B01D1/10

GRAIN ALCOHOL DISTILLATION PLANTS
20170266582 · 2017-09-21 · ·

Improvements in grain alcohol distillation plants by incorporating a novel internal arrangement in the wort column and the rectifying column with distributors and accumulators inside thereof, achieving a stable and safe process in wide ranges of operation, guaranteeing the productivity of the plant and the quality of the products. The wort column features detachable perforated plates, easy to access and clean through manholes. By having easily detachable plates and, also, a manhole for each plate with “holder” type connections, the access to the interior of the column for cleaning and maintenance purposes is facilitated. The rectifying column is a special filling column with flow distributors, it has an intermediate alcohol accumulator and a condenser which is an integral part of the column that prevents the use of pumps. The arrangement of distributors and accumulators within the rectifying column favors the operational stability of the plant, allowing a low scale equipment to work similarly to an industrial scale column. The improvements include an integrated automation system with Internet communication for self-management of the plant with remote monitoring and autonomous operation.

GRAIN ALCOHOL DISTILLATION PLANTS
20170266582 · 2017-09-21 · ·

Improvements in grain alcohol distillation plants by incorporating a novel internal arrangement in the wort column and the rectifying column with distributors and accumulators inside thereof, achieving a stable and safe process in wide ranges of operation, guaranteeing the productivity of the plant and the quality of the products. The wort column features detachable perforated plates, easy to access and clean through manholes. By having easily detachable plates and, also, a manhole for each plate with “holder” type connections, the access to the interior of the column for cleaning and maintenance purposes is facilitated. The rectifying column is a special filling column with flow distributors, it has an intermediate alcohol accumulator and a condenser which is an integral part of the column that prevents the use of pumps. The arrangement of distributors and accumulators within the rectifying column favors the operational stability of the plant, allowing a low scale equipment to work similarly to an industrial scale column. The improvements include an integrated automation system with Internet communication for self-management of the plant with remote monitoring and autonomous operation.

Photovoltaic distiller for the recycling of greywater to potable water
11285398 · 2022-03-29 ·

A low to medium output solar fluid evaporation/distillation system is described that is practical to manufacture using current photovoltaic solar panels or enhanced photovoltaic panels designed exclusively for this application. The system works in conjunction with a water feed in system that provides a minimum quality of water or other fluid to the distillation chamber. The system utilizes a warming envelope and can have optimized dielectric mirrors designed to enhance the water purity and increase output.

Apparatus and method for separation of components with different volatility in a mixed fluid
11097200 · 2021-08-24 · ·

The invention concerns an apparatus (10) for separation of components with different volatility in a mixed fluid, said apparatus (10) comprising: a first heat exchanging unit (100) provided with first and second flow path structures (131, 132) forming separate flow paths for a first and a second fluid flow through the first heat-exchanging unit (100); an inlet (118) for feeding the mixed fluid to the apparatus (10); an inlet (119) for feeding steam to the apparatus (10); an arrangement for feeding a cooling medium through the apparatus (10), wherein said arrangement comprises at least one cooling medium inlet (105, 106, 107, 108). The invention is characterized in that the apparatus (10) comprises a second heat-exchanging unit (200) provided with third and fourth flow path structures (233, 234) forming separate flow paths for a first and a second fluid flow through the second heat-exchanging unit (200), wherein the cooling medium arrangement comprises at least one cooling medium inlet (205, 206, 207, 208) arranged in fluid communication with the fourth flow path structure (234) and wherein the first and third flow path structures (131, 233) are arranged in fluid communication with each other.

Apparatus and method for separation of components with different volatility in a mixed fluid
11097200 · 2021-08-24 · ·

The invention concerns an apparatus (10) for separation of components with different volatility in a mixed fluid, said apparatus (10) comprising: a first heat exchanging unit (100) provided with first and second flow path structures (131, 132) forming separate flow paths for a first and a second fluid flow through the first heat-exchanging unit (100); an inlet (118) for feeding the mixed fluid to the apparatus (10); an inlet (119) for feeding steam to the apparatus (10); an arrangement for feeding a cooling medium through the apparatus (10), wherein said arrangement comprises at least one cooling medium inlet (105, 106, 107, 108). The invention is characterized in that the apparatus (10) comprises a second heat-exchanging unit (200) provided with third and fourth flow path structures (233, 234) forming separate flow paths for a first and a second fluid flow through the second heat-exchanging unit (200), wherein the cooling medium arrangement comprises at least one cooling medium inlet (205, 206, 207, 208) arranged in fluid communication with the fourth flow path structure (234) and wherein the first and third flow path structures (131, 233) are arranged in fluid communication with each other.

