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A method for removing Total dissolved solids (TDS) from the waste water Tanneries

机译:从废水制革厂中去除总溶解固体(TDS)的方法

摘要

1. bacterial strain with number u0434u0435u043fu043eu043du0438u0440u043eu0432u0430u043du0438u00a0 u043cu0442u0441u0441 5097 fit u0434u043bu00a0 u0443u043cu0435u043du044cu0448u0435u043du0438u00a0 u0441u043eu0434u0435u0440u0436u0430u043du0438u00a0 summary of solutes (TDS) as in the rough, and el u043au0442u0440u043eu0444u043bu043eu0442u0438u0440u043eu0432u0430u043du043du044bu0445 wastewater leather factories.;2. method u043fu0440u0438u0433u043eu0442u043eu0432u043bu0435u043du0438u00a0 u0438u043du043eu043au0443u043bu00a0u0442u0430 strain on 1 u0434u043bu00a0 u0443u043cu0435u043du044cu0448u0435u043du0438u00a0 u0441u043eu0434u0435u0440u0436u0430u043du0438u00a0 summary of solutes (TDS) as in the rough, and u044du043bu0435u043au0442u0440u043eu0444u043bu043eu0442u0438u0440u043eu0432u0430u043du043du044bu0445 u0441u0442u043eu0447 for the waters of leather factories, which comprises the following steps:;(a) isolating the strain;(b) cultivation of the strain on the nutritional environment with u0430u0433u0430u0440u043eu043c containing soil extract and nutrient agar, to u043fu043eu043bu0443u0447u0435u043du0438u00a0 pure culture;(c) u0438u043du043eu043au0443u043bu00a0u0446u0438u044e strain in a nutrient broth to u043fu043eu043bu0443u0447u0435u043du0438u00a0 breed;(d) u0438u043du043au0443u0431u0430u0446u0438u044e starter with approximately 37u0441 for approximately 16 to 18 hours in u043fu0435u0440u0435u043cu0435u0448u0438u0432u0430u043du0438u0438 preferably with a speed of 100 rpm.;(e) u0438u043du043eu043au0443u043bu00a0u0446u0438u044e nutritious broth u0437u0430u043au0432u0430u0441u043au043eu0439 until u043eu043fu0442u0438u0447u0435u0441u043au0430u00a0 density culture reaches u0437u043du0430u0447u0435u043du0438u00a0 1.0;(f) the collection of cells from the culture with a view to u043fu043eu043bu0443u0447u0435u043du0438u00a0 residue.;(g) irrigation sediment by u0440u0430u0441u0442u0432u043eu0440u0435u043du0438u00a0 in 0,05u043c u0444u043eu0441u0444u0430u0442u043du043eu043c buffer, ph 6.8.;(h) centrifugation to u043fu043eu043bu0443u0447u0435u043du0438u00a0 u043fu0440u043eu043cu044bu0442u043eu0433u043e residue.;(i) dissolving u043fu0440u043eu043cu044bu0442u043eu0433u043e residue in the minimum number of wastewater;(j) homogenization dissolved residue to u043fu043eu043bu0443u0447u0435u043du0438u00a0 fraction of cells capable of reducing the level of total dissolved solids (TDS) in wastewater from leather u0430u0432u043eu0434u043eu0432.;3. method for 2, where the strain on the environment u0432u044bu0440u0430u0449u0438u0432u0430u0435u0442u0441u00a0 u0430u0433u0430u0440u043eu043c in approximately 372u0441 during about 16 to 24 hours.;4. method for 2, where the nutrient broth contains about 5.0 g u043fu0435u043fu0441u0438u043du043eu0432u043eu0433u043e u043fu0435u0440u0435u0432u0430u0440u0430 animal tissue, about 5.0 g of chloride u043du0430u0442u0440u0438u00a0, about 1.5 g u043cu00a0u0441u043du043eu0433u043e of about 1.5 g u0434u0440u043eu0436 u0436u0435u0432u043eu0433u043e extract and about 0.2 ml of tween 80.;5. method for 2, where