Hydro-osmotic Power Generation from Low-Temperature Waste Heat

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Solution Overview

Problem

Current technologies for converting low-temperature waste heat into electrical energy are limited by low efficiency and high capital costs, particularly for temperature ranges of 150-275°C, where existing systems like Steam Rankine Cycles, Organic Rankine Cycles, and Kalina cycles have efficiencies ranging from 1% to 15% and are economically impractical.

Innovation Solution

A power generation system utilizing forward osmosis with CO2-philic polymers, such as amine-terminated branched polyethylene glycols, that regenerate using CO2 absorption, allowing for high osmotic pressure differences to drive water across a semi-permeable membrane, generating power through a hydro-turbine, and utilizing a heat exchanger to efficiently transfer waste heat, thereby achieving efficiencies greater than 25%.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Use of energy by moving object

If conventional heat engine cycles (Steam Rankine, Organic Rankine, Kalina) are used for low-temperature waste heat conversion, then power generation is achieved, but thermal efficiency remains low (1-15%) due to Carnot efficiency limitations at low temperature differences

Engineering Contradiction:
Improvethermal efficiencyVSAvoidsystem complexity
Core Design Contradiction:
Use of energy by moving objectVSDevice complexity

Solution Approach 1:

The patent replaces the thermal-mechanical conversion system (heat engine cycles with turbines) with a direct osmotic-hydroelectric conversion system. Forward osmosis membranes convert thermal energy directly into hydraulic pressure through osmotic effects, eliminating the intermediate thermal-mechanical conversion step that is constrained by Carnot efficiency. This substitution enables high efficiency conversion of low-temperature heat without complex heat engine machinery.

Inventive Principle:
Principle #28Mechanics substitution (Replace mechanical system)

Solution Approach 2:

The patent changes the fundamental conversion parameter from temperature difference (ΔT) to osmotic pressure difference. Instead of relying on small temperature differences (150-275°C) to drive heat engines, the system uses osmotic pressure generated by concentration gradients across membranes to drive water flow through hydro-turbines. This parameter transformation bypasses Carnot limitations and enables efficient conversion at low temperatures.

Inventive Principle:
Principle #35Parameter changes

2Use of energy by moving object

If heat exchanger surface area is increased to improve heat transfer from low-temperature waste heat sources, then heat recovery efficiency improves, but capital costs increase disproportionately

Engineering Contradiction:
Improveheat recovery efficiencyVSAvoidcapital cost
Core Design Contradiction:
Use of energy by moving objectVSEase of manufacture

Solution Approach 1:

The patent uses hydraulic principles to amplify small pressure differences generated by osmosis into sufficient driving force for water flow through hydro-turbines. The osmotic pressure, though small in absolute terms, is efficiently converted into hydraulic energy that can drive turbines without requiring large heat transfer surface areas. This hydraulic amplification reduces the need for extensive heat exchanger surfaces.

Inventive Principle:
Principle #29Pneumatics and hydraulics

3Use of energy by moving object

If forward osmosis with CO2-philic polymers is used for power generation, then thermal efficiency exceeds 35%, but system complexity increases due to CO2 absorption and regeneration processes

Engineering Contradiction:
Improvethermal efficiencyVSAvoidprocess complexity
Core Design Contradiction:
Use of energy by moving objectVSDevice complexity

Solution Approach 1:

The patent implements a cyclic process where CO2 is temporarily absorbed by the polymer draw solution to generate high osmotic pressure for power generation, then recovered and released to regenerate the polymer for reuse. The CO2 is not discarded but cycled through absorption and desorption stages, enabling continuous operation. This recovery approach maintains high efficiency while managing the complexity through systematic material cycling.

Inventive Principle:
Principle #34Discarding and recovering

Solution Approach 2:

The system operates in periodic cycles: CO2 absorption phase generates high osmotic pressure and power generation, followed by CO2 desorption phase that regenerates the polymer draw solution. This periodic operation allows the system to alternate between power generation mode and regeneration mode, managing process complexity through time-separated functions rather than simultaneous operations.

Inventive Principle:
Principle #19Periodic action

Applied Scientific Principles

This section explains which scientific principles are used to turn an abstract innovation direction into a practical engineering solution.

Function Achieved in This Case

The system achieves thermal efficiency exceeding 35% in converting low-temperature waste heat to power, significantly surpassing existing methods like Organic Rankine cycles and Kalina cycles, while reducing capital costs by using commercially available membranes and materials, and minimizing heat transfer requirements.

Implementation Method 1

CO2-philic polymers, such as amine-terminated branched polyethylene glycols, that regenerate using CO2 absorption

Methodology Applied
Scientific EffectCO2 absorption: Absorption (physical)

Implementation Method 2

high osmotic pressure differences to drive water across a semi-permeable membrane

Methodology Applied
Scientific EffectOsmosis: Osmosis

Implementation Method 3

utilizing a heat exchanger to efficiently transfer waste heat

Methodology Applied
Scientific EffectHeat transfer: Conduction (thermal)

Data Source

PatentUS10143970B2Power generation from low-temperature heat by hydro-osmotic processes
Publication Date: 2018.12.04 NRGTEK INC
  • US10143970B2 patent drawing

AI summary

A system and method for generating power from waste heat, the system including (1) a forward osmosis module having an FO membrane a water inlet, a water outlet, a draw solution solute inlet and a diluted draw solution outlet; (2) a hydro-turbine using the diluted draw solution for generating power; (3) a CO2 absorption reactor to permit the introduction of compressed CO2 into the diluted draw solution to cause substantial separation of draw solution solute from the water, which water can be processed for subsequent recycling to the FO module, the CO2 absorption reactor configured to discharge a mixture of separate draw solution solute and absorbed CO2; and (4) a heat exchanger for transferring waste heat from an incoming heated fluid to the mixture of draw solution solute and CO2.