=3D=3D=3D=3D=3D=3D=3D=3D=3D=3D=3D=3D=3D=3D=3D=3D=3D=3D=3D=3D=3D=3D= =3D=3D=3D=3D=3D=3D=3D=3D=3D=3D=3D=3D=3D=3D=3D=3D=3D=3D=3D=3D=3D=3D=3D=3D=3D= =3D=3D=3D=3D=3D=3D=3D=3D=3D=3D=3D=3D=3D=3D=3D=3D=3D=3D=3D=3D=3D=3D=3D=3D Mixer

=3D=3D=3D=3D=3D=3D=3D=3D=3D=3D=3D= =3D=3D=3D=3D=3D=3D=3D=3D=3D=3D=3D=3D=3D=3D=3D=3D=3D=3D=3D=3D=3D=3D=3D=3D=3D= =3D=3D=3D=3D=3D=3D=3D=3D=3D=3D=3D=3D=3D=3D=3D=3D=3D=3D=3D=3D=3D=3D=3D=3D=3D= =3D=3D=3D=3D=3D=3D=3D=3D=3D=3D Mixer

= &nb= sp; = &nb= sp; = &nb= sp; Mixer

PROGRAM MIXER = &nb= sp; = &nb= sp; Mixer

= = &nb= sp; = &nb= sp; = Mixer

VERSION 76= -1 (NOVEMBER 1976) = &nb= sp; = Mixer

VERSION 81= -1 (APRIL 1981) *IBM VERSION = &nb= sp; Mixer

VERSION 82= -1 (AUGUST 1982) *COMPUTER INDEPENDENT VERSION = Mixer

VERSION 84= -1 (JUNE 1984) *SPECIAL I/O ROUTINES TO GUARANTEE Mixer

= &nb= sp; ACCURACY OF ENERGY. = Mixer

= &nb= sp; *DOUBLE PRECISION TREATMENT OF ENERGY Mixer

= &nb= sp; (REQUIRED FOR NARROW RESONANCES). Mixer

VERSION 86= -1 (JANUARY 1986)*FORTRAN-77/H VERSION = Mixer

VERSION 88= -1 (JULY 1988) *OPTION...I= NTERNALLY DEFINE ALL I/O Mixer

= &nb= sp; FILE NAMES (SEE, SUBROUTINE FILIO1 Mixer

= &nb= sp; AND FILIO2 FOR DETAILS). = Mixer

= &nb= sp; *IMPROVED BASED ON USER COMMENTS. Mixe= r

VERSION 89= -1 (JANUARY 1989)*PSYCHOANALYZED BY PROGRAM FREUD TO Mixer

= &nb= sp; INSURE PROGRAM WILL NOT DO ANYTHING Mixer

= &nb= sp; CRAZY. = = Mixer

= &nb= sp; *UPDATED TO USE NEW PROGRAM CONVERT Mixer

= &nb= sp; KEYWORDS. = &nb= sp; Mixer

= &nb= sp; *ADDED LIVERMORE CIVIC COMPILER &nbs= p; Mixer

= &nb= sp; CONVENTIONS. = &nb= sp; Mixer

VERSION 92= -1 (JANUARY 1992)*UPDATED BASED ON USER COMMENTS Mixer

= &nb= sp; *ADDED PHOTON CROSS SECTIONS = Mixer

= &nb= sp; *ADDED FORTRAN SAVE OPTION = Mixer

= &nb= sp; *OUTPUT IN ENDF/B-VI FORMAT = Mixer

= &nb= sp; *COMPLETELY CONSISTENT I/O ROUTINES - Mixer

= &nb= sp; TO MINIMIZE COMPUTER DEPENDENCE. Mixe= r

= &nb= sp; *NOTE, CHANGE IN INPUT PARAMETER Mixer

= &nb= sp; FORMAT. = &nb= sp; Mixer

VERSION 94= -1 (JANUARY 1994)*VARIABLE ENDF/B DATA FILENAMES Mixer

= &nb= sp; TO ALLOW ACCESS TO FILE STRUCTURES Mixer

= &nb= sp; (WARNING - INPUT PARAMETER FORMAT Mixer

= &nb= sp; HAS B= EEN CHANGED) = &nb= sp; Mixer

= &nb= sp; *CLOSE ALL FILES BEFORE TERMINATING Mixer

= &nb= sp; (SEE, SUBROUTINE ENDIT) = Mixer

= &nb= sp; *INCREASED INCORE PAGE SIZE FROM Mixer

= &nb= sp; 1002 TO 4008. = &nb= sp; Mixer

VERSION 96= -1 (JANUARY 1996) *COMPLETE RE-WRITE = Mixer

= &nb= sp; *IMPROVED COMPUTER INDE= PENDENCE Mixer

= &nb= sp; *ALL DOUBLE PRECISION = Mixer

= &nb= sp; *ON SCREEN OUTPUT = &nb= sp; Mixer

= &nb= sp; *UNIFORM TREATMENT OF ENDF/B I/O Mixe= r

= &nb= sp; *IMPROVED OUTPUT PRECISION = Mixer

= &nb= sp; *DEFINED SCRATCH FILE NAMES = Mixer

= &nb= sp; *INCREASED INCORE PAGE SIZE FROM&nb= sp; Mixer

= &nb= sp; = 4008 TO 12000. = &nb= sp; Mixer

VERSION 99= -1 (MARCH 1999) *CORRECTED CHARACTER TO FLOATING Mixe= r

= &nb= sp; = POINT READ FOR MORE DIGITS = Mixer

