SIST EN 15170:2009
Characterization of sludges - Determination of calorific value
Characterization of sludges - Determination of calorific value
This European Standard specifies a method for the determination of the gross calorific value of sludge at constant volume and at the reference temperature 25 °C in a bomb calorimeter calibrated by combustion of certified benzoic acid.
The result obtained is the gross calorific value of the sample at constant volume with both the water of the combustion products and the moisture of the sludge as liquid water. In practice, sludges are burned at constant (atmospheric) pressure and the water is either not condensed but is removed as vapour with the flue gases. Under these conditions, the operative heat of combustion to be used is the net calorific value of the fuel at constant pressure. In this European Standard the net calorific value at constant volume is described as it requires less additional determinations.
This method is applicable to all kinds of sludges.
Charakterisierung von Schlämmen - Bestimmung des Brenn- und Heizwertes
Diese Europäische Norm ist auf Folgendes anwendbar:
- die Behandlung von Regenwasser;
- Kanalisationssysteme für kommunales Abwasser;
- Anlagen für die Behandlung von kommunalem Abwasser;
- Behandlung von industriellem Abwasser, die auf ähnliche Weise erfolgt wie die von kommunalem Abwasser (wie in der Richtlinie 91/271 festgelegt);
- Aufbereitungsanlagen für die Wasserversorgung;
- Wasserverteilungssysteme.
Dieses Verfahren ist auch auf Schlammsuspensionen anderer Herkunft anwendbar.
Caractérisation des boues - Détermination du pouvoir calorifique
La présente Norme européenne spécifie une méthode de détermination du pouvoir calorifique supérieur des
boues, à volume constant et à la température de référence de 25 °C dans une bombe calorimétrique
étalonnée par combustion d’acide benzoïque certifié.
Le résultat obtenu est le pouvoir calorifique supérieur de l’échantillon à volume constant, l’eau des produits de
combustion et l’humidité des boues étant à l’état liquide. Dans la pratique, les boues sont brûlées à pression
(atmosphérique) constante et l’eau n’est pas condensée mais retirée sous forme de vapeur avec les produits
de combustion. Dans ces conditions, la chaleur effective de la combustion à utiliser est le pouvoir calorifique
inférieur du combustible, à pression constante. La présente Norme européenne décrit le pouvoir calorifique
inférieur à volume constant, car cela nécessite moins de déterminations supplémentaires.
La présente méthode s’applique à tous les types de boues.
Karakterizacija blata - Določevanje kalorične vrednosti
General Information
Standards Content (Sample)
2003-01.Slovenski inštitut za standardizacijo. Razmnoževanje celote ali delov tega standarda ni dovoljeno.Charakterisierung von Schlämmen - Bestimmung des Brenn- und HeizwertesCaractérisation des boues - Détermination du pouvoir calorifiqueCharacterization of sludges - Determination of calorific value13.030.20Liquid wastes. SludgeICS:Ta slovenski standard je istoveten z:EN 15170:2008SIST EN 15170:2009en,fr,de01-maj-2009SIST EN 15170:2009SLOVENSKI
STANDARD
SIST EN 15170:2009
EUROPEAN STANDARDNORME EUROPÉENNEEUROPÄISCHE NORMEN 15170November 2008ICS 13.030.40 English VersionCharacterization of sludges - Determination of calorific valueCaractérisation des boues - Détermination du pouvoircalorifiqueCharakterisierung von Schlämmen - Bestimmung desBrenn- und HeizwertesThis European Standard was approved by CEN on 11 October 2008.CEN members are bound to comply with the CEN/CENELEC Internal Regulations which stipulate the conditions for giving this EuropeanStandard the status of a national standard without any alteration. Up-to-date lists and bibliographical references concerning such nationalstandards may be obtained on application to the CEN Management Centre or to any CEN member.This European Standard exists in three official versions (English, French, German). A version in any other language made by translationunder the responsibility of a CEN member into its own language and notified to the CEN Management Centre has the same status as theofficial versions.CEN members are the national standards bodies of Austria, Belgium, Bulgaria, Cyprus, Czech Republic, Denmark, Estonia, Finland,France, Germany, Greece, Hungary, Iceland, Ireland, Italy, Latvia, Lithuania, Luxembourg, Malta, Netherlands, Norway, Poland, Portugal,Romania, Slovakia, Slovenia, Spain, Sweden, Switzerland and United Kingdom.EUROPEAN COMMITTEE FOR STANDARDIZATIONCOMITÉ EUROPÉEN DE NORMALISATIONEUROPÄISCHES KOMITEE FÜR NORMUNGManagement Centre: rue de Stassart, 36
