

JUST A NOTE I FINISHED MY IMAC ALBUM AND NOW IM ON MY OKC ALBUM / FILE
THE RIGHT TANK IS THE ONE THAT HAD A HOSE RUPTURE ON THE RECIRC PUMP
I JUST REALIZED TODAY 1/22/25 THEY WERE OVER CIRCULATING THE RECIRC PUMP INTENTIONALLY TO BREAK IT AND CAUSE A MESS. MECHANICS AT DRAPER DO THIS THEY LIKE TO BREAK THINGS ESPECIALLY IF THEY ARE UNDER WARRANTY. AND IT DOESN’T HELP THAT ALL THESE PEOPLE COMPLAIN AND SAY EVERYTHING NEGATIVE THAT THEY CAN ABOUT A BRAND NEW 20 MILLION DOLLAR SLUDGE FACILITY
THE RECIRC PUMPS ARE FOR WHEN THE POLYMER SETTLES
I DID A SETTLEABILITY TEST ON THE POLYMER AND IT WAS ONLY LIKE NOT EVEN 10/100 MLS A WEEK OR EVEN LESS LIKE EVEN 5 OR 7 REALLY HARD TO EVEN READ. IT SHOULD BE RERAN WITH A WHOLE LITER FOR BETTER ACCURACY AND REPRESENTATION BUT THE POINT IS ITS AN EXTREMELY SLOW SETTLEABILITY FLUX CURVE
MEANING THAT INSTEAD OF RECIRCULATING EVERY 15 MINUTES FOR 5 MINUTES LIKE THEY WERE IT ONLY NEEDED TO BE LIKE ONCE A DAY FOR 15 MINUTES OR EVEN 7. HONESTLY IT DOESN’T EVEN NEED RECIRCULATED UNTIL IT IS TIME TO PRESS WHICH MAY BE ONCE A MONTH OUT THERE. THE WHOLE MIXING TANK TAKES LIKE A WHOLE WEEK TO PRESS. ID SAY THEY ONLY PRESS LIKE 2 OR 3 MONTHS OUT OF THE YEAR OUT THERE CUMULATIVELY BUT IM SURE THEY DRAG IT OUT AND JUSTIFY IT LIKE THEY DO EVERYTHING AND SAY THAT ITS HALF THE YEAR WHICH IS A LIE.
I CAN GET INTO 20 OTHER THINGS ABOUT THE WEAKENED DISTORTED DEFENSE THEY ARE RUNNING OUT HERE BUT THAT’S WORTH ITS OWN TOUR / FILE. I PROBABLY WROTE 20 THINGS ON A PAGE ABOUT IT THERES LOTS MORE ILLEGAL THINGS ABOUT IT
HERE IS A CLEAN WEDGE ZONE WHICH I THINK IS WORTH NOTING AT THE DRPER BELT FILTER PRESSES
NO LIME SCALE AND DRAPER USES CALCIUM HYDRATE SLAKED LIME NOT THE QUICKLIME CAO
IF YOU DON’T RUN THESE FEBS LOW AND EMPTY THIS IS WHY SLUDGE WILL SETTLE IN THEM
U CAN SEE THE WATER IS CLEAR AND CALM INDICATING NO OR SLOW FLOW
THERE WOULD HAVE TO BE 7MGD IN 1 FEB BEFORE JUSTIFYING TURNINGA NOTHER ONE ONE
252 631 3 1 SAYS FOLLOW OWNERS MANUALS AND PROCEDURES
CONTRACTORS PROVIDED OKC WITH THIS INFO ON THE CONTROL NARRATIVE FROM ARCHER WESTERN AND THE ENGINEERS
THIS IS THE DRAPER NORTH FEB
THIS IS THE INSTANT MPY CORROSION METER AT DRAPER LAKE
ITS IN THE OPS LAB
IT MEASURE IN LIKE MICRONS PER YEAR
IT IS FOR ESTIMATING STABILITY
I BELIEVE OKC IS USING IT AS PART OF THEIR CORROSION STUDY
I LISTENED TO SEGRAVES PRESENTATION OF THE CORROSION STUDY AT THE AWWA CONVENTION
A LOT OF THE DATA WAS INCONCLUSIVE AS IT WAS MOSTLY QUALITATIVE FROM THE PUBLIC
I DON’T REMEMBER MY QUESTIONS FROM THE STUDY BUT I DID HAVE PLENTY THAT WERE EASY ENOUGH BEING THAT WERE ON THE SAME TEAM AND THERE IS A LARGE CROWD
HE DIDN’T TAKE UP ANY QUESTIONS AT THE END OF HIS STUDY HE KIND OF WRAPPED IT SHORT AND CUT THE CROWD OFF SARCASTICALLY
HEFNER NEEDS ONE OF THESE
AND OPERATORS OF THE LIME DOSAGE MUST SUBSCRIBE TO IT
I AM NOT AWARE OF ITS METHOD CALCULATIONS. IT MAY BE MORE CRUDE THAN THE SM2330B
THE SM2330B IS VERY EXTENSIVE ESPECIALLY IF U HAVE A FULL MINERAL ANALYSIS CONTENT
OKC DOES NOT DO THE FULL MINERAL ANALYSIS CONTENT I BELIEVE
SM2330B CALCIUM CARBONATE SATURATION DETERMINATION
STANDARD METHODS
HERE IS DENNIS PHILLIPS TRYING TO DETEST THE ENGINEERS
EPA FORCE MAIN DESIGN REGS ARE PUBLISHED AND ARE CRITICAL TO DESIGN
THE LARGETS ISSUE I FIND IN OPERATING IS OPERATORS NOT BEING AWARE OF THIS
WATER AND WASTEWATER BOTH NEED TO REACH PAST CERTAIN VELOCITIES OF 2 FEET PERSECOND
THIS KEEPS THE SOLIDS FROM SETTLING
