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irradiation of dissolving pulp by electron beams - Lenzing

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6.5<br />

IRRADIATION OF DISSOLVING PULP BY ELECTRON BEAMS<br />

Different <strong>dissolving</strong> <strong>pulp</strong>s were treated <strong>by</strong><br />

<strong>electron</strong> <strong>beams</strong>. The dose-DP relation was<br />

invesugated <strong>by</strong> different accelerators. The<br />

Parameters <strong>of</strong> the Sakurada equation differ<br />

from <strong>pulp</strong> to <strong>pulp</strong>.<br />

As a result <strong>of</strong> our examinations the DP<br />

distribution inside a mini bale Shows a great<br />

inhomogeneity <strong>of</strong> the viscosity. The strongest<br />

degradation was observed at the edge<br />

positions <strong>of</strong> Single <strong>pulp</strong> sheets in a Penetration<br />

depth <strong>of</strong> 30 sheets. The uniformity <strong>of</strong> the DP<br />

distribution, measured <strong>by</strong> GPC in<br />

LiWDMAc, <strong>of</strong> the alkali cellulose (AC) before<br />

xanthation was compared to conventional AC<br />

for different <strong>pulp</strong>s. In all these examinations<br />

no significant differentes between pre-aged<br />

and irradiated <strong>pulp</strong> was observed.<br />

The Phase transition from cellulose 1 to<br />

cellulose 11 depending on temperature and<br />

steeping lye concentration, measured <strong>by</strong> FT-<br />

IR-spectroscopy, takes place in the same<br />

range <strong>of</strong> NaOH-concentration for irradiated<br />

and untreated <strong>pulp</strong> samples.<br />

The influence <strong>of</strong> CS2, cellulose content, and<br />

alkali ratio (AR) was examined using<br />

hemicellulose-free steeping lye in Order to<br />

check the influence <strong>of</strong> <strong>irradiation</strong> on viscose<br />

quality. In case <strong>of</strong> irradiated <strong>pulp</strong> the steeping<br />

lye concentration was 16%. In these trials the<br />

Introduction<br />

There has been some correspondence among<br />

several research groups claiming that <strong>irradiation</strong><br />

<strong>of</strong> <strong>dissolving</strong> <strong>pulp</strong>s Prior to viscose production<br />

could be beneficial in several ways:<br />

. the caustic requirement for steeping will be<br />

reduced because the conversion to the cellulose<br />

11 statle could be achieved at a remarkably lower<br />

caustic soda concentration;<br />

l the degree <strong>of</strong> polymerization tan be easily<br />

adjusted and, thus, the aging step after<br />

alkalization could be omitted;<br />

G. Kraft, N. Schelosky<br />

<strong>Lenzing</strong> AG, A - 4860 <strong>Lenzing</strong>, Austria<br />

viscosity <strong>of</strong> AC before xanthation was the<br />

same for both types <strong>of</strong> <strong>pulp</strong>. In a wide range<br />

<strong>of</strong> CIS2 input (36% to 26% calculated on a-<br />

cellulose) and AR from 0.60 down to 0.47 no<br />

differente between the irradiated samples and<br />

the conventional pre-aged <strong>pulp</strong> was observed.<br />

Increasing the cellulose content up to 15.7%<br />

(relaLtive to Standard), no benefit was observed<br />

<strong>by</strong> using irradiated <strong>pulp</strong>. Only in case <strong>of</strong> a<br />

drastic reduction <strong>of</strong> the input chemicals down<br />

to 22% CS2 and AR 0.5 the irradiated <strong>pulp</strong><br />

gives a better viscose quality than the<br />

reference <strong>pulp</strong> under the same conditions. The<br />

same trials performed in the 2kg lab plant did<br />

not show any statistical differente between<br />

irraldiated and conventional pre-aged <strong>pulp</strong>.<br />

Reg:arding the fibre quality there was no<br />

differente between irradiated and<br />

conventional pre-aged <strong>pulp</strong> samples in terms<br />

<strong>of</strong> elongation and tenacity. The fibres from the<br />

irraldiated <strong>pulp</strong> showed a higher degree <strong>of</strong><br />

yellowing. The formation <strong>of</strong> H2S was not<br />

increased according to <strong>by</strong>-product analyses.<br />

The frequently published results <strong>of</strong> drastically<br />

bettier viscose quality <strong>by</strong> using irradiated <strong>pulp</strong><br />

could not be confirmed in our study.<br />

Keywords: viscose, <strong>irradiation</strong>, <strong>electron</strong> beam<br />

l the xanthation will occur with substantially<br />

reduced carbon disulfide input and, because <strong>of</strong> a<br />

higber reactivity <strong>of</strong> <strong>pulp</strong> degradation, still give a<br />

viscose with good filterability;<br />

l less CS*-derived <strong>by</strong>product formation will<br />

result in a reduced H2S-formation.<br />

The objective <strong>of</strong> this study was the evaluation <strong>of</strong><br />

the potential <strong>of</strong> <strong>electron</strong> treatment <strong>of</strong> <strong>dissolving</strong><br />