B-1050 Brussels© 2008 CENAll rights of exploitation in any form and by any means reservedworldwide for CEN national Members.Ref. No. EN 15170:2008: ESIST EN 15170:2009
EN 15170:2008 (E) 2 Contents Page Foreword.3 Introduction.4 1 Scope.5 2 Normative references.5 3 Terms and definitions.5 4 Principle.6 5 Reagents.6 6 Apparatus.7 7 Procedure.9 8 Calibration.13 9 Gross calorific value.14 10 Calculation of net calorific value.15 11 Precision.17 12 Test report.17 Annex A (informative)
Example of a calorimeter.18 Annex B (informative)
Temperature evolution.19 Annex C (informative)
Results of the interlaboratory comparison.20 Bibliography.21
SIST EN 15170:2009
EN 15170:2008 (E) 3 Foreword This document (EN 15170:2008) has been prepared by Technical Committee CEN/TC 308 “Characterization of sludges”, the secretariat of which is held by AFNOR. This European Standard shall be given the status of a national standard, either by publication of an identical text or by endorsement, at the latest by May 2009, and conflicting national standards shall be withdrawn at the latest by May 2009. Attention is drawn to the possibility that some of the elements of this document may be the subject of patent rights. CEN [and/or CENELEC] shall not be held responsible for identifying any or all such patent rights. According to the CEN/CENELEC Internal Regulations, the national standards organizations of the following countries are bound to implement this European Standard: Austria, Belgium, Bulgaria, Cyprus, Czech Republic, Denmark, Estonia, Finland, France, Germany, Greece, Hungary, Iceland, Ireland, Italy, Latvia, Lithuania, Luxembourg, Malta, Netherlands, Norway, Poland, Portugal, Romania, Slovakia, Slovenia, Spain, Sweden, Switzerland and the United Kingdom.
SIST EN 15170:2009
EN 15170:2008 (E) 4 Introduction This method is a simple way to evaluate the amenability of sludge and sludge products to be treated by thermal processes. In this European Standard some thermo-chemical corrections are not considered. For detailed descriptions of analytical procedures and theoretical background see ISO 1928 or CEN/TS 14918. The result obtained is the gross calorific value of the sample at constant volume with both the water of the combustion products and the moisture of the sludge as liquid water. The net calorific value can be obtained by calculation from the gross calorific value. For this either the hydrogen content of the sludge or the amount of water found in the combustion test has to be determined. Sludges usually contain much water and (un-burnable) solids. Therefore their calorific value – especially on the “as received” basis – is quite low. For many purposes it may be sufficient to determine the gross calorific value only, and not the net calorific value for which additional determinations are necessary. The calculation of the net calorific value at constant volume is described here only, for calculation at constant pressure refer to either ISO 1928 or CEN/TS 14918. SIST EN 15170:2009
EN 15170:2008 (E) 5 1 Scope This European Standard specifies a method for the determination of the gross calorific value of sludge at constant volume and at the reference temperature 25 °C in a bomb calorimeter calibrated by combustion of certified benzoic acid. The result obtained is the gross calorific value of the sample at constant volume with both the water of the combustion products and the moisture of the sludge as liquid water. In practice, sludges are burned at constant (atmospheric) pressure and the water is not condensed but is removed as vapour with the flue gases. Under these conditions, the operative heat of combustion to be used is the net calorific value of the fuel at constant pressure. In this European Standard the net calorific value at constant volume is described as it requires less additional determinations. This method is applicable to all kinds of sludges. 