My notes (and other findings) related to the FN 5.7x28mm Weapon System (Ammunition, Five-seveN pistol, P90 PDW, PS90 carbine, CMMG Banshee Mk57, SCHV weapons in general, conversion of other weapons, accessories, reloading, etc.)
Tuesday, June 22, 2010
5.7x28
5.7X28 INCENDIARY FIREBALL AMMO 20RD [57x28-inc-20ct] - $62.00 : Clark Custom Cartridge Company
$62.00
THESE ARE THE MOST FUN INCENDIARYS I HAVE COME ACROSS IN A LONG TIME! THEY SHOOT GREAT AND ADD ABIT OF FLAVOR TO YOUR FIVE SEVEN OR PS90. THEY SHOOT FLAT AND BLOW UP BIG. THESE ARE TOP OF THE LINE BUT IM NOT TRYIN TO GET RICH OFF ONE BOX OF AMMO SO I AM LISTING THEM AT A 'REASONABLE' PRICE. IF YOU WANT MORE LET ME KNOW WHAT NUMBERS YOU ARE LOOKING FOR AND ILL SEE IF I CAN HELP YOU. I DID GET 'ALOT' OF THESE IN SO IT SHOULDN'T BE A PROBLEM. I DO DISCOUNT FOR BULK. THE BULLETS ARE !!NON!! MAGNETIC SO NO STEEL GOING DOWN THAT EXPENSIVE BARREL!!!
PLEASE DONT BID IF ILLEGAL IN YOUR AREA. LIKE CA WASH' DC , NYC, MASS...
GO TO http://www.youtube.com/watch?v=L2g8vMN9SVo TO SEE A 10 RD MAG OF THESE RDS."
Sunday, June 20, 2010
Inhalt_Wiederladen.pdf (application/pdf Object)
Table of contents for the RWS/RUAG/Nobel reloading manual (in German) "Wiederladen"
Reloading 9mm
Saturday, June 19, 2010
Print Page - New info on True Blue!
Wiley::Propellants, Explosives, Pyrotechnics
An International Journal Dealing with Scientific and Technological Aspects of Energetic Materials
An international journal full of PEP
PEP is the leading source for information on
- Propellants
- Explosives
- Pyrotechnics
- Ignition, combustion and detonation
Coverage includes
Synthesis, formulation, analysis, detection, characterization, ballistics, detonation, application and demilitarization
To keep you up-to-date
Meetings notification and book reviews
Interdisciplinary
Contributions from experts in chemistry, physics and engineering
Indispensable
The latest research results are also available online for institutional subscribers
International
PEP is the forum for the exchange of science and technology in energetic materials.
2008 Impact Factor: 1.110
Readership
Scientists and technologists working on propellants, explosives, primers and pyrotechnics, combustion and detonation processes as well as safety regulations
Combustion Labs
Other Combustion Labs
Wiley::Principles of Combustion, 2nd Edition
Preface.
Preface to the First Edition.
Introduction.
Importance of Combustion for Various Applications.
Related Constituent Disciplines for Combustion Studies.
General Method of Approach to Solving Combustion Problems.
General Objectives of Combustion Modeling.
Classification of Combustion Problems.
General Structure of a Theoretical Model.
Governing Equations for Combustion Modeling (Conservation & Transport Equations).
Some Common Assumptions Made In Combustion Models.
Several Basic Definitions
1. Review of Chemical Thermodynamics.
Nomenclatures.
1. Brief Statement of Thermodynamic Laws.
2. Equation of State.
3. Conservation of Mass.
4. The First Law of Thermodynamics; Conservation of Energy.
5. The Second Law of Thermodynamics.
5. 1 Equilibrium Thermodynamics.
5. 2 Non-equilibrium Thermodynamics.
