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拉伸硬化在炭黑填充橡膠加工中的重要性性能方面:炭黑作為橡膠的補(bǔ)強(qiáng)劑,提高模量,斷裂強(qiáng)度,耐磨性等具有重要作用;加工方面:炭黑對橡膠的熔體剪切粘度,拉伸粘度有重要影響,因此對加工行為有重要影響;不同種類的炭黑具有不同的性質(zhì),如比表面積,結(jié)構(gòu)性等,對橡膠的影響各不相同,因此,需要 炭黑對拉伸性能的影響.炭黑生產(chǎn)工藝及其性質(zhì)炭黑的結(jié)構(gòu)性炭黑的結(jié)構(gòu)性炭黑的結(jié)構(gòu)性是指炭黑粒子連接成長鏈并熔結(jié)在一起而成為三度空間的結(jié)構(gòu),這種體在制造過程中由粒子與粒子間熔合在一起的,這些體(一次結(jié)構(gòu))也可形成疏松的締合物或者稱“二次結(jié)構(gòu)”,他們很容易破壞,故稱暫時(shí)結(jié)構(gòu)。炭黑結(jié)構(gòu)越高,膠料的粘度、定伸應(yīng)力及硬度就會增加,加工性能改善。炭黑的結(jié)構(gòu)性炭黑用量對丁苯橡膠拉伸流動的影響圖(a)炭黑用量增加,拉伸粘度升高,在較低的伸長率下斷裂。圖(b)拉伸粘度隨炭黑用量減小和拉伸速率增大而降低,同時(shí)隨拉伸速率增大,不同炭黑用量的膠料之間,其粘度差別縮小,這與炭黑用量對剪切粘度的影響所得結(jié)果相似。這可能與在高應(yīng)變速率下炭黑網(wǎng)絡(luò)受破壞有關(guān)。炭黑對丁苯橡膠拉伸硬化的影響從圖可見,該曲線與聚乙烯、聚苯乙烯熔體的拉伸流動曲線有區(qū)別,即使在最低的=
1.8×10-4s-1也沒有穩(wěn)態(tài)粘度的趨勢,反而持續(xù)上升,這是拉伸硬化的結(jié)果。不存在穩(wěn)態(tài)粘度,橡膠在外力拉伸作用下發(fā)生結(jié)晶,導(dǎo)致拉伸粘度提高.在炭黑用量、結(jié)構(gòu)性相同的條件下,隨著炭黑表面積增大(N234
>N347
>N351>N550),拉伸粘度增大。在炭黑用量相同,表面積相近的條件下,隨著炭黑結(jié)構(gòu)性增高(N347>N330>N326),拉伸粘度有所提高,但流動曲線形狀不變。炭黑表面積和結(jié)構(gòu)性對丁苯橡膠拉伸流動的影響從上述結(jié)果可見,表面積大的炭黑,其膠料在拉伸流動過程中易產(chǎn)生我們需要的應(yīng)變硬化效應(yīng);而結(jié)構(gòu)性的改變,對應(yīng)變硬化效應(yīng)影響很小。據(jù)此,
等建議,‘采用結(jié)構(gòu)性較低而表面積較大的炭黑(如低拉伸中超耐磨爐黑N231)較好。因?yàn)榻Y(jié)構(gòu)性低,有效體積較小,剪切粘度較低,而表面積較大(粒徑小)則拉伸應(yīng)變硬化效應(yīng)較強(qiáng)。這樣的混煉膠對某些加工過程有利.含N330和N23l的丁苯混煉膠與含N330的天然橡膠的拉伸流動曲線當(dāng)伸長率為300%(即e=1.4)時(shí),含
N23l的丁苯混煉膠的應(yīng)力比含N330的高30%,可見N231較好,這是因?yàn)镹23l的表面積比N330的大。在室溫條件下,天然橡膠混煉膠比丁苯橡膠混煉膠有高得多的扯斷應(yīng)
(5000kPa)
和扯斷伸長率(e=2.4)。天然膠料在室溫條件下當(dāng)伸長率超過
300%時(shí),其應(yīng)力—應(yīng)變曲線陡然上升,這是應(yīng)變結(jié)晶的結(jié)果,而100oC時(shí)是沒有強(qiáng)烈應(yīng)變硬化效應(yīng)的。中島認(rèn)為,對于炭黑與橡膠之間的混煉,希望產(chǎn)生應(yīng)變硬化,以便分
散。為此,耍提高密煉機(jī)轉(zhuǎn)子的轉(zhuǎn)速,并且轉(zhuǎn)子凸棱與室壁之間的間隙要小些,采用低溫或分段混煉。粒子團(tuán)聚體在混煉時(shí)所受應(yīng)力的分析,基體應(yīng)變硬化有利于將應(yīng)力傳遞給粒子團(tuán)
