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Patent 1093749 Summary

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(12) Patent: (11) CA 1093749
(21) Application Number: 295012
(54) English Title: EXPANDED STYRENE-POLYMERS AND POLYOLEFIN MICRO-BITS AND THEIR PREPARATION
(54) French Title: OBTENTION DE MICRO-ECLATS DE POLYOLEFINES DE POLYMERES DE STYRENE EXPANSE
Status: Expired
Bibliographic Data
(52) Canadian Patent Classification (CPC):
  • 241/135
  • 403/60
(51) International Patent Classification (IPC):
  • C08J 9/36 (2006.01)
  • B01D 37/02 (2006.01)
  • B01D 39/04 (2006.01)
  • B01D 39/16 (2006.01)
  • B29B 9/00 (2006.01)
  • B29B 13/10 (2006.01)
  • B29B 17/04 (2006.01)
  • B29C 44/00 (2006.01)
  • C02F 1/28 (2006.01)
  • C08J 3/12 (2006.01)
  • C08J 11/04 (2006.01)
  • C08L 23/02 (2006.01)
  • C08L 25/04 (2006.01)
  • D21H 17/57 (2006.01)
(72) Inventors :
  • KLEIN, MAX (United States of America)
(73) Owners :
  • KLEIN, MAX (Not Available)
(71) Applicants :
(74) Agent: GOWLING LAFLEUR HENDERSON LLP
(74) Associate agent:
(45) Issued: 1981-01-13
(22) Filed Date: 1978-01-16
Availability of licence: N/A
(25) Language of filing: English

Patent Cooperation Treaty (PCT): No

(30) Application Priority Data:
Application No. Country/Territory Date
833,644 United States of America 1977-09-15

Abstracts

English Abstract




ABSTRACT OF INVENTION
Involved are (I) expanded, thermoplastic, non-brittle as
expanded polymers selected from a styrene-polymer and a poly-
olefin from polyethylene to poly-methylpentene, said expanded
polymer being in form of micro-bits which (a) are from about
40 to about 325 microns long and from about 20 to about 325
microns wide, (b) are substantially completely to entirely com-
pletely free (i) of intact cells of expanded polymer bit-pieces
from which they were produced and of (ii) any uniformity in out-
line of individual micro-bit particles, and (c) in density are
from about 85 percent of, to about substantially the same as,
the specific unexpanded polymer from which there was provided
the aforesaid expanded polymer; and (II) a method of preparing
these micro-bits by impelling a mixture of them in water in a
confined comminuting zone through a circular path by repeated
impact by a plurality of impact surfaces spaced axially and
radially apart from one another and rotated about the circular
path's axis from about 4700 to about 8000 r.p.m. thereby driving
the bit-pieces against cornered edges of a plurality of from
circular to substantially rectangular orifices arranged in
screening array in an arcuate plane, thus repeatedly tearing,
ripping and shearing the desired micro-bits from bit-pieces of
the starting expanded polymer.


Claims

Note: Claims are shown in the official language in which they were submitted.



WHAT IS CLAIMED IS:
1. An expanded, thermoplastic, non brittle in its said
expanded form polymer selected from
(i) a styrene-polymer,
(ii) a polyolefin which is a polymer member of the group of
olefin homologs from ethylene to a methylpentene and having 2
to 5 carbons in its chain,
(iii) a melt alloy of polyethylene with about ten percent by
weight of polystyrene,
(iv) a compolymer of polypropylene with from about 20 to about
30 percent of polyethylene by weight, and
(v) a melt alloy of polypropylene in an amount exceeding 50
percent by weight of said alloy and a copolymer of polyethylene
and polyvinyl acetate to the extent of up to about 30 percent,
which expanded polymer is characterized by being in the form of
micro-bits (a) from about 40 to about 325 microns long and from
about 20 to about 325 microns wide, (b) from substantially
completely to entirely completely free of intact cells of the
starting expanded polymer bit-pieces from which said micro-bits
were produced, (c) substantially without any uniformity in out-
line of the individual micro-bit particles, and (d) in density
from about 85 percent of, to about substantially the same as,
the specific unexpanded polymer from which there was provided
the aforesaid starting expanded polymer.

22

2. Micro-bits as claimed in claim 1, wherein said thermo-
plastic polymer is a styrene polymer.

3. Micro-bits as claimed in claim 2, wherein said styrene
-polymer is polystyrene.

4. Micro-bits as claimed in claim 3, wherein said expanded
polystyrene is expanded prime polystyrene.

5. Micro-bits as claimed in claim 3, wherein said expanded
polystyrene is expanded scrap polystyrene.

6. Micor-bits as claimed in claim 1, wherein said thermo-
plastic polymer is a polyolefin.

7. Micro-bits as claimed in claim 6, wherein said poly
olefin is a polyethylene.

8. Micro-bits as claimed in claim 7, wherein said poly-
ethylene is low density polyethylene.


23



9. Micro-bits as claimed in claim 7, wherein said polyethylene
is a melt alloy with by weight about ten percent of polystyrene.

10. Micro bits as claimed in claim 6, wherein said polyolefin
is polypropylene.

11. Micro-bits as claimed in claim 6, wherein said polyolefin
is a copolymer of polypropylene with from about 20 to about 30 per-
cent of polyethylene by weight.

12. Micro-bits as claimed in claim 6, wherein said polyolefin
is a melt alloy of polypropylene with a copolymer of polyethylene with
up to about 30 percent of said copolymer being polyvinyl acetate, and
said polypropylene exceeding at least 50 percent of said melt alloy,
said percentages being by weight.

13. An aqueous slurry of the micro-bits as claimed in claim 1,
which slurry contains by weight from about one to about two percent
of said micro-bits.

14. An aqueous slurry as claimed in claim 13, wherein said
thermoplastic polymer is a styrene-polymer.

15. An aqueous slurry as claimed in claim 13, wherein said
thermoplastic polymer is polystyrene.

16. Micro-bits as claimed in claim 1, which are dry-to the
-touch and contain by weight from about 16 to 100 percent of solids
as micro-bits and the balance being substantially only water.

17. Micro-bits as claimed in claim 16, wherein said thermo-
plastic polymer a styrene-polymer.

18. Micro-bits as claimed in claim 17, wherein said thermo-
plastic styrene-polymer is polystyrene.

24



19. The method of preparing micro-bits as claimed in claim 1
from bit-pieces of said expanded thermoplastic polymer, which method
comprises feeding into a confined comminuting zone, having a feed
inlet thereto, expanded bit-pieces of said expanded polymer and
water, repeatedly impelling the resulting mixture of the starting
bit-pieces in the water through a circular path by repeated impact
on them in the water by a plurality of impact surfaces spaced apart
from one another and rotated around the axis of said circular path at
from about 4700 to about 8000 revolutions per minute, and at the
same time by said impact surfaces driving said expanded bit-pieces
to and against corner-shaped edges of a dispersed plurality of from
substantially circular orifices (i) having a diameter of from about
0.102 to about 3.175 millimeters to substantially rectangular ori-
fices of from about 0.254 to about 3.175 millimeters in width by
from about 3.81 to about 12.7 millimeters in length, and (ii) being
arranged in screening array in an arcuate plane spaced radially out
of range of said impact surfaces to an extent that need be only suffi-
cient to avoid collision between said orifices and said impact sur-
faces, as from about 0.508 to 1.016 millimeters, and thereby repeated-
ly tearing, ripping and ahearing micro-bits of the expanded
polymer from said bit-pieces thereof; said fed in water being so
proportioned to said fed in expanded polymer bit-pieces to prevent
the content of the comminuting one from reaching a temperature that
would adversely effect the starting properties of said starting bit
-pieces that enable providing said micro-bits.

