Synthesis of Ultramarine from Reservoir Silts

Ultramarine blue was synthesized by using reservoir silts as a major raw material to replace traditional kaolin clay. The reservoir silts were pretreated to collect the fines, in which the main mineral composition is illite clay. The fine part was mixed with sodium carbonate, sulfur, and activated carbon, and calcined at 800◦C for 8 h. The products were examined by X-ray powder diffraction (XRD) and a scanning electron microscope (SEM) to identify the mineral phases and particle morphology. The color characteristics were measured according to the CIELab system. Brilliant blue ultramarine powders were successfully synthesized with a chroma of 52.4, which is competitive with the commercial ultramarine.


Introduction
The annual sedimentation rate of the world's reservoirs averages about 1%, but it is much higher in Asia [1,2].Due to climatic, geographic and geologic situations, the reservoir sedimentation problem is very serious in southern Taiwan, R.O.C.All the streams have steep slopes in their catchment areas.The rainfall intensity and runoff flow are strong during the summer typhoon season.Even worse, major irrigation and city water supply reservoirs are located in Pliocene and Pleistocene shale and mudstone areas.The accumulated sediment volume in these reservoirs accounts for about one third or more of the reservoir designed capacity [3].To extend the operation life of these reservoirs, desiltation is essential.Reservoir desiltation involves three major processes, namely the removal, deposition and reuse of the silt.The reuse of the silt is the most important one because improper handling of dredged silts will interrupt the removal operation.
The major mineral components of reservoir sediments in southern Taiwan are sand (mostly quartz) and clay (illite and chlorite) [4].Since the hardness of quartz is greater than that of the clay minerals, these two types of minerals are concentrated in different size ranges, i.e. sand in the coarse-grained range and clay minerals in the fine-grained range.Using sedimentation technique in mineral processing, it is easy to separate out clay minerals.From the point of view of chemical composition, after the removal of quartz, reservoir silts can be regarded as a natural aluminosilicate mineral source.
Ultramarine with its deep vivid blue is a valuable inorganic pigment.Natural ultramarine is derived from grinding lapis lazuli, which is a rock composed of lazurite with small amounts of calcite, pyroxene, etc.Most of today's ultramarine is synthetically produced based upon processes invented by Guimet in 1826 and Gmelin in 1828 [5].
The ratio of Si to Al determines the amount of chromophores encapsulated inside β cages.When fewer Al ions are present in the framework, the required number of sodium ions is reduced for lattice stabilization, and more sodium ions are free to act as counter-ions for the polysulfide.The polysulfide content can be increased and thereby improve color quality [19,20].Within limits set by stability considerations, the proportions of the chemical constituents can vary.Some empirical formulas, likeNa6.9Al5.6Si6.4O24S4.2[19], are reported.
Traditionally, the raw material used in the synthesis of ultramarine is kaolin clay.The industrial process of ultramarine synthesis involves the dehydration of kaolin at about 550°C.The dehydrated clay is mixed with sulfur, sodium carbonate and a reducing agent, e.g.coke or active carbon.Heating of the mixture produces a synthesis reaction [21].In the reaction, the formation of ultramarine blue proceeds in two stages: first a reduction stage followed by an oxidation stage.In the reduction stage, the mixture is heated to about 750 °C, and held at that temperature for a given period of time.The container for the mixture is covered so that a reducing atmosphere can be maintained within it.When the holding time is reached, the temperature starts to descend, and the reaction enters the oxidation stage.The oxidation stage is achieved by either keeping the mixture at about 450 °C for a fixed time or simply slowing the cooling rate.During this stage, S2 − ions are oxidized to S3 − ions to produce a vivid blue hue [20,21].
In a previous study, the reservoir silts were first treated hydrothermally to transform them to hydroxycancrinite [28]; then the hydroxycancrinite was transformed to ultramarine blue via a solid-state reaction process.In this study, reservoir silts were used directly to synthesize − encapsulated in β cages and surrounded by four sodium cations [7].
The ratio of Si to Al determines the amount of chromophores encapsulated inside β cages.When fewer Al ions are present in the framework, the required number of sodium ions is reduced for lattice stabilization, and more sodium ions are free to act as counter-ions for the polysulfide.The polysulfide content can be increased and thereby improve color quality [19,20].Within limits set by stability considerations, the proportions of the chemical constituents can vary.Some empirical formulas, likeNa 6.9 Al 5.6 Si 6.4 O 24 S 4.2 [19], are reported.
Traditionally, the raw material used in the synthesis of ultramarine is kaolin clay.The industrial process of ultramarine synthesis involves the dehydration of kaolin at about 550 • C. The dehydrated clay is mixed with sulfur, sodium carbonate and a reducing agent, e.g., coke or active carbon.Heating of the mixture produces a synthesis reaction [21].In the reaction, the formation of ultramarine blue proceeds in two stages: first a reduction stage followed by an oxidation stage.In the reduction stage, the mixture is heated to about 750 • C, and held at that temperature for a given period of time.The container for the mixture is covered so that a reducing atmosphere can be maintained within it.When the holding time is reached, the temperature starts to descend, and the reaction enters the oxidation stage.The oxidation stage is achieved by either keeping the mixture at about 450 • C for a fixed time or simply slowing the cooling rate.During this stage, S 2 − ions are oxidized to S 3 − ions to produce a vivid blue hue [20,21].Besides kaolin, other aluminosilicate sources, including pure chemicals, natural or synthetic minerals and wastes have been used.Chemicals, such as sodium silicate and tetramethylammonium hydroxide [22]; silicon tetrachloride and aluminum chloride [8]; silica, diatomaceous earth and sodium aluminate [23]; natural or synthetic minerals, like zeolite A, X, Y [24][25][26], cancrinite [27], hydroxycancrinite [28]; wastes, such as fly ash [20] and kaolin mine tailings [29], were reported to be technologically feasible.In a previous study, the reservoir silts were first treated hydrothermally to transform them to hydroxycancrinite [28]; then the hydroxycancrinite was transformed to ultramarine blue via a solid-state reaction process.In this study, reservoir silts were used directly to synthesize ultramarine.The reaction conditions, such as raw materials ratio, calcination temperature and mineral composition of silts on the product phase and color properties, were investigated.