2 Normative references The following referenced documents are indispensable for the application of this document. For dated references, only the edition cited applies. For undated references, the latest edition of the referenced document (including any amendments) applies. EN 12832:1999, Characterization of sludges — Utilization and disposal of sludges — Vocabulary EN 12880, Characterization of sludges — Determination of dry residue and water content EN ISO 16720, Soil quality — Pretreatment of samples by freeze-drying for subsequent analysis (ISO 16720:2005) ISO 651, Solid-stem calorimeter thermometers ISO 652, Enclosed-scale calorimeter thermometers ISO 1770, Solid-stem general purpose thermometers ISO 1771, Enclosed-scale general purpose thermometers ISO/TS 12902, Solid mineral fuels — Determination of total carbon, hydrogen and nitrogen — Instrumental methods 3 Terms and definitions For the purposes of this document, the terms and definitions given in EN 12832:1999 and the following apply. 3.1 gross calorific value (at constant volume) absolute value of the specific energy of combustion, in Joules, for unit mass of a solid sludge burned in oxygen in a calorimetric bomb under the conditions specified. The products of combustion are assumed to consist of gaseous oxygen, nitrogen, carbon dioxide and sulfur dioxide, of liquid water (in equilibrium with its vapour) saturated with carbon dioxide under the conditions of the bomb reaction, and of solid ash, all at the reference temperature 3.2 net calorific value (at constant volume) absolute value of the specific energy of combustion, in Joules, for unit mass of a solid sludge burned in oxygen under conditions of constant volume and such that all the water of the reaction products remains as SIST EN 15170:2009
EN 15170:2008 (E) 6 water vapour (in a hypothetical state at 0,1 MPa), the other products being as for the gross calorific value, all at the reference temperature 3.3 net calorific value (at constant pressure) absolute value of the specific energy of combustion, in Joules, for unit mass of a solid sludge burned in oxygen at constant pressure under such conditions that all the water of the reaction products remains as water vapour (in a hypothetical state at 0,1 MPa), the other products being as for the gross calorific value, all at the reference temperature 3.4 corrected temperature rise change in calorimeter temperature caused solely by the processes taking place within the combustion bomb. It is the total observed temperature rise corrected for heat exchange, stirring power etc. 4 Principle 4.1 Gross calorific value A weighed portion of the analysis sample of the solid sludge is burned in high-pressure oxygen in a bomb calorimeter under specified conditions. The effective heat capacity of the calorimeter is determined in calibration experiments by combustion of certified benzoic acid under similar conditions, accounted for in the certificate. The corrected temperature rise is established from observations of temperature before, during and after the combustion reaction takes place. The duration and frequency of the temperature observations depend on the type of calorimeter used. Water is added to the bomb initially to give a saturated vapour phase prior to combustion, thereby allowing all the water formed, from the hydrogen and moisture in the sample, to be regarded as liquid water. The gross calorific value is calculated from the corrected temperature rise and the effective heat capacity of the calorimeter, with allowances made for contributions from ignition energy, combustion of the fuse(s) and for thermal effects from side reactions such as the formation of nitric acid. Furthermore, a correction is applied to account for the difference in energy between the aqueous sulfuric acid formed in the bomb reaction and gaseous sulfur dioxide, i. e. the required reaction product of sulfur in the sludge. The corresponding energy effect between aqueous and gaseous hydrochloric acid can be neglected due to the usually low chlorine content of most sludges. 4.2 Net calorific value The net calorific value at constant volume of the sludge is obtained by calculation from the gross calorific value at constant volume determined on the analysis sample. The calculation of the net calorific value at constant volume requires information about the moisture and hydrogen contents of the analysis sample. In principle, the calculation of the net calorific value at constant pressure also requires information about the oxygen and nitrogen contents of the sample. NOTE The main difference between the gross and net calorific values is related to the physical state of water in the reaction products. 5 Reagents 5.1 Oxygen, at a pressure high enough to fill the bomb to 3 MPa, pure with an assay of at least 99,5 % (V/V), and free from combustible matter. NOTE Oxygen made by the electrolytic process may contain up to 4 % (V/V) of hydrogen. SIST EN 15170:2009