20. The method as claimed in claim 19, wherein the surfaces of
said expanded thermoplastic polymer bit-pieces are wetted with water
prior to their being fed into said comminuting zone.





21. The method as claimed in claim 19, wherein said impact
surfaces are axially and also angularly spaced apart from one
another.

22. The method as claimed in claim 19, wherein said expanded
thermoplastic polymer bit-pieces in said comminuting zone are driven by
said impact surfaces alternately (i) to and against cornered edges of
at least one pre-breaking surface located between said feed inlet and
said plurality of orifices and spaced circumferentially away from
said orifices and radially similarly out of range of said impact sur-
faces as are said orifices, and (ii) to and against said orifices.

23. The method as claimed in claim 22, wherein there is a
plurality of said pre-breaking surfaces and they are elongated and
extend for about the width of said comminuting zone parallel to the
axis of said circular path and are circumferentially spaced apart
from one another about said axis.

24. The method as claimed in claim 19, wherein the ratio of
the water fed with said thermoplastic polymer bit-pieces into said
comminuting zone is from about 55 to about 100 times the weight of
the starting styrene-polymer bit-pieces.

25. The method as claimed in claim 19, wherein said micro-bits
leave said comminuting zone as a slurry of them in water containing
at least about one percent of said micro bits as solids, and said
slurry is subjected to vacuum filtration thereby to increase the
solids content to at least 16 percent by weight.


26


26. The method as claimed in claim 19, wherein said micro-bits
continuously leave the comminuting zone as a slurry in said water,
which slurry then is applied to a surfaces of a moving continuous
first sheet of a non-water-absorbent foraminous member continuously
to provide on said first surface a removably adhering continuous web
of partially de-watered micro-bits, applying suction to the other
surface of said first foraminous member to withdraw therethrough
part of the water from said web of micro-bits, covering the initially
uncovered surface of said web of micro-bits with one surface of a
second moving continuous sheet of a non-water absorbent foraminous
member to provide a moving sandwich of said micro-bits web between
the opposed facing surfaces of both of said foraminous members, and
the exposed surface of each of said foraminous members continually
is covered by a continuous run of a water-absorbent sheet material
having a stronger absorbent affinity for water than the surface
tension holding water to the micro-bits, and the resulting five
-layered assembly sequentially is passed through the nip between
opposed rollers of a pair of pressure rollers constituted to provide
against the five-layered assembly sufficient pressure to enhance
significantly the absorption attraction of the water by the water
-absorbent sheet material from said web of micro-bits; and as the
consecutive portions of the five-layered assembly leave said pres-
sure rollers, removing the micro-bits from said foraminous sheet
material, thereby providing a micro-bits product consisting by
weight of from about 50 to about 90 percent micro-bits solids.

27


27. The method as claimed in claim 26, wherein said slurry
of micro-bits in water continuously is fed into a liquid confining
zone wherein there is supported a rotatable vacuum drum partially
immersed in a body of said slurry maintained in said zone, and
said first non-water-absorbent foraminous member passes into that
body of slurry maintained in said confining zone and around under
and in contact with the immersed part of said rotating vacuum drum
whereby as suction is maintained in said drum as it rotates in said
body of slurry with said first foraminous member moving in contact
with the drum, a continuous layer of water-holding micro bits con-
tinuously is provided along that foraminous member and as the latter
leaves that body of slurry and approaches the second foraminous
member, the layer of water-holding micro-bits is sandwiched between
both of said firaninous members as both of them come close enough
for the second foraminous member to meet and continue in contact
with that layer of water-holding micro-bits.
28. The method as claimed in claim 26, wherein after the
micro-bits are removed from between said foraminous members, the
water-absorbent sheet material is treated to remove water from
it before returning again to contact the exposed surface of its
respective one of said foraminous members between which is sand-
wiched a further amount of micro-bits from which water is to be
absorbent.
29. The method as claimed in claim 19, wherein said ex-
panded thermoplastic polymer is selected. from the class con-
sisting of a styrene-polymer and a polyolefin of the group of
those from polyethylene to a poly-methylpentene.

28

Description

Note: Descriptions are shown in the official language in which they were submitted.


~9~

EXPAMDED STYRENE-POI.Y~ERS AND POLYOLEFIN

This invention is that of (a) micro bits of' an expanded
th~rmoplastic polymer which i~ non-brit~le in its expanded ~orm
and selected from a styrene~polymer, a polyethylene~ polypro-
pylene, a polybutene9 and a poly-methylpentene, and ~b~ a method
for preparing these micro-bi~s from bi~pieces of the respecti~e
styrene-polymer or polysle~in ~rom polyethylene to the poly
-methylpentene~
These micro-bits~ which briefly may be called expanded
styrene polymer or expanded polyolefin micro~bits, of the inven
tion Si) range in size from about 325 microna in length and also
from possibl~ about the same in width down to about ~0 microns
or less in lengt~ and to about 20 microns or less in widthp (ii)
have a speci~ic gravity of ~rom about 85 percent, to about the
same as that, of the s~arting polymer which was expanded and then
i .
15~ disintegrated:]nto the micro~bits; (iii) are substantially com~ i
pletely to entirely~compl~tely ~ree o~ intact cells of the expanded
polymer ~rom which ~hey were produced and (iv) their particles lack
uni~ormi-~y in outli~e.
Viewed ~a) a~ a magni~ioation of, for example, 161 times (by
; 20 transmitted light, ~in FXGo 1 below) they appear as clusters o~
randomly arrayed ~ibers,:and (b) under a sca~ning electron micro-
scope (abbreviated SEM) at magnifications o~ 360 and 380 times (in
FIGS. 4 and 13) th~y appear much like irregular separate pieGe
writing paper that were indi~idually compress~d coarsely in the
hand and then àllowed to rebo~nd to the exten~ pos~ible ~rom the
resilience a~ter releasing:-the pressure by opening the hand.
Further SEM examination at other:magni~ications as at (i) 1800
times Sin FIG. ~ below) of part o~ the same looation as in FIG. ~
s~ows~ormations of~what~appear to be extended apart and distorted
outlines o~ ruptured boundaries of what be~ore being ruptured was an
expanded honeycQmb array o~ h~xagonal;~d pentago~al cross ~ection~ o~

