Guidelines for Air Emission Regulation

10. Recommended limit values for emissions and inspection rules for thermal and catalytic oxidation installations for the destruction of organic solvents

10.1 Introduction
10.2 Operating conditions
10.3 Limit values for emissions
10.3.1 Limit value for emissions of TOC (Total Organic Carbon gases)
10.3.2 Limit value for emissions of CO
10.3.3 Limit value for odours
10.3.4 Limit value for emissions of NOX
10.4  Calculation of the height of outlets
10.4.1 Unburned specific organic compounds
10.4.2 TOC (Total Organic Carbon gases)
10.4.3 CO
10.4.4 NOX
10.4.5 Odours
10.5 Monitoring
10.5.1 AMS
10.5.2 Performance measurements

10.1 Introduction

This chapter deals with thermal and catalytic oxidation installations used for destruction of organic solvents containing carbon, oxygen and hydrogen. Where other elements such as halogens and nitrogen are involved, please refer to the rules in chapter 3.

10.2 Operating conditions

Destruction of organic compounds should not commence before the installation reaches its optimal operating conditions (e.g. temperatures at the set points).

10.3 Limit values for emissions

10.3.1 Limit value for emissions of TOC (Total Organic Carbon gases)

The limit value for emissions of TOC is set at 1 % by weight of the expected maximum concentration in g TOC/normal m3 added to the installation (averaged over 1 hour), but normally up to a maximum of 100 mg TOC/normal m3 and down to a minimum of 20 mg TOC/normal m3.

Reference condition is the actual concentration of oxygen.

10.3.2 Limit value for emissions of CO

100 mg/normal m3 at actual concentration of oxygen.

10.3.3 Limit value for odours

At first, the limit value for emissions of odours can be set at 4,000 LE/normal m3 at the actual concentration of oxygen. However, in some cases, for technical or financial reasons, it may be necessary to set a high limit value. (In such cases more than 95 % purification or abatement should be required.)

10.3.4 Limit value for emissions of NOX

200 mg/normal m3 calculated as NO2 at actual concentration of oxygen.

10.4 Calculation of the height of outlets

The source strength which has the greatest dispersion coefficient found in sections 10.4.1 – 10.4.5, should be used to calculate the height of stacks and other outlets, see chapter 4.

10.4.1 Unburned specific organic compounds

Source strength is equal to the unburned part of the specific organic compounds measured or calculated after purification or abatement.

10.4.2 TOC (Total Organic Carbon gases)

As a basis, calculations of dispersion coefficients should use a C-value of 0.1 mg TOC/m3. This C-value should take into account the fact that unknown, harmful substances such as aldehydes are formed during combustion. However, at effective combustion plants, most of the substances emitted will be light hydrocarbons such as methane, ethane, and propane. If it is possible to confirm that most of the TOCs emitted comprise these light hydrocarbons, the C-value can be increased to 1 mg/m3

10.4.3 CO

The source strength for CO is calculated on the basis of the limit value for emissions of CO.

10.4.4 NOX

The source strength for NOX is calculated on the basis of the limit value for emissions of NOX.

10.4.5 Odours

The source strength for odours is calculated as described in section 4.5.

10.5 Monitoring

10.5.1 AMS

  1. If the mass flow exceeds 25 kg TOC/hour, the installation should be equipped with automatic measuring and registration devices to monitor emissions of TOCs from the installation.
        
  2. The installation should establish continuous monitoring and registration of temperature. The measuring point and set point for temperature measurements should be approved by the supervising authority. Normally, measurement of the highest temperature occurring at the installation will be relevant.

Refer also to section 5.2.4.

10.5.2 Performance measurements

Performance measurements for TOC should be carried out with a flame ionisation detector (FID).