Liquid Effluent Decontamination and Carcass Disposal for Biocontainment Facilities

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Liquid Effluent Decontamination and Carcass Disposal for Biocontainment Facilities 2011 ABSA Annual Scientific Symposium November 2, 2011 Anaheim, California Presented by: Joe Wilson

Today s word is: Perspective Responsibility

Conventional Wisdom Drives High Temperature Batch EDS Selection

Leadership in Energy and Environmental Design LED Are we taking this seriously? If we don t then who will? In Bio-Containment Facility EDS Specification we re not seeing it!

Effluent Decontamination Systems Now is the time for us to think outside the Box!!

Killing pathogens / select agents in an EDS is easy An EDS is not an Autoclave! Planning treatment parameters around autoclave parameters could be old school thinking! An EDS is a wet system with a homogeneous environment; an ideal physical environment for rapidly killing pathogens

Let s Take A Closer Look at Some Other Options Continuous Flow with Energy Recovery Thermo- Chemical Chemical

The Basic Batch Chemical EDS

Chemical EDS Options Continuous Chemical!! Chemical Batch

Chemical EDS Sterilization; ------ CAN BE FAST!!

Case Challenge 1: A Southeast Asia Vaccine Test Facility They desired an EDS to replace their current effluent disposition system They hired a consultant of our choice to evaluate their situation and the report came back 3,500 lpd wastewater 240 lpd of it is swine manure (high solids, high organic loading) Potable water is not potable enough for a steam boiler (in fact it has high turbidity and solids present in the water) They have little money to operate a system They vaccinate animals that they subsequently infect with virulent disease agents to test the vaccines

The Dilemma The Piping The Slaughterhouse

Could there be an EDS for this situation? Batch Chemical EDS was the only option they could consider when all factors were understood. Here is where they want to put it!! Level 3? lab Piggery Where the effluent goes

Case Challenge 2: Modular BSL-3 labs were ordered and in the final phases of construction, but there was no EDS Budgets were constrained The customer wanted the peace of mind afforded by an EDS Time was of the essence Technical resources were virtually non-existant

The Challenges Develop an EDS for modular BSL-3 laboratory wastewater with the following attributes: Affordable to acquire Easy to service by locals; no PLC or Computer Robust and Reliable To be located outdoors (in one case with indoor monitoring capability) Compatible with a variety of corrosive chemicals Uses minimum energy and no additional water Could operate on unstable power Would use reagents that are readily available

We Knew Just as there is a need for modular container based laboratories worldwide, so would there be a need for a simple EDS solution That cost would always be an issue and without affordability they would do without the system That this could be done effectively with chemicals

An Answer!! 18

Why consider thermochemical? How about unreliable steam supply for starters? How about energy reduction? How about flexibility? Georgia State University University of Nebraska

What is the next big change in EDS? Continuous flow with energy recovery and solids handling capabilities shows great promise Uses 1/10 of the energy as thermal batch systems Can attain temperatures over 150 degrees C (can sterilize in a 2 minute hold cycle) Can be designed for high solids loads Cost effective in comparison to batch systems Requires much smaller utilities (steam supply) Not all continuous flow EDS systems are equal; just as not all incinerators are equal so be very careful to select vendors with the correct experience. We have driven this technology to an advanced point; and will now be pushing it into the marketplace. Goodbye Pressure Vessels!!!!

Continuous Flow EDS Options A large redundant 150 degree C system with regeneration A large redundant 100 degree C system with regeneration

Materials of Construction Material Condition System Cost 316-L Stainless SAF 2205 Duplex Thermal, Low Chlorides (<5 mg/l) $$$ Thermal, Low Chlorides (<100 mg/l) $$$$ SAF 2507 Duplex AL6XN Super Austenitic Thermal, Medium Chlorides (<250 mg/l) Thermal, High Chlorides, 20 plus year life (<10,000 mg/l) $$$$$$$ $$$$$$$$$!!!! Hastelloy C22 Super Austenitic Teflon Lined Stainless 22 Thermal, High Chlorides, 25 plus year life (<10,000 mg/l) Thermal, Very High Chlorides, 30 plus year life (>250 mg/l) Plastic Chemical, Very High Chlorides, 25 year life plus (any chloride concentration) $$$$$$$$$$$$$ $!!!!!!!! $$$$$$$$ $

Carcass Disposal Systems

The Carcass Disposal Challenge

Alkaline Hydrolysis Systems The first commercially installed alkaline hydrolysis system was for human cadaver digestion, and was put into service in 1995 and is still in use today! Built by the fathers of the modern tissue digester, WR 2 Founders Dr. Gordon I. Kaye (above L) and Dr. Peter B. Weber (above R) Owned and operated by: State of Florida Anatomical Gifts Program Location: Shands Hospital, University of Florida, Gainesville, Florida