~2



cells, (ii) 4000 times (in FIG. 2) shows them to appear much like that
of ran~omly spread apart and partially overlapping not quite fully
open rose petals. Other SEM magni~ications ranging from 500 to 5~00
times show the micro-bits to resemble minute coral formations (as in
at least FIGSo 7 to 9), in wave-like appearanc2 (magnif.ied 1000 times
as in FIG~ 10~, and in somewhat ruffled ~luted formation (magni~ied
10~000 times, FIGS 11 and 14, and 20,000 times~ FIGS. 12 and 15).
The expression "styrene polymer" embraces not only polystyrene
itself but also thermoplastic polymers of any poly~erizable substituted
styrenes as well as eopolymers of styrene with one or more other com-
patible polymerizable substances as the nuclear-allcylate~ or -halo-
genated styrenes such as the ring~me-thyl or -chlorine-substituted
styrenesj or even alpha-methyl styrene, or with beta unsaturated
esters9 ethers, amides, or nitriles of acrylic acid and their alpha
: 15 -position-alkylated homoloGs, vinyl esters o~ a:liphatic and aromatic
carboxylic aci~s, N-vinyl compounds of N-vinylcarbazole 9 N~vinyl-
imidazole or N-vlnylpyrrolidone.
Such thermoplastic copol~ners of styrene usually should contain
at least about 50~,~ o~ ~xtyrene by weigh-tt or lt may be the predomina~ing
component or at least equal in predominance to any other hi~her
present co~ponent of any terpolymers.. The copolymers of styrene
include also any of the various impact polystyrene containin~ a major
~art o~ styrene and a minor part o~ a styrene-buta~iene rubber (usual-
ly d~sienated SBR, sometimes called Buna-S), ~or example, as produced
;~ 25 by emulsion po].y~eriza-tion of ~bout 75 parts o~ butadiene and about
25 parts o~ .styrene. Thu5 ~ styrene polymers also include styrene
alloys (i.e. pressure or melt ~nixtures~ o~ polystyrene with other
compatiblQ poly~ers generally of ethylenlcally unsaturated monomer~,
The te ~ 'ipolyethylene 1l in the expression l'an expanded poly~
ethylene" or ~!a polye~yl~ne" int~nds ~th~ h m~lecul~r weight.

~ J


~2A-

3'~


(at least 60~0) product an~ is generic as embracing low ~.ensity
no1yethylenP (speci~ic gravity below 0.92), the hi~h density procluct
(sp. g. over 0.94, ~enerally 0.941 to ~.965)~ and the meflium density
polymer J?ro-luct (a b~en~ of both the hiGh an~ low), as ~e].l as the
impr~natabl~ polyethyl~ne (e.g~ an extrude~ melt mix of polyethylene
wi.th 10~ poly.~tyrene and which can be calJ.ed "polyethyle~e-poly
styrene al].oy"); all of which are ava.ilable in f1ak~ or in oube.s
simi.lar to ~olystyrene pPllet.
The term "bit pieces" inc.ludes any of -the ~iscretc free-:rlo~in~
~orms n~ ~a11y 0~ th~ ~t,yrenc-~?olymers an~ o~ ~ny o~ the polyole~s
~rom polyetllylcne to th~ T?oly-rnethy].penteno, such as thP various siz~;
o~ crallule.s mad~ l~y cut1;.ing the respective e:~trucled ~ol.ymer into
small. lcn~th,s u.~ually called pe1lets or cry.s-tal (as ~i-th 7.t styrene
-j?olymPr) or pellets or cubes of a pol.yethylene-polystyrenc al.loy,
.15 the ~ariou~s si.zes of styrere-polymer beads obtainecl ~rom suspension
po~?..ymerizati.on or otherwi.se as by mo].di.nG the J?arti~cs ob-tained b~
.i.sinte~ral;i.n~ ,3ny o~ -~hese dif~rent pc?lymer forms, a11d the so-calle~
"grin~" incl.udin~ the coars~ly groun~ molde~ polymer or waste or oth~r
scrap .sueh po].~fm~r (o:~ ~arious ~:i.ze3, e.g. ~ ]./8 inch thic~nes.~ 4
il~ch ~lidth, and 3/8~inch len~th~, and ~ny other small size~ shapes
of an~y o~ l;hem.
.pandable styrene-polymer bi-t-pieces can be pr~parcd by
s~i~a~le lcno~l1 m~thods 9 for examl~le, prep~rin~ expandable st~rene
-pcllynner bit-pieces as disclosed in U. S. paten~ No. 2,~33,692
issued ~ay 9~ l9~ ,xpanclable polyethylene styrene a1loy can b~
~repared similarly.
r~xpancled ~tyrenc polymer bj.t~piec~s can be prepare~ from
evpandabl~ polystyrene by s~titable lcnown mcthods. 3ne ~c-thod for
~reparin~ expallded .s~yrene polymer bit pieces is by he~-ting them,
~or:examp3.~p wi.th ai~r or steam as disclos~d in U.S. pa~en* 2~9~3,69Z

~ '7~


(column 4 lines 65-69), "to a temperature above the so~tenin~ point
o~ the styrene pol~ner" as disclosed in U. S. patent No. 3,001,954
(column 3 lines 20-23). See also U. S/ patent No. 3~259r594 tcolumn
2 lines 24-27). Expanded polyethyl~ne-polys-tyrene ~lloy bit-pieces
can be prepared s.imilarly.
Expanded bit-pieces of the polyethylene, polypropylene9 pQiy
butene or poly methylpentene can be produced by preparing the respec-
tiYe expande~ polyolefin by suitable known methods inoluding incor~
porating into the specific polyolefin (before extruding it~ a
chemical ~oamin~ agent (so-called pneumato~en, usually a complex
nitro~en-containing organic compoun~ that decomposes at the ex-trusion
t~mperature, liberatin~ nitrogen) with extrusion temperature adjusted
so that the pneumatogen decomposes as the polyolefin leaves the out-
let of the e~trusion die, as briefly described in Plas~ics Extrusion
Technology, by Allan L. Gri~, Reinhold Publishin~ Corp., New Yor~,
N.~. (1968) pace 2219 and reducing the expanded polyole~ins into
~: blt-pieces by cutting or otherwise.
Certain physical ~ea-tures o~ the micro-bits o~ the invention are
sho~ by the ~hotomicrographs of tlle dry micro-bits in the ~irst
~iPteen f`i~lres o~ the accompanyin~ drawinGs, of which F~GS. 1 to 9,
14 and 15 are o~ polystyre~e ~icro-bi-ts and FIGS. 10 to 13 are of
low density pol~leth~lene micro~bits, and wherein
FIG. 1 is a pho~omicrograp~ at a ma~nificatio~ of 161 times, by
transmitted ll~ht~;
FIG. 2 is a SEM~photomicrograph of the micro-bits at magnifica~
tion o~ 4~000 times;
FIG, 3 is a SEM microphotograph at magnification of 1800 times
o~ about the area that gave ~he lower le~t qua~ter see~ in FIG, 4;
FlG. 4 is a S~M microphotograph take~ at magnification o~ 360
times;



