The present invention addresses to a third stage system with self-bleeding by means of the use of an internally or externally installed ejector with application in all multicyclone systems operating at positive pressure, whether for application in particulate abatement or protection systems of turbo-expanders or in industrial units that involve the need of recovering solid products carried by the process gas, aiming at eliminating the need for any additional separation systems using cyclones or filters to carry out the bleeding of the cyclone legs.

A separator apparatus includes an intake nozzle, first cyclone device, and a second cyclone device. The first and second cyclone devices each include an inlet section, a scroll, a barrel centered on a first axis, a vortex finder, and an underflow portion. The scroll is attached to the inlet section and to the barrel such that the scroll connects the inlet section to the barrel. The vortex finder has a vortex tube arranged concentrically on the axis in an interior volume of barrel. The underflow portion defines an annular gap in fluid connection with the interior volume. The intake nozzle is fluidly connected to the inlet sections of the first and second cyclone devices.

A low-density suspended solid separation apparatus and method is disclosed. The apparatus comprises a separation tube adapted to receive pre-filtered wastewater and a vortex generator rotated to create a vortex in the separation tube such that the vortex separates low-density suspended solids having a density less than one (1) from the pre-filtered wastewater when the pre-filtered wastewater is passed through the vortex generator. An adjustable tube is inserted from the opposite end of the separation tube into the vortex wherein air inside the adjustable tube is at a pressure less than that of the separation tube causing the low density suspended solids to be removed from the vortex. Remaining water is then discharged from the separation tube.

A low-density suspended solid separation apparatus and method is disclosed. The apparatus comprises a separation tube adapted to receive pre-filtered wastewater and a vortex generator rotated to create a vortex in the separation tube such that the vortex separates low-density suspended solids having a density less than one (1) from the pre-filtered wastewater when the pre-filtered wastewater is passed through the vortex generator. An adjustable tube is inserted from the opposite end of the separation tube into the vortex wherein air inside the adjustable tube is at a pressure less than that of the separation tube causing the low density suspended solids to be removed from the vortex. Remaining water is then discharged from the separation tube.

A cyclonic separator (10) comprises a separation chamber (14), a feed inlet (16) leading into the separation chamber and an underflow discharge (18) leading from the separation chamber. The cyclonic separator further comprises a vortex finder which has an inlet end positioned in the separation chamber, an outlet end defining an overflow discharge, and a bleed opening (48) defined by the inlet and outlet ends of the vortex finder and through which a portion of an overflow stream can be bled from the vortex finder to remove oversized particles from the overflow stream.

A cyclonic separator (10) comprises a separation chamber (14), a feed inlet (16) leading into the separation chamber and an underflow discharge (18) leading from the separation chamber. The cyclonic separator further comprises a vortex finder which has an inlet end positioned in the separation chamber, an outlet end defining an overflow discharge, and a bleed opening (48) defined by the inlet and outlet ends of the vortex finder and through which a portion of an overflow stream can be bled from the vortex finder to remove oversized particles from the overflow stream.

A centrifugal separation type oil separator includes an oil separator body having a cylindrical body portion, and a bent pipe provided on an outer peripheral side of the body portion to surround the body portion in a circumferential direction, to introduce a fluid containing an oil into the oil separator body. The bent pipe includes an outer wall portion extending in the circumferential direction of the body portion and expanding radially outward from the body portion, and an inner wall portion extending along the outer wall portion and blocking an open part of the outer wall portion. The outer wall portion and the inner wall portion are formed by different members. An upper side of the body portion is open. The oil separator body has an upper cover blocking an open portion of the body portion. The inner wall portion and the upper cover are formed by an integral member.

A centrifugal separation type oil separator includes an oil separator body having a cylindrical body portion, and a bent pipe provided on an outer peripheral side of the body portion to surround the body portion in a circumferential direction, to introduce a fluid containing an oil into the oil separator body. The bent pipe includes an outer wall portion extending in the circumferential direction of the body portion and expanding radially outward from the body portion, and an inner wall portion extending along the outer wall portion and blocking an open part of the outer wall portion. The outer wall portion and the inner wall portion are formed by different members. An upper side of the body portion is open. The oil separator body has an upper cover blocking an open portion of the body portion. The inner wall portion and the upper cover are formed by an integral member.

The disclosed gas-liquid separation device separates, from a liquid, gas mixed in the liquid. The gas-liquid separation device includes a body configured to allow mixed fluid to be introduced into a longitudinally central portion thereof, and to have a cylindrical structure having an inner diameter gradually reduced as the body extends from the central portion to opposite ends thereof, a pair of gas discharge pipes respectively provided at the opposite ends of the body and configured to discharge, to an exterior of the body, gas separated from the mixed fluid in an interior of the body, and a pair of liquid discharge pipes respectively provided at the opposite ends of the body and configured to discharge, to the exterior of the body, the mixed fluid from which the gas has been separated.

The disclosed gas-liquid separation device separates, from a liquid, gas mixed in the liquid. The gas-liquid separation device includes a body configured to allow mixed fluid to be introduced into a longitudinally central portion thereof, and to have a cylindrical structure having an inner diameter gradually reduced as the body extends from the central portion to opposite ends thereof, a pair of gas discharge pipes respectively provided at the opposite ends of the body and configured to discharge, to an exterior of the body, gas separated from the mixed fluid in an interior of the body, and a pair of liquid discharge pipes respectively provided at the opposite ends of the body and configured to discharge, to the exterior of the body, the mixed fluid from which the gas has been separated.