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2results about How to "High enthalpy" patented technology

A purging device for a liquid preparation system

ActiveCN224405947Uavoid shockHigh removal rateMicroorganismMicrobial pollution
The application relates to a purging device for a liquid preparation system and relates to the technical field of medicine liquid preparation. In order to solve the problem that a traditional purging device cannot completely purge, the purging device comprises a conveying pipeline, the inlet end of the conveying pipeline is provided with a compressed air supply source, the outlet end of the compressed air supply source is sequentially and serially provided with a pressure reducing valve and an electric heater along the conveying pipeline, a plurality of heating modules are arranged in the electric heater, the plurality of heating modules are vertically stacked along the height direction of the electric heater, a heating channel is formed in the electric heater from bottom to top, and a temperature gradient from low to high is formed when the compressed air flows through the heating channel. The application has the effects of effectively stripping the residual moisture on the surface of the system, improving the removal rate of the residual moisture and solving the microbial pollution risk caused by incomplete purging.
Owner:南通海发智能科技有限公司

Evaporation and concentration device for polyamide 6 extraction water

The utility model relates to the technical field of nylon production, and particularly provides a polyamide 6 extraction water evaporation and concentration device, which is characterized in that the tube pass of a first-effect heat exchanger, the tube pass of a second-effect heat exchanger and the tube pass of a third-effect heat exchanger are respectively provided with a circulation loop, after circulating heat exchange and concentration, the steam enters a tube pass of a second-effect heat exchanger, enters a third-effect heat exchanger after further circulating heat exchange and concentration, and enters a fourth-effect heat exchanger and a third separator after circulating heat exchange, steam generated by a tube pass of a first-effect heat exchanger enters a first separator to be separated, and a gas phase enters a shell pass of the second-effect heat exchanger; steam generated by tube passes of the second-effect heat exchanger and the third-effect heat exchanger enters a second separator to be separated, a separated gas phase and a gas phase separated by a third separator are connected to a spray washing tower and a compressor together, and compressed steam provides steam for a shell pass of the first-effect heat exchanger and a shell pass of the third-effect heat exchanger. The device is reasonable in structural arrangement, heat energy can be fully utilized, and energy is saved.
Owner:HUBEI SANNING CHEM