= &nb= sp; *UPDATED TEST FOR ENDF/B FORMAT Mixer

= &nb= sp; = VERSION BASED ON RECENT FORMAT CHANGE Mixer

= &nb= sp; *GENERAL IMPROVEMENTS BASED ON Mixer

= &nb= sp; USER FEEDBACK = &nb= sp; Mixer

VERSION 99= -2 (JUNE 1999) *ASSU= ME ENDF/B-VI, NOT V, IF MISSING Mixer

= &nb= sp; = MF=3D1, MT-451. = &nb= sp; Mixer

VERS. 2000= -1 (FEBRUARY 2000)*GENERAL IMPROVEMENTS BASED ON Mixer

= &nb= sp; = USER FEEDBACK = &nb= sp; Mixer

VERS. 2002= -1 (MAY 2002) *OPTIONAL INPUT PARAMETERS = Mixer

VERS. 2004= -1 (MARCH 2004) *ADDED INC= LUDE FOR COMMON = Mixer

= &nb= sp; *INCREASED INCORE PAGE SIZE FROM Mixe= r

= &nb= sp; = 12000 TO 60000. = &nb= sp; Mixer

VERS. 2005= -1 (OCT. 2005) *CORR= ECTED MERGE ERROR = Mixer

VERS. 2007= -1 (JAN. 2007) *CHEC= KED AGAINST ALL ENDF/B-VII Mixer

= &nb= sp; *INCREASED INCORE PAGE SIZE FROM Mixe= r

= &nb= sp; = 60,000 TO 240,000. = Mixer

= &nb= sp; = &nb= sp; = &nb= sp; Mixer

OWNED, MAINTAINED AND DISTRIBUTED BY = &nb= sp; Mixer

------------------------------------ = = Mixer

THE NUCLEA= R DATA SECTION = &nb= sp; = Mixer

INTERNATIO= NAL ATOMIC ENERGY AGENCY = &nb= sp; Mixer

P.O. BOX 100 = &nb= sp; = &nb= sp; Mixer

A-1400, VIENNA, AUSTRIA = &nb= sp; = Mixer

EUROPE = &nb= sp; = &nb= sp; = Mixer

= &nb= sp; = &nb= sp; = &nb= sp; Mixer

ORIGINALLY WRITTEN BY = &nb= sp; = Mixer

------------------------------------ = &nb= sp; Mixer

DERMOTT E. CULLEN = &nb= sp; = &nb= sp; Mixer

UNIVERSITY OF CALIF= ORNIA = &nb= sp; = Mixer

LAWRENCE LIVERMORE NATIONAL LABORATORY = &nb= sp; Mixer

L-159 = &nb= sp; = &nb= sp; = Mixer

P.O. BOX 808 = &nb= sp; = &nb= sp; Mixer

LIVERMORE, CA 94550 = &nb= sp; = &nb= sp; Mixer

U.S.A.<= span style=3D'mso-spacerun:yes'> = &nb= sp; = &nb= sp; = Mixer

TELEPHONE<= span style=3D'mso-spacerun:yes'> 925-423-7359 = &nb= sp; = Mixer

E. MAIL CULLEN1@LLNL.GOV = &nb= sp; = Mixer

WEBSITE HTTP://WWW.LLNL.GOV/CULLEN1 = &nb= sp; Mixer

= &nb= sp; = &nb= sp; = Mixer

PURPOSE = &nb= sp; = &nb= sp; = Mixer

------- = &nb= sp; = &nb= sp; = Mixer

THIS PROGR= AM IS DESIGNED TO CALCULATE THE ENERGY DEPENDENT CROSS Mixer

SECTION FO= R A COMPOSITE MIXTURE OF UP TO 10 DIFFERENT MATERIALS. Mixer

= &nb= sp; = &nb= sp; = &nb= sp; Mixer

THE PRESENT VERSION WILL ONLY CALCULATE THE CROSS SECTION FOR ONE Mixer

FINAL REAC= TION (ENDF/B SECTION), E.G. TOTAL CROSS SECTION, BUT NOT Mixer

ANY OTHER REACTION. = &nb= sp; = &nb= sp; Mixer

= &nb= sp; = &nb= sp; = = Mixer

NOTE, THIS PROGRAM WILL NOT COMBINE ALL REACTIONS FOR A MIXTURE Mixer

OF MATERIA= LS DURING A SINGLE RUN - ONLY ONE REACTION WILL BE Mixe= r

CREATED PER RUN. = &nb= sp; = &nb= sp; Mixer

= &nb= sp; = &nb= sp; = &nb= sp; Mixer

EVALUATED = DATA FORMAT = &nb= sp; = Mixer

--------------------- = &nb= sp; = Mixer

THE CROSS SECTION= S ARE READ FROM THE ENDF/B FORMAT AND THE Mixer

COMPOSITE = CROSS SECTION IS CONVERTED TO AN EQUIVALENT BARNS/ATOM Mixer

FORM AND O= UTPUT IN THE ENDF/B FORMAT WITH AN EQUIVALENT ATOMIC Mixer