6. Criteria for Equilibrium.
7. Conservation of Atomic Species.
8. Various Methods for Reactant-Fraction Specification.
8.1 Mole and Mass Fractions.
8.2 Fuel-Oxidant and Fuel-Air Ratios.
8.3 Equivalence Ratio.
8.4 Mixture Fraction.
9. Standard Enthalpies of Formation.
10. Thermochemical Laws.
11. Relationship Between Bond Energies and Heats of Formation.
12. Heats of Reaction for Constant-Pressure and Constant-Volume Combustion.
12.1 Constant-Pressure Combustion.
12.2 Constant-Volume Combustion.
13. Energy Balance Considerations for Flame Temperature Calculations.
14. Equilibrium Constants.
15. Real-Gas Equations of State and Fugacity Calculation.
16. More Complicated Dissociation in the Combustion of Hydrocarbons.
17. The Clausius-Clapeyron Equation for Phase Equilibrium.
18. Calculation of Equilibrium Compositions with NASA's CEA Computer Program.
18.1 Assumptions and Capabilities.
18.2 Equations Describing Chemical Equilibrium.
18.2.1 Thermodynamic Equations.
18.2.2 Minimization of Gibbs Free Energy.
19. Other Well-Established Chemical Equilibrium Codes.
References.
Homework.
Projects.
2. Chemical Kinetics and Reaction Mechanisms.
Additional Symbols.
1. Rates of Reactions and Their Functional Dependence.
1.1 Total Collision Frequency.
1.2 Equation of Arrhenius.
1.3 Apparent Activation Energy.
1.4 Rates of Reaction.
1.5 Methods for Measurement of Gas-Phase Reaction Rates.
1.5.1 Static Methods.
1.5.1.1 Flash Photolysis Resonance Fluorescence Technique.
1.5.1.2 Relative Rate Constant Photolysis Technique.
1.5.1.3 Laser Photolysis/Laser Induced Fluorescence Technique.
1.5.2 Dynamic Methods for Reactions in Flow Systems.
1.5.3 Several Methods for Measuring Rapid Reaction Rates.
2. One-Step Chemical Reactions of Various Orders.
2. 1 First-Order Reactions.
