我以前也是挺着急性别的，就买了盒intelligender测试下，本来也就是让老婆没那么焦虑的，后来B超的结果也一致，还挺准的。 intelligender真正国外的注册产品。

卵泡期，我也高，12.01，无奈，医生说如果和LH比例不大于2就没多大关系

France IFP CCR ??a second-generation technologies more 80934kwh12I. 40 cycles Chengyuan ∞ 5lo4m87.78 Wan t4.39 fuel gas per A3 ∞ Park x1O336 [10. Suo ...Yan ugly steam per l5-I 5 [1 ship Wan tI5.44 catalytic Jing & a 235-6I_15 ten thousand yuan of 90 A units. I6 Based on the above results, the use of second-generation technology solutions and first-generation technology A, B program, compared with the entire small investment (investment by Norwegian 3s2 million, 1.9% of total investment), your operating costs annual increase of 901,600 yuan, but the annual increase of 11.148 million yuan output value, profits and taxes of the annual Taiwan increased by nearly 10 million, is economically beneficial. IFP second-generation technology in addition to CCR regenerator structure is more complex , the other with the same first generation, and has been simplified,ghd piastra, so the color will not affect the degree of localization. However, due to the new second-generation technology is developed, we have not mastered, such as deciding on the purchase of the patent's basic design, by the domestic work are responsible for all engineering design is understood, first and second generation patents is expensive the same, basic design needs to spend more to buy some foreign exchange, but because of the introduction of a special valve to reduce the amount of the need for additional external i [small, compared with the first generation about (the switch 8). 8. Kin-billion restructuring of communications 19SO response system in people, too light naphtha hydrotreating first vertical and then into the reaction system. Heavy naphtha catalytic reaction conditions similar to the firefly whole, but slightly higher temperature and pressure slightly lower. Population of each reactor temperature is 500-600 ℃, reaction pressure is 0_3 ~ O. 7MPaCgl liquid space velocity is 0. S- 2.0 h. Z-Forming of aromatics with reaction severity slaughter capacity increased and improved, but costs also increased. For example, the reaction pressure is low by the heat required for the reaction speed can be increased or low-aromatic products, but the equipment investment and utility costs. Thus, there are two options: Option 1 is the low investment program, investment and public works equipment cost control must, aromatics yield slightly lower; Option 2 is a high aromatics yield program, exhaust gas recirculation increased aromatics yield, plant investment and utility costs. Three different materials, such as the yield of aromatics listed in Table 5. Table 5 Lan different branches of aromatic raw materials of light stone and dried grass by the butane C i pull program I212l2 aromatics production Zhuo, weight% 6OD63 .156.25 are Bo of the aromatics BTX,moncler outlet, weight% 589j81L989.78I. O892 data can be seen from Table 5, aromatics production slaughter (busy for fresh material) about 5O-60% (weight) of the smell,dsquared sito ufficiale, according to the light naphtha 'butane, propane's lower order. Scenario 2 and l difference between about 3-4%. Solution l of the aromatics BD (about 8O%, Scenario 2 is about 90%, the remaining 10 to 20% of c, more aromatics in the BTX is the main component of toluene, about 50% light naphtha Z-Forming the product yield and heavy naphtha catalyst, the former products are more benzene and toluene, c6 few more non-aromatic, more emissions. processing capacity of 8600t / a ( 200 barrels / working days) of the Industrial test equipment built in Japan, Kawasaki, Mitsubishi Oil refinery, the raw material is light naphtha and butane, the reaction system consists of two groups of two reactors in series form,christian louboutin italia, began operations in 1991, l1 months, the end of trial operation in December, confirmed a catalyst and process performance are good. New processing capacity of 430,000 t / a (10000 barrels / day to start) and plant (1991, Japan), with a light naphtha as raw materials , investment $ 73 million; butane as raw materials. invest $ 69 million. BTx fractionation system, plus a total investment of $ 85 million. utility consumption higher than the heavy naphtha catalytic reforming. Scenario 2 Compared with Scenario 1, the investment increase of 20 - 30% public works costs increased by about 30% with propane as the raw material of plant investment and utility costs and butane as the raw material of similar (on the next page] 2l increase the amount of $ 320,000 foreign exchange, accounting for 5.1% of the total foreign exchange is currently the world's using FP technology of catalytic reforming unit has more than 90 sets, IFP developed second-generation technology as continuous reforming process simplified, easy to operate, safe, reliable, easy maintenance, royalties and technology package price and the first generation of computing technology, 12 months, has sold 12 units at the patent, three already in operation,puma scarpe, nine sets under construction. In addition to Italy, South Africa, India, Venezuela and other traditional markets have got the project , Texas, USA also has a second-generation device uses a IF'P patented technology, patented as IFP rapid development of our proposed continuous reforming unit select the same patented technology has a strong appeal.