7.\u00a0\u00a0 \u00a0 A 99.99% destruction and removal efficiency (DRE) for each principal organic hazardous constituent (POHC) in the waste feed where: <\/p>\n
DRE = [(Win – Wout)\/Win]*100
\n5. \u00a0\u00a0 \u00a0 There should be no drinking or smoking on the site. <\/p>\n
C.E=% CO2\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0 x 100
\nAny other device or measurement that may be considered necessary <\/p>\n
8\u00a0\u00a0 \u00a0Location \/ Siting\u00a0\u00a0 \u00a01.\u00a0\u00a0 \u00a0 Must be sited in accordance with the relevant local municipal authority planning scheme, the topography of the area and be compatible with assumptions in the area, <\/p>\n
2.\u00a0\u00a0 \u00a0 Has to be placed in a suitably ventilated room.
\n6.\u00a0\u00a0 \u00a0 Ensure the gas temperature as measured against the inner wall at the secondary chamber & not in the flame zone, is less than 1100oC. <\/p>\n
7.\u00a0\u00a0 \u00a0 Verify the oxygen content of the emitted gases is less than 11%.
\nSilver\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0 Ag
\n4.\u00a0\u00a0 \u00a0 Have fly ash containerization and storage prior to disposal. <\/p>\n
12\u00a0\u00a0 \u00a0Health & Safety (Protective Gear)\u00a0\u00a0 \u00a01.\u00a0\u00a0 \u00a0 Staff managing waste must be well trained on safe handling of hazardous wastes
\n5.\u00a0\u00a0 \u00a0 All the emission to the air apart from steam or water vapour must be odourless and free of mist, fume and droplets. <\/p>\n
6.\u00a0\u00a0 \u00a0 The Authority may require the certificate holder have tests carried out by an accredited institution to determine stack and\/or ground level concentrations of the following substances. <\/p>\n
Cadmium and compounds as\u00a0\u00a0\u00a0\u00a0 Cd
\n4.\u00a0\u00a0 \u00a0 Ensure minimal exit temperature is not less than 850oC <\/p>\n
4\u00a0\u00a0 \u00a0Secondary Combustion Chamber (Afterburner).\u00a0\u00a0 \u00a0 The secondary combustion chamber must: <\/p>\n
1.\u00a0\u00a0 \u00a0
\nA gas flow meter\/recorder
\nParticulate Scrubbers
\nHydrofluoric acid\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0 HF
\nAcid Gas Scrubbers
\nArsenic\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0 As
\n8.\u00a0\u00a0 \u00a0 Ensure both main and the combustion temperatures are maintained until all waste was completely combusted <\/p>\n
5\u00a0\u00a0 \u00a0Particulate Removers\u00a0\u00a0 \u00a0A mechanical particulate collector must be integrated after secondary combustion chamber for removal of particulate pollutants entrained in the flue gas flow. The particulate collectors may include any of the following or a combination thereof: <\/p>\n
Cyclone separator
\nAntimony\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0 Sb\n<\/p>\n
1\u00a0\u00a0 \u00a0Fundamental Plant Design\u00a0\u00a0 \u00a0An approved plant must have four distinct sections that demonstrate three fundamentals of Turbulence, Residence Time and Temperature are inbuilt in the plant design .The regulated segments may include but not limited to: <\/p>\n
Overall plant design.
\nHydrochloric\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0 HCL
\n3.\u00a0\u00a0 \u00a0 The addition of dilution air after combustion to be able to reach the requirement of these guidelines is unacceptable. <\/p>\n
4.\u00a0\u00a0 \u00a0 The minimum exit velocity should be 10 m\/s and at least two times the surrounding wind speed (Efflux velocity = wind speed x 2) whichever is greater to make sure no down washing of exiting gases. <\/p>\n
5.\u00a0\u00a0 \u00a0 Point for the measurement of emissions shall be provided. <\/p>\n
7\u00a0\u00a0 \u00a0Instrumentation\u00a0\u00a0 \u00a0Instrument for discovering the inside wall temperature and not burner flame temperature must be given for both primary and secondary chambers. An audible and visible alarm must be set up to warn the operator once the secondary temperature drops to below the required temperature. In addition to the above the following instruments may also be required.
\n2.\u00a0\u00a0 \u00a0 Be paired with secondary burner\/s burning gas or low sulphur liquid fuel or some other suitable fuel.
