PROCESS FOR THE DESTRUCTION OF BIOLOGICAL WASTE PRODUCTS

Abstract: Biological waste products are destroyed in a process comprising heating said products in a sealed chamber (1) and passing the output stream of the chamber (1) to a bath (3) of molten aluminum.

Description: This invention relates to a process and a device for the destruction of bilogical waste products. Human and veterinary hospitals, surgical clinics, patho­ logy laboratories and associated health care facilities throughout the world are routinely removing and dispos­ ing of tissues and body fluids from sick, injured and frequently infected humans and animals. In addition, large volumes of contaminated syringes, tubes, surgical bandages and blood products enter the waste streams of these institutions. In many cases, these materials are harmless and pose no threat of infection to persons who handle or who are otherwise exposed to them. In some ca­ ses, however, these materials can contain infective viruses, pathogenic bacteria, toxins and/or bacterial spores which constitute a threat of patients, health care professionals and the general public. In many cases, hos­ pital and clinical waste carries with it a noxious odor and may be considered unsightly. In addition to the above-mentioned facilities, there are numerous university and medical school facilities in which research into the etiology of disease, experimental thera­ peutics and basic reasearch is conducted. Fermentation broths and tissue cultures, as well as experimental animals, may frequently contain higher concentrations of rare and pathogenic organisms and toxic and carcino­ genic chemical agents than would be found in hospital and clinical wastes. Agricultural research facilities frequently produce mosses, ferns and fungi which repro­ duce through sporulation and which may be either patho­ genic or allergenic. Recent advances in genetic engineering enable the pro­ duction of potent pharmaceuticals, toxins, and other biochemicals in large fermentation cultures. Once the desired chemical products have been isolated from the broth, the broth must be properly treated to control both odor and the possibility that potentially infectious agents and toxins may be released into the environment. The disposal of small amounts of infectious laboratory wastes, bandages and similar contaminated materials has, since the invention of the Chamberland autoclave in 1884, been performed using wet steam. Wet steam is effective against most bacteria and mycotoxins, but is frequently ineffective against spores, toxins and the so-called "slow" viruses. Steam sterilization is extremely energy intensive; must be monitored regularly for effectiveness, usually produces an odiferous product, and results in no dimunu­ tion in the size of the waste. The autoclaving of whole research animals and large volumes of tissue is rarely practiced, except in extreme emergencies. Chemical treatment of pathological waste has never achieved routine use. Chemical treatment of tissues requires the handling of comparatively large volumes of corrosive and toxic chemicals, such as chloride of lime and formal­ dehyde. The end result is an increased volume of a ste­ rile, albeit chemically hazardous, waste. The incineration of whole bodies, parts thereof and tissues has been a routine procedure at medical facilities, morgues, mortuaries and veterinary hospitals. Incineration involves minimum transportation within and especially outside of the institution, produces a small volume of essentially sterile waste, and is comparatively energy efficient. The use of small, pathological incinerators for the disposal of laboratory wastes and patient contact items is limited by the design of a pathological incinerator, which is ty­ pically a small solid hearth, single chamber unit. The incineration of significant volumes of plastic laboratory items such as petri dishes and syringes results in the emmission of large quantities of black smoke, and the BTU content of these items frequently causes dramatic changes in combustion chamber temperatures. The incorporation of tissue and infectious waste into the general waste stream of an institution has been attempted at several large me­ dical institutions, but entails the installation of new and complex incinerators and the hiring of additional, qualified operators, and is frequently beyond the finan­ cial capabilities of small and medium sized hospitals. Keeping this in account it is the problem of the invention to provide a process and a device capable of destroying pathogenic organisms, spores and viruses, as well as the tissues and laboratory equipment in which they are con­ tained, which process and device are capable of signifi­ cantly reducing the volume of waste while producing gaseous and particulate emissions of low toxicity or which are easily trapped or otherwise contained. The device should be amenable to production in sizes suit­ able for installation in facilities zoned for light industry and require minimum operator training and ser­ vice. Finally, the cost of construction and operation must be competitive with other, less efficient, methods of disposal. For solving the problem the process according the present invention comprises the steps of: a) heating said waste products in a sealed chamber, to vaporize volatile materials and pyrolyze