聚體,使之解團(tuán)聚,從而提高分散性。通過對炭黑/橡膠拉伸流動行為的研究得到以下結(jié)論炭黑類型方面:選用結(jié)構(gòu)性較低而表面積較大加工方面:提高密煉機(jī)轉(zhuǎn)子的轉(zhuǎn)速,減少轉(zhuǎn)子凸棱與室壁之間的間隙,低溫或分段混煉;目的都是降低剪切黏度以降低加工能耗,同時(shí)提高拉伸黏度改善分散效果提高加工效率。拉伸法Stretching
method)紡絲法(Spinning)收縮流法(Converging
flow
method)毛細(xì)管斷裂(Capillary
break
up)駐點(diǎn)流(Stagnation
flow
method)拉伸流變行為的研究方法Stretching
methodStretching
techniquesA
Filament Stretching
ExtensionalRheometer
is
used
to measure
thetransient
extensional
viscosity
of
fluidswith
varying
polymerconcentrations.The
diameter
of
the
stretching
filamentis
monitored
using
a
planar
LASERdevice
allowing
a
computer-ontrolledmotor
to
maintain
a
constant
extensionrate
acting
on
the
fluid.An
extremely
sensitive
force
transduceris
attached
to
the
upper
fluid
platesample
holders,
and
is
used
to
measurethe
force
acting
on
the
filament.Advantages:1.
The
process
allowsthe
extensionalviscosity
to
be
measured in
anearly
shear-
free
flow.2.
Experiments
can
be
run
at
a
variety
ofextension
rates
and
can
reach
relativelylarge
Hencky
strainsStretching
techniques(1)恒拉伸速率測定法,即給定e
,測de
。例如Ide—WhiteextensionaI,測單絲,單絲長約21.5cm,其一端由夾持器夾緊,另一端固定在卷繞
Roller上,并置于硅油浴槽內(nèi),用加熱裝置將絲條熔化,卷繞Roller以恒速轉(zhuǎn)動將絲牽引,熔體張力記錄在記錄儀上,主要用于測定膠料的拉伸粘度。恒拉伸速率測定法,即給定,測e。恒拉伸應(yīng)力測定法,即給定e,測。這要求外加拉力隨拉仲斷面積的減少而自動減小。..Trouton
ratioextensional
viscositythe
shear
viscosityTo
describe
strain
hardeningThe
material
initially
look
like
a
Newtonian
sample,
then
look
more
andmore
elastic
as
the
polymer
chains
begin
to
align
and
stretch
out
in
theflow.
Termed
"strain
hardening,"
the
extensional
viscosity
will
begin
toincrease.
The
extensional
viscosity
isoften
non-dimensionalized
withthe
shear
viscosity.
This
ratio
is
called
the
Trouton
Ratio
.
For
aNewtonian
fluid,
the
Trouton
ratio
Tr=3.絲條半徑保持不變Tr=1000Tr=3As
the
plot
shows
below,
the
non-Newtonian
fluidinitially
reaches
a
Tr=3,
then
increases
by
3orders
of
magnitude.
After
the
deformation
halts,
the
polymer
chains
relax,
cause
the
stressand
hence
the
Trouton
ratio
to
decrease.