\nManganese\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0 Mn
\nFabric filters
\nOs\u00a0\u00a0 \u00a0= Regular oxygen concentration
\n4. \u00a0\u00a0 \u00a0 Fire fighting equipment must be provided
\nBarium\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0 Ba
\nTin\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0 Sn
\nVanadium\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0 V
\nElectrostatic precipitators
\nBeryllium\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0 Be
\n2. \u00a0\u00a0 \u00a0 Staff must be provided with proper protective equipment such as, gas mask, aprons, gumboots, helmets, gloves, goggles. <\/p>\n
3. \u00a0\u00a0 \u00a0 Caution and Warning signs must be provided.
\n2.\u00a0\u00a0 \u00a0 If the minimum combustion temperatures aren’t maintained.
\n2\u00a0\u00a0 \u00a0Feeding And Charging\u00a0\u00a0 \u00a0Controlled hygienic, mechanical or automatic feeding methods must be used which will not affect the air temperature in the primary and secondary chambers of the incinerator negatively. <\/p>\n
No waste is to be fed into the incinerator: <\/p>\n
1.\u00a0\u00a0 \u00a0 Until the minimum temperatures have been reached.
\n21 – OM <\/p>\n
Where:\u00a0\u00a0 \u00a0Es\u00a0\u00a0 \u00a0= Calculated emission concentration at the standard percentage oxygen concentration
\n5.\u00a0\u00a0 \u00a0 Ensure residence time isn’t less than two (2) minutes.
\nLead\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0 Pb
\n2.\u00a0\u00a0 \u00a0 Be equipped with a burner\/s burning gas\/fuel or low sulphur liquid fuels. Ensure main air supply is controlled economically
\nThallium\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0 Tl <\/p>\n
Chromium\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0 Cr
\n3.\u00a0\u00a0 \u00a0 The incinerator must be preheated to working temperature before charging any waste.
\nFeed chamber\/ charging
\nA solid particulate meter\/recorder
\n5.\u00a0\u00a0 \u00a0 The incinerator must be in good working order at all times and must not be used if any part fails. Any malfunction should be recorded in a log book and reported to the relevant authority. <\/p>\n
6.\u00a0\u00a0 \u00a0 The incinerator operator and all relevant personnel must be trained to the satisfaction of the relevant control authority. <\/p>\n
11\u00a0\u00a0 \u00a0Housekeeping\u00a0\u00a0 \u00a0The site where the incinerator is built must: <\/p>\n
1.\u00a0\u00a0 \u00a0 Have running water.
\n% CO2 + CO <\/p>\n
2.\u00a0\u00a0 \u00a0 The temperature of the primary chamber shall be 800 \u00b1 50o C <\/p>\n
3.\u00a0\u00a0 \u00a0 <\/p>\n
4\u00a0\u00a0 \u00a0Opacity of the smoke must not exceed 20% Viewed from 50 meters with naked eyes
\nA carbon monoxide and\/or oxygen meter\/recorder
\nWout = mass emission rate of POHC in the stack prior to the release to the air. <\/p>\n
8.\u00a0\u00a0 \u00a0 The average dioxin and furan concentration in the emissions should not exceed 80ng\/m3 total dioxins and furans if measured for a period of 6 to 16 hours. <\/p>\n
Note:
\nA smoke density meter\/recorder
\n6\u00a0\u00a0 \u00a0Chimney \/ Stack\u00a0\u00a0 \u00a01.\u00a0\u00a0 \u00a0 The chimney should have a minimum height of 10 meters above ground level and clear the maximum point of the building by not less than 3 meters for all roofs. The topography and height of adjacent buildings within 50 meters radius should be taken into consideration. If possible the chimney needs to be visible to the operator from the feeding area.
\n3.\u00a0\u00a0 \u00a0 Whenever the preceding charge hasn’t been completely combusted in the case of batch feeding. <\/p>\n
4.\u00a0\u00a0 \u00a0 Until such time as the addition of more waste will not cause the design parameters of the incinerator to be surpassed. <\/p>\n
3\u00a0\u00a0 \u00a0Main Combustion Chamber\u00a0\u00a0 \u00a0The main combustion chamber must: <\/p>\n
1.\u00a0\u00a0 \u00a0 Be accepted as the main combustion zone.
\nCopper\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0 Cu
\nAll pollutant concentrations have to be expressed at Oo C and 1.013 x 10 5 N\/m2, dry gas and 11% oxygen correction. <\/p>\n
Oxygen correction is calculated as: <\/p>\n
Es = \u00a0\u00a0 \u00a021 — Os\u00a0\u00a0\u00a0 x EM
\nCobalt\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0 Co
\nWhere: Win = mass feed rate of the POHC in the waste stream fed to incinerator, and
\nOM\u00a0\u00a0 \u00a0= measured oxygen concentration <\/p>\n
10\u00a0\u00a0 \u00a0Operation\u00a0\u00a0 \u00a01.\u00a0\u00a0 \u00a0 Materials destined for incineration should be of known origin and makeup and have to be just incinerated in a furnace that’s registered for the particular type of waste. <\/p>\n
2.\u00a0\u00a0 \u00a0 A record must be kept of the quantity, type and origin of the waste to be incinerated.<\/p>\n
10\u00a0\u00a0 \u00a0Operation\u00a0\u00a0 \u00a01.\u00a0\u00a0 \u00a0Materials destined for incineration should be of known origin and composition and must be only incinerated in a furnace that is registered for the particular type of waste.<\/p>\n
2.\u00a0\u00a0 \u00a0A record must be kept of the quantity, type and origin of the waste to be incinerated.