non-volatiles, thereby producing an output stream comprising gas with residual biological matter entrained therein; b) passing said output stream into a bath of molten alu­ minum. The device according the present invention for carrying out the process indicated above contains a closed and heated chamber preferably in the form of a vessel in a gas-tight encasement, a second vessel containing an alu­ minum bath and communicating with the chamber by a deli­ very tube which runs from the top of the chamber to a point near the bottom of the aluminum bath. With the features according the present invention it is possible pyrolytically and chemically detoxifying and destroying all toxic and infectious bilogical waste products e.g. human or animal tissues, biological fluids such as blood, and bandages, cultures and combustible laboratory apparatus containing infectious bacteria, bacterial spores, toxins and viruses, as well as pharma­ ceuticals and other trace chemicals which may be inclu­ ded therein. The aluminum metal bath provides a long residence time for a secondary thermal treatment of the pyrolysis gases, as well as a chemically reactive medium which reduces residual physiologiclly active waste as well as organic compounds of physiological origin, typical pharmaceuti­ cals, and metal-based tissue strains to hydrogen, hydro­ carbons, carbon, nitrogen, etc.. The gaseous byproducts from the molten aluminum treatment do not require filtra­ tion or scrubbing such as that which would normally be required for the effluents from single and multiple cham­ ber incinerators and can, when containing economic amounts of combustible gases, e. g. hydrogen and hydrocarbons, be used for combustion, e. g. to provide heat energy. As indicated above, heating of the waste products herein in closed chamber means is carried out to vaporize vola­ tile materials and to pyrolyze residual organic non-vola­ tiles. The gas produced in the initial vaporization carries with it some solid and/or liquid biological material and is routed under pressure generated by the vaporization of the volatile materials into the bath of molten aluminum where the entrained solid and/or liquid biological mate­ rial is reduced by the molten aluminum and is thus de­ stroyed, along with the volatile components of the stream. As heating in the closed chamber means continues, non-­ volatiles are pyrolyzed. The resulting off-gases, which can have bilogical wastes entrained therein are routed to the molten aluminum bath where said biological wastes are reduced by the molten aluminum and destroyed. When further heating results in no further vaporization the vapors remaining in the pyrolysis chamber may be swept into the molten aluminum by means of a stream of nitrogen or other inert gas. Turning now in more detail to the heating step, the most volatile components in the waste being treated, e. g. chemicals used in treating pathological specimens such as ethyl alcohol and toluene, are flashed off. As heating continues and the temperature in the waste which is be­ ing treated increases, proteins coagulate and water vapor is formed from ruptured cells, saline solution and the fluids attendant to tissue specimens. Fats, oils and other organic compounds which are not watersoluble are steam distilled during this initial heating. On further heating, collagen proteins and any included higher molecular weight compounds and other non-volatile materials begin to de­ compose until the decomposition products become volatile. At the conclusion of the heating step, the residue remain­ ing in the pyrolysis chamber consists primarily of carbon and metal salts, from tissues and from the decomposition of bone. When they are present with the tissue, cellulosic materials and as bandages and plastics decompose and volatilize at the appropriate temperatures. Water-soluble organic compounds such as pharmaceuticals, stains, and compounds being screened in such processes as the Ames test of toxicological feeding tests are either volatilized at low temperatures or degraded at higher temperatures, thereby becoming volatile. Viruses and enzymes,which are proteinaceous in character, are normally denatured as the temperature in the pyrolysis chamber increases. Protein­ aceous materials within tissues, however, can be protected by the char of the tissue surrounding the protein and can remain viable as they pass out of the pyrolysis chamber in small particles entrained in the gases. Bacterial spores, which are particularly heat resistant, are likewise able under some circumstances, to exit the chamber in this way. It has been discovered herein that physiologically active materials and organic compounds in gases from the heating, i. e. pyrolysis, chamber can be effectively treated by passage into molten aluminum. The invention described here­ in provides a method for treating pyrolysis gases at high temperatures under reducing conditions as well as modifi­ cations necessary to a pyrolysis chamber to make secondary treatment efficient and controllable. The pyrolysis products of human and animal tissue, fermen­ tation broths, bacterial cells, viruses, spores and toxins are further decomposed when bubbled through the bath of molten aluminum. The decomposed products react with the hot aluminum metal and are reduced ot low molecular weight hydrocarbons, hydrogen, nitrogen, etc. Since