4;~

3'~ ~

~IG. 5 is a microphoto~raph taken at ~ magnification of l~O
tirnes;
I~IG. 6 i~s a S~ mlcrophotocraph taken a-t magnification of 5~0
times of the area -that ~ave the del.inea-tcd center portion of FIG, 5;
FIG. 7 is a SFJM photomicro~raph a-t l,n~O times magnification
of the arca tl~at gave the de].ineated portion of FIG. 6;
FIG. ~ is a S~M photomicrograph at magnification of Z,OOO tim~s
of the area 1;hat gave the prominent ri~ht portion of FIG~ 7;
FIG. 9 is a SEM photomi~ro~raph takcn a-t magni~ication of 5,000
ln time.s and shows the area th~t a~peared in the lower right hand quarter
of FIG. ~;
~IG. l~ ;.s a SE~ ~hotomicro~raph taken a~ ma~nification of ln~O
time~ of ~olye-thyIene micro~b.its and ~parcntly o~ the loca-tion that
ave tl1e area in -ti1e Iot1er left hand ~uarter of the up~er ri~ht hand
quartcr of ~IG. 13;
: FIG7 1.l i..s a ,~F.,M pho-tom.icro~ra~h takcn a-t magni~.ication of
lO,O~O times and ~mbracing t.he area of the slide fieen in about the
center ~f ~.IG. 10;
~ FIG, 12 i~ a ~S~M ~hotor,1ioroGraph taken a~t maGni:fication o~
2n 2~ 0 timos and coverin~ ~.he area of th~ ~lide seen .in lo~l~r magni-
fica~ion in about ~h~ mid~le o~ FIGo ll;
FI~. .L3 is a S~M~ho-tomicroc~raph ~aken at magni~ication o~ 380
times o~ tl1e same pol~ethylene micro~bit.~ involved in FIG~. lO to 12;
~ ;'.IG. 14 i~s a SEM ~ho-torn.i.~rogrira~h l;aken at ma~n.ification of
Z5 lO,O~O t~r;les o~ l~olys~yl~n~ micro-hits; c~n~l
FIC, 15 is a S~ photomicro~raph at ma~nifica~ion o* 20,~0
time~ o~ a portion o~ the polystyrene micro-bits sli~e view~d in
FIG~ 140
::
'




~5-

3~7


FIG. 16 is a schematic illustration of a s~stem for remo~ing
the trapped water from the mi.cro-bits of the invention as obtained
in the aqueous slurry leaving the comminutor wherein the micro-bits
are produced from the expanded startin~ polymer (a~ more fully de
scribed shortly after Example 2 below).
The expanded micro-bits of the invention are prepared by con-
tinuously feeding expanc7~d bit-pieces of a styrene-polymer cr any of
the aforesaid polyol.efin~ and wa-ter into a con~ined comminuting zon~
ha~in~ a feed inlet to it, repeatedly impelling the resulting mixtur~
of the startinG bit-pieces in -the ~ater t,hrou~h a circular path by
repeated impact on them in -the t~a-ter by a plnrality o~ impact sur-
faces spaced a~art from one another and rotated around the axis of
said circular path at from about 4700 to about 8000 revolutions per
minute, an~ a t the same time by said impact surfaces ~riving said
expanded bit-pieces~to~and a~ainst corner-shaped edges of a dispersed
- plurality of ~rom substantially circular orifices (a) having a dia-
me~er of from aboub 0.102 to about 3.17~ millimeters (i.e. mm.) to
substantially rectangular orifices ~rom about 0.254 to about 3.175
mm. in width by from about 3.81 to about 12.7 mm. in length, ànd ( b )
20 ~ being arranged in screenin~ array in an arcua-te plane spaced radially
out o~ range of s~id impact surfaces to an extent that need be cnly
sufficient to avoid collision between said orifices and said impact
surfaces, as ~rom about 0.508 to 1.016 mm., and thereby repeatedly
tearing, ripping aild shearin~ micro-bits of the respective expanded
2~ polymer from said bit-pleces thereof; said fed in water being so
propor~lQned to said fed~in~expanded polymer bit~pieces to prevent
~the content o~ the~co ~ lnuting zone ~rom reaching a tempera~ure that
would adversely effect~ e ~ntegri~y o~ said starting bi~-pieces
and~or the desired~ mloro-bitsO ~ `



~ ~ ~ f

~6
:

'7

The pre~aration o~ these micro-bits of a styrene-polymer or o~
a polyolefin (~rom a polyethylene to a poly-methylpentene), and so
also t,he method o~ the invention, can be conducted by disintegrating
: ~he respective starting expanded st~rene-polymer or polyolefin bit
-pieces in a comminuting machine (such as that produced by FitzpatriGk
Company, of 832 Industrial Drive, Eimhurst, Illinoi~ 60126, U.S.A.)9
acGording to their Bulletin No. 152 copyright 1968~ using the broach-
ed ~ixed blades (identified therein by "Code DS 225") to replace the
blades or other comminuting elements, moun-ted for rotation in the
co~inuting chamber model ~AS06~ both shown on that bulletin's page
5~ m at chamber is liquid-ti~htly capped7 for example, by a cover
such as shown in theîr Code M44D6 or Code MA44D6 (upper hal~ of
page 3 o~ their Bulletin 152).
That model DAsO6 comminuting chamber is rectan~ular in hori-
zontal cross-section and has a pair o~ opposed parallel entirely
vertical walls integrally Joined at each o~ their opposite ends by
~ a aeparate one or a pair o~ opposed vertically arcuate walls each
::~ with its con~ex ~ace e~ osed to the exterior.
Sixteen identicalg slat-shaped comminuting arms are separately
removably but fixedly carried with their snugly ad~acent to one
another bases encircled about~ ~nd keyed to, the operating sha~t and
intermediate its ~ree outer mounting ends. m ese arms extend radial-
ly out from t~e s~a~t (e.g. 127 mm. ~rom its axis to the outer end
of each arm) w.ith the first of each consecutive four o~ them extend-
ing horizontal1y toward one arcuate wall, the~second of each ~ourexteDding vertioally9 the thind four of them extending toward ~he
: other arouate wall~ and the ~ourth ~our of them extending ~ert~cally
downwa~d.
Earh arm is rec~angular in c~o~s~sec~ion in a plane ~unning
30 throu~h the entlre length o~ the s~aft's a~cl5 and o~ ~ha~ arm, and

::

'7~


of each arm 180 removed from it~ The outer end of eaoh arm meets at
right angles with its two wider sides (25.4 mm. width) and its narrow
or impact side ~9.525 mm. wide) ~acing the direc~ion of rotation.
That narrow side also meets at right angles with the t~o wider side~
which are paralle~ to one another for most o~ their width and with
the trailing third of their surfaoes t.apering to one another a~d ter-
minating in a knife ed~e o~ their trailing end~
Each free exposed end of the sha~t extends through its respective
stu~fing box in its neighboring one of the two parallel vertioal walls
on throuLrh a bearing carried on a respcctive trunnion a~.~ixed to the
m~chine's ~oundation and spaced outwardly away from the respective wall.
A drlving pulley is mounted on each end o~ the shaft extending out-
wardly ~rom its respective mounting -trunnion.
The bottom o~ the comminuting chamber is an exchangeable dish
-~ha~ed, arcuate screen curved convexly downward with an inside radius
rom t~he axls of the operatlng shaft~ equal to the length of a com-
mlnuti:n~ arm plus~0~762~mm~. clearance) The screen's overall rec-

