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:
\n2.\u00a0\u00a0 \u00a0 Be paired with secondary burner\/s burning gas or low sulphur liquid gas or some other suitable fuel. <\/p>\n
3.\u00a0\u00a0 \u00a0 Ensure secondary air supply is controlled efficiently.
\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
\n2.\u00a0\u00a0 \u00a0 If the minimum combustion temperatures aren’t maintained.
\nSecondary Combustion Chamber.
\n4.\u00a0\u00a0 \u00a0 The incinerator should not be overcharged.
\nSulphur dioxide\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 S02 <\/p>\n
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
\nA gas flow meter\/recorder
\nAcid Gas Scrubbers
\n3.\u00a0\u00a0 \u00a0 Have light if 24hrs operation
\n2.\u00a0\u00a0 \u00a0 Have a solid floor.
\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
\nParticulate Scrubbers
\n2. \u00a0\u00a0 \u00a0 Staff must be provided with proper protective equipment such as, gas mask, aprons, gumboots, helmets, goggles, gloves. <\/p>\n
3. \u00a0\u00a0 \u00a0 Caution and Warning signs must be provided.
\nNickel\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 Ni
\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
\n21 – OM <\/p>\n
Where:\u00a0\u00a0 \u00a0Es\u00a0\u00a0 \u00a0= Calculated emission concentration at the standard percentage oxygen concentration
\nWhere: Win = mass feed rate of the POHC from the waste stream fed to incinerator, and
\n3.\u00a0\u00a0 \u00a0 The inclusion 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 rate should be 10 m\/s and at least two times the surrounding wind speed (Efflux velocity = wind speed x 2) whichever is higher to ensure no down washing of leaving 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 interior wall temperature rather than burner flame temperature has to be provided for both primary and secondary chambers. <\/p>\n
2.\u00a0\u00a0 \u00a0 An audible and visible alarm must be installed to warn the operator when the secondary temperature drops to below the required temperature. <\/p>\n
3.\u00a0\u00a0 \u00a0 Besides the above the following instruments may also be required.
\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 The secondary chamber\u00a0 gas residence time shall be at least 1 (one) second at 1050 \u00b1 50o C, with 3% Oxygen in the stack gas. <\/p>\n
4\u00a0\u00a0 \u00a0Opacity of the smoke must not exceed 20% Viewed from 50 meters with naked eyes
\nOs\u00a0\u00a0 \u00a0= Regular oxygen concentration
\n 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 account. <\/p>\n
2.\u00a0\u00a0 \u00a0 If possible the chimney should be visible to the operator from the feeding area.
\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 is registered for the particular sort 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.
\n5.\u00a0\u00a0 \u00a0 Ensure residence time isn’t less than two (2) seconds.
\n3.\u00a0\u00a0 \u00a0 Whenever the previous charge has not been fully combusted in the case of batch feeding. <\/p>\n
4.\u00a0\u00a0 \u00a0 Until such time as the inclusion of more waste won’t cause the layout parameters of the incinerator to be exceeded. <\/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.
\n5. \u00a0\u00a0 \u00a0 There should be no smoking or eating on the website. <\/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
\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
\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 computed as: <\/p>\n
Es = \u00a0\u00a0 \u00a021 — Os\u00a0\u00a0\u00a0 x EM
\n6.\u00a0\u00a0 \u00a0 Ensure the gas temperature as measured against the inner wall in the secondary chamber & not in the fire zone, is less than 1100oC. Verify the oxygen content of the emitted gases is less than 11%.
\n3.\u00a0\u00a0 \u00a0 The incinerator has to be preheated to working temperature before charging any waste.
\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
\n2\u00a0\u00a0 \u00a0Feeding And Charging\u00a0\u00a0 \u00a0Controlled hygienic, mechanical or automatic feeding methods must be used which won’t affect the air temperature in the primary and secondary chambers of the incinerator negatively. <\/p>\n
No waste is to be fed to the incinerator: <\/p>\n
1.\u00a0\u00a0 \u00a0 Until the minimum temperatures have been reached.\n<\/p>\n
1\u00a0\u00a0 \u00a0Fundamental Plant Design\u00a0\u00a0 \u00a0An approved plant has to have four different sections that demonstrate three principles of Turbulence, Residence Time and Temperature are inbuilt in the plant layout .The regulated sections may include but not limited to: <\/p>\n
Overall plant layout.
