Catalytic converter and method of controlling exhaust emission
10213778 ยท 2019-02-26
Assignee
Inventors
Cpc classification
F01N3/105
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F01N2430/06
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F01N2450/00
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F01N2900/1402
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
B01D53/9431
PERFORMING OPERATIONS; TRANSPORTING
F01N2510/06
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F01N13/0093
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F01N3/28
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F01N2510/0682
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
B01D53/9445
PERFORMING OPERATIONS; TRANSPORTING
F01N2900/1624
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F01N2340/02
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F01N13/0097
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F01N2560/025
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F01N3/2006
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
B01D53/9495
PERFORMING OPERATIONS; TRANSPORTING
F01N3/2803
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
Y02T10/12
GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
F02D41/126
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F02D41/123
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F01N3/101
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
B01J35/19
PERFORMING OPERATIONS; TRANSPORTING
B01J37/0244
PERFORMING OPERATIONS; TRANSPORTING
F02D41/0295
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
International classification
F01N3/00
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
B01J35/00
PERFORMING OPERATIONS; TRANSPORTING
F01N3/28
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F01N3/10
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F01N3/20
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
Abstract
The present disclosure relates to an improved catalytic converter capable of significantly reducing emissions by reducing the activation time of a catalytic device thereby improving emissions reduction performance, and an exhaust emission emissions reduction control method using the improved catalytic converter. The improved catalytic converter includes: a housing and two or more catalyst substrates disposed inside the housing, wherein the two or more catalyst substrates are separated inside the housing along a longitudinal direction, and the two or more catalyst substrates have a different diameter and a different volume.
Claims
1. An improved catalytic converter comprising: a housing; and two catalyst substrates disposed inside the housing; wherein the catalyst substrates are separated inside the housing, wherein the catalyst substrates have a different radius and a different volume, wherein the two catalyst substrates comprise a first catalyst substrate adjacent to an inlet side of the housing and a second catalyst substrate adjacent to an outlet side of the housing, wherein one of the two catalyst substrates has two zones having different amounts of catalyst, wherein the first catalyst substrate comprises a first zone located on a first side of the first catalyst substrate and a second zone located on a second side of the first catalyst substrate, wherein the first zone and the second zones are comprised of catalysts having different noble metal contents, and wherein the first zone has a higher noble metal content than the second zone, and the second zone has a higher noble metal content than the second catalyst substrate.
2. The improved catalytic converter of claim 1, wherein the radius of the first catalyst substrate is smaller than the radius of the second catalyst substrate.
3. The improved catalytic converter of claim 1, wherein the volume of the first catalyst substrate is smaller than the volume of the second catalyst substrate.
4. The improved catalytic converter of claim 1, further comprising a mixing region formed between the first catalyst substrate and the second catalyst substrate.
5. The improved catalytic converter of claim 4, further comprising an oxygen sensor is installed in the mixing region.
6. An exhaust gas emissions reduction control method using the improved catalytic converter according to claim 1, the method comprising the steps of: determining whether an air-fuel ratio is lean by measuring oxygen concentration of engine exhaust gas passing through the catalytic converter during combustion of the engine; if the air-fuel ratio is lean, performing lambda control of the air-fuel mixture; and following lambda control, determining whether the air-fuel ratio is rich by measuring the oxygen concentration of the engine exhaust gas.
7. An exhaust gas emissions reduction control method using the improved catalytic converter according to claim 1, the method comprising: determining whether an air-fuel ratio is lean by measuring oxygen concentration of engine exhaust gas passing through the catalytic converter after a fuel cut; if the air-fuel ratio is lean, supplying fuel to the engine and purging oxygen; and after purging oxygen, determining whether the air-fuel ratio is rich by measuring the oxygen concentration of the engine exhaust gas.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
(1) The objects, features and advantages of the present disclosure will be more apparent from the following detailed description in conjunction with the accompanying drawings, in which:
(2)
(3)
(4)
(5)
(6)
(7)
(8)
DETAILED DESCRIPTION OF EXAMPLE EMBODIMENTS
(9) Example embodiments of the present disclosure are described with reference to the accompanying drawings in detail. The same reference numbers are used throughout the drawings to refer to the same or like parts. Detailed descriptions of well-known functions and structures incorporated herein may be omitted to avoid obscuring the subject matter of the present disclosure.
