A system 400 for obtaining a substance from a commodity has a first apparatus 420 with first 422 and second 424 openings, a device 426 for moving the commodity through the first apparatus, and at least one blade 428 for shearing the commodity. The at least one blade 428 is positioned between the first opening 422 and the second opening 424. A second apparatus 440 has a first opening 442 and a second opening 444, with the first opening 442 being fluidly connected to the second opening 424 of the first apparatus 420. The second apparatus 440 includes a device 446 for moving the sheared commodity from the second apparatus first opening 442 to the second opening 444. A third apparatus 460 obtains the substance from the sheared commodity, including a separator 460 having a first opening 462 fluidly connected to the second opening 444 of the second apparatus 440.

A system (1; 101) and a method for purification of oil, said system comprising:—at least one feed tank (3) comprising oil to be purified;—a separation aid dosing device(13);—at least one basic sedimentation tank (21a, 21b) comprising at least one inlet (23a, 23b) connected to the feed tank (3) and to the separation aid dosing device (13) for receiving oil to be purified and separation aid, said at least one basic sedimentation tank (21a, 21b) further comprising at least one sludge phase outlet (41a, 41b) provided in a bottom part (37a, 37b) of the basic sedimentation tank and at least one oil phase outlet (39a, 39b);—at least one advanced sedimentation tank (121) comprising at least one sludge phase inlet (122) connected to the at least one sludge phase outlet (41a, 41b) of the at least one basic sedimentation tank (21a, 21b), said advanced sedimentation tank (121) further comprising at least one sludge phase outlet (141; 141a, 141b) connected to a sludge tank (143) and at least one oil phase outlet (139a, 139b; 39), wherein said advanced sedimentation tank (121) further comprises at least one sensor (55; 55a, 55b, 55c) for detecting the presence of an oil phase or a sludge phase.

A device (10) for a skimming operation for petrochemical or chemical fluid storage or process tanks working by gravitation, comprising buoyancy means (20), means (30) for collecting surface fluid to be skimmed including an opening (31) emerging just above the interface between the fluid with density d1 and the fluid with density d2, as well as connection means (32), and discharge means (40) for the collected surface fluid. The discharge means (40) includes at least two flexible pipes (41, 42) connected symmetrically to the connection means (32) and extending vertically in the fluid with density d2 toward the bottom of the tank.

An improved contactor/separator process is presented where one or more stages of contact and separation is achieved by providing one or more shroud and disengagement device combinations within a vessel, where the disengagement device is connected to the top of the shroud that contains vertically hanging fibers. A liquid admixture of immiscible fluids is directed co-currently upward through the shroud at flooding velocity or greater, where all of the admixture exits the disengagement device through a coalescing material. Tray supports are used to stack additional shroud and disengagement combinations vertically within the vessel. Each tray allows less dense liquids exiting one disengagement device from a lower shroud and disengagement device combination to enter the bottom of a shroud of a shroud and disengagement device combination position vertically above the lower shroud and disengagement device combination.

A separation tank for crude oil. Fluid enters an inlet section of a center column of the tank via an offset inlet pipe so the fluid enters swirling. Solids that settle in the inlet section are removed by a center column drain and a solids removal system. Free gas rises and exits from the top of the tank. Liquid flows out of the center column via a diffuser that spirals the fluid evenly toward the wall of the tank where oil coalesces and wicks upward. Liquid flows downward around two flow diverting baffles where more oil coalesces and wicks upward via an oil conduit into the oil layer. The water flows under the lower flow diverting baffle and exits the tank through the outlet section. A large circular oil collector weir uniformly removes oil from the oil layer. Interface draw offs located below the oil-water interface remove excess BS&W.

A bearing housing includes a hollow shell with opposite ends having coaxial openings for at least one bearing element at each end thereof. The shell between the openings has, when assembled in position for use, a bottom with a bottom surface, the bottom having an oil outlet and the bottom surface having an oil outlet opening. The cavity for impurities is arranged below the bottom surface of the shell, and the cavity is arranged in flow communication with the oil outlet and the oil outlet opening.

A hydrocarbon emulsion treatment system includes a treatment tank having a gas vent for operating the treatment tank near atmospheric pressure. The treatment tank separates water and oil in the emulsion for discharge to separate water and oil tanks respectively. According to a preferred embodiment, the treatment tank and the oil tank are supported on a common frame including an integral secondary containment structure providing secondary containment to both the treatment tank and the oil tank. The treatment tank is supported at greater elevation than the oil tank to allow the flow of oil from the treatment tank to the oil tank primarily under force of gravity.

An industrial washing process for various items such as precision small parts, mechanical parts, printed circuits, lenses, watchmaking articles, jewelry, eyewear or the like, includes regeneration of the used solvent by means of a first distillation and the step of drying the material in a vacuum chamber. The regeneration step includes at least one step of distillation through thermocompression carried out by compressing the solvent vapors by a pump and conveying them to an exchanger at higher pressure and temperature than the distiller. In this way the liquid to be evaporated can be used to condense the vapors with total recovery of the condensation energy, in this way avoiding the use of external thermal energy sources and obtaining a very high distillation capacity with lower energy consumption compared to a traditional condenser, and can also be used in a vacuum distillation step, if necessary, to further concentrate the distillation residues.

A skimmer apparatus is provided to separate a less dense upper liquid layer from on top of a denser lower liquid layer. The skimmer apparatus includes a skimmer vessel at least partially submerged within a fluid and preferentially receive the less dense fluid. A first conduit is located within the skimmer vessel by a plurality of support arms. The plurality of support arms affixes the first conduit's vertical and radial location within skimmer vessel. In use, the skimmer height is set to collect the less dense fluid into the skimmer vessel. A lower end of the first conduit is in fluid communication with the inside of the skimmer vessel and the collected fluid therein. An upper end of the first conduit is configured for being suctioned thereby withdrawing fluid from the skimmer vessel.

Systems and methods of removing coke/tar from water in a quench water recycling loop of a steam cracker quench system are disclosed. The systems include a quench water separator that has a feed calming compartment for reducing eddies in feed to the quench water separator. The feed calming compartment is defined, at least in part, by a perforated baffle in the quench water separator. The methods include the use of the quench water separator with the perforated baffle and the calming compartment to separate coke/tar from quench water in the quench water recycling loop.