WEIGHT. TH= E USER MUST SPECIFY THE COMPOSITION BY GIVING THE ZA, Mixer

MT AND GRA= MS/CC OF EACH CONSTITUENT. IN ADDITION THE USER MUST Mixer

IDENTIFY T= HE COMPOSITE CROSS SECTION BY SPECIFYING THE ZA, MAT Mixer

AND MT TO = BE USED IN THE ENDF/B FORMATTED OUTPUT. = Mixer

= &nb= sp; = &nb= sp; = &nb= sp; Mixer

SINCE ONLY= THE CROSS SECTIONS IN FILE 3 AND 23 ARE USED, AND THE Mixer

FORMAT FOR= FILE 3/23 IS THE SAME IN ALL VERSIONS ON ENDF/B, THIS Mixer

PROGRAM MA= Y BE USED WITH ANY VERSION OF ENDF/B DATA (I.E., Mixer

ENDF/B-I, = II, III, IV, V OR VI). DURING A SINGLE RUN IT MAY EVEN Mixer

BE USED TO= READ AND COMBINE EVALUATIONS WHICH ARE IN DIFFERENT Mixer

VERSIONS O= F THE ENDF/B FORMAT. = &nb= sp; = Mixer

= &nb= sp; = &nb= sp; = &nb= sp; Mixer

ENDF/B FOR= MATTED OUTPUT WILL BE IN THE ENDF/B-VI FORMAT REGARDLESS Mixer

OF THE FOR= MAT OF THE INPUT ENDF/B DATA. THIS WILL ONLY EFFECT THE Mixer

HOLLERITH SECTION (MF=3D1, MT=3D451). THE FORMAT OF CROSS SECTIONS Mixer

(MF=3D3) I= S THE SAME IN ALL VERSION OF THE ENDF/B FORMAT. = Mixer

= &nb= sp; = &nb= sp; = &nb= sp; Mixer

IN ORDER TO GUARANTEE PROPER OPERATION OF THIS PROGRAM THE DATA Mixer

MUST BE PR= OPERLY CODED IN THE ENDF/B FORMAT. NO ERROR CHECKING IS Mixer

PERFORMED.= IT IS PARTICULARLY IMPORTANT THAT THE FOLLOWING DATA Mixer

BE CORRECT= = &nb= sp; = &nb= sp; Mixer

= &nb= sp; = &nb= sp; = &nb= sp; Mixer

(1) ZA, MF= , MT - MUST BE CORRECT IN ORDER TO ALLOW PROGRAM TO Mixer

= SELECT THE APPROPRIATE SECTIONS TO BE COMBINED. = Mixer

(2) AWRE - ATOMIC WEIGHT RATIO MUST BE CORRECT TO ALLOW PROGRAM Mixer

= TO CONVERT THE USER SPECIFIED GRAMS/CC INTO ATOMS/CC FOR Mixe= r

= PROPER ATOM RATIO MIXING. = &nb= sp; = Mixer

(3) (ENERG= IES, CROSS SECTIONS) - MUST BE CORRECT, LINEARLY Mixer

= = &nb= sp; = =3D=3D=3D=3D=3D=3D=3D=3D Mixer

= INTERPOLABLE, IN ASCENDING ENERGY ORDER OF (E, BARNS). Mixer

= =3D=3D=3D=3D=3D=3D=3D=3D=3D=3D=3D=3D = &nb= sp; = &nb= sp; Mixer

= &nb= sp; = &nb= sp; = Mixer

= TO CONVERT ENDF/B FORMATTED DATA TO THE REQUIRED INPUT FORM Mixer

= THE FOLLOWING PROGRAMS MAY BE USED, = &nb= sp; Mixer

= LINEAR - CONVERT TABULATED CROSS SECTIONS TO LINEARLY = Mixer

= INTERPOLABLE FORM. = &nb= sp; = Mixer

= RECENT - RECONSTRUCT RESONANCE CONTRIBUTION, ADD TO BACKGROUND Mixer

= CROSS SECTION AND OUTPUT THE COMBINATION IN LINEARLY Mixer

= INTERPOLABLE FORM. = &nb= sp; = Mixer

= SIGMA1 - DOPPLER BROADEN CROSS SECTIONS TO ANY TEMPERATURE AND Mixer

= OUTPUT THE RESULT IN LINEARLY INTERPOLABLE FORM. Mixer

= &nb= sp; = &nb= sp; = &nb= sp; Mixer

DOCUMENTATION = &nb= sp; = &nb= sp; Mixer

------------- = &nb= sp; = &nb= sp; Mixer

THE FACT T= HAT THIS PROGRAM HAS COMBINED THE DATA IS DOCUMENTED Mixer

IN THE OUT= PUT ENDF/B FORMAT IN THE HOLLERITH SECTION BY FIRST Mixer

IDENTIFYIN= G THE VERSION OF THIS PROGRAM THAT WAS USED, IN THE FORM Mixer

= &nb= sp; = &nb= sp; = &nb= sp; Mixer