(10) Referring to
(11)
(12) An inlet cap 12 may be provided in one end of housing 15, and inlet cap 12 may include an inlet hole 12a through which exhaust gas flows enters catalytic converter 10. An outlet cap 13 may be provided in the other end of housing 15, and outlet cap may include an outlet hole 13a through which the exhaust gas is discharged from catalytic converter 10.
(13) One or more covers 20 may be provided on the outer surface of inlet cap 12. The covers 20 act to insulate the interior of inlet cap 12, thereby increasing the interior temperature of inlet cap 12.
(14) Because cover 20 is provided on the outer surface of inlet cap 12 as described above, thermal energy of the exhaust gas flowing into catalytic converter 10 at startup may be prevented from being lost to the outside, thereby reducing the time needed to reach LOT and significantly improving the emissions reduction performance.
(15) The two or more catalyst substrates 40 and 45 are separated inside housing 15 along a longitudinal direction to form a cascaded catalytic converter.
(16) The two or more catalyst substrates 40 and 45 may have a different volume, and thus, the catalyst substrates 40 and 45 may perform different functions and may cooperate with each other to more efficiently reduce emissions. Accordingly, it is possible to reduce the time needed to reach LOT and significantly improve the emissions reduction performance.
(17) According to an embodiment of the present disclosure, catalyst substrates 40 and 45 may include a first catalyst substrate 40 adjacent to an inlet of housing 15, i.e., inlet cap 12; and a second catalyst substrate 45 adjacent to an outlet of housing 15, i.e., outlet cap 13.
(18) First catalyst substrate 40 and Second catalyst substrate 45 may have a different radius R1 and R2, respectively. Accordingly, first catalyst substrate 40 and second catalyst substrate 45 may also have a different volume.
(19) According to one embodiment, radius R1 of first catalyst substrate 40 is smaller than radius R2 of second catalyst substrate 45, so that volume of first catalyst substrate 40 is smaller than the volume of second catalyst substrate 45. First catalyst substrate 40 and second catalyst substrate 45 may have the same length or a different length.
(20) According to an embodiment of the present disclosure, it is possible to facilitate a rapid feedback control loop through the rapid detection of the oxygen concentration and the reduction of the catalyst activation time. Because the volume of the first catalyst substrate 40 is relatively small, it requires less time to reach LOT, but has less ability to process the volume of emissions in the exhaust gas. Therefore to improve overall emissions reduction, first catalyst substrate 40 may be supplemented by the emissions reduction performance of second catalyst substrate 45, which has a relatively large volume.
(21) In addition, housing 15 may include a first accommodating section 15a for accommodating first catalyst substrate 40 and a second accommodating section 15b for accommodating second catalyst substrate 45. The inner diameter of first accommodating section 15a corresponds to the outer diameter of first catalyst substrate 40 and the inner diameter of second accommodating section 15b corresponds to the outer diameter of second catalyst substrate 45.
(22) When radius R1 of first catalyst substrate 40 is smaller than the radius R2 of the second catalyst substrate 45, the inner diameter of first accommodating section 15a may be smaller than the inner diameter of second accommodating section 15b. Thus, an inclined plane 15c may be formed between first accommodating section 15a and second accommodating section 15b, and the radius of inclined plane 15c increases from first accommodating section 15a towards second accommodating section 15b side.
(23) The outer surface of first catalyst substrate 40 may be wrapped by a support mat and may be accommodated in first accommodating section 15a of housing 15, and the outer surface of the second catalyst substrate 45 may be wrapped by the support mat and may be accommodated in second accommodating section 15b of housing 15.
(24) In an example embodiment, first catalyst substrate 40 may have a diameter of 105.7*(8084) mm, and its volume may be approximately 0.7 to 0.74 L. Because first catalyst substrate 40 has a compact structure with a relatively small diameter and volume, the distance to the outlet of the exhaust system of the engine may be reduced, and the heat capacity of the catalyst may be reduced. It is possible not only to significantly reduce the time needed to reach LOT but also to significantly improve the emission emissions reduction performance.
