{"id":6695,"date":"2023-11-11T06:32:13","date_gmt":"2023-11-11T06:32:13","guid":{"rendered":"https:\/\/www.hiclover.com\/?p=6695"},"modified":"2023-11-11T06:32:13","modified_gmt":"2023-11-11T06:32:13","slug":"small-capacity-incinerators-3","status":"publish","type":"post","link":"https:\/\/gofullday.com\/incineration\/small-capacity-incinerators-3\/","title":{"rendered":"small capacity incinerators"},"content":{"rendered":"<p> 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<p> DRE = [(Win &#8211; Wout)\/Win]*100<br \/>\n2.\u00a0\u00a0 \u00a0 If the minimum combustion temperatures aren&#8217;t maintained.<br \/>\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<br \/>\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<br \/>\n5.\u00a0\u00a0 \u00a0 All the emission to the air apart from steam or water vapour has to be odourless and free of mist, fume and droplets.  <\/p>\n<p> 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<p> Cadmium and compounds as\u00a0\u00a0\u00a0\u00a0 Cd<br \/>\n21 &#8211; OM <\/p>\n<p> Where:\u00a0\u00a0 \u00a0Es\u00a0\u00a0 \u00a0= Calculated emission concentration in the standard percentage oxygen concentration<br \/>\nWout = mass emission rate of POHC from the stack before the release to the air.  <\/p>\n<p> 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<p> Note:<br \/>\n2.\u00a0\u00a0 \u00a0 Be fitted with secondary burner\/s burning gas or low sulphur liquid gas or some other acceptable fuel.  <\/p>\n<p> 3.\u00a0\u00a0 \u00a0 Ensure secondary air supply is controlled efficiently.<br \/>\n4.\u00a0\u00a0 \u00a0 The incinerator must not be overcharged.<br \/>\n6.\u00a0\u00a0 \u00a0 Ensure the gas temperature as measured against the inner wall at the secondary room &#038; not in the flame zone, is less than 1100oC.   Ensure the oxygen content of the emitted gases is less than 11%.<br \/>\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<br \/>\nA solid particulate meter\/recorder<br \/>\n3.\u00a0\u00a0 \u00a0 The incinerator has to be preheated to working temperature before charging any waste.<br \/>\nPercent CO2 + CO <\/p>\n<p> 2.\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<p> 4\u00a0\u00a0 \u00a0Opacity of the smoke must not exceed 20% Viewed from 50 meters with naked eyes<br \/>\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 ought to be taken into consideration.  <\/p>\n<p> 2.\u00a0\u00a0 \u00a0 If possible the chimney needs to be visible to the operator from the feeding area.<br \/>\n3.\u00a0\u00a0 \u00a0 Whenever the previous charge hasn&#8217;t been fully combusted in the case of batch feeding.   Until such time as the addition of more waste won&#8217;t cause the layout parameters of the incinerator to be surpassed.  <\/p>\n<p> 3\u00a0\u00a0 \u00a0Main Combustion Chamber\u00a0\u00a0 \u00a0The main combustion chamber must: <\/p>\n<p> 1.\u00a0\u00a0 \u00a0 Be accepted as the main combustion zone.<br \/>\nThe Combustion efficiency is computed as follows; <\/p>\n<p> C.E=% CO2\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0 x 100<br \/>\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<p> 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<br \/>\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<br \/>\nMercury\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0\u00a0 Hg<br \/>\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<br \/>\nAny other instrument or measurement that may be considered necessary <\/p>\n<p> 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 Region and be compatible with premises in the area, <\/p>\n<p> 2.