BRINE SOLUTION CLEANING SYSTEMS, APPARATUSES, AND METHODS
20210269330 · 2021-09-02 ·

Systems, apparatuses, and methods for cleaning brine solution are provided. In particular, one or more embodiments comprise a brine cleaning system that includes a brine cooker, a brine filter, and a brine storage unit. The brine cooker heats a dirty brine solution to separate the dirty brine solution into a liquid portion and a solids portion. The brine filter is coupled to the brine cooker to receive the liquid portion and the solids portion from the brine cooker and then substantially remove the solids portion. The brine storage unit is coupled to the brine filter to accumulate the liquid portion once the solids portion have been substantially removed by the brine filter. This allows for more efficient and environmentally friendly use of brine solution in the curing of animal.

Brine solution cleaning systems, apparatuses, and methods

Systems, apparatuses, and methods for cleaning brine solution are provided. In particular, one or more embodiments comprise a brine cleaning system that includes a brine cooker, a brine filter, and a brine storage unit. The brine cooker heats a dirty brine solution to separate the dirty brine solution into a liquid portion and a solids portion. The brine filter is coupled to the brine cooker to receive the liquid portion and the solids portion from the brine cooker and then substantially remove the solids portion. The brine storage unit is coupled to the brine filter to accumulate the liquid portion once the solids portion have been substantially removed by the brine filter. This allows for more efficient and environmentally friendly use of brine solution in the curing of animal.

Methods of distillation
10913010 · 2021-02-09 · ·

In an improved method of distilling fluids, some or all of the fluid is recovered as distillate and the fluid is situated in the shell side of a first shell and tube heat exchanger. The fluid to be recovered as distillate is successively boiled, demisted, compressed and then introduced into upper ends of the tubes. A second shell and tube heat exchanger is located below the first heat exchanger, and distillate from upper ends of the tubes in the second heat exchanger are arranged to receive distillate liquid and/or vapor from the lower ends of tubes of the first heat exchanger. The fluid is located in the shell of the second heat exchanger and that fluid is heated but is not boiled. A mechanism is provided to supply at least some of the heated fluid to the shell of the first heat exchanger.

Photovoltaic Distiller for the Recycling of Greywater to Potable Water
20210008463 · 2021-01-14 ·

A low to medium output solar fluid evaporation/distillation system is described that is practical to manufacture using current photovoltaic solar panels or enhanced photovoltaic panels designed exclusively for this application. The system works in conjunction with a water feed in system that provides a minimum quality of water or other fluid to the distillation chamber. The system utilizes a warming envelope and can have optimized dielectric mirrors designed to enhance the water purity and increase output.

APPARATUS AND METHOD FOR SEPARATION OF COMPONENTS WITH DIFFERENT VOLATILITY IN A MIXED FLUID
20200215452 · 2020-07-09 ·

The invention concerns an apparatus (10) for separation of components with different volatility in a mixed fluid, said apparatus (10) comprising: a first heat exchanging unit (100) provided with first and second flow path structures (131, 132) forming separate flow paths for a first and a second fluid flow through the first heat-exchanging unit (100); an inlet (118) for feeding the mixed fluid to the apparatus (10); an inlet (119) for feeding steam to the apparatus (10); an arrangement for feeding a cooling medium through the apparatus (10), wherein said arrangement comprises at least one cooling medium inlet (105, 106, 107, 108). The invention is characterized in that the apparatus (10) comprises a second heat-exchanging unit (200) provided with third and fourth flow path structures (233, 234) forming separate flow paths for a first and a second fluid flow through the second heat-exchanging unit (200), wherein the cooling medium arrangement comprises at least one cooling medium inlet (205, 206, 207, 208) arranged in fluid communication with the fourth flow path structure (234) and wherein the first and third flow path structures (131, 233) are arranged in fluid communication with each other.