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sweetening相关的网络例句

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与 sweetening 相关的网络例句 [注:此内容来源于网络,仅供参考]

Depending on the sugar content of the liquor you choose, you can use more or less than the stated half-shot of sugar syrup: an amaretto sour, based on the amaretto liqueur (minimum 100 grams of sugar per liter) will clearly require less than a half-shot of sugar syrup, whereas a rye whisky sour may require more sweetening.

根据不同的含糖量的酒,您可以使用多于或少于规定的一半拍摄的糖浆:一份杏仁酸,基于杏仁利口酒(每公升最低100克糖)显然将需要至少半盎司的糖浆,而黑麦威士忌酸可能需要更多的甜味剂。

The coal gas dry process desulphurization technology application early, most early applies in the coal gas dry process desulphurization technology is take the bog ore as the sweetening agent ferric oxide desulphurization technology, afterwards, studies successful and the production cost along with the coal gas desulphurization activated charcoal reduces relatively, the activated charcoal desulphurization technology also starts widely to apply.

煤气干法脱硫技术应用较早,最早应用于煤气的干法脱硫技术是以沼铁矿为脱硫剂的氧化铁脱硫技术,之后,随着煤气脱硫活性炭的研究成功及其生产成本的相对降低,活性炭脱硫技术也开始被广泛应用。

Uses most early the ferric oxide sweetening agent for the bog ore and the artificial ferric oxide, for increases its factor of porosity, the sweetening agent take the sawdust as the stopping, again sprays the right amount water and the few white lime, sun-dries repeatedly makes, its PH value is generally about 8-9, this kind of sweetening agent desulphurization efficiency is low, must outside the tower regenerate, the regeneration difficulty, then is substituted for soon by other sweetening agents.

最早使用的氧化铁脱硫剂为沼铁矿和人工氧化铁,为增加其孔隙率,脱硫剂以木屑为填充料,再喷洒适量的水和少量熟石灰,反复翻晒制成,其PH值一般为8-9左右,该种脱硫剂脱硫效率较低,必须塔外再生,再生困难,不久便被其他脱硫剂所取代。

Both static and dynamic tests showed that the sweetening of the LY-02 cocoanut charcoal was more superior to both coal and common cocoanut charcoals.

静态及动态试验结果表明,其脱臭性能明显优于煤质活性炭和普通椰壳活性炭。

Accordingly, as catalyst of light oil sweetening,the binuclear cobalt sulfonate phthalocyanine was selected in this paper. Due to the double active centers in a plane, bi-CoSPc not only increases the solubility in alkaline, but also avoids its dimerisation, which expects to increase the catalyst activity in sweetening process.

为此,本文选用双核酞菁钴磺酸盐作为轻质油品脱臭催化剂,该催化剂具有平面双核的分子结构,这不仅增加了其在碱液中的溶解度,同时也减弱了二氧加合物的形成趋势,有望在轻质油品催化氧化脱臭工艺中具有更高的催化活性和使用寿命。

The results showed that Weipa ore is gibbsite and its leaching efficiency is high when digested at higher than 200 ℃,so applicable to sweetening ore in digestion process,under conditions that the sweetening process is controlled in the range of 195~200 ℃ for 15~20 min and the dosage of Weipa .

对澳大利亚韦帕矿的溶出性能及以韦帕矿为后加矿的增溶溶出技术进行了实验研究。考察了增溶温度,增溶时间,后加矿加入量对溶出效果的影响,同时对后加矿增溶溶出的矿浆性能进行了对比性研究。结果表明:韦帕矿为三水铝石矿,在200℃以上溶出时,浸出率较高,适宜作为增溶溶出过程的后加矿。以韦帕矿为后加矿,其适宜的增溶溶出条件为:增溶温度195~200℃,增溶时间15~20 min,后加矿的质量分数为15%~20%。后加矿增溶溶出矿浆具有优良的沉降压缩性能

So find out which arouse sweetening solution foam reason is one of the problems that natural gas sweetening in the present stage.

因此找到引起脱硫溶液发泡的原因,并以一定的处理手段降低这些物质在脱硫溶液中的含量,是天然气脱硫工艺急需解决的问题之一。

The desulfurizers (cyclobutyl sulfone and diisopropanolamine) have poisonousness. If the sweetening solution foamed seriously that can't be used, sweetening solution's discharge will affect environment.

脱硫溶液严重发泡后将不能再使用,且脱硫溶剂环丁砜和二异丙醇胺都具有毒性,脱硫溶液的排放将会对环境安全造成严重地影响。

No 2 combined workshop of Yulin refinery under Shaanxi Yanchang Petroleum Company Limited adopts semi-regenerated active carbon fixed bed process for its gasoline sweetening process, because of unadvanced technology limited treatment capacity, big consumption of caustic, as well as being unable to satisfy production requirements. In the light of above, Yulin Refinery built up a new gasoline sweetening unit with treatment capacity of 45t/h in 2007, the unit adopts patented fiberfilm contactor gasoline sweetening technology from Merichem company in USA.

陕西延长石油有限责任公司榆林炼油厂联合二车间催化旧汽油脱硫醇装置采用的是半再生活性炭固定床工艺,由于工艺技术落后,处理量小,消耗碱量大,产生的碱渣无法处理、不能满足生产等制约因素,榆林炼油厂于2007年新建一套汽油脱硫醇装置,处理量为45t/h,该装置引进美国Merichem公司金属纤维膜接触器脱硫技术。

Recently the consumption structure of the sweetening agent has taken place great changes and the market demands are growing rapidly. Meanwhile, the domestic export quantities and the demands from the fruit sweetener and medicinal preparation for the sweetening agents keep growing tendency. It is estimated that in the next few years the demands of the sodium cyclamate for the cyclohexylamine will keep a speed of 8-10% per year and the cyclohexylamine consumed by the sodium cyclamate will be 14-15 thousand tons.

近年来国内甜味剂消费结构发生较大变化,甜蜜素市场需求增长迅速,同时国内产品出口保持稳定增长态势,此外在水果甜剂、药物制剂等方面对甜蜜素的需求也呈现较快增长势头,预计未来几年甜蜜素对环己胺的需求将保持年均8%-10%的增速,2010年甜蜜素生产约消耗环己胺1.4万-1.5万吨。

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