\u00a0\u00a0 \u00a0 Has to be placed in a suitably ventilated room.   Combustion efficiency: <\/p>\n<p> Combustion efficiency (CE) shall be at least 99.00%<br \/>\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<br \/>\n4.\u00a0\u00a0 \u00a0 Have fly ash containerization and storage before disposal.  <\/p>\n<p> 12\u00a0\u00a0 \u00a0Health &#038; Safety (Protective Gear)\u00a0\u00a0 \u00a01.\u00a0\u00a0 \u00a0 Staff handling waste must be well trained on safe handling of hazardous wastes<br \/>\n2\u00a0\u00a0 \u00a0Feeding And Charging\u00a0\u00a0 \u00a0Controlled hygienic, mechanical or automatic feeding methods have to be used which won&#8217;t influence the air temperature in the primary and secondary chambers of the incinerator negatively.  <\/p>\n<p> No waste is to be fed into the incinerator: <\/p>\n<p> 1.\u00a0\u00a0 \u00a0 Until the minimum temperatures have been reached.<br \/>\nAll pollutant concentrations must be expressed at Oo C and 1.013 x 10 5 N\/m2, dry gas and 11% oxygen correction.  <\/p>\n<p> Oxygen correction is computed as: <\/p>\n<p> Es = \u00a0\u00a0 \u00a021 &#8212; Os\u00a0\u00a0\u00a0 x EM<br \/>\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<br \/>\nOM\u00a0\u00a0 \u00a0= measured oxygen concentration <\/p>\n<p> 10\u00a0\u00a0 \u00a0Operation\u00a0\u00a0 \u00a01.\u00a0\u00a0 \u00a0 Materials destined for incineration should be of known origin and makeup and must be only incinerated in a furnace that&#8217;s registered for the specific type of waste.  <\/p>\n<p> 2.\u00a0\u00a0 \u00a0 A record must be kept of the amount, type and origin of the waste to be incinerated.<br \/>\n3.\u00a0\u00a0 \u00a0 The addition of dilution air after combustion in order to reach the requirement of these guidelines is unacceptable.   The minimum exit velocity should be 10 m\/s and at least twice the surrounding wind speed (Efflux velocity = wind speed x 2) whichever is greater to make sure no down washing of exiting gases.  <\/p>\n<p> 5.\u00a0\u00a0 \u00a0 Point for the measurement of emissions shall be provided.  <\/p>\n<p> 7\u00a0\u00a0 \u00a0Instrumentation\u00a0\u00a0 \u00a0Instrument for determining the interior wall temperature rather than burner flame temperature has to be provided for both primary and secondary chambers.  <\/p>\n<p> 2.\u00a0\u00a0 \u00a0 An audible and visible alarm must be set up to warn the operator when the secondary temperature drops to below the required temperature.  <\/p>\n<p> 3.\u00a0\u00a0 \u00a0 In addition to the above the following instruments may also be required.<br \/>\n4. \u00a0\u00a0 \u00a0 Fire fighting equipment must be provided<br \/>\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 ought to be recorded in a log book and reported to the relevant authority.  <\/p>\n<p> 6.\u00a0\u00a0 \u00a0 The incinerator operator and all relevant personnel must be trained to the satisfaction of the relevant control authority.  <\/p>\n<p> 11\u00a0\u00a0 \u00a0Housekeeping\u00a0\u00a0 \u00a0The site where the incinerator is built must: <\/p>\n<p> 1.\u00a0\u00a0 \u00a0 Have running water.<br \/>\nWhere: Win = mass feed rate of the POHC from the waste stream fed to incinerator, and<br \/>\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<br \/>\n4.\u00a0\u00a0 \u00a0 Ensure minimum exit temperature is not less than 850oC <\/p>\n<p> 4\u00a0\u00a0 \u00a0Secondary Combustion Chamber (Afterburner).\u00a0\u00a0 \u00a0 The secondary combustion chamber must: <\/p>\n<p> 1.\u00a0\u00a0 \u00a0<br \/>\nFabric filters<br \/>\nA smoke density meter\/recorder<br \/>\nAcid Gas Scrubbers<br \/>\n3.