| ²é¿´: 446 | »Ø¸´: 1 | ||
hellen7256ľ³æ (СÓÐÃûÆø)
|
[ÇóÖú]
Çó¸ßÊÖ°ïæ·Ò룬ÖÐÒëÓ¢
|
|
1. ¾¹ýÒÔÉÏ·ÖÎöµÃÖª£¬×ÔÖ§³ÅNaA·Ö×ÓɸĤÓÃÓÚÉøÍ¸Æû»¯¹ý³ÌÍÑË®µÄ×î¼Ñ½øÁÏ×é³ÉΪÕáÌÇ/Ë®(15/85 wt%)¡£ 2.¾¹ýÒÔÉÏ·ÖÎöµÃÖª£¬×ÔÖ§³ÅNaA·Ö×ÓɸĤÓÃÓÚÉøÍ¸Æû»¯¹ý³ÌÍÑË®£¬ÔÚÏàͬµÄ½øÁÏ×é³ÉÏ£¨¼´½øÁÏÈÜÒºÖÐÕáÌÇŨ¶ÈΪ15wt%£©Ëæ×ŽøÁÏζȵÄÉý¸ß£¬ÉøÍ¸Æû»¯¹ý³ÌµÄͨÁ¿¡¢·ÖÀëÒò×Ó¡¢·ÖÀëÖ¸ÊýPSI¶¼Ôö´ó¡£ 3.ÉøÍ¸Æû»¯ÊµÑé×°ÖÃʾÒâͼ |
» ²ÂÄãϲ»¶
һ־Ը̫ÔÀí¹¤°²È«¹¤³Ì300·Ö£¬Çóµ÷¼Á
ÒѾÓÐ5È˻ظ´
µ÷¼ÁÇóԺУÕÐÊÕ
ÒѾÓÐ4È˻ظ´
Çó»¯Ñ§µ÷¼Á
ÒѾÓÐ4È˻ظ´
085600£¬²ÄÁÏÓ뻯¹¤321·ÖÇóµ÷¼Á
ÒѾÓÐ7È˻ظ´
Ò»Ö¾Ô¸Î人Àí¹¤£¬×Ü·Ö321£¬Ó¢Ò»Êý¶þ£¬ÇóÀÏʦÊÕÁô¡£
ÒѾÓÐ6È˻ظ´
¿¼Ñе÷¼Á
ÒѾÓÐ6È˻ظ´
0856Çóµ÷¼Á
ÒѾÓÐ12È˻ظ´
0703»¯Ñ§
ÒѾÓÐ9È˻ظ´
0703»¯Ñ§Çóµ÷¼Á
ÒѾÓÐ10È˻ظ´
317Çóµ÷¼Á
ÒѾÓÐ6È˻ظ´
¸ßÑÒ¸ßÒô
ľ³æ (Ö°Òµ×÷¼Ò)
- ·ÒëEPI: 25
- Ó¦Öú: 2 (Ó×¶ùÔ°)
- ½ð±Ò: 2922
- É¢½ð: 325
- ºì»¨: 19
- Ìû×Ó: 3047
- ÔÚÏß: 251.5Сʱ
- ³æºÅ: 2253067
- ×¢²á: 2013-01-21
- ÐÔ±ð: MM
- רҵ: Ò©Îﻯѧ
¡¾´ð°¸¡¿Ó¦Öú»ØÌû
¡ï ¡ï ¡ï ¡ï ¡ï ¡ï
RXMCDM: ½ð±Ò+1, ¶àлӦÖú£¡ 2014-07-04 08:06:14
hellen7256(ÕæÇ¿±ØÊ¤´ú·¢): ½ð±Ò+5 2014-07-25 12:59:28
RXMCDM: ½ð±Ò+1, ¶àлӦÖú£¡ 2014-07-04 08:06:14
hellen7256(ÕæÇ¿±ØÊ¤´ú·¢): ½ð±Ò+5 2014-07-25 12:59:28
|
1£¬After the above analysis that the self-supporting NaA zeolite membranes for pervaporation dehydration optimum feed composition is sucrose / water (15/85 wt%). 2,After the above analysis that in the process of the self-supporting NaA zeolite membranes for pervaporation dehydration ,in the same feed composition (i.e., the sucrose concentration in the feed solution of 15wt%) as the feed temperature, the vaporization of the permeate flux, separation factor , PSI separation index are increased. 3,The experimental setup of penetration. ![]() |

2Â¥2014-07-02 14:22:36














»Ø¸´´ËÂ¥