<strong>pulp</strong>s with a special focus on the feasibility <strong>of</strong> a<br />

drastic reduction <strong>of</strong> CS* and NaOH charges in<br />

the case <strong>of</strong> Solucell <strong>dissolving</strong> <strong>pulp</strong>.


Economical considerations. . The price <strong>of</strong><br />

irradiated <strong>of</strong> <strong>pulp</strong> is composed <strong>of</strong> high costs <strong>of</strong><br />

botlh investment and Operation, the latter one<br />

mainly depending on expenses for electric<br />

power. From this Point <strong>of</strong> view, the <strong>irradiation</strong> <strong>of</strong><br />

<strong>pulp</strong> would become an economically interesting<br />

innovation only if it is possible to carry out the<br />

viscose process with drastically reduced input<br />

chemicals (22% CS*, AR: 0.5) without any<br />

impairment <strong>of</strong> the fiber quality.<br />

Experimental<br />

For the experiments at lab plant and Pilot plant,<br />

50 sheets (isostack) <strong>of</strong> Solucell 450 were<br />

irraldiated at STUDER AG with a 1OMeV<br />

Rhodotron TT300 accelerator built <strong>by</strong> IBA.<br />

The viscose quality was evaluated <strong>by</strong> PVC and<br />

KWP filter value (constant pressure) and particle<br />

i<br />

-<br />

I<br />

Irradiated Pulp fl2 kCy)<br />

BA: 10 MeV<br />

homogeneous nking <strong>of</strong> prllp chips<br />

Steeping lye concentratioe: 16%<br />

/ Viscose <strong>of</strong> the sanuz composition was prepared for irradiated and<br />

-.<br />

LAB PLANT<br />

Viscose Quality<br />

Viscose Rheology I<br />

- -----.~-~~--~ _-_- - - ---~~_<br />

66<br />

count. The viscose was also characterized <strong>by</strong><br />

rheological investigations and analysis <strong>of</strong><br />

<strong>by</strong>products, see Table 1 and Figure 1.<br />

No optimization <strong>of</strong> spinning conditions was done<br />

for these experiments.<br />

Table 1. Viscose composition for the experiments at lab<br />

plant and Pilot plant.<br />

Plant CS2 (%) AR Ce11 conc.<br />

Lab 36 0.6<br />

Lab 32 0.6<br />

Lab’ 28 0.55<br />

Lab 26 0.5<br />

Lab 22 0.5<br />

Lab 28 0.55<br />

Lab<br />

Pilot<br />

Figure 1. Experimental setup.<br />

--<br />

28<br />

22<br />

0.475<br />

0.5<br />

Standard<br />

Standard<br />

Standard<br />

Standard<br />

Standard<br />

Standard +<br />

15.6%<br />

Standard +<br />

15.6%<br />

Standard<br />

Con~entionai Ageiag<br />

Sieeping lye co~~~~~rati~a Standard<br />

-.--I--~ --.x .._““


Viscosity [ml/g]<br />

290 1 without aftertreatment<br />

260-<br />

Irrxhatwn Doiage: 12 kGy<br />

250L 0 - I - I - I - . . 1<br />

0 10 20 30 40 50<br />

Sheet Numher<br />

Figure :t. Intrinsic viscosity distribution within one mini<br />

bale: homogeneity <strong>of</strong> <strong>irradiation</strong> at a dosage <strong>of</strong> 12 kGy.<br />

In case <strong>of</strong> irradiated <strong>pulp</strong> the hemicellulose<br />

concentration in press lye was higher than in the<br />

conventional process (2.25 g/l versus 1.48 g/l).<br />

67<br />

Ball J?zLZ <strong>of</strong> viscose. As published, the ball fall <strong>of</strong><br />

viscose made from irradiated <strong>pulp</strong> should be<br />

lowel than that <strong>of</strong> viscose made from<br />

conventionally pre-aged <strong>pulp</strong>. Thus, it should be<br />

possible to increase the production capacity <strong>by</strong><br />

using a higher content <strong>of</strong> irradiated cellulose<br />

under retention <strong>of</strong> the same ball fall <strong>of</strong> the<br />

viscose as before. However, only at high<br />

celluliose content (115.6% <strong>of</strong> Standard) and very<br />

low alkali content a lower ball fall seemed to<br />

result from the use <strong>of</strong> irradiated <strong>pulp</strong> (Figure 3).<br />