Materials
The reservoir silt samples were taken from the city water supply of Nan-Hua Reservoir that is located in Tainan County.The silts were screened through a 200 mesh sieve (75 µm), to remove the non-mineral constituents, such as humus, etc., and then the material was designated as the "raw" silt.The raw silts were further classified via hydraulic sedimentation to separate out the <10 µm, <5 µm, and <2 µm parts.
The size distribution of the raw silts is shown in Figure 2. The distribution fits quite well that of the Gates-Gaudin-Schuhmann distribution function with the distribution modulus of 0.77 and d 50 of 5.7 µm.From the distribution curve, it can be determined that the <10 µm, <5 µm and <2 µm parts account for 62, 47, and 33 wt % of the raw silts, respectively.ultramarine.The reaction conditions, such as raw materials ratio, calcination temperature and mineral composition of silts on the product phase and color properties, were investigated.

Materials
The reservoir silt samples were taken from the city water supply of Nan-Hua Reservoir that is located in Tainan County.The silts were screened through a 200 mesh sieve (75 μm), to remove the non-mineral constituents, such as humus, etc., and then the material was designated as the "raw" silt.The raw silts were further classified via hydraulic sedimentation to separate out the <10 μm, <5 μm, and <2 μm parts.
The size distribution of the raw silts is shown in Figure 2. The distribution fits quite well that of the Gates-Gaudin-Schuhmann distribution function with the distribution modulus of 0.77 and d50 of 5.7 μm.From the distribution curve, it can be determined that the <10 μm, <5 μm and <2 μm parts account for 62, 47, and 33 wt% of the raw silts, respectively.The XRD patterns of the raw and classified silt samples are shown in Figure 3.The diffraction peaks show that the minerals comprising the silt are quartz, illite, clinochlore and albite.As the size of the silts is decreased, the peaks of quartz and albite decrease rapidly, whereas those of illite and clinochlore are more prominent.The change in mineral composition shows that size classification can separate quartz and albite, which are unusable in the synthesis reaction, from clay minerals effectively.
The chemical compositions of all silt samples determined by XRF are listed in Table 1.With the removal of quartz from classified silts, the molar ratio of Si/Al decreases from 2.77 to 1.42.The XRD patterns of the raw and classified silt samples are shown in Figure 3.The diffraction peaks show that the minerals comprising the silt are quartz, illite, clinochlore and albite.As the size of the silts is decreased, the peaks of quartz and albite decrease rapidly, whereas those of illite and clinochlore are more prominent.The change in mineral composition shows that size classification can separate quartz and albite, which are unusable in the synthesis reaction, from clay minerals effectively.
The chemical compositions of all silt samples determined by XRF are listed in Table 1.With the removal of quartz from classified silts, the molar ratio of Si/Al decreases from 2.77 to 1.42.The SEM images of the raw and classified silts are shown in Figure 4.It is clear that with decreasing particle sizes, the major mineral images gradually vary from massive, which represents quartz, to sheet-like, which represents clay minerals.The SEM images of the raw and classified silts are shown in Figure 4.It is clear that with decreasing particle sizes, the major mineral images gradually vary from massive, which represents quartz, to sheet-like, which represents clay minerals.The SEM images of the raw and classified silts are shown in Figure 4.It is clear that with decreasing particle sizes, the major mineral images gradually vary from massive, which represents quartz, to sheet-like, which represents clay minerals.

Procedures
The silts were fully mixed with sulfur (purified, Katayama Chemical Co. Ltd., Osaka, Japan) and active carbon (100-400 mesh, Sigma-Aldrich Chemie GmbH, Munich, Germany).An aliquot of sodium carbonate (reagent grade, Fisher Scientific, Leicestershire, UK) solution of assigned concentrations was slowly added to the powder and was hand-kneaded to balls and then dried in air.It was reported [29,30] that in the reaction, sulfur and sodium carbonate are reacted as: From the Na 2 CO 3 /S 8 molar ratio in the above equation, the Na 2 CO 3 /S 8 weight ratio is approximately equivalent to 1.This ratio was held constant in this study.The dried balls were placed in an alumina crucible covered with a lid and calcined at 700, 800 and 900 • C for 2, 4, 8 and 12 h.
After completion of the reaction, the crucible was allowed to cool down to room temperature in the furnace.The cooling took about 8 h.The reacted balls were mixed with deionized water, stirred thoroughly and filtered several times to remove all dissolved ions.The solids were dried at 120 • C for 24 h and for further analyses.

Characterization
The mineral phases of the sediment and products were characterized using an X-ray diffractometer (DX-2600, Fangyuan Co., Dandong, China) with Cu K α (λ = 1.5418Å) radiation and a scan rate of 0.04 • /s.The chemical compositions were analyzed using an X-ray Fluorescence Analyzer (NEX CG EDXRF elemental analyzer, Rigaku Corp., Tokyo, Japan).The particle size distribution was determined using an Andreasen pipette.The morphology and individual particle sizes were examined using a Hitachi 8000 High-Resolution Scanning Electron Microscope (HRSEM, Hitach Ltd., Ibaraki, Japan).The color characteristics of the synthesized products were measured using a sphere spectrophotometer SP-60 (X-Rite Inc., Grand Rapids, MI, USA) employing the CIELab (Commission Internationale de l'Éclairage) color spaces system.The measurements (Standard Illuminant D65/10 • ) performed were chromaticity or color saturation (C* = 0 for grey color, C* = 100 for pure chromatic components), lightness (L* = 0 for a black sample, L* = 100 for a white sample) and hue (h* = 0 • , 90 • , 180 • , 270 • for red, yellow, green and blue colors, respectively).

Reaction Temperature
The <5 µm silts were used in these calcination tests.The mass ratio of (Na 2 CO 3 + S 8 ) and active carbon to silt were maintained at 1.5 and 0.2, respectively.The XRD patterns of the products calcined at 700, 800 and 900 • C for 8 h are shown in Figure 5.For all reaction temperatures, lazurite was the major phase formed.Nepheline was also formed for temperatures below 800 • C. When reaction temperature reached 900 • C, nepheline disappeared.
The color properties of the products are listed in Table 2.When calcination was performed at 800 • C, the chroma of the product achieved optimum.Both lower or higher than this temperature were deleterious.This could be because that lower temperature does not promote the reaction efficiently, whereas higher temperature accelerates the loss of sulfur chromophores.The results of Figure 5 and Table 2 shows that the color properties are determined by crystal structure as well as the amount of polysulfide radical anions kept in the β cage.The latter is more important, as can be seen from the XRD patterns of the 800 °C product.Although some nepheline is still present, it represents the best color properties.