Carcass Disposal Technology Options Inside the Containment Barrier Options: Alkaline Hydrolysis (Carcass Digester) Rendering (Cooking / Drying with or without alkali) Autoclaving Outside the Containment Barrier Options: Incineration (Starved Air, Pyrolisis, Gasification, etc.) Alkaline Hydrolysis (Carcass Digester) Bulk or Rotary Autoclaving Rendering

Visual Progression of Alkaline Hydrolysis A low temperature digester allows us to view the progression of the alkaline hydrolysis digestion process. Animals loaded (L) and with dry alkali added (R) Solbulization / Hydrolysis Hydrolysis / Saponification Advancing Hydrolysis Hydrolysis Complete

Alkaline Hydrolysis Process Complete!! Residue Safe!!

Effluent from Alkaline Hydrolysis Pounds of Animals Processed Undiluted Effluent Volume in Gallons 10 3 100 30 1000 300 10,000 3,000 Essential Effluent Characteristics BOD~100,000 mg/l COD~160,000 mg/l ph ~12 With CO 2, ph <9 TSS<10,000 mg/l

Effluent from Alkaline Hydrolysis Effluent from Alkaline Hydrolysis is a homogeneous true solution that varies from Yellow and thin (poultry) to light brown and thin (wild animals) to dark brown and thick (sheep) the effluent can vary but the smell of strong ammonia is the same and the other essential properties (BOD/COD, dissolved solids, nitrates, etc. are very similar)

MW in kda Can a low temperature Tissue Digester destroy Prion infectivity? Below, results from a MALDI-TOF analysis show that throughout the digestion process, the largest peptides recovered from the effluent never exceeded 2.8 kda, well below the smallest size of a Prion. Prion Range Average human protein (40 kda) PrP C, PrP Sc (30-36 kda) PrP 27-30 (27-30 kda) Miniprion PrP106 a synthetic construct of 106 amino acids used in laboratory testing to express some of the neurodegenerative effects of prions NOTE: BioLiquidator fragments are MUCH smaller than even this synthesized 12 kda fragment. Smallest human protein (5.5 kda) Largest BioLiquidator fragment (2.8 kda) Low Temperature Digester Range

Ohio Department of Ag Large Digester 7-28-05 WR 2 Tissue Digester Ohio Department of Agriculture, Animal Disease Diagnostic Lab Reynoldsburg, Ohio, U.S.A.

Ohio Ag Necropsy Facility

Carcasses and a Large Gut Bucket

Large Carcasses Handled by Hoist

All Carcasses Loaded Now for the Gut Bucket

Digester Fully Loaded

Digestion Complete; a Clean Process!

A Typical Laboratory Size Digester System shown, up to 50 kg (110 pounds) per cycle 39

Interfacing with the Barrier 3 1 2 1. Digester in barrier, autoclave bones out 2. Digester with glove box 3. Top of Digester in barrier 4. Digester in barrier, pass bones out side 5. Digester outside barrier with barrier interface 4 5 40

Jeff Edwards Makes History! The first commercially sold and operated funeral disposition system in the world; Edwards Funeral Home, Columbus, Ohio February, 2011 10% of the carbon footprint of cremation 5% of the energy and resource waste as burial Patent Pending

Innovation: Digester Technology for Facilities with Limited Height

Bringing the Animal from Necropsy In the Barrier 1 Hoist by local contractors (the higher the better) 3.26 meters Ceiling height 1.26 meters Load Height both sides 300 cm 220 cm (patent pending)

Loading the Animal(s) In the Barrier 2

Closing the unit In the Barrier 3

Tipping the unit In the Barrier 4

Fill, heat, digest And the mixer seals are above water at all times; pump seals are the Achilles of alkaline hydrolysis systems In the Barrier 5 Water level is variable, based on tissue weight Propeller agitation is dramatic and focuses on the bottom edge of the basket

Drain and rinse In the Barrier 6 At the end of the cycle the bones are directly impacted by the very close propeller agitation for a complete finish.

Final spray rinse In the Barrier 7 Final spray yields clean, cool end product, a clean basket, and very little if any remaining odor.

Removing the bones In the Barrier 8 Rake it out and ready to go again!

Something New!! Up to 400 Pound Capacity, low temperature High level nonsegregated cycle Patent Pending

Hey Joe!! We give up! Enough is Enough!!! Thank You!

www.bioresponsesolutions.com Contact: Joseph H. Wilson Cell: 317.432.3626 Office: 317.892.5200 Skype: jhwilson1 Plant: Bio-Response Solutions, Inc. 1298 E. US Hwy 136, Suite A Pittsboro, IN 46167 Email: info@bioresponsesolutions.com