There is no benefit in ball fall <strong>by</strong> using irradiated<br />

Pulp=<br />

Polytlispersity <strong>of</strong> AC. No differente regarding<br />

polydispersity between aging and <strong>electron</strong> beam<br />

treatment could be observed in the respective<br />

viscosity range (Figure 4).<br />

100% [ca 100% [CS 100% [ca 100% 100% 115.6% [CS2z 115.6% [cs2:<br />

360/0; ARZ 0.q 32v4 AR: 0.6) 280/0; AR: o.5.q [oi2:26%, AR [cs2:22%, AR BS, AR 0.55j 28%, AR:<br />

O-Tl Wl 0.47Sj<br />

2.6<br />

Figure 3. Ball fall <strong>of</strong> various compositions <strong>of</strong> viscose prepared from irradiated and pre-aged <strong>pulp</strong>;<br />

lab-plant trials. Ball fall corrected to target cellulose concentration.<br />

1.6<br />

400 300<br />

Intrinsic viscosity [mYg]<br />

Figure 4. Polydispersity vs. intrinsic viscosity <strong>of</strong> AC.


68<br />

Phase transition Cellulose I - Cellulose II. The networks under extreme conditions (CS2<br />

pha.se transition takes place in the same range <strong>of</strong> reduction, increase in cellulose) than reference<br />

Na0H: concentration for irradiated and untreated <strong>pulp</strong>. It has a higher potential for savings from<br />

<strong>pulp</strong> s amples . this Point <strong>of</strong> view.<br />

Rheology <strong>of</strong> Viscose Spinning Dope. Under Viscose from irradiated <strong>pulp</strong> under saving<br />

Standard conditions, irradiated <strong>pulp</strong> yields conditions is rheologically worse than one from<br />

rheologically worse viscose than reference <strong>pulp</strong>. reference <strong>pulp</strong> under Standard conditions.<br />

Under conditions <strong>of</strong> CS2 reduction and increase Quality <strong>of</strong> viscose. The <strong>of</strong>ten published results <strong>of</strong><br />

in cellulose, irradiated <strong>pulp</strong> yields rheologically drastically better viscose quality <strong>by</strong> using<br />

better viscose than reference <strong>pulp</strong>. Irradiated irradiated <strong>pulp</strong> could not be confirmed in our<br />

<strong>pulp</strong> seems to have a lower tendency <strong>of</strong> forming study <strong>of</strong> Solucell450.<br />

800<br />

700<br />

0 600<br />

L 500<br />

2<br />

P 400<br />

5 300<br />

-z<br />

200<br />

100<br />

0<br />

HFilter value [PVC] q Total particle volume[ppm]<br />

Fignre 5. Viscose quality. Trials made at lab plant with Standard cellulose concentration (average +/- 95,4% conf. interval).<br />

Filter value (higher is better) and total particle content at Standard cellulose content in viscose [CS,%/AR].<br />

IFilter value [PVC] q Total particle volume [ppm]<br />

pre aged - CS2: 28 % ; Irradiated - CS2: 28%; pre aged - CS2: 28%; Irradiated -CS2: 28%;<br />

AR: 0.55 AR: 0.55 AR: 0.475 AR: 0.475<br />

Figure 6. Viscose quality. Trials made at lab plant with Standard cellullose concentration (average +/- 95,4% conf. interval).<br />

Filter value (higher is better) and total particle content at 15.6% higher cellulose content in viscose [C,‘$%/AR].<br />

20<br />

18


In a wide range <strong>of</strong> CS2 input (36% to 26%<br />

calculated on a-cellulose) and AR from 0.60<br />

down to 0.47 no significant differente in viscose<br />

quality between the irradiated samples and the<br />

conventionally pre-aged <strong>pulp</strong> was observed.<br />

Upon increase <strong>of</strong> the cellulose content up to<br />

115.7% <strong>of</strong> Standard, no benefit was observed <strong>by</strong><br />

using irradiated <strong>pulp</strong>. Only in case <strong>of</strong> a drastic<br />