\n3.\u00a0\u00a0 \u00a0The incinerator must be preheated to working temperature before charging any waste.
\n4.\u00a0\u00a0 \u00a0The incinerator must not be overcharged.
\n5.\u00a0\u00a0 \u00a0The incinerator must be in good working order at all times and must not be used if any component fails. Any malfunction should be recorded in a log book and reported to the relevant authority.<\/p>\n
6.\u00a0\u00a0 \u00a0The incinerator operator and all relevant staff must be trained to the satisfaction of the relevant control authority.<\/p>\n
11\u00a0\u00a0 \u00a0Housekeeping\u00a0\u00a0 \u00a0The site where the incinerator is built must:<\/p>\n
1.\u00a0\u00a0 \u00a0Have running water.
\n2.\u00a0\u00a0 \u00a0Have a solid floor.
\n3.\u00a0\u00a0 \u00a0 Have lighting if 24hrs operation
\n4.\u00a0\u00a0 \u00a0Have fly ash containerization and storage before disposal.<\/p>\n
12\u00a0\u00a0 \u00a0Health & Safety (Protective Gear)\u00a0\u00a0 \u00a01.\u00a0\u00a0 \u00a0Staff handling waste must be well trained on safe handling of hazardous wastes
\n2. \u00a0\u00a0 \u00a0Staff must be provided with appropriate\u00a0 protective gear such as, gas mask, aprons, gumboots, helmets, gloves, goggles.<\/p>\n
3. \u00a0\u00a0 \u00a0Caution and Warning signs must be provided.
\n4. \u00a0\u00a0 \u00a0Fire fighting equipment must be provided
\n5. \u00a0\u00a0 \u00a0There should be no smoking or eating on the site.<\/p>\n","protected":false},"excerpt":{"rendered":"
7.\u00a0\u00a0 \u00a0 A 99.99% destruction and removal efficiency (DRE) for each principal organic hazardous constituent (POHC) in the waste feed where: DRE = [(Win – Wout)\/Win]*100 5. \u00a0\u00a0 […]<\/p>\n","protected":false},"author":1,"featured_media":2010,"comment_status":"closed","ping_status":"closed","sticky":false,"template":"","format":"standard","meta":{"footnotes":""},"categories":[1],"tags":[],"_links":{"self":[{"href":"https:\/\/gofullday.com\/incineration\/wp-json\/wp\/v2\/posts\/5025"}],"collection":[{"href":"https:\/\/gofullday.com\/incineration\/wp-json\/wp\/v2\/posts"}],"about":[{"href":"https:\/\/gofullday.com\/incineration\/wp-json\/wp\/v2\/types\/post"}],"author":[{"embeddable":true,"href":"https:\/\/gofullday.com\/incineration\/wp-json\/wp\/v2\/users\/1"}],"replies":[{"embeddable":true,"href":"https:\/\/gofullday.com\/incineration\/wp-json\/wp\/v2\/comments?post=5025"}],"version-history":[{"count":1,"href":"https:\/\/gofullday.com\/incineration\/wp-json\/wp\/v2\/posts\/5025\/revisions"}],"predecessor-version":[{"id":10159,"href":"https:\/\/gofullday.com\/incineration\/wp-json\/wp\/v2\/posts\/5025\/revisions\/10159"}],"wp:featuredmedia":[{"embeddable":true,"href":"https:\/\/gofullday.com\/incineration\/wp-json\/wp\/v2\/media\/2010"}],"wp:attachment":[{"href":"https:\/\/gofullday.com\/incineration\/wp-json\/wp\/v2\/media?parent=5025"}],"wp:term":[{"taxonomy":"category","embeddable":true,"href":"https:\/\/gofullday.com\/incineration\/wp-json\/wp\/v2\/categories?post=5025"},{"taxonomy":"post_tag","embeddable":true,"href":"https:\/\/gofullday.com\/incineration\/wp-json\/wp\/v2\/tags?post=5025"}],"curies":[{"name":"wp","href":"https:\/\/api.w.org\/{rel}","templated":true}]}}