Reaction Duration
Figure 6 shows the XRD patterns of the products calcined at 800 °C for 2-12 h.After 2 h of calcination, lazurite formed with a minor amount of nepheline.Lazurite obviously is the stable phase, as it can be seen that all diffraction peaks kept increasing even after 12 h of calcination.Nepheline on the other hand, seemed to be an intermediate phase, and disappeared gradually as calcination proceeded.The color properties of the products are listed in Table 3.The best chroma was obtained at the reaction time of 8 h.It is obvious for long time calcination that S3 − chromophores may vaporize from the clathrate.According to the above results, 800 °C and 8 h were used as the calcination conditions for the next test.The results of Figure 5 and Table 2 shows that the color properties are determined by crystal structure as well as the amount of polysulfide radical anions kept in the β cage.The latter is more important, as can be seen from the XRD patterns of the 800 °C product.Although some nepheline is still present, it represents the best color properties.

Reaction Duration
Figure 6 shows the XRD patterns of the products calcined at 800 °C for 2-12 h.After 2 h of calcination, lazurite formed with a minor amount of nepheline.Lazurite obviously is the stable phase, as it can be seen that all diffraction peaks kept increasing even after 12 h of calcination.Nepheline on the other hand, seemed to be an intermediate phase, and disappeared gradually as calcination proceeded.The color properties of the products are listed in Table 3.The best chroma was obtained at the reaction time of 8 h.It is obvious for long time calcination that S3 − chromophores may vaporize from the clathrate.According to the above results, 800 °C and 8 h were used as the calcination conditions for the next test.The results of Figure 5 and Table 2 shows that the color properties are determined by crystal structure as well as the amount of polysulfide radical anions kept in the β cage.The latter is more important, as can be seen from the XRD patterns of the 800 °C product.Although some nepheline is still present, it represents the best color properties.

Reaction Duration
Figure 6 shows the XRD patterns of the products calcined at 800 °C for 2-12 h.After 2 h of calcination, lazurite formed with a minor amount of nepheline.Lazurite obviously is the stable phase, as it can be seen that all diffraction peaks kept increasing even after 12 h of calcination.Nepheline on the other hand, seemed to be an intermediate phase, and disappeared gradually as calcination proceeded.The color properties of the products are listed in Table 3.The best chroma was obtained at the reaction time of 8 h.It is obvious for long time calcination that S3 − chromophores may vaporize from the clathrate.According to the above results, 800 °C and 8 h were used as the calcination conditions for the next test.The results of Figure 5 and Table 2 shows that the color properties are determined by crystal structure as well as the amount of polysulfide radical anions kept in the β cage.The latter is more important, as can be seen from the XRD patterns of the 800 °C product.Although some nepheline is still present, it represents the best color properties.

Reaction Duration
Figure 6 shows the XRD patterns of the products calcined at 800 °C for 2-12 h.After 2 h of calcination, lazurite formed with a minor amount of nepheline.Lazurite obviously is the stable phase, as it can be seen that all diffraction peaks kept increasing even after 12 h of calcination.Nepheline on the other hand, seemed to be an intermediate phase, and disappeared gradually as calcination proceeded.The color properties of the products are listed in Table 3.The best chroma was obtained at the reaction time of 8 h.It is obvious for long time calcination that S3 − chromophores may vaporize from the clathrate.According to the above results, 800 °C and 8 h were used as the calcination conditions for the next test.
The results of Figure 5 and Table 2 shows that the color properties are determined by crystal structure as well as the amount of polysulfide radical anions kept in the β cage.The latter is more important, as can be seen from the XRD patterns of the 800 • C product.Although some nepheline is still present, it represents the best color properties.

