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Special Report                                                                   Special Report



 Managing air emissions profi tably     High thermal durability;  usually involves a single solvent, usu-  Concentration: 6,000-ppm by volume
                                         ally ethyl acetate. This would be suit-
                                                                             Recovery: 364-tonnes/year.
           Superior mechanical properties; and
       
          High conversion effi ciencies.  able for recovery and reuse of solvent   Includes fuel used for steam, power,
 ir emission control need not al-  tor unit inlet capacity may range from   D.M. MOHUNTA  by absorption technology. It also eco-  and natural gas for heating.
 ways be a cost it can at many   5,000-Nm /hr to 130,000-Nm /hr.  Commercial Chemical and Develop-  Odour removal   friendly as it has lower CO  footprint   Absorption technology using Geno-
 3
 3
                                                                2
 Atimes be profi table. Large num-  ment Company   Due to the very low VOC concentra-  than oxidation technology.   sorb: 271.
 ber of volatile organic and other com-  Recovery  Chennai  tion, a catalytic oxidizer is the most suit-  Thermal oxidation with recuperation:
 pounds like nitrogen oxides) (NO ),   A  large  range  of  VOCs  can  be  re-  Email: dmm@ccdcindia.com  able approach for waste odorous organic  Case Study: Carbon dioxide foot-  1,161-tonnes CO /year.
                                                                                       2
 x
 sulphur dioxide (SO ), hydrogen sul-  covered from process and tank vents   www.ccdcindia.com  streams compared to other technologies.  print of ethyl acetate recovery (only   Global warming potential  (GWP)
 2
 phide (H S), carbon monoxide (CO),   using absorption technology because of   Catalytic oxidizers are capable of conti-  for process)  for ethyl acetate: 3.2-4.0 per kg.
 2
 and ammonia (NH ), are emitted into the   fairly high concentration. We have suc-  lytic oxidiser. The preferred process is   nuous steady state operating conditions   Solvent: ethyl acetate   Recovery  of 364 tonnes  would
 3
 atmosphere by chemical processes and   cessfully used Genosorb, a high boiling  catalytic  oxidation to  water, nitrogen   for nearly indefi nite periods and accom-  Table 1: Comparison of absorption system (Genosorb) for ethyl acetate (EA)
 other  processes like  substrate  coating,   absorption media supplied by Clariant.  and CO . It operates at lower tempera-  plish VOC destruction at relatively low   recovery
 2
 combustion of fuels and wastes.  The CO  footprint is lower than in the  ture and gives better thermal economy   temperatures.  With few moving parts
 2
 case of incineration.  than high temperature oxidizer process.   and constant stable operating pressures   Parameter   Units   Without Rotary   With Rotary
 Environmental norms require a   In practice, the equipment is quite   and temperatures, a properly designed   concentrator  Concentrator
 maximum level of emission reduction;   Incineration or destruction/decom-  compact with minimum ducting   oxidizer can easily achieve more than   Air fl ow rate   m /hr   20,000  20,000
                                                                 3
 therefore these must be either recovered   position  (see Figure 1).   99% destruction effi ciency. Lower ope-  EA quantity   kg/hr   42  42
 or destroyed to environmentally non-  This can be applied to VOCs as well   rating temperatures in conjunction with   EA in air   mg/m    2,100  2,100
                                                                    3
 hazardous or less harmful products.  as to gas species like nitrogen dioxide   Selection of  suitable catalyst from   heat recovery can give lower operating
 (NO , nitric oxide (NO), nitrous oxide  the  wide range  of catalysts  available   expenses.   Steam   kg/hr   1,250  180
 2)
                                                                 3
 A further and increasingly important   (N O), NH , and CO that may emanate  from Clariant-Sudchemie,  for a given   Cooling water   m /hr   200  35
 2
 3
 consideration in the choice of process   from chemical processes or combustion  application  is key to overall perfor-  Printing   Refrigeration   TR   200  60
 for emission control, is  generation of   equipment like boilers. Incineration is  mance/destruction effi ciency.  Printing  of  fl exible  packaging  uses   Power (connected load)   KWH   48  50
 global warming gases like CO , etc.  suitable for vapours from high boiling   inks with multiple solvents like ketones
 2
 products like tar, phenolic bodies, resins,   Advantages of catalytic  emission   (e.g., acetone, methyl ethyl ketone,   Fuel LPG or natural gas  KW   0  110
 Recovery or incineration  etc. and also other organic odours.  control are:  methyl isobutyl ketone, etc.), esters   Genosorb loss   gm/hr   112.1  50
 Under certain conditions it would be      Low operating temperature;  (e.g.,  methyl  acetate,  ethyl  acetate,   Base price (India)   Rs. lakhs  350  300
 economical to recover and recycle the   The incineration may be done in a   Wide range of operating tempera-  n-propyl acetate, n-butyl acetate, isobutyl

 volatile organic compounds (VOCs).   high  temperature  oxidiser or  in a  cata-  tures;  acetate, etc.), alcohols (e.g., methanol,
 When the VOC concentration is high but   ethanol, n-propanol, isopropanol, buta-
 requires abnormally low temperatures in   nol, etc.), mineral turpentine, etc. High
 the condenser to achieve the emission   volumes of hot air are used to dry and set
 target, Genosorb absorption technology   the ink. The hot air emanating from the
 can be used for economic recovery. In   machine have low level concentrations
 other cases, where the VOC concentra-  of the solvents – typically a few hundred
 tion is low, the operating costs of such   parts per million (ppm) – and is a cause
 recovery are very high (see example be-  of odour and pollution.
 low). However, in such instances, it may
 be possible to increase concentration, by   A recovery system would give a
 using a specially  designed rotary  con-  mixture that is diffi cult to separate and
 centrator, to level where it is economical   therefore  has  only  calorifi c  value.  A
 to recover or process. Where the concen-  catalytic  oxidation system with rotary
 trations are of the order of 50-100 ppm,   concentrator to bring the concentration
 the concentration can be increased 20-30   up  to  25%  of  Lower  Explosive  Limit
 times. Thus, a volume of 50,000-m /hr is   (LEL) will reduce the volume by 10-30
 3
 reduced to 2,500-m /hr while still keep-  times and would be an economic
 3
 ing the concentration well below the   solution.
 lower explosive limit. There will be very
 large reduction in  capex as well opex   Fig. 1: Schematic of catalytic oxidation process  Laminating and coating   Fig. 2: Schematic of solvent recovery system
 for recovery or incineration. A concentra-  Adapted from Siebu-Giken Co. Ltd.  The laminating of fl exible package   Adapted from Siebu-Giken Co. Ltd.


 180  Chemical Weekly  September 3, 2024  Chemical Weekly  September 3, 2024                           181


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