IF YOU TREAT THIS HUGE 100 SOME FOOT FEB AS A PIPE AND SOLVE FOR THE FLOW IT WOULD TAKE TO EXCEED THAT VELOCITY OF 2FPS IT WOULD ALIGN WITH THE DESIGN REGS
THIS IS WHY THE FEB WAS DESIGNED TO BE THE SIZE THAT IT IS
THIS IS WHY THE WETWELL LEVEL FOR THE PUMPS IS CALLED A WETWELL LEVEL NOT A FEB LEVEL
IF I RECALL THE WETWELL LEVEL NEEDED TO BE SET AROUND 5 FEET DOWN THERE AT DRAPER BUT I WAS ONLY LUCKY ENOUGH IN MY TIME FOR THAT NOT TO BE CHANGED IM SURE SOME ONE HAS CHANGED IT SINCE I LEFT BECAUSE I CANT HAVE ANYTHING I EVER ASK FOR
ESPECIALLY IF ITS PUBLISHED RESEARCH IN GOVERNMENT OR ENGINEERING OR OPERATING AND EVEN OF MY OWN
this is from alfa luval belt filter press manual
I have all the manuals I can possibly own on any water treatment equipment that I have operated
which reminds me in trucking ur supposed to have certain documents within arms reach and that’s how I like to view operating the water we at least at a minimum need to have access to important literature for the equipment we operate
THIS IS THE CLARIFER EFFLUENT AT LAKE HEFNER CLARIFIER 4
10.4 IS RECORD LOW NTU OPTIMAL PERFORMANCE
EVERY FREAKS OUT AND ACTS LIKE THEY DON’T KNOW HOW TO OPERATE THEM OR THEY ARE ANY DIFFERENT THEY ARE THE SAME IT’S THE SAME WATER CHEMISTRY
THERE MAY BE A DIFFERENT MIXING ENERGY TO THE MIXER BUT ITS ALL GENERALLY VERY MUCH THE SAME HORSEPOWER AND RPM
THIS IS PROBABLY THE MOST CRITICAL SYSTEM WHEN OPERATING AS HARDNESS IS THE LARGEST MASS
THE ISSUE I HAVE WITH OKC PH IS THEY ROUND IT TO THE TENTH WHICH IS VERY CRUDE
THIS GRAPH WOULD LOOK A LOT BETTER AND 10X TIMES MORE CONFIDENT IF THEY WOULD RECORD DATA TO THE 1 HUNDREDTH
ALL OF THE VERTICAL GAPS WOULD BE MORE FILLED AND THE GRAPH ITSELF WOULD LOOK A LOT MORE LIKE WATER
THIS IS A NOVEMBER 2020 DOR DAILY OPERATIONAL REPORT
I FOUND THAT THE AUTHOR WAS KEN BRISCOE WHO OPERATED BEFORE MY TIME
MANY SAID HE WAS A DRUNK
MANY PEOPLE ASSUME THINGS ARE THE WAY THEY ARE BECAUSE SOMEBODY HAD THEM THAT WAY FOR A REASON
THE FIRST DAY I HIRED AT OKC I WANTED TO HAVE A SEIZURE BECAUSE OF THE FORMAT
FORMAT ALONE SHOULD BE A REGULATION BUT THAT ISNT TRUE ART
I JUST ALWAYS CHANGE STUFF AND EVERYBODY FREAKS OUT NOBODY QUESTIONS ANYTHING LIKE I DO
I COULD DO A LOT MORE OF MY JOB ON A LOT LESS PAPER SPACE
MY BIGGEST CONCERN IS REFORMATTING
IM NOT A COMPUTER GOD WHO CAN GRAPH QUICKER WITHOUT REFORMATTING BUT THE WAY I GRAPH IS BASIC AND VERY SIMPLE X VS Y AND THE WAY I GRAPH HAS TO BE IN A PARTICULAR FORMAT
EVEN IF I HAVE GAPS OR SPACES IT MESSES WITH MY GRAPHS
IVE HAD FREE HELP FROM COMPUTER GODS ON MICROSOFT HELP TECH COMMUNITY FOR EXCEL
I ACTUALLY STILL HAVE A QUESTION FOR AUTOMATING MY STOCKS BUT 700 PEOPLE HAVE VIEWED IT AND NO ONE ANSWERS MY QUESTION
I MAY RE ASK THE QUESTION AND DUMB IT DOWN
THEY SAID IN THE PAST A LOT OF COLLEGE KIDS WOULD MESS UP WATER PLANTS TINKERING WITH THINGS
ME I CAN NOT BE MORE STATISTICALLY CONFIDENT I AM NOT OPINIONATED BUT LET THE MATH REPRESENT ITSELF
MY STOCKS ARE THE SAME WAY
WHAT IM SAYING HERE IS OKC NEEDS TO LET ME REFORMAT
THIS IS A MIXING ENERGY %SOLUTION OF THE POLYMER SKID PUMPS FOR THE SLUDGE FACILITY
THEY ARE PROMINENT BRAND PROGRESSIVE CAVITY PUMPS
RECORD LOW OPTIMAL PERFORMANCE ON THE FILTRATE HAPPENS WHEN THESE MIXING ENERGIES RANGE IN THE 0.333 %
I MADE THIS XSHEET FOR THE MANUALLY OPERATED ONES AT DRAPER BUT FORTUNATELY AT HEFNER IT DISPLAYS THEM FOR YOU
MORE OPERATORS NEED TO KNOW TO OPERATE WITHIN THESE TARGETS.
