PH27030A - A method of de-inkins waste paper material - Google Patents
A method of de-inkins waste paper material Download PDFInfo
- 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
Links
Classifications
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21C—PRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
- D21C5/00—Other processes for obtaining cellulose, e.g. cooking cotton linters ; Processes characterised by the choice of cellulose-containing starting materials
- D21C5/02—Working-up waste paper
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21C—PRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
- D21C5/00—Other processes for obtaining cellulose, e.g. cooking cotton linters ; Processes characterised by the choice of cellulose-containing starting materials
- D21C5/02—Working-up waste paper
- D21C5/025—De-inking
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/64—Paper recycling
Landscapes
- 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
PRR i. A . oo
El oo — Lv 0 oo a Lo : ov, : A . £ oh on La eAD oRiGiN bf Ch ag——
Jetta | wh :
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SESE BE
Cash Ci .
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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
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HE Li ORGINA- Re bo uo FI BAv TE
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ER ee CT Gi) oo Pe LT pA as i a
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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
Pili. 2 LE LE
CO i an Ce
Poh “
Pam, ce To iz mm— tern — i BRE =~ EE TT
RL is iff ot ST TC ag TE .
REE BS ALE i ode ) > :
EER RI do 1 er AO 630 To. hu
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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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Boer eet ROE .
Claims (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 ERVEL. (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 }
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 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| PH27030A true PH27030A (en) | 1993-02-01 |
Family
ID=10653370
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PH40180A PH27030A (en) | 1989-03-15 | 1990-03-13 | A method of de-inkins waste paper material |
Country Status (16)
| Country | Link |
|---|---|
| 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) |
-
1989
- 1989-03-15 GB GB8905942A patent/GB8905942D0/en active Pending
-
1990
- 1990-03-06 ZA ZA901713A patent/ZA901713B/en unknown
- 1990-03-09 MY MYPI90000373A patent/MY107139A/en unknown
- 1990-03-12 IN IN205CA1990 patent/IN174412B/en unknown
- 1990-03-13 NZ NZ23289290A patent/NZ232892A/en unknown
- 1990-03-13 PH PH40180A patent/PH27030A/en unknown
- 1990-03-14 CA CA 2048618 patent/CA2048618C/en not_active Expired - Fee Related
- 1990-03-14 PT PT93425A patent/PT93425B/en not_active IP Right Cessation
- 1990-03-14 BR BR9007224A patent/BR9007224A/en not_active IP Right Cessation
- 1990-03-14 KR KR1019910701116A patent/KR0151110B1/en not_active Expired - Fee Related
- 1990-03-14 MC MC90@@D patent/MC2179A1/en unknown
- 1990-03-14 DE DE69017205T patent/DE69017205T2/en not_active Expired - Fee Related
- 1990-03-14 FI FI914276A patent/FI914276A0/en not_active Application Discontinuation
-
1991
- 1991-09-13 MW MW5091A patent/MW5091A1/en unknown
- 1991-10-10 BG BG095308A patent/BG95308A/en unknown
-
1994
- 1994-01-31 LT LTIP1852A patent/LTIP1852A/en not_active Application Discontinuation
Also Published As
| Publication number | Publication date |
|---|---|
| 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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