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<strong>Multibase</strong> <strong>gun</strong> <strong>propellants</strong><br />

<strong>cont<strong>in</strong>uous</strong> <strong>process</strong> <strong>production</strong><br />

<strong>in</strong> KARLSKOGA<br />

Authors:<br />

Anders HAFSTRAND (EURENCO Bofors)<br />

Jean Louis PAULIN (EURENCO France)


Most of exist<strong>in</strong>g <strong>gun</strong> <strong>propellants</strong> <strong>production</strong> l<strong>in</strong>es use batch <strong>process</strong>es:<br />

• For mix<strong>in</strong>g: by kneader (solvent way) or roll<strong>in</strong>g mill (solventless way)<br />

• For extrusion: by press<br />

Many attempts were made to develop new <strong>process</strong>es aimed at reduc<strong>in</strong>g<br />

capacity and sav<strong>in</strong>g money (labor cost and <strong>in</strong>vestments) “safe, agile and low<br />

cost facility”.<br />

The <strong>cont<strong>in</strong>uous</strong> <strong>process</strong> us<strong>in</strong>g automatic feed<strong>in</strong>g and s<strong>in</strong>gle or tw<strong>in</strong> screw is one<br />

response and it is advisable to select this way for the new <strong>in</strong>vestments.<br />

In this paper we plan to show, for <strong>cont<strong>in</strong>uous</strong> <strong>process</strong>es, NEXPLO and SME<br />

background, the exist<strong>in</strong>g <strong>in</strong>dustrial l<strong>in</strong>es with additional features and the<br />

<strong>in</strong>vestment <strong>in</strong> the new company EURENCO.


SUMMARY<br />

• Karlskoga <strong>in</strong>dustrial l<strong>in</strong>e for the <strong>cont<strong>in</strong>uous</strong> manufacture of:<br />

- solventless double base (DB) <strong>gun</strong> <strong>propellants</strong><br />

- composite (LOVA) <strong>gun</strong> <strong>propellants</strong><br />

• SNPE experience with <strong>cont<strong>in</strong>uous</strong> <strong>process</strong><br />

• Ma<strong>in</strong> products and <strong>production</strong> l<strong>in</strong>es <strong>in</strong> the field of <strong>gun</strong> <strong>propellants</strong><br />

• New <strong>production</strong> l<strong>in</strong>e for solvent multibase <strong>cont<strong>in</strong>uous</strong> <strong>process</strong><br />

• Small scale validation achieved for new <strong>production</strong> <strong>process</strong> phase<br />

• Conclusions and perspectives


KARLSKOGA <strong>in</strong>dustrial l<strong>in</strong>e for the <strong>cont<strong>in</strong>uous</strong><br />

manufacture of solventless DB <strong>gun</strong> propellant<br />

• Concept: → <strong>cont<strong>in</strong>uous</strong> water <strong>process</strong> from wet NC up to propellant gra<strong>in</strong>s<br />

with pelletaz<strong>in</strong>g phase and two s<strong>in</strong>gle screw stages, <strong>in</strong>-l<strong>in</strong>e cutt<strong>in</strong>g and<br />

automatic blend<strong>in</strong>g of either gra<strong>in</strong>s or sticks.<br />

• Innovation <strong>in</strong> <strong>process</strong>: → fully under water <strong>process</strong> with mix<strong>in</strong>g of<br />

<strong>in</strong>termediate products for a very even product.<br />

• Innovation <strong>in</strong> equipment: → conical s<strong>in</strong>gle barrel/screw extruders for auto<br />

feed<strong>in</strong>g and high sheer<strong>in</strong>g work. Ignition led to the separation of the barrel<br />

and max. two days repair.


KARLSKOGA <strong>in</strong>dustrial l<strong>in</strong>e for the <strong>cont<strong>in</strong>uous</strong><br />

manufacture of solventless DB <strong>gun</strong> propellant<br />

NITROGLYCERINE<br />

NITROCELLULOSE<br />

ADDITIVES<br />

MIXING OF RAW MATERIALS IN WATER<br />

PELLETAZING WITH SOLVENT<br />

SINGLE-SCREW EXTRUSION<br />

TO GRANULATE<br />

DRYING OF GRANULATE<br />

SINGLE-SCREW EXTRUSION<br />

TO PROPELLANT<br />

CUTTING<br />

DRYING<br />

GLAZING<br />

BLENDING<br />

SIEVING<br />

PACKING<br />

SOLVENT RECOVERY<br />

TANK<br />

STORAGE<br />

STORAGE


KARLSKOGA <strong>in</strong>dustrial l<strong>in</strong>e for the <strong>cont<strong>in</strong>uous</strong><br />

manufacture of solventless DB <strong>gun</strong> propellant<br />

• Production has been runn<strong>in</strong>g s<strong>in</strong>ce 1977<br />

• Advantages: Safe, <strong>cont<strong>in</strong>uous</strong>, low <strong>production</strong> cost, small lot to lot variation<br />

