The present invention relates to a process and plant for manufacturing cement, especially in the oxyfuel mode, and to a use of the oxygen generated by photoautotrophic organisms as oxygen feed for burners in a cement plant. The application further relates to the analogous process and plant for making lime.
The cement industry is (under the umbrella of ECRA, European Cement Research Academy) working on a so-called oxyfuel cement kiln, see e.g.: http://www.ecra-online.org/fileadmin/redaktion/files/pdf/ECRA_Technical_Report_CCS_Phase_III.pdf, http://www.worldcement.com/europe-cis/10042015/ECRA-research-on-carbon-capture-in-cement-industry-661/and http://www.worldcement.com/europe-cis/10042015/ECRA-research-on-carbon-capture-in-cement-industry-662/.
An oxyfuel kiln is very similar to a traditional cement or lime kiln, however it is operated differently. The exhaust gas is being recirculated to the cooler inlet, to replace ambient air. In order to have enough oxygen at the flame of the kiln (>20%), pure oxygen (or at least air that has been stripped of its nitrogen) is injected at the cooler and/or kiln inlet. The amount of oxygen needed is so high that an oxyfuel kiln of usual commercial scale needs an on-site oxygen generating unit that requires a large amount of electrical energy.
As a result of the recycling of the exhaust gas the CO2-concentration is lifted from 25% for regular kilns to >70% for oxyfuel operation mode. After enrichment of the exhaust gas, finally a part of the exhaust gas has to be vented to allow new oxygen to enter the system.
The CO2 level of the exhaust gas can either be further concentrated (by capturing techniques) or the exhaust gas can be liquefied as it is for further steps (storage and/or utilization). The capture of high concentrated CO2 when running in oxyfuel-mode is considered to be the most economical solution (better than the end-of-pipe techniques like amine scrubbers for kilns in regular operation mode with ambient air). Still it is very expensive due to the high additional costs of operation.
It has already been suggested to use CO2 from exhaust gas as feed for photoautothrophic organisms that generate valuable products from it when exposed to light. Such organisms typically build-up biomass that is subsequently converted to the desired product. In an improved more recent approach organisms have been obtained by genetic modification that can convert CO2 directly into carbon based products like hydrocarbons and alcohols, see e.g. WO 2009/036095 A1 and WO 2010/044960 A1.
It has now surprisingly been found that the oxygen generated by photoautotrophic organisms is a cost effective source of oxygen for oxyfuel and other cement kilns for manufacturing cement. The same applies to lime kilns. The organisms can advantageously be fed with the CO2 vented from the cement plant.
Thus, the present invention solves the problem of providing less costly oxygen for a process for operating a cement or lime plant comprising an oxyfuel kiln and/or oxyfuel calciner, wherein the oxygen is at least partly provided by photoautotrophic organisms. Furthermore, the oxygen generated by photoautotrophic organisms can also be used to provide oxygen enriched air for normal cement or lime kilns and calciners, allowing e.g. more alternative fuels to be used or a higher flame temperature. Therefore, the present invention also solves the problem of improving the combustion in a cement kiln and/or calciner or in a lime kiln, wherein heat is generated by combustion of a fuel in the kiln and/or calciner and a gas fed to the kiln and/or to the calciner for combustion of the fuel contains an oxygen rich exhaust gas from a bioreactor containing photoautotrophic organisms. The problem of providing less costly oxygen and improving combustion is further solved with a cement or lime plant wherein the cement plant comprises a kiln and a calciner and the lime plant comprises a kiln, especially comprising an oxyfuel kiln and/or oxyfuel calciner, a bioreactor containing photoautotrophic organisms and means for passing oxygen generated by the organisms into the kiln and/or calciner. The problem is finally solved by using oxygen enriched exhaust gas from a bioreactor containing photoautotrophic organisms as full or partial replacement of air for combustion of a fuel in a kiln and/or calciner of a cement or lime plant for manufacturing cement or lime, respectively.
It is advantageous to use the exhaust gas from the cement or lime plant as feed gas for the photoautotrophic organisms in the bioreactor. This is especially beneficial for cement and lime plants operated in the oxyfuel mode, where the exhaust gas contains a high amount of CO2. But it is also a good way of utilization for CO2 exhausted by normal cement or lime plants. In the case of normal cement or lime plants an enrichment of CO2 in the exhaust gas by any known means can be foreseen.
For cement and lime plants operated in the oxyfuel mode there exists a further problem. The cement or lime plant works continuously but the bioreactor only during day time, i.e. when sunlight is available. Thus, the problem of oxygen supply to the kiln (and/or calciner) during the night has to be solved. For the preferred utilization of CO2 vented from the cement or lime plant as feed gas for the bioreactor the same problem arises for normal and oxyfuel operation, i.e. the bioreactor cannot consume CO2 during the night. To solve this problem the generated oxygen and/or CO2 is/are partly stored, so that the operating conditions of the kiln (and/or calciner) can be kept more or less constant during day and night. Advantageously, the gas(es) are stored by liquefying. While it seems possible to store all exhaust gas over the whole time it is expected to be more efficient to store only parts and use the rest directly as long as possible. Storage of parts needs more conduits and means for control and regulation, but it is expected to have a better energy efficiency.
It is of course also possible to supply oxygen from another source during the night, e.g. from water electrolysis that utilizes cheap surplus power in the electric supply network. Likewise, CO2 vented during the night can be used in other ways than feeding it to the bioreactor. One possible use is conversion to carbon based products using the hydrogen generated by water electrolysis.