Reaction Duration
Figure 6 shows the XRD patterns of the products calcined at 800 • C for 2-12 h.After 2 h of calcination, lazurite formed with a minor amount of nepheline.Lazurite obviously is the stable phase, as it can be seen that all diffraction peaks kept increasing even after 12 h of calcination.Nepheline on the other hand, seemed to be an intermediate phase, and disappeared gradually as calcination proceeded.The color properties of the products are listed in Table 3.The best chroma was obtained at the reaction time of 8 h.It is obvious for long time calcination that S 3 − chromophores may vaporize from the clathrate.According to the above results, 800 • C and 8 h were used as the calcination conditions for the next test.The <5 μm silts were used in this test.There are two concerns about raw material ratios, one is the weight ratio of Na2CO3+ S8 to silts (at Na2CO3/S8=1), the other is the active carbon to silts.The mixtures were heated at 800 °C for 8 h.The color properties of the products of all tests are summarized in Table 4.
The effect of (Na2CO3+ S8)/silts ratio on the color properties (chroma, lightness and hue) of the products for reactions with active carbon/silts ratio = 0.2is shown in Figure 7.With the (Na2CO3+ S8)/silts ratio increased from 1 to 1.5, 2, the chroma increased from 38.9 to 50.2, 53.3, while lightness and hue still remained at the similar levels but much improved to around 30° and 275°, respectively.For the economical reason, the (Na2CO3+ S8)/silts ratio= 1.5 was adopted in the later tests.The <5 μm silts were used in this test.There are two concerns about raw material ratios, one is the weight ratio of Na2CO3+ S8 to silts (at Na2CO3/S8=1), the other is the active carbon to silts.The mixtures were heated at 800 °C for 8 h.The color properties of the products of all tests are summarized in Table 4.
The effect of (Na2CO3+ S8)/silts ratio on the color properties (chroma, lightness and hue) of the products for reactions with active carbon/silts ratio = 0.2is shown in Figure 7.With the (Na2CO3+ S8)/silts ratio increased from 1 to 1.5, 2, the chroma increased from 38.9 to 50.2, 53.3, while lightness and hue still remained at the similar levels but much improved to around 30° and 275°, respectively.For the economical reason, the (Na2CO3+ S8)/silts ratio= 1.5 was adopted in the later tests.The <5 μm silts were used in this test.There are two concerns about raw material ratios, one is the weight ratio of Na2CO3+ S8 to silts (at Na2CO3/S8=1), the other is the active carbon to silts.The mixtures were heated at 800 °C for 8 h.The color properties of the products of all tests are summarized in Table 4.
The effect of (Na2CO3+ S8)/silts ratio on the color properties (chroma, lightness and hue) of the products for reactions with active carbon/silts ratio = 0.2is shown in Figure 7.With the (Na2CO3+ S8)/silts ratio increased from 1 to 1.5, 2, the chroma increased from 38.9 to 50.2, 53.3, while lightness and hue still remained at the similar levels but much improved to around 30° and 275°, respectively.For the economical reason, the (Na2CO3+ S8)/silts ratio= 1.5 was adopted in the later tests.The <5 μm silts were used in this test.There are two concerns about raw material ratios, one is the weight ratio of Na2CO3+ S8 to silts (at Na2CO3/S8=1), the other is the active carbon to silts.The mixtures were heated at 800 °C for 8 h.The color properties of the products of all tests are summarized in Table 4.
The effect of (Na2CO3+ S8)/silts ratio on the color properties (chroma, lightness and hue) of the products for reactions with active carbon/silts ratio = 0.2is shown in Figure 7.With the (Na2CO3+ S8)/silts ratio increased from 1 to 1.5, 2, the chroma increased from 38.9 to 50.2, 53.3, while lightness and hue still remained at the similar levels but much improved to around 30° and 275°, respectively.For the economical reason, the (Na2CO3+ S8)/silts ratio= 1.5 was adopted in the later tests.The <5 μm silts were used in this test.There are two concerns about raw material ratios, one is the weight ratio of Na2CO3+ S8 to silts (at Na2CO3/S8=1), the other is the active carbon to silts.The mixtures were heated at 800 °C for 8 h.The color properties of the products of all tests are summarized in Table 4.
The effect of (Na2CO3+ S8)/silts ratio on the color properties (chroma, lightness and hue) of the products for reactions with active carbon/silts ratio = 0.2is shown in Figure 7.With the (Na2CO3+ S8)/silts ratio increased from 1 to 1.5, 2, the chroma increased from 38.9 to 50.2, 53.3, while lightness and hue still remained at the similar levels but much improved to around 30° and 275°, respectively.For the economical reason, the (Na2CO3+ S8)/silts ratio= 1.5 was adopted in the later tests.The <5 µm silts were used in this test.There are two concerns about raw material ratios, one is the weight ratio of Na 2 CO 3 + S 8 to silts (at Na 2 CO 3/ S 8 = 1), the other is the active carbon to silts.The mixtures were heated at 800 • C for 8 h.The color properties of the products of all tests are summarized in Table 4.
The effect of (Na 2 CO 3 + S 8 )/silts ratio on the color properties (chroma, lightness and hue) of the products for reactions with active carbon/silts ratio = 0.2 is shown in Figure 7.With the (Na 2 CO 3 + S 8 )/silts ratio increased from 1 to 1.5, 2, the chroma increased from 38.9 to 50.2, 53.3, while lightness and hue still remained at the similar levels but much improved to around 30 • and 275 • , respectively.For the economical reason, the (Na 2 CO 3 + S 8 )/silts ratio = 1.5 was adopted in the later tests.

Active Carbon/Silts Ratio
The effect of active carbon/silts ratio on the products color properties is shown in Table 5 and Figure 8.For active carbon/silts ratios ≤ 0.2, with the increase of active carbon/silts ratio, the chroma and lightness were improved prominently from 44.5, 45.3 to 50.2 and 41.7, 37.3 to 31.2, respectively.Increasing the ratio to 0.35 and 0.5, the color properties deteriorated.The chroma decreased to 31.9 and 12.9, while the lightness became 29.5 and 46.3.The function of active carbon is to provide a reduced atmosphere in the reaction container to transform elemental sulfur to S2 − .However, over-dosing of active carbon may deter the formation of S2 − by its reaction with the sulfur to form carbonyl sulfide (COS).The oxidation stage, in which the yellow chromophore S2 − is oxidized to the blue chromophore S3 − , can also be influenced by carbon reacting with oxygen in the crucible to produce carbon monoxide [20].The hue of the products of active carbon/silts ratio at 0.35 and 0.5 dropped to 258.9° and 157°, inclining to a green (180°) tone, probably due to incomplete oxidation.Thus the proper active carbon/silts ratio is 0.2.

Active Carbon/Silts Ratio
The effect of active carbon/silts ratio on the products color properties is shown in Table 5 and Figure 8.For active carbon/silts ratios ≤ 0.2, with the increase of active carbon/silts ratio, the chroma and lightness were improved prominently from 44.5, 45.3 to 50.2 and 41.7, 37.3 to 31.2, respectively.Increasing the ratio to 0.35 and 0.5, the color properties deteriorated.The chroma decreased to 31.9 and 12.9, while the lightness became 29.5 and 46.3.The function of active carbon is to provide a reduced atmosphere in the reaction container to transform elemental sulfur to S2 − .However, over-dosing of active carbon may deter the formation of S2 − by its reaction with the sulfur to form carbonyl sulfide (COS).The oxidation stage, in which the yellow chromophore S2 − is oxidized to the blue chromophore S3 − , can also be influenced by carbon reacting with oxygen in the crucible to produce carbon monoxide [20].The hue of the products of active carbon/silts ratio at 0.35 and 0.5 dropped to 258.9° and 157°, inclining to a green (180°) tone, probably due to incomplete oxidation.Thus the proper active carbon/silts ratio is 0.2.