• Disadvantages: Limited composition possibilities due to the under water <strong>process</strong><br />

• Ma<strong>in</strong> equipment designed <strong>in</strong>-house: tanks, extruders, dryers, cutters<br />

• Over 10.000 tons produced for howitzer (105 & 155) and tank <strong>gun</strong> (105 & 120)<br />

• DB <strong>propellants</strong> with 50-60% NC<br />

and 50-40% NG/<strong>in</strong>ert plasticizer


KARLSKOGA <strong>in</strong>dustrial l<strong>in</strong>e for the <strong>cont<strong>in</strong>uous</strong><br />

manufacture of composite <strong>gun</strong> <strong>propellants</strong><br />

• Concept:→ <strong>cont<strong>in</strong>uous</strong> <strong>process</strong> with automatic feeders for solid filler and<br />

liquids solvents and one tw<strong>in</strong> screw.<br />

→ for higher safety level, filler is first coated with part of b<strong>in</strong>der<br />

for sensitivity decreas<strong>in</strong>g,<br />

• Innovation <strong>in</strong> <strong>process</strong>: → feedstock is only 1.3 or 1.4 class raw materials,<br />

• Innovation <strong>in</strong> equipment: → tw<strong>in</strong> screw mach<strong>in</strong>e with fully computerized<br />

control.


KARLSKOGA <strong>in</strong>dustrial l<strong>in</strong>e for the <strong>cont<strong>in</strong>uous</strong><br />

manufacture of composite <strong>gun</strong> <strong>propellants</strong><br />

SOLVENT<br />

SOLVENT<br />

FILLER (RDX)<br />

BINDER (CAB, NC)<br />

PLASTICIZER (INERT / ENERG.)<br />

DISSOLVING AND PRECIPITATION,<br />

DRYING OF POWDER<br />

TWIN-SCREW EXTRUSION<br />

TO PROPELLANT<br />

CUTTING<br />

DRYING<br />

GLAZING<br />

BLENDING<br />

SIEVING<br />

PACKING<br />

SOLVENT RECOVERY<br />

SOLVENT<br />

SOLVENT<br />

SOLVENT<br />

TREATMENT<br />

STORAGE


Nexplo KARLSKOGA <strong>in</strong>dustrial l<strong>in</strong>e for the <strong>cont<strong>in</strong>uous</strong><br />

manufacture of composite <strong>gun</strong> <strong>propellants</strong><br />

• Production has been runn<strong>in</strong>g s<strong>in</strong>ce 1996<br />

• Advantages: Safe, <strong>cont<strong>in</strong>uous</strong>, low <strong>production</strong> cost, small lot to lot<br />

variation<br />

• Computer <strong>process</strong> control system designed <strong>in</strong> house<br />

• Over 200 tons produced for 40 & 57 mm IM, automotive safety<br />

• M39 / M43 type <strong>propellants</strong> with 50-80% RDX<br />

and 20-50% b<strong>in</strong>der / plasticizer<br />

• The <strong>in</strong>novative and patented precipitation<br />

<strong>process</strong> is licensed to NSWC IH


EURENCO experience with <strong>cont<strong>in</strong>uous</strong> <strong>process</strong><br />

At first, feasibility tests were performed us<strong>in</strong>g tw<strong>in</strong> screw between 1990 and 1993 for<br />

s<strong>in</strong>gle base <strong>propellants</strong>:<br />

• Validation step was reached with successful fir<strong>in</strong>g tests <strong>in</strong> 105 mm <strong>gun</strong>,<br />

• This experience was used <strong>in</strong> design<strong>in</strong>g <strong>in</strong> 1997 the new hunt<strong>in</strong>g s<strong>in</strong>gle base<br />

propellant l<strong>in</strong>e: one mach<strong>in</strong>e D = 120 mm operates at 120 kg/h <strong>in</strong> three shifts.<br />