********************( PROGRAM MIXER 2007-1) ********************** Mixer

= &nb= sp; = &nb= sp; = &nb= sp; Mixer

THIS IS FO= LLOWED BY THE TWO LINE IDENTIFICATION INPUT BY THE USER. Mixer

THIS IS FO= LLOWED BY COMPOSITION INPUT BY THE USER. = Mixer

= &nb= sp; = &nb= sp; = &nb= sp; Mixer

NEUTRON OR= PHOTON DATA = &nb= sp; = Mixer

---------------------- = &nb= sp; = Mixer

THIS PROGR= AM WILL ALLOW YOU TO PROCESS EITHER NEUTRON OR PHOTON Mixer

CROSS SECT= IONS - BUT YOU CANNOT MIX THE TWO TYPES TOGETHER. BY Mixer

INPUT YOU = CAN SPECIFY THE OUTPUT MF =3D 3 (NEUTRONS) OR 23 (PHOTONS) Mixer

WHATEVER T= YPE YOU SPECIFIED FOR OUTPUT IS THE ONLY TYPE OF DATA Mixer

WHICH WILL= BE PROCESSED BY THIS PROGRAM. = &nb= sp; Mixer

= &nb= sp; = &nb= sp; = &nb= sp; Mixer

DEFINING T= HE COMPOSITION = &nb= sp; = Mixer

------------------------ = = &nb= sp; Mixer

THE USER M= AY SPECIFY UP TO 10 DIFFERENT SECTIONS OF DATA TO BE Mixer

COMBINED, = EACH SECTION IDENTIFIED BY ZA AND MT NUMBER. THE Mixer

AMOUNT OF = EACH MATERIAL IS SPECIFIED BY DEFINING THE NUMBER OF Mixer

GRAMS/CC O= F EACH MATERIAL IN THE COMPOSITE MIXTURE. THIS CAN BE Mixer

DERIVED FR= OM THE VOLUME FRACTION SIMPLY BY MULTIPLYING THE STP Mixer

DENSITY OF= EACH MATERIAL BY ITS VOLUME FRACTION. NOTE, DO NOT Mixer

INPUT ATOM FRACTIONS. = &nb= sp; = Mixer

= &nb= sp; = &nb= sp; = &nb= sp; Mixer

THE LIST OF SECTIONS TO BE COMBINED MAY BE SPECIFIED IN ANY Mixer

ORDER, I.E= . THEY NEED NOT BE IN ZA ORDER OR THE ORDER THAT THE Mixer

EVALUATED = DATA APPEARS ON THE ENDF/B FORMATTED TAPE. = Mixer

= &nb= sp; = &nb= sp; = &nb= sp; Mixer

IF ANY REQ= UESTED SECTION OF DATA IS NOT FOUND ON THE ORIGINAL Mixer

ENDF/B FOR= MATTED FILE, THE PROGRAM WILL PRINT A LIST OF THE Mixer

MISSING SE= CTIONS AND TERMINATE. IF ALL REQUESTED SECTIONS ARE Mixer

FOUND THE = PROGRAM WILL PRODUCE A COMPOSITE SECTION USING THE Mixe= r

UNION OF ALL ENERGIES FOUND IN ANY SECTION. THE COM= POSITE SECTION Mixer

WILL NOT BE THINNED. = &nb= sp; = &nb= sp; Mixer

= &nb= sp; = &nb= sp; = &nb= sp; Mixer

PRIOR TO L= ATER USE IN ANY APPLICATION THE NUMBER OF ENERGY POINTS Mixer

IN THE COM= POSITE CROSS SECTION MAY BE MINIMIZED BY USING PROGRAM Mixer

LINEAR, UCRL-50400, VOL. 17, PART B TO THIN THE DATA. = Mixer

= &nb= sp; = &nb= sp; = &nb= sp; Mixer

ONLY LINEA= RLY INTERPOLABLE DATA = &nb= sp; = Mixer

------------------------------- = &nb= sp; Mixer

THE CROSS SECTIONS TO BE COMBINED MUST BE IN LINEARLY INTERPOLABLE Mixer

TABULATED = FORM (I. E., FILE 3 OR 23, INTERPOLATION LAW 2). Mixer

= &nb= sp; = &nb= sp; = Mixer

TO CONVERT TABULATED CROSS SECTIONS TO LINEARLY INTERPOLABLE FORM Mixer

SEE, PROGR= AM LINEAR, UCRL-50400, VOL. 17, PART A. = Mixer

= &nb= sp; = &nb= sp; = Mixer

TO CONVERT RESONANCE PARAMETERS TO LINEARLY INTERPOLABLE FORM SEE, Mixer

PROGRAM RE= CENT, UCRL-50400, VOL. 17, PART C. = &nb= sp; Mixer

= &nb= sp; = &nb= sp; = &nb= sp; Mixer

TO DOPPLER BROADEN LINEARLY INTERPOLABLE DATA TO ANY TEMPERATURE Mixer