EN 15170:2008 (E) 7 5.2 Fuse 5.2.1 Ignition wire, of nickel-chromium 0,16 mm to 0,20 mm in diameter, platinum 0,05 mm to 0,10 mm in diameter, or another suitable conducting wire with well-characterized thermal behaviour during combustion. 5.2.2 Cotton fuse, of white cellulose cotton, or equivalent, if required. It is necessary to use a fuse with the same length and sections both in the calibration step and in the measurements. 5.3 Combustion aids of known gross calorific value, composition and purity, like benzoic acid, n-dodecane, paraffin oil, combustion bags or capsules may be used. 5.4 Benzoic acid, of calorimetric-standard quality, certified by (or with certification unambiguously traceable to) a recognized standardizing authority. The benzoic acid is burned in the form of pellets. It is normally used without drying or any treatment other than pelletizing; consult the sample certificate. 6 Apparatus 6.1 General The calorimeter (see a typical example in Annex A), consists of the assembled combustion bomb, the calorimeter can (with or without a lid), the calorimeter stirrer, water, temperature sensor, and leads with connectors inside the calorimeter can required for ignition of the sample or as part of temperature measurement or control circuits. During measurements the calorimeter is enclosed in a thermostat. The manner in which the thermostat temperature is controlled defines the working principle of the instrument and hence the strategy for evaluation of the corrected temperature rise. In combustion calorimetric instruments with a high degree of automation, especially in the evaluation of the results, the calorimeter is in a few cases not as well-defined as the traditional, classical-type calorimeter. Using such an automated calorimeter is, however, within the scope of this European Standard as long as the basic requirements are met with respect to calibration conditions, comparability between calibration and fuel experiments, ratio of sample mass to bomb volume, oxygen pressure, bomb liquid, reference temperature of the measurements and repeatability of the results. A print-out of some specified parameters from the individual measurements is essential. Equipment, adequate for determinations of calorific value in accordance with this European Standard, is specified below. 6.2 Calorimeter with thermostat 6.2.1 Combustion bomb, capable of withstanding safely the pressures developed during combustion. The design shall permit complete recovery of all liquid products. The material of construction shall resist corrosion by the acids produced in the combustion of sludges. A suitable internal volume of the bomb would be from 250 ml to 350 ml. 6.2.2 Calorimeter can, made of metal, highly polished on the outside and capable of holding an amount of water sufficient to completely cover the flat upper surface of the bomb while the water is being stirred. 6.2.3 Stirrer, working at constant speed. The stirrer shaft should have a low-heat conduction and/or a low-mass section below the cover of the surrounding thermostat to minimize transmission of heat to or from the system; this is of particular importance when the stirrer shaft is in direct contact with the stirrer motor. 6.2.4 Thermostat (water jacket), completely surrounding the calorimeter, with an air gap of approximately 10 mm separating calorimeter and thermostat. SIST EN 15170:2009