Additional feasibility tests between 1992 and 2003:<br />

• Industrial scale <strong>in</strong> Angoulême with TSE 120 mm,<br />

• Research scale <strong>in</strong> Le Bouchet with TSE 45 mm,<br />

• Compositions with solvent: double base GB and multibase like M30 type, HUX.<br />

Also dur<strong>in</strong>g the 90’s feasibility tests were performed with composite HTPB <strong>gun</strong><br />

<strong>propellants</strong> for MURAT.<br />

Due to the high qualification cost of exist<strong>in</strong>g <strong>propellants</strong>, many of these projects were<br />

canceled. It will not be the case for new <strong>propellants</strong>, and our new <strong>in</strong>vestments today<br />

are often related to <strong>cont<strong>in</strong>uous</strong> <strong>process</strong>, like <strong>in</strong> Sa<strong>in</strong>t Médard <strong>in</strong> 1996 for <strong>production</strong> of<br />

composite gra<strong>in</strong>s with 3 TSE <strong>in</strong> three shifts for automotive safety.


Ma<strong>in</strong> products and <strong>production</strong> l<strong>in</strong>es <strong>in</strong> the field of <strong>gun</strong> <strong>propellants</strong><br />

The merger between SME Explosives and Propellants and NEXPLO lead to the creation <strong>in</strong><br />

the field of <strong>gun</strong> propellant of the strongest <strong>in</strong>dustrial tool, <strong>in</strong> spite of Angoulême closure.<br />

Blast<strong>in</strong>g oils<br />

Nitrocellulose<br />

Wet paste<br />

Products<br />

S<strong>in</strong>gle base propellant<br />

Solvent multibase propellant<br />

Solventless multibase propellant<br />

Spherical propellant<br />

Extruded impregnated propellant<br />

Composite propellant (LOVA)<br />

Combustible cartridge<br />

Groupe SNPEEURENCO<br />

Angoulême Karlskoga + Vihtavuori Karlskoga+Vihtavuori<br />

Bergerac Bergerac + Vihtavuori Vihtavuori<br />

Angoulême Karlskoga + Karlskoga Vihtavuori + Vihtavuori<br />

Bergerac + Karlskoga Karlskoga + Vihtavuori + Vihtavuori<br />

Angoulême<br />

Sa<strong>in</strong>t Karlskoga Médard (<strong>cont<strong>in</strong>uous</strong> Karlskoga l<strong>in</strong>e) (<strong>cont<strong>in</strong>uous</strong>)<br />

PB ClermontPB<br />

Clermont<br />

Vihtavuori<br />

Karlskoga (<strong>cont<strong>in</strong>uous</strong> Karlskoga l<strong>in</strong>e) (<strong>cont<strong>in</strong>uous</strong>)<br />

Bergerac<br />

Bergerac<br />

NEXPLO<br />

Vihtavuori


New <strong>production</strong> l<strong>in</strong>e for solvent multibase <strong>cont<strong>in</strong>uous</strong> <strong>process</strong><br />

Only one solvent multibase propellant l<strong>in</strong>e was needed, <strong>in</strong> order to be <strong>in</strong> position to<br />

carry on with manufacture of:<br />

• particular high energy double base for French tank <strong>gun</strong> cartridges,<br />

• additional standardized <strong>gun</strong> <strong>propellants</strong> like M26, M30, M31…<br />

Experience from NEXPLO and SME <strong>in</strong> the field of <strong>gun</strong> propellant <strong>production</strong> and<br />

<strong>cont<strong>in</strong>uous</strong> <strong>process</strong> lead to the choice and design of a new <strong>cont<strong>in</strong>uous</strong> l<strong>in</strong>e with an<br />

<strong>in</strong>novative <strong>process</strong> chosen for:<br />

• high safety level,<br />

• low <strong>production</strong> cost level,<br />

• High reproducibility.