SEE PROGRAM SIGMA1, UCRL-50400, VOL. 17, PART B. = Mixer

= &nb= sp; = &nb= sp; = &nb= sp; Mixer

PAGING SYSTEM = &nb= sp; = &nb= sp; Mixer

------------- = &nb= sp; = &nb= sp; Mixer

THERE IS NO LIMIT TO THE THE NUMBER OF DATA POINTS IN EACH OF THE Mixer

SECTIONS T= O BE COMBINED, NOR IS THERE A LIMIT TO THE NUMBER OF Mixer

DATA POINT= S IN THE COMPOSITE MIXTURE CROSS SECTION. = Mixer

= &nb= sp; = &nb= sp; = &nb= sp; Mixer

ALL REQUIR= ED SECTIONS OF DATA ARE READ FROM THE ORIGINAL ENDF/B Mixer

FORMATTED = FILE. ANY SECTION OF 60000 OR FEWER POINTS WILL BE Mixe= r

TOTALLY CO= RE RESIDENT. LARGER SECTIONS ARE LOADED INTO A PAGING Mixer

SYSTEM USI= NG A SCRATCH FILE WITH ONLY 60000 POINTS PER SECTION Mixer

CORE RESID= ENT AT ANY ONE TIME. SIMILARLY THE COMPOSITE SECTION Mixer

WILL BE TO= TALLY CORE RESIDENT IF IT CONTAINS 60000 OR FEWER POINTS Mixer

AND LARGER COMPOSITE SECTIONS WILL BE LOADED INTO A PAGING Mixer

<= /p>

SYSTEM WHE= RE ONLY 60000 POINTS ARE CORE RESIDENT AT ANY TIME. SINC Mixer

A PAGING S= YSTEM MAY BE USED BY ANY SECTION OF DATA THERE IS NO Mixer

LIMIT TO T= HE SIZE OF EITHER THE ORIGINAL SECTIONS, NOR TO THE Mixer

COMPOSITE SECTION, E.G. A SECTION MAY CONTAIN 100,000 ENERGIES Mixer

AND CROSS SECTIONS TO DESCRIBE A GIVEN REACTION. = Mixer

= &nb= sp; = &nb= sp; = = Mixer

PAGE SIZE<= span style=3D'mso-spacerun:yes'> = &nb= sp; = &nb= sp; Mixer

---------<= span style=3D'mso-spacerun:yes'> = &nb= sp; = &nb= sp; Mixer

THE PAGE S= IZE USED IN THIS PROGRAM IS DEFINED BY THE PARAMETER Mixer

NPAGE AND = THE DIMENSIONS OF THE ARRAYS XTAB AND YTAB. IN ORDER Mixer

TO ADAPT T= HIS PROGRAM FOR USE ON ANY COMPUTER THE PAGE SIZE MAY Mixer

BE INCREAS= ED OR DECREASED BUT THE FOLLOWING RULES MUST BE FOLLOWED Mixer

= &nb= sp; = &nb= sp; =3D=3D=3D=3D = Mixer

= &nb= sp; = &nb= sp; = &nb= sp; Mixer

(1) NPAGE = - MUST BE A MULTIPLE OF 3 IN ORDER TO ALLOW THE PROGRAM Mixer

= TO READ FULL CARDS OF ENDF/B DATA (3 POINTS PER LINE). FAILURE Mixer

= TO FOLLOW THIS RULE CAN LEAD TO LOSS OF DATA AND/OR PROGRAM Mixer

= ERRORS DURING EXECUTION. = &nb= sp; = Mixer

(3) YTAB - THE DIMENSION OF YTAB MUST BE (NPAGE,11). = Mixer

(4) XTAB - THE DIMENSION OF XTAB MUST BE (NPAGE,11). = Mixer

= &nb= sp; = &nb= sp; = &nb= sp; Mixer

DOPPLER BROADENING &n= bsp; = &nb= sp; = Mixer

------------------ = &nb= sp; = &nb= sp; Mixer

THE COMPOS= ITE CROSS SECTION OUTPUT FROM THIS PROGRAM SHOULD NOT Mixer

BE DOPPLER BROADENED USING PROGRAM SIGMA1, OR THE EQUIVALENT. THE Mixer

ATOMIC WEI= GHT USED TO IDENTIFY THE COMPOSITE MIXTURE IS BASED ON Mixer

THE ATOM FRACTION OF EACH CONSTITUENT AND CANNOT BE USED TO Mixer

CHARACTERI= ZE THE BROADENING OF ANY GIVEN RESONANCE IN THE MIXTURE Mixer

DUE TO THE CONTRIBUTION OF ONE CONSTITUENT. IN ORDER TO CONSIDER Mixer

DOPPLER BROADENING FIRST USE PROGRAM SIGMA1 TO BROADEN THE CROSS Mixer

SECTION FO= R EACH OF THE CONSTITUENTS AND THEN COMBINE THE = Mixer