2.2 Second-Order Reactions.
2.3 Third-Order Reactions.
3. Consecutive Reactions.
4. Competitive Reactions.
5. Opposing Reactions.
5.1 First-Order Reaction Opposed by a First-Order Reaction.
5.2 First-Order Reaction Opposed by a Second-Order Reaction.
5.3 Second-Order Reaction Opposed by a Second-Order Reaction.
6. Chain Reactions.
6.1 Free Radicals.
6.2 Lindemann's Theory for First-Order Reaction.
6.3 Complex Reactions.
6.3.1 Hydrogen-Bromine Reaction.
7. Chain-Branching Explosions.
8. CHEMKIN Analysis and Code Application for Gas-Phase Kinetics.
8.1 Thermodynamic Properties.
8.2 Reaction Rate Expressions.
8.3 Brief Description of Procedures in Using CHEMKIN Code.
9. Surface Reactions.
9.1 Surface Adsorption Processes.
9.1.1 The Langmuir Adsorption Isotherm.
9.1.2 Adsorption with Dissociation.
9.1.3 Competitive Adsorption.
9.2 Surface Reaction Processes.
9.2.1 Reaction Mechanism.
9.2.2 Unimolecular Surface Reactions.
9.2.3 Bimolecular Surface Reactions.
9.2.4 Desorption.
9.3 Kinetic Model of Hydrogen-Oxygen Reaction on Platinum Surface.
9.3.1 Simple Kinetic Model of H2/O2 Reaction on Platinum Surface.
9.3.2 Kinetic Rates of H2/O2 reaction on Platinum Surface.
9.4 Experimental Methods to Study Surface Reactions.
9.4.1 Spectroscopic Methods.
9.4.1.1 Auger Electron Spectroscopy.
9.4.2 Temperature Controlled Methods.
9.4.3 Combination of Spectroscopic and Temperature-Controlled Methods.
9.5 Surface Reaction Rate Determination.
9.5.1 Application of LIF Technique in Surface Reaction Rate Determination.
9.5.1.1 The Elementary Steps.
9.5.1.2 Experimental Setup.
9.5.1.3 Experimental Results.
10. Rate Laws for Isothermal Reactions Utilizing Dimensionless Parameters.
10.1 Equilibrium Constants.
10.2 Net Rate of Production of Chemical Species.
11. Procedure and Applications of Sensitivity Analysis.
11.1 Introduction to Sensitivity Analysis.
11.2 The Procedure for Local Sensitivity Analysis.
11.2.1 Time-Dependent Zero-Dimensional Problems.
11.2.2 The Procedure for Steady-State One-Dimensional Problems.
11.2.3 The Procedure for Time-Dependent Spatial Problem.
11.3 The Example of Sensitivity Analysis of Aliphatic Hydrocarbon Combustion.
11.3.1 Local Sensitivity Analysis in One-Dimensional Flame Fronts.
11.3.2 Sensitivity Analysis for Zero-Dimensional Problems.
12. Reaction Flow Analysis.
13. Reaction Mechanisms of H2/O2 Systems.
13.1 Background Information about H2/O2 Reaction Systems.
13.2 Explosion Limits of H2/O2 Systems.
14. Gas-Phase Reaction Mechanisms of Aliphatic Hydrocarbon and Oxygen System.
14.1 Specific Mechanisms.
14.1.1 Gas-Phase Kinetics of H2 Oxidation.
14.1.2 O3 Decomposition Mechanism.
14.1.3 CO Oxidation Mechanism.
14.1.4 CH2O Reaction.
14.1.5 CH4 Oxidation.
14.1.6 C2H6 (Ethane) Oxidation.
14.1.7 C2H4 (Ethylene) Oxidation.
14.1.8 C2H2 (Acetylene) Oxidation.
14.1.9 CH2CO (Ketene) Oxidation.
14.1.10 CH3OH (Methanol) Reactions.
14.1.11 C2H5OH (Ethanol) Reactions.
14.1.12 CH3CHO (Acetaldehyde) Reaction.
14.2 Discussion of More Complex Cases.
15. Reduction of Highly Complex Chemical Kinetic Mechanism to Simpler Reaction Mechanism.
15.1 Quasi-Steady State Assumption (QSSA) and Partial Equilibrium Assumption.
15.2 Computational Singular Perturbation Methods for Stiff Equations.
15.2.1 Stiff Equations.
15.2.2 Chemical Kinetic Systems as Stiff Equations.
15.2.3 Formulation of the Problem.
15.2.4 Procedures for Solving the Chain Reaction Problem.
15.3 Some Observations of the CSP Method.
16. Formation Mechanism of Nitrogen Oxides.
16.1 Thermal NO Mechanism (Zeldovich Mechanism).
16.2 Prompt NO Mechanism (Fenimore Mechanism).
16.3 NO Production from Fuel Bound Nitrogen.
16.3.1 The Oxidation of HCN.
16.3.2 The NO r HCN r N2 Mechanism.
16.3.3 The Oxidation of NH3.
16.4 NO2 Mechanism.
16.5 N2O Mechanism.
16.6 Overall Remarks on NOx Formation.
17. Formation and Control of CO and Particulates.
17.1 Carbon Monoxide.
17.2 Particulate Matters.
17.2.1 Major Types of Particulates.
17.2.2 Harmful Effects.
17.2.3 Particulate Matter Control Methods.
References.
Homework.
3. Conservation Equations for Multicomponent Reacting Systems.
Additional Symbols.
1. Definitions of Concentrations, Velocities, and Mass Fluxes.
2. Fick's Law of Diffusion.
3. Theory of Ordinary Diffusion in Gases at Low Density.
4. Continuity Equation and Species Mass Conservation Equations.
5. Conservation of Momentum.
5. 1Momentum Equation in Terms of Stress.
5.1.1 Momentum Equation Derivation By Infinitesimal Particle Approach.
5.1.2 Momentum Equation Derivation By Infinitesimal Control Volume Approach.
5.1.3 Finite Control Volume.
5.2 Stress-Strain-Rate Relationship (Constitutive Relationship).
5.2.1 Strain Rate.
5.2.2 Stress Tensor.
5. 3 Navier-Stokes Equations.
6. Conservation of Energy.
7. Physical Derivation of the Multicomponent Diffusion Equation.
8. Other Necessary Equations in Multicomponent Systems.
9. Solution of a Multicomponent-Species System.
10. Shvab-Zel'dovich Formulation.
11. Dimensionless Ratios of Transport Coefficients.
12. Boundary Conditions at an Interface.
References.
Homework.
Projects.
4. Detonation and Deflagration Waves of Premixed Gases.
Additional Symbols.