reduct-ion <strong>of</strong> the input chemicals down to 22%<br />

CS; and AR 0.5 the irradiated <strong>pulp</strong> gave a better<br />

viscose quality than the reference <strong>pulp</strong> under the<br />

same conditions (Figures 5 and 6). The same<br />

trials iperformed at the 2kg Pilot plant did not<br />

show any statistical differente between irradiated<br />

and conventionally pre-aged <strong>pulp</strong> (Table 2).<br />

B~JW&KLS. There seems to be a slight tendency<br />

to lower trithiocarbonate formation in the viscose<br />

made from the irradiated <strong>pulp</strong>.<br />

Fibre properties. Viscose <strong>of</strong> reduced CS2 content<br />

showed good spinning properties, the spinning<br />

conditions were not optimized. Tenacity and<br />

elonga.tion were not significantly influenced <strong>by</strong><br />

the use <strong>of</strong> irradiated <strong>pulp</strong>, the tendency is slightly<br />

better for aged <strong>pulp</strong>.<br />

Tenacity and elongation were significantly<br />

impaired <strong>by</strong> the reduction <strong>of</strong> CS2 Charge using<br />

Standard spinning conditions (Figure 7).<br />

69<br />

Brightness and yellowing <strong>of</strong> fibres were<br />

nega.tively influenced <strong>by</strong> both the use <strong>of</strong><br />

irrad.iated <strong>pulp</strong> and the reduction <strong>of</strong> CS2 Charge<br />

(Figure 8).<br />

Table 2. Results <strong>of</strong> trials at a Pilot plant [averagehange].<br />

conventional irradiated<br />

CS2 l%l Std. 22 Std. 22<br />

Alkali ratio Std. 0.5 Std. 0.5<br />

unfiltered viscose<br />

Filter value, PVC 452 252 393 1156 335 /IO3<br />

125 1167<br />

Filter value, 77 144 230 117169 123 139<br />

KWP 1230<br />

Total particle 12.4 28.3 18.6/17.1 22.1 /3.2<br />

volume [ppm] 17.8 140.0<br />

Time for 43 78 60 70<br />

filtration, min.<br />

viscose spinning dope<br />

Filter value, PVC 528 233 528 134 439 132<br />

/186 /121<br />

Filter value, 26112 47116 40115 43 145<br />

KWP<br />

Total particle 1.2 2.5 1.4 IO.5 1.3 IO.3<br />

volume [ppm] IO.6 11.8<br />

Ball fall [sec] 49 83 60 93<br />

Ripening ind., “H 14.7 6.5 15.9 7.8<br />

aged Standard irradiated aged 22% CS2; AR irradiated 22%<br />

Standard 0.5 CS2; AR 0.5<br />

Figure 7. Tenacity and elongation <strong>of</strong> fibers at standarcl spinning conditions (Pilot plant trials).


1<br />

-<br />

&Q<br />

75<br />

E 70<br />

lQ5<br />

-E<br />

60<br />

55<br />

50<br />

45<br />

aged standard irradiated aged 22% CS2; AR irradiated 22%<br />

Standarcl 0.5 (32; AR 0.5<br />

Figve 8. Brightness <strong>of</strong> unbleached fibers at standard spinning conditions (pilot plant hi&).<br />

Conclusion References<br />

Electron beam treatment <strong>of</strong> <strong>pulp</strong> slightly<br />

improves viscose filterability at a very low level<br />

<strong>of</strong> CS2 charge (lab plant).<br />

However, this improvement is not liirge enough<br />

to justify the additional costs <strong>of</strong> <strong>electron</strong> beam<br />

treatment. The higher hemicellulose conteat in<br />

the steeping lye and the enhanced yellowing <strong>of</strong><br />

the fibers are further arguments against <strong>electron</strong><br />

beam treatment <strong>of</strong> <strong>dissolving</strong> <strong>pulp</strong>.<br />

The <strong>of</strong>ten published results <strong>of</strong> drastically better<br />

viscose quality <strong>by</strong> using irradiated <strong>pulp</strong> could not<br />

be confirmed in our study <strong>of</strong> Solucell450.<br />

[ 11 Fisher, K.; Goldberg, W.; Wilke, M. Lanz.<br />

BeE 1985,59,32.<br />

[Z] Rajagopal, S. et al. "Enhancement <strong>of</strong><br />

Cellulose Reactivity in Viscose Production<br />

Using Electron F'rocessing Technology"'<br />

Viscose Chemistry Seminat, Stockholm,<br />

1994.<br />

[3] Rajagopal, S. PETAS Seminar, Hamburg,<br />

1995.<br />

[4] Rajagopal, S. Cellulosic Man-Made Fibre<br />

Summit, Singapore, 1997.<br />

[5] Stavtsov, A.; Cassel, A. Cellulosic Man-<br />

Made Fibre Sumit, Singapore, 1997.<br />

[6]<br />

Schleicher, H.; Bomneister, B.; Voges, M.<br />

Cellulosic -Made Fibre Summit,<br />

Singapore, 1997.

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