,
tangular peripheral opening has such dimensions and shape to enable it
: to be removably fitted in a liquid-tight engagement with the ~ottom of
the four ~alls o~ ~he comminutingr chamber~
m e screen ha~ sta~gered rows of, for example, circular holes
varylng~ln fl.iameter as~rom;0.102 to about 3.175 mm. and closely
spaced to one another with surficient space between them ~or the screen
to~hold up under workln~r conditions.
: 25~ Except ~or its starting material feed hopper inlet a-t one side
of:;it;~ the rest o~ the chamber's cover is arcuate :and convex upwardly
with~a radlus (from~the~axls of ~the operatir~ shaft) sufficien~ for the
rotatlng a3ms to have a~ 0.;762 mm. clearance from ~the lnwardly faclng
~ ;sur~aoes o~ a plurali~y (eOg- three~ pre-brea~er bars (about 20,32 cmO
30 ~ lon~ and 6.3~ mm~ wide) :protrudlne for 3.175 mm. along their entire


:
-8-

~ 3'~ ~

length into the interior of the oomminuting Ghamber~ and extending
spaced apart ~rom one another and parallel to the axis o~ the Dpera-
ting shaft.
The selected driving pulley on the operating shaft is connected
by driving belts extending from a mQtor shaft drive pulley ~nd can be
op~rated at speeds embracing the range o~ from about 4700 to about
8000 r.p.m., and more effectively from about 5000 to about 7500 r.p.m~
The micro-bits of the invention are variously applicable, for
example, in filtering and impro~ing ~luids~ both liquid and gaseous,
lQ That is done, for example~ by admixing the selected styrene-polymer
or polyolefin micro bits into the liquid to be impro~ed and there-
after filtering them out, or by ~iltering the liquid to be impro~ed
through a bed of the micro-bits. m e polymer micro-bits thereby re~
move invisible dissol~ed or invisibly suspended organic material ~rom
the liquid and ord:inarily leave it free ~rom development thereof even
after long standing.
:~ To illustrate~:tap water in Matawan9 New Jersey, U~SoA~ was
filtered through a ~hatman No~ 2 filter paper to the extent of 473.2
cubic centimeters ~i e. cc.) into a first clean, 946.3 cc. Mason jar
which then W~6 tightl~ sealed. 0.4 g~ams of the micro-bits (prepared
from expanded polystyrene bit-pieces) were wetted with about 20 cc.
of this same tap water and admixed with about 473.2 cc. of the tap
water and then ~iltered through another l~hatman No. Z filter ~aper
into a similar second clean, 946O33 Mason jar and tightly sealed~
A week later a slight yellow ha~e wa~ noted in the first jar,
but the water (which had been admixed with the ~icro-bits) in the
: :
second jar still was per~ectly clear. The yellow haze in the fir~t
ar;increased:in amount and in density with later settling to the
bottom~ o~ -the~ Jar~during observati~on over a period of three months~
: 30 - Yet the water that had been :~iltered through the poly~yrene micro
bits into the~second ~ar wa8 still per~ectly clear.



~: : :

.


37 ~ ~

Illustrating use in ~iltering and improving a gaseous fluid,
~hese polymer micro bits also can be used as the packing in air
filters by being admixed with sui~able paper-making fibers and
made up into sheets for loading into air ~ilter frames.
Comparable liquid and gas filtering result~ are pro~ided by
micro~bits of a polyethylene. Micro~bi~s oX the other polyole~in~
are similarly use~ul.
Some batches o~ these polymer micro-bits o~ the invention
produr.ed, ~or example, b~ the abo~e-descri~ed comminuting machi~e
10 using a screen having circular openings of sorne sizes, are obtained
with content of varying amounts from ~ery little or at times up
to about 20% or so of fibrous particles s-till finer in size than
: that in the ran~es desoribed earlier above, for example, down to
15 microns or to 10 microns or so in ~idt~. Generally the pres
. ~15 ence of any such amounts of these smaller sizes may not introduc~
: ~ any disadvantage in the particular use that is to be made o~ the
micro-bits. : ~
`: :However, i~ need be, these finer si~es can be removed by
being filtered out by available screening or other suitable means~
for example, a high capacity centrifugal si~ter produced by the
Kason Corporation, oP Newar~9 New Jersey, U.S.A. This invol~es
:~ ~ uni~ormly ~eeding the~micro bits by a feed screw di~charging into
a h~elical paddle ro~ating in a horizontally positioned cylindrical
si~ting chamber wherein centri~ugal__orce accelerates movem~nt o~
Z5~ ~he micra-bi~ pa~ticles against the siev~ whi~ a~taohed to i~




::: :::: : ;:

~:
~la-

.

,~


su~porting basket in a ma~ner ~hat allows the sleeve ~o ~ibra~e
~reely.
~n conducting the method o~ ~he inventio~, the operating
conditions may cause an increase in -~emperature of the charge v~
expanded styrene~polymer or polyolefin bit~ieces being di~in~
tegrated in the comminu~ing zone, Tha~ may be mors mar~ed with
some styrene-polymers than wit~ others, so that ln ~ome o~ them
the temperature rise may reach a level suoh tha~ at it and higher
t~e styrene-polymer bit-pieces would not readily or satis~actorily
tear or shear un~er ~he particular operating conditions and poss~
~ly have a tendency to stretch or o~herwise modi~y the reac~ion
o~ the material being tre~ted, and so ad~brsely e~ect the
desired tearing or shearing o~ the starting bit-pieces or ~J~at
already has been to~n or shorn ~rom th~m. m at is to be a~oided,
as by feeding more water with ~he bit~pieces~
The finished comminuted polymer micro-bi~s leavin~ the
comminutor mani~es~ the p~operty o~' holding onto water to the
exken~ o~ :~rom possibly about 40 to 50 times their dr~y weight,
a~d wi~ch i ts so held water ~orming a non-:~luid plastic mass which
is de~or~able and ¢arl roll, but w~thout becoming ~luid . me water
is not released ~rom this mass by dralning or o~inary ~iltra~ion,
~ut requires pressure or æuction, but yet it retains a signi~i-;ant
amount o~ wa~er. For example, sQme high pre~sure reduces the mass
to a wa~er content OI on~y about 50 percen~.
~5 The propo~ion o~ water fed in~o t~e comminu~ing c~am~er then
should ~e at least enough ~o~ the mix~ure o~ wat~r ~d produced polymer
micro-bi~s ~o be ~u~lc~en~ly :~u~d ~eadily to now ~hrou~ t~a~ orif~e8




