| US20150336051A1 | 2015-11-26 | |||
| US20110200505A1 | 2011-08-18 | |||
| US20130149225A1 | 2013-06-13 | |||
| US20110041481A1 | 2011-02-24 | |||
| US4309386A | 1982-01-05 |
| Claims 1. A method for the removal of nitrogen oxides from flue gas from combustion facilities, comprising the steps of passing the flue gas through one or more fabric filter bags catalysed with a catalyst for selective reduction of nitrogen oxides in presence of ammonia added to the flue gas either as such or in form of a precursor there- of; injecting an effluent gas containing nitrogen dioxide into the flue gas upstream the one or more fabric filter bags ; providing the effluent gas containing nitrogen dioxide by steps of catalytically oxidizing ammonia or a precursor thereof with an oxygen containing atmosphere to an effluent gas containing nitrogen monoxide and oxygen in presence of an oxidation catalyst; cooling the effluent gas to ambient temperature and oxi¬ dizing the nitrogen monoxide in the cooled effluent gas to the nitrogen dioxide containing effluent gas. 2. The method of claim 1, wherein the oxygen con- taining atmosphere comprises flue gas. 3. The method of claim 1, wherein the oxygen atmos¬ phere is ambient air. 4. The method according to any one of claims 1 to 3, wherein the nitrogen dioxide containing effluent gas is injected into the flue gas in an amount resulting in 45 to 55% by volume of the nitrogen oxides is nitrogen di¬ oxide at inlet to the catalyst for selective reduction of nitrogen oxides. 5. The method according to any one of claims 1 to 4, wherein the oxidation of the nitrogen monoxide in the cooled effluent gas to the nitrogen dioxide containing effluent gas is performed in presence of an oxidation catalyst . 6. System for use in the method according to any one of claims 1 to 5, comprising within a flue gas duct a filter bag house with one or more fabric filter bags catalysed with a catalyst for selective reduction of ni¬ trogen oxides; upstream the one or more fabric filter bags or the fil¬ ter bag house injection means for injection of ammonia or a urea solution into the flue gas duct; upstream the one or more fabric filter bags or the fil¬ ter bag house, injection means for injection of nitrogen dioxide containing effluent gas; and outside the flue gas duct, an ammonia oxidation catalyst unit; and means for cooling and oxidizing nitrogen monoxide containing effluent gas withdrawn from the ammonia oxida¬ tion catalyst to the nitrogen dioxide containing efflu¬ ent gas connected at its outlet end to the injection means for injection of the nitrogen dioxide containing effluent gas. 7. The system of claim 6, wherein the means for cooling and oxidizing the nitrogen monoxide containing effluent gas is in form of a heat exchanger. 8. The system of claim 6, wherein the means for cooling and oxidizing the nitrogen monoxide containing effluent gas is in form of a spirally wound tube. 9. The system of any one of claims 6 to 8, wherein the means for the cooling and oxidizing nitrogen monoxide containing effluent gas is provided with an oxida¬ tion catalyst. |
FILTER
BAGS WITH AN SCR CATALYST
The present invention relates to a method and system for 5 reducing emission particulate matter and nitrogen oxides (NOx) from off-gasses and flue gases. In particular, the method and system of the invention provides an improved re ¬ duction of NOx at low gas temperatures.
10 Flue gases from different combustion facilities, e.g. boil ¬ ers in solid or liquid fired power plants gas, oil-fired generators or cement kilns, biofuel fuelled combustion plants and waste incineration plants contain a number of environmentally problematic or even poisonous compounds.
15 These comprise particulate matter and NOx.
Use of particulate filters and catalytic cleaning of flue gas reduces the amount of particulate matter and NOx and is therefore beneficial for the environment in general. In 20 most areas, legislation requires reduction of NOx in the flue gas .
Fabric filter bags are extensively used in many industries for removal of particulate matter from flue and process 25 gases. They are the most efficient types of dust collec ¬ tors .
As mentioned above, off and flue gases very often contain a plurality of pollutants, inter alia nitrogen oxides in con- 30 centrations that have to be removed or reduced depending on local legislation. For this purpose, several conventional methods are available. In all cases additional units up/downstream the fabric filter bags have to be installed and operated.
In assignees co-pending patent application US 2017/0080387, which by reference thereto is included herein in its en ¬ tirety, filter bags catalysed with SCR active catalysts are disclosed. These filter bags reduce or remove the NOx con ¬ centration and particulate matter, when the off or flue gas passes through the filter bags.
Due to the composition of fibers constituting the filter bags, these must be operated at temperatures lower than 250°C. In Selective Catalytic Reduction (SCR) of NOx, nitrous ox ¬ ide compounds are selectively reduced to harmless nitrogen and water by reaction with a reduction agent, e.g. ammonia, over a catalyst. The low gas temperature required by the filter bag composi ¬ tion encounters a problem in the NOx removal by means of SCR.
The problem with the known SCR catalysts is the relatively low efficiency at gas temperatures below 250°C.