New <strong>production</strong> l<strong>in</strong>e for solvent multibase <strong>cont<strong>in</strong>uous</strong> <strong>process</strong><br />

SME experience <strong>in</strong> Angoulême corresponds with four NC/NG mix<strong>in</strong>g<br />

<strong>process</strong> ways and two solvent composition adjustment, mix<strong>in</strong>g,<br />

extrusion ways:<br />

Production scale (up to 1998) spherical gra<strong>in</strong>s <strong>process</strong> → kneader → press<br />

(chosen first for safety)<br />

Production scale (1998 to 2003) premixed paste <strong>process</strong> → kneader → press<br />

(no more spherical <strong>in</strong> the plant)<br />

Feasibility (1993) solventless granules <strong>process</strong> → TSE<br />

Feasibility ( 1999, 2000) direct feed<strong>in</strong>g <strong>process</strong> → TSE


Double base mix<strong>in</strong>g comparison for first step with exist<strong>in</strong>g <strong>process</strong><br />

Process NC<br />

Premixed<br />

paste<br />

Spherical<br />

gra<strong>in</strong>s<br />

Solventless<br />

granules<br />

Direct<br />

feed<strong>in</strong>g<br />

New <strong>production</strong> l<strong>in</strong>e for solvent multibase <strong>cont<strong>in</strong>uous</strong> <strong>process</strong><br />

Dry<br />

Water wet<br />

Water wet<br />

Dry<br />

F<strong>in</strong>al<br />

Product<br />

Solvent paste<br />

Dry gra<strong>in</strong>s<br />

Dry granules<br />

Solvent paste<br />

Batch<br />

quantity<br />

Small<br />

Large<br />

Small<br />

Gelat<strong>in</strong>ized<br />

NC<br />

Yes & no<br />

Yes<br />

Yes<br />

Cont<strong>in</strong>uous Cont<strong>in</strong>uous<br />

Homogen<br />

mix<br />

And for <strong>in</strong>novative <strong>process</strong> based on EURENCO experience<br />

Process NC<br />

Direct way<br />

by<br />

impregnation<br />

Water<br />

wet<br />

F<strong>in</strong>al<br />

Product<br />

Granulates <strong>in</strong><br />

water tank<br />

Batch<br />

quantity<br />

Gelat<strong>in</strong>ized<br />

NC<br />

No<br />

Yes<br />

Yes<br />

Yes<br />

Homogen<br />

mix<br />

Safety Process<br />

-<br />

++<br />

Done twice<br />

+ Easy<br />

+<br />

Easy<br />

Lack<br />

<strong>in</strong> flexibility<br />

Safety Process<br />

≈ 20 tons Partly Yes +++ Easy


New <strong>production</strong> l<strong>in</strong>e for solvent multibase <strong>cont<strong>in</strong>uous</strong> <strong>process</strong><br />

Solvent multibase <strong>in</strong>novative <strong>process</strong><br />

Composition adjustment, mix<strong>in</strong>g and extrusion can be made by tw<strong>in</strong> screw and<br />

automatic feeders because:<br />

• New <strong>in</strong>vestment need gives opportunity for free choice,<br />

• New qualification must be done <strong>in</strong> any case<br />

• This solution provides advantages:<br />

- Lower <strong>in</strong>vestment and <strong>production</strong> costs<br />

- Smaller variations <strong>in</strong> <strong>production</strong> quality<br />

- Smaller quantities <strong>in</strong>side the mach<strong>in</strong>e reduc<strong>in</strong>g the risk zones<br />

- Better logistics and additional possibilities for new <strong>propellants</strong>


New <strong>production</strong> l<strong>in</strong>e for solvent multibase <strong>cont<strong>in</strong>uous</strong> <strong>process</strong><br />

NITROGLYCERINE<br />

NITROCELLULOSE<br />

ADDITIVES<br />

SOLVENTS<br />

FILLERS<br />

SOLVENT MULTIBASE<br />

PROPELLANT PLANT<br />

MIXING OF RAW MATERIALS IN WATER<br />

PELLETAZING IN SOLVENT<br />

SINGLE SCREW EXTRUDING<br />

TO GRANULATE<br />

DRYING OF GRANULATE<br />

TWIN SCREW EXTRUDING<br />

TO PROPELLANT<br />

CUTTING<br />

DRYING<br />

GLAZING<br />

BLENDING<br />

SIEVING<br />

PACKING<br />

SOLVENT RECOVERY<br />

TANK<br />

STORAGE<br />

SOLVENT<br />

RECOVERY<br />

DISTILLATION<br />

STORAGE


New <strong>production</strong> l<strong>in</strong>e for solvent multibase <strong>cont<strong>in</strong>uous</strong> <strong>process</strong><br />

The ma<strong>in</strong> part of <strong>in</strong>vestment will be the tw<strong>in</strong> screw extruder, our proposal is<br />

strenghened by the experience we have together <strong>in</strong> three different knowledge areas:<br />

