The task of reducing energy costs and creating more sustainable local energy sources is a familiar challenge across many industry sectors. Polyolefin process plants require a considerable amount of energy, often in the form of steam. Given the challenge of coming up with a more sustainable solution that would reduce its energy use, engineers focused on the untapped potential of low-pressure steam.
In an ongoing pilot project, this particular polyolefin plant, located in the Dutch municipality of Terneuzen, uses mechanical vapor recompression (MVR) to upgrade low-pressure steam so it can be reused to supply energy. Central to this MVR solution is an Atlas Copco Gas and Process two-stage centrifugal compressor that compresses superheated steam from 3 barg to 12.5 barg in two steps. The result has been a significant reduction of natural gas usage and a net reduction in CO2 emissions.
Power to Products: electrification and flexibility
The story goes back to 2014 and the Dutch government’s “Power to Products” project, in which numerous companies from the process industry, energy suppliers, network operators and technology partners came together to address three interrelated central points: how, at what cost and revenues, and under what conditions the process industry could make its electricity demand more flexible. The aim was to allow the process industry to use cheap renewable wind and solar electricity while at the same time contributing to grid stability.
The process industry can achieve this in two ways: increased electrification and greater flexibility. The first, electrification, simply means that the industry will use electricity instead of fossil fuels, such as natural gas. The second, flexibility, means that the process industry can offer control of power requirements, which it does in two possible ways: One is by storing energy during those cheaper moments (in chemical products and intermediates, such as hydrogen, as pressure, or heat or cold thermal storage via charging and discharging) and then using this later, during the more expensive periods. The second way is to reduce production and power demand temporarily at expensive times, and then catch up later when the price is reduced.
By doing this, industry helps in reducing the demand for fossil fuels and reducing CO2 emissions. The result is to make the overall energy supply more sustainable and cost efficient.
Mechanical vapor recompression
For its part in the Power to Products project, our customer chose mechanical vapor recompression. MVR, or in this case steam recompression, is a good example of the electrification of industrial energy demand. It is also a highly energy-efficient solution because residual heat is upgraded to high-quality heat.
MVR technology was appealing in this case because of the availability of low-pressure steam at the Terneuzen polyethylene processing plant, even though the supply is not constant (especially during winter, when it is needed to heat buildings and for steam tracing). In contrast, when the plant is running steam turbines, or during summer when buildings are not heated, there is excess. Usually, excess low-pressure steam is condensed and the water sent to the boiler to create high-pressure steam.
A feasibility study for steam recompression, with the aim of using MVR to convert heat from condensation to efficient energy, was undertaken in 2015. The polyethylene plant uses water for reactor cooling. At the end of the process, the cooling water becomes low-pressure steam. Especially during the summer, the demand for heating is lower, which in some periods means that part of the low-pressure steam from the polyethylene plant cannot be used and must be sent to the atmosphere or is condensed. During the initial research phase, it became clear that MVR had the potential to be a good solution to avoid this waste of energy by uprating the steam to 12.5 barg or 35 barg.
MVR economically viable
The result of the 2015-2016 feasibility study showed that the MVR project was economically less feasible for the smaller flowrates, at 10 t/h. The most feasible case study from an economic viewpoint back then were those with 50t/h. However, Dow wanted to test the MVR technology on a small scale, with the prospect of including the technology in possible future polyethylene expansion projects (and other projects where this would be an option).
Key to the decision on which of the tens of case studies to use for the MVR pilot project, therefore, was selection based on the preferred steam pressure level rather than a more attractive flow rate. In this case it meant using the low-pressure steam (from the reactor cooling water) that supplies the 3.5 barg grid. This is used mostly for process heating purposes and upgrading it to the lowest pressure level would result in less firing of the auxiliary boilers and a reduction of fossil-fuel usage. For this reason, even though 3.5 barg (10 t/h) was economically less attractive, this lower pressure provided the best conditions for the pilot’s primary aim: simply testing the technology. The MVR pilot project got underway in 2018.
Selecting integrally geared compression for MVR
Atlas Copco Gas and Process was chosen as the rotating equipment partner for the Terneuzen pilot project, with its proposed solution of an integrally geared centrifugal compressor playing a central role. The company has more than 30 years of experience in the steam compressor field, and each compressor can be designed to specific process and control requirements. This wealth of experience includes working on projects upgrading low-pressure steam to high-pressure steam and enabling it to be used as an energy source.
