the solid being dried. The air entering the dryer contains 3% water by weight (mass) .and the air leaving the dryer contains 6% water by weight (mass). a) What is the recycle ratio to the granulator? b) What is the rate of air flow to the dryer? *note: please do not forget to draw the flow chart diagram. please do not copy from any other sites such do not take any answers from other sites. Please provide easy to understand solution (detailed with given, required, and solutions) in orderly manner.

I need a labeled process flow chart and a DOF analysis for this problem:  One way to make coal “cleaner” is to gasify the coal into “city gas”. In a proposed molten-iron coal gasification process pulverized coal of up to 3 mm size is blown into a molten iron bath and oxygen and steam are blown in from the bottom of the vessel. Materials such as lime for settling the slag, or steam for batch cooling and hydrogen generation can be injected at the same time. The sulfur in the coal reacts with lime to form calcium sulfide, which dissolves into the slag. The process operates at atmospheric pressure and 1400 to 1500°C. Under these conditions, coal volatiles escape immediately and are cracked. The carbon conversion rate is said to be above 98% and the gas is typically 65 to 70% CO, 25 to 35% hydrogen, and less than 2% carbon dioxide. Sulfur content of the gas is less than 20 ppm. Assume that the product gas is 68% Co, 30% H2, and 2% CO2. Calculate the enthalpy change that occurs on the…

Some cold milk (temperature 10.2 degrees C) is added to 231g of hot milk (86.9 degrees C). Once mixed, all of the milk will reach a final temperature of 72.4 degrees C. What mass of cold milk was used?    The specific heat capacity of the milk is 3930 J/kg degrees C

air at dry ball temperature 90 ° C and RH 8% is passed over the cooling coil so that the air dry ball temperature becomes 45 ° C. How much heat is released from the air in the process? = answer (kJ / kg)

An evaporation-crystallization process of the type described in Example 4.5-2 is used to obtain solid potassium sulfate from an aqueous solution of this salt. The fresh feed to the process contains 19.6 wt % K2SO4. The wet filter cake consists of solid K2SO4 crystals and a 40.0 wt % K2SO4 solution, in a ratio 10 kg crystals/kg solution. The filtrate, also a 40.0% solution, is recycled to join the fresh feed. Of the water fed to the evaporator, 45.0% is evaporated. The evaporator has a maximum capacity of 175 kg water evaporated/s. (a) Assume the process is operating at maximum capacity. Draw and label a flowchart and do the degree-of-freedom analysis for the overall system, the recycle-fresh feed mixing point, the evap- orator, and the crystallizer. Then write in an efficient order (minimizing simultaneous equations) the equations you would solve to determine all unknown stream variables. In each equation, cir- cle the variable for which you would solve, but don't do the calculations.…

L-serine is produced by fermentation and recovered and purified by crystallization at 10oC. To increase the yield of the crystallization step, methanol is added to the system.  An aqueous solution containing 27wt% L-serine is added with methanol to a batch crystallizer and cooled to 10oC. The crystals are then recovered by filtration. Draw a flowchart for this process showing the key unit operations with appropriate stream labels and composition.

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2) Filtration involves the separation of solid particles from fluid through a filtering medium and ranges from simple straining to more complex operations. Depending on the objective of the filtration process, the fluid, solid or both may be useful outputs of the overall process(a)Describe the basic principles offiltration as applied in the chemical industry. Using a suitable example, explain with clear illustrationshow filtration technique can be used to separate solids from filtrates at industrial scale

Material Science please help

If Equimolar mixture of A and B is mixed, 200  kgmol/hr of water (component C) is used to extract B  into aqueous phase. The product flow rates is 350  kgmol/hr. Find the Feed flowrate and the product  composition.