OKC USES A LOT OF INACCURATE RANGES FOR TARGETS THAT ARE NOT CENTERED THEY ARE INACCURATE AND OFFSET
MY TARGETS ARE EXACT FOR EVERY TEMPERATURE WITH MOST GRAPHS IN WATER THAT IS THE LARGEST NEXT SIGNIFICANT VARIABLE THAT CAN SKEW A GRAPH
AGAIN AS MENTIONED BEFORE MANY OF THESE TEMPERATURE GRADIENTS ARE LIKE COCA COLA SINE WAVES THEY MAY NOT BE BIG BUT THEY ARE EXISTENT AND BEING AWARE OF THEM HELPS BEATING RECORD OPERATING COSTS
THIS IS THE HEFNER SLUDGE WETWELL HMI TO TOPERATE THE SYSTEM
JEFF BOLDEN NEVER ANSWERED ME AND JERRY THE UNION REP TOLD ME JEFF BOLDEN CAME OUT EARLY AND WAS AT THE SLUDGE FACILITY AND GOING TO THE WETWELL TO SEE WHAT I WAS TALKING ABOUT DID JEFF EVER STOP BY TO TALK TO ME? NO WHAT A COWARD
THE THREE PICTURES INVOLVE FORMAT
NO ONE WOULD EVER ANSWER ME WHEN I HAD VERY SIMPLE QUESTION TO CHANGE THE AMBIGUITY
I DON’T NEED THE AVERAGE OF THE WETWELL
I DON’T CARE ABOUT THE SETPOINTS THAT CAN BE CHECKED ON SCADA
THE HMI DOES NOT MATCH THE LOGBOOKS
ITS NOT INTUITIVE TO FILL OUT THE LOGBOOK AND SUBJECTIVE OBJECTIVE TO INTERPRETATION
I DON’T CARE ABOUT THE LAG AND LEAD PUMP AND STOP SETPOINTS THAT CAN BE CHECKED FROM SCADA
THE FORCE MAIN FLOW CAN NOT BE VERIFIED WITHOUT GETTING ON A LADDER AND VIEWING THE EQUIPMENT TAGS ON THE MAINS WHICH ISNT SAFE AND IF U HAVE BEEN DOWN THERE IN THE WETWELL YOU WOULD SEE EVEN A 20' LADDER ISNT EVEN THE SAFEST I THINK ITS LIKE A 30 FT LADDER TO GET UP THAT HIGH AND IM NOT EVEN SURE IF THERES ROOM FOR THAT ITS PROBABLY JUST ENOUGH ROOM OR HOW THEY DESIGNED IT
THE SLUDGE PUMP STATIONS PUMPS ON OFF AUTO MANUAL IS STUPID AND ON SCADA
OIL LEVEL IS THE ONLY THING I PHYSICALLY CHECK BEING OUT THERE ROUTINELY
THE SOLIDS WW BYPASS VALVE IS ALSO A SILLY OLD WAY THAT HAS NOTHING TO DO WITH DAY TO DAY OPERATION AND NEEDS ABROGATED
I AM ALL FOR TWO DIFFERENT SETS OF EYES CHECKING THIS ARENA ONCE A DAY AND IT SHOULD BE 2 PEOPLE INSTEAD OF JUST 1 PERSON CHECKING IT TWICE THE CHIEF AT SLUDGE FACILITY NEEDS A REASON TO GET UP AND GO AND GET OUT WALK RIDE BIKE OR DRIVE THE GO CARTS
MOST OF THIS STUFF CAN BE CHECKED ON SCADA AND REALLY KILLS ME EVERYDAY I CAN COME UP WITH MORE IMPORTANT STUFF TO CHECK BUT THIS IS A VERY SMALL SYSTEM WORTHY OF ABOUT 15 MINUTES OF MY TIME DAY TO DAY IN A 12 HR SHIFT
I CAN KEEP GOING ON AND ON ABOUT THIS BUT BASICALLY JOSH FLOWERS MAKES A LOT OF THESE AND IS EXTREMELY SQUARE AND TAKES FOREVER DOING ANYTHING AND I KNOW HE CANT OPERATE A CLARIFIER OR A PRESS
IM LIKE A TRAILBLAZER OR A NASCAR PITCREW I DON’T WANNA DO IT UNLESS IT MAKES A DIFFERENCE
ALSO YOU CANT ACTUALLY KNOW WHICH NORTH OR SOUTH FORCE MAIN IS ON WITH YOUR EYES BY VERUFYING IT WITH SCADA TAGS. AT FACE VALUE ALONE WITH THE SILLY LOGBOOK ITS 5050 CHANCE AND IM NOT PUTTING MY LICENSE ON THAT.
I ALSO USE LESS WORDS TO LABEL MUCH LESS AMBIGUOUSLY
I STARTED WRITIGN ONE DAY ABOUT FORMAT ALONE AND IT TURNED INTO LIKE 20 REQUIREMENTS JUST ON MSFT EXCEL
I KNOW IM A BIG FORMAT NAZI BUT IF I CAN JUSTIFY REASONS FOR IT IN WATER BE IT UNTO ME AS YOU SAY
HERE ARE NEGATIVE VALUES ON THE OCTOBER MONTH FOR AN MOR MEANING THE WATER IS CORROSIVE
IT’S THE FAR RIGHT COLUMN
24044 SATURATION INDEX
CR IS CORROSION RATE
NEGATIVE IS CORROSIVE
I ACTUALLY HAD ZACH BEABER TRY AND TELL ME THAT NEGATIVE IS SCALING. I TOLD HIM NUH UH AND I DOUBLE CHECKED AND I WAS RIGHT BUT ITS IN MY NATURE TO LET A LOT OF THINGS SLIP WITH FOLKS IN GROUPS
WHICH REMINDS ME WHEN JEFF BOLDEN CALLED KERRY SMITH TO INCREASE THE MONOCHLORAMINE RATIO. MEANING MORE CHLORINE AND LESS AMMONIA. I DO NOT RECALL WHAT THE RATIO WAS CURRENTLY AT BUT I WAS VERY SUSPICIOUS OF EAVESDROPPING ON THE CALL. ITS NOT EVEN REALLY EAVESDROPPING BECAUSE OF OUR LICENSES AND THE SPOTS WERE IN ESPECIALLY IF IT INVOLVES TREATMENT. NOW I TOLD KERRY WHO WAS THAT? HE SAID JEFF BOLDEN. HE SAID TO TURN IT UP DUE TO TASTE AND ODOR CALLS. I SAID KERRY U KNOW INCREASING THE MONOCHLORAMINE RATIO CONTRIBUTES TO TASTE AND ODOR ISSUES RIGHT?