BROADENED = DATA USING PROGRAM MIXER. = &nb= sp; Mixer

= &nb= sp; = &nb= sp; = &nb= sp; Mixer

EXAMPLE US= E = &nb= sp; = &nb= sp; Mixer

----------= - = &nb= sp; = &nb= sp; Mixer

THE OUTPUT= FROM THIS PROGRAM HAS BEEN FOUND TO BE EXTREMELY Mixer

USEFUL IN = THE FOLLOWING APPLICATIONS... = &nb= sp; Mixer

= &nb= sp; = &nb= sp; = &nb= sp; Mixer

(1) CALCUL= ATE A COMPOSITE TOTAL CROSS SECTON FOR LATER USE AS Mixer

= A WEIGHTING FUNCTION IN SELF-SHIELDING THE CROSS SECTIONS Mixer

OF EACH CONSTITUENT OF= THE MIXTURE SEPARATELY. = Mixer

= &nb= sp; = &nb= sp; = &nb= sp; Mixer

= PROGRAM GROUPIE CAN USE THE CALCULATED COMPOSITE TOTAL CROSS Mixer

= SECTION AS THE TOTAL CROSS SECTION FOR EACH CONSTITUENT OF Mixer

= THE MIXTURE IN ORDER TO CALCULATE&n= bsp; SELF-SHIELDED CROSS SECTION Mixer

= FOR EACH CONSTITUENT OF THE MIXTURE. = &nb= sp; Mixer

= &nb= sp; = &nb= sp; = Mi= xer

(2) CALCUL= ATE COMPOSITE TOTAL AND FISSION CROSS SECTIONS IN Mixer

= ORDER TO CALCULATE THE TRANSMISSION AND SELF-INDICATION Mixer

= THROUGH COMPOSITE MATERIALS. GENERALLY IN THIS CASE THE Mixer

= TOTAL CROSS SECTION WILL BE CALCULATED FOR THE COMPOSITION Mixer

= OF THE SAMPLE AND THE FISSION CROSS SECTION WILL BE = Mixer

= CALCULATED FOR THE COMPOSITION OF THE FISSION CHAMBER = Mixer

= (WHICH GENERALLY WILL HAVE A DIFFERENT COMPOSITION THAN THE Mixer

= SAMPLE). = &nb= sp; = &nb= sp; Mixer

= &nb= sp; = &nb= sp; = Mixer

= PROGRAM VIRGIN CAN USE THE OUTPUT FROM THIS PROGRAM TO Mixer

= PERFORM TRANSMISSION AND SELF-INDICATION CALCULATIONS. Mixer

= PROGRAM VIRGIN WILL ANALYTICALLY CALCULATE THE UNCOLLIDED Mixer

= (I.E. VIRGIN) FLUX TRANSMITTED AND REACTION RATE DUE TO ANY Mixer

= TABULATED LINEARLY INTERPOLABLE INCIDENT SPECTRUM. RESULTS Mixer

= WILL BE PRESENTLY FOR UP TO 10 DIFFERENT SAMPLE THICKNESSES Mixer

= AND BINNED INTO ENERGY GROUPS IN ORDER TO SIMULATE AN = Mixer

= EXPERIMENTAL MEASUREMENT. = &nb= sp; = Mixer

= &nb= sp; = &nb= sp; = &nb= sp; Mixer

(3) THE OU= TPUT FROM THIS PROGRAM IS VERY USEFUL TO PLOT IN ORDER Mixer

= TO SEE THE IMPORTANCE OF SPECIFIC CROSS SECTION FEATURES IN Mixer

= THE COMPOSITE CROSS SECTION. = &nb= sp; = Mixer

= = &nb= sp; = &nb= sp; Mixer=

= PROGRAM COMPLOT CAN BE USED TO PLOT THE OUTPUT FROM THIS Mixe= r

= PROGRAM AND IF REQUIRED EXAMINE ANY PARTICULAR ENERGY RANGE Mixer

= IN DETAIL. IN ORDER TO DO THIS THE (ZA, MT) EQUIVALENCE OPTION Mixer

= OF PROGRAM COMPLOT SHOULD BE USED. TO COMPARE ANY CONSTITUENT Mixer

= CROSS SECTION TO THE COMPOSITE CROSS SECTION THE INPUT TO Mixer

= COMPLOT SHOULD EQUATE THE (ZA,MT) OF THE COMPOSITE TO THE Mixer

= (ZA,MT) OF ONE CONSTITUENT AND THE MULTIPLIER INPUT TO Mixer

= COMPLOT SHOULD BE THE ATOM FRACTION FOR THE CONSTITUENT (THE Mixer

= ATOM FRACTIONS ARE DEFINED IN THE OUTPUT LISTING FROM PROGRAM Mixer

= MIXER). = &nb= sp; = &nb= sp; Mixer

= &nb= sp; = &nb= sp; = &nb= sp; Mixer

INPUT FILE= S = &nb= sp; = = Mixer

----------= - = &nb= sp; = &nb= sp; Mixer