EN 15170:2008 (E) 8 The mass of water of a thermostat intended for isothermal operation shall be sufficiently large to outbalance thermal disturbances from the outside. The temperature should be controlled to within ± 0,1 K or better throughout the experiment. 6.2.5 Temperature measuring instrument, capable of indicating temperature with a resolution of at least 0,001 K so that temperature intervals of 2 K to 3 K can be determined with a resolution of 0,002 K or better. The absolute temperature shall be known to the nearest 0,1 K at the reference temperature of the calorimetric measurements. The temperature measuring device should be linear, or linearized, in its response to changes in temperature over the interval it is used. As alternatives to the traditional mercury-in-glass thermometers, suitable temperature sensors are platinum resistance thermometers, thermistors, quartz crystal resonators, etc. which together with a suitable resistance bridge, null detector, frequency counter or other electronic equipment provide the required resolution. The short-term repeatability of this type of device shall be 0,001 K or better. Long-term drift shall not exceed the equivalent of 0,05 K for a period of six months. For sensors with linear response (in terms of temperature), drift is less likely to cause bias in the calorimetric measurements than are non-linear sensors. Mercury-in-glass thermometers shall conform to ISO 651, ISO 652, ISO 1770 or ISO 1771. A viewer with magnification about 5 × is needed for reading the temperature with the resolution required. A mechanical vibrator to tap the thermometer is suitable for preventing the mercury column from sticking. If this is not available, the thermometer shall be tapped manually before reading the temperature. 6.2.6 Ignition circuit The electrical supply should be 6 V to 12 V alternating current from a step-down transformer. It is desirable to include a pilot light in the circuit to indicate when current is flowing. 6.3 Crucible, of silica, nickel-chromium, platinum or similar un-reactive material The crucible should be 15 mm to 25 mm in diameter, flat based and about 20 mm deep. Silica crucibles should be about 1,5 mm thick and metal crucibles about 0,5 mm thick. 6.4 Ancillary pressure equipment 6.4.1 Pressure regulator, to control the filling of the bomb with oxygen. 6.4.2 Pressure gauge (e. g. 0 MPa to 5 MPa), to indicate the pressure in the bomb with a resolution of 0,05 MPa. 6.4.3 Relief valve or bursting disk, operating at 3,5 MPa, and installed in the filling line, to prevent overfilling the bomb. CAUTION — Equipment for high-pressure oxygen shall be kept free from oil and grease (high vacuum grease recommended by the manufacturer can be used according to the operating manual of the instrument). Do not test or calibrate the pressure gauge with hydrocarbon fluid. 6.5 Timer, indicating minutes and seconds 6.6 Balances 6.6.1 Balance for weighing the sample, fuse etc., with a resolution of at least 0,1 mg; 0,01 mg is preferable and is recommended when the sample mass is of the order of 0,5 g or less (see 7.2.4). 6.6.2 Balance for weighing the calorimeter water, with a resolution of 0,5 g (unless water can be dispensed into the calorimeter by volume with the required accuracy). SIST EN 15170:2009
EN 15170:2008 (E) 9 6.7 Pellet press Capable of applying a force of about 100 kN, either hydraulically or mechanically, and having a die suitable to press a pellet having a diameter about 13 mm and a mass of (1 ± 0,1) g. 7 Procedure 7.1 General The calorimetric determination consists of two separate operations under specified conditions: combustion of the calibrant (benzoic acid); combustion of sample. The procedure for both above determination is essentially the same. In fact, the overall similarity is a requirement for proper cancellation of systematic errors caused, for example, by uncontrolled heat leaks not accounted for in the evaluation of the corrected temperature rise θ . It consists in carrying out quantitatively a complete combustion reaction (in high-pressure oxygen in the bomb) and of measuring the change in temperature caused by the total bomb process. The combustion of the calibrant makes it possible to determine the effective heat capacity of the calorimeter. Certain sludges may persistently burn incompletely; leaving residues that contain significant amounts of unburned sample or soot. By adding known amounts of an auxiliary material (e. g. benzoic acid, n-dodecane or paraffin oil), by using bags or capsules or cotton fuse, or by omitting the distilled water from the bomb, or by using a lower oxygen filling pressure, a clean combustion can in most instances be achieved. The temperature measurements required for the evaluation of the corrected temperature rise θ are made during a fore period, a main (reaction) period, and an after period (see 7.7.3 and Annex B). 