KERRY SHOOK HIS HEAD AT ME AND SAID HE WAS JUST TAKING ORDERS
WE HAVE SOPS OR READ AND SIGNS SIGNATURES ON NOT GOING AROUND OUR BOSS AND USING OUR CHAIN OF COMMAND. DOESN’T THIS WORK BOTH WAYS? I DON’T REMEMBER IF JEFF WAS WQS AT THAT TIME OR WHATEVER ELSE HE MOVED UP TO BUT HE WAS MORE THAN 1 2 EVEN 3 BOSSES OVER KERRY. SO I INFORMED / ASKED ZACH BEABER ABOUT IT AND HE REACTED LIKE IT WAS A JUICY THING AND THAT HE WOULD TALK TO PHILLIP ABOUT IT.
WHAT IM SAYING IS DID JEFF BOLDEN INCLUDE PHILLIP WHEN HE MADE DETRIMENTAL DECISIONS AFFECTING THE WATER? LIKE IF I WAS PHILIP THAT WOULD MAKE ME FEEL BAD. SURE IT’S A COMMON EVERYDAY CHANGE BUT I RUN A TIGHT SHIP. MY FAITH IS A LONG LEASH. I LOVE MANAGEMENT SCIENCE. SO MUCH THAT I READ 3 OR 4 BOOKS ON ASSHOLES FROM A PHD BOB SUTTON IN CALI. HE ANSWERED ME FASTER IN AN EMAIL THAN ANY BOSS I HAVE EVER HAD. I HAD SCRIPTURE FOR EVERYONE OF HIS STUDIES AND PUBLISHED RESEARCH.
THIS NEEDS MORE DATA
ITS CLARIFIER 1 AT LAKE HEFNER
THIS IS THE AMOUNT OF MINUTES PEOPLE WAIT TO BLOW DOWN THE SLUDGE VS SETTLEABILITY ON THE SETTLEABILITY TEST
MY RANGES WOULD BE NEARLY 33 TO 133 ISH
NOW THAT I THINK ABOUT IT THERES A CROSSOVER POINT BETWEEN THE LIME PPM AND THE INTERVAL PPM THAT IS VERY CONVENIENT TO USE
I CAN QUANTIFY THAT LATER
I USUALLY USED 66 OR 77 OR 88 MOST OF THE TIME
IT TAKES CLARIFIER DAYS TO RESEED AND GROW THESE CRYSTALS WHICH ALSO AIDS IN TREATMENT
ITS PUBLISHED RESARCH I HAVE ELSEWHERE THAT I SCORED FROM OLD DOCUMENTS IN THE HEFNER CHIEF WATCH TOWER
7 8 OR 9 MLS IS ALSO THE BEST TO HAVE FOR PRODUCING LOW NTU NONTURBID WATER
PEOPLE DON’T AGE THE SLUDGE LONG ENOUGH
SLUDGE AGE IS A COMMON CALCULATION IN WASTEWATER
IT HELPS IN SLUDGE FACILITY AND THE CLARIFIERS
OF COURSE U DON’T WANT TO GO TOO LONG BECAUSE THE SLUDGE WILL PLUG UP THEN AND CREATE WORK TO FLUSH IT
WHICH REMINDS ME OF DRAPER CRAP
I GOT EXTREMELY WELL AT AGING SLUDGE AND KEEPING IT THICK
THIS IS ONE OF THOSE FINE LINES IN WATER TREATMENT THAT IS FUN TO RIDE
MANY OPERATORS JUST ARENT EXPERIENCED ENOUGH IN SLUDGE BLOWDOWNS
I WAS FLUSHING MAINS PROACTIVELY TO KEEP TREATMENT TRAINS RUNNING AND THE SLUDGE FACILITY AT DRAPER BECAUSE OTHER OPERATORS WOULDN’T CATCH THEM
IM PRETTY SURE THE NEW CLARIFIER 4 AT HEFNER IS MORE EFFICIENT IN ITS MIXING ENERGY AND HEFNER OVERMIXES IT
I DON’T REMEMBER IF ITS VFD BUT IT SHOULD BE LIKE THE OTHER CLARIFIERS
THIS GRAPH NEEDS MORE DATA IN THE 5 - 10 RANGE ON THE X AXIS AT THE BOTTOM
WAYYY TOO MUCH DATA ON THE SHORT END OF LOW SETTLEABILITY
I BELIEVE THE CLARIFIER 4 IS SHEARING THE POLYMER OF OVERMIXING
I HAVE DATA ON MIXING ENERGY SETTLEABILITIES WITH CLARIFIER 2 ON ANOTHER FILE
I GOT GOOD AT UNDERSTANDING ITS BEHAVIOR AND HOW DRASTIC THE MIXING ENERGY AFFECTS ITS AMPLITUDE OF THE SETTLEABILITY
I TOOK ADVANTAGE OF THE OPPORTUNITY WHEN THE THING WAS OFFLINE AND IT GAVE GREAT CONFIDENCE TO THE DIMENSION VARIABLE / SPECTRUM
HERE IS THE EMAIL THAT GOT ME FIRED
I DOUBT IT EVEN WENT TO CHRIS BROWNING
STEVE I THINK HIS NAME IS STEVE THE MECHANIC HE MENTIONED IT TO ME BEFORE HOW HE SHOWED SOMEONE HOW TO FILTER OUT EMAILS FROM CERTAIN PEOPLE OR LIKE INTERCEPT THEM.
