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UASB反应器设备化拼装式反应器 Lipp技术圆形和矩形反应器 The Standardized and Equalization of Upflow Anaerobic Sludge Blanket Reactor Beijing Municipal Research Institute of Environmental Protection Abstractor:In this paper, the development of anaerobic treatment processes are analyzed, the Equalization of the most popularized in application among various kind anaerobic reactors, UASB reactor is trend of technology in abroad and at home.

本研究通过对国内外厌氧工艺的发展分析,提出了各种厌氧反应器中应用最为广泛的UASB反应器设备化是国内外的发展方向的观点。

Under toxic load shocking, The PGANN found by the database of UASB acclimated by the toxicant could be applied to predict the dynamic variation of the UASB been not acclimated. The PGANN found by the database of the UASB been not acclimated could also be applied to predict the dynamic variation of the UASB acclimated by the toxicant.

毒物负荷冲击下,在未驯化的UASB反应器上建立的PGANN可用来预测驯化过的UASB反应器各参数的变化,在驯化过的UASB反应器上建立的PGANN也可用来预测未经毒物驯化的UASB反应器各参数的变化。

A novel photocatalytic reactor, which can use sun light and graniform photocatalyst, was developed and evaluated. Hydraulics studies show that the actual mean residence time was approximately 1. 5 to 2 times greater than the theoretical mean residence time, which is of great advantage for degrading the pollutants in the reactor, and that the high reaction rate can be obtained by increasing the rotational speed.

设计了一种新型提升式圆盘多相光催化反应器(exalting round-platephotocatalytic reactor,ERPPR),该反应器的主要特点是能够利用太阳光和粒状催化剂,通过对ERPPR水力学特性的研究发现,该反应器的实际平均水力停留时间约为理论平均停留时间的1.5到2倍,反应器内循环流量与提升桨转速成正比。

By comparison, the TATSR has higher efficiency of pumping. plasticization and mixing than that of twin screw reactor. At the same time, the productivity ratio of TATSR is bigger than that of twin screw and four-screw extruder. So TATSR has a good outlook of engineering application.

与双螺杆反应器相比,三螺杆反应器具有较强的物料输送能力、塑化和混合能力;同时,三螺杆反应器的产能比又大于双螺杆和四螺杆反应器,因此,三螺杆反应器具有较好的工程应用前景。

The invention relates to a method for treating gaseous VOCs by a solid extraction-electro-catalytic oxidation method and a device thereof. The method has the steps that: firstly, an electromagnetic type air compressor is used for controlling the gas flowing velocity by a glass rotameter so as to ensure contaminations in the contamination solution in a gas washing bottle to be stripped into an electrochemical reactor; secondly, microporous aeration heads are distributed in the electrochemical reactor, after being stripped into the electrochemical reactor, the gas is distributed in the electrochemical reactor by the microporous aeration heads, takes parts in the electrochemical reaction and passes through the cathode of absorptive and conductive porous material and the anode of iron sheet in sequence; thirdly, the treated gas finally flows out from the top end of the electrochemical reactor and enters into the gas absorption solution.

本发明涉及一种固态萃取-电催化氧化法处理气态VOCs的方法及装置,方法步骤:第一步,电磁式空压机通过玻璃转子流量计控制气体流速,将气体洗瓶中的污染物溶液中的污染物吹脱进电化学反应器;第二步:电化学反应器中布有微孔曝气头,气体吹脱进入电化学反应器后,通过微孔曝气头分布于电化学反应器内,参加电化学反应,依次经过通过吸附性导电多孔材料阴极和Fe片阳极;第三步,经处理后的气体最后从电化学反应器顶端流出进入气体吸收溶液。

The FNN built by database of unacclimated UASB reactor shocked by toxic load did not adapt to predict UASB reactor acclimated by toxicant, The FNN built by database of UASB reactor acclimated by toxicant also did not adapt to predict unacclimated UASB reactor.

由未经毒物驯化的UASB反应器建立的模糊神经网络不适合预测毒物驯化过的UASB反应器,由毒物驯化过的UASB反应器建立的模糊神经网络也不适合预测未驯化的的UASB反应器

English Outline Describes the classification and characteristics of biochemical reactions, major metabolic pathways; biochemical thermodynamics, biokinetics, immobilization technology, bioreactor construction, experimental design, mass transfer, heat transfer, and flow pattern; mathematical modeling, computer simulation, and optimization; the classification of reactors, aerobic and anaerobic, their operational characteristics and applications.

