Mixed entanglement distillation by means of parity measurements

We present a mixed entanglement distillation protocol by means of the parity measurement of qubits. Without the use of controlled-NOT (CNOT) operations, the efficiency of our protocol can approach that of the CNOT protocol. In comparison, the total successful probability of our protocol can reach a quantity twice as large as that of the linear optics-based protocol.

Preparation and properties of microporous membrane from poly(vinylidene fluoride-co-tetrafluoroethylene) (F2.4) for membrane distillation

Flat-sheet microporous membranes from F2.4 for membrane distillation (MD) were prepared by phase inversion process. Dimethylacetamide (DMAC) and LiClO(4)(.)3H(2)O/trimethyl phosphate (TMP) were, respectively, used as solvent and pore-forming additives. The effects of casting solution composition, exposure time prior to coagulation and temperature of precipitation bath on F2.4 membrane structure were investigated. The morphology of resultant porous membrane was observed by scanning electron microcopy. Some natures of F2.4 porous membrane after drying in air, such as mechanical properties and hydrophobicity, were exhibited and compared with poly(vinylidene fluoride) (PVDF) membrane prepared by the same ways. Stress-at-break and strength stress of F2.4 microporous membrane are higher than that of PVDF membrane, and elongation percentage of F2.4 membrane at break is about eight-fold as great as that of PVDF membrane. Contact angle of F2.4 microporous membrane to water (86.6 +/- 0.51degrees) was also larger than that of PVDF mernbrane (80.0 +/- 0.78degrees). MD experiment was carried out using a direct contact membrane distillation (DCMD) configuration as final test to permeate performance of resultant microporous membrane.

Preliminary research on microporous membrane from F2.4 for membrane distillation

An asymmetric hydrophobic microporous membrane from the copolymer of tetrafluoroethylene and vinyliden fluoride (F2.4) has been fabricated by phase inversion process. Some characteristics, such as mechanical properties and hydrophobicity, have been examined and compared with polyvinylidenefluoride (PVDF) membrane. Experimental data exhibit F2.4 membrane excellent mechanical properties and hydrophobicity. F2.4 microporous membrane was approximately 6-8 times as high as PVDF membrane in stretching strain and extension ratio at break, and contact angle to distilled water of the fore (88.5degrees) was larger than the latter (80.0degrees), too. The results from membrane distillation (MD) process were well agreed with the fundamental laws of membrane distillation.

SURFACE-MODIFIED HYDROPHILIC MEMBRANES IN MEMBRANE DISTILLATION

The porosity and the hydrophobicity of membranes are two essential requirements for membrane distillation (MD) of aqueous solutions. So far, the hydrophobic porous membranes used in MD studies have been prepared from hydrophobic materials. In this work, hydrophilic cellulose acetate and cellulose nitrate membranes were modified into hydrophobic membranes by radiation grafting polymerization and plasma polymerization, and used in MD studies successfully. The results indicated that modified membranes with good performance in MD can be obtained if the modifying conditions are controlled appropriately. Especially plasma polymerization, in which many particular kinds of monomer could be polymerized onto the surface of porous materials, has become an efficient method to prepare hydrophobic porous membrane with high performance from hydrophilic membranes. It will stimulate the development and practical application of MD.

PLASMA POLYMERIZATION OF OCTAFLUOROCYCLOBUTANE AND HYDROPHOBIC MICROPOROUS COMPOSITE MEMBRANES FOR MEMBRANE DISTILLATION

In this paper, hydrophilic microporous cellulose nitrate membranes have been surface-modified by plasma polymerization of octafluorocyclobutane (OFCB). The microporous composite membranes with a hydrophilic layer sandwiched between two hydrophobic layers have been obtained. The obtained composite membranes have been used in a membrane distillation (MD) process and have exhibited good performance. The effects of polymerization conditions, such as glow-discharge power and deposition time, on the structures and MD performances of the obtained composite membranes have been investigated by SEM, X-ray microscopical analysis, and XPS. The polymerization conditions should be as mild as possible in order to prepare the hydrophobic composite membrane with good MD performance. The typical MD behaviors of the obtained hydrophobic composite membranes are in agreement with that of hydrophobic membranes directly prepared from hydrophobic polymeric materials, like PVDF, PTFE, or PP.