Active Carbon/Silts Ratio
The effect of active carbon/silts ratio on the products color properties is shown in Table 5 and Figure 8.For active carbon/silts ratios ≤ 0.2, with the increase of active carbon/silts ratio, the chroma and lightness were improved prominently from 44.5, 45.3 to 50.2 and 41.7, 37.3 to 31.2, respectively.Increasing the ratio to 0.35 and 0.5, the color properties deteriorated.The chroma decreased to 31.9 and 12.9, while the lightness became 29.5 and 46.3.The function of active carbon is to provide a reduced atmosphere in the reaction container to transform elemental sulfur to S2 − .However, over-dosing of active carbon may deter the formation of S2 − by its reaction with the sulfur to form carbonyl sulfide (COS).The oxidation stage, in which the yellow chromophore S2 − is oxidized to the blue chromophore S3 − , can also be influenced by carbon reacting with oxygen in the crucible to produce carbon monoxide [20].The hue of the products of active carbon/silts ratio at 0.35 and 0.5 dropped to 258.9° and 157°, inclining to a green (180°) tone, probably due to incomplete oxidation.Thus the proper active carbon/silts ratio is 0.2.

Active Carbon/Silts Ratio
The effect of active carbon/silts ratio on the products color properties is shown in Table 5 and Figure 8.For active carbon/silts ratios ≤ 0.2, with the increase of active carbon/silts ratio, the chroma and lightness were improved prominently from 44.5, 45.3 to 50.2 and 41.7, 37.3 to 31.2, respectively.Increasing the ratio to 0.35 and 0.5, the color properties deteriorated.The chroma decreased to 31.9 and 12.9, while the lightness became 29.5 and 46.3.The function of active carbon is to provide a reduced atmosphere in the reaction container to transform elemental sulfur to S2 − .However, over-dosing of active carbon may deter the formation of S2 − by its reaction with the sulfur to form carbonyl sulfide (COS).The oxidation stage, in which the yellow chromophore S2 − is oxidized to the blue chromophore S3 − , can also be influenced by carbon reacting with oxygen in the crucible to produce carbon monoxide [20].The hue of the products of active carbon/silts ratio at 0.35 and 0.5 dropped to 258.9° and 157°, inclining to a green (180°) tone, probably due to incomplete oxidation.Thus the proper active carbon/silts ratio is 0.2.

Active Carbon/Silts Ratio
The effect of active carbon/silts ratio on the products color properties is shown in Table 5 and Figure 8.For active carbon/silts ratios ≤ 0.2, with the increase of active carbon/silts ratio, the chroma and lightness were improved prominently from 44.5, 45.3 to 50.2 and 41.7, 37.3 to 31.2, respectively.Increasing the ratio to 0.35 and 0.5, the color properties deteriorated.The chroma decreased to 31.9 and 12.9, while the lightness became 29.5 and 46.3.The function of active carbon is to provide a reduced atmosphere in the reaction container to transform elemental sulfur to S 2 − .However, over-dosing of active carbon may deter the formation of S 2 − by its reaction with the sulfur to form carbonyl sulfide (COS).The oxidation stage, in which the yellow chromophore S 2 − is oxidized to the blue chromophore S 3 − , can also be influenced by carbon reacting with oxygen in the crucible to produce carbon monoxide [20].The hue of the products of active carbon/silts ratio at 0.35 and 0.5 dropped to 258.9 • and 157  reduced atmosphere in the reaction container to transform elemental sulfur to S2 − .However, over-dosing of active carbon may deter the formation of S2 − by its reaction with the sulfur to form carbonyl sulfide (COS).The oxidation stage, in which the yellow chromophore S2 − is oxidized to the blue chromophore S3 − , can also be influenced by carbon reacting with oxygen in the crucible to produce carbon monoxide [20].The hue of the products of active carbon/silts ratio at 0.35 and 0.5 dropped to 258.9° and 157°, inclining to a green (180°) tone, probably due to incomplete oxidation.Thus the proper active carbon/silts ratio is 0.2.and 12.9, while the lightness became 29.5 and 46.3.The function of active carbon is to provide a reduced atmosphere in the reaction container to transform elemental sulfur to S2 − .However, over-dosing of active carbon may deter the formation of S2 − by its reaction with the sulfur to form carbonyl sulfide (COS).The oxidation stage, in which the yellow chromophore S2 − is oxidized to the blue chromophore S3 − , can also be influenced by carbon reacting with oxygen in the crucible to produce carbon monoxide [20].The hue of the products of active carbon/silts ratio at 0.35 and 0.5 dropped to 258.9° and 157°, inclining to a green (180°) tone, probably due to incomplete oxidation.Thus the proper active carbon/silts ratio is 0.2.and 12.9, while the lightness became 29.5 and 46.3.The function of active carbon is to provide a reduced atmosphere in the reaction container to transform elemental sulfur to S2 − .However, over-dosing of active carbon may deter the formation of S2 − by its reaction with the sulfur to form carbonyl sulfide (COS).The oxidation stage, in which the yellow chromophore S2 − is oxidized to the blue chromophore S3 − , can also be influenced by carbon reacting with oxygen in the crucible to produce carbon monoxide [20].The hue of the products of active carbon/silts ratio at 0.35 and 0.5 dropped to 258.9° and 157°, inclining to a green (180°) tone, probably due to incomplete oxidation.Thus the proper active carbon/silts ratio is 0.2.

Effects of Mineral Composition of Starting Silts
The results of Table 1 and Figure 4 show that as the silt sizes are fine, more clay minerals are contained in the silts.In this test, the raw and classified silts were used to investigate the effects of mineral composition on the ultramarine synthesis.The reactions were performed at 800 °C for 8 h with (Na2CO3+ S8)/silts ratio and the active carbon/silts ratio as 1.5 and 0.2, respectively.
Figure 9 is the XRD patterns of the products synthesized from different silts.For raw (Si/Al ratio=2.77),<10 μm (Si/Al ratio=2.32)and <5 μm (Si/Al ratio=1.95) silts, both lazurite and nepheline were formed, since the peak heights of lazurite are low, its amount may not be high.For < 2 μm (Si/Al ratio=1.58)silts, lazurite was the only phase and it was very distinct.Kowalak et al. [25] used different types of zeolite as aluminosilicate sources to synthesize ultramarine.Their results showed that the sodalite structure could be synthesized using zeolite A (Si/Al ratio=1) and zeolite X (Si/Al ratio=1-1.5),while it could not using zeolite Y (Si/Al ratio=1.5-3),mordenite (Si/Al ratio=5-10) and ZSM-5 (Si/Al ratio ≥10).They concluded that the sodalite structure can be synthesized from aluminosilicate sources with small Si/Al ratios.Large Si/Al ratios are unfavorable to the formation of sodalite phase and favor the formation of other undesired phases.From the results of Figure 9, <5 μm silts seem to be on the margin between good and bad raw materials and agree with Kowalak et al.

