Desulfurization plant - Gazpack

Sulfur as an element is ubiquitous. In the universe, it ranks 10th inprevalence; on the earth, it comes in fifth. It is found in vitamins, amino acids, the earth&#;s crust, and virtually every plant and animal. There are myriad uses of sulfur in industry and agriculture, including herbicides, pesticides and fertilizers. Needless to say, it is a critical element in nature and in the economy. Nevertheless, when present in certain chemical compounds and mixtures, sulfur does not play well with others. These compounds can be hazardous to health; damaging to the ecology; and corrosive to many materials utilized for industrial purposes. The organisms and matter where these dangerous compounds are found must be subject to the desulfurization process.

CHIDA are exported all over the world and different industries with quality first. Our belief is to provide our customers with more and better high value-added products. Let's create a better future together.

What Does That Mean?

The desulfurization meaning is actually two-fold: it could refer to removing elemental sulfur at the molecular level or, alternatively, extracting sulfur compounds from chemical mixtures. On its own, sulfur can be extricated from subterranean deposits by melting it through the injection of water heated above the boiling point. Once melted, the sulfur is piped out to the surface. Simple enough. What, though, about those dangerous compounds that find themselves in diverse compositions like natural gas, biomass and petroleum, for instance? What does desulfurization look like when the element is bonded to others?

Natural Gas

Natural gas formations exist all over the world. The largest deposits are located in the Middle East, the Russian Federation and Europe. In North America, natural gas is most abundant in Texas, Oklahoma, New Mexico, Wyoming, and Louisiana. In the United States, over 50 percent of homes are heated by natural gas and this fuel accounts for 24 percent of energy use overall. Natural gas is also a constituent ingredient of many paints, plastics and even medicines. Propane gas &#; popular with avid grillers and barbecue enthusiasts &#; is also derived from natural gas.

Natural gas is often retrieved from its earthen deposits in the same manner as petroleum &#; through drilling or hydraulic fracturing. Sometimes a &#;horse head&#; pump is employed to draw both natural gas and oil to the surface. This resource is found in shale formations, coal beds and sandstone. Once the gas is drawn from its source, it is transported via 300,000 miles of pipeline to locations throughout the U.S., eventually available to customers. Before this lengthy trip, however, the gas must be treated to remove the hydrogen sulfide (H2S) and carbon dioxide (CO2).

The desulfurization of natural gas is necessary for two very important reasons. The H2S that is present is not only toxic to workers and consumers but it is also detrimental to the very pipeline networks that deliver the fuel. At its worst, it can induce respiratory failure, coma and even death to those exposed. Meanwhile, it can quickly oxidize the metal interiors of natural gas pipelines, thereby damaging their safety and overall efficiency. Therefore, natural gas needs treatment at a desulfurization plant soon after its retrieval from wherever it is deposited.

If hydrogen sulfide presence surpasses 5.7 milligrams per cubic meter of natural gas, the gas passes a threshold from user-grade to &#;sour&#; gas. Under such a circumstance the gas is ordinarily run through a tower or column that contains amine, i.e. a derivative of ammonia. The amine solution absorbs the H2S compound as the gas stream passes through, leaving a purer effluent natural gas in its wake. The amine solution is available for further use over many cycles of H2S removal. This procedure for H2S removal is performed in the vast majority of occasions when hydrogen sulfide absorbtion is necessary.

Biogas

Essentially, biogas is the methane (and CO2) that gets released from organic matter under anaerobic &#; or oxygen-deprived &#; conditions. This can take place naturally, as at the core of a compost heap or landfill, or it can be induced by human technology, i.e. engineered anaerobic digesters. Absent oxygen, bacterial micro-organisms operate on the organic material, breaking it down so that biogas is released from the solids that had retained it. The material is as diverse as sewage, food waste, compost, wastewater, rotting vegetation and animal manure. Once captured, the biogas powers combustion engines which, subsequently, charge electrical generators. Biogas can provide energy to vehicles, farms, neighborhoods and even public transit systems.