7.2 Sample preparation 7.2.1 Measure the dry residue of the sample following EN 12880, so that the matter obtained has a mass sufficient for the following test. If the sludge is visibly wet or contains too much moisture dewater (e. g. by pressing) or dry carefully at a temperature not exceeding 40 °C or by freeze-drying following EN ISO 16720. Repeat measuring the moisture content of the sample to be analysed. Note: Drying of samples to e. g. 5% moisture is advantageous as less sample has to be weighed for combustion experiments compared to non-dries ones. 7.2.2 Grind the sample to powder with a particle size of about to 0,2 mm nominal topsize. 7.2.3 The sample shall be well-mixed and in reasonable moisture equilibrium with the laboratory atmosphere. The moisture content shall either be determined simultaneously with the weighing of the samples for the determination of calorific value, or the sample shall be kept in a small, effectively closed container until moisture analyses are performed, to allow appropriate corrections for moisture in the analysis sample. Calibration experiments will give a temperature rise of about 2 K to 3 K (depending on the type of calorimeter, see Clause 8). In order to have the same range of temperature rises for the combustion of samples their mass should be sufficient to ensure this. If the temperature rise is too small, dry the sample (see 7.2.1) and/or increase the sample mass and/or use a combustion aid or combustion bags and repeat the combustion. Otherwise, the accuracy of measurements may be be insufficient. NOTE 1 It is difficult to give suitable sample masses due to varying solids and moisture contents. However, an indication is given. Experiments in an isoperibolic calorimeter gave a temperature rise of 1 K using 1 g of a sludge from an SIST EN 15170:2009
EN 15170:2008 (E) 10 urban wastewater treatment plant containing about 45 % residue on ignition (at 550°C) and about 5 % moisture. The temperature rise was thought to be insufficient; therefore combustion aid was added for the actual determination. NOTE 2 Automated calorimetric instruments are often aneroid systems (systems without a fluid) where the calorimeter can, stirrer and water are replaced by a metal block. Characteristically they have a small heat capacity, leading to large changes in calorimeter temperature, thus facilitating the measurement of θ
with a relatively high resolution. Conversely, large values of
tend to increase the risk for introducing systematic error, in aneroid systems aggravated by difficulties in achieving uniform calorimeter surface temperature during combustion of the sample. A countermeasure is to limit the sample mass, bearing in mind that for smaller samples particular attention need to be given to their being representative. 7.2.4 Press the tablet with a suitable force to produce a compact, unbreakable test piece, containing the weighted fuse, weigh to nearest 0,1 mg and put it into the crucible. Alternatively put the ground sludge into the crucible, weighed to nearest 0,1 mg. 7.2.5 Connect the ends of the ignition wire to the electrodes; make sure that the ignition wire will contact the sludge. Check the resistance of the ignition circuit of the bomb; for most bombs it should not exceed 5 Ω to 10 Ω measured outside connectors of the bomb head, or between the connector for the insulated electrode and the bomb head. 7.3 Preparation of the bomb 7.3.1 Place the crucible in its support. Make sure that the position of the crucible in the assembled bomb will be symmetrical with respect to the surrounding bomb wall. 7.3.2 Add the prescribed amount of water to the bomb, for example (1 ± 0,1) ml. 7.3.3 Assemble the bomb. 7.3.4 Charge the bomb slowly with oxygen to obtain a pressure of (3 ± 0,2) MPa. 7.3.5 Using combustion aid Liquid combustion aid: After the mass of the sample pellet has been determined, auxiliary liquid material shall be added drop by drop on the pellet placed in the crucible (allowing the liquid to be absorbed) and the added amount shall be determined by weighing to the nearest 0,1 mg. Solid combustion aid: Use of solid combustion aids (benzoic acid recommended) without combustion bags or capsules is not recommended (a homogenous mixture of sample and combustion aid before pressing the test pellet might be difficult to achieve). Combustion bags or capsules: Combustion capsules or bags, or combustible crucibles with precisely known calorific value (gelatine, acetobutyrate or polyethylene) can be used as combustion aids (as such or with e. g. benzoic acid) according to the manufacturers instructions. They shall be weighed precisely before filling. The sample and the combustion aid like benzoic acid shall be mixed cautiously in the bag or capsule before testing. 