Effects of Mineral Composition of Starting Silts
The results of Table 1 and Figure 4 show that as the silt sizes are fine, more clay minerals are contained in the silts.In this test, the raw and classified silts were used to investigate the effects of mineral composition on the ultramarine synthesis.The reactions were performed at 800 °C for 8 h with (Na2CO3+ S8)/silts ratio and the active carbon/silts ratio as 1.5 and 0.2, respectively.
Figure 9 is the XRD patterns of the products synthesized from different silts.For raw (Si/Al ratio=2.77),<10 μm (Si/Al ratio=2.32)and <5 μm (Si/Al ratio=1.95) silts, both lazurite and nepheline were formed, since the peak heights of lazurite are low, its amount may not be high.For < 2 μm (Si/Al ratio=1.58)silts, lazurite was the only phase and it was very distinct.Kowalak et al. [25] used different types of zeolite as aluminosilicate sources to synthesize ultramarine.Their results showed that the sodalite structure could be synthesized using zeolite A (Si/Al ratio=1) and zeolite X (Si/Al ratio=1-1.5),while it could not using zeolite Y (Si/Al ratio=1.5-3),mordenite (Si/Al ratio=5-10) and ZSM-5 (Si/Al ratio ≥10).They concluded that the sodalite structure can be synthesized from aluminosilicate sources with small Si/Al ratios.Large Si/Al ratios are unfavorable to the formation of sodalite phase and favor the formation of other undesired phases.From the results of Figure 9, <5 μm silts seem to be on the margin between good and bad raw materials and agree with Kowalak et al.

Effects of Mineral Composition of Starting Silts
The results of Table 1 and Figure 4 show that as the silt sizes are fine, more clay minerals are contained in the silts.In this test, the raw and classified silts were used to investigate the effects of mineral composition on the ultramarine synthesis.The reactions were performed at 800 °C for 8 h with (Na2CO3+ S8)/silts ratio and the active carbon/silts ratio as 1.5 and 0.2, respectively.
Figure 9 is the XRD patterns of the products synthesized from different silts.For raw (Si/Al ratio=2.77),<10 μm (Si/Al ratio=2.32)and <5 μm (Si/Al ratio=1.95) silts, both lazurite and nepheline were formed, since the peak heights of lazurite are low, its amount may not be high.For < 2 μm (Si/Al ratio=1.58)silts, lazurite was the only phase and it was very distinct.Kowalak et al. [25] used different types of zeolite as aluminosilicate sources to synthesize ultramarine.Their results showed that the sodalite structure could be synthesized using zeolite A (Si/Al ratio=1) and zeolite X (Si/Al ratio=1-1.5),while it could not using zeolite Y (Si/Al ratio=1.5-3),mordenite (Si/Al ratio=5-10) and ZSM-5 (Si/Al ratio ≥10).They concluded that the sodalite structure can be synthesized from aluminosilicate sources with small Si/Al ratios.Large Si/Al ratios are unfavorable to the formation of sodalite phase and favor the formation of other undesired phases.From the results of Figure 9, <5 μm silts seem to be on the margin between good and bad raw materials and agree with Kowalak et al.

Effects of Mineral Composition of Starting Silts
The results of Table 1 and Figure 4 show that as the silt sizes are fine, more clay minerals are contained in the silts.In this test, the raw and classified silts were used to investigate the effects of mineral composition on the ultramarine synthesis.The reactions were performed at 800 °C for 8 h with (Na2CO3+ S8)/silts ratio and the active carbon/silts ratio as 1.5 and 0.2, respectively.
Figure 9 is the XRD patterns of the products synthesized from different silts.For raw (Si/Al ratio=2.77),<10 μm (Si/Al ratio=2.32)and <5 μm (Si/Al ratio=1.95) silts, both lazurite and nepheline were formed, since the peak heights of lazurite are low, its amount may not be high.For < 2 μm (Si/Al ratio=1.58)silts, lazurite was the only phase and it was very distinct.Kowalak et al. [25] used different types of zeolite as aluminosilicate sources to synthesize ultramarine.Their results showed that the sodalite structure could be synthesized using zeolite A (Si/Al ratio=1) and zeolite X (Si/Al ratio=1-1.5),while it could not using zeolite Y (Si/Al ratio=1.5-3),mordenite (Si/Al ratio=5-10) and ZSM-5 (Si/Al ratio ≥10).They concluded that the sodalite structure can be synthesized from aluminosilicate sources with small Si/Al ratios.Large Si/Al ratios are unfavorable to the formation of sodalite phase and favor the formation of other undesired phases.From the results of Figure 9, <5 μm silts seem to be on the margin between good and bad raw materials and agree with Kowalak et al.

