MILL INTEGRATION-PULPING, STEAM REFORMING AND DIRECT CAUSTICIZATION FOR BLACK LIQUOR RECOVERYCooperative Agreement • September 3rd, 2008
Contract Type FiledSeptember 3rd, 2008tubing forming the gas inlet and outlet at the bottom of the outer quartz tube are attached to fixed points to minimize virtual weight changes due to vertical movement of the reactor resulting from weight change of the reaction mixture. The weight change, flow rates, temperature and exhaust gas composition are recorded by a computer. The reactor system is flushed at a known N2 flow rate at 500℃ for one hour. Then the furnace temperature is raised in less than 5 minutes to the