An ethanol distillation arrangement comprising:
- (a) a distillation portion including a beer column, a rectifier column and a side stripper, the beer column having an inlet for receiving ethanol laden beer including milled grain, the beer column and the rectifier column connected by a line for conveying 120 proof ethanol vapor from the beer column to the rectifier column and a beer bottom outlet for discharging beer bottoms, the ethanol vapor from the beer column also supplying heat to the rectifier column, the rectifier column producing 190 proof ethanol vapor and liquid rectifier bottoms, the rectifier column and the side stripper connected by a line for conveying rectifier bottoms to the side stripper, the side stripper in communication with a source of subatmospheric steam for heating the side stripper, the side stripper also having an outlet for discharging side stripper bottoms which are removed from the distillation portion, the side stripper and the rectifier column connected by a line for conveying ethanol vapor having an ethanol concentration below 190 proof from the side stripper to the rectifier column,
- (b) a condenser, a line connecting the rectifier column of the distillation portion and the condenser for conveying 190 proof ethanol vapor from the distillation portion to the condenser, the condenser adapted for condensing the 190 proof ethanol vapor to produce 190 proof liquid ethanol, the condenser adapted to operate at a pressure that is below atmospheric pressure and to thereby maintain the distillation portion at a pressure that is below atmospheric pressure,
- (c) a separator and a line connecting the separator and the beer column of the distillation portion for conveying beer bottoms from the beer column to the separator, the separator for the beer bottoms and separating the beer bottoms into distiller's grains and thin stillage,
- (d) a set of first effect evaporators including at least a first and a second first effect evaporator each having a shell side and a tube side, each shell side of each first effect evaporator connected to a source of hot vapor, the tube side of the first evaporator having an inlet in communication with the separator for receiving thin stillage, a first effect steam outlet for releasing first effect steam as stillage boils in response to the heat from the hot vapor and a stillage outlet for releasing stillage, the tube side of each subsequent evaporator having a stillage inlet in communication with the stillage outlet of the previous first effect evaporator, each first effect evaporator also having valves for isolating the evaporator and bypass valves associated therewith for redirecting stillage into a line which bypasses the evaporator and reroutes the stillage to the stillage intake of the next evaporator, the first effect evaporators each having sufficient excess capacity to support the distillation arrangement when an evaporator is off line, whereby a bypassed first effect evaporator may be isolated and bypassed for cleaning and maintenance while the other first effect evaporators continue to receive stillage and incrementally evaporate the stillage to produce mid-stillage and first effect steam,
- (e) a set of second effect evaporators including at least a first and a second evaporator each having a shell side and a tube side, each shell side of each second effect evaporator connected to the steam outlets of the first effect evaporators, the tube side of the first second effect evaporator having an inlet in communication with the stillage outlet of the last first effect evaporator, a second effect steam outlet for releasing second effect steam as stillage boils in response to the heat from the first effect steam and a stillage outlet for releasing stillage, the tube side of each subsequent evaporator having a stillage inlet in communication with the stillage outlet of the previous second effect evaporator, each second effect evaporator also having valves for isolating the evaporator and bypass valves associated therewith for redirecting stillage into a line which bypasses the evaporator and reroutes the stillage to the stillage intake of the next evaporator, the second effect evaporators each having sufficient excess capacity to support the distillation arrangement when an evaporator is off line, whereby a bypassed second effect evaporator may be isolated and bypassed for cleaning and maintenance while the other second effect evaporators continue to receive stillage and incrementally evaporate the stillage to produce syrup and second effect steam,
- (f) a second effect steam line connecting between the second effect steam outlets of the second effect evaporators and the beer column of the distillation portion, the second effect steam line for conveying second effect steam from the second effect evaporators to the beer column, thereby providing heat for the operation of the beer column.