Simulation of the Industrial Oil Adsorption Purification Process for Automation Tasks

Figure 1

Structural scheme of the TS for the preparation processes of raw material and adsorption and cooling of the adsorbent. RM: contaminated raw material; SOL1: solvent at the diaphragm mixer inlet; MS1: mixture of raw material and solvent; W1, W2: water at the refrigerator R1 inlet and outlet, respectively; SOL2: solvent for the water seal; MS2: cooled mixture of raw material and solvent; A1, A2: regenerated adsorbent hot and cooled, respectively; W3, W5, W7, W9: water at the coil inlet of the refrigerator R2; W4, W6, W8, W10: water at the coil outlet of the refrigerator R2; AW1: air to create a fluidized bed in the refrigerator R2; AW2: air for the pneumatic transport system; A: the adsorbent at the adsorber inlet (hereinafter, referred to as the adsorbent); RS1: purified product; CA1: contaminated adsorbent.