A centrifugal field-flow fractionation device capable of improving analysis performance and shortening analysis time is provided. A first channel 111 communicating with a channel member is formed on a rotational shaft 11 that rotates together with a rotor. A second channel 644 communicating with the first channel 111 is formed on a fixing portion 60 fixed in a state of facing the rotational shaft 11 along a rotational axis L. A mechanical seal 66 having a pair of seal rings 661 and 662 that come into contact with each other and a biasing member 663 is provided to attach one seal ring 661 to the rotational shaft 11 and the other seal ring 662 to the fixing portion 60. The biasing member 663 biases the pair of seal rings 661 and 662 in a direction in which the pair of seal rings come in contact with each other. Since the rotational shaft 11 can be rotated at a high speed and the liquid sample can be fed at a high pressure, the analysis performance can be improved and the analysis time can be shortened.

A centrifugal field-flow fractionation device capable of improving analysis performance and shortening analysis time is provided. A first channel 111 communicating with a channel member is formed on a rotational shaft 11 that rotates together with a rotor. A second channel 644 communicating with the first channel 111 is formed on a fixing portion 60 fixed in a state of facing the rotational shaft 11 along a rotational axis L. A mechanical seal 66 having a pair of seal rings 661 and 662 that come into contact with each other and a biasing member 663 is provided to attach one seal ring 661 to the rotational shaft 11 and the other seal ring 662 to the fixing portion 60. The biasing member 663 biases the pair of seal rings 661 and 662 in a direction in which the pair of seal rings come in contact with each other. Since the rotational shaft 11 can be rotated at a high speed and the liquid sample can be fed at a high pressure, the analysis performance can be improved and the analysis time can be shortened.

An enhanced gravity separation device rotates a plurality of rectangular section vessels about a central drive shaft. Each vessel has an array of closely spaced plates positioned with the vessel between outer regions and inner regions. A feed of mixed dense and less dense fluid matter is fed to the outer regions via a pipe and conduits, through the plate arrays and into the inner regions. Overflow of less dense matter reports to the inner regions and underflow of denser matter reports to the outer region. The vessels may be fluidized by liquid supplied into the outer regions via annulus and conduits.

An enhanced gravity separation device rotates a plurality of rectangular section vessels about a central drive shaft. Each vessel has an array of closely spaced plates positioned with the vessel between outer regions and inner regions. A feed of mixed dense and less dense fluid matter is fed to the outer regions via a pipe and conduits, through the plate arrays and into the inner regions. Overflow of less dense matter reports to the inner regions and underflow of denser matter reports to the outer region. The vessels may be fluidized by liquid supplied into the outer regions via annulus and conduits.

A classifying rotor has a rotatable frame body and classifying blades. The frame body has an opening portion on an outer peripheral portion and an ejection port for ejecting a fluid having flowed into an inside through the opening portion to an outside. The classifying blades are disposed at a desired interval in a circumferential direction on an outer peripheral side part in the frame body. The classifying blades are provided in the frame body so that an angle formed by a direction of the classifying blade and a rotating direction of the frame body becomes a desired inclination angle. The desired inclination angle is an angle at which classification accuracy becomes better when the classifying blades are inclined so that the formed angle becomes gradually smaller from 90 degrees.

A classifying rotor has a rotatable frame body and classifying blades. The frame body has an opening portion on an outer peripheral portion and an ejection port for ejecting a fluid having flowed into an inside through the opening portion to an outside. The classifying blades are disposed at a desired interval in a circumferential direction on an outer peripheral side part in the frame body. The classifying blades are provided in the frame body so that an angle formed by a direction of the classifying blade and a rotating direction of the frame body becomes a desired inclination angle. The desired inclination angle is an angle at which classification accuracy becomes better when the classifying blades are inclined so that the formed angle becomes gradually smaller from 90 degrees.

A system for separating coal from iron oxide and sulfur comprises a first tank having crusher to grind the coal. Steam is directed into the first tank to mix with the coal to produce a maximum substrate area for chemolithotrophic bacteria and algal species to act upon. A mechanical pulverizer is fed with the coal and steam. A sieve and a second tank receiving the coal from the pulverizer apparatus. An air exchanger connected to the second tank collects nanosized particulates of coal. A pipeline feeds the coal within the second tank with a mixture of chemolithophic bacteria from a breeding tank. A holding tank receives the mixture of coal and chemolithophic bacteria. A centrifuge receives the mixture of coal and chemolithophic bacteria from the holding tank and separates the coal from the mixture. A fourth tank receive the separated and hydrated coal particles from the centrifuge.

A system for separating coal from iron oxide and sulfur comprises a first tank having crusher to grind the coal. Steam is directed into the first tank to mix with the coal to produce a maximum substrate area for chemolithotrophic bacteria and algal species to act upon. A mechanical pulverizer is fed with the coal and steam. A sieve and a second tank receiving the coal from the pulverizer apparatus. An air exchanger connected to the second tank collects nanosized particulates of coal. A pipeline feeds the coal within the second tank with a mixture of chemolithophic bacteria from a breeding tank. A holding tank receives the mixture of coal and chemolithophic bacteria. A centrifuge receives the mixture of coal and chemolithophic bacteria from the holding tank and separates the coal from the mixture. A fourth tank receive the separated and hydrated coal particles from the centrifuge.

Provided is a kaolin having a finer particle size and a narrower particle size distribution, in combination with suitable morphology. Also provided are a method of preparing the kaolin product and methods of use.

Provided is a kaolin having a finer particle size and a narrower particle size distribution, in combination with suitable morphology. Also provided are a method of preparing the kaolin product and methods of use.