I DON’T RECALL EXACTLY HOW HE SAID IT BUT IT MADE ME WONDER IF CHRIS BROWNING EVEN READ MY EMAIL. IT SHOULDN’T TAKE 2 OR 3 YEARS TO GET AN ANSWER
ALSO KELLI AND JEFF CALLED ME ALL THE WAY TO DOWN TOWN AND IT WAS JUST TO FEEL OUT MY REACTION BECAUSE THEY NEEDED TO SEE WHO IS DOING ALL THE REPORTING TO THE DEQ AND THE EPA. MY DUMBASS REVEALED AND I SHOULD HAVE ACTED DUMB LIKE WHAT WHAT R U TALKING ABOUT. ALL THEY TOLD ME WAS TO WORK WITH ROB ON ISSUES. LIKE AS OPPOSED TO WHAT? HE HAS LOST ALL CREDIBILITY WITH ME AND ACTS LIKE HE IS ON DRUGS AND DOESNT KNOW THE LAW. AND I THINK HE CAME FROM TEACHING ANYWAYS IDR I ALWAYS WONDER WHAT HE IS DOING IN WATER
JEFF BOLDEN SAID IT HISSELF HE DOESN’T KNOW WATER LAW
THERE IS AN OPTIMIZATION CURVE NEAR THE BOTTOM OF THE GRAPH THAT IS OUR AREA OF INTEREST HERE
NEED MORE DATA
I WAS TRYING TO DEVELOP THIS BUT IM SURE AS I WAS DRAWING / DEVELOPING THE GRAPH PEOPLE CAUGHT ON AND SHUT ME DOWN. I WOULDN’T BE SURPRISED IF 333 ENDED UP BREAKING RECORDS
I DIDN’T LABEL MY GRAPHS ENOUGH BUT I KNOW THAT THIS IS CLARIFIER 1 COLDEST QUARTER OF THE YEAR ML SETTLEABILITY VS INTERVAL. INTERVAL IS THE TIME BETWEEN SLUDGE BLOWDOWNS
AND THE RED ONE FROM BEFORE IS WHEN ITS HOT
THERE IS A FLUSH MECHANISM ON SOME OF THE CLARIFIERS TO HELP WITH KEEPING THE SLUDGE FROM CLOGGINF
IT NEEDS TO BE IN SECONDS INSTEAD OF MINUTES
I WAS SURPRISED 1 MINUTE WAS ANY BETTER THAN COMPLETELY OFF ZERO 0
SOME OF THE FLUSH GOES BACK TO THE CLARIFIER
THERE IS A POOF OF SLUDGE WHEN THIS HAPPENS
I HAVE QUANTIFIED IT WITH FLUX CURVES
THERE ARE FLUX CURVES IN STATE POINT ANALYSIS FROM HI TECH CALCULATORS ONLINE TO ENSURE YOU ARE OPERATING UNDERNEATH THE FLUX CURVES
THEY ARE TOO COMPLICATED AND I PREFER A ROUGHER QUICKER CUT WITH 2 OR 3 DIMENSIONS OF VARIABLE
I CAN STABILIZE THE WATER WITHOUT LOOKING AT ANY GRAPHS
THIS IS A YEAR OF CLARIFIER CONE AND EFFLUENT RANGES
THIS DOES RESEMBLE A COCA COLA SINE WAVE BUT ITS TOO DEVIANT
THIS GRAPH 1ST OF ALL NEEDS THE 1/100TH VALUE OF PH NOT TENTHS FOR BETTER RESOULTION
NEXT IT NEEDS TO ONLY RANGE OR BE TARGETED NEAR 10.33 HOT 10.44 AVERAGE 17*C 10.55 COLD
THEY SAMPLE THE CONE AS OFTEN AS THE EFFLUENT BUT ITS MORE DEVIANT AND DOESN’T MATTER
IF IT WERE MYWAY ID SAMPLE THE CONE TWICE LESS OFTEN AND JUST GRAB THE EFFLUENT AS IT’S THE PRODUCT AND LESS DEVIANT
I RAN A WHOLE YEAR OF AVERAGES AND STANDARD DEVIATIONS
I OWE THIS CREDIT DUE TO LUCAS BERRY HE IS A GREAT LAB OPERATOR HE CAME FROM THE ENV LAB TO THE EAST AT HEFNER
THERE IS AN ENV LAB ON THE EAST SIDE OF HEFNER
I ALWAYS WANTED THE ENVIRONMENTAL CHEMIST JOB BECAUSE THEY HAVE DEGREES BUT I WASTED 7 YEARS DOING THIS SILLY WATER PLANT CRAP
THERE WERE LIKE ONLY EVER 4 JOBS THAT CALL FOR A DEGREE WITH OKC
BACK WHEN WE COULD SEARCH THE JOB DESCRIPTIONS NOW THEYRE HIDING IT WHICH SHOULD BE MORE PUBLICLY ACCESSIBLE FOR LEGAL RIGHTS
I BELIEVE THEY ARE OBSCURING OR MIGRATING A LOT OF TECH
THEY SAY THEYRE MAKING ALL THESE CHANGES BUT THEYRE HIDING THE TECH
ROB MILLER SAID IM LESS IMPORTANT THAN BILL SCHOSSER TO MY FACE
HE SAYS THIS INFO IM SEEKING FOR FEDERAL WATER LAW ISNT MY BUSINESS
IM THE MOST QUALIFIED OPERATOR AND THEY PROMOTED BILL SCHOSSER BEFORE ME
