Page 48 - demo
P. 48

3                              CURRENT STATUS OF









                                              TECHNOLOGY & TRENDS









                 n the previous sections basic routes of production of syngas, methanol and DME from different
                 hydrocarbon  sources  have  been  discussed.  In  this  section  present  trend  of  commercial
              Iproduction of these products including problems and issues have been looked at.


                  3.1     Present Commercial Production Routes

               At present there are large numbers of methanol production units all over the world. The total
               production capacity of methanol during the 2013 was about 100 MT while the demand was
               about 65 MT. Thirty five percent of the total production is being used in fuel. The consumption
               for DME was about 8% [21]. The global demand is primarily for methanol as a building block for
               various chemicals, but the fuel application is also growing fast. Therefore, the unused capacity
               is progressively reducing. China is the largest producer of methanol in the world and also the
               major user of methanol and methanol derivatives as fuel. The use of methanol and DME is
               growing at a fast rate in several countries in the world including North America. The current
               methanol production capacity in India is about 1.5 MT. Since the demand of methanol in India
               for chemical production is higher than its production, India is one of the largest importers of
               methanol [25]. Most of the large methanol plants in the world are based on natural gas, while in
               China both natural gas and coal are used. All the methanol plants in India are based on natural
               gas or naphtha; there is no coal based methanol plant in India. These units produce syngas
               through steam reforming.
               While  the  popular  technology  for  reforming  of  natural  gas  or  naphtha  is  auto-thermal
               reforming, gasification is gaining importance over reforming. When heavier feedstocks such
               as hydrocarbon residue, coal, coke or solid waste biomass or MSW are used, reforming is not
               feasible. In such cases gasification is the only option to produce syngas.
               The most important development in methanol/DME production scenario is use of biomass for
               production of syngas for methanol. However, due to the inherent issues with biomass, large
               scale mega plants are not feasible. Several demonstration units and a few commercial plants
               are operating based on biomass gasification.


                  3.2     Recent Trends in Gasification Process

               For  gas  as  well  as  solid  carbon  source,  including  coal,  solid  waste  based  methanol  plants
               produce syngas via partial oxidation (POX). Many of the plants use pure oxygen as the oxidant
               source, with IGCC for simultaneous power generation. Although investment is high, IGCC with
               oxygen firing and carbon dioxide capture makes the plant practically carbon neutral. All these
               technologies are commercially available, and many plants are operating in several parts of
               the world. Generally, as the capacity of gasifier increased, the investment per unit basis is
               lower and profitability is higher. In this light, 3000 TPD coal based methanol plant are being
               considered in China.






                  48      Methanol and DME Production: Survey and Roadmap | 2017
   43   44   45   46   47   48   49   50   51   52   53