AN EXPERIMENTAL-STUDY ON MEMBRANE DISTILLATION CRYSTALLIZATION FOR TREATING WASTE-WATER IN TAURINE PRODUCTION

The solution of non-volatile solutes can be concentrated to saturation by membrane distillation. If the solute is easy to crystalize, the membrane distillation-crystallization phenomenon will appear during the membrane distillation of saturated solutions. It is possible that crystalline products are separated from concentrated solutions by a membrane process. In this work the PVDF capillary membrane, which was improved on hydrophobicity by using LiCl instead of a water-soluble polymer as an additive, has been used for treating the waste water of taurine. The crystalline product has been obtained from the waste water by the membrane distillation-crystallization technique. The results have shown good prospects for a membrane distillation application for treatment of industrial waste water.

AN EXPERIMENTAL-STUDY ON MEMBRANE DISTILLATION FOR TREATMENT OF GINSENG DEW AND GINSENG WASHING WATER

Membrane distillation is a new membrane separation process which has been developed in the last few years. When a piece of microporous hydrophobic membrane separates two kinds of aqueous solutions different in temperature, the solutions cannot transport through the pores of membrane in any directions because of the hydrophobicity of membrane. However, vapor can readily penetrate through the

内蒙古草原中生物土壤结皮生态学研究

1. 生物土壤结皮是干旱半干旱生态系统中的重要组成部分，它可通过增加土壤肥力和稳定性、影响水分再分配和植物萌发、成活、生长和繁殖而对生态系统结构和功能产生重要影响。为阐明生物结皮在内蒙古草地中的作用，本报告对两个草地生态系统进行了为期三年的调查，对生物结皮的氮素输入、对放牧的响应及其与植物的关系进行了综合研究。 2. 利用乙炔还原法，本研究对内蒙古退化草地中的生物土壤结皮中的蓝藻、地衣和地耳的氮素输入进行了为期30个月的连续测定。研究发现：1) 生物结皮固氮活性主要集中于5-10月，呈单峰型曲线，表明生物土壤结皮的固氮作用主要受温度和降雨影响;2) 生物结皮年固氮量为12.99-129.9 kg N•ha-1，98%的氮素固定于6-9月份;3) 按固氮量排序，蓝藻 (61%) > 地衣 (33%) > 地耳 (6%)，表明物种组成和丰度对生物结皮的氮素输入具重要影响。生物结皮的固氮量和季节变化表明生物结皮可以是影响退化草地中植物生长和促进退化草地恢复的重要影响因子。 3. 本研究选择三个放牧处理（长期放牧、短期围封和近期放牧）对生物结皮固氮活性进行了为期3年的研究。结果表明，与短期围封相比，长期放牧造成生物土壤结皮固氮活性下降了99.5%。固氮活性在放牧时间不足11个月时即可下降至最低水平，因此，放牧持续时间短于4个月的轮牧可能有利于生物土壤结皮的固氮。 4. 本研究选择6个放牧梯度（对照：0.00 羊/公顷, 极轻度放牧：1.33羊/公顷，轻度放牧：2.67羊/公顷，中度放牧：4.00羊/公顷，重度放牧：5.33羊/公顷，极重度放牧：6.67羊/公顷)，研究放牧强度对于生物结皮丰度、物种组成和固氮输入的影响。不同放牧强度对生物结皮丰度、物种组成和固氮输入具有重要影响，表明长期放牧可抑制生物土壤结皮在氮素输入和土壤固定方面的作用。极轻度放牧对生物土壤结皮影响不大;轻度放牧造成氮素输入降低了50%;重度和极重度放牧造成氮素输入降低了90%，并可使移动性较强的物种成为生物土壤结皮的优势组分，从而可抑制其土壤固定作用。因此，极轻度和轻度放牧是有利于生物土壤结皮固氮和固定土壤的草地利用方式。 5. 在处于恢复早期的一个退化草地中，我们对生物结皮和植物之间的关系进行了为期2年的研究。结果表明，生物结皮的丰度和物种组成与植物地上生物量和盖度高度相关。生物结皮丰度和氮素输入随植物生物量和盖度下降。结果还表明生物结皮是退化草地的主要氮素输入来源，尤其是在草地恢复初期。植物组织δ15N 低于土壤，这种差异随植物生产力增高而减小，表明生物结皮所固定氮素首先被植物利用，而后返回土壤。生物结皮的固氮输入变化可能是这种变化模式的主要原因，在分解作用和氮素损失中的同位素分馏，以及菌根真菌对于氮素的转运可能也是这种变化模式的原因。结果还显示生物土壤结皮与植物之间可能存在负反馈关系。这种自我调节的反馈过程可能是影响退化草地生态系统生产力和氮素循环的重要调节机制。