Still, biogas, too, has an H2S problem, the very same problem evident with natural gas. The public health threat and infrastructure impairment are equally real with biogas production. Fortunately, biogas desulfurization is available by means of two distinct methods.

1. Wet de-sulfurization &#; can be further broken down into three versions:

• Chemical absorption &#; is most akin to amine sweetening with natural gas. Besides amine, straight ammonia and carbonate serve as alternate solvents for the attraction and intake of hydrogen sulfide.
• Physical absorption &#; combines components of solvent with a drop in pressure to separate the H2S from the biogas.
• Wet oxidation &#; uses a weak basic solution to absorb and oxidize the H2S, thereby removing the elemental sulfur from the compound.

2. Dry de-sulfurization &#; rather than using a solvent or solution, dry de-sulfurization utilizes powder/particle agents to treat the biogas. Doing so minimizes the possibility of corrosion in the biogas tank. In general, this method works better when sulfur content is on the low side.

Once properly purified, biogas is an unsung hero of renewable fuels. Not only is it environmentally friendly and cost-effective, it answers a large part of the seemingly eternal waste management question.

Flue Gas

Hydrogen sulfide is not the only problematic sulfur compound in energy production. Sulfur dioxide (AO2) is emitted from exhaust flues at energy plants that burn fossil fuels and facilities that incinerate solid wastes. In nature, SO2 is released when volcanoes erupt. On a smaller scale, it is emitted whenever a match is lighted. Implicated in acid rain, SO2 is a major air pollutant that affects habitat livability and the survival of various plant and animal species.

How does flue gas desulfurization work? As with the categories noted above, there are multiple ways to do this. One such procedure is wet scrubbing. This involves an alkaline absorbent slurry &#; limestone, lime or even seawater &#; that is sprayed directly on the gas stream or pooled to receive the stream. At other times the slurry is converted to powder by means of hot gas. When the flue gas makes contact with the particles, a similar reaction removes the sulfur molecules. This method is known as spray-dry scrubbing. Other means of flow gas desulfurization are employed depending on sulfur content and related factors. Like atmospheric CO2 scrubbers, these treatments isolate the SO2 from the flue gas stream before it is released into the air.

The atmospheric residue desulfurization process helps to keep toxic particulates from doing damage to ecosystems and the air we breathe. The various methods heretofore mentioned take place in an atmospheric residue desulfurization unit where not only sulfur dioxide, but nitrogen oxides and other particulates are captured and isolated.

How Is Sulfur Retrieved from Compounds?

Many of the agents responsible for neutralizing H2S can separate the sulfur from its compounds. However, research demonstrates that an iron oxide sold sponge &#; i.e. wood shavings infused with iron, or ferric, oxide &#; is effective in hydrogen desulfurization by first absorbing the H2S, and then converting ferric oxide into ferric sulfide. The ferric sulfide subsequently reverts to ferric oxide after releasing elemental sulfur.

Adsorptive Desulfurization

Adsorptive Desulfurization is an innovative technique that has transformed the way we address the presence of sulfur in gas streams. At Gazpack, we pride ourselves on leveraging cutting-edge technology such as Adsorptive Desulfurization to remove sulfur from a variety of gases. This process involves adsorbents like zeolites, activated carbons, or metal-oxides that selectively trap sulfur compounds, resulting in a cleaned gas stream. Importantly, Adsorptive Desulfurization provides a more efficient, economical, and environmentally friendly alternative to conventional desulfurization methods, particularly when dealing with gas streams containing low concentrations of sulfur. 

In Summary

Energy sources with less CO2 emission than traditional fossil fuels promise greater energy independence and a cleaner environment. Yet even these gases have contaminants that require removal before they are burned for electrical generation or combusted for vehicular performance. The good news is that technology (desulfurization plant) provides for the removal of sulfur compounds before the energy is consumed.