Technology<br />

Mathematical model<strong>in</strong>g<br />

Instrumentation<br />

• Feed<strong>in</strong>g equipment<br />

• Tw<strong>in</strong> screw mach<strong>in</strong>e<br />

• Die<br />

design<br />

• Material extraction from the hopers,<br />

• Flow rate control (stability, accuracy),<br />

• Feeders calibration (LT2B equipment).<br />

• Safety concerns,<br />

• Screw designs, ie knead<strong>in</strong>g,<br />

• Process control,<br />

• Barrel design.<br />

• Tw<strong>in</strong> screw flow (LUDOVIC, Code),<br />

• Residence time distribution (ECLIPSE),<br />

• Die flow (poly. 3D).<br />

• Infra red temperature control,<br />

• Paste rheological behavior<br />

• Computor controlled <strong>process</strong>


Small scale validation achieved for new <strong>production</strong> <strong>process</strong> phase<br />

Prelim<strong>in</strong>ary <strong>process</strong> validation was done last year:<br />

At Karlskoga plant for:<br />

• Pellets and granulate <strong>production</strong> with the same composition<br />

as the candidate propellant:<br />

• NG: 29,9% ; NC: 68,3% ; stabilizer: 1% ; plasticizer: 0,6%,<br />

with addition of Mg- stearate for the s<strong>in</strong>gle screw extrusion,<br />

• Geometrie, D: 5mm, thickness: 3mm, density: 0,7 kg/m3 ,<br />

• Cont<strong>in</strong>uous dry<strong>in</strong>g <strong>in</strong> oven.<br />

At Le Bouchet Research Center for:<br />

• Granulates and solvent paste safety test,<br />

• Propellant gra<strong>in</strong>s by <strong>cont<strong>in</strong>uous</strong> <strong>process</strong> with BC 45 TSE.<br />

and Angoulême for:<br />

• Propellant gra<strong>in</strong>s by batch <strong>process</strong> with Werner kneader<br />

and press (<strong>in</strong>dustrial scale).<br />

We have made one lot with same composition, same<br />

geometry and same mechanical properties level at<br />

shot <strong>gun</strong> test: impact+CV.<br />

RQ = 0,97 RI = 1,01


Tw<strong>in</strong> screw comparison for large scale solvent multibase <strong>production</strong><br />

Parameter<br />

BC 45<br />

CRB<br />

APV 65 BC72 APV65<br />

Screw diameter (mm) 55 65 95 65<br />

L/D 21 25 28 25 28<br />

Granulates type D: ≈ 5mm, thickness: ≈ 3mm<br />

BC72<br />

95<br />

D: ≈ 5mm,<br />

Thickness: ≈ 1mm<br />

Dwell time 24 m<strong>in</strong> 12 m<strong>in</strong><br />

Q: quantity of paste<br />

<strong>in</strong>side the barrel (1.3)<br />

1.5 kg 5 kg 7 kg 5 kg 7 kg<br />

Production flow (kg/h) 4 ≈ 15 ≈ 20 ≈ 25 - 30 ≈ 35 - 50


Equipments for large scale solvent multibase <strong>production</strong><br />

TSE mach<strong>in</strong>e BC72 CLEXTRAL type is able to reach the requirements<br />

• slid<strong>in</strong>g barrel with 8 modules,<br />

• pressure release nozzle for safety,<br />

• addition of feeders for solid fillers (modified multibase composition).


Conclusions<br />

• The new l<strong>in</strong>e use the experience of <strong>cont<strong>in</strong>uous</strong> <strong>process</strong> <strong>production</strong> for<br />

solventless and composite (LOVA) <strong>gun</strong> propellant and the experience on solvent<br />

double base compositions,<br />

• The new l<strong>in</strong>e use an <strong>in</strong>novative <strong>process</strong> with two <strong>cont<strong>in</strong>uous</strong> stages us<strong>in</strong>g one<br />

s<strong>in</strong>gle screw and one tw<strong>in</strong> screw,<br />

• The ma<strong>in</strong> phases of this new <strong>process</strong> were checked by us<strong>in</strong>g three <strong>production</strong><br />

equipments <strong>in</strong> Karlskoga, Angoulême and Le Bouchet,<br />

• The new l<strong>in</strong>e will be use for <strong>production</strong> of multibase <strong>gun</strong> propellant also with<br />

solid filler.

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