A system includes a fin apparatus that is installed on a heat transfer medium pipe using thermally conductive mastic (heat transfer compound) and bands for holding the components in place. The system further includes a tank containing material of high viscosity, primarily Polymer Modified or Ground Tire Rubber Asphalts (PMAs and GTRs), that requires heating. The fin apparatus increases the surface area of the heat transfer medium piping and increases the effectiveness of the heat transfer that takes place between the medium and the high viscosity material. There is a need for the fin apparatus because to date, traditional fin designs are prone to fouling and decreased performance when used with high viscosity materials like PMAs and GTRs.

A high-temperature flow-splitting component, applicable to a temperature range from a first temperature to a second temperature, includes an entrance channel, at least one primary channel and at least one subordinate channel. The entrance channel is used for introducing a fluid at a total flow rate. The at least one primary channel for introducing the fluid from the entrance channel at a first flow rate is connected with the entrance channel by a first angle ranging from 90°˜270°. The at least one subordinate channel for introducing the fluid from the entrance channel at a second flow rate is connected with the at least one primary channel by a second angle ranging from 30°˜150°. A sum of the first flow rate and the second flow rate is equal to the total flow rate.

A system is disclosed for cleaning an object, such as a heat exchanger including a bundle of feed-through tubes extending between two end plates. In an embodiment, the system includes a connection body for connecting the system to an object, a holder for holding a cleaning device and a moving system for moving the holder with respect to the connection body in a first direction and a second direction at least having a component perpendicular to the first direction. The moving system includes a rotation motor and a linear motor.

The present disclosure is directed to petrochemical processing systems that may include a component including a first surface oriented to contact a process fluid, which may define a plurality of channels. The petrochemical processing systems may further include a plurality of metal spheres disposed at least partially in the plurality of channels. Each one of the plurality of metal spheres may be fixed in place within one of the plurality of channels such that each of the plurality of metal spheres is freely rotatable. Methods for reducing accumulation and formation of solid deposits during petrochemical processing using the petrochemical processing systems are also disclosed.

The present disclosure is directed to petrochemical processing systems that may include a component including a first surface oriented to contact a process fluid, which may define a plurality of channels. The petrochemical processing systems may further include a plurality of metal spheres disposed at least partially in the plurality of channels. Each one of the plurality of metal spheres may be fixed in place within one of the plurality of channels such that each of the plurality of metal spheres is freely rotatable. Methods for reducing accumulation and formation of solid deposits during petrochemical processing using the petrochemical processing systems are also disclosed.

A process for removing or reducing the accumulation of foulant within furnaces and heat exchangers in industrial systems such as an oil refinery by introducing a periodic steam blast. The steam blast is directed into the fluid stream from which the foulants form on to the heat exchanger surfaces. The steam blast increases the flow rates, creates turbulence and increases the temperature within the heat exchanger to dislodge foulant in both a soft and hardened states from internal surfaces upon which foulants have adhered and accumulated.

This invention relates to a polymerization process for forming polymer comprising: contacting (typically in a solution or slurry phase), a monomer and a catalyst system in a reaction zone comprising at least one spiral heat exchanger and recovering polymer, wherein the monomer, the catalyst system and the polymer flow through the at least one spiral heat exchanger in a cross-flow direction relative to spirals of the at least one spiral heat exchanger.

A heat exchange area (4) of a heating plate (1) of a plate heat exchanger having corrugations, wherein the corrugations have additional local corrugations on their front and/or side surfaces forming notches (45, 4F) and the apex line (4L) of the corrugations has discontinuous form, preferably it is a polygonal curve or a wavy line.

A reaction/mixing/heat exchange tube, including an outer tube, an inner tube disposed in the outer tube; and a fluid channel formed between the outer tube and the inner tube. The outer tube includes a wall including a plurality of first flat segments, and a plurality of first communication holes formed between every two adjacent first flat segments.

A successive thermal pyrolysis apparatus for waste rubber has a pyrolysis furnace unit and a steam heating unit. The pyrolysis furnace unit is a tube chain type pyrolysis furnace and substantially has conveyor tubes and a chain disc conveyor mounted through the conveyor tubes for conveying waste rubber along the conveyor tubes. The steam heating unit encloses a segment of the conveyor tubes and has multiple baffles mounted therein to form a tortuous flowing path for steam passing through to heat the pyrolysis furnace unit. The successive thermal pyrolysis apparatus can prevent the carbonized fragments from sticking to and blocking inner surfaces of the conveyor tubes. The waste rubber fragments are successively thermally decomposed while being conveyed through the conveyor tubes.