(25) In an example embodiment, second catalyst substrate 45 may have a diameter of approximately 118.4*(80) mm, and a volume of approximately 0.9 L. Because the diameter and the length of second catalyst substrate 45 are larger than those of first catalyst substrate 40, a relatively large volume may be achieved. Thus, the catalyst emissions reduction performance of the first catalyst substrate 40, which has a relatively small volume, may be compensated for by the larger volume of second catalyst substrate. In addition, as second catalyst substrate 45 has a relatively large volume, the heat capacity may be increased. Accordingly, it is possible to reduce the time needed to reach LOT of the HOT START section of the Federal Test Procedure (FTP), thereby improving the emission reduction performance.
(26) As described above, according to the present disclosure, the time needed for the first catalyst substrate to reach LOT may be reduced by the smaller diameter and smaller volume of the first catalyst substrate 40. Overall emission reduction performance may be improved by supplementing first catalyst substrate with 40 with second catalyst substrate 45, which has a relatively large volume. Accordingly, it is possible to overcome various drawbacks of the related art at the same time.
(27) According to an embodiment of the present disclosure, the volume ratio of first catalyst substrate 40 to second catalyst substrate 45 may be between about 40-60% to about 50-50%. Preferably, the volume ratio of the first catalyst substrate 40 to second catalyst substrate 45 is 45%:55%.
(28)
(29) In
(30) As can be seen from
(31) First catalyst substrate 40 and second catalyst substrate 45 may be separated from each other in housing 15, creating a mixing region 36 them. Exhaust gas passed through the first catalyst substrate may be diffused by mixing region 36 so that the exhaust gas uniformly flows toward second catalyst substrate 45.
(32) An inclined plane 15c may be formed between first accommodating section 15a and second accommodating section 15b of housing 15, and the inclined plane 15c may be formed to be inclined in response to a difference between the inner diameter of the first accommodating section 15a and the inner diameter of the second accommodating section 15b. Accordingly, the mixing region 36 may be defined by the inclined plane 15c, the rear end of first catalyst substrate 40, and the front end of the second catalyst substrate 45. As described above, mixing region 36 is configured so that one end corresponds to the radius R1 of first catalyst substrate 40 and the other end corresponds to the radius R2 of second catalyst substrate 45, and inclined plane 15c of housing 15 extends from the first accommodating section to the second accommodating section, providing stable flow of the exhaust gas between the two catalyst sections. In an example embodiment, mixing region 36 may have a length of about 20 to 30 mm.
(33) A first oxygen sensor 50 may be installed in inlet cap 12 and a second oxygen sensor 55 may be installed in mixing region 36. The first oxygen sensor 50 and the second oxygen sensor 55 may be connected to a controller 70 such as an engine management system (EMS).
(34) The amount of oxygen in the exhaust gas may be measured by first oxygen sensor 50 and second oxygen sensor 55, and the rich/lean state of the air-fuel mixture may be transmitted to controller 70 (e.g. by the output voltage of the first and second oxygen sensors 50 and 55).
(35) According to an embodiment of the present disclosure, because second oxygen sensor 55 is disposed in the mixing region 36, i.e., between the first catalyst substrate 40 and the second catalyst substrate 45, the feedback lambda control may be performed quickly according to the air-fuel mixture condition of first catalyst substrate 40. Accordingly, the emissions reduction performance may be significantly improved.
(36) Because first catalyst substrate 40 is smaller in volume than second catalyst substrate 45, the second oxygen sensor 55 may more quickly detect the oxygen storage capacity (OSC). Particularly, because the oxygen concentration for first catalyst substrate 40 is quickly detected after the fuel cut and the second catalyst substrate 45 maintains a relatively high temperature, the NOx reduction performance may be improved when the O2 purge control is applied. As described above, as the NOx reduction performance is improved, the fuel cut control may be increased, thereby improving the fuel efficiency.
(37) According to an embodiment of the present disclosure, at least one of the two or more catalyst substrates may have two or more zones coated with different amounts of catalyst by zone.
(38) Referring to
(39) According to one embodiment, first catalyst substrate 40 may include first zone 41 located in a first side of first catalyst substrate 40 and second zone 41 located in a second side of first catalyst substrate 40. First zone 41 may be disposed adjacent to inlet cap 12 of catalytic converter 10 and second zone 42 may be disposed adjacent to second catalyst substrate 45.
(40) First zone 41 may be coated with a catalyst having a high noble metal content in comparison with second zone 42. In addition, the noble metal content in second zone 42 of first catalyst substrate 40 may be higher than that in second catalyst substrate 45. That is, the noble metal content may be highest in first zone 41 of first catalyst substrate 40, lowest in second catalyst substrate 45, and in the middle in second zone 42 of first catalyst substrate 40.