Chinese Outline 探讨生物化学反应种类及其特性,主要代谢路径;生物热力学、生物动力学、酵素特性探讨与酵素动力学,固定化技术、生物反应器之组装、实验设计、反应器内质传、热传及流动型态解析;数学模式,电脑模拟及最适化;简介反应器种类:好氧及厌氧反应器,其操作特性与应用。

The sludge settling characteristic is satisfying with SV varying from 22 to 30 and SVI varying from 58 to 80ml/g.The sludge bulking problem has been avoided successfully. The excess sludge can be thickened to 3%-4 %. The alkalinity remains equilibrious between the nitrification and denitrification in SBR-BAF system. The COD and TP loading of SBR are 2.08kgCOD/kgMLSS·d and 41.68gTP/kgMLSS·d, respectively. The NH4+-N loading of BAF is 1.16kgNH_4~+-N/m~3.d. The total HRT is about 10 hours which is only about half of suspended growth process for simultaneous phosphorous and nitrogen removal. Under the above mentioned high loadings and short HRT, the mean removal efficiency of COD, TP, NH4+-N, TN is 96%, 98%, 93%, and 84%, respectively. The mean effluent concentration of COD, TP, NH4+-N, TN, SS is 20mg/L, 0.23 mg/L, 3.24 mg/L, 7.68 mg/L, 5 mg/L respectively, which means every index can meet the first class of Discharge Standard of Pollutants for Municipal Wastewater Treatment Plant.

最后,以上述最佳运行参数控制SBR-BAF系统运行,长期运行结果表明:系统中悬浮污泥的絮凝、沉降性能良好,SV值为22~30,SVI值为58~80,不再有污泥膨胀之虞,而且可以对剩余污泥进行重力浓缩,浓缩后污泥浓度可以达到3~4%;短程硝化和反硝化使得系统可以维持碱度平衡,无需额外补充碱度;系统在高负荷(SBR反应器COD负荷为2.08kgCOD/kgMLSS.d,TP负荷为41.68gTP/kgMLSS.d,BAF反应器NH4+-N负荷为1.16kgNH_4~+-N/m~3.d)、低水力停留时间(SBR反应器9h,BAF反应器1h,总计10h,约为同步脱氮除磷悬浮污泥工艺的一半)下稳定高效运行,对COD(不计BAF加入的外碳源)、TP、NH_4~+-N、TN的平均去除率为96%、98%、93%、84%,出水COD、TP、NH4+-N、TN、SS的平均浓度为20mg/L、0.23 mg/L、3.24 mg/L、7.68 mg/L、5 mg/L,各项水质指标均达到《城镇污水处理厂污染物排放标准》(GB 18918-2002 )一级标准的A标准的要求。

It included the make-up and operation modes of reactor system, the selection of operation phases, the feasibility of feeding and draining simultaneously and the volumetric exchange rate, the measurement of retention time distributionin the reactor, the analysis of flow pattern in the reactor, the calculation of hydrodynamic shear force in the reactor and the analysis of its effects and the measurement of oxygen transfer coefficients and oxygenating performance parameters.

它包括:反应器系统的组成和运行模式、运行阶段的选择;探讨SBBR同时进出水方式的可行性及确定体积置换率;测定反应器的停留时间分布;分析反应器中的流态;计算反应器中的水力剪切力和分析其影响;测定反应器中氧传递系数和充氧性能参数等。

When A〓-A〓-O-A〓 system, using fixed beds as anaerobic and anoxic reators and draft-tube fluidised bed as aerobic reactor (total hydraulic residence time 26. 2h, 9, 5, 7. 2 and 5h for each stage, and recycle ratio of mixed liquor from oxic reactor to the first anoxic reactor 5: 1), is used, the removal rates of COD, NH〓N and TN reach 97, 95. 5 and 90% respectively (influent COD, NH〓-N and TN 1204. 8, 274. 3 and 443mg/l respectvely).

采用A〓-A〓-O-A〓流程和简捷硝化-反硝化过程,以固定床作厌氧反应器和缺氧反应器,以内循环式生物反应器作好氧反应器,系统总水力停留时间为26.2h,各段停留时间分别为9h,5h,7.2h和5h,好氧反应器和第一级缺氧反应器之间的混合液回流比为5:1,系统进水COD为1204.8mg/l,NH〓-N为274.3mg/l,TN为443mg/l时,COD、NH〓-N和TN的去除率分别可达97%、95.5%和90%。

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We have no common name for a mime of Sophron or Xenarchus and a Socratic Conversation; and we should still be without one even if the imitation in the two instances were in trimeters or elegiacs or some other kind of verse--though it is the way with people to tack on 'poet' to the name of a metre, and talk of elegiac-poets and epic-poets, thinking that they call them poets not by reason of the imitative nature of their work, but indiscriminately by reason of the metre they write in.

索夫农 、森那库斯和苏格拉底式的对话采用的模仿没有一个公共的名称;三音步诗、挽歌体或其他类型的诗的模仿也没有——人们把&诗人&这一名词和格律名称结合到一起,称之为挽歌体诗人或者史诗诗人,他们被称为诗人,似乎只是因为遵守格律写作,而非他们作品的模仿本质。

The relationship between communicative competence and grammar teaching should be that of the ends and the means.

交际能力和语法的关系应该是目标与途径的关系。

This is not paper type of business,it's people business,with such huge money involved.

这不是纸上谈兵式的交易,这是人与人的业务,而且涉及金额巨大。