THEY HIRED A MOMMAS BOY WHOS MOM WAS RETIRED RIGHT BEFORE HE PROMOTED TO ENGINEERING TECHNICIAN WHICH I HAVE A DEGREE IN
THEY SAID THEY HIRED SOMEONE MORE QUALIFIED
THAT’S A LIE
WALKER BOOTH ISNT MORE QUALIFIED THAN ME TO BE AN ENGINEER TECH
HE CAME FROM RENTAL CARS AT THE AIRPORT AND I HAVE A DEGREE IN ENGINEERING THAT’S ILLEGAL PURSUANT TO OK 475 1 & 2 & 20
PHILLIP DID RESPOND TO ME AND IT WAS VERY INFORMATIVE AND QUITE LENGTHY
BUT THIS IS AS FAR AS HE WENT WIH ME AND CLAIMED EVERYTHING I QUESTION IS NON NEGOTIABLE
IT DIDN’T TAKE ME BUT LIKE MY OWN CURIOSITY AND EXPERIMENTING IN A DAY TO CRACK THE CODE TO THE BALANCE TANK
THEN THAT’S WHEN I REALIZED THEY DESIGNED IT WRONG
IDK IF THE ENGINEER FIRM CP&Y RAN A CFD ON IT OR IF THEY CANT GO WIDER ON IT AND LESS TALLER BUT ITS UNDUE STRESS ON THE PUMPS TO GO OVER THE ELEVATION OF THE GRAVITY THICKENER
I USUALLY PICK RED WHEN I MAKE DATA HOT FOR MY WATER GRAPHS
THIS IS THE HOT TEMPS AND WHEN I SAMPLE HOT OR COLD TEMPS I USUALLY DO 3 MONTHS MAYBE 4 I DON’T REMEMBER
OF COURSE I SHOULD HAVE MADE MY GRAPHS BETTER BUT I WAS CRANKING OUT A LOT OF INFO WHILE I WAS THERE AND I KINDA LIKE TO TRANSCRIBE A BIT TO OBSCURE MY WORK
RECORD OPTIMAL PERFORMANCE IS NEARLY AT 8 OR 9 MLS HERE
FOR PRODUCING LOW TURBIDITY WATER
CLARIFIER 1
OH THOSE ARE THE MONTHS
JULY AUGUST SEPTEMBER MONTHS OF 2020
THIS IS THE CO2 RECARBONATED WATER SAMPLE
IT’S A LITTLE NOISY TO TELL WHERE IS OPTIMAL BUT I KNOW FROM CHEMISTRY ON THE STABILITY THAT A HIGHER PH HERE WOULD HELP BEST BECAUSE WE WANT THE WATER TO BE STABLE AND NOT CORROSIVE
I THINK THEY HAVE IT SET TO 9.11 BUT ID SET IT TO 9.22
AGAIN THIS GRAPH COULD BE 10X TIMES BETTER IF THEY WOULDN’T ROUND THE DANG PH WHICH IS ILLEGAL
I KNOW IT TAKES UP MORE PAPER SPACE BUT I FORMAT WELL ENOUGH I KNOW WHAT SPACE TO USE AND WHAT NOT
THIS MAY BE MORE OF A COLD TEMP ALSO ITS BETTER TO SEE A WHOL EYEAR OF THE DATA I THINK I WAS JUST PEEKING AT IT
THE DEQ ALSO HIRED COMPUTER PROGRAMMERS FOR THEIR WATER DEPARTMENT I FORGET THE JOB TITLE BUT IT WAS VERY SUSPICIOUS BEING NEAR THE END OF MY TIME WITH OKC
THIS MAY BE A HOT TEMP GRAPH BUT I DO RECALL 10.46 BEING RECORD OPTIMAL PH FOR THE CLARIFIERS
HOPE IM NOT REPEATING MYSELF
IM ALMOST FINISHED WITH THE GRAPHS BUT I KNOW THAT THESE ARE JUST A TASTE OF MANY MORETHAT I HAVE VIEWED AND GRAPHED
IWHEN I DECODE A SYSTEM I VIEW EVERY GRAPH I GRAPH EVERY VARIABLE VS EVERY VARIABLE
COMBINATION N CHOOSE K
1 OUT OF 10 = 10 GRAPHS
2 OUT OF 10 = 45 GRAPHS
3 OUT OF 10 = 120
4 OUT OF 10 IS 210
5 OUT OF 10 = 252
6 OUT OF 10 = 210
7 OUT OF 10 = 45
8 OUT OF 10 = 120
9 OUT OF 10 = 10
CUMULATIVE SUM OF GRAPHS = 10 + 45 + 120 + 210 + 252 + 210 + 120 + 45 + +10 = 1022 GRAPHS
5 MINUTES IS A PRETTY LENGHTY BLOWDOWN BUT IF MORE PEOPLE WOULD AGE THEIR SLUDGE IT WOULD BE MORE PRACTICAL
MOST PEOPLE BLOWODN TOO LITTLE AND TOO FREQUENTLY
THEY NEED LARGER INTERVALS AND LONGER DURATIONS
THERES 2 LONG ARMS TO THE RAKE ON THE CLARIFIER
IT TAKES 15 MINUTES TO TURN LIKE 180 DEGREE
ITS 2 REPS PER HOUR I THINK
THERE I A POOF OF SLUDGE BEHIND THE RAKE TRAILING ALL THE TIME
AND THERE IS ANOTHER POOF OF SLUDGE AFTER THE FLUSH AFTER A BLOWDOWN
WHATS AMAZING ABOUT THIS IS THAT ABOUT THE SAME FRACTION OF TIME ITS NATURAL TO GET A HIGH PEAK OF THE FLUX CURVE.