Production and characterization of biodiesel from tung oil

The feasibility of biodiesel production from tung oil was investigated. The esterification reaction of the free fatty acids of tung oil was performed using Amberlyst-15. Optimal molar ratio of methanol to oil was determined to be 7.5:1, and Amberlyst-15 was 20.8wt% of oil by response surface methodology. Under these reaction conditions, the acid value of tung oil was reduced to 0.72mg KOH/g. In the range of the molar equivalents of methanol to oil under 5, the esterification was strongly affected by the amount of methanol but not the catalyst. When the molar ratio of methanol to oil was 4.1:1 and Amberlyst-15 was 29.8wt% of the oil, the acid value decreased to 0.85mg KOH/g. After the transesterification reaction of pretreated tung oil, the purity of tung biodiesel was 90.2wt%. The high viscosity of crude tung oil decreased to 9.8mm(2)/s at 40 degrees C. Because of the presence of eleostearic acid, which is a main component of tung oil, the oxidation stability as determined by the Rancimat method was very low, 0.5h, but the cold filter plugging point, -11 degrees C, was good. The distillation process did not improve the fatty acid methyl ester content and the viscosity.

Production of biodiesel from soapstock using an ion-exchange resin catalyst

The feasibility of biodiesel production from soapstock containing high water content and fatty matters by a solid acid catalyst was investigated. Soapstock was converted to high-acid acid oil (HAAO) by the hydrolysis by KOH and the acidulation by sulfuric acid. The acid value of soapstock-HAAO increased to 199.1 mg KOH/g but a large amount of potassium sulfate was produced. To resolve the formation of potassium sulfate, acid oil was extracted from soapstock and was converted to HAAO by using sodium dodecyl benzene sulfonate (SDBS). The maximum acid value of acid oil-HAAO was 194.2 mg KOH/g when the mass ratio of acid oil, sulfuric acid, and water was 10:4:10 at 2% of SDBS. In the esterification of HAAO using Amberylst-15, fatty acid methyl ester (FAME) concentration was 91.7 and 81.3% for soapstock and acid oil, respectively. After the distillation, FAME concentration became 98.1% and 96.7% for soapstock and acid oil. The distillation process decreased the total glycerin and the acid value of FAME produced a little.

Optimization of biodiesel production from trap grease via acid catalysis

As a kind of waste collected from restaurants, trap grease is a chemically challenging feedstock for biodiesel production for its high free fatty acid (FFA) content. A central composite design was used to evaluate the effect of methanol quantity, acid concentration and reaction time on the synthesis of biodiesel from the trap grease with 50% free fatty acid, while the reaction temperature was selected at 95 degrees C. Using response surface methodology, a quadratic polynomial equation was obtained for ester content by multiple regression analysis. Verification experiments confirmed the validity of the predicted model. To achieve the highest ester content of crude biodiesel (89.67%), the critical values of the three variables were 35.00 (methanol-to-oil molar ratio), 11.27 wt% (catalyst concentration based on trap grease) and 4.59 h (reaction time). The crude biodiesel could be purified by a second distillation to meet the requirement of biodiesel specification of Korea.

Novel biodiesel production technology from soybean soapstock

This paper describes an attractive method to make biodiesel from soybean soapstock (SS). A novel recovery technology of acid oil (AO) from SS has been developed with only sulfuric acid solution under the ambient temperature (25 +/- 2 degrees C). After drying, AO contained 50.0% FFA, 15.5% TAG 6.9% DAG 3.1% MAG 0.8% water and other inert materials. The recovery yield of AO was about 97% (w/w) based on the total fatty acids of the SS. The acid oil could be directly converted into biodiesel at 95 degrees C in a pressurized reactor within 5 hours. Optimal esterification conditions were determined to be a weight ratio of 1 : 1.5 : 0.1 of AO/methanol/sulfuric acid. Higher reaction temperature helps to shorten the reaction time and requires less catalyst and methanol. Ester content of the biodiesel derived from AO through one-step acid catalyzed reaction is around 92%. After distillation, the purity of the biodiesel produced from AO is 97.6% which meets the Biodiesel Specification of Korea. The yield of purified biodiesel was 94% (w/w) based on the total fatty acids of the soapstock.