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    Detailed Project Report on Soda Ash Plant

    Detailed Project Report on Soda Ash Plant
    Detailed Project Report on Soda Ash Plant
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      SODA ASH PLANT
      [CODE NO. 3473]  


      Next to sulfuric acid and ammonia, soda ash (sodium carbonate) is the third largest manufactured chemical in the world. Comparatively, baking soda (Sodium bicarbonate), a byproduct of the soda ash industry also enjoys good market demand. While soda ash is commercially used for the production of glass, inorganic chemicals, soaps, synthetic detergents and processed food, baking soda is primarily used as a leavening agent and in medicines. The world production capacity of soda ash and baking soda is estimated to be 42 million tons in 2005 (Web 1) and 1 million tons in 2001 respectively. Today, more than 90% of soda ash and baking soda are manufactured using Solvay’s process.

      Despite being cost effective for the manufacture of both soda ash and baking soda, Solvay’s process is disadvantageous from the pollution abatement perspective. Solvay’s process produces huge quantities of CaCl2 which does not have much market value. Other waste streams produced in the process contain lower quantities of CaCO3 and other impurities of limestone. In addition, magnesium and calciumions in the brine solution are removed as carbonates which are also regarded as additional waste products. An alternative for the Solvay’s process is the Dual and Hou’s process in which ammonia is not recovered, but is transformed into ammonium chloride product, which can be sold as a fertilizer component. In addition, it is important to note that apart from enhanced utility usage, the Dual process requires purer brine solution and does not eliminate the generation of waste carbonate products in the brine purification step.

      Existing trends in chemical process industries indicate a strong bias towards integrated processing, co-generation, and minimization of waste product generation. Process intensification coupled with techno-economic analysis enables the selection of most potential physical and chemical transformation routes that maximize process efficiency and minimize waste generation and energy consumption. Considering the necessity to address theoretical and experimental investigations for the alternative route, this work presents a preliminary techno-economic analysis of soda ash and baking soda production from sodium sulfate. Amongst several alternate routes for soda ash and baking soda production, a critical review of the industrial processes for soda ash indicates a partial utilization of the modified Leblanc process to initially produce Na2SO4 and HCl from NaCl and H2SO4.

      Eventually, Na2SO4 can be used as the source for the production of baking soda (and soda ash) and (NH4)2SO4 (Bichel et al., 2008). Compared to the Solvay’s process, the alternate process has certain advantages. Firstly, pure chemicals are used as raw materials and therefore, further purification steps are eliminated, and waste generation is reduced. Secondly, all products namely HCl, baking soda, soda ash and ammonium sulfate have good market value compared to their raw-materials. Thirdly, the process allows the simultaneous removal of SOx and NOx from flue gases using regenerated sodium bicarbonate/carbonate solutions along with the production of fertilizers.


      COST ESTIMATION

      Plant  Capacity                                                   :    100.00 MT/day                          
      land & Building  (28000 Sq.Mtr)                      :    Rs. 21.20 Cr
      Plant & Machinery                                              :    Rs. 20.00 Cr
      Working Capital for 2 Months                          :    Rs. 10.45 Cr
      Total Capital Investment                                   :    Rs. 52.45 Cr
      Rate of Return                                                     :    27%
      Break Even Point         :    58%