IT PAYS AS AN OPERATOR TO KNOW WHEN THESE EVENTS OCCUR SO U SAMPLE THEM WHEN THEY ARE CLEANER
THIS IS THE FLUX CURVE OF THE POOF OR THE CLOUD OF SLUDGE UNDERWATER
IT’S THE MINUTES PER HOUR WHICH IS DURATION DIVIDED BY INTERVAL FOR MPH
AND THE ML IS THE SETTLEABILITY
THIS HELPS UNDERSTAND WHICH MLS PRODUCE THE HIGHEST AMOUNT OF SLUDGE IN THE COLD IN THE 5 - 9 RANGE
IT IS HARD TO GET ANY SETTLEABILITY IN THE COLD ALSO
THIS CURVE IS BEST REPRESENTED WITH STATE POINT ANALYSIS BUT I HAVE SIMPLIFIED IT WITH 3 DIMENSIONS
STATE POINT ANALYSIS
THE POOF
THE CLOUD OF SLUDGE
THE FLUFF
THIS ONE ISNT VERY BOLD OR CONTRASTED ENOUGH TO SEE SORRY FOR THE LOW RESOLUTION
BUT THIS IS A GREAT SPREAD OF THE NUMBERS TRIED FOR INTERVALS AND DURATION
CLEARLY NO ONE GOES ABOVE 60 BUT ME AND THERE ISNT ENOUGH DATA OR RESOLUTION HERE TO ILLUSTRATE MORE CONFIDENCE
THERE NEEDS TO BE MORE ABOVE 60 ON THE Y AXIS AND MORE AROUND 5 ON THE X AXIS
IF SOMEONE NEEDS A 10 OR 15 MINUTE BLOWDOWN THEY ARE LOST
10.33 PH WHEN ITS HOT USES LESS CHEMICAL
NEED BETTER RESOLUTION AND DATA
CLARIFIER 1 EFFLUENT NTU
THESE ARE THE MLS VS THE TEMPERATURE
ITS JUST LESS SETTLEABILITY WHEN ITS COLD
THERES A LOT MORE FLUFF TO THE SLUDGE WHEN ITS HOT
I MAY HAVE ALREADY SHARED THIS OR IT COULD BE WHEN ITS COLD
IT’S THE IMPORTANT APPLICABLE GRAPHS THAT I SAVE AS IMAGES
I DIDN’T REALIZE HOW MUCH QUALITY IS LOST WHEN CONVERTING
FOR FUTURE REFERENCE I WILL FORMAT BETTER
CLARIFIER 1 HOT NTU EFFLUENT OPTIMAL PH 10.5
NEED MORE DATA AND BETTER RESOLUTION
COLD SLUDGE SETTLEABILITY = ~ 5 6 OR 7 ISH
IM REMINDED OF HOW MANY SYSTEMS HAVE FARRR TOO MUCH DATA
ONLINE PROCESS ANALYZERS CAN BE USED IN LIEU OF MANUALLY SAMPLING
THE TAP PH IN THE HEFNER LAB EVERY FREAKING HOUR IS RETARDED
WE ONLY LEGALLY HAVE TO GRAB IT LIKE TWICE A DAY
AND WE CAN WRITE IT DOWN FROM THE SCADA IT CAN BE AUTOMATED FROM SCADA
WE DON’T NEED THE MOST SPACE WASTED ON THE DOR TO GET UP EVERY FREAKING HOUR TO RUN THE SILLY TEST
I HAVE LOTS OF OTHER PAPERS AND THINGS THAT CAN COME TO MIND BUT IM HAPPY ENOUGH WITH WHAT IVE COVERED
IM SURE ILL KEEP LEARNING AND REPEATING MYSELF BUT I ACTUALLY REALLY ENJOYED GOING THRU ALL THIS AGAIN AND HAVE REALLY ENJOYED MY TIME DOING IT
I HATE THAT ITS AN UNDERTAKING TO DO IT BUT AGAIN WHEN I DO THIS STUFF THERE IS NO TIME TO ME BECAUSE I ENJOY DOING IT
I THINK AS A YOUNG NATURAL ARTIST GROWING UP IM NATURALLY GIFTED AT STORING IMAGES IN MY HEAD AND KNOWING HOW THINGS BEHAVE BECAUSE OF WHERE THEY’VE BEEN WHERE THEY ARE AND WHERE THEYRE GOING
JESUS IS MORE IMPORTANT THAN WATER
SOME PEOPLE ASK IF WATER IS GOD
THIS PIC IS MY OWN PUBLISHED RESEARCH DRAWING FROM VARIOUS SOURCES ABOUT THE STANDARDIZATION OF WATER AND IS ALSO STILL A WORK OF PROGRESS
IF I COULD HAVE MY OWN A-TEAM IT WOULD BE DAN PALMER & MAX SANDERS
PROBABLY EVERY INSTRUCTOR AT ROSE STATE
PEJA SINDJIC NEEDS PROMOTED AND HAS MANAGEMENT EXPERIENCE
PATRICK RYAN OSBORNE IS GOOD WITH AUTOMATION
MAYBE KIEL VAUGHN I WOULDN’T DOUBT HIM IM JUST THINKING
I MIGHT SAY CHANSE WELCH BECAUSE HE BROUGHT ME TOGETHER WITH MANAGEMENT TO TELL THEM WHAT IM ALWAYS TALKING ABOUT
CHANSE MOVED UP WAY TOO FAST ALSO SO ITS NOT FAIR BUT IT MAKES SENSE
OH ALSO HONORABLE MENTION JAROD JOHNSON COX BUT I NEVER WORKED WITH PPL SPOKE WELL OF HIM
AND ERIC BALL BECAUSE HE IS A MECHANIC BUT NEEDS TO OPERATE I THINK HES AUTISTIC BUT IDK HE WAS WEARING AN AUTISTIC SHIRT
JOEY TUCKER AND BRIAN MAIRET WERE FUN COWORKERS
DENNIS PHILLIPS WAS THE WORSE 2 -3 YRS OF MY LIFE
MIDDLETON MAKES GOOD ICE CREAM AT DRAPER
A LOT OF PEOPLE AT DRAPER WOULDN’T BE SO BAD IF THEY WOULD JUST GET RID OF DENNIS
DENNIS PHILLIPS IS A WHOLE NOTHER FILE
SONNEY MASSEY IS GOOD HE JUST SAYS TO KEEP THE WATER WET