Because
the
material
has
strain-hardened,
thefilament
radius
remains
constant
for
several
seconds
after
cessation
of
stretching.恒應(yīng)力法測定法,即給定e,
測。這要求外加拉力隨拉伸斷面積的減少而自動減小。通過光學(xué)裝置測量樣品的橫截面積,自動降低拉伸應(yīng)力(2)
恒拉伸應(yīng)力.eA(t)
(t)
F
(t)
const用旋轉(zhuǎn)流變儀實(shí)現(xiàn)拉伸流動的測量Fiber
Spinning:
Spinning
Viscosity1.
The
principle
of
the
fibre
spinning
method
is
to
measurethe
force
required
when
stretching
an
extrudate
underspecified
haul-off
conditions.
From
the
response
of
thematerial
to
the
stretching
deformation
and
the
forcemeasured,
approximate
extensional
viscosities
can
bedetermined.
As
indicated
in
anresults
obtained
are
dependent
onoperation
of
the
instrument
and
subsequentparison
thethe
preciseysis
ofthe
raw
data.
Furthermore,
the
"melt
strength"
can
bedetermined
-
a
measure
of
the
extensional
response
ofthe
material
at
high
strains
-
and
is
suitable
for
qualitycontrol
type
applications.2.
Data
derived
from
the
draw-down
of
the
extrudate
in
amelt
flow
rate
test
has
recently
beencorrelatedsuccessfully
with
tensile
stress
growth
coefficient
dataobtained
from
stretching
measurements.
The
benefitsof
this
simple
technique
have
been
demonstrated
in
anindustrial
case
study
indicating
that
it
has
considerablepotential
for
quality
control
type
applications.The
Rheotensmeasures
theproperties of
polymerdrawing
a vertical
meltextensionalmelts
bystrandonstant
pull-off
speedor
with
a
linear
or
exponentiallyaccelerating
velocity.The
Rheotens
measures
the
forcesneeded
to
elongate
the
strand
andcalculates
elongational
stress,
drawratios,
rate
of
elongation
andelongational
viscosity.The
polymer
melt
is
drawn
downward
from
the
die
by
a
pair
of
counter
rotating
wheelsmounted
on
a
balance
beam.
The
tensile
force
applied
on
the
strand
during
extension
isplotted
against
time
or
velocity
of
the
wheels.
The
velocity
of
the
wheels
accelerates
until
thepolymer
strand
breaks
and
the
force
at
which
the
polymer
melt
breaks
is
defined
as
themelt
strength.Fiber
Spinning:G?ttfert
melt
strength
(熔體強(qiáng)度)tester拉伸流變測試中易出現(xiàn)的問題Converging
flow
methods:用類似于毛細(xì)管流變儀(剪切流變儀)測量拉伸流動Extensional
viscosity
might
be
obtained
from
themeasurement
of
pressure
drop
and
flow
rate
in
a
convergingflow.實(shí)驗(yàn)簡單,數(shù)據(jù)處理麻煩,不能研究拉伸硬化行為.用零長毛細(xì)管流變儀測量拉伸流動兩種聚合物兩種聚合物加工行為有很大差異。拉伸粘度的測量以上介紹的是聚合物熔體或橡膠的拉伸流變實(shí)驗(yàn),聚合物溶液,懸浮液,膠體的拉伸流變行為較難研究Capillary
Breakup
RheometryCapillary
BreakupA
MFR
that
can
be
used
toreadily
differentiate
between
theresponseof
different
fluid
formulations.The
device
relies
on
a
detailed
observation
of
the
rate
of
extensional
thinning
of
a
Newtonian
or
aviscoelastic
fluid
filament
and
provides
a
direct
measurement
of
the
ultimate
time
to
break-up
of
thefluid
filament.Measurements
are
performed
in
a
controlled
temperatureand
environmental
conditions.We
consider
four
different
classes
of
entangled
polymer
liquids
that
are
of
importance
commerciallyincluding(i)pressure
sensitiveadhesives(PSA,壓敏膠),(ii)branched
and
linear
polymer
melts,(iii)concentrated
polymer
solutions
and(iv)aqueous
solutions
of
associating
polymers
such
as
HEUR(Hydrophobically
modified
urethane-ethoxylate).We
observed
that
the
breakup
dynamics
in
theseliquids
