METHOD FOR UPGRADING COMBUSTION ASH |
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| 申请号 | EP10803628.6 | 申请日 | 2010-12-02 | 公开(公告)号 | EP2507187B1 | 公开(公告)日 | 2014-07-30 |
| 申请人 | Sonoash LLC; | 发明人 | OEHR, Klaus, H.; CYR, Gary, A.; JANKE, Travis; ARATO, Claudio, I.; MCELROY, Roderick, O.; | ||||
| 摘要 | |||||||
| 权利要求 | |||||||
| 说明书全文 | The invention pertains to methods of upgrading combustion ash, particularly coal combustion ash, for applications such as use as a pozzolanic additive for blended cement or as cement kiln raw material for cement clinker manufacture. It is known in the art of cement manufacture that combustion ash, particularly bituminous coal fly ash, is a useful additive in the making of cements, by virtue of its pozzolanic properties. A pozzolan is a material which, when combined with calcium hydroxide released by cement (e.g. Portland cement) during its hydration with water, exhibits cementitious properties in the presence of water. Pozzolanic ash, such as class F bituminous fly ash, can be used as a component of blended cements if it meets certain quality specifications (e.g. ASTM C618). The technical benefits to be gained from addition of such materials to blended cements include reduced use of Portland cement per unit volume of mortar or concrete, increased strength and reduced water permeability of the mortar or concrete. Economic benefits arise from the reduction in the amount of Portland cement used, the higher quality of the mortar or concrete produced and the minimization of coal fly ash sent to landfill. The value of bituminous coal fly ash as a pozzolan is enhanced by reducing its particle size, which increases the surface area and reactivity of silica and siliceous materials towards the free calcium hydroxide generated by hydration of Portland cement, reduces water porosity and increases the compressive strength of the resulting concrete. Reducing the ammonia content of bituminous fly ash also increases its value as a pozzolan since little or no gaseous ammonia is released when the ammonia-depleted ash is added to cement clinker and water to make blended cement, mortar or concrete. It is also known that the reduction of overall particle size distribution of aluminosilicate raw materials for cement kilns, including bituminous fly ash, enhances cement kiln throughput. However, the high mercury content of bituminous fly ash relative to shale or clay dramatically reduces its acceptance as a cement kiln raw material. The only cement kiln raw material having a mean mercury content higher than coal fly ash is recycled cement kiln dust: Other prior art references pertaining to the state of the art are: (1) Accordingly, there exists a need for practical, economical, large-scale processes that can upgrade combustion ash, especially bituminous coal fly ash, by reducing its mercury content. The present inventors have determined that wet froth flotation is able to dramatically reduce the mercury content of pozzolanic combustion ash, especially bituminous combustion ash. Moreover, when pulverization of the ash is carried out before wet froth flotation, mercury reduction is further enhanced, mercury-depleted ash recovery from flotation is improved, and the value of the ash is increased as a pozzolanic or cement kiln raw material, due to reduced particle size and dramatically reduced mercury content. In one embodiment, the invention provides a method for reducing the mercury content of pozzolanic combustion ash. A slurry is formed of the combustion ash and water, the combustion ash is Pulverized before or after forming the slurry. The slurry is subjected to froth flotation to form a mercury-enriched ash slurry and a mercury-depleted ash slurry. The product mercury-depleted ash slurry is separated from the mercury-enriched ash slurry. The invention further provides methods for reducing the ammonia content of pozzolanic combustion ash, such that the levels of both mercury and ammonia in the combustion ash are reduced. The invention further provides mercury-depleted combustion ash slurry, and partially dried and fully dried combustion ash, made by the foregoing methods. Pozzolanic applications for these products include, for the wet mercury-depleted ash slurry, use in wet cement kilns, mortar or concrete. The dried mercury-depleted ash product is useful in dry cement kilns for cement clinker manufacture. Further aspects of the invention and features of specific embodiments are described below. Combustion ash for use in the process of the invention can be any kind of pozzolanic combustion ash, in particular coal combustion ash, having a mercury content such that it is desirable to reduce the mercury content for use of the combustion ash in pozzolanic applications or cement clinker manufacture. An example is bituminous coal combustion ash, especially bituminous coal fly ash. The combustion ash may include ammonia in addition to the mercury. Referring to The froth flotation is operated so as to render the mercury hydrophobic by the use of a suitable collector chemical, in order to separate it into the froth. The collector may be hydrophobic, or hydrophobic and slightly hydrophilic. Kerosene, or a mixture of kerosene and tall oil, are examples of suitable collectors. During the froth flotation step, water (stream 30), the collector (stream 32) and a frothing agent (stream 34) are added as required. Optionally, acid (stream 36) may be added. The conventional processing parameters of froth flotation, well known in the art and including flotation cell volume, pH control, impeller speed, aeration flow rate, collector type and ratio, frothing agent type and ratio, mixture temperature, pulp density, length of ash conditioning period i.e. reagent mixing time, and length of aeration, i.e. froth collection time, are selected and controlled according to the requirements for a particular