all biologi­ cal materials which can be volatilized in a pyrolysis chamber are composed, almost exclusively, of oxygen, carbon, hydrogen, nitrogen, sulfur, phosphorus and, on occasion, halogens, the resultant byproducts of the reaction with the alumi­ num are limited in number and character, regardless of the biological nature of the feed. For example, in addi­ tion to the gaseous reaction products set forth above, other products can inlcude aluminum oxide and sulfide and on occasion carbides, nitrides, phosphides or phos­ phorus. Because the reactions are carried out unter re­ ducing conditions no water or carbon dioxide is formed or exhausted. Effluent from the aluminum treatment can-be vented to the atmosphere. In such case it is preferred to flare the com­ bustible materials. In some cases, the effluent is pre­ ferably treated being vented to the atmosphere. It is preferred to recover the heating values from the combu­ stible gases and in such case the combustible gases are routed to a burner for this purpose. The following is a description of a preferred working and operation example with respect to the drawing. Herein fig. 1 schematically illustrates a system for carrying out the process herein. The system includes a normally closed chamber means in the form of a heating pyrolysis retort or chamber 1 which is a refractory-lined vessel enclosed in a gas-tight, preferably steel, encasement 2. Waste material to be treated is fed into the chamber 1 bathwise through a door or chute (not depicted) which is preferably fitted with gasketed doors or other means to prevent or minimize the entry of air. A second gasketed door (not depicted) is preferably fitted just above the level of the hearth for removal of ashes. The chamber 1 can be heated by any con­ ventional underfiring technique or, in the rpeferred em­ bodiment, electrically. The chamber 1 is equipped with a valved line 5. The chamber 1 communicates with a re­ fractorylined vessel 8 containing an aluminum bath 3 having an upper surface 7 via a delivery tube 4 which receives exhaust from the top of the chamber 1 and vents to a point near the bottom of the aluminum bath 3. The tube 4 is rea­ dily made from a refractory material, although high tempe­ rature metal alloys are also satisfactory. An exhaust stack 9 emanates from the head space 10 above the molten aluminum, and may discharge directly to the out-of-doors, through a treatment system as require to meet local emissions re­ gulations. In the preferred embodiment, the exhaust in­ cludes a flash arrester, The valved inlet 5 is provided to admit air or nitrogen and may be fitted with a vacuum release device to prevent backsyphoning. In operation, the waste material is introduced into cham­ ber 1 and the molten aluminum bath 3 is brought up to operating temperature. Temperatues for the molten alu­ minum can range from its melting point to its boiling point, i.e. from 660°C to 2450°C, and are selected not only to provide reduction, but also to provide decompo­ sition of thermally resistant and low reactivity materials. Since the maximum operating temperature in the secondary chamber or commercially available incinerators is appro­ ximately 1400°C, it can be seen that the molten aluminum bath is capable of provifing as much or more heat than is available in the traditional processes. When the aluminum in vessel 8 has reached its operating temperature, heat is applied to chamber 1 to raise the temperture in it to range from 600°C to 850°C, prefer­ ably from 800°C to 825°C. As the temperature in chamber 1 rises, vaporization and pyrolysis occur and the expansion and volatilization force vapor and materials entrained in it to leave chamber 1 by the tube 4 and ultimately pass into the molten aluminum bath 3, wherein reduction and secondary thermal treatment occurs and the treated mate­ rials are converted to innocuous compounds. Transfer of gases, vapors and solids from chamber 1 to bath 3 is pre­ ferably assisted by the introduction of nitrogen or other inert gas at line 5. When the pyrolysis process is completed, the entry port can be reopened and the chamber 1 recharged. Alternative­ ly, when all of the waste amterial has been destroyed, the heat may be turned off and the valve in line 5 opened to prevent back-syphoning as the chamber cools. It is ad­ vantageous to introduce nitrogen instead of room air into the chamber during cool-down to prevent flaring of any unburned material on the hearth and to provide an oxygen deficient atmosphere when the chamber is recharged. The operation of this process in different mechanical configurations is apparent to those skilled in the art. The following examples illustrate the practice of the in­ vention without limitation thereof. Example I A young rat weighing 205 grams is humanely sacrificed and placed in an 8 quart cast iron pot. The pot is sealed with a cast iron lid fitted with a copper wire gasket and secured by clamps. A transfer tube constructed of ¼ inch ID SS316 tubing connects the pot to a Dixon graphite cucible (size 16), approximately one-half filled with molten aluminum. A stainless steel exhaust tube fitted through a cover directs the gases from the head space above the aluminum to a glass cold finger trap immersed in a dry ice/actone bath. The cast iron pyrolysis chamber is heated by two Meker