Desulphurization of Liquid Steel

Desulphurization of Liquid Steel

Solubility of sulphur (S) in liquid iron (Fe) is quite high. But the solubility of S in solid iron is limited. It is 0.002 % in ferrite at room temperature and 0.013 % in austenite at around deg C. Hence, when liquid steel cools down, sulphur is liberated from the solution in the form of iron sulphide (FeS) which forms a eutectic with the surrounding iron. The eutectic is segregated at the iron grain boundaries. The eutectic temperature is comparatively low at around 988 deg C. Fe-FeS eutectic weakens the bonding between the grains and causes sharp drop in the properties of steel at the temperatures of hot deformation.

During the continuous casting of liquid steel, sulphur present in liquid steel (i) causes the formation of undesirable sulphides which promotes granular weaknesses and cracks in steel during solidification, (ii) lowers the melting point and inter-granular strength, (iii) contributes to the brittleness of steel and thus acts as stress raiser in steel, and (iv) results in the hot shortness. Sulphur, present in solid steel as FeS inclusions, has several detrimental effects on steel processing. During deformation, FeS inclusions act as crack initiation sites and zones of weakness. Such inclusions from sulphur adversely affect the toughness, ductility, formability, weldability, and corrosion resistance of steel. An increase in manganese (Mn) content (not less than 0.2 %) however, helps prevent formation of FeS. Sulphur is thus an undesirable element in steel. Manganese actively reacts with iron sulphides during solidification of steel transforming FeS to MnS according to the following reaction.

FeS (slag) + Mn (steel) = MnS (slag) + Fe

The melting temperature of manganese sulphide (MnS) is comparatively high (around deg C). Hence steel containing manganese can be deformed in hot state. However MnS inclusions (i) are brittle (less ductile than steel), (ii) may have sharp edges, and (iii) are located between the steel grains. All these factors determine negative influence of sulphide inclusions on the mechanical properties of steel.

Since sulphur is one of the detrimental impurities in the steel affecting both internal and surface quality, desulphurization of steel is essential during the steelmaking process. Also ever increasing specification requirements for material properties of various steel grades have resulted in an extreme demand on steel cleanliness. For the production of clean steel, especially with regards to the precipitation of sulphides, it is necessary that the sulphur content in liquid steel is kept as low as possible. In practice, the removal of sulphur from liquid steel is mainly achieved in ladles during secondary steelmaking.

Desulphurization of steel during the secondary steelmaking process depends on temperature, concentrations of sulphur and oxygen (O2) in the steel, but mainly on the chemical composition and physical properties of slag. The refining of liquid steel during secondary steelmaking to meet the required compositional range requires the optimization of the process parameters.

In modern steel melting shops the primary steelmaking furnaces are primarily used for the treatment of hot metal and melting of scrap. All other metallurgical objectives, such as alloying, homogenization, refining and temperature adjustment, are performed during the secondary steelmaking process with control of top slag. There are several tasks which the ladle slag is to perform. It protects the liquid steel against oxidizing atmosphere on the one hand and is used to carry out metallurgical operations on the other hand. Therefore, the ladle slag is to have suitable physical and chemical properties which are characterized mainly by a low melting temperature, low oxygen potential as well as a high capacity for sulphur.

The desulphurization of liquid steels with a refining ladle slag is one of the most important processes of secondary steelmaking. But process control is based on empirical guidelines even today. Deviations from the sulphur contents aimed at can often be observed in practice. An improvement of the process control supported by knowledge of the thermodynamics and kinetics of the desulphurization reaction is of great importance, especially for the production of steels with very low sulphur levels.

Contact us to discuss your requirements of Desulfurizer. Our experienced sales team can help you identify the options that best suit your needs.

Thermodynamics of desulphurization of liquid steel 

There are four aspects which are important during the desulphurization of liquid steel. These are (i) sulphide capacity, (ii) sulphur distribution ratio, (iii) desulphurization potential, and (iv) rate of desulphurization.