application. The froth flotation step may be single-stage or multi-stage. The pH of the combustion ash slurry in the froth flotation cell may be adjusted to optimize the yield of mercury-reduced ash. The pH of combustion ash varies greatly and may be alkaline or acidic. An alkaline ash slurry having, for example, a pH of about 8, may be acidified in the flotation cell to a pH of about 4, or in the range of 3.5 - 4.5, or 3.8 - 4.2, by addition of acid, e.g. sulphuric acid. The flotation process works better at low pH. However, if the ash rejects from the process are to be discharged to an unlined landfill, the pH may be adjusted upward in the flotation cell. The froth flotation process separates the combustion ash slurry into a mercury-enriched combustion ash slurry (i.e. having a higher concentration of mercury than the input combustion ash slurry) and a mercury-depleted combustion ash slurry (i.e. having a lower concentration of mercury than the input combustion ash slurry). The mercury-enriched ash slurry is removed from the flotation cell as froth product (stream 38) and is sent to a froth collector to be discarded or further processed. The mercury-depleted ash slurry is removed (stream 40) and is allowed to separate from excess water. The process is effective in removing both oxidized and elemental mercury, both forms of mercury being present in combustion ash. Optionally, the mercury-depleted ash slurry may be sent to a dryer D, where water is partly or completely removed (stream 42), leaving partly or completely dried mercury-depleted ash product (stream 44). Drying may be done, for example, by means of centrifuging the slurry to partially dry it, or centrifuging followed by oven drying at 105° C. for 24 hours to fully dry it. The drying step would be omitted if the mercury-depleted ash slurry is to be used in a wet cement kiln. The combustion ash may be pulverized before being subjected to froth flotation. In this embodiment of the process, instead of feeding it directly to the froth flotation apparatus F, the combustion ash slurry (stream 44) is fed to a pulverizer P. Pulverizing the combustion ash reduces its mean particle size and has been determined to enhance the flotation yield of product mercury-depleted ash slurry. Any suitable pulverizing apparatus can be used. For example, the pulverizer may be an acoustic frequency sonicator of the type described by The pulverized combustion ash (stream 48) is then fed to the froth flotation apparatus F and the process continues as described above. In an alternative embodiment (not shown in the drawing) the combustion ash is pulverized in dry form and is then fed to the slurry mixing tank, and the slurry is then subjected to froth flotation as described above. Samples of bituminous coal fly ash A having 250 parts per billion mercury, 28.6 micron mean particle size and a pH of 8.4 were subjected to froth flotation. The flotation conditions were: 1200 rpm impeller speed; 10 liters per minute aeration flow rate, i.e. 1.09 liters air/liter of pulp/minute; kerosene and tall oil (from pine) as collector, 0.004 grams kerosene per gram fly ash, 0.004 grams tall oil per gram fly ash; 0.002 grams Dowfroth 2b0-C (1-(1-methoxypropan-2-yloxy)propan-2-ol) per gram of fly ash as frothing agent; 10% pulp density (dry mass of ash/mass of ash slurry); slurry temperature 35° C.; 9.2 L flotation cell; no pH adjustment; 5 minute conditioning period; 20 minute aeration period. One comparative sample was not pulverized before froth flotation and other samples were pulverized in batch mode or continuous mode using an acoustic frequency sonicator. After froth flotation, the mean particle size, mercury content and yield of the product mercury-depleted ash slurry were measured. The results are shown in Table 1. The notation "<20" in Table 1 indicates a mercury content less than the detection limit of the testing equipment, namely 20 ppb. The results show that froth flotation of the combustion ash dramatically reduces the mercury content, and that initial pulverization enhances the reduction. Samples of bituminous fly ash A as in Example 1 were processed under the same conditions except that the pH of the ash slurry was adjusted to pH 4 by adding 0.0037 grams sulphuric acid per gram fly ash to the flotation cell. The results are shown in Table 2. The results demonstrate that acidification of the ash increases the yield of mercury-depleted ash slurry. Raw unsieved class F bituminous coal fly ash B containing 205 ppb mercury and 192 parts per million available ammonia nitrogen was wet pulverized in an acoustic frequency 3 litre sonication chamber for 3 minutes under the following conditions: 8.8 kg of 1.18 mm steel shot pulverization media, 0.6 kg of water, and 0.85 kg of raw bituminous fly ash, resulting in a chamber void volume of 23%. The available ammonia nitrogen content after pulverization was 2.67 ppm, thus achieving a 98.6% reduction. The pulverized fly ash was then subjected to wet froth flotation as described in Example 1. There was a further reduction of available ammonia nitrogen to 1.86 ppm, or 99% reduction overall. Throughout the foregoing description and the drawing, specific details have been set forth in order to provide a more thorough understanding to persons skilled in the art. However, well known elements may not have been shown or described in detail to avoid unnecessarily obscuring the disclosure. The description and drawing are to be regarded in an illustrative, rather than a restrictive, sense. As will be apparent to those skilled in the art in the light of the foregoing disclosure, many alternations and modifications are possible in the practice of this invention without departing from the scope thereof. The scope of the invention is to be construed in accordance with the following claims. |
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