As a third alternative, especially for cement and lime plants that are not operated in the oxyfuel mode, the supply of extra oxygen can simply be stopped during the night and the fuel and/or conditions of burning are adapted accordingly.
It is especially preferred to apply the methods and plants according to the invention to the manufacturing of cement, specifically to making ordinary portland cement.
The invention will be illustrated further with reference to the attached figures, without restricting the scope to the specific embodiments described. If not otherwise specified any amount in % or parts is by volume and in the case of doubt referring to the total volume of the composition/mixture concerned. The invention further includes all combinations of described and especially of preferred featurest that do not exclude each other. A characterization as “approximately”, “around” and similar expression in relation to a numerical value means that up to 10% higher and lower values are included, preferably up to 5% higher and lower values, and in any case at least up to 1% higher and lower values, the exact value being the most preferred value or limit.
In the figures:
In all figures the gas streams are shown with simple arrows and streams of solid material with wider arrows having a frame. Sunlight is depicted as wave. Inactive parts are shown in dotted lines.
The kiln 1 is operated in the oxyfuel mode, that means the gas entering the clinker cooler 3 does not contain any substantial amount of nitrogen, preferably it consists of oxygen and the recirculated gas containing unburnt oxygen and CO2. It contains only traces of other gases like nitrogen, argon and other components of air, that would require an inadequate expenditure to be removed. The recirculated CO2 is preferably dried. The gas entering the cooler 3 is preheated while the clinker cools. The preheated gas enters the kiln 1 where fuel is burnt to sinter the preheated or calcined raw meal to form the cement clinker which moves into the cooler 3. The hot gas is passed into the preheater/calciner 2, where the raw meal is preheated and usually also at least partly calcined. Typically, full calcination requires an additional burner.
The exhaust gas from the preheater/calciner 2 is recirculated to the cooler 3 and partly vented. Generally the vented gas contains 70% or more CO2 whereas the exhaust from a normal cement plant contains 20% to 25%.
In the shown embodiment, the vented gas is fed to the bioreactor 4 to be converted into valuable products by the organisms. In the bioreactor 4 photoautotrophic organisms convert CO2 into valuable products using sunlight as energy source. Besides the valuable product the organisms generate oxygen, which is added to the gas entering the cooler 3 according to the invention. The oxygen could of course also be added to the kiln inlet.
The day time operation is shown in
In all embodiments the process and device according to the invention can also be used when only the calciner is operated in the oxyfuel mode instead of the kiln and calciner. The CO2 reduction achieved with only an oxyfuel calciner in comparison to a normal kiln will be less than for the oxyfuel kiln but still considerable. The advantage is that the necessary changes to the plant are less. Since oxyfuel operation requires to keep out air, the demands on the tightness of the cooler, kiln and preheater/calciner are high. Restricting these requirements to the preheater/calciner section will lower the demands noticeably.
As noted previously, the bioreactor (4, 14) is only operating during day time while the cement plant runs 24 hours a day. Therefore, unless it is acceptable to operate the oxyfuel cement plant with differing conditions during night and day, some sort of oxygen supply has to be provided during the night. When no scheme as above described, i.e. a storage of part of the oxygen generated during the day, is possible or desired, oxygen supply as known in the art will be used during the night. The most common supply is by isolating oxygen from the ambient air, e.g. with the Linde process or some improved method.
Another possible approach is generation of oxygen by electrolysis of water, wherein it is desirable to utilize the hydrogen generated concurrently for converting the CO2 to valuable products. Such a process is described e.g. in WO 2015/055349 A1.
With regard to the bioreactor (4, 14), the most preferred photoautotrophic organisms are ones of the type described in WO 2009/036095 A1 and WO 2010/044960 A1. These produce the valuable end product, for example ethanol, directly. However, is is also possible to rely on other known processes and organisms, like algea, that utilize light and CO2 to build up biomass that is subsequently converted into the desired valuable end products.
For an exemplary oxyfuel kiln the mass balance for oxygen and carbon dioxide has been calculated and is shown in the following table 1.
It can be seen, that for a typical cement kiln and a bioreactor dimensioned to be fed all the CO2 evaporated from the kiln operated in the in oxyfuel mode at least 65 tons/hour oxygen are available for storage and/or other uses.
The process according to the invention for operating a cement plant comprising a cement kiln and a calciner, wherein heat is generated by combustion of a fuel in the kiln and/or calciner, uses as gas for combustion of the fuel an oxygen rich exhaust gas from a bioreactor containing photoautotrophic organisms. Thereby, a cost effective source of oxygen is provided for improving combustion in the cement plant and utilizing the oxygen rich exhaust gas from the bioreactor generates an additional economical benefit for the reactor-plant.
In the preferred embodiment the cement plant is operated in the oxyfuel mode by using exhaust gas from the kiln and/or calciner together with the oxygen from the bioreactor as the gas fed to the kiln and/or calciner for combustion of the fuel. Thereby, a cost effective source of oxygen is provided for the oxyfuel cement plant and the gas vented from the cement plant is converted into valuable products by the organisms in the bioreactor.
The illustrated devices and methods can be applied analogously to the manufacturing of lime as shown in
Of course, the lime plants may be equipped with the same oxygen and/or carbon dioxide storage devices as the cement plants described before. Also the same methods of providing oxygen and using carbon dioxide during the night can be applied.
Number | Date | Country | Kind |
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16165521.2 | Apr 2016 | EP | regional |
Filing Document | Filing Date | Country | Kind |
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PCT/EP2017/057751 | 3/31/2017 | WO | 00 |