1. Qualitative Differences between Detonation and Deflagration.
2. The Hugoniot Curve.
3. Properties of the Hugoniot Curve.
3.1Entropy Distribution along the Hugoniot Curve.
3.2 Comparison of the Burned-Gas Velocity Behind a Detonation Wave with the Local Speed of Sound.
4. Determination of Chapman-Jouguet Detonation-Wave Velocity.
4.1 Trial-and-Error Method.
4.2 The Newton-Raphson Iteration Method.
4.3Comparison of Calculated Detonation-Wave Velocities with Experimental Data.
5. Detonation-Wave Structure.
5.1ZND One-Dimensional Wave Structure.
5.2Multidimensional Detonation-Wave Structure.
5.3Numerical Simulation of Detonations.
6. The Mechanism of Deflagration-to-Detonation Transition (DDT) in Gaseous Mixtures.
7. Detonability and Chemical Kinetics: Limits of Detonability.
7.1 Classical Model of Belles.
7.2 Detonability Limits of Confined Fuel Mixtures .
7.2.1 Initial Condition Dependence.
7.2.2 Boundary Condition Dependence.
7.2.3 Single-Head Spin Detonation.
7. 3 Detonability Criteria and Detonation Cell Size.
7. 4 Chemical Kinetics of Detonation in H2-Air-Diluent Mixtures.
8. Non-Ideal Detonations.
8.1 Definition of Non-ideal Detonation and Zel'dovich and Shchelkin's Detonation Mechanisms in Rough Tubes.
8.2 Theoretical Considerations of Energy and Momentum Losses.
8.3 Critical Pipe Diameter Consideration.
8.4 Effect of Several Physical and Chemical Parameters on detonability.
8.5 Possible Measures for Reducing Potential of Detonation Wave Generation.
9. Consideration of Spontaneous Detonation Initiation.
9.1 Functional Form of Distribution of Ignition Delay.
9.2 Experimental Verification of Processes of Non-Explosive Detonation Initiation.
9.2.1 Photochemical Initiation of Detonation in Mixtures with Non-Uniform Concentration.
9.2.2 Gasdynamic Jet as a Method of Creating Temperature-Concentration Non-Uniformity.
9.3 General Observation and Status of Understanding.
References.
Homework.
Project.
5. Premixed Laminar Flames.
Additional Symbols.
1. Introduction and Flame Speed Measurement Methods.
1.1 Bunsen Burner Method.
1.2 Constant-Volume Spherical Bomb Method.
1.3 Soap-Bubble (Constant-Pressure Bomb) Method.
1.4 Particle-Track Method.
1.5 Flat-Flame Burner Method.
1.6Diagnostic Method for Flame Structure Measurements.