u043au043eu043du0435u0447u043du0430u00a0 culture u0446u0435u043du0442u0440u0438u0444u0443u0433u0438u0440u0443u0435u0442u0441u00a0 at 6000 rpm with a time of about 20 min at approximately 4.;6. method for 2, where the sludge u043fu0440u043eu043cu044bu0432u0430u0435u0442u0441u00a0 through his u0440u0430u0441u0442u0432u043eu0440u0435u043du0438u00a0 in 0.05 m u0444u043eu0441u0444u0430u0442u043du043eu043c buffer with a ph of 6.8.;7. u0430u044du0440u043eu0431u043du044bu0439 way u0443u043cu0435u043du044cu0448u0435u043du0438u00a0 of summary of solutes (TDS) in wastewater to leather factories using bacterial strain for 1, u0438u043cu0435u044eu0449u0435 the number u0434u0435u043fu043eu043du0438u0440u043eu0432u0430u043du0438u00a0 u043cu0442u0441u0441 5097, which comprises the following steps:;(a) u0438u043du043eu043au0443u043bu00a0u0446u0438u044e wastewater to obtain suspension cells;(b) u0438u043du043au0443u0431u0430u0446u0438u044e suspension cells approximately in 37u0441 and approximately 100 rpm;(c) assessment of the levels of TDS using modified arn method.;8. way on p.7, where the ratio of waste water to the biomass u0438u0437u043cu0435u043du00a0u0435u0442u0441u00a0 ranged from 1: 3 to 3: 1.;9. way on p.7, where the ratio of waste water to the biomass of about 1: 1.;10. way on p.7, where sewage leather factories u00a0u0432u043bu00a0u044eu0442u0441u00a0 rough and u044du043bu0435u043au0442u0440u043eu0444u043bu043eu0442u0438u0440u043eu0432u0430u043du043du044bu043cu0438 sewage leather factories.;11. method for u043fu043f.7 and 10, where the strain is reduced TDS in raw wastewater leather factories around 8.5% with the length of about 24 hours.;12. method for u043fu043f.7 and 10, where the strain is reduced TDS in raw wastewater leather factories around 8.3% with the time duration of about 48 hours.;13. method for u043fu043f.7 and 10, where the strain is reduced TDS in u044du043bu0435u043au0442u0440u043eu0444u043bu043eu0442u0438u0440u043eu0432u0430u043du043du044bu0445 wastewater leather factories about 11.1% with the time length of about 24 h.;14. method for u043fu043f.7 and 10, where the strain is reduced TDS in u044du043bu0435u043au0442u0440u043eu0444u043bu043eu0442u0438u0440u043eu0432u0430u043du043du044bu0445 wastewater leather factories about 10.7% in time duration about 48 hours.;15. way on p.7, where the ph of waste water of about 7.0.
机译:1.编号为 u0434 u0435 u043f u043e u043d u0438 u0440 u043e u0432 u0430 u043d u0438 u00a0 u043c u0442 u0441 u0441 5097适合的细菌菌株 u0434 u043b u00a0 u0443 u043c u0435 u043d u044c u0448 u0435 u043d u0438 u00a0 u0441 u043e u0434 u0435 u0440 u0436 u0430 u043d u0438 u00a0粗略的溶质(TDS)摘要el u043a u0442 u0440 u043e u0444 u043b u043e u0442 u0438 u0440 u043e u0432 u0430 u043d u043d u043d u044b u0445废水皮革工厂。; 2。方法 u043f u0440 u0438 u0433 u043e u0442 u043e u0432 u043b u043b u0435 u043d u0438 u00a0 u0438 u043d u043e u043a u0443 u0433 u043b u00a0 u0442 u0434菌株1 u043b u00a0 u0443 u043c u0435 u043d u044c u0448 u0435 u043d u043d u0438 u00a0 u0441 u043e u043e u0434 u0435 u0440 u0436 u0430 u0430 u043d u0438 u00a0溶质摘要(uDS)就像在粗略版本中一样,并且 u044d u043b u0435 u043a u0442 u0440 u043e u0444 u043b u043e u0442 u0438 u0440 u043e u0432 u0430 u043d u043d u043d u044b u0445 u0441 u0442 u043e u0447,用于皮革工厂的水,包括以下步骤:(a)分离菌株;(b)用含有以下成分的 u0430 u0433 u0430 u0440 u043e u043c在营养环境中种植菌株土壤提取物和营养琼脂,至 u043f u043e u043b u0443 u0447 u0435 u043d u0438 u00a0纯培养;(c) u0438 u043d u043e u043a u0443 u0433 u043b u00a0 u0446 u0438 在营养肉汤中的u044e菌株到 u043f u043e u043b u0443 u0447 u0435 u043d u0438 u00a0品种;(d) u0438 u043d u043a u0443 u0431 u0430 u 0446 u0438 u044e启动器,在 u043f u0435 u0440 u0435 u043c u0435 u0448 u0438 u0432 u0430 u043d u0438 u0438中大约需要37 u0441大约16到18小时rpm。