Brayton cycle adsorption desalination system

Patent metadata

Field	Value
Publication number	US-11311818-B1
Application number	US-202117487252-A
Country	US
Kind code	B1
Filing date	Sep 28, 2021
Priority date	Sep 28, 2021
Publication date	Apr 26, 2022
Grant date	Apr 26, 2022

Abstract

A Brayton cycle adsorption desalination system includes an adsorption desalination system including an evaporator for evaporating saline water to obtain water vapor, an adsorbent bed for adsorbing and desorbing the water vapor, and a condenser for condensing the water vapor to obtain distilled water. The Brayton cycle adsorption desalination system further includes a Brayton cycle system including a primary heat exchanger (PHE) and a cooler configured to cool an exhaust from the PHE. The Brayton cycle system and the adsorption desalination system are connected at the PHE so that the PHE is configured to function as a heat source for the adsorbent bed. The Brayton cycle system and the adsorption desalination system are connected at the cooler so that the evaporator is configured to absorb heat rejected from the cooler.

First claim

The invention claimed is:

1. A Brayton cycle adsorption desalination system, comprising:
an adsorption desalination system comprising an evaporator for evaporating saline water to obtain water vapor, an adsorbent bed for adsorbing and desorbing the water vapor, and a condenser for condensing the water vapor to obtain distilled water; and
a Brayton cycle system comprising a primary heat exchanger (PHE) and a cooler configured to cool an exhaust from the PHE,
wherein the Brayton cycle system and the adsorption desalination system are connected at the PHE so that the PHE is configured to function as a heat source for the adsorbent bed, and
the Brayton cycle system and the adsorption desalination system are connected at the cooler so that the evaporator is configured to absorb heat rejected from the cooler.

2. The Brayton cycle adsorption desalination system of claim 1 ,
wherein the Brayton cycle system further comprises:
a compressor that compresses a working fluid from a low pressure to a high pressure;
a recuperator that pre-heats the working fluid to obtain a pre-heated working fluid;
a heater that heats the pre-heated working fluid to obtain a heated working fluid; and
a turbine through which the heated working fluid passes such that the heated working fluid expands to output work and obtain an expanded working fluid,
wherein the expanded working fluid passes through the PHE to obtain the exhaust.

3. The Brayton cycle adsorption desalination system of claim 2 , wherein the compressor, the recuperator, the heater, the turbine, the PHE, and the cooler are configured to define a closed path cycle for the working fluid, wherein:
an outlet of the compressor is connected to a first inlet of the recuperator,
a first outlet of the recuperator is connected to an inlet of the heater,
an outlet of the heater is connected to an inlet of the turbine,
an outlet of the turbine is connected to an inlet of the PHE,
an outlet of the PHE is connected to a second inlet of the recuperator,
a second outlet of the recuperator is connected to an inlet of the cooler, and
an outlet of the cooler is connected to an inlet of the compressor.

4. The Brayton cycle adsorption desalination system of claim 3 , wherein:
the recuperator comprises a heat exchanger for a compressed working fluid from the compressor and the exhaust from the PHE to exchange heat.

5. The Brayton cycle adsorption desalination system of claim 1 , wherein the adsorption desalination system comprises:
two or more adsorbent beds that operate in an alternate sequence of adsorption and desorption modes, and
a switching valve configured to control the alternate sequence of adsorption and desorption modes.

6. The Brayton cycle adsorption desalination system of claim 1 , further comprising a storage tank such that the storage tank, the PHE and the adsorbent bed are configured to define a closed path cycle for a heat transfer medium, wherein:
an outlet of the storage tank is connected to an inlet of the PHE,
an outlet of the PHE is connected to an inlet of the adsorbent bed, and
an outlet of the adsorbent bed is connected to an inlet of the storage tank.

7. The Brayton cycle adsorption desalination system of claim 1 , wherein the PHE and the adsorbent bed are in direct contact for heat exchange.

8. The Brayton cycle adsorption desalination system of claim 1 , further comprising a coolant storage tank such that the coolant storage tank, the cooler and the evaporator are configured to define a closed path cycle for a coolant, wherein:
an outlet of the coolant storage tank is connected to an inlet of the cooler,
an outlet of the cooler is connected to an inlet of the evaporator, and
an outlet of the evaporator is connected to an inlet of the coolant storage tank.

9. The Brayton cycle adsorption desalination system of claim 1 , wherein the evaporator and the cooler are in direct contact for heat exchange.

10. The Brayton cycle adsorption desalination system of claim 2 , wherein the working fluid comprises supercritical carbon dioxide.

11. The Brayton cycle adsorption desalination system of claim 1 , wherein the adsorbent bed comprises silica gel for adsorbing and desorbing water vapor.

Assignees

• Univ King Abdulaziz

Inventors

• Almatrafi Eydhah
• Narasimhan Arunkumar
• Kamal Rajeev

Classifications

• F02C1/05

  characterised by the type or source of heat, e.g. using nuclear or solar energy · CPC title

• Y02A20/124

  Water desalination · CPC title

• Y02C20/40

  of CO2 · CPC title

• B01D1/0082

  Regulation; Control · CPC title

• B01D5/006 Primary

  with evaporation or distillation · CPC title