(

~9 3'7~ ~


of the screen bo-ttom of the comminutor. Con~eniently9 th~ water should
be lrom about 55 to a~out lOO times ~he weight of the produced expanded
: styrene-polymer micro-bits.
It is beneficial also to admix the starting expanded styrene
~pol~ner or polyolefin bit pieces with an amount of water su~ficient
substan-tially completely to wet their exposed surfaces before ~eeding
them into the comminuting chamber~
It is advanta~eous also to the conduct of the method of the inven-
tion that the bit-pieces in the comminutin~ zone are driven by the im~
pact surfaces alternately (i) to and against cornered ed~es of at least
one pre breakin~ or impact surface (of at least one pre-breaker bar dc-
scribed above, page 8 line Z7 to page 9 line 2) spaced circumferential-
ly away from said ori~ices and radially similarly out of range o~ said
impact sur~aces as are said orifices, and then (ii) to and against said
orif1ces.
It is also advantageous that ~he impact arms be axially and angu-
larly spaced away from one another. -
~ : For som~ u.se.s to:~be made of these styrene-polymer or polyolefin.
; m.icro-bits, they can be used with the water which is held by them or
'O any lower amount that is retained after either or both o~ application
o~ pressure or vacuum to remoYe AS much as it is desirable to remove
of that which thus can be removed.
To~remove the rest o~ the water when dry micro-bits are desired,
one way is to freeze the product having the wa~er co:itent left after
its partial removal by pres,sure and/or vacuum. Then the frozen micro
-bi~ts are left, or heated,~o thaw out and attain a temperature just
abo~e ~reezin~ or up tG ambient, at which the still retained water
then ~reely dra1ns o~ hen all that can drain o~ has lefty ~he
:residual water c~n be ~xpres~e~ a~/or withdr~n ~y ~acuum ~ollowed
:30 by ~inal dryin~



:'

~ 3 ~ ~ ~

Another anc~ more prac-tical way to remove the water held by the
micro~bi-ts di.schar~ed by the comminutor is described further below
in relation to the system .illustratec] in FIG, 16 o~ the drat~1in~s.
The inven-tion is illustrated by, but not restricted to, -the
followin~ examples:
a ~ - ~ :
~5 li-ters o~ e~pan~in~a~ent .impre~nated, extruded polystyrene pellets
(crystal) expanded to f'rom about 6.35 to abou-t 12.7 mm. substantially
round pellet;s havin~ a bullc density ol 12 ~rams per liter ~!ere com-
rninuted in a comminutin~ machine (as des~ribe~. on pa~e 7 line 4 topa~e ~ line 6) ecluipped ~ith an input, feeder 1~.16 cm. in diameter by
7,G2 cm. long and a bottom arcuate screen with holes o~ O..lO16 mm.
niameter.
Th~ ro-tor is set to run at 6,~ r.p.m. an~ the J.'eecler set to
].5 char~ the expanded polystyrene bj.t-pieces a-t the rate o~ ~5.4 li-ters
~ever~ 5 n,inutes (i.e. ~25 liters per hour). The startin~ expanded
:polys~tyrene bit-pieces to~ be lntroduce~ in~to the fec~er ~ere wetted
~: ~ with sufI1c1ent water qub~stant,ially completel~ to cover their outer
surface.s. The thus wettP~ expandecl pol~styr.ene bit-pieces were char~ecl
ZO irlto t~le ~e~r con-tinuously at a r~te o~ 35.4 li.ters cvery 5 minutrs,
~hil~ at the s~m~ time water was injected i.nto the co~minutin~ ch~mber
throu~h ~lle two 1.6 mm.~diameter Jet orlfices at a rate o:~ 7.57 liters
~er inj.nute.
The m.ixture of l;he c~n~e~ poj~.ly~tyrelle micro~ s .le~vinG the
~5 screen bottom of the comminut:ing chamber was collected in open ~ru~s
wi.th ~otto1n drain ~lugs:, wherein the free w~ter sett].e~ to -the bottom
~an~ ~he ~o.l~styrene~mlcro bi~s ~Jith the boun~ ter held by th~rn in
the ~ro]~ortion of 2 parts of mlcro-bits to 9~ ~arts o~ ~later, due to
~the entrapped air~ rose on top o~ the ~ree waterO The ~ree water
was drain~d o~ leavin~ ~hind a plastic mass o~ t~e (disintegrated~



13-

. '

3~7~


expanded polystyrene micro-bits in the water physically bound to them,
The plastic mass wei~he~ 255.15 kilos and contained 5~1 kilos of miGro
-bi~s with 25~.05 kilo.~ of water boun~ by them.
27.24 I~.ilos o~ the plastic mass ~hen placed i~ a close weave
double cotton bag wer~ subjected to pressure until 22.71 liters of
water were expr~sse~. The remaining 4,08 ~ilos containing 544 grams
OI expanded polystyrene micro-bit;s then were dried in an open dish in
an oven maintained at 110F.
In this connection1 ~or example, micro-bits produced as in
1~ Example 1 from expande~ polystyrene bit-pieces prepared from v.ir~in
~sometimes call~d "prime" 3 poly,s-tyrene havin~ a density of 1.1, showed
a density o~ 1~0. That is 90.9 percent of the density o~ the original
starting polystyrene crystals, from which there was prepared the ex-
pande~ polystyrene bit-pieces usçd as the starting material from which
; 15 the ultimate polystyrene micro-bits were prepared. The density o~
; the dry micro-bits o~f the invention thus is substantially the same as
that of the sty~ene-poIymer from.which there was prepared the expanded (~
styrene-polymer that wa.s used as the starting material used in pre-
paring the aforesaid micro-bits.
~.e 2 - ~ = ~ ^ One inc~
O
pieces o~ impregnated polystyrene scrap having a bulk density of 16
: : grams per liter we~e treate~ by the same steps as in Example 1 but
~ed at the rate of Z8.32 liters in 6 minutes and with the rotor at
6500 rcp.m.; and in the .same way yielded a plastic mass like that
25: obtained in Example 1 except ~or its havin~ a lighter grayish pink
hue than that o~ the bulk o~ t~e starting impregnated scrap.
Replacipg the starting:expanded polystyrene bit-pie¢es of each
o~ Examples 1 and 2 by som~ other ~antlty o~ any other d.e~si~y o~
: .
: :
~: :

.

