5results about How to "Avoid affecting heat transfer efficiency" patented technology

This utility model discloses a waste heat recovery device for an oxalyl chloride distillation column, relating to the field of waste heat recovery technology. The utility model includes a heat exchange tank; the heat exchange tank is frustoconical in shape, and a water storage tank is fixedly connected inside the heat exchange tank. The water storage tank and the heat exchange tank have the same inverted cone inclination angle. An annular slide rail is fixedly connected to the bottom surface of the heat exchange tank, and a turntable is rotatably connected to the surface of the heat exchange tank. Several sets of extension plates are symmetrically hinged to the bottom surface of the turntable. Several sliding rods are symmetrically slidably connected inside the extension plates. Stops are fixedly connected to the periphery of the sliding rods, and springs are provided between the stop blocks and the extension plates. Moving plates are fixedly connected between the sliding rods in the same group, and brush bristles are provided on the moving plates. In use, by pulling the handle back and forth, multiple sets of brush bristles can be driven to repeatedly scrape away impurities on the outer surface of the water storage tank, preventing impurities on the steam from contaminating the outer surface of the water storage tank during waste heat recovery, thus avoiding impact on waste heat recovery efficiency.

This utility model discloses an optimized structure for an aluminum alloy heat exchanger, relating to the field of heat exchanger technology. It includes a top plate, a partition plate attached to the bottom side of the top plate, and several sequentially stacked flow channel layers attached to the bottom side of the partition plate. A bottom plate is attached to one side of each flow channel layer. Several flow distribution ports are symmetrically arranged on the flow channel layers. Mutually perpendicular heat exchange mechanisms are provided on both sides of the flow channel layers. Each heat exchange mechanism includes a flow distribution groove connected to the corresponding flow distribution port, one end of which is connected to a mixing groove. Several corrugated heat exchange plates are installed between the two sets of mixing grooves of the heat exchange mechanism. Several flow distribution plates are installed within the heat exchange mechanism. This utility model solves the problems of low utilization rate and low heat exchange efficiency of the flow channel layers caused by the gaps in the diffusion grooves in the prior art. This utility model increases the path of the medium flow by using corrugated heat exchange plates, and the heat exchange plates of adjacent flow channel layers are arranged at intervals, increasing the heat exchange area between the flow channel layers and the medium, thereby improving the heat exchange efficiency.

The utility model discloses low-temperature concentration equipment for whey protein peptide production, and relates to the technical field of whey protein peptide production, the low-temperature concentration equipment comprises an enzymatic hydrolysate low-temperature concentration tank, the upper end of the enzymatic hydrolysate low-temperature concentration tank is connected with a modularized end cover through a bolt, a shaft end power coupler is arranged above the modularized end cover, and the shaft end power coupler is connected with the modularized end cover through a bolt. A stirring mechanism connected with the shaft end power coupler is arranged in the enzymatic hydrolysate low-temperature concentrated steaming tank, the upper end of the modular end cover is fixedly connected with an annular water storage sleeve, and the lower end of the modular end cover is fixedly connected with a plurality of Venturi self-suction type spraying units; the upper ends of the plurality of Venturi self-suction type spraying units penetrate through the modularized end cover and are communicated with the annular water storage sleeve, a water feeding mechanism connected with the annular water storage sleeve is arranged on one side of the enzymatic hydrolysate low-temperature concentrated steaming tank, and a heating mechanism is arranged on the outer wall of the enzymatic hydrolysate low-temperature concentrated steaming tank. Liquid milk is effectively prevented from being adhered to the inner wall of the enzymatic hydrolysate low-temperature concentrated steaming tank, heat transfer efficiency and product quality are prevented from being affected, equipment sanitation is ensured through an automatic cleaning system, and cleaning difficulty is lowered.

This utility model discloses an energy-saving low-temperature desalination and dehydration device, relating to the technical field of desalination and dehydration equipment. It includes a vacuum evaporator and a feed inlet: the feed inlet is located above the vacuum evaporator. After the concentrated water discharged from the membrane separation component of this energy-saving low-temperature desalination and dehydration device enters the crystallization reactor, a second motor drives the drive shaft to rotate, causing the wall-scraping agitator to operate continuously within the crystallization reactor. This agitation promotes uniform crystallization of salts in the solution, preventing disordered crystal growth due to localized supersaturation, thus improving crystallization efficiency and purity. Furthermore, the outer end of the wall-scraping agitator moves closely against the inner wall of the crystallization reactor, effectively preventing crystals from adhering to the reactor wall and forming scale, thus avoiding impact on the reactor's heat transfer efficiency and subsequent cleaning difficulty. This ensures uniform solid-liquid distribution of the mixed liquid entering the centrifugal separator, providing favorable conditions for subsequent solid-liquid separation, thereby guaranteeing the efficient and stable operation of the entire desalination and dehydration process.

The utility model discloses a bottom sealing head structure of a heat exchanger, which comprises a cylinder body, and an upper distribution plate is fixedly arranged at the top of the inner side of the cylinder body. According to the bottom sealing head structure of the heat exchanger, an upper distribution plate, a first lower distribution plate and a second lower distribution plate are sequentially and fixedly arranged in a barrel from top to bottom; a plurality of first through holes with the diameter of 16mm, a plurality of second through holes with the diameter of 13mm and a plurality of third through holes with the diameter of 14mm are respectively formed in the middle parts of the upper distribution plate, the first lower distribution plate and the second lower distribution plate, and the plurality of first through holes, the plurality of second through holes and the plurality of third through holes are distributed in a staggered manner; the fluid in the barrel can uniformly flow through the heat exchange area, the situation that the heat exchange efficiency is affected due to uneven local flow speed is avoided, the fluid can be guided to be in a turbulent state, the dead area is reduced, and the heat transfer effect is enhanced.