This invention is based on forming NO 2 externally to the flue gas duct and injecting the prepared NO 2 into the flue gas in an amount that promotes the so called "fast" SCR re- action. NO 2 can be formed from N¾ by oxidation of the N¾ to NO over a precious metal containing catalyst in a first step and subsequently oxidation of NO to O 2 in a second step .
It is known that the SCR reaction can be considerably ac- celerated, and the low temperature activity can be signifi ¬ cantly raised at equimolar amounts of NO and NO 2 in the flue gas by the "fast" SCR reaction:
2NH 3 + NO + N0 2 → 2N 2 + 3H 2 0.
Thus, the invention provides in a first aspect a method for the removal of nitrogen oxides from flue gas from combus ¬ tion facilities, comprising the steps of
passing the flue gas through one or more fabric filter bags catalysed with a catalyst for selective reduction of nitro ¬ gen oxides in presence of ammonia added to the flue gas ei ¬ ther as such or in form of a precursor thereof;
injecting an effluent gas containing nitrogen dioxide into the flue gas upstream the one or more fabric filter bags; providing the effluent gas containing nitrogen dioxide by steps of
catalytically oxidizing ammonia or a precursor thereof with an oxygen containing atmosphere to an effluent gas contain- ing nitrogen monoxide and oxygen in presence of an oxida ¬ tion catalyst;
cooling the effluent gas to ambient temperature and oxidiz ¬ ing the nitrogen monoxide in the cooled effluent gas to the nitrogen dioxide containing effluent gas.
The problem with the known methods and systems is the rela ¬ tively low efficiency of the SCR catalyst at flue gas tem- peratures below 250°C, as mentioned hereinbefore. This problem is solved by the invention with injection of O2 into the flue gas at the low temperatures to promote the "fast" SCR reaction. This reaction is responsible for the promotion of low temperature SCR.
At flue gas temperatures above 250°C, SCR catalysts have sufficient efficiency and injection of O2 into the flue gas can be disrupted when the gas temperature reaches
250°C.
Ammonia oxidation to NO externally to the flue gas duct, is usually performed in a reactor with a noble metal catalyst, typically platinum or an alloy of platinum with other pre- cious metals as minor components at reaction temperatures of between 250 and 800°C in presence of oxygen containing atmosphere .
To provide the required reaction temperature, the oxidation reactor can be heated by e.g. electrical heating or induc ¬ tion heating.
In an embodiment, the oxygen containing atmosphere includes hot recirculated gas which provides then additionally part of the oxidation reactor heating duty.
NO formed from N¾ in a first step by oxidation of the N¾ in contact with a precious metal containing catalyst is subsequently oxidized to NO2 in the NO containing effluent gas from the first step by cooling the gas to ambient tem ¬ perature to push the equilibrium reaction 2 ΝΟ+θ2^2 NO2 to ¬ wards formation of NO2 . The term "ambient temperature" as used herein, shall mean any temperature prevailing in the surroundings of a combus ¬ tion facility employing the method and system of the inven- tion. Typically, the ambient temperature will be between -20°C and 40°C.
Cooling and oxidation of the NO containing effluent gas can be performed in an aging reactor sized so that the resi- dence time of the gas is about 1 minute or longer.
In an embodiment the oxidation reaction is performed in presence of a catalyst promoting the oxidation of NO to NO 2 · Those catalysts are known in the art and include Pt on T1O 2 , Pt on S1O 2 and activated carbon or Pt and/or Pd on alumina .
As mentioned hereinbefore the desired fast SCR reaction re ¬ quires equal amounts of NO and NO 2 . Consequently, the amount of NO 2 injected into the flue gas at a temperature below 250°C is controlled to result in 45 to 55% by volume of the nitrogen oxides content in the flue gas is NO 2 at inlet to the SCR catalyst unit. In another aspect, the invention provides a system for use in the method according to the invention.
The system comprises within a flue gas duct a filter bag house with one or more fabric filter bags catalysed with a catalyst for selective reduction of nitrogen oxides; upstream the one or more fabric filter bags or the filter bag house injection means for injection of ammonia or a urea solution into the flue gas duct;
upstream the one or more fabric filter bags or the filter bag house, injection means for injection of nitrogen dioxide containing effluent gas; and
outside the flue gas duct,
an ammonia oxidation catalyst unit; and
means for cooling and oxidizing nitrogen monoxide contain- ing effluent gas withdrawn from the ammonia oxidation cata ¬ lyst to the nitrogen dioxide containing effluent gas con ¬ nected at its outlet end to the injection means for injec ¬ tion of the nitrogen dioxide containing effluent gas. As mentioned above, the oxidation reaction of NO to NO 2 needs a residence time of the NO containing gas of at least 1 minute. Typically, 1-2 minutes.
This can be achieved in a heat exchanger either gas cooled or water cooled or alternatively when shaping the cooling and oxidizing means as a spirally wound tube with a length resulting in the desired residence time of the gas passing through the tube . In another embodiment, the means for cooling and oxidizing nitrogen monoxide containing effluent gas is provided with an oxidation catalyst promoting the oxidation of NO to NO 2 .