~14

3~


bit-pieces ol virgin or scrap expanded polystyrene, or of any
expanded styrene-acrylonitrile copolymer or o~ any other ex~
panded styrene-polymer or any above described herein applicable
polyolefin; and separately respectively repeating the steps o~
either o~ those examples with the same or somewhat different
proportions of water or different rotor rate9 ~rovides the
corresponding relatively similar micro-bits o~ any o~her e~panded
styrene polymer cr of any e~panded above described herei~ applic~
able polyolefin, ~he respective corresponding additional ex~mples
are to be oonsidered as i~ presented herein in completely writte~
out form, to avoid making this specification prolix~
By replacing the screen bottom of the comminutor described
above (page ~ lines 4 to 24) by a screen o~ the same o~erall
dimensions but instead having a herring-bone array o~ rectangular
ori~ices 12.7 mm, lo~g by Q.254 mm. wide, and using the thus
: changed comminutor in repeating Example 1 and Example 2, the
: selected startîng mat~rial expanded styrene polymer bit-pieces
or expanded polyoleîin bit-pieces similarly yields the same type
o:~ respective end product micro-bits being to the extent oî sub~
stantially co~pletely or entirely completely 1005S 0:~ ~rom about
5 to 15 micro~s wide and o~ many Yarying lengths up ~o about ~25
microns ar~d from substantially comple~ely to com~letely free o~
intact cells.
me at least 9~ percen~ OI water in the ~luid mix*ure or
Z5 ~ ~lurry of s~yrene- polymer or polyolefln micro bi'cs in wat~r




.


leavi.ng the commin~tor, as ~rom the operation o:f either Example 1
or 2 or any modification o~ them (such as provided by the second
and third just preceding paragraphs), can be removed considerably
to provide dry-to-the touch chunks, cakes or mats of the respec-
tive styrene-polymer or po~yolefin micro~blts having, for ex-
ample/ as much as 84 percen-t solids or more, by a water-elim~na~
tion method USiPg a system such as is schematically shown in ~IG.
16.
Thls method o~ produc~ng~such dry-to the-touch chunks,
0 cakes or mats o~ -these respective polymer micro-bits ~rom the
highly aqueou$ slurry o* them leaving the comminutor involves
in-terposing a first ~oraminou$ carrier mernber (e.g. wire gauze~
between said polymer mi.cro~bits s-urry and a source of vacuum an~
th~reby to apply reduced pressure -to said aqueous slurry through
said carrier member to an ex-tent at least sufflcient -to deposit
- on said carrier member a removably adhering layer or web (of
practical thicknessS say, about 3.2 rnm.~ of said micro-bits with
an intermediate reduced wa-ter content (for example, sol.ids con
ten-t o~ at least 16% by weight) low enough to enable -the web
to retain its continuity on said carrier member, con-tacting
-the free sur~ace o~ the adher:ing m:lcro~bits web with a second
foramlnous member thereby forming a sandwich of the micro~bits
web between both said foraminou~ membersg covering the ~ree e~
~ posed ~ide o~ each ~oramino~ member with a continuous layer o~
wa-ter~absorbent shee-t material h;aving a greater water absorp-ticn
capacity than that o~ said micro-bit,s web; then subjecting the
re~ulting five layer assembly to pressure to enable the layers
o~ water-absorbent sheet material to absorb its practical capable
extent of wa-ter ~rom~-the micro~bits mat through the interposed


: : :


B



foraminous member3, and thereafter separa~ting ~ach layer o~ ter
-absorbent sheet material from its respectively contiguous forami~ous
member and separatin~ each foraminous member from its respective sur~
face ol the further reduced in water content micro-bits mat, and
dischargirl~ said lat-ter mat,
A feature of this m~thod is ~hat it can be operated continously
in tll~t ~ach foraminous member and water-absorbent sheet is continuous
and there i.5 included a further step of then passing each separate
water-absorbent mat~ri~l sheet (after the pr~ssure-applyinG st~p)
throu~,h a dryill¢ zon~ to rid these she~ts o~ absor~ed water ~o an
e~tellt to en~le using -them ~ain to ab.sorb water ~rom succes~ive
fur~ther ~ortions of intermediate la-t;er content r~duced micro-bits
m~t picked up from the exit ~nd o~ the vacuurn application step.
Thus, ~Yith each foraminous member bein~ continuous the first
15 one of ~h~m is re turned to the starting slurry there again under the
~ influence of the vacuum to continue to pick up a continuous run o~
; depositi.n~ Micro-bits ma-t. At thc same time, the second continuous
foraminolls member returns to the discharge end o~ the vacuum zone
to com~lete thc s~nd~ichin~ o~ the continuously forming micro-bits
~leb be-twee~l the t~o oppose~3 continuous :Coraminous membersO Then
in turn each of the t~lo cont~nuous water-absorbent sheets continuous-
ly contac-ts tho free sur~ace o:f i ts respec-tive ~orarllino-ls member.
'i'he continuous ~ressure applied to the moving five-layer
avs~m~ cl~hances the cont~nuous absorp-tiorl of water from tlle Inicro
-bits ~:eb into the continuously o~pos~d water~a~sorbin~ sh~ets
through t,he for~minous members from -the continuous micro-bits w~b.
This web: thcn contlnuously is d.i,schar~ed a~-ter the withdrawal of the
water-absorbent sheets followed by the separation of th~ foraminous
; mcmbers, wi~h each water absorbent ~he~t continuin~ on through its
3~ re~pcctive drying ~one.



~17


Referring now to FIC~ 16 the slurry of micro-bits in water
is discharged from the comminutor into the starting slurry-receiving
tank 10. Spaced upwardly from the bottom of tank 10 and i~wardly
from its ends, vacuum drum 11 is mounted rotatably on its horizontal
shaft 12 coaxial with vacuum d~lm 11, and supported outside of tan~
10 on bushings ~not shown) rotatably mounted on supports (ngt s~own).
A first continuous wire gauze Iilter screen 13 (e.g~ 40 mesh, for-
aminou~ member~ supported on idler rollers 14 and 15 travels in the
direction shown by arro~J a downwardly under and around the lower
half of vacuum drum 11 where the wire gauze 13 passing through the
slurry picks up a web deposit of partially water content reduced
micro-bits.
A second wire gauze ~ilter screen 17 (also 40 mesh, foramino~s
member) supported over rollers 1~ and 19 pas.ses over tensioning
roller 20 and under guide rollers 21 and 22 in the dire~tion show~
. by arrow b, thereby the intermediate water content micro-bits web
adhering to filter~screen 13 is sandwic~ed between i~ and filter
screen 17.
~ A sontinuous water-absorbing felt sheet 24 supported on rolle~s
25 and 26 travels in the direction shown by arrow c under te~sioning
roller 27 and around guide roller 28 and ~here continuing to guide
; roller 29.~ m ereby~he:stre~ch of screen 13 extending over the
: : distance between rollers 28 and 29 covers the exposed ~urface of
wire gauze screen 13.
~ A second water-absorbent felt sheet 31 suppor~ed over rollers
: 32~:and 33 travels~in the direction shown by arrow d under idler
: rollers 34 and 35~and over tensioning roller 36, whereby felt sheet
31 for the distance:bétween rollers 32 and 33 contacts ~he exposed
under~ide of filter screen i~. T~at the~ completes the ~i~e layered
;30 ~ assembly o~ micro-bits web s~dwiched betweQn the ~ir~ gauze filter

`


~8~
. .

