COMPRESORP - Twin Screw Compressor
Projects

COMPRESORP

Upgrading low temperature waste water streams of separation processes with compression resorption heat pumps.

Goal

The goal of the COMPRESORP project is to upgrade low temperature waste streams from the process industry (e.g. cooling water from cooling towers) into valuable utility streams making use of compression-resorption heat pumps which operate in the wet regime.

Incentive

Thermal energy (heat) represents a large part of the global energy usage and about 43% of this energy is used for industrial applications. Ultimately, 20-50% of the energy used is lost via waste heat contained in hot exhaust gases and liquid streams. Nevertheless the share of waste heat recovery (upgraded energy) within the total energy used is still negligible.

Compression Resorption heat Pumps (CRHP) can be used to upgrade waste water streams to streams which are applicable for heating and cooling purposes. In this way the rest heat available inthese streams can be re-used in the separation processes. Waste water streams with temperatures in the range 35 to 60°C can be partly cooled down to 5°C and partly heated up to temperatures above the 110°C. These product flows with higher exergy can be used in separation processes which need cooling / heating respectively. Limiting for the commercial introduction of these cycles in practice is the unavailability of compressors which can operate under the operating conditions required by these cycles.

Objective

The focus of this project is on the development of a compressor suitable for the operating conditions of compression resorption cycle and its integration in the cycle.

A compressor prototype suitable for the operating conditions of compression-resorption heat pump cycles for heat recovery will be designed and experimentally tested.

Results

The impact of adding small amounts of CO2 to the working fluid has been investigated. Indicating a ca. 5% improvement in COP.

COP of CRHPs heating pressurized water from 90 to 130 °C (a) and from 60 to 140 °C (b). Solid lines apply for NH3-H2O systems and dotted lines apply for NH3 -H2O-CO2 systems.

A thermodynamic model has been developed for twin-screw wet compressors which allows localization of major irreversibility losses during the compression process in CRHPs.

Main irreversibility losses during compression

An experimental set-up has been constructed at the TU Delft to test the performance of the wet compressor prototype.

A summary of the results can be found in Gudjonsdottir PhD thesis.

Acknowledgement & partners

This project is co-funded by TKI-E&I with the supplementary grant 'TKI- Toeslag' for Topconsortia for Knowledge and Innovation (TKI’s) of the Ministry of Economic Affairs and Climate Policy.