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Please hide the replies; no scoring will be given in principle if they are not hidden. Specific hiding method: http://bbs.hcbbs.com/viewthread.php?tid=492556&highlight=%D2%FE%B2%D8 Posts that have been edited are not rated. (The questions in this issue are taken from page 6 of \"Technical Worker Training Question Bank – Soda Ash Production Operators.\" An electronic version of this book is available for download in the soda ash information sharing area: http://bbs.hcbbs.com/thread-13140-1-2.html) Fill-in-the-blank questions: 6. In the carbonation process of the ammonia-soda method, ( ) and ( ) are two important process parameters. 7. As the temperature increases, the sodium utilization rate ( ). 8. As the temperature for carbonation removal increases, the NH3 and NaCl concentrations of the ammonium salts required to reach point P1 are ( ). 9. When the concentration of the ammonia salt solution remains constant, the higher the temperature at the carbonation outlet, the greater the resulting value; therefore, when the carbonation mother liquor is not cooled sufficiently, it will lead to (). 10. The sodium chloride solution used in the ammonia-alkali process can be ( ), or it can be ( ).
6. Sodium utilization rate, ammonia utilization rate 7. Increase 8. Increase regularly 9. The lower the sodium utilization rate; a decrease in the sodium utilization rate 10. Brine obtained directly from salt wells, with solid table salt dissolved to create it
6. During the carbonation process in the ammonia-alkali method, (sodium utilization rate) and (ammonia utilization rate) are two important process parameters. 7. As the temperature increases, sodium utilization improves. 8. As the temperature for carbonation removal increases, the NH3 and NaCl concentrations of the ammonium salt required to reach point P1 increase (in a regular manner). 9. When the concentration of the ammonia salt solution remains constant, the higher the temperature at the carbonation outlet, the lower the sodium utilization rate. Therefore, insufficient cooling of the carbonation mother liquor leads to a decrease in sodium utilization rate. 10. The sodium chloride solution used in the ammonia-alkali process can be (brine obtained directly from salt wells), or it can be (prepared by dissolving solid table salt).
6. Sodium utilization rate, ammonia utilization rate; 7. Improve ; 8. Regular increase ; 9. The lower the sodium utilization rate, the greater the decrease in this rate ; 10. Brine obtained directly from seawater, made by dissolving solid table salt.
1# chen3jun 6. Temperature, concentration 7. Increase 8. Decrease 9. The higher, the more crystallization 10. Saturated, unsaturated
6. Sodium utilization rate, ammonia utilization rate 7. Increase 8. Increase regularly 9. The lower the sodium utilization rate; a decrease in sodium utilization rate 10. Brine obtained directly from salt wells, with solid table salt dissolved to create it
6. Sodium utilization rate, Ammonia utilization rate 7. Increase 8. Increase regularly 9. The lower the sodium utilization rate; a decrease in sodium utilization rate 10. Brine extracted directly from salt wells, prepared by dissolving solid salt
6.6 Circulation rate, losses 7. Symmetric common saturation point 8. Sodium utilization rate, P1 9. First of all, there must be a certain ammonia-to-salt ratio; Second, there must be an appropriate amount of water. 10. Increase the ammonium ion concentration in the carbonization mother liquor
6 Sodium utilization rate, Ammonia utilization rate 7 Increase, 8 Increase in a regular pattern, 9 The lower the sodium utilization rate, 10 Directly extracted brine, Prepared by dissolving salt
6. Sodium utilization rate, ammonia utilization rate 7. Increase 8. Increase regularly 9. The lower the sodium utilization rate, the greater its decrease 10. Brine is drawn directly from salt wells, and solid table salt is dissolved to create it 1# chen3jun
6. Sodium utilization rate, ammonia utilization rate 7. Increase 8. Increase regularly 9. The lower the sodium utilization rate, the greater its decrease 10. Brine obtained directly from salt wells, formed by the dissolution of solid table salt