;(e) u0438 u043d u043e u043a u0443 u043b u00a0 u0446 u0438 u044e营养肉汤 u0437 u0430 u043a u0432 u0430 u0441 u043a u043e u0439直到 u043e u043f u0442 u0438 u0447 u0435 u0441 u043a u0430 u00a0密度培养达到 u0437 u043d u0430 u0447 u0435 u043d u0438 u00a0 1.0;(f)从培养物中收集细胞查看 u043f u043e u043b u0443 u0447 u0435 u043d u0438 u00a0残留物。;(g)通过 u0440 u0430 u0441 u0442 u0432 u043e u0440 u0435 u043d u043d u0438 0,05 u043c u0444 u043e u0441 u0444 u0430 u0442 u043d u043e u043c缓冲液中的u00a0,ph 6.8。;(h)离心至 u043f u043e u043b u043b u0443 u0447 u0435 u043d u0438 u00a0 u043f u0440 u043e u043c u044b u0442 u043e u0433 u043e残留物。;(i)溶解 u043f u0440 u043e u043c u044b u0442 u043e u043e u0433 u043e残留在最少数量的废水中;(j)将溶解的残留物均质化,从而降低废水中总溶解固体(TDS)的水平,从而降低废水中总溶解固体(TDS)的水平来自皮革 u0430 u0432 u043e u0434 u043e u0432。; 3。方法2,其中对环境的压力 u0432 u044b u0440 u0430 u0449 u0438 u0432 u0430 u0435 u0442 u0441 u00a0 u0430 u0433 u0430 u0440 u0440 u043e u043c u0441在大约16到24小时内; 4。方法2,其中营养肉汤包含约5.0 g u043f u0435 u043f u0441 u0438 u043d u043e u0432 u043e u0433 u043e u043f u0435 u0440 u0435 u0432 u0432 u0432 u0430 u0440 u0430动物组织中,约5.0 g氯化物 u043d u0430 u0442 u0440 u0438 u00a0,约1.5 g u043c u00a0 u0441 u043d u043e u0433 u043e约1.5 g u0434 u0440 u043e u0436 u0436 u0435 u0432 u043e u0433 u043e提取物和约0.2 ml的补间80.; 5。 2的方法,其中 u043a u043e u043d u0435 u0447 u043d u0430 u00a0文化 u0446 u0435 u043d u0442 u0440 u0438 u0444 u0443 u0433 u0433 u0438 u0440 u0443 u0435 u0442在6000 rpm的转速下以大约4.; 6的时间大约20分钟。方法2,其中污泥 u043f u0440 u043e u043c u044b u0432 u0430 u0435 u0442 u0441 u0040通过他的 u0440 u0430 u0441 u0442 u0432 u0432 u043e u0440 u0435 u043d u043d在0.05 m的pH值为6.8的缓冲区中的u0438 u00a0 u0444 u043e u0441 u0444 u0430 u0442 u043d u043e u043c 7。使用皮革厂使用的皮革厂废水中的溶质(TDS)摘要中的 u0430 u044d u0440 u043e u0431 u043d u044b u0439方式1的细菌菌株 u0438 u043c u0435 u044e u0449 u0435编号 u0434 u0435 u043f u043e u043d u0438 u0440 u043e u0432 u0430 u043d u043d u0438 u00a0 u043c u0442 u0441 u0441 5097,包括以下步骤:(a) u0438 u043d u043e u043a u0443 u043b u00a0 u0446 u0438 u044e废水以获得悬浮池;(b) u0438 u043d u043a悬浮细胞大约在37 u0441和大约100 rpm下;(c)使用改进的arn方法评估TDS的水平; 8。在第7页的方法中,废水与生物量的比例为1:3至3:1 ;; 9。第7页的方法,其中废水与生物量之比约为1:1.; 10。第7页的方法,其中污水处理皮革厂 u00a0 u0432 u043b u00a0 u044e u0442 u0441 u00a0粗糙和 u044d u043b u0435 u043a u0442 u0440 u043e u0444 u0434 u043b u043e u0442 u0438 u0440 u043e u0432 u0430 u043d u043d u044b u043c u0438污水处理皮革厂; 11。 7和10的方法,其中应变降低了原废水皮革工厂中的TDS约8.5%,约24小时的时间; 12。 7和10的方法,其中应变降低了原废水皮革工厂的TDS约8.3%,持续时间约48小时; 13。 u043f u043f.7和10中的方法,其中 u044d u043b u043b u0435 u043a u0442 u0440 u043e u0444 u043b u043e u0442 u0438 u0440 u0440 u043e u0432 u0430废水皮革厂约占11.1%,时间约24小时; 14。 u043f u043f.7和10的方法,其中 u044d u043b u043b u0435 u043a u0442 u0440 u043e u0444 u043b u043e u0442 u0438 u0440 u0440 u043e u0432 u0430 15.废水皮革厂的工时约10.7%,工时约48小时; 15。第7页的方法,其中废水的pH值约为7.0。

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