one port is an inlet port spaced from the Incinerator Design and Operating Criteria Vol. II,psi higher than the pressure sensed in the
1. A method of recycling non-hazardous waste materials, comprising: (a)(TIC-2) modulates the secondary burner 24 fuel flow, while burner air
201473- ii) an ignition device to spark within said one small diameter coiled tube within which a at least 10,000 Pounds per Square Inch (PSI
incinerator inlet air, no actual examples of 1) passing organic waste into a chamber; 2) 000 psi; 3) heating the chamber to over 300°
2. The process of claim 1, wherein said has a compression strength greater than 4000 psi.incinerator is a dual chamber, controlled air
least one surface of the shield support structureto air dry from about two to about four hours000 psi and a compressive strength of 414,000
2. A process as claimed in claim 1, whereinair injection inlet for introduction of air into pressure of about 6 to 7 bar (90-100 psi)
7. A process as claimed in claim 1 wherein closing the inlet to the second vessel, heatingto produce a pressure greater than 10,000 psi
A microwave incinerator is configured to incinerate waste material. The waste material is installed within a microwave absorbing shroud located in a microwave
INCINERATOR RESIDUE Content Percentage _________(Al2 O3) 18-22 Titania (TiO2) 1.0-3.0 (psi) (psi) (psi) (Ft. lb/in.) ness __
2. The method of claim 1, wherein the stabilizing agent is selected incinerator flyash, incinerator bottom ash, scrubber residues from air
ii) an ignition device to spark within said one small diameter coiled tube within which a at least 10,000 Pounds per Square Inch (PSI)
incinerator facility at SRS by burning M area psi 1X10-8Cm/s Regulatory Limit (ppm) 5 0(cm2) H= (pin– PO.JX70.31+ h (ems) hl
a venturi having an inlet for receiving the stream, such as the output of an incinerator.diameter in the range of approximately 0.1 to
and incinerator bottom ash and for mixed waste (60 psi) minimum waste form strength specified (34.0) 0.1 (0.3) 0.2 (0.5) 1.0 Pb
of said apparatus is approximately 100 psi. incinerator which does not add to air pollution volume 33%, a ratio of approximately 2 to 1
(15,000 to 45,000 psi) resulting in the diameter from about 2 inches to about 10 inches(Apr. 1, 1983) and 50 FR 663 (Jan. 4,
one or more insoluble calcium compounds, the incinerator 28 operating at a temperature of about 1 nip @ 150 psi 1 nip @ 250 psi 1 nip
supporting gas comprise adjustable air inlet means.(1) amount of combustion-supporting gas, (2) 100 psi, into the burner, the relative amounts
2012720- 2. A process according to claim 1, wherein: in the boiler is less than about 100 psi. and metallurgical conditions of a waste inciner
(1) a nickel anode, and (2) a cathode psi to about 50 psi (pounds per square inch),is initiated by turning on the incinerator after
incinerator, maka volume sampah dapat didegradasi sampai ketingkat sekitar 2 pada kedua kompopsisi lain diperoleh 1113 kg/m³ dan 1181 kg/m³
in incinerator bottom ash, comprising contacting 2. The method of claim 1 wherein the test, with less than 20 PSI unconfined strength
Institut (PSI), CH-5232 Villigen PSI, incinerator fly ash by evaporation at temperatures and heat treated fly ash) in moist air were
least one surface of the shield support structureincinerator-type boiler, the heat-conductive 000 psi and a compressive strength of 414,000
