中试装置

SBS改性沥青中试装置工艺流程的研究

The study of SBS modified asphalt pilot plant process flow

中试装置在0～5℃的条件下采用自然启动方式，60d左右完成启动过程。

It takes about 60 days to complete the pilot plant start-up under the temperature of 0-5 ℃ without seed sludge or sewage .

300t/aP2O5湿法磷酸净化中试装置生产技术

Technology of pilot test on 300 t / a P_2O_5 WPA purification unit

PROFIBUS现场总线和软PLC在色谱分离中试装置中的应用

Application of PROFIBUS and Software PLC in Set of Middle-experiment Equipment for Chromatographic Separation

FCC助剂中试装置的设计与探讨

Design and Discussion of FCC Additive Pilot Plant

AIP吸收器传质特性中试装置及KLa测试方法研究

Pilot test rig for mass-transfer performance of absorbers in AIP and measurement of K_L a

的工业化中试装置，中间实验证明，获得的净化磷酸能达到工业级热法磷酸的标准，每吨产品P刃。

, Ltd. The pilot experiments have shown that the purification cost for each ton products ( P2O5 ) which meet industrial standards on furnace-process phosphoric acid is about 250 Yuan .

PTA中试装置的设计与开发

Research and Development of PTA Medium Test Device

二甲基硫醚中试装置工程建设的HSE管理

HSE Management in Construction of Semi - work Test Equipment for Dimethyl Sulfide

介绍粘泥剥离剂的评价方法以及高效粘泥剥离剂QS-17在中试装置试验的情况和结果。

Presents the appraisal method of the sludge strippers , as well as the testing and result of high efficiency sludge stripper QS-17 .

最后借助aspenplus模拟软件对年产597t甲醇的中试装置进行了计算，得到了系统的特性参数。

Finally , it calculates the device of producing 597 tons methanol per year by ASPEN plus and obtains system characteristic parameters .

应用aspenplus软件对己烷油中试装置进行流程模拟，提出改造方案；

Process simulation for hexane oil pilot plant is done by applying Aspen Plus software , in order to present revamping scheme .

由此确定了中试装置连续运行的操作参数，实现了次临界通量[30L/（m2·h）]条件下处理城市污水的稳定运行。

Therefore the operation parameters of continuous motion of the pilot installation was determined and under the condition of sub-critical flux of 30L / ( m2 · h ), stable motion of sewage treatment was realized .

利用XTL-5型提升管中试装置，对LHO-1和CDC型重油裂解降烯烃催化剂的裂化性能进行了评价。

The properties of LHO-1 and CDC FCC catalysts were tested on XTL-5 riser pilot plant .

在实验室固定床中试装置上以硫含量为1290μg/g的FCC汽油为原料对FCC汽油吸附脱硫工艺（LADS技术）的工艺条件进行了考察。

The operating conditions of the adsorption desulfurization process of FCC naphtha ( LADS technology ) were investigated with a feedstock contained 1290 μ g / g of sulfur in a laboratory fixed-bed reactor .

通过渣油加氢脱硫（HDS）中试装置实测数据，对渣油HDS反应集总动力学进行事前模拟。

Based on the data of residual oil HDS reaction in pilot plant , the lumping kinetic of residual oil HDS reaction was researched by means of prior simulation .

本文针对一个小型中试装置设计并建立了VOCS流向变换催化燃烧反应器监控系统，对原有的自动化程度较低的人工数据采集和控制方式进行了改造；

Aimed at a pilot scale reverse flow reactor for catalytic combustion of VOCS in contaminated air , the advanced monitoring system was designed and built , with rebuilding the former manual data-collections and control mode .

对大颗粒的适应性强.可望在中试装置上得到应用.以实现PFBC高温炉渣的连续排放和冷却。

Because of the foregoing the said system is expected to find application in an intermediate test plant to realize the continuous disposal and cooling of PFBC high-temperature boiler slag .

GPC分析结果表明，中试装置溶液聚合物的重均相对分子质量可达到5.0×106以上，减阻率55%-63%，具有工业化价值。

Results by GPC indicated that , in a pilot plant the weight-average relative molecular mass of the solution polymers could reach over 5.0 × 106 , and the drag reducing efficiency of the polymers was 55 % ~ 63 % .

最后通过地下水原位修复中试装置，结合中试实验数据和基础试验数据，建立了ZVI修复污染地下水的预测模型。

In combination of the in situ groundwater treatment pilot plant data with the base experiment data we established a prediction model for the ZVI groundwater restoration .

中试装置的生产能力为20t/年，产品纳米氧化锌粒径为35～80nm，收率达到80%。

The production amount of pilot test installation is 20t / year , the particle diameter of nanometer size ZnO prepared is 35 ~ 80nm and yield 80 % .

在一个四段绝热固定床甲烷化中试装置中，对RHM-266耐高温甲烷化催化剂及甲烷化工艺进行了中试考察。

Thermal stability of high temperature-tolerant methanation Catalyst RHM-266 and methanation processes were studied in pilot unit with four-stage adiabatic fixed bed reactors .

聚乙烯新型催化剂QCP-01在气相法聚乙烯中试装置上进行了聚合评价试验。

The evaluation test of QCP - 01 novel PE catalyst was performed in the gas phase polyethylene pilot plant in this paper .

基于气升式内循环反应器原理，对一体式膜-生物反应器结构进行了优化设计，构建了处理量为15.6m3/d的中试装置。

A pilot-scale submerged membrane bioreactor with treating capacity of 15.6m3/d was developed on the basis of its structural optimization design according to the principle of air-lift internal-loop reactor .

在中试装置上合成出高乙烯基溶聚丁苯橡胶新牌号Y837V基础胶，并填充芳烃油。

The basic solution polymer on new brand ( Y837V ) of solution polymerized butadiene - styrene rubber was synthesized in the pilot plant , and filled aromatic oil .

采用MP-01新型异丙苯催化剂，在中试装置上进行了苯与丙烯液相烷基化反应合成异丙苯试验，通过催化剂寿命试验及条件试验考察了MP-01新型异丙苯催化剂的性能。

This article described the pilot trial for synthesis of cumene with MP-01 new catalyst in liquid-phase alkylation of benzene and propylene . The performance of MP-01 new catalyst was examined by the life experiment and technical condition experiment .

在采用R150自动控制系统的基础上，对乙烯氧化生产环氧乙烷催化剂的评价中试装置的控制系统进行了改进，并增建一套采用高压水撤热的反应系统。

In this paper , an automatic control system for ethylene oxidation silver catalyst evaluation unit was reformed based on R-150 modular automation system , A new set of oxidation reactor with highpressure water as coolant was rebuilt .

在10L发酵罐和3000L中试装置上，以正构烷烃为原料对重复批式发酵生产长链二元酸工艺进行了研究。

The repeated batch fermentative process for long chain dicarboxylic acids ( DCA ) from alkane was studied . The 10L bioreactor and 3000L pilot plant results showed that the microbe cells from different fermentative times could be applied as seeds for cultivating again .

利用200kW的中试装置，在常压下研究了天然气在氮热等离子体中的裂解行为，考察了输入功率、甲烷流量以及CH4/N2摩尔比对反应的影响。

The pyrolysis of natural gas in the DC nitrogen plasma arc at atmospheric pressure was studied in a 200 kW plasma generator . The effect of methane flow , input power and molar radio of CH_4 / N_2 on the production of carbon black was investigated .

超临界水氧化法中试装置的建立和考察

Establishment and Review of a Pilot-plant-scale Experimental Set for Supercritical Water Oxidation