Coldry – A gateway solution to high value-add

Drying lignite is easy. Drying it efficiently and cost-effectively is much more complex.

For some, drying low-rank coal isn’t terribly exciting when compared to the technical complexity of some cutting edge coal conversion processes. Nevertheless, drying is a fundamental requirement before lignite can be further upgraded to produce oil, gas, chars, fertilisers and the myriad of other higher-value downstream products, including high efficiency electricity generation such as Super Critical and Ultra Super Critical.

Cost effective drying is the ‘gateway’ to higher value-added outcomes for lignite asset owners. For ‘downstream’ technology providers, it’s an enabler, creating new markets for their existing technology.

Thermax is a great example of this. They make power stations designed to use black coal. By integrating Coldry into their power station designs, they would be able to offer their existing suite of solutions to brown coal mine owners, which are higher efficiency, lower CO2 emitting assets.

Now, this ability to use lignite in place of black coal is important from another perspective too. Keep in mind as you read ahead that the majority of coal consumed is higher rank coal (e.g. black coal, thermal coal, steam coal, coking coal) yet more than half of our global reserves are lower rank coal such as lignite and sub-bituminous.

image-coal rank and resources
Low-rank coal is under utilised due largely to its higher moisture and lower net energy content, yet it is a better candidate for coal conversion in most cases, due to its higher reactivity and yield of gas and oil, compared to higher rank coal.

A note on fossil fuels vs. renewables: While the desire to move away from coal toward renewables is strong, coal is forecast to remain the dominant source of electricity globally for decades to come. The EIA expects coal consumption to rise by 38% from 2012 to 2035. Lignite is expected to increase in demand as its value as a feedstock for conversion to oil, gas and fertiliser and relatively low price compared to black coal drives consumption. Underpinning the longevity of coal is the problem of scale and cost for renewables. Wind and solar require significantly larger footprints to generate the same amount of electricity as coal and cost significantly more per unit of energy. Solar and wind also require back up for times when the sun doesn’t shine and wind doesn’t blow. Typically gas-fired power generation is used as it can be adjusted quickly compared to coal-fired stations. So, in addition to the cost of building and maintaining the solar and wind generators, we need to build sufficient gas generators, adding significantly to the cost of the solar-wind system.

With this bit of background in mind, let’s take a deeper look at the ‘Gateway’ solution covered in our last article (http://www.ectltd.com.au/newsletters/developing-fit-for-purpose-coldry-pellets-for-key-markets/) and explain what it all means, starting with a recap of the Coldry process itself, then drilling down a little on how we program the process to produce a fit for purpose, dry lignite product that’s an ideal feedstock for downstream conversion processes.

First, a quick recap on the Coldry process itself to provide some context around the ‘gateway’ concept.

The Coldry process achieves cost-effective drying through the combination of two distinct mechanisms that result in very low purchased energy input:

  1. Brown coal densification
  2. Low-grade waste heat utilisation

Brown coal densification involves the destruction of the coal porous structure via mechanical shear, leading to mobilisation of the trapped moisture. The shearing of the coal structure effectively reduces the particle size of the dry matter. The mobilised moisture and finely sheared coal particles form a paste, which is extruded under mild pressure to form the cylindrical pellet shape. The process of Brown coal densification is initiated during this step. This topic can get extremely technical, but suffice to say the rate and extent of densification is influenced by shear level, temperature, particle sizing and pH level among other variables, which can be manipulated within the process to achieve the desired outcome.

A note on removing moisture from lignite

There are three types of moisture to consider when drying lignite:

(1) Surface moisture; this type isn’t locked in and is subject to simple evaporative removal. The energy required to evaporate is the latent heat of evaporation (~2.3MJ/kg).

(2) Structurally bound (trapped) moisture; this type is held in the porous structure of the coal, requiring more energy to force the moisture to the surface.

(3) Chemically bound moisture; also known as inherent moisture, internal atomic bonding increases the holding strength of water molecules around and within coal particles, requiring yet more energy to remove.

At this point, the extruded pellet has the consistency of play-doh. It’s tacky, and if piled too deep, can stick to other pellets and deform under their collective weight. So, they’re conditioned on a shallow bed, mesh conveyor, where warm air provides sufficient drying to the pellet surface to eliminate the tackiness and develop enough strength to withstand both placement into the packed bed dryer, and the weight of the pellets that are deposited on top, shortly after.