1.6.1 Velocity Measurements.
1.6.2 Density Measurements.
1.6.3 Concentration Measurements.
1.6.4 Tempetature Measurements.
2. Classical Laminar Flame Theories.
2.1 Thermal Theory: Mallard and LeChatelier's Development.
2.2 Comprehensive Theory: The Theory of Zel'dovich, Frank-Kamenetsky and Semenov.
2.3 Diffusion Theory: The Theory of Tanford and Pease.
3. Contemporary Method for Solving Laminar Flame Problems.
3.1 Premixed O3/O2 Laminar Flames.
3.2 CHEMKIN Code for Solving Premixed Laminar Flame Structures.
4. Dynamic Analysis of Stretched Laminar Premix Flames.
4.1 Definition of Flame Stretch Factor and Karlovitz Number.
4.2 Balance Equation for Premixed Laminar Flame Area.
4.3 The Use of Expanding Spherical Flames to Determine Burning Velocities and Stretch Effects in Hydrogen/Air Mixtures.
4.4 Laminar Burning Velocities and Markstein Numbers of Hydrocarbon/Air Flames.
4.5 Burning Rates of Ultra-Lean to Moderately-Rich H2/O2/N2 Laminar Flames with Pressure Variations.
5. Effect of Chemical and Physical Variables on Flame Speed.
5.1 Chemical Variables.
5.1.1 Effect of Mixture Ratio.
5.1.2 Effect of Fuel Molecular Structure.
5.1.3 Effects of Additives.
5.2 Physical Variables.
5.2.1 Effect of Pressure.
5.2.2 Effect of Initial Temperature.
5.2.3 Effect of Flame Temperature.
5.2.4 Effect of Thermal Diffusivity and Specific Heat.
6. Principle of Stabilization of Combustion Waves in Laminar Streams.
7. Flame Quenching .
8. Flammability Limits of Premixed Laminar Flames.
8.1 Flammability Limits Determined from a Standard Glass Tube.
8.2 Effect of Pressure and Temperature on Flammability Limit.
8.3 Spalding's Theory of Flammability Limits and Flame Quenching.
8. 4 Flame Structure Near the Flammability Limits of Premixed Hydrogen-Oxygen Flames.
References.
Homework.
Projects.
6. Gaseous Diffusion Flames and Combustion of a Single Liquid Fuel Droplet.
1. Burke and Schumann's Theory of Laminar Diffusion Flames.
1. 1 Basic Assumptions and Solution Method.
1. 2 Flame Shape and Flame Height.
2. Phenomenological Analysis of Fuel Jets.
3. Laminar Diffusion Flame Jets.
3.1 Laminar Jet Mixing.
3.2 Laminar Jet with Chemical Reactions.
3.3 Numerical Solution of Two Dimensional Axisymmetric Laminar Diffusion Flames.
3.4 Effect of Preferential Diffusion of Species and Heat in Laminar Diffusion Flames.
4. Evaporation and Burning of a Single Droplet in a Quiescent Atmosphere .
4.1 Evaporation of a Single Fuel Droplet.
4. 2 Mass Burning Rate of a Single Fuel Droplet.
5. Fuel Droplet in a Convective Stream.
5.1 Correlation Development for Nearly Spherical Droplets in Convective Streams.
5.2 Simulation of Deformed Droplets Dynamics.
5.3 Effect of Internal Circulation on Droplet Vaporization Rate.
6. Supercritical Burning of Liquid Droplets in a Stagnant Environment .
6.1 Thermodynamic and Transport Properties.
6.1.1 Extended Corresponding-State Principle.
6.1.2 Equation of State.
6.1.3 Thermodynamic Properties.
6.1.4 Transport Properties.
6.2 Vapor-Liquid Phase Equilibrium.
6.3 Droplet Vaporization in Quiescent Environments.
6.4 Droplet Combustion in Quiescent Environments.
6.5 Droplet Vaporization in Supercritical Convective Environments.
6.6 Droplet Response to Ambient Flow Oscillation.
References.
Homework.
Projects.
Appendix A: Evaluation of Thermal and Transport Properties of Gases and Liquids .
Appendix B: Constants and Conversion Factors Often Used in Combustion.
Appendix C: Naming of Hydrocarbons and Properties of Hydrocarbon Fuels.
Appendix D: Melting, Boiling, and Critical Temperatures of Elements.
Appendix E: Periodic Table and Electronic Configurations of Neutral Atoms in Ground States.
References.
Author Index.
Subject Index.
Combustion and Flame - Elsevier
The mission of the journal is to publish high quality work from experimental, theoretical, and computational investigations on the fundamentals of combustion phenomena and closely allied matters. While submissions in all pertinent areas are welcomed, past and recent focus of the journal has been on:
- Development and validation of reaction kinetics, and reduction of reaction mechanisms and modeling of combustion systems, including
- Conventional, alternative, surrogate fuels
- Pollutants, particulate and aerosol formation and abatement
- Heterogeneous processes
- Experimental, theoretical, and computational studies of laminar and turbulent combustion phenomena, including
- Premixed and non-premixed flames
- Ignition, extinction
- Flame propagation
- Flame structure
- Instabilities and swirl
- Flame spread
- Multi-phase reactants
- Advances in diagnostic and computational methods in combustion, including
- Measurement and simulation of scalar and vector properties
- Novel techniques and state-of-the art applications
- Fundamental investigations of combustion technologies and systems, including
- Internal combustion engines
- Gas turbines
- Small- and large-scale stationary combustion and power generation
- Catalytic combustion
- Combustion synthesis
- Combustion under extreme conditions
- New concepts
alliant "product" "relative quickness" - Google Search
Since Alliant doesn't seem to publish their RQ numbers any more...
