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Laboratory Scale Nitration of Cellulose as a Cost Effective Risk Mitigation Tool for the Production of Nitrocellulose at Radford Army Ammunition Plant
Dr. Benjamin R. Vaughan, Zach Higginbotham, Dr. Anand Mangalam, Leslie Ben’Ous, Peter Bonnett
May 13,2009
Laboratory Scale Nitration of Cellulose as a Cost Effective Risk Mitigation Tool for the Production of Nitrocellulose at Radford Army Ammunition Plant
Dr. Benjamin R. Vaughan, Zach Higginbotham, Dr. Anand Mangalam, Leslie Ben’Ous, Peter BonnettMay 13,2009
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OUTLINE
NITROCELLULOSE MANUFACTURING AT RFAAP
LAB SCALE NITRATION / STABILIZATION
PART I: LAB SCALE NITRATION STUDY
• MIXED ACID COMPOSITION
• KEY INPUT VARIABLES – EFFECTS
PART II: CELLULOSE SOURCE STUDY
• KRAFT VS SULFITE PULP
• ACADEMIC WORK
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ACID BOILING
POACHING& BLENDING
ACID
NITRATION
CELLULOSE
REFINING
ANALYSIS
NITROCELLULOSE MFG. 101
OO
O O
O
O
OONO2
O2NO
ONO2
O2NO
O O
O2NOONO2
O2NO ONO2
O2NOONO2
ONO2O2NO
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ACID BOILING
POACHING
NITRATION
CELLULOSE
REFINING
LABSCALE NITRATION
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PART I: NC REACTION CONDITIONS STUDY
1.Demonstrate that laboratory nitration can be used as a tool to aid production with risk mitigation associated with sensitive products
2.Understand how mixed acid composition
and key process input variables (KPIV)
change our
nitrocellulose in terms of:
• % Average Nitrogen
• Acetone solubility, and Ether / Alcohol Solubility
• Processing of NC
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Grade D Water Sensitivity Models
Water sensitivity models developed for Grade D and E nitrocellulose products
AFY09 NC production data fits within lab scale model’s 95% prediction limits for Grade D NC
Process data fits have led the NC technical team to use less water set changes during manufacturing
Lab data shows linear response of %N to water at current process acid composition
Good fit of data to simple model
14.2 14.3 14.4 14.5 14.6 14.7
12.0
12.1
12.2
12.3
12.4
% Water
%N
Resp
onse
%N Response = 18.6145 - 0.446 % Water
S = 0.0285671 R-Sq = 89.7 % R-Sq(adj) = 88.2 %
RegressionLab Scale
95% PI
Grade D NC % Water in Nitrating Acid Sensitivity
Scale ModelProduction
GRADE D WATER SENSITIVITY AT CONSTANT NITRIC ACID CONTENT
12.00
12.05
12.10
12.15
12.20
12.25
12.30
12.35
% WATER IN ACID
% N
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Nitration with various mixed acids
PRODUCTION IS CURRENTLY USING THE MODELS DEVELOPED IN THE LAB TO ADJUST NITRATING ACIDS FOR PRODUCTION OF GRADES D
AND E NITROCELLULOSE
%WATER
%N
ITR
IC
14.714.614.514.414.314.2
75
70
65
60
55
50
45
40
35
30
Grade D Nitrating Acid Sensitivity
% WATER
% N
ITR
IC
14.814.714.614.514.414.3
75
70
65
60
55
50
45
40
35
30
> – – – – – < 10.0
10.0 10.510.5 11.011.0 11.511.5 12.012.0 12.5
12.5
%N
Grade E Nitrating Acid Sensitivity
INCREASING Δ 0.5 % INCREASING Δ 0.5 %
INC
REA
SIN
G Δ
45 %
INC
REA
SIN
G Δ
45 %
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KEY PROCESS INPUT VARIABLES AFFECTING ATK NC
VARIABLE
(NITRATING ACID MAKEUP FIXED)
RESPONSE
AI EAS %N
ACID \
CELLULOSE
TEMP.
TIME
CHIPS OVER FIBERS
Run Time (min) Temp (ºC) A/C Ratio Cellulose %N AI EA %Sol %N AI EA %Sol
1 HIGH LOW HIGH Chips 12.051 0.21 99.70 12.315 0.93 98.932 HIGH HIGH HIGH Fibers 12.038 0.19 99.71 12.251 0.59 98.283 MID MID MID Fibers 11.740 0.59 98.70 12.182 0.22 99.184 LOW HIGH LOW Fibers 11.740 0.91 97.78 12.040 1.16 97.575 HIGH HIGH LOW Chips 11.819 0.10 99.94 12.105 0.07 99.666 HIGH LOW LOW Chips 11.804 2.30 97.78 12.038 4.15 95.467 LOW HIGH HIGH Chips 12.043 1.14 98.65 12.371 0.93 99.148 LOW LOW HIGH Fibers 11.809 1.93 93.71 12.235 2.50 93.729 LOW LOW LOW Chips 11.714 15.68 79.66 11.865 11.94 86.9210 MID MID MID Chips 11.985 0.26 99.74 12.306 0.14 99.80
GRADE E GRADE D
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PART II: CELLULOSE SOURCE STUDY
Answer two Questions:
1.