As the pellets move vertically down through the packed bed dryer, warm air is passed horizontally through the bed of pellets, taking up the moisture that’s being expelled as the pellet densifies and shrinks. The porous structure collapses forcing moisture inside the pellet to migrate to the surface, where it evaporates at a steady rate and is carried away by air and vented to atmosphere as water vapour.

A note on water recovery: If desired, the saturated air can be condensed, recovering the moisture. This involves an energy cost, so is optional and it’s deployment depends on the need for high-quality water at the site and the cost of alternative sources of supply.

Through the extensive pilot and bench scale testing over several years, we were able to focus not only on scaling up the process, but also on refining the parameters that influence the strength of the pellet.Developing a commercial process around these two drivers (brown coal densification and waste heat utilisation) has been the main focus of our research activities that have taken us through several design iterations at our Pilot Plant and underpinned our current detailed, project-specific engineering works with engineering partner Thermax in India.

The result has been a stepwise improvement in density and strength and a reduction in fines generation through transport and handling, as outlined in our previous article (http://www.ectltd.com.au/newsletters/developing-fit-for-purpose-coldry-pellets-for-key-markets/)

In our quest for tougher pellets, we ran the Coldry process in countless configurations, varying pellet size, residence time in the mill and extruder pressure, among a range of other variables.

We found that higher temperatures of around 60-90°C accelerated the drying time but resulted in some reduction in pellet strength; Clearly, not the objective when aiming for an exportable product.

However, we also noticed that the throughput of a given plant footprint increased significantly, translating to lower cost per tonne; Clearly ideal when designing for an integrated front-end drying process where the need for robust handling properties is significantly less.

Gateway concept

The ‘Gateway’ concept was born.

Put simply, under this deployment scenario the Coldry process is designed to closely integrate with a downstream process such as a pyrolysis, gasification or conversion plant. This close integration maximises waste heat transfer, delivering potentially up to 90°C temperatures, creating a ‘rapid-dry’ pellet.

This pellet is lower strength than ‘export’ grade Coldry, however this doesn’t matter as it’s destined for near-immediate delivery to the downstream process. No transport, no large stockpiles. It’s tough enough for the target process without being ‘over-engineered’.

picture-coldry products 2
Image: From left to right, our gateway, domestic and export grade Coldry products.

The cost-saving implications for this type of deployment are significant, given the need to minimise production cost to ensure the viability of the overall conversion process being deployed.

Conversion Pathways

 

image-coldry gateway solutionThe above diagram highlights the role of the Coldry ‘Gateway’ product in value-added projects aimed at creating new market for lignite asset owners and diversifying supply options for technology owners and project developers as they work to meet energy and resource demands.

Drying alternatives

Lignite drying has been around for a long time and broadly fit into two categories:

  • Evaporative
  • Non- evaporative

Steam Tube Drying (STD) has been the mainstay of established evaporative methods since the 1920’s and, as the name suggests, applies indirect heat from steam via a rotating tube-in-shell heat exchanger to evaporate the moisture from the lignite.

Flash mill and rotary drum dryers apply direct heat, with coal particles contacting a flow of recycled hot flue gas or pre-heated air to drive evaporation. These methods are generally less efficient than STD and risks such as fire and explosion need to be carefully managed.

The above methods require high-grade energy and are generally higher pressure and as a consequence, higher cost.

Other evaporative methods include Fleissner, Geo-coal, GTLE, SynCoal, Encoal. and LiMax.

On the non-evaporative team sit processes such as hydrothermal dewatering, microwave drying, UBC and Mechanical Thermal Expression.

Hydrothermal dewatering and mechanical thermal expression have a significant waste water clean up challenge. Microwave drying utilises a considerable amount of purchased energy. UBC uses an expensive light oil to displace the water within the coal, as well as significant temperature and pressure.

image-coldry competitors

The chart above shows how the Coldry process compares to other drying processes on the market or under development in terms of pressure and temperature.

The key takeaway from this chart is that Coldry is both lower in temperature and pressure than other drying methods, resulting in cost and operational efficiencies and net CO2 benefits.

The Coldry ‘Gateway’ process delivers what we believe to be the most cost-effective, CO2 effective front-end drying solution for higher value lignite conversion processes, enabling new markets for lignite asset owners and downstream technology providers.

As we progress the planned demonstration of the Coldry process in India, we’ll be working with Thermax to develop integrated solutions that take maximum advantage of our Gateway product to deliver highly efficient, drying and power generation systems, extending to other value added processes and projects as opportunities are developed.

For further information contact:

Ashley Moore – Managing Director info@ectltd.com.au