Burn rate of Red Dot? - TheHighRoad.US
Unfortunately it was printed before they came out with e3 and the current book does not go into such detail. Probably afraid some Internet Expert would use those laboratory numbers to try to 'calculate' a load.
Listing at
https://www.rrarms.com/catalog.php?prod=E31
shows e3 with the same 94.1 r.q. as Red Dot and Promo."
Friday, June 18, 2010
The Sure Fix Home Improvements
Totally NOT gun related. I needed some home repairs, and Ivan was located close by.
VihtavuoriReloadingGuideEdition8.pdf (application/pdf Object)
VV's Reloading Guide version 8
Burn rate chart on pg. 2
Spherical powders - EURENCO
For a more detailed description of PB Clermont's products, a link SPHERICAL POWDERS
Spherical powders
PB Clermont, the Belgian subsidiary of EURENCO, has one of the largest spherical powder production capacities in the world for small and medium caliber ammunition. PB Clermont produces a wide range of single base and double base (nitrocellulose-nitroglycerine) spherical powders and supplies many of today's leading international ammunition manufacturers. Its range of products is continuously improved to meet customers' present and future needs and developed for the following military and civil uses:
Spherical powder for Military uses
# Small and medium caliber ammunition: from 4.6 mm to 25 mm
# Mortar secondary charges: 60 mm, 81 mm
# Pyrotechnics
Spherical powder for Civil applications
# All kind of sporting cartridges
# Hunting cartridges:
- 12 gauge: all lead loads, steel-shot, subsonic steel-shot,
- 16 and 20 gauges
# Industrial uses:
- Cartridges for power tools: all types
- Cartridges for cattle slaughter (caliber 8Kiln)
- Automotive safety
# Pyrotechnics"
Thursday, June 17, 2010
Lachauss�e New - Start Page
Belgian with connections to FNH
Wednesday, June 16, 2010
Powley Computer Instructions | NFA, National Firearms Association, Canada gun information
{mosauthorxtd noshow}
Disclaimer:
This spreadsheet uses calculations that are theoretical and empirical and should not be relied on as your sole source of information for load development. Consult other reliable data sources such as reloading manuals, bullet, and powder manufacturers to confirm the calculated data. This calculator has been included in this package for comparison and academic purposes only.
Data required:
Cartridge Name (optional - but very useful for future reference)
Case Length (inches)
Bullet Length (inches)
Cartridge Length (inches)
Full Water Capacity of Case (grains) - use calculator below
Bullet Diameter (inches)
Bullet Mass (grains)
Height (axial length) of boat-tail (inches) - if the bullet has no boat-tail, enter 0
Tail Diameter of boat-tail (inches) - if the bullet has no boat-tail, enter 0
Rifle Barrel Length (inches)
It is a good idea to reduce the suggested charge by an additional 5% - no matter WHICH powder is suggested. This spreadsheet lists charges for IMR POWDERS only.
Powley Computer (MS Excel)
Case Water Capacity Calculator (MS Excel)"
Tuesday, June 15, 2010
Comparative Powder Burning Rates
Effect Of Temperature On Various Powders
(0F) (70F) (125F) Changes
Powder Pressure
(kpsi) Velocity
(f/s) Pressure
(kpsi) Velocity
(f/s) Pressure
(kpsi) Velocity
(f/s) D P
Cold D V
Cold D P
Hot D V
Hot
Accurate 2520 50.5 2781 49.9 2805 52.6 2844 600 -24 2700 39
IMR 4064 51.3 2651 51.1 2686 49.7 2697 200 -35 -1400 11
Reloader 15 48.7 2665 50.3 2715 47.3 2705 -2100 -50 -3000 -10
Win 748 47.3 2655 50.2 2724 51.1 2769 -2900 -69 900 45
Varget 51.2 2778 51.1 2771 51.5 2779 100 7 -440 8
Vit N140 47.5 2629 49.6 2665 51.0 2679 -2100 -36 1400 14
Vit N555 48.8 2778 50.1 2808 51.5 2834 -1300 -30 1400 26
Data based upon the 308 Win. cartridge using all the same lot number Winchester cases, Winchester Large Rifle Primers and Sierra 168 gr. BTHP Match bullets. Note that many ball powders can exhibit unexpected extreme changes in pressure below 35 degrees F and above 105 degrees F, rising pressures 10,000 psi or more at elevated temperatures. Be careful at the temperature extremes! In addition do not use ball powders at very low load densities.