depend
on
the
extensional
viscosity,on
molecular
parameters
such
as
the
chain-length,entanglement
density
or
degree
of
chain
branching,and
on
external
factors
such
as
solvent
volatility.Varying
these
factors
changes
the
dominant
time
scales
in
the
extensional
flow.For
example,
PSA
are
elastically
stabilized
against
break
up
and
are
'tacky'
if
the
solventevaporation
rate
-1evap=
h/R0
(where
h
is
the
mass
transfer
coefficient
for
thesolvent
and
R0
is
the
initialradiusof
the
filament)
is
significantly
larger
than
the
stress
relaxation
ra
-1whereas
they
are
'non-tacky'and
undergo
capillary
breakup
if
theevaporation
rate
is
much
slower
than
thecapillary
necking
rate
-1neck
0
0
0=
/
R
)(
where
is
the
surface
tension
and
is
the
zero
shear
viscosity).In
the
case
of
associativepolymers,
the
breakup
mechanism
also
depends
on
the
concentration
of
micelles
and
the
ionicsurfactant
strength.Elasto-Capillary
Thining
in
a
Microfilament
Rheometer,Test
Fluid:
Glycerinentov
glycerin.avi(1.6
MB)Elasto-Capillary
Thiningin
a
MicrofilamentRheometer,
Test
Fluid:
HEUR
(Associative
Polymer)entov
heur.avi(1.6MB)Elasto-Capillary
Thining
in
a
Microfilament
Rheometer,
Test
Fluid:
Pressure
Sensitive
Adhesive
(PSA)entov
psa.avi(2.3
MB)Stretching
and
Breakup
of
Polymeric
Liquids
in
a
MicrofilamentRheometer
(MFR)Polystryene
with
Clay
Particles0%
Clay3%
Clay10%
ClayApplication
in
Food
industry
---
Dannon
YogurtOpen
Stretch
BreakThe
difference
in
fluid
property
of
regular
and
non-fat
yogurt
is
evaluated
to
understand
the
effect
of
milkfat
suspended
in
yogurt.Example:Optimization
of
the
filling
process
of
shampoo
sachetsThe
HAAKE
CaBER
1
extensional
rheometer
iscapable
of
an
easy-tohandle
and
quick
way
ofdistinguishing
between
different
shampoos
and
ofpredicting
filament
life
times
for
production
andquality
control.
Shampoos
3
-
5
will
need
to
bereformulated
to
solve
the
serious
filling
problems.In
this
way
it
is
possible
to
optimize
the
quality
ofthe
shampoos
and
the
production
process.With
certain
shampoo
formulations,
‘strings’
of
shampoo
are
formed
when
filling
the
sachets,
whichcauses
the
product
to
spill
across
the
seam
area.
As
a
consequence,
the
sachet
cannot
be
properlysealed.
This
failure
is
expensive
as
it
will
result
in
the
disposal
of
many
improperly
sealed
sachets.(剝離)The
experiment
shown
was
done
using
apolystyreneBoger
fluid
('SM3')
at
De=43.4.
Theendplate
diameteris
5mm
and
the
initialendplateseparation
is
0.1mm.研究peeling的意義對粘合劑的性質(zhì)進(jìn)行研究:
研究剝離現(xiàn)象;必須避免拉伸實(shí)驗(yàn)中出現(xiàn)類似的問題:一旦出現(xiàn),無法判斷實(shí)際受力面積.The
buckling
instability,
which
occurs
on
the
platesof
the
lament
stretching
device,
can
seriouslycompromise
the
utility
of
the
device
unless
measuresare
taken
to
prevent
it.Development
of
the
buckling
instability,
after
Spiegelberg
and
McKinley'sgure.Thedash-dot
curves
represent
streamlines.Fluid
is
drained
from
the
'foot'
of
the
column
to
feed
the
extending
column.The
reservoir
next
to
the
column
is
depleted,
at
which
time
the
foot
begins
tobreak
up
into
fibrils.
As
the
reservoir
at
the
foot
of
the
column
is
drained,
thestreamlines e
increasingly
more
c
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