      INTRODUCTION    
      SALT    
      GRADES, SPECIFICATIONS & PROPERTIES    
      TABLE: MARKET SPECIFICATION OF DENSE SODA ASH    
      PHYSICAL PROPERTIES AND HYDRATES OF SODIUM CARBONATE    
      TABLE: SOLUBILITY OF THE HYDRATES OF SODIUM CARBONATE    
      CHEMICAL PROPERTIES OF SODIUM CARBONATE    
      CHEMICAL COMPOSITION OF BRINES    
      USES & APPLICATION    
      FIGURE: USES OF BOTH HEAVY AND LIGHT SODIUM CARBONATE    
      USES OF SODA ASH    
      GLASS INDUSTRY    
      DETERGENT INDUSTRY    
      STEEL INDUSTRY    
      CHEMICAL INDUSTRY    
      A) SODIUM BICARBONATE    
      B) SODIUM SESQUICARBONATE    
      C) CHEMICALLY PURE SODIUM CARBONATE    
      D) SODIUM PERCARBONATE    
      E) OTHER APPLICATIONS    
      MARKET POTENTIAL OF SODA ASH    
      CONSUMPTION OF SODA ASH IN US    
      OVERVIEW OF SODA ASH INDUSTRY    
      WORLD REVIEW    
      WORLD RESOURCES:    
      CINER OF TURKEY TO INVEST $1.35 BILLION IN SODA ASH PLANT, POWER    
      TURKISH-CHINESE COOPERATION AIMS FOR THE TOP
      IN SODA ASH PRODUCTION    
      SOLVAY TO REINFORCE ITS GLOBAL LEADERSHIP IN SODA ASH    
      OUTLOOK    
      MANUFACTURERS/SUPPLIERS OF SODA ASH    
      CHEMISTRY OF SOLVAY PROCESS    
      SOLAR EVAPORATION PONDS    
      SEQUENCES IN MANUFACURE OF SODA ASH    
      BRINE PURIFICATION    
      AMMONIATION OF BRINE    
      REACTION IN KILN    
      REACTION IN SOLVAY TOWER    
      FORMATION OF SODIUM CARBONATE    
      RECOVERY OF AMMONIA    
      REACTION:    
      OVER ALL REACTION    
      PROCESS FLOW DIAGRAM    
      PROCESS IN DETAILS    
      BLOCK DIAGRAM OF SODA ASH PRODUCTION BY SOLVAY METHOD:    
      ALTERNATE SODA ASH PRODUCTION PROCESS    
      ONSITE GENERATION OF NA2SO4    
      PROCESS BLOCK DIAGRAMS FOR THE PRODUCTION OF (A) SODA ASH
       FROM SODIUM SULFATE AND (B) SODIUM SULFATE FROM NACL & H2SO4    
      TECHNOLOGY OF SODA ASH    
      A) BICARBONATE PRECIPITATION:    
      B) BICARBONATE THICKENING:    
      C) BICARBONATE FILTRATION:    
      D) CALCINING:    
      E) COMPACTION:    
      UTILITIES    
      STEAM    
      THE STEAM PROCESS CONSUMPTIONS LIE IN THE RANGE OF:    
      PROCESS WATER    
      COOLING WATERS    
      ELECTRICITY    
      GASEOUS, LIQUID & SOLID EFFLUENTS    
      GASEOUS EFFLUENTS    
      PARTICULATE DUST    
      CARBON DIOXIDE AND MONOXIDE    
      NITROGEN OXIDES    
      SULFUR OXIDES    
      AMMONIA    
      THE EMISSIONS FLUCTUATE AND CAN BE EXPLAINED BY:    
      HYDROGEN SULFIDE    
      LIQUID EFFLUENTS    
      WASTEWATER FROM BRINE PURIFICATION    
      ELECTRICITY AND POWER PLANTS    
      FLUIDIZED BED POWER PLANTS    
      FIG: FLOW DIAGRAM FOR A POWER-FLUID CIRCULATING FLUIDIZED
      BED BOILER    
      FLUIDIZED BED BOILERS HAVE SEVERAL IMPORTANT ADVANTAGES:    
      BY PRODUCTS AND WASTE    
      SUPPLIERS OF RAW MATERIALS    
      SUPPLIERS OF PLANT AND MACHINERY    
      CONDENSER    
      WASTE WATER TREATMENT PLANT    

              
      APPENDIX – A:

       1.      COST OF PLANT ECONOMICS      
       2.      LAND & BUILDING                                      
       3.      PLANT AND MACHINERY                                  
       4.      FIXED CAPITAL INVESTMENT                             
       5.      RAW MATERIAL                                         
       6.      SALARY AND WAGES                                     
       7.      UTILITIES AND OVERHEADS                              
       8.      TOTAL WORKING CAPITAL                                
       9.      COST OF PRODUCTION                                   
      10.      PROFITABILITY ANALYSIS                               
      11.      BREAK EVEN POINT                                     
      12.      RESOURCES OF FINANCE                           
      13.      INTEREST CHART                                       
      14.      DEPRECIATION CHART                                   
      15.      CASH FLOW STATEMENT                                   
      16.      PROJECTED BALANCE SHEET      
       

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