Data courtesy of Varget."
Browse Reloaders' Reference Files on SourceForge.net
Monday, June 14, 2010
22 CCM Cooper Centre fire Magnum page176.pdf (application/pdf Object)
The .22 Cooper Centerfire
Magnum is the .22 Extra
Long Centerfire reborn.
The .22 Extra Long Centerfire
was designed for the
Model 1882 Maynard single
shot hunting and gallery
rifles. It was replaced by
the .22 WCF.
The .22 CCM can be thought of as a reloadable .22 WMR. Its performance actually places
it midway between the .22 WMR and the .22 Hornet.
The maximum loads shown below are approved by Cooper Arms.
.249 dia.
.308
.245 dia.
1.156
.050
ASSRA Forum - old .22 CF cartridge question
ASSRA Forum - old .22 CF cartridge question: "Posts: 90
Durham, Connecticut, USA
Re: old .22 CF cartridge question
Reply #7 - 10/27/07 at 23:08:50
Fred Boulton wrote on 10/26/07 at 14:53:29:
I don't know why, but Eley used to make a .22 centre fire!
Fred.
The recently published 'The Classic British Rook & Rabbit Rifle' by Colin Greenwood (2006) has a nice discussion of 'The 22 Long Rifle Central-Fire'. A 22 Long CF appeared around 1899, and the 22 LR CF a few years later. They were available up to 1937 or so. Apparently they were used in 'Morris Tubes', conversion units for large bore rifles. By using a CF case, the conversion unit could be simpler and cheaper. If the attached picture comes through, it shows a 22 LR CF solid, a 22 LR CF HP, and a sectioned case. The cases had a deep cannelure near the base to support the primer.
Doug Nelson
Heat Shrink Tubing, Heat Shrinkable Tubing, Heat Shrink Tube, Heat Shrink Sleeve - HeatShrinkTubingDirect.com
Heat Shrink Tubing, Heat Shrinkable Tubing, Heat Shrink Tube, Heat Shrink Sleeve - HeatShrinkTubingDirect.com: "If you're looking for a particular type of shrink tubing that you don't see on our site, or need additional information about any heat shrink sleeve product available in our current inventory, just give us a call and our highly trained heat shrink tubing professionals will be happy to assist you! We're always just a phone call or email away!"
1-1-Data.pdf (application/pdf Object)
Load data from another version of the previous article.
http://www.gun-tests.com/performance/apr96reloading.html
Untitled Document
...
The Right Shell Holder The first step is getting a shell holder that will hold the .22 WMR case. You can make one by modifying a .25 ACP shell holder by chucking an empty .22 WMR case in an electric drill and coating the rim with grinding compound. While the case is spinning, push the .25 ACP shell holder over the rim so the grinding compound will relieve the slot in the holder for the rim.
...
Saturday, June 12, 2010
Thursday, June 10, 2010
IMR Trail Boss for reduced loads (Pistol and Rifle)
http://hodgdon.com/PDF/Trail-Boss-data.pdf
Trail Boss is a unique powder that was developed originally for the Cowboy Action shooters to produce light, low recoil handgun loads with lead bullets. Some guys started experimenting with it in reduced loads for rifles both with cast lead AND jacketed bullets.
Hodgdon (who now owns IMR) also began experimenting with it and came up with the info in that PDF file."
...
Bullet (not cartridge) overall lengths
Norma 197.5g .322' FJ BT 1.340'
SinterFire SF308-125NTP (w/can) 1.160'
SinterFire SF224-42WTP 0.740'
SinterFire SF762x39-123NTP 1.09'
SinterFire 38 Super .356' 121g 0.79'
Hornady .310' 123g SP #3140 0.85'
Hornady .355' 147g BTHP/XTP #35580 0.65'
Hornady 44 Cal 240g HP #4420 0.705'
Hornady 44 Cal 240g HP/XTP #44200 0.70'
Speer 308 Plinker 100g 0.625'
Speer 308 HP 110g 0.625'
Speer .429' TMJ 240g #4459 0.745'
Lyman 45 LC CAB 250 LRNFP 0.64'
Lyman #311008 0.64'
Lyman #311410 0.82'
Lyman #358429 0.74'
Lyman #429421 0.77'
Lyman #429360 0.72'
NEI #148358 0.652'
RCBS 308-165-SIL w/GC 1.00'
Saeco 68BB 0.64'"
Sunday, June 06, 2010
Dynamic Research Technologies - lead free frangible ammunition in time proven calibers
DRT™ lead-free centerfire ammunition is designed to out-perform all other ammunition and it is environmentally friendly!"
