The present invention relates to a continuous on-board drying method for Antarctic krill and a continuous on-board processing method of shelled Antarctic krill. The drying method includes the following steps: 1) subjecting fishing materials to cleaning, sorting, and dewatering with a vibrating screen; 2) rapidly heating the krill to the temperature of up to 70? C. using infra-red rays; 3) hot-air drying; 4) impurity removal by vacuum; 5) cooling to obtain dried krill. The processing method includes the following steps: a) subjecting fishing materials to cleaning, sorting, and dewatering with a vibrating screen; b) rapidly heating the krill to the temperature of up to 70? C. using infra-red rays; c) hot-air drying; d) subjecting the dried krill to shelling treatment to separate shell from meat, to obtain shelled krill; e) impurity removal by vacuum to obtain shelled krill product. The methods in the present invention are highly efficient, energy saving, green and environmental protection, and the krill products have high quality and safety.

The present invention relates to a production apparatus for hydrothermal synthesis of lithium iron phosphate, which comprises first stirring devices, a preheating device, a second stirring device, and a drying device, wherein there are two first stirring devices, and the preheating device comprises a housing, a heating box, two feeding pumps, two first transfer assemblies, and several first heating tubes; the two first transfer assemblies each comprise an inlet pipe, an outlet pipe, and several transfer branch tubes. In the present application, the arrangement of multiple transfer branch tubes increases the heated area of the slurry, enhances the thermal conduction efficiency, and improves the heating effect. The equidistant arrangement of the transfer branch tubes ensures uniform heating of the slurry within the multiple transfer branch tubes, guaranteeing the heating effect. The arrangement of the preheating device can reduce the heating time of the slurry, thereby enhancing the heating effect.

Embodiments for implementing a produce dryer system, method, and apparatus are provided. For example, a produce dryer system may include a pickup station comprising a bin configured to be contain produce that is designated for drying, a first dryer and a second dryer configured to receive the bin and dry the produce in the bin by running for a dryer cycle associated with the produce, and a transport device. The transport device may include a ground transport chassis configured to travel along a predetermined path, a driven arm attached to the ground transport chassis that is configured to pick up and set down the bin, and a controller configured to determine which of the first dryer and the second dryer to use for drying the produce in the bin and for positioning and removing the bin from the first dryer or second dryer with the transport device.

Embodiments for implementing a produce dryer system, method, and apparatus are provided. For example, a produce dryer system may include a pickup station comprising a bin configured to be contain produce that is designated for drying, a first dryer and a second dryer configured to receive the bin and dry the produce in the bin by running for a dryer cycle associated with the produce, and a transport device. The transport device may include a ground transport chassis configured to travel along a predetermined path, a driven arm attached to the ground transport chassis that is configured to pick up and set down the bin, and a controller configured to determine which of the first dryer and the second dryer to use for drying the produce in the bin and for positioning and removing the bin from the first dryer or second dryer with the transport device.

A spray drying system for drying liquid into powder including a plurality of processing towers each including an elongated drying chamber, a spray nozzle assembly at an upper end of the drying chamber and a powder collection chamber at a lower end of the drying chamber. The powder collection chamber of each processing tower being configured to discharge power to a common conveyor system.

A spray drying system for drying liquid into powder including a plurality of processing towers each including an elongated drying chamber, a spray nozzle assembly at an upper end of the drying chamber and a powder collection chamber at a lower end of the drying chamber. The powder collection chamber of each processing tower being configured to discharge power to a common conveyor system.

A system for drying a wet lactose product stream includes a disperser configured to disperse agglomerated lactose particulates in a wet lactose stream into a dispersed wet lactose stream. A back-mixed partial drying zone is configured to at least partially dry the dispersed wet lactose stream by recirculating a partially dried lactose stream with the dispersed wet lactose stream. A plug-flow secondary drying zone is configured to dry the partially dried lactose stream to generate a substantially dried lactose stream.

An electrode plate heating device includes a box; two roller groups installed in the box, where the two roller groups are spaced apart along a first direction, and each roller group includes at least one first guide roller for the electrode plate to be alternately wound around all the first guide rollers in the two roller groups successively; and a heating assembly installed in the box and configured to heat the electrode plate after coated.

The present invention relates to a process for the control of Ostwald Ripening phenomenon occurring in particle suspensions without the need for addition of stabilizing agents, by using high pressure homogenization at mild conditions in a way that no increase or decrease in particle size occurs, thus allowing the stabilization of the suspension during the isolation step in the form of a dried powder.

The present invention relates to a process for the control of Ostwald Ripening phenomenon occurring in particle suspensions without the need for addition of stabilizing agents, by using high pressure homogenization at mild conditions in a way that no increase or decrease in particle size occurs, thus allowing the stabilization of the suspension during the isolation step in the form of a dried powder.