Effects of Mineral Composition of Silts
The results of 1 and Figure 4 show that as the silt sizes are fine, more clay minerals are contained in the silts.In this test, the raw and classified silts were used to investigate the effects of mineral composition on the ultramarine synthesis.The reactions were performed at 800 • C for 8 h with (Na 2 CO 3 + S 8 )/silts ratio and the active carbon/silts ratio as 1.5 and 0.2, respectively.
Figure 9 is the XRD patterns of the products synthesized from different silts.For raw (Si/Al ratio = 2.77), <10 µm (Si/Al ratio = 2.32) and <5 µm (Si/Al ratio = 1.95) silts, both lazurite and nepheline were formed, since the peak heights of lazurite are low, its amount may not be high.For < 2 µm (Si/Al ratio = 1.58) silts, lazurite was the only phase and it was very distinct.Kowalak et al. [25] used different types of zeolite as aluminosilicate sources to synthesize ultramarine.Their results showed that the sodalite structure could be synthesized using zeolite A (Si/Al ratio = 1) and zeolite X (Si/Al ratio = 1-1.5),while it could not using zeolite Y (Si/Al ratio = 1.5-3), mordenite (Si/Al ratio = 5-10) and ZSM-5 (Si/Al ratio ≥10).They concluded that the sodalite structure can be synthesized from aluminosilicate sources with small Si/Al ratios.Large Si/Al ratios are unfavorable to the formation of sodalite phase and favor the formation of other undesired phases.From the results of Figure 9, <5 µm silts seem to be on the margin between good and bad raw materials and agree with Kowalak et al.The SEM images of the products are shown in Figure 10.According to Cork [19,20], the mean particle size of a commercial ultramarine should range from 0.7 to 5.0 μm.It is obvious that the products derived from the classified silts with particle size less than 5 μm and so on meet the requirement.The SEM images of the products are shown in Figure 10.According to Cork [19,20], the mean particle size of a commercial ultramarine should range from 0.7 to 5.0 µm.It is obvious that the products derived from the classified silts with particle size less than 5 µm and so on meet the requirement.The SEM images of the products are shown in Figure 10.According to Cork [19,20], the mean particle size of a commercial ultramarine should range from 0.7 to 5.0 μm.It is obvious that the products derived from the classified silts with particle size less than 5 μm and so on meet the requirement.The color properties of the products from the four starting materials are listed in Table 6.It shows that as the particle size becomes fine, the color properties make great progress, and when the particle size of the silts is <5 µm, the chroma of the products can achieve over 50 with lightness below 40 and hue around 270 • .From the results of Table 1, the Si/Al ratio of <5 µm silts is 1.95, therefore either from the criterion of the sodalite phase formation or the color performance, a requirement of the silt size for the synthesis of ultramarine is passing 5 µm.In Table 6, the color properties of additional three ultramarine samples, a commercial painting pigment (Sennelier l'Aquarelle), a natural lapis lazuli bead, and a recent report of ultramarine synthesized from kaolin clay [31], are also listed.It is obvious that the ultramarine of this study is competitive.The color properties of the products from the four starting materials are listed in Table 6.It shows that as the particle size becomes fine, the color properties make great progress, and when the particle size of the silts is <5 μm, the chroma of the products can achieve over 50 with lightness below 40 and hue around 270°.From the results of Table 1, the Si/Al ratio of <5 μm silts is 1.95, therefore either from the criterion of the sodalite phase formation or the color performance, a requirement of the silt size for the synthesis of ultramarine is passing 5 μm.In Table 6, the color properties of additional three ultramarine samples, a commercial painting pigment (Sennelier l'Aquarelle), a natural lapis lazuli bead, and a recent report of ultramarine synthesized from kaolin clay [31], are also listed.It is obvious that the ultramarine of this study is competitive.

Conclusions
This study provides a possibility to synthesize ultramarine blue from reservoir silts, thereby offering a new utilization of the silts.To remove the unusable quartz and keep the useful clays, so as to decrease the Si/Al ratio of the silts to less than 2, the raw silts must be classified to obtain the fine part.In this study the particle sizes must be smaller than 5 μm.Ultramarine can be synthesized with the conditions: Na2CO3/S8 wt.ratio = 1; (Na2CO3 + S8)/silts ratio of 1.5; active carbon/silts ratio of 0.2 and calcination at 800 °C for 8 h.Under the optimal conditions, the ultramarine synthesized from <2 μm silts has the following color properties: chroma 52.4; lightness 38.5 and hue 271.2°.
The color properties of the products from the four starting materials are listed in Table 6.It shows that as the particle size becomes fine, the color properties make great progress, and when the particle size of the silts is <5 μm, the chroma of the products can achieve over 50 with lightness below 40 and hue around 270°.From the results of Table 1, the Si/Al ratio of <5 μm silts is 1.95, therefore either from the criterion of the sodalite phase formation or the color performance, a requirement of the silt size for the synthesis of ultramarine is passing 5 μm.In Table 6, the color properties of additional three ultramarine samples, a commercial painting pigment (Sennelier l'Aquarelle), a natural lapis lazuli bead, and a recent report of ultramarine synthesized from kaolin clay [31], are also listed.It is obvious that the ultramarine of this study is competitive.

Conclusions
This study provides a possibility to synthesize ultramarine blue from reservoir silts, thereby offering a new utilization of the silts.To remove the unusable quartz and keep the useful clays, so as to decrease the Si/Al ratio of the silts to less than 2, the raw silts must be classified to obtain the fine part.In this study the particle sizes must be smaller than 5 μm.Ultramarine can be synthesized with the conditions: Na2CO3/S8 wt.ratio = 1; (Na2CO3 + S8)/silts ratio of 1.5; active carbon/silts ratio of 0.2 and calcination at 800 °C for 8 h.Under the optimal conditions, the ultramarine synthesized from <2 μm silts has the following color properties: chroma 52.4; lightness 38.5 and hue 271.2°.
The color properties of the products from the four starting materials are listed in Table 6.It shows that as the particle size becomes fine, the color properties make great progress, and when the particle size of the silts is <5 μm, the chroma of the products can achieve over 50 with lightness below 40 and hue around 270°.From the results of Table 1, the Si/Al ratio of <5 μm silts is 1.95, therefore either from the criterion of the sodalite phase formation or the color performance, a requirement of the silt size for the synthesis of ultramarine is passing 5 μm.In Table 6, the color properties of additional three ultramarine samples, a commercial painting pigment (Sennelier l'Aquarelle), a natural lapis lazuli bead, and a recent report of ultramarine synthesized from kaolin clay [31], are also listed.It is obvious that the ultramarine of this study is competitive.

Conclusions
This study provides a possibility to synthesize ultramarine blue from reservoir silts, thereby offering a new utilization of the silts.To remove the unusable quartz and keep the useful clays, so as to decrease the Si/Al ratio of the silts to less than 2, the raw silts must be classified to obtain the fine part.In this study the particle sizes must be smaller than 5 μm.Ultramarine can be synthesized with the conditions: Na2CO3/S8 wt.ratio = 1; (Na2CO3 + S8)/silts ratio of 1.5; active carbon/silts ratio of 0.2 and calcination at 800 °C for 8 h.Under the optimal conditions, the ultramarine synthesized from <2 μm silts has the following color properties: chroma 52.4; lightness 38.5 and hue 271.2°.
The color properties of the products from the four starting materials are listed in Table 6.It shows that as the particle size becomes fine, the color properties make great progress, and when the particle size of the silts is <5 μm, the chroma of the products can achieve over 50 with lightness below 40 and hue around 270°.From the results of Table 1, the Si/Al ratio of <5 μm silts is 1.95, therefore either from the criterion of the sodalite phase formation or the color performance, a requirement of the silt size for the synthesis of ultramarine is passing 5 μm.In Table 6, the color properties of additional three ultramarine samples, a commercial painting pigment (Sennelier l'Aquarelle), a natural lapis lazuli bead, and a recent report of ultramarine synthesized from kaolin clay [31], are also listed.It is obvious that the ultramarine of this study is competitive.