308 Winchester Pages 260 to 262.pdf (application/pdf Object)
http://www.accuratepowder.com/data/PerCaliber2Guide/Rifle/Standarddata%28Rifle%29/308Cal%287.82mm%29/308%20Winchester%20Pages%20260%20to%20262.pdf
Sabot data at the very end.
.308 Winchester
The most exciting feature of our sabots is the uniform 'flowering' which occurs immediately as the bullet exits the muzzle. The design is intended to allow the user to maintain excellent group shooting. For successful group shooting it is recommended that any previously fired barrel be cleaned prior to shooting sabot rounds as the residue will foul the accuracy of the sabot."
Search results for: 'FN5-7'
eHobbyAsia appears to have the largest supply of airsoft accessories for the TM FN5-7
1 Stop Tactical Gear - Blackheart International LLC - Training Manuals/Books
BHI's ads say that their handbook on the FsN is "coming soon"
KTOG Forum - PMR-30
Comparative Powder Burning Rates
Effect Of Temperature On Various Powders
(0F) (70F) (125F) Changes
Powder Pressure
(kpsi) Velocity
(f/s) Pressure
(kpsi) Velocity
(f/s) Pressure
(kpsi) Velocity
(f/s) D P
Cold D V
Cold D P
Hot D V
Hot
Accurate 2520 50.5 2781 49.9 2805 52.6 2844 600 -24 2700 39
IMR 4064 51.3 2651 51.1 2686 49.7 2697 200 -35 -1400 11
Reloader 15 48.7 2665 50.3 2715 47.3 2705 -2100 -50 -3000 -10
Win 748 47.3 2655 50.2 2724 51.1 2769 -2900 -69 900 45
Varget 51.2 2778 51.1 2771 51.5 2779 100 7 -440 8
Vit N140 47.5 2629 49.6 2665 51.0 2679 -2100 -36 1400 14
Vit N555 48.8 2778 50.1 2808 51.5 2834 -1300 -30 1400 26
Data based upon the 308 Win. cartridge using all the same lot number Winchester cases, Winchester Large Rifle Primers and Sierra 168 gr. BTHP Match bullets. Note that many ball powders can exhibit unexpected extreme changes in pressure below 35 degrees F and above 105 degrees F, rising pressures 10,000 psi or more at elevated temperatures. Be careful at the temperature extremes! In addition do not use ball powders at very low load densities."
DRT TerminalShock™ .224 dia 79gr Bullet 50 pcs
unavailable
Price: $22.50
In stock
Item Number: 62201
Manufacturer Item No: 62201
Quantity:
* Whole number only
At DRT™ we are proud to introduce to you our revolutionary lead free frangible bullets. DRT bullets are design to out-perform all others in both accuracy and especially terminal performance. The bullets will both penetrate deeply and still fragment, causing massive wound cavities, bringing that trophy down quickly and humanely.
Recommended for use in 1:7-1:9 twist rate. BC - .370 (G1 scale).
Note: Make sure to clear all hollowpoints from debris in order for the bullets to perform as advertised."
Ballistic coefficients of centerfire bullets.
[nice table]
Develop Subsonic
The ultimate danger in subsonic loading is a phenomenon known as Secondary Explosive Effect (SEE). SEE can destroy the strongest rifle action and it can happen on the first shot or the tenth. In fact it is more likely to happen after the bore is dirty from the first few shots. SEE is the result of slow or incomplete ignition of small amounts of smokeless powder. The powder smolders and releases explosive gases which, when finally ignited, detonate in a high order explosion. The warning sign for imminent SEE is a hangfire or delayed ignition."
...
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