Is it feasible to make nitrocellulose from Kraft paper? Which pulp candidates look most promising?
2.
Why do similar pulps nitrate so differently? What are the key cellulose characteristics influencing nitration?
•Hemicelluloses content
•Crystallinity
•Fiber wall thickness
•Tree species used
•Sheet Physical Properties
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TWO MAJOR PULPING PROCESSES
SULFATE (KRAFT)
•Basic digestion
•Universal process for recovery of cooking chemicals
•Dominant process
•Cost ~ $ -
0.20 / lb
•Use most types of trees
SULFITE
•Acidic digestion
•Limited recovery of acid gas
•Mills diminishing
•Cost ~ $baseline
•Use limited tree species
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NITRATION QUALITY AND SOLUBILITY
12.2
12.3
12.4
12.5
12.6
12.7
12.8
0.0 0.5 1.0 1.5 2.0 2.5% Acetone Insolubles
% N
itrog
en
SULFITESULFATE
%N (FeSO4) %AI %EAS
SULFITE A 12.68 0.2 99.8SULFITE B 12.28 0.6 98.9SULFITE C 12.23 1.7 97.1SULFITE D 12.53 0.5 99.3SULFITE E 12.55 0.1 99.9SULFITE F 12.29 1.0 98.4SULFITE G 12.71 0.2 99.9SULFITE H 12.34 1.4 97.9SULFATE A 12.57 0.6 99.3SULFATE B 12.62 0.7 99.1SULFATE C 12.37 2.0 97.5SULFATE D 12.54 0.9 98.9SULFATE E 12.61 0.1 99.8SULFATE F 12.68 0.3 99.8
SEVERAL OF THE SULFATE PULPS TESTED TO DATE APPEAR TO HAVE PROPERTIES THAT MEET MILITARY GRADE NC SPECS
% NITROGEN = 12.6 +
0.1% , ACETONE INSOLUBLES < 0.4%
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FIBER QUALITY
10 100 1000
0
2
4
6
8
10
FINES
SULFATE-E SULFITE-A
PER
CEN
T
FIBER LENGTHW
FREE FIBERSSAMPLE >850 um 500 - 849 um 250 - 499 um FINES < 200um
SULFITE A 28% 26% 11% 31%SULFATE E 0 7% 20% 18%
PARTICLES
SULFATE-E IS EASILY SEPARATED INTO
FIBERS AND HAS A LOW PERCENT FINES
(µm)
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WOOD PULP FIBERS
Resin (Extractable) –
can survive the pulping process
Lignin –
(binder) likely removed during the pulping process
Hemicelluloses (polysaccharides) –
can survive pulping process
Alpha Cellulose –
survives pulping process
micro fibrils
Hemicelluloses bind elementary fibrils
elementary fibrils (cellulose)
fiber
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CRYSTALLINITY % AND HEMICELLULOSE %
XRD SULFATE PULP - E
14.798 16.38718.898
22.37
10 15 20 25 30 350
1020304050607080
01020304050607080
10
30
50
70
90
10
30
50
70
90XRD SULFATE - E NITROCELLULOSE
12.699
19.832
10 20 30 40-5
0
5
10
15
-5
0
5
10
15
0
5
10
15
20
0
5
10
15
20
60% CRYSTALLINITY 5% CRYSTALLINITY
SULFITE PULPS SULFATE PULPSAVG HEMICELLULOSES = 5% AVG HEMICELLULOSES = 19%
NEITHER CRYSTALLINITY OR HEMICELLULOSES CONTENT APPEAR TO BE MAJOR FACTORS IN THE NITRATABILITY OF CELLULOSE
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CONFOCAL RAMAN MICROSCOPY
Nitrate Stretches
Ram
an intensity
z
SURFACE
INTERIOR
cellulose fiber
WE ARE COMPARING THE NITRATION LEVEL AT DIFFERENT DEPTHS WITHIN THE FIBER WALL FOR DIFFERENT PULP SAMPLES
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CONCLUSIONS
•WE HAVE BEEN ABLE TO PERFORM NITRATION EXPERIMENTS AT THE LAB SCALE WHICH WOULD HAVE BEEN DIFFICULT, TIME CONSUMING, AND EXTREMELY EXPENSIVE AT THE PRODUCTION SCALE.
•LAB SCALE NITRATION HAS BEEN AN EFFECTIVE METHOD FOR TUNING NITRATION CONDITIONS FOR THE PRODUCTION SCALE PROCESS.
•LAB SCALE NITRATION IS HELPING ATK TO ASSESS FUTURE SOURCES OF CELLULOSE FOR NC PRODUCTION AS WELL AS ANSWERING SOME FUNDAMENTAL QUESTIONS .
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ACKNOWLEGMENTS
We would like to thank PM Joint Services and ARDEC for funding the cellulose source study portion of this research.