• Sulphide capacity &#; It is the ability of liquid slag to adsorb sulphur. This is often characterized by the equilibrium between the slag phase and the gas phase with respect to sulphur and oxygen partial pressures. The sulphide capacity is a property depending only on the temperature and the slag composition. It can be directly measured by experimental tests under isobaric and isothermal conditions. The achievable data on the sulphide capacities of many binary, ternary and multi-component slag systems are available in the literature. The sulphide capacity of slag normally increases with rising temperature and concentration of basic oxides. Hence, highly basic ladle slags are to be used for steel desulphurization. Different mathematical models have also been developed to calculate the sulphide capacity of multi-component liquid slags.
• Sulphur distribution ratio &#; Sulphur is distributed between the metal and slag phase at equilibrium. The sulphur distribution ratio normally depends on the oxygen activity in the liquid steel. Steel desulphurization becomes more effective with the decreasing oxygen activity.
• Desulphurization potential &#; Desulphurization potential is also a function of the slag composition. To characterize the slag behaviour a lime saturation index defined by the ratio of the actual CaO (calcium oxide) content to the CaO content for lime saturated slags is generally used. The &#;lime saturation index&#; changes with the slag composition. The lime saturated index value for lime saturated slag is one. Slags with a lime saturation index of less or more than one are under-saturated slags or slags with a surplus of lime, respectively. The influence of lime saturation index on the desulphurization potential is shown in Fig 1. The highest desulphurization potential can be achieved by using lime saturated slags. An under-saturation of lime in the ladle slag leads to a decrease in desulphurization for thermodynamic reasons. As opposed to that, a surplus of lime leads to heterogeneous slags, resulting in a decrease of the desulphurization potential for kinetic reasons. Therefore, an optimization of the slag composition is required to ensure a satisfying removal of sulphur from liquid steel.
• Desulphurisation rate &#; The sulphide capacity as well as the desulphurization potential describe the maximum ability of slags to absorb sulphur at thermodynamic equilibrium. In practice, there is a ladle treatment time which is required to be adapted as per the production requirement of the steel melting shop. A rapid refining process in the ladles is desirable. It has been seen that at steelmaking temperatures the reaction rate between the metal and the slag phase is mostly determined by the mass transport. As regards steel desulphurization with a refining ladle top slag, the reaction rate is dependent on how fast sulphur is transported from the metal phase to the metal/slag interface and how fast it is transported away from the interface into the slag phase. In this case a rapid mass transfer caused by intensive gas stirring leads to an acceleration of the desulphurization rate. Today the gas stirring treatment of liquid steel in the ladle is a standard operational practice. For the performance of gas stirring treatment, inert gas (normally argon gas) is injected into liquid steel through porous plugs located in the ladle bottom or using a submerged top lance. The injected gas ascends in the liquid steel in the form of gas bubbles and is separated on the bath on the surface. Because of the buoyancy force of gas bubbles a circulating flow field of liquid steel is formed in the ladle. The pattern of the steel flow field is of great importance for the desulphurization process. The flow velocity of liquid steel increases with the increase of the stirring gas rate. Hence, an acceleration of reactions between the steel and the slag phase can be achieved.

Fig 1 Influence of lime saturation index on the desulphurization potential

The desulphurization rate increases considerably if the gas stirring rate exceeds a critical value. This phenomenon can be caused by emulsification of slag droplets into the metal phase.

Theoretical aspects of slag emulsification

Liquid steel desulphurization by slag-metal reaction is an exchange reaction between two non-miscible phases, thermodynamically governed by the sulphur partition ratio between the two phases, and kinetically governed by the inter phase exchange area and sulphur transfer driving force. The kinetic aspects can be suitably influenced by fluid dynamics effects. Since proper bath stirring induced by gas injection affects the relative velocity at the interface of metal and slag, it, in turn, affects the solute mass transport coefficient. High interface velocities can even cause slag emulsification, resulting in a great increase of exchange surface area. Moreover, efficient metal mixing in the liquid steel bath makes faster the attainment of the desired final sulphur level in the liquid steel, resulting in a decrease of the duration of desulphurization operation.