Conclusions
This study provides a possibility to synthesize ultramarine blue from reservoir silts, thereby offering a new utilization of the silts.To remove the unusable quartz and keep the useful clays, so as to decrease the Si/Al ratio of the silts to less than 2, the raw silts must be classified to obtain the fine part.In this study the particle sizes must be smaller than 5 μm.Ultramarine can be synthesized with the conditions: Na2CO3/S8 wt.ratio = 1; (Na2CO3 + S8)/silts ratio of 1.5; active carbon/silts ratio of 0.2 and calcination at 800 °C for 8 h.Under the optimal conditions, the ultramarine synthesized from <2 μm silts has the following color properties: chroma 52.4; lightness 38.5 and hue 271.2°.
The color properties of the products from the four starting materials are listed in Table 6.It shows that as the particle size becomes fine, the color properties make great progress, and when the particle size of the silts is <5 μm, the chroma of the products can achieve over 50 with lightness below 40 and hue around 270°.From the results of Table 1, the Si/Al ratio of <5 μm silts is 1.95, therefore either from the criterion of the sodalite phase formation or the color performance, a requirement of the silt size for the synthesis of ultramarine is passing 5 μm.In Table 6, the color properties of additional three ultramarine samples, a commercial painting pigment (Sennelier l'Aquarelle), a natural lapis lazuli bead, and a recent report of ultramarine synthesized from kaolin clay [31], are also listed.It is obvious that the ultramarine of this study is competitive.

Conclusions
This study provides a possibility to synthesize ultramarine blue from reservoir silts, thereby offering a new utilization of the silts.To remove the unusable quartz and keep the useful clays, so as to decrease the Si/Al ratio of the silts to less than 2, the raw silts must be classified to obtain the fine part.In this study the particle sizes must be smaller than 5 μm.Ultramarine can be synthesized with the conditions: Na2CO3/S8 wt.ratio = 1; (Na2CO3 + S8)/silts ratio of 1.5; active carbon/silts ratio of 0.2 and calcination at 800 °C for 8 h.Under the optimal conditions, the ultramarine synthesized from <2 μm silts has the following color properties: chroma 52.4; lightness 38.5 and hue 271.2°.
The color properties of the products from the four starting materials are listed in Table 6.It shows that as the particle size becomes fine, the color properties make great progress, and when the particle size of the silts is <5 μm, the chroma of the products can achieve over 50 with lightness below 40 and hue around 270°.From the results of Table 1, the Si/Al ratio of <5 μm silts is 1.95, therefore either from the criterion of the sodalite phase formation or the color performance, a requirement of the silt size for the synthesis of ultramarine is passing 5 μm.In Table 6, the color properties of additional three ultramarine samples, a commercial painting pigment (Sennelier l'Aquarelle), a natural lapis lazuli bead, and a recent report of ultramarine synthesized from kaolin clay [31], are also listed.It is obvious that the ultramarine of this study is competitive.

Conclusions
This study provides a possibility to synthesize ultramarine blue from reservoir silts, thereby offering a new utilization of the silts.To remove the unusable quartz and keep the useful clays, so as to decrease the Si/Al ratio of the silts to less than 2, the raw silts must be classified to obtain the fine part.In this study the particle sizes must be smaller than 5 μm.Ultramarine can be synthesized with the conditions: Na2CO3/S8 wt.ratio = 1; (Na2CO3 + S8)/silts ratio of 1.5; active carbon/silts ratio of 0.2 and calcination at 800 °C for 8 h.Under the optimal conditions, the ultramarine synthesized from <2 μm silts has the following color properties: chroma 52.4; lightness 38.5 and hue 271.2°.
The color properties of the products from the four starting materials are listed in Table 6.It shows that as the particle size becomes fine, the color properties make great progress, and when the particle size of the silts is <5 μm, the chroma of the products can achieve over 50 with lightness below 40 and hue around 270°.From the results of Table 1, the Si/Al ratio of <5 μm silts is 1.95, therefore either from the criterion of the sodalite phase formation or the color performance, a requirement of the silt size for the synthesis of ultramarine is passing 5 μm.In Table 6, the color properties of additional three ultramarine samples, a commercial painting pigment (Sennelier l'Aquarelle), a natural lapis lazuli bead, and a recent report of ultramarine synthesized from kaolin clay [31], are also listed.It is obvious that the ultramarine of this study is competitive.

Conclusions
This study provides a possibility to synthesize ultramarine blue from reservoir silts, thereby offering a new utilization of the silts.To remove the unusable quartz and keep the useful clays, so as to decrease the Si/Al ratio of the silts to less than 2, the raw silts must be classified to obtain the fine part.In this study the particle sizes must be smaller than 5 μm.Ultramarine can be synthesized with the conditions: Na2CO3/S8 wt.ratio = 1; (Na2CO3 + S8)/silts ratio of 1.5; active carbon/silts ratio of 0.2 and calcination at 800 °C for 8 h.Under the optimal conditions, the ultramarine synthesized from <2 μm silts has the following color properties: chroma 52.4; lightness 38.5 and hue 271.2°.

Figure 2 .
Figure 2. Particle size distribution of raw silts.

Figure 2 .
Figure 2. Particle size distribution of raw silts.

Figure 3 .
Figure 3. XRD patterns of raw and classified silts.

Figure 3 .
Figure 3. XRD patterns of raw and classified silts.

Figure 3 .
Figure 3. XRD patterns of raw and classified silts.

Table 1 .
Chemical analysis of raw and classified silts.

Table 1 .
Chemical analysis of raw and classified silts.
a: Below the detection limit 0.44%.

Table 1 .
Chemical analysis of raw and classified silts.