A method for producing products, advantageously solvents, is by fermentation, advantageously multi-stage fermentation. The fermentation is complemented with pervaporation as in situ product recovery technology, combined with a multistage condensation of the permeate. The condensates are separately introduced in the downstream processing to recover the produced products, advantageously solvents. The method for producing products, advantageously solvents, by fermentation is simplified and has an overall improved energy efficiency. A related system uses method for producing products, advantageously solvents, is by fermentation.

A method for producing products, advantageously solvents, is by fermentation, advantageously multi-stage fermentation. The fermentation is complemented with pervaporation as in situ product recovery technology, combined with a multistage condensation of the permeate. The condensates are separately introduced in the downstream processing to recover the produced products, advantageously solvents. The method for producing products, advantageously solvents, by fermentation is simplified and has an overall improved energy efficiency. A related system uses method for producing products, advantageously solvents, is by fermentation.

The hybrid desalination system (10) includes a reverse osmosis filtration system (14), a forward osmosis filtration system (18), and a multi-effect distillation system (16). A condenser (12) receives seawater (S) and produces cooled seawater (CS). The cooled seawater (CS) is filtered by the reverse osmosis filtration system (14), which outputs a first brine reject stream (BR1) and a permeate stream (P). The multi-effect distillation system (16) outputs a second brine reject stream (BR2). A feed side (20) of the forward osmosis filtration system (18) receives the first brine reject stream (BR1), and the second brine reject stream (BR2) is received by the draw side (22), which outputs diluted brine (DB). The multi-effect distillation system (16) is in fluid communication with the forward osmosis filtration system (18) and recycles the diluted brine (DB). The multi-effect distillation system (16) outputs a return condensate (RC) and a pure water distillate (D).

The hybrid desalination system (10) includes a reverse osmosis filtration system (14), a forward osmosis filtration system (18), and a multi-effect distillation system (16). A condenser (12) receives seawater (S) and produces cooled seawater (CS). The cooled seawater (CS) is filtered by the reverse osmosis filtration system (14), which outputs a first brine reject stream (BR1) and a permeate stream (P). The multi-effect distillation system (16) outputs a second brine reject stream (BR2). A feed side (20) of the forward osmosis filtration system (18) receives the first brine reject stream (BR1), and the second brine reject stream (BR2) is received by the draw side (22), which outputs diluted brine (DB). The multi-effect distillation system (16) is in fluid communication with the forward osmosis filtration system (18) and recycles the diluted brine (DB). The multi-effect distillation system (16) outputs a return condensate (RC) and a pure water distillate (D).

A water distillation system including a reservoir unit configured to reserve a second liquid of higher concentration than the first liquid; a pipe including a first end communicated with the first liquid and a second end communicated with the second liquid in the reservoir unit; a semipermeable membrane fitted on the pipe to separate the first liquid and the second liquid, so that the first liquid is mixed into the second liquid through the semipermeable membrane and led to the reservoir unit by osmotic action; and a distillation unit configured to distill the second liquid in the reservoir unit by solar energy.

The present invention aims at providing a method for producing a high-concentration alcohol from a water-alcohol mixture, in which the overall process is efficient and the present invention relates to a production method of a high-concentration alcohol, including a water adsorption step of adsorbing water of a water-alcohol mixture on an adsorption column to obtain a first concentrated alcohol, a water desorption step of introducing an alcohol to obtain a hydrous alcohol, and a membrane separation step of introducing the hydrous alcohol into a membrane separation unit provided with a membrane composite containing zeolite having an SiO.sub.2/Al.sub.2O.sub.3 molar ratio of 5 to 15 to obtain a second concentrated alcohol.

The present invention aims at providing a method for producing a high-concentration alcohol from a water-alcohol mixture, in which the overall process is efficient and the present invention relates to a production method of a high-concentration alcohol, including a water adsorption step of adsorbing water of a water-alcohol mixture on an adsorption column to obtain a first concentrated alcohol, a water desorption step of introducing an alcohol to obtain a hydrous alcohol, and a membrane separation step of introducing the hydrous alcohol into a membrane separation unit provided with a membrane composite containing zeolite having an SiO.sub.2/Al.sub.2O.sub.3 molar ratio of 5 to 15 to obtain a second concentrated alcohol.

Separation processes using engineered osmosis are disclosed generally involving the extraction of solvent from a first solution to concentrate solute by using a second concentrated solution to draw the solvent from the first solution across a semi-permeable membrane. Enhanced efficiency may result from using low grade waste heat from industrial or commercial sources.

Provided is a method for separating a specific gas from a raw gas using a gas separation membrane module that includes a gas separation membrane element enclosed in a housing. The element includes a gas separation membrane including a hydrophilic resin composition layer. The method includes: preparing the module; increasing pressure in an interior of the module; increasing a temperature in the interior; and feeding a raw gas to the interior. The layer of the module prepared is adjusted to contain moisture, and a moisture content thereof is an amount that allows an equilibrium relative humidity at a temperature of 23 C. of a gas phase portion in the housing to be 10% RH or more. The raw gas feeding step is performed after the preparation step. The pressure increase step and the temperature increase step are performed after the preparation step and before the raw gas feeding step.

Provided is a method for separating a specific gas from a raw gas using a gas separation membrane module that includes a gas separation membrane element enclosed in a housing. The element includes a gas separation membrane including a hydrophilic resin composition layer. The method includes: preparing the module; increasing pressure in an interior of the module; increasing a temperature in the interior; and feeding a raw gas to the interior. The layer of the module prepared is adjusted to contain moisture, and a moisture content thereof is an amount that allows an equilibrium relative humidity at a temperature of 23 C. of a gas phase portion in the housing to be 10% RH or more. The raw gas feeding step is performed after the preparation step. The pressure increase step and the temperature increase step are performed after the preparation step and before the raw gas feeding step.