Knowledge is hence needed of in-ladle fluid-dynamics induced by gas injection, in order to reach the best conditions in terms of suitable flow field namely (i) at the metal-slag interface, to favour emulsification and, in turn, acceleration of the chemical kinetics, and (ii) in the ladle bath, in order to allow the mixing of just desulphurized steel at the interface with liquid steel in the ladle bulk up to reaching perfect mixing throughout all the ladle at the target sulphur level. On the other hand, too intense stirring actions which are related to high operational costs and bath temperature losses, are to be avoided.

Mechanical energy is transferred to the bath by means of (i) bottom blowing, from one or more porous plugs, (ii) top blowing, through lance, or (iii) combined blowing. Several investigations have been performed on the effects of gas stirring on in-ladle fluid-dynamics, focused on the gas path or on slag-metal interface processes, involving desulphurization reaction as well. The most relevant aspects arising from these investigations are the following.

• In several steelmaking processes in which bath stirring is concerned, mixing times depend on the power transferred to the bath in the ladle at the power of 0.3 &#; 0.4.
• The mono-plug bottom blowing stirring which ensure the shortest mixing times for a fixed bath and a fixed gas flow rate supply is achieved with plug eccentrical with respect to the ladle. A position between quarter and half ladle radius is generally desired.
• Multiple porous plugs stirring in the ladle is to be set carefully in order to have the relative velocity at the interface slag-metal to favour emulsification. Asymmetrical plug positions proved to be of maximum efficiency in reducing mixing times. With symmetrical plug positions, flow recirculations are induced in the ladle with zones which have counteracting flows destroying their stirring effects. Lance blowing is beneficial for emulsification, whereas bottom stirring is beneficial for ladle mixing. A suitable combined blowing merges the two desired effects.
• Studies carried out on the effect of the slag properties on the emulsification phenomenon show that there are critical conditions which are required to be met for steel velocity at the interface with the slag and flow rate of gas blown from the plugs to allow emulsification onset. These relationships take into account slag physical properties such as viscosity and density.
• Among the parameters used to define improved conditions for mixing in the ladle and mass transfer at the slag metal interface, of great importance are the ratio between ladle diameter (D) and the bath height (H). Normally, the ratio D/H is not far from 1.
• Data available in literature on the effect of gas flow rate injection on desulphurization rate show that the most interesting aspect is that an onset gas flow rate is to be found for enhancing significantly desulphurization rate.

Process of desulphurization

Primarily, there are two options available for the removal of sulphur from the liquid steel. These are (i) by means of metal-slag reaction, where the top slag is mixed intensively with the liquid steel, and (ii) by injection of metallic calcium (Ca) into liquid steel, where a precipitation of sulphides occurs.

The ladle top slag after primary steelmaking normally consists of (i) slag carried over from the primary steelmaking furnace, (ii) deoxidation products, (iii) residual ladle slag of the previous heat, (iv) wear of the ladle lining, and (v) slag forming agents charged into the ladle.

For efficient desulphurization, steel is required to be deoxidized and slag carry-over from primary steelmaking furnace is to be minimized. Ladles lined with fireclay and alumina refractories are not suitable if low level of sulphur in the steel is to be obtained. Use of dolomite or other basic refractory lined materials are to be used for efficient desulphurization.

After tapping of the liquid steel from the primary steelmaking furnace the amount of slag carried over is not known. Another unknown parameter is the loss of aluminum (Al) during tapping, which results in different amounts of Al2O3 in the slag. In secondary steelmaking it is essential to know the composition and amount of ladle slag just after tapping in order to be able to modify the ladle slag for the purpose of deoxidation and desulphurization. Normally, lime (CaO), alumina (Al2O3) and slag deoxidizer are used to modify the ladle slag. For steel desulphurization it is important to reduce the mass content of FeO and MnO to a low level. The desulphurization process uses the following different steps.

