Abstract:Limestone particle size has a crucial influence on SO2 capture efficiency, however there are few studies on the sulfation reactivity, which covers a broad range of particle sizes at low SO2 concentrations. In this paper, a large-capacity thermogravimetric analyzer (LC-TGA) was developed to obtain the sulfur removal reaction rate under a wide range of particle sizes (3 μm–600 μm) and SO2 concentrations (250 ppm–2000 ppm), and then compared with the results of a traditional fixed bed reactor and a commercial TGA… Show more
“…This was distinguished with the sulfation test in the thermogravimetric analyzer (TGA), where the conversion degree reached the maximum value and remained unchanged within an much shorter time. 24,25 The attrition that resulted in the exposure of the fresh reaction surface via the removal of protuberances is believed to be one of the dominant reasons for the slow but continuous increase of the conversion degree in fluidized bed conditions.…”
Limestone is widely
used as a sorbent in fluidized bed combustors.
The study of limestone attrition characteristics is significant for
mass balance and desulfurization efficiency. The present study investigates
the sulfation and attrition behavior of limestone in a bubbling fluidized
bed reactor. The product distribution and development of the product
layer are analyzed by scanning electron microscopy. The experimental
results show the attrition rate dropped dramatically at the initial
kinetic-controlled regime of the sulfation reaction. The observations
show that the distribution of the product is not uniform but primarily
concentrated on the external surface of the particle. Meanwhile, the
thickness of the product layer at the initial stage of the sulfation
reaction reaches 0.7 μm, which is larger than that predicted
by previous investigators, and it results in a dramatic decrease in
the attrition rate. As sulfation continues, the thickness of the product
layer increases and reaches 1.6 μm at the diffusion-controlled
regime of the reaction, whereas the attrition rate decays to a steady
state. A random pore model is also used to analyze the development
of the product layer thickness by counting in the whole reaction surface,
but the results show a much smaller value as a result of the lack
of consideration of the unreacted core, which verifies the early pore
blockage in the initial stage observed in the present study.
“…This was distinguished with the sulfation test in the thermogravimetric analyzer (TGA), where the conversion degree reached the maximum value and remained unchanged within an much shorter time. 24,25 The attrition that resulted in the exposure of the fresh reaction surface via the removal of protuberances is believed to be one of the dominant reasons for the slow but continuous increase of the conversion degree in fluidized bed conditions.…”
Limestone is widely
used as a sorbent in fluidized bed combustors.
The study of limestone attrition characteristics is significant for
mass balance and desulfurization efficiency. The present study investigates
the sulfation and attrition behavior of limestone in a bubbling fluidized
bed reactor. The product distribution and development of the product
layer are analyzed by scanning electron microscopy. The experimental
results show the attrition rate dropped dramatically at the initial
kinetic-controlled regime of the sulfation reaction. The observations
show that the distribution of the product is not uniform but primarily
concentrated on the external surface of the particle. Meanwhile, the
thickness of the product layer at the initial stage of the sulfation
reaction reaches 0.7 μm, which is larger than that predicted
by previous investigators, and it results in a dramatic decrease in
the attrition rate. As sulfation continues, the thickness of the product
layer increases and reaches 1.6 μm at the diffusion-controlled
regime of the reaction, whereas the attrition rate decays to a steady
state. A random pore model is also used to analyze the development
of the product layer thickness by counting in the whole reaction surface,
but the results show a much smaller value as a result of the lack
of consideration of the unreacted core, which verifies the early pore
blockage in the initial stage observed in the present study.
“…38,39 Thus, an LC-TGA was developed to characterize the sulfation reactivity of different limestones and its reliability and accuracy had been validated in previous studies. 40 As shown in Figure 2, a heating furnace can move along the sliding rail so that the fast calcination can be achieved, which was much closer to the injection condition in fluidized beds. Prior to the experiments, 15−30 mg of limestone samples were uniformly spread on a 32 mm-ID crucible by deionized water and then dried at a temperature of lower than 150 °C in an oven.…”
Section: Methodsmentioning
confidence: 91%
“…Despite the significant effect of particle size on the sulfation process, there remain a few reports on research results regarding the sulfation reactivity exhibited by a certain type of limestone with the particle size ranging widely from several micrometers to several hundred micrometers. , Thus, an LC-TGA was developed to characterize the sulfation reactivity of different limestones and its reliability and accuracy had been validated in previous studies . As shown in Figure , a heating furnace can move along the sliding rail so that the fast calcination can be achieved, which was much closer to the injection condition in fluidized beds.…”
Section: Methodsmentioning
confidence: 99%
“…Moreover, a larger reaction gas flow rate (5 standard L/min) is conducive to improving the external mass transfer, for which the reaction rates can be closer to a differential reactor, especially in the initial sulfation stage. The detailed description about the LC-TGA and the experimental procedure can be found in previous works …”
Section: Methodsmentioning
confidence: 99%
“…The detailed description about the LC-TGA and the experimental procedure can be found in previous works. 40 Shengzhou limestone, which was also used in the pilot-scale (PS) CFB boiler, was sieved with an ultrasonic sieving machine into three groups, including the screen meshes of 0−20, 75− 106, and 400−600 μm. As shown in Figure S2 (SI), the distribution of their particle size was measured by a Malvern Mastersizer particle analyzer, with the SMDs being 3.5, 39.4, and 602.8 μm, respectively.…”
With
the stringent emission regulation taking effect, it is difficult
for the conventional desulfurization technology in circulating fluidized
bed (CFB) boilers to meet the requirements of ultralow SO2 emission. Therefore, in this paper, the application of natural ultrafine
limestone, with a Sauter mean diameter of less than 20 μm, was
tested by conducting bench-scale, pilot-scale, and commercial-scale
experiments to realize highly efficient desulfurization in CFB furnaces.
In the past, such small-size limestone was considered unsuitable for
CFB boilers. However, as demonstrated by bench-scale results, the
desulfurization performance was clearly superior to that of coarse
limestone, especially at low SO2 concentrations. In a 3
MWth pilot-scale CFB boiler, the ultrafine limestone exhibited
competent desulfurization efficiency to that of the coarse limestone
but clearly less significant catalytic effects on NOx formation. As
revealed by field tests in four commercial-scale CFB boilers, when
high-efficiency cyclones were applied to CFB boilers, the mass inventory
of ultrafine particles was significantly increased and the residence
time would be extended accordingly; thus, the ultrafine limestone
can be used to achieve high desulfurization efficiency and even ultralow
SO2 emission with a favorable Ca/S ratio. Furthermore,
a technical roadmap was drawn for the cost-effective control of SO2 emission.
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