UNIT DESCRIPTION = &nb= sp; = &nb= sp; Mixer

---- ----------- = &nb= sp; = Mixer=

2 INPUT CARDS (B= CD - 80 CHARACTERS/RECORD) = Mixer

10 ORIGINAL EVALUATED DATA IN E= NDF/B FORMAT = Mixer

= &nb= sp; (BCD - 80 CHARACTERS/RECORD) = Mixer

= &nb= sp; = &nb= sp; = &nb= sp; Mixer

OUTPUT FILES = &nb= sp; = &nb= sp; Mixer

------------ = &nb= sp; = &nb= sp; Mixer

UNIT DESCRIPTION = &nb= sp; = &nb= sp; Mixer

---- ----------- = &nb= sp; = &nb= sp; Mixer

3 OUTPUT LISTING= (BCD - 120 CHARACTERS/RECORD) = Mixer

11 COMPOSITE EVALUATED DATA IN = ENDF/B FORMAT = Mixer

= &nb= sp; (BCD - 80 CHARACTERS/RECORD) = &nb= sp; Mixer

= &nb= sp; = &nb= sp; = &nb= sp; Mixer

SCRATCH FILES = &nb= sp; = &nb= sp; Mixer

------------- = &nb= sp; = &nb= sp; Mixer

UNIT DESCRIPTION = &nb= sp; = &nb= sp; Mixer

---- ----------- = = &nb= sp; = Mixer

12 SCRATCH FILE FOR EACH OF THE= 10 SECTIONS WHICH = Mixer

13 WILL BE ADDED TOGETHER TO DE= FINE THE FINAL = Mixer

. SECTION (BINAR= Y - 60000 AND 480000 WORDS/RECORD) = Mixer

. . = &nb= sp; = &nb= sp; = Mixer

20 .= = &nb= sp; = = Mixer

21 .= = &nb= sp; = &nb= sp; = Mixer

22 SCRATCH FILE FOR COMBINED SECTION. = &nb= sp; Mixer

= (BINARY - 2004 WORDS/RECORD) = &nb= sp; = Mixer

= &nb= sp; = &nb= sp; = &nb= sp; Mixer

STANDARD F= ILE NAMES (SEE SUBROUTINES FILIO1 AND FILIO2) = Mixer

---------------------------------------------------------------- Mixer

UNIT FILE NAME = &nb= sp; = &nb= sp; Mixer

---- ---------- = &nb= sp; = &nb= sp; Mixer

2 MIXER.INP = &nb= sp; = &nb= sp; Mixer

3 MIXER.LST = &nb= sp; = &nb= sp; Mixer

10 ENDFB.IN = &nb= sp; = &nb= sp; Mixer

11 ENDFB.OUT = &nb= sp; = &nb= sp; Mixer

12-22 (SCRATCH) = &nb= sp; = &nb= sp; Mixer

= &nb= sp; = &nb= sp; = &nb= sp; Mixer

INPUT CARD= S = &nb= sp; = &nb= sp; Mixer

----------= - = &nb= sp; = &nb= sp; Mixer

LINE COLS. FORMAT NAME DESCRIPTION = &nb= sp; Mixer

---- ----- ------ ------- ---------- = &nb= sp; Mixer

1-2<= span style=3D'mso-spacerun:yes'> 1-66 16A4,A2 TITLE TWO LINE TITLE DESCRIBING PROBLEM Mixer

= &nb= sp; = (THIS TITLE IS USED TO IDENTIFY THE Mixer

= &nb= sp; = OUTPUT LISTING AND IS ALSO WRITTEN Mixer

= &nb= sp; = IN MF=3D1, MT=3D451 (HOLLERITH SECTION) Mixer

= &nb= sp; = OF THE ENDF/B FORMATTED OUTPUT TO Mixer

= &nb= sp; = IDENTIFY THE COMPOSITE MIXTURE). Mixer

3 1-60 = ENDF/B INPUT DATA FILENAME = Mixer

= &nb= sp; = (STANDARD OPTION =3D ENDFB.IN) = Mixer

4 1-60 = ENDF/B OUTPUT DATA FILENAME = Mixer

= &nb= sp; = (STANDARD OPTION =3D ENDFB.OUT) Mixer

5 1-11 I11 IZAOUT ZA IDENTIFICATION FOR COMBINATION<= span style=3D'mso-spacerun:yes'> Mixer

5 12-17 I6 MATOUT MAT IDENTIFICATION FOR COMBINATION= Mixer

5 18-19 I2 MFOUT MF IDENTIFICATION FOR COMBINATION Mixer

5 20-22 I3 MTOUT MT IDENTIFICATION FOR COMBINATION Mixer

6-N<= span style=3D'mso-spacerun:yes'> 1-11 I11 IZAGET ZA (1000*Z+A) OF MATERIAL = Mixer

6-N<= span style=3D'mso-spacerun:yes'> 12-22 I11 MTGET MT OF REACTION = &nb= sp; Mixer