(41) According to an embodiment of the present disclosure, the ratio of the noble metal content of first catalyst substrate 40 to the noble metal content of second catalyst substrate 45 may be from about 75 wt %:25 wt % to about 85 wt %:15 wt %. Preferably, the noble metal content ratio of first catalyst substrate to second catalyst substrate 45 is about 80 wt %:20 wt %.
(42) According to another embodiment of the present disclosure, the ratio of the noble metal content in each of the three catalyst regions (i.e. first zone 41 of first catalyst substrate 40, second zone 42 of first catalyst substrate 40, and second catalyst substrate 45) is about 45 wt %:25 wt %:20 wt %. and thus, it is possible to satisfy regulations such as ULEV 70 which is highly regulated.
(43) According to another embodiment of the present disclosure, the noble metal content ratio of the three zones is about 55 to 65 wt %:15 to 25 wt %:20 wt %, and thus, it is possible to satisfy regulations such as ULEV 70 which is highly regulated.
(44) According to another embodiment of the present disclosure, the noble metal content ratio of the three zones is about 60 wt %:20 wt %:20 wt %.
(45) As described above, when the content of the noble metal in first zone 41 of first catalyst substrate 40 is high, the deviation of total emissions is small, and thus the emission discharge amount may be lower than a target value.
(46) As described above, according to the present disclosure, as the noble metal content of first zone 41, second zone 42, and second catalyst substrate 45 is different, the noble metal content required for the catalytic converter may be reduced in comparison with that of the conventional catalytic converter. Accordingly, the manufacturing cost may be significantly reduced.
(47)
(48) Axis A indicates the noble metal content (wt %) of first zone 41 of first catalyst substrate 40. The noble metal content of first zone 41 increases towards a point D from a point J on the A axis.
(49) Axis B indicates the noble metal content (wt %) of second zone 42 of first catalyst substrate 40. The noble metal content of second zone 42 increases towards a point I from a point J on the B axis.
(50) The C axis indicates the noble metal content (wt %) of second catalyst substrate 45. The noble metal content of the second catalyst substrate 45 increases towards a point K from the point J on the C axis.
(51) Point J is a point where the noble metal content (wt %) of first zone 41 of first catalyst substrate 40, the noble metal content (wt %) of second zone 42 of first catalyst substrate 40, and the noble metal content (wt %) of second catalyst substrate 45 are all the lower limit values. At point J (LLL), the emission discharge amount of emission is 124% of the target value.
(52) Point D is a point where the noble metal content (wt %) of first zone 41 of first catalyst substrate 40 is the upper limit value, and the noble metal content (wt %) of second zone 42 of first catalyst substrate 40 and the noble metal content (wt %) of second catalyst substrate 45 are all the lower limit values. At point D (HLL), the emissions discharge amount is 95% of the target value.
(53) Point E is a point where the noble metal content (wt %) of first zone 41 of first catalyst substrate 40 is the upper limit value, the noble metal content (wt %) of second zone 42 of first catalyst substrate 40 is the lower limit value, and the noble metal content (wt %) of the second catalyst substrate 45 is the upper limit value. At point E (HLH), the emissions discharge amount is 87% of the target value.
(54) Point F is a point where the noble metal content (wt %) of first zone 41 of first catalyst substrate 40, the noble metal content (wt %) of second zone 42 of first catalyst substrate 40, and the noble metal content (wt %) of second catalyst substrate 45 are all the upper limit values. At point F (HHH), the emissions discharge amount is 74% of the target value.
(55) Point G is a point where the noble metal content (wt %) of first zone 41 of first catalyst substrate 40 and the noble metal content (wt %) of second zone 42 of first catalyst substrate 40 are the upper limit values, and the noble metal content (wt %) of second catalyst substrate 45 is the lower limit value. At point G (HHL), the emissions discharge amount is 74% of the target value.
(56) Point H is a point where the noble metal content (wt %) of first zone 41 of first catalyst substrate 40 is the lower limit value, and the noble metal content (wt %) of second zone 42 of first catalyst substrate 40 and the noble metal content (wt %) of second catalyst substrate 45 are the upper limit values. At point H (LHH), the emissions discharge amount is 98% of the target value.