A key compressor characteristic is its overhung arrangement of the impellers on the pinion shaft ends. One pinion shaft is designed for one or two (opposing) compressor stages and separate compressor bearings are not necessary.
The bearings of the pinion shafts are identical to those of the compressor rotor, and the rotor shafts are made from a single piece of heat-treated forged low-alloy steel. Shaft seals can be labyrinths, dry gas seals or, as used at this polyolefin facility, floating carbon rings. The high-speed rotors use tilting pad bearings and sleeve bearings for the slow-speed shaft, while multiple disk couplings connect the driver and the compressor gear box. Operational control is via a fixed-speed E-motor drive with inlet guide vanes (IGV) installed upstream of the first stage impeller (which is part of the compressor casing)
By making use of the untapped potential of low-pressure steam via mechanical vapor recompression, plant operators successfully found a more energy efficient and sustainable supply of energy. The project additionally highlighted that MVR has the potential to be used anywhere where there is low-pressure steam. The key component at this particular plant was an Atlas Copco two-stage centrifugal compressor, which compresses superheated steam from 3 barg to 12.5 barg in two steps.
The compressor now operates without significant problems, and it has only been briefly out of service for maintenance of the steam network. In a 12-month period in 2020/2021, approximately 10 million Nm³ of natural gas was saved and a CO2 reduction of 17.8 kton was achieved.
The integrally geared compressor features optimized aerodynamic speed capability with increasing rotor speeds along the compression process (something that helps maintain a compact design). Furthermore, its integral set up makes it possible to have intercooling, or as in this MVR (steam) application, to have a desuperheater after each stage of compression, which results in better overall efficiency.
The broadening use of this compression technology in hydrocarbon processing environments has been supported by several factors, including advances in shaft seal technology, modern aerodynamics, and increased rotor dynamic and thermodynamic knowledge. With these advances, added to their simplicity, reliability, light-weight and compact design, IGCs have become more widely accepted in the hydrocarbon world.
Two-stage compressor design
The MVR is a two-stage integrally geared centrifugal compressor that compresses superheated steam from 3 barg to 12.5 barg. The nominal mass flow of the installation is 12 tons per hour. Both at the inlet and between the stages, the steam is cooled by the injection of water with a desuperheater, and larger droplets are caught downstream by a knock-out drum. The steam enters the compressor on the suction side at 3 barg and a temperature of 150 to 220 °C – though the steam is sent through the desuperheater and knock-out drum in case of temperatures higher than 170 °C to avoid to higher temperatures in the compressor discharge stage.
Once the compressor was up and running, initial research on the compressor’s coefficient of performance (COP) was performed.
The result of 7.5 represents a high performance (this is partly attributable to the inherent advantage of an open heat pump compared to a normal compression heat pump). Between 17th of November 2020 and 17th of November 2021, the compressor had an isentropic efficiency of 76% to 77%, and with it an overall COP of 7.5 (a COP of 7.5 means that for 1 unit of electricity 7.5 units of steam were produced).
The COP value provides an indication of the energy efficiency of a range of machines, such as chillers, heat pumps and MVRs. In simple terms, COP shows the ratio between the recovered thermal power and the supplied electrical compressor power. COP experts expect that as efficiencies and the compressor design improve (such as it did with the replacement of the oil cooler in 2020) the COP value for the compressor at will increase.
Conclusion
By making use of the untapped potential of low-pressure steam via mechanical vapor recompression, plant operators successfully found a more energy efficient and sustainable supply of energy. The project additionally highlighted that MVR has the potential to be used anywhere where there is low-pressure steam. The key component at this particular plant was an Atlas Copco two-stage centrifugal compressor, which compresses superheated steam from 3 barg to 12.5 barg in two steps.
The compressor now operates without significant problems, and it has only been briefly out of service for maintenance of the steam network. In a 12-month period in 2020/2021, approximately 10 million Nm³ of natural gas was saved and a CO2 reduction of 17.8 kton was achieved.
Explore more about Atlas Copco Gas and Process
Follow the below links to learn more about our technology and solutions.