\u00a0\u00a0 \u00a0  Have light if 24hrs operation<br \/>\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<br \/>\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\n<\/p>\n<p> 1\u00a0\u00a0 \u00a0Basic 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 segments may include but not limited to: <\/p>\n<p> Overall plant layout.<br \/>\n4.\u00a0\u00a0 \u00a0 Make sure fire contact with gases is achieved.<br \/>\nElectrostatic precipitators<br \/>\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<br \/>\n5.\u00a0\u00a0 \u00a0 Ensure residence time isn&#8217;t less than two (2) seconds.<br \/>\nOs\u00a0\u00a0 \u00a0= Standard oxygen concentration<br \/>\nPrimary Combustion Chamber.<br \/>\n5. \u00a0\u00a0 \u00a0 There should be no smoking or eating on the site.  <\/p>\n<p> 3. \u00a0\u00a0 \u00a0 Caution and Warning signs must be provided.<br \/>\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<br \/>\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<br \/>\nA carbon monoxide and\/or oxygen meter\/recorder<br \/>\nEM\u00a0\u00a0 \u00a0= Measured emission concentration<br \/>\n2.\u00a0\u00a0 \u00a0 Have a good floor.<br \/>\n8.\u00a0\u00a0 \u00a0 Ensure both main and the combustion temperatures are maintained until all waste was fully combusted <\/p>\n<p> 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<p> Cyclone separator<br \/>\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<p> 3.\u00a0\u00a0 \u00a0 Ensure main air supply is controlled efficiently<\/p>\n<p>6.\u00a0\u00a0 \u00a0The incinerator operator and all relevant staff must be trained to the satisfaction of the relevant control authority.<\/p>\n<p>11\u00a0\u00a0 \u00a0Housekeeping\u00a0\u00a0 \u00a0The site where the incinerator is built must:<\/p>\n<p>1.\u00a0\u00a0 \u00a0Have running water.<br \/>\n2.\u00a0\u00a0 \u00a0Have a solid floor.<br \/>\n3.\u00a0\u00a0 \u00a0 Have lighting if 24hrs operation<br \/>\n4.\u00a0\u00a0 \u00a0Have fly ash containerization and storage before disposal.<\/p>\n<p>12\u00a0\u00a0 \u00a0Health &amp; Safety (Protective Gear)\u00a0\u00a0 \u00a01.\u00a0\u00a0 \u00a0Staff handling waste must be well trained on safe handling of hazardous wastes<br \/>\n2. \u00a0\u00a0 \u00a0Staff must be provided with appropriate\u00a0 protective gear such as, gas mask, aprons, gumboots, helmets, gloves, goggles.<\/p>\n<p>3. \u00a0\u00a0 \u00a0Caution and Warning signs must be provided.<br \/>\n4. \u00a0\u00a0 \u00a0Fire fighting equipment must be provided<br \/>\n5. \u00a0\u00a0 \u00a0There should be no smoking or eating on the site.<\/p>\n","protected":false},"excerpt":{"rendered":"<p>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 &#8211; Wout)\/Win]*100 2.\u00a0\u00a0 \u00a0 [&hellip;]<\/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\/6695"}],"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=6695"}],"version-history":[{"count":1,"href":"https:\/\/gofullday.com\/incineration\/wp-json\/wp\/v2\/posts\/6695\/revisions"}],"predecessor-version":[{"id":9397,"href":"https:\/\/gofullday.com\/incineration\/wp-json\/wp\/v2\/posts\/6695\/revisions\/9397"}],"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=6695"}],"wp:term":[{"taxonomy":"category","embeddable":true,"href":"https:\/\/gofullday.com\/incineration\/wp-json\/wp\/v2\/categories?post=6695"},{"taxonomy":"post_tag","embeddable":true,"href":"https:\/\/gofullday.com\/incineration\/wp-json\/wp\/v2\/tags?post=6695"}],"curies":[{"name":"wp","href":"https:\/\/api.w.org\/{rel}","templated":true}]}}