| ²é¿´: 1310 | »Ø¸´: 3 | |||
| ¡¾ÐüÉͽð±Ò¡¿»Ø´ð±¾ÌûÎÊÌ⣬×÷ÕßKK0709½«ÔùËÍÄú 5 ¸ö½ð±Ò | |||
KK0709ͳæ (СÓÐÃûÆø)
|
[ÇóÖú]
Çë¸÷λ´óÉñ¿´Ò»ÏÂÕâÊôÓÚendnoteÖеÄÄÄÖÖ¸ñʽ£¬²»ÖªµÀ¸ÃÌí¼ÓÄÄÒ»ÖÖÁË ÒÑÓÐ1È˲ÎÓë
|
||
|
ÕýÎÄÖÐÊÇÕâÑùµÄ¡±Catalyst degradation is due to platinum agglomeration and oxidation. Sustained degradation reduces the available catalyst surface in the anode and cathode, leading to power loss [22, 23]¡° ¡±The PEMFC system model is based on the semiempirical generalized steady-state electrochemical model (GSSEM) that can reliably predict the performance of a PEMFC system [24¨C26]. ¡° ²Î¿¼ÎÄÏ×ÊÇÕâÑùµÄ¸ñʽ [24] J. C. Amphlett, R. M. Baumert, R. F. Mann, B. A. Peppley, P. R. Roberge, and T. J. Harris, ¡°Performance Modeling of the Ballard Mark IV Solid Polymer Electrolyte Fuel Cell: I. Mechanistic Model Development,¡±Sample Text142, no. 1 (1995): 1¨C8. [25] R. F. Mann, J. C. Amphlett, M. A. I. Hooper, H. M. Jensen, B. A. Peppley, and P. R. Roberge, ¡°Development and Application of a Generalised Steady-State Electrochemical Model for a PEM Fuel Cell,¡± Journal of Power Sources 86, no. 1-2 (2000): 173¨C180.ÆäÖÐÆÚ¿¯ÃûÊÇбÌåµÄ |
» ±¾ÌûÒÑ»ñµÃµÄºì»¨£¨×îÐÂ10¶ä£©
» ²ÂÄãϲ»¶
Ò»Ö¾Ô¸ÎäÀí085500»úеרҵ×Ü·Ö300Çóµ÷¼Á
ÒѾÓÐ6È˻ظ´
²ÄÁÏѧÇóµ÷¼Á
ÒѾÓÐ5È˻ظ´
¿¼Ñе÷¼Á
ÒѾÓÐ4È˻ظ´
281Çóµ÷¼Á
ÒѾÓÐ4È˻ظ´
0805 316Çóµ÷¼Á
ÒѾÓÐ6È˻ظ´
085601Çóµ÷¼Á×Ü·Ö293Ó¢Ò»Êý¶þ
ÒѾÓÐ3È˻ظ´
08¹¤Ñ§µ÷¼Á
ÒѾÓÐ17È˻ظ´
340Çóµ÷¼Á
ÒѾÓÐ4È˻ظ´
311Çóµ÷¼Á
ÒѾÓÐ3È˻ظ´
ʳƷר˶ һ־Ը˫һÁ÷ 328
ÒѾÓÐ4È˻ظ´

2Â¥2024-12-24 23:34:10
sylviamusic
гæ (³õÈëÎÄ̳)
- Ó¦Öú: 0 (Ó×¶ùÔ°)
- ½ð±Ò: 88
- Ìû×Ó: 2
- ÔÚÏß: 8.1Сʱ
- ³æºÅ: 25477808
- ×¢²á: 2021-02-28
- רҵ: ¼ÆËã»úÈí¼þ
| ±È½ÏÏñChicago Manual of Style 17th edition£¬µ«ÒýÓõÄʱºòÐèÒª×Ô¼º¸Ä³Énumeric citation |
3Â¥2024-12-25 17:14:55
nono2009
³¬¼¶°æÖ÷ (ÎÄѧ̩¶·)
No gains, no pains.
-

ר¼Ò¾Ñé: +21105 - SEPI: 10
- Ó¦Öú: 28684 (Ժʿ)
- ¹ó±ö: 513.911
- ½ð±Ò: 2555230
- É¢½ð: 27828
- ºì»¨: 2148
- ɳ·¢: 66666
- Ìû×Ó: 1602255
- ÔÚÏß: 65200.9Сʱ
- ³æºÅ: 827383
- ×¢²á: 2009-08-13
- ÐÔ±ð: GG
- רҵ: ¹¤³ÌÈÈÎïÀíÓëÄÜÔ´ÀûÓÃ
- ¹ÜϽ: ¿ÆÑмҳﱸίԱ»á
4Â¥2024-12-26 04:50:14













»Ø¸´´ËÂ¥
ÐǼÊÕ½»ú