• Slag adjustment with respect to (i) slag deoxidation, and (ii) lime saturation
• Slag homogenization and liquefying
• Reduction of FeO and MnO
• Intensive stirring for desulphurization

Depending on the metallurgical reactors (Vacuum degassing unit, and ladle furnace etc.) these process steps need different periods of time. The available treatment time in secondary steelmaking is first determined by the casting times. The casting times in steel melting shops are in a range from 25 minutes to 60 minutes depending on several factors. In the case of a fast casting process, there is a short time available for secondary steelmaking, which is not sufficient for carrying out all the steps mentioned above. Therefore, the desulphurization process itself not only requires metallurgical knowledge but also involves a logistic aspect, which is a great challenge for the steelmaker.

Synthetic slag practice is normally used for the desulphurization of liquid steel. Synthetic slag practice is adopted to meet the following objectives.

• For covering the surface of liquid steel to reduce the heat losses.
• For avoiding reoxidation of liquid steel from atmospheric oxygen
• For removal of inclusions from the liquid steel.

Use of synthetic slag can desulphurize steel up to 50 % to 60 % of the original sulphur level in the steel. The desirable properties of the synthetic slag are (i) slag is to have high sulphide capacity, (ii) it is to be basic in nature, (iii) it is to be fluid to obtain faster reaction rates, and (iv) it is not to cause excessive refractory wear.

Argon bubbling is normally done to obtain intensive mixing for efficient desulphurization. Using synthetic slag of desired basicity and sulphide capacity, deoxidized steel can be desulphurized to as low as 0.005 %.

Design of synthetic slag

In ladles lined with dolomite or magnesite bricks, the major components of the initial ladle slag are CaO, Al2O3, SiO2, FeO, MnO and MgO. During ladle treatment for desulphurisation the components FeO and MnO are to be well reduced. In addition, the contents of CaO, AI2O3, SiO2, and MgO are to be kept in a suitable range in order to obtain a liquid and homogeneous ladle slag. A high surplus of CaO and MgO leads to heterogeneous slags, which has a negative influence on the process performance and hence is to be avoided.

The synthetic slag normally contains CaO, Ca F2, and Al2O3 and with small amount of SiO2. The main component of synthetic slag is lime (CaO). Calcium fluoride (CaF2) increases the sulphide capacity of slag and helps fluidizing the slag. Frequently Al is present to deoxidize the liquid steel since transfer of sulphur from liquid steel to slag is followed by transfer of oxygen from slag to steel. Therefore, effective deoxidation of steel is must for efficient desulphurization.

Typically, the composition of synthetic slag consists of 45 % to 55 % of CaO, 10 % to 20 % of CaF2, 5 % to 16 % of Al2O3 and up to 5 %of SiO2. This slag is pre fused in solid state.

Issues related to synthetic slag practice

Synthetic slag practice appears to be simple and not much capital investment is needed. Certain issues related to synthetic slag practice are as given below.

• Desulphurization may vary from one heat to other if slag carry- over from the primary steel melting furnace is not controlled. Oxygen level of liquid steel is required to be same for consistent results.
• CaO is the main component. It is hygroscopic and leads to the pick-up of hydrogen (H2) in the steel.
• Argon bubbling is done to stir the bath. Temperature drop due to bubbling of argon can be of the order of 10 deg to 25 deg C for a heat of weight 150 tons to 250 tons. The temperature drop is resulting from radiation heat losses from the surface and heat transfer due to the argon bubbling. The slag attacks the ladle refractory. Excessive amount of CaF2 results in refractory wear. Higher tapping temperature also has an effect on the refractory wear.

A pre melted slag based on CaO and Al2O3 with small amount of CaF2 can reduce the problem of refractory wear and hydrogen pick-up. Composition of CaO and Al2O3 can be selected so as to melt at deg C to deg C. Small amount of CaF2 can be added. This re-melted slag, when used for desulphurization, is found to have reduced problems associated with pre fused slag.

An important parameter to characterize synthetic slag for its suitability to desulphurize liquid steel is sulphide capacity of slag. Further the extent of desulphurization depends on extent of deoxidation. Aluminum killed steel can desulphurize more effectively than the steel where either Fe-Mn or Fe-Si is used to deoxidize the steel.

For more information, please visit Ferro Silicon.