(57) Point I is a point where the noble metal content (wt %) of first zone 41 of first catalyst substrate 40 is the lower limit value, the noble metal content (wt %) of second zone 42 of first catalyst substrate 40 is the upper limit value, and the noble metal content (wt %) of second catalyst substrate 45 is the lower limit value. At the point I (LHL), the emissions discharge amount is 101% of the target value.
(58)
(59) The catalyst may further comprise a washcoat, a noble metal, etc. According to an embodiment of the present disclosure, the noble metal of the catalyst may be selected from platinum-group metals such as palladium (Pd), platinum (Pt), rhodium (Rh), ruthenium (Ru), iridium (Ir), osmium (Os), and the like.
(60) As shown in
(61) As described above, it is possible to achieve the desired benefits of improved emissions reduction performance and correspondingly reduced emissions, compact form, and the like, by using a structure that has two or more catalyst substrates 40 and 45 having different volumes where catalytic converter 10 is installed close to the engine.
(62)
(63) Referring to
(64) Oxygen concentration of the exhaust gas passing through catalytic converter 10 may be measured by the first and second oxygen sensors 50 and 55. Based on the measured oxygen concentration, controller may determine whether the air-fuel ratio is lean (S10). As used herein, a lean air-fuel ratio means a fuel-air mixture state in which the air-fuel equivalence ratio, lambda (), is greater than 1 (>1).
(65) If the air-fuel ratio is lean at step S10, the controller 70 may perform a lambda control (S20) to adjust the air-fuel mixture ratio.
(66) When the state where the air-fuel ratio is lean, as the second catalyst substrate 45 may have a larger volume than the first catalyst substrate 40, it may have a high heat capacity, thereby improving the reduction performance of NOx, etc.
(67) After the lambda control, controller 70 may determine whether the resulting air-fuel ratio is rich (S30). If it is determined, at step S30, that the air-fuel ratio is rich, the logic of
(68) The air-fuel ratio control logic of
(69) As described above, in the state in which the air-fuel ratio is rich, the rich hydrocarbon (HC) cannot be fully purified when passing through the smaller first catalyst substrate 40 directly. However, when the air-fuel ratio is changed from the lean condition to the rich condition, as the larger second catalyst substrate 45 maintains the lean condition for a certain period of time, the rich hydrocarbon may be effectively reduced by the second catalyst substrate 45. Further, the reduction of the rich hydrocarbon may be more effectively achieved by the high temperature and large volume of the second catalyst substrate 45.
(70)
(71) Referring to
(72) If it is determined, at step S110, that the air-fuel ratio is lean, the air-fuel ratio is adjusted to a rich composition by performing an oxygen purge while terminating the fuel cut (i.e., supplying fuel) (S120).
(73) When the air-fuel ratio is lean, because the second catalyst substrate 45 has a larger volume than the first catalyst substrate 40, it has a higher heat capacity, thereby improving the reduction performance of NOx, etc.
(74) After the termination of the fuel cut and the O2 purge (S120), controller 70 again determines whether the air-fuel ratio is rich (S130).
(75) If it is determined, at step S130, that the air-fuel ratio is rich, the process proceeds to step S10 of
(76) When the air-fuel ratio is rich, the rich hydrocarbon (HC) cannot be fully purified when passing through the smaller first catalyst substrate 40 directly. However, when the air-fuel ratio is changed from the lean condition to the rich condition, because the larger second catalyst substrate 45 maintains the lean condition for a certain period of time, the rich hydrocarbon may be effectively reduced by the second catalyst substrate 45. Further, the reduction of the rich hydrocarbon may be more effectively achieved by the high temperature and large volume of the second catalyst substrate 45.
(77) If it is determined, at step S130, that the air-fuel ratio is lean, the termination of the fuel cut and the performing of O2 purge (S120) is repeated.
(78) By applying the exhaust gas emissions reduction control method using the improved catalytic converter 10 according to the present disclosure as described above, it is possible to significantly reduce the time needed to reach catalyst LOT and improve the emissions reduction performance in the T-GDI engine. It is also possible not only to reduce the amount of noble metal needed in the catalyst, but also to significantly reduce total emissions.
(79) Hereinabove, although the present disclosure has been described with reference to example embodiments and the accompanying drawings, the present disclosure is not limited thereto, but may be variously modified and altered by those skilled in the art to which the present disclosure pertains without departing from the spirit and scope of the present disclosure claimed in the following claims.