7.4 Assembling the calorimeter 7.4.1 Bring the calorimeter water to within ± 0,3 K of the selected initial temperature and fill the calorimeter can with the required amount. This quantity of water in the calorimeter can shall be the same to within 0,5 g or better in all experiments. 7.4.2 Place the bomb in the calorimeter can. 7.4.3 Check the bomb for gas leaks as soon as it’s top becomes covered with water. If the gas valves are not fully submerged, check for leaks with a drop of water across the exposed opening. SIST EN 15170:2009
EN 15170:2008 (E) 11 7.4.4 Connect the leads for the ignition circuit and mount the thermometer. WARNING — If gas escapes from the bomb, discard the test, eliminate the cause of leakage and begin again. Cooling water, temperature controls, stirrers, etc. are turned on. Make sure that the stirrer works properly. A period of about 5 min is normally required for the assembled calorimeter to reach a steady state in the thermostat, irrespective of the type of calorimeter. 7.5 Combustion reaction and temperature measurements (see also Annex B) NOTE Temperatures can be read manually and plotted in a graph. From that the temperature rise can be calculated and any corrections can be implemented. Modern calorimetric systems with data systems can do that automatically. 7.5.1 Start taking temperature readings as soon as the calorimeter has reached steady-state conditions. Readings at 1 min intervals normally suffice to establish the drift rate of the fore period. When a mercury-in-glass thermometer is used for the temperature measurements, tap the thermometer lightly for about 10 s before each reading and take care to avoid parallax errors. 7.5.2 At the end of the fore period, the initial temperature ti has been established when the combustion is initiated firing the ignition wire. Hold the switch closed only for as long as it takes to ignite the wire. 7.5.3 Continue taking temperature readings at 1 min intervals. The time corresponding to ti marks the beginning of the main period. During the first few minutes of this period, when the temperature is rising rapidly, readings to the nearest 0,01 K are adequate. 7.5.4 Resume reading temperature to the nearest 0,001 K or better as soon as practicable, but no later than 5 min after the beginning of the main period. Criteria for the length of the fore, main and after periods, and hence the total number of temperature readings required, depend on the type of calorimeter (adiabatic, static jacket or isoperibol). For detailed descriptions see ISO 1928 or CEN/TS 14918. 7.5.5 After beginning of the after period continue taking temperature readings at 1 min intervals for additional 5 min. 7.6 Disassembling the calorimeter 7.6.1 At the end of the after period, when all the required temperature readings have been completed, remove the bomb from the calorimeter, release the pressure slowly (following manufacturers manual) and dismantle the bomb. 7.6.2 Examine the interior of the bomb, the crucible and any solid residue carefully for signs of incomplete combustion. Discard the test if unburned sample or any soot deposit is visible. 7.6.3 Remove and measure any unburned pieces of ignition wire. If the sulfur content of the sludge and the nitric acid correction are known or will not be regarded, the following steps may be omitted. 7.6.4 Wash the contents of the bomb quantitatively into a beaker with distilled water. Make sure that the underside of the bomb head, the electrodes and the outside of the crucible are also washed. 7.6.5 The bomb washings from fuel combustions are analysed for nitrate and sulphate (for details see ISO 1928 or CEN/TS 14918). SIST EN 15170:2009
EN 15170:2008 (E) 12 7.7 Corrections 7.7.1 Therm
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