~ ~ 3~7~ ~

screens 13 and 17 covered by the felt sheets 24 and 31 respectively.
Intermediate the two pairs of respectively opposed idler
rollers 28 amd 32 an~ Z9 and 319 this five-layered assembly passes
between opposed pressure roll~rs 38 a~d ~9, ~hereby their 56 cm.
length applies a total pressure o~, for example, ~08 kilos (thus
7,3 kilos per centimeter, i.e. cm.) by pressure roller 38 again~t
that assembly.
After ~elt sheets 24 and ~1 separate at the junctions of rollers
29 and 33, the filter screens later separate as screen 17 passes down
o~er idler roller 19. Then the micro-bits web reduced to a cake o~
84 percent solids is removed from screen 17 by separator blade ~0
and drops into micro-bits cake receiver 41. At the same time the
~irst or upper ~ilter screen 13 passes upwardly around idler roller
42 and any micro-bits cake adhering to that screen is removed from
it by upper separator blade 4~ and drops i~to micro bits cake
recei~er 41.
~perating the fore~oing water content reducing system with a
:. 28 cm. in diameter and 56 cm. in length vacuum drum 11 at a sp~ed f!
of 10 revolutions per minute (r.pOm.) with a feed o~ 11.4 liters
per minute of styrene-polymer.micro~bits slurry ~containing 2 per~
cent o~ solids~ ~rom ~he corrlminutor provided a 30175 mm. thick wet
mlsro-bits layer, and with the foregoing 7.~ ~ilos per cm. pres.sura
by pressure roller 38 ga~e a yield o~ 10.9 kilos per hour containing
~4 percent o~ solids ~ styrene~polymer micro-bits~
; 25 In its respecti~e drying zone (not shown) each water absorbent: ~ sheet can be hot air ~or suitably otherwise) dried and with prelim-
inary passage between pressure rolls when its water content is high
enough that a signi~icant part o~ it can be expressed.
The foregoing .system and apparatus for remo~al ~rom micro;bits
of wa~er or other llquid inert ~o them i~ not limited ~o its aust
above described specîfic use on expanded poly~tyrene micro-bits. m e
: method and system also are applicakle similarly to micro-bits o~ any
of the other expanded styrene~polymers as well as to tho~e o~ any

~19~

~3~


polyole.fin micro-bi'cs. So also, the system is not r~stricted to
the earlier above indicated dimensions or layout shown in the
illustrative drawing~ but can be modi~ied to provide such other
production capacity as is practical and ~ariation in layout o~
the respective pa~ts to meet particular requirements of plant pro-
: duction capacity and plant space accommodations.
mis system for withdrawing such large content of water ~rom
the micro-bits is not limited to using a rotating vacuum drum to
provide the web o~ high water conten~ micro-bits to be passed
through pressure rolls 38, 39 ( FIGo 16~ ~ Slurr~-receiving tank 10
and vacuum drum 11 and its shaft can be eliminated and rollers 18,
Z0 and 21 moved to about the le~t o~ the ~ormer location of tank
10 with filter screen 17 correspondingly extended.
Then the highly liquid slurry product from the commi~utor is
~ed to a feed box (similar to the head-box from which paper pulp
~ is ~ed to the fourdrinier in paper making); located above ~ilter: ~ screen 17 (slightly to tbe right o~ roller 18) and discharging
onto that screen~ There ~he free water accompanying the micro-bi~
drains through the early portion of screen 17 after passing o~er
roller 18. Before screen 17 reaches pressure rolls 38 and 39 it
passes o~er a suction box (much li~e that at the fou~drinier di~-
~; : charge end) where part o~ thewRter held by the micro bits is with
drawn.
Roller 15 i~ moved somewhat to the right so as to be located
: 2~ just to the righ~ of the e~tension upward ~rom roller 18. Screen
13~is shortened and maintained taut by running under a roller re-
placing drum ll and posi~ioned ad~jaoent to wire screen 17 as it
travels past ~he suctlon box. m e layer o~ wet micro~bits started
on screen 17 ls sandwiohed between screens 13 and 17 as they con~
~0 tinue a~ter roller l8 to and through ~he nip be~ween pressure rolls
:~ 3~ and 39.
.

~ -2~-

~ 3 ~

Water-a~sorben-t sheets 24 and 31 bene~icially are of cotton
~elt but can be o~ any other suitable water;absorbent sheet
material having a grea-ter ai~inity f~r wa~er than the apparent
surface tensio~ holding the water to the micro-bits~
The comrninu~ing machine is not limited to the speci~ic
details of the i~lustrative appl~.cable unit described at page 7
line 4 to page 9 line 6. For example~ the mAmber o~ comminutirlg
arms can be varied even up to 32 in relation to the specific
plant production needs and the conXiguration of the housing can
be mod.i~ied accordingly. Some variation in certain parts o~ the
cornminuting arms also are possible. mose o~ its ~eatures which
pro~ide the effective commlnuting function should be retained
while allowing some varia~ion in o~her areas o~ these arm~. Also,
the pre-breaker bars are not limited, for example, ~o the speoi-
15~ ~ic length or number, ~or either oan be ~aried with respect to
:
the speci~ic~p~oduction plan and in some cases they might be
omltted. ~ ~ ¦
e nature o~ the comminuting operatian and the appearance
o~ the micro bits (as in FIGS. 1 to 5) show that the indi~idual
micro-~it particles have no signi~icant uniformity in outline.
at the starting styrene-polymers and polyole~ins (~rom
a polyethylene to a poly-methylpentene), the expanded bit pieces
o~ which are conve~ked into -the micro-bits of the invention, are
thermoplastic shows tha^t they also are ex-trudable.
: 25 That:the mîcro-blts~herein, even though holding a consider
able amount of~wa-ter~e~g. as much a~ about 80 percent); are said
to :be dry-to-the-touch means that the micro~bits when touchQd do
not wet the flngers or th~e palm o~ the hand wl~aen held in :it.
:~ ~ While the inven-tior~ has been e~ ined by d~tail~d descrip-
~30 tlon o~ ce~aln speci~ic embodlments of it~ it is understood that
various modificat:ions~ and su~stitutions may be made in them within
~he scope o~ the ~?Rended clalms whic~ are in~ended ~l~o ~o coYer
~qui~ale~ts o~ t;hefie embodiments.
~:
~1~

Representative Drawing

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Administrative Status

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Administrative Status

Title Date
Forecasted Issue Date 1981-01-13
(22) Filed 1978-01-16
(45) Issued 1981-01-13
Expired 1998-01-20

Abandonment History

There is no abandonment history.

Payment History

Fee Type Anniversary Year Due Date Amount Paid Paid Date
Application Fee $0.00 1978-01-16
Owners on Record

Note: Records showing the ownership history in alphabetical order.

Current Owners on Record
KLEIN, MAX
Past Owners on Record
None
Past Owners that do not appear in the "Owners on Record" listing will appear in other documentation within the application.
Documents

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Document
Description 
Date
(yyyy-mm-dd) 
Number of pages   Size of Image (KB) 
Drawings 1994-03-04 9 1,962
Claims 1994-03-04 7 355
Abstract 1994-03-04 1 58
Cover Page 1994-03-04 1 25
Description 1994-03-04 21 1,340