6-N 23-33 E11.4 DENSE DENSITY OF MATERIAL (GRAMS/CC) Mixer

= &nb= sp; = &nb= sp; = &nb= sp; Mixer

THE SIXTH = LINE IS REPEATED FOR EACH SECTION (FROM 2 TO 10). Mixer

SINCE THE = ENDF/B FORMATTED OUTPUT IS IN BARNS/ATOM FORM A MINIMUM Mixer

OF TWO SEC= TIONS MUST BE COMBINED (I.E., IF ONLY ONE SECTION IS Mixer

SPECIFIED = THE OUTPUT WOULD BE IDENTICAL TO THE INPUT AND AS SUCH Mixer

THE PROGRA= M WILL CONSIDER THIS TO BE AN ERROR AND NOT PERFORM THE Mixer

CALCULATIO= N). THE LIST OF SECTIONS IS TERMINATED BY A BLANK LINE. Mixer

= &nb= sp; = &nb= sp; = &nb= sp; Mixer

THE LIST OF SECTIONS TO BE COMBINED MAY BE SPECIFIED IN ANY Mixer

ORDER, I.E= . THEY NEED NOT BE IN ZA ORDER OR THE ORDER THAT THE Mixer

EVALUATED = DATA APPEARS ON THE ENDF/B FORMATTED TAPE. = Mixer

= &nb= sp; = = &nb= sp; Mixer

EXAMPLE IN= PUT NO. 1 = &nb= sp; = &nb= sp; Mixer

------------------- = &nb= sp; = &nb= sp; Mixer

CREATE THE= TOTAL CROSS SECTION (MT=3D1) FOR STAINLESS STEEL AND Mixer

IDENTIFY T= HE COMBINED MATERIAL WITH ZA=3D26800 AND MAT=3D4000, Mixer

THE COMPOS= ITION BY VOLUME OF THE STEEL WILL BE... = Mixer

= &nb= sp; = &nb= sp; = = Mixer

THE DATA F= ROM \ENDFB6\K300\LIBRARY.DAT AND WRITE DATA TO = Mixer

\MIXER\STEEL.DAT = &nb= sp; = &nb= sp; Mixer

= &nb= sp; = &nb= sp; = Mixer

IRON - 74.8 PER-CENT = &nb= sp; = Mixer

CHROMIUM - 16.0 = &nb= sp; = &nb= sp; Mixer

NICKEL - 6.0 = &nb= sp; = &nb= sp; Mixer

MANGANESE = - 2.0 = &nb= sp; = &nb= sp; Mixer

SILICON - 1.0 = &nb= sp; = &nb= sp; Mixer

CARBON - 0.2 = &nb= sp; = &nb= sp; Mixer

= &nb= sp; = &nb= sp; = Mixer

THE INPUT = MUST SPECIFY THE COMPOSITION BY GRAMS/CC. THIS IS Mixer

DEFINED AS= THE PRODUCT OF THE STANDARD DENSITY (GRAMS/CC) = Mixer

TIMES THE = VOLUME FRACTION. NOTE, DO NOT USE ATOM FRACTIONS. Mixer

FOR THIS E= XAMPLE THE FOLLOWING 12 INPUT CARDS ARE REQUIRED.... Mixer

= &nb= sp; = &nb= sp; = &nb= sp; Mixer

STAINLESS = STEEL. COMPOSITION BY PER-CENT VOLUME IS 74.8-IRON, Mixer

16-CHROME, 6-NICKEL, 2-MANGANESE, 1-SILICON, 0.2-CARBON = Mixer

\ENDFB6\K300\LIBRARY.DAT = &nb= sp; = Mixer

\MIXER\STEEL.DAT = = &nb= sp; = Mixer

= 26800 4000 3 1 = &nb= sp; = Mixer

= 26000 = 1 5.88676 = (NOTE, GRAMS/CC INPUT FOR EACH Mixer

= 24000 = 1 1.150448 CONSTITUENT, E.G. FOR IRON THE Mixer

= 28000 = 1 0.533928 STP DENSITY IS 7.87 GRAMS/CC. Mixer

= 25055 = 1 0.1486 &nb= sp; THE INPUT VALUE OF 5.88676 IS Mixer

= 14000 = 1 0.0233 &nb= sp; 0.748 X 7.87,I.E. VOLU= ME Mixer

= 6012 = 1 0.0044958 FRAC= TION TIMES STP DENSITY). Mixer

= &nb= sp; = (BLANK LINE TERMINATES INPUT LIST) Mixer

= &nb= sp; = &nb= sp; = Mixe= r

EXAMPLE IN= PUT NO. 2 = &nb= sp; = &nb= sp; Mixer

------------------- = &nb= sp; = &nb= sp; Mixer

THE SAME E= XAMPLE AS THE ABOVE PROBLEM, ONLY USE THE STANDARD Mixe= r

ENDF/B DATA FILENAMES - ENDFB.IN AND ENDFB.OUT (THIS CAN BE Mixer

DONE BY LE= AVING THE THIRD AND FOURTH INPUT LINES BLANK). = Mixer

FOR THIS E= XAMPLE THE FOLLOWING 12 INPUT CARDS ARE REQUIRED.... Mixer

= &nb= sp; = &nb= sp; = Mixer

STAINLESS = STEEL. COMPOSITION BY PER-CENT VOLUME IS 74.8-IRON, Mixer

16-CHROME, 6-NICKEL, 2-MANGANESE, 1-SILICON, 0.2-CARBON = Mixer

(NOTE - TH= IS LINE IS REALLY BLANK) = &nb= sp; Mixer

= 26800 4000 3 1 = &nb= sp; = Mixer

= 26000 = 1 5.88676 = (NOTE, GRAMS/CC INPUT FOR EACH Mixer

= 24000 = 1 1.150448 CONSTITUENT, E.G. FOR IRON THE Mixer

= 28000 = 1 0.533928 STP DENSITY IS 7.87 GRAMS/CC. Mixer

= 25055 = 1 0.1486 THE INPUT VALUE OF 5.88= 676 IS Mixer

= 14000 = 1 0.0233 &nb= sp; 0.748 X 7.87,I.E. VOLUME Mixer

= 6012 = 1 0.0044958 FRAC= TION TIMES STP DENSITY). Mixer

= &nb= sp; = (BLANK LINE TERMINATES INPUT LIST) Mixer

= &nb= sp; = &nb= sp; = &nb= sp; Mixer