MANY PEOPLE CALLED JIM CRAWFORD CRAWDAD CAUSE HES ALWAYS CRAWDADDING AWAY FROM EVERYBODY
MASOUD AND PAOLA ARE ALSO FUN I LIKE WORKING WITH THEM
THESE ARE THE RANKS AND POSITIONS
I KNEW ONE DAY WHEN I AID THEY EITHER NEED TO CUT HALF THE BULLCRAP OR HIRE MORE PEOPLE THEYD RATHER HIRE MORE PEOPLE
AND THEY DID
IM PRETTY SURE THEY RECORD AUDIO IN PLACES AT THE PLANT
I HAVE EVERY MOR ON FILE FROM 1960
MONTHLY OPERATIONAL REPORT
WHAT I NEED TO SIMPLIFY IS EACH CHEMICAL COST IN PPM AND THE OPERATING RANGES WITH ANNUALIZED RATES OF COST
THIS WAY PEOPLE WILL UNDERSTAND HOW 33 PPM OF LIME CAN COST A DIFFERENCE OF ABOUT 350K A YEAR
I THINK ITS ABOUT 30K EVERY PART PER MILLION
OPERATORS ARE TURNING IT UP OR DOWN LIKE 30 OR 40 PPM A DAY
I CAN LOWER ALL THE CHEMICAL COSTS WITH GRAPHS ALONE
AND I CAN LOWER CHEMICAL COSTS EVEN FURTHER WITH OPTIMIZED PERCENT SOLUTIONS
I ALSO MUST SAY I HAVE 7GB OF WATER ON FILE IN 7 YEARS
I ALSO HAVE 9GB OF WATER ON MUSIC ALONE
ILL PROOFREAD THIS A BIT AGAIN AND CONSIDER IT POLISHED OFF
I ALSO HAVE A WATER HEATER THAT I HAVE TO FLUSH AND IT HIGHLY RESEMBLES THE GRIT AT THE SLUDGE FACILITY I HAVE PRECONDITIONED IT WITH 100 MESH PRE SED FILTER AND SILIPHOS PROPRIETARY TRADEMARK CHEMICAL
THE SILIPHOS IS SLOW DISSOLVING PHOSPHATE WITH SILICA
THIS IS 100 SAMPLES I FETCHED IMMEDIATELY WHEN I GOT TO THE HEFNER SLUDGE FACILITY SO THAT I COULD GET A QUICK IDEA OF HOW ITS SYSTEM IS BEHAVING. ITS 100 ROWS OF ABOUT MAYBE 9 VARIABLES. THIS ISNT NEARLY ALL OF THE GRAPHS I MAKE AT ALL BUT ITS FUN TO SHOW IN ONE PAGE HOW MANY OF THE SCATTER PLOTS ARE LIKE SHOTGUN SHOTS.
IT WAS 3 - 7 MLS OF VARYING SETTLEABILITY ON THE OFFLINE CLARIFIER 2
FROM 40 % TO 50%
THIS IS QUITE IMPRESSIVE TO ME HOW ONLY A 10% MARGIN CAN CHANGE SO MUCH OF THE SETTLEABILITY
I COULD REALLY GET INTO LOWERING CHEMICAL COSTS EVEN FURTHER BY ADDING MORE MIXING ENERGY TO IT.
THIS IS EFFECTIVE FOR UNDERSTANDING HOW MANY MLS OF SETTLEABILITY YOU CAN GET OUT OF A CLARIFIER BEFORE TURNING ANOTHER ONE ON OR OFF
THE FASTER THE WATER FLOWS IN THE MORE IT MIXES AND THE HIGHER THE SETTLEABILITY
IVE USED THIS FOR REFERENCE FOR BOSSES WHO DIDN’T KNOW WHEN TO TURN ONE ON OR OFF
TO ME HERE YOU WANT TO TAKE A CLARIFIER TO ABOUT 20 MGD BEFORE TURNING ON ANOTHER
MAYBE EVEN 22 OR SO. I CAN TREAT WATER UP TO 25 OR EVEN 30 ON A CLARIFIER THE EASIEST OTHER PEOPLE DON’T LIKE DOING IT BUT I KNOW EXACTLY WHERE IM AT
WHEN IT WAS HOT I WAS BORED ENOUGH IN THE LAB TO ILLUSTRATE FLUX CURVES OF THE SETTLEABILITY TEST
THIS IS ALSO WHAT MANY OF THE SCATTER PLOTS REPRESENT IN SHAPE
THE SETTLEABILITY IS LIKE THE BIG CLOUD OF SLUDGE SETTLING IN THE CLARIFIER
ITS LIKE SLUDGE GETTING MIXED UP AND THEN SETTLING
AND THE RAKE SCRAPES IT TO THE MIDDLE TO THE BOTTOM
FOUND THIS EXTRA FILE
ITS ABOUT 6 MONTHS OF CHEMICAL TRUCKS
WE SHOULD ONLY GET ABOUT 2 TRUCKS A DAY AT WASTEFUL SPENDING OPERATING
WHEN MARTIN AND BEABER PUT ME IN THE LAB BECAUSE CHERYL HUTCHINSON WAS BEING AN ANNOYING BITCH THEY SLAMMED WITH LIKE 13 CHEMICAL TRUCKS IN ABOUT 34 HOURS WHICH IS WHAT LIKE WERE SUPPOSED TO HAVE 4.04 IN 2 DAYS OR 2.89 IN 34 HRS
BUT I HAD 13 IN 34 HOURS
UNFAIR WORKLOAD IS ILLEGAL
THAT’S THAT’S 449% ANOMOLY OFF THE CHART INDICATING HUMAN BIAS
I CAN SAMPLE THE DEVIATIONS NOW TO FURTHER PROVE IT ANOTHER DIMENSION BUT IM MOVING ON TO THIS HUGE CHEMICAL COST FILE FROM 1960
GONNA TRY TO PUT IT AS AN ANNUAL BASIS OF EVERY PPM OF CHEMICAL WASTED ITS LIKE 10,000 FOR LIME OR SOMETHING. SO IF THEYRE OFF 33PPM ITS LIKE 330K A YEAR. ROUGH ESTIMATE
IVE BEEN A LITTLE DEVIANT ON THE CHEMICAL ESTIMATES SINCE 1960 BUT ITS HUGE AND NOW IM GOING TO POLISH OFF THAT FILE AFTER BEING FIRED 26 MONTHS AGO
1/25/25
THE LEFT GRAPH IS WEEKDAYS