burners. The crucible is heated by a gas flame in al melting furnace. The pyrolysis cham­ ber is raised to a temperture of 600°C - 650°C as measured by a thermister and the molten aluminum is maintained in the liquid state throughout. After 30 minutes, the heat is turned off and the lid removed from the pot. After an additional 15 minutes, the cold finger trap is removed and the condensate is quantitativel y removed to a tared glass vessel and weighted. The liquid is then analyzed for total organic carbon (TOC); less than 2 parts per million TOC is found. Example II Using the apparatus as described in Example I, three plastic petri dishes containing cultures of Bacillus stearothermophilis are introduced into the pyrolysis chamber and the temperature raised to a surface tempera­ ture reading of 800°C. The cold finger trap is replaced by a Matsson-Garvin slit to agar sampler timed to complete one revolution in 60 Minutes. At the completion of the cycle, the agar plate from the slit to agar sample is covered and removed to an incubator. After 72 hours at 37°C, no growth is seen on the plate. Example III Five grams of α-naphthylamine (a suspected carcinogen) is placed on 3 agar filled petri dishes containing a Salmonella culture to simulate an Ames test and intro­ duced into the pyrolysis chamber, as described in Example II. The slit to agar sampler is replaced by a glass T-tube with a serum cap on one end. During the treatment, 100 micro liter aliquots are removed via a gas-tight syringe at 15 minute intervals. The aliquote are injected into a gas chromatograph fitted with a flame ionization detector. Substantially no bacteria or α-naphthylamine is detected; acetylene is present at less than 50 parts per million. The ash in the pyrolysis chamber is collected, slurried in a minimal amount of carbon disulfide, filtered, con­ centrated by bubbling nitrogen gas through the carbon di­ sulfide in a test tube and analyzed by gas chromatography. Substantially no bacteria or α-naphthylamine is detectable in the extract. Example IV A plastic 3 mil. thick bag with a volume of 1 quart is half-filled with cotton bandages and a cotton hand towel. Ten 1 cc plastic Tuberculin syringes are filled from a fermentation broth containing approximately 5x10⁴ spores (B. subtilis) per litre, their contents injected into the bandages, and the syringe dropped into the bag. An addi­ tional 10 cc of broth is carefully poured onto the banda­ ges and towel and the bag is tied with a wire utilizing apparatus as described in Example II. The bag is intro­ duced into the iron pot and the destruction process is performed with sampling as described in Example II. After three experiments the plates from the slit to agar samples average fewer than 1 colony per plate. The contents of the pot, after cooling, are washed out with 100 ml of sterile water, filtered through coarse cloth, streaked on Tripti­ case Soy agar plates and incubated at 37°C for 72 hours. The plates from the extraction of the ash contain 5-10 colonies per plate. While the foregoing describes perferred embodiments, modi­ fications within the scope of the invention will be evi­ dent to those skilled in the art. Thus, the scope of the invention is intended to be defined by the claims.

Claims: 1. A process for the destruction of bilogical waste products comprising the steps of a) heating said waste products in a sealed chamber (1) to vaporize colatiles and to pyrolyze non-­ volatiles and producing an output stream compri­ sing gas with residual biological matter entrai­ ned therein, b) passing said output stream into a bath (3) of molten aluminum. 2. A process as claimed in claim 1 wherein the waste products comprise tissue from a mammal and/or bio­ logical fluids and/or infectious bacteria or their spores and/or carcinogenic agents. 3. A process as claimed in claim 1 wherein the reactions are carried out under reducing conditiones. 4. A process as claimed in claim 1 wherein to recover the heating values from the combustible gases said gases are preferably routed a burner. 5. A process as claimed in claim 1 wherein the sealed chamber (1) is heated to a range from 600°C to 850°C. 6. A process as claimed in claim 1 wherein transfer of gases, vapors and solids from the chamber (1) to bath (3) is assisted by introduction of inert gas, prefer­ ably nitrogen, to the chamber (1). 7. Device for carrying out the process as claimed in any of the forgoing claims characterized by a closed and heated chamber (1) preferably in the form of a vessel in a gas-tight encasement (2), a second vessel (8) containing an aluminum bath (3) and communicating with the chamber (1) by a delivery tube (4) which runs from the top of the chamber (1) to a point near the bottom of the aluminum bath (3). 8. A device as claimed in claim 7whereby the chamber (1) has a feeding door or chute and is fitted preferably with gasketed door or doors for prevent or minimize the entry of air and/or removal of ashes. 9. A device as claimed in claim 7 whereby the chamber (1) is heated electrically. 10. A device as claimed in claim 7 whereby an exhaust stack (9) emanates from a head space (10) above the bath (3), preferably including a flash arrestor.

Inventors: SHULTZ, CLIFFORD G.
Applicants: SHULTZ, CLIFFORD G.
Application year: 1986
Main classification: B09B3
IPC codes: C10J3, C10B49, C10B53