1) MC2179A1 (en)
MW (1) MW5091A1 (en)
MY (1) MY107139A (en)
NZ (1) NZ232892A (en)
PH (1) PH27030A (en)
PT (1) PT93425B (en)
ZA (1) ZA901713B (en)

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BG95308A (en) 1993-12-24
FI914276A7 (en) 1991-09-11
KR0151110B1 (en) 1999-05-15
FI914276A0 (en) 1991-09-11
PT93425B (en) 1996-09-30
ZA901713B (en) 1990-12-28
DE69017205T2 (en) 1995-10-19
KR920701565A (en) 1992-08-12
IN174412B (en) 1994-12-03
MW5091A1 (en) 1993-02-10
MY107139A (en) 1995-09-30
NZ232892A (en) 1991-11-26
BR9007224A (en) 1992-02-18
CA2048618C (en) 2002-04-23
GB8905942D0 (en) 1989-04-26
MC2179A1 (en) 1992-05-22
PT93425A (en) 1990-11-07
DE69017205D1 (en) 1995-03-30
LTIP1852A (en) 1995-08-25
CA2048618A1 (en) 1990-09-16

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