\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
\n4. \u00a0\u00a0 \u00a0 Fire fighting equipment must be provided
\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
\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
\nElectrostatic precipitators
\n5.\u00a0\u00a0 \u00a0 All the emission to the air other than steam or water vapour has to be odourless and free of mist, fume and droplets. <\/p>\n
6.\u00a0\u00a0 \u00a0 The Authority may require that 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 flame contact with gases is achieved.
\nThe Combustion efficiency is computed as follows; <\/p>\n
C.E=% CO2\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0 x 100
\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
\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
\n8.\u00a0\u00a0 \u00a0 Ensure both main and the combustion temperatures are maintained until all waste was fully combusted <\/p>\n
5\u00a0\u00a0 \u00a0Particulate Removers\u00a0\u00a0 \u00a0A mechanical particulate collector has to be incorporated after secondary combustion chamber for removal of particulate pollutants entrained in the flue gas stream. The particulate collectors may include any of the following or a combination thereof: <\/p>\n
Cyclone separator
\n2.\u00a0\u00a0 \u00a0 Be equipped with a burner\/s burning gas\/fuel or low sulphur liquid fuels. Other combustion methods will be judged on merits. <\/p>\n
3.\u00a0\u00a0 \u00a0 Ensure main air supply is controlled economically
\n5.\u00a0\u00a0 \u00a0 The incinerator must be in good working order at all times and should not be used if any component fails. Any malfunction should be recorded in a log book and reported to the appropriate authority. <\/p>\n
6.\u00a0\u00a0 \u00a0 The incinerator operator and all appropriate staff must be trained to the satisfaction of the appropriate control authority. <\/p>\n
11\u00a0\u00a0 \u00a0Housekeeping\u00a0\u00a0 \u00a0The website where the incinerator is built must: <\/p>\n
1.\u00a0\u00a0 \u00a0 Have running water.
\nAny other instrument 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 applicable local municipal authority planning scheme, the topography of the Region and be compatible with assumptions in the area, <\/p>\n
2.\u00a0\u00a0 \u00a0 Must be placed in a suitably ventilated room. Combustion efficiency: <\/p>\n
Combustion efficiency (CE) shall be at least 99.00%<\/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":"
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. Note: 2.\u00a0\u00a0 \u00a0 Be paired with secondary burner\/s burning gas or low sulphur liquid gas or some other suitable fuel. 3.\u00a0\u00a0 \u00a0 Ensure secondary air supply […]<\/p>\n","protected":false},"author":1,"featured_media":2011,"comment_status":"closed","ping_status":"closed","sticky":false,"template":"","format":"standard","meta":{"_joinchat":[]},"categories":[6],"tags":[22],"aioseo_notices":[],"_links":{"self":[{"href":"https:\/\/3w.haiwo.net\/en\/wp-json\/wp\/v2\/posts\/3040"}],"collection":[{"href":"https:\/\/3w.haiwo.net\/en\/wp-json\/wp\/v2\/posts"}],"about":[{"href":"https:\/\/3w.haiwo.net\/en\/wp-json\/wp\/v2\/types\/post"}],"author":[{"embeddable":true,"href":"https:\/\/3w.haiwo.net\/en\/wp-json\/wp\/v2\/users\/1"}],"replies":[{"embeddable":true,"href":"https:\/\/3w.haiwo.net\/en\/wp-json\/wp\/v2\/comments?post=3040"}],"version-history":[{"count":0,"href":"https:\/\/3w.haiwo.net\/en\/wp-json\/wp\/v2\/posts\/3040\/revisions"}],"wp:featuredmedia":[{"embeddable":true,"href":"https:\/\/3w.haiwo.net\/en\/wp-json\/"}],"wp:attachment":[{"href":"https:\/\/3w.haiwo.net\/en\/wp-json\/wp\/v2\/media?parent=3040"}],"wp:term":[{"taxonomy":"category","embeddable":true,"href":"https:\/\/3w.haiwo.net\/en\/wp-json\/wp\/v2\/categories?post=3040"},{"taxonomy":"post_tag","embeddable":true,"href":"https:\/\/3w.haiwo.net\/en\/wp-json\/wp\/v2\/tags?post=3040"}],"curies":[{"name":"wp","href":"https:\/\/api.w.org\/{rel}","templated":true}]}}