通过光纤传输的信号会变弱，因此信号必须通过一种称为再生器的设备才能传输到更远的地方。
Signals running through fiber-optic cables deteriorate, and so the signals must be run through a piece of equipment called a regenerator before being transmitted farther.
这与再生器的实际情况是相符的。
This is in accordance with the actual conditions of regenerator.
此外，对再生器的传输特性进行了研究。
Furthermore, the transmission characteristic of the regenerator is also discussed.
洗油再生器是焦化厂蒸苯工序中的重要设备之一。
Wash oil regenerator is one of the important equipment during the evaporation of benzol in the. coking mill.
对斜管与再生器相贯线部位的衬里结构进行了改进。
The lining structure at the linked position between inclined pipe and regenerator was improved.
它用来控制再生器的压力和调节烟气输送机入口流量。
It is used to control the pressure of regenerator and regulate the inlet flow of flue gas blower.
再生器造渣能力直接关系到循环洗油质量和洗油消耗。
Slagging capacity of regenerator has direct influences on the quality of circulating wash oil and consumption of wash oil.
溶液除湿空调系统中最重要的部件是除湿器和再生器。
The dehumidifier and regenerator are the main parts of liquid desiccant equipments.
摘要再生器是溶液除湿空调系统中的重要传热传质部件。
Regenerator is a crucial component in the liquid desiccant air conditioning system.
催化裂化装置反应器、再生器、烟道、提升管斜插口等部位。
Reactor, regenerator, flue, inclined inserting mouth and so on in catalyst cracking apparatus.
在再生器中放进冷却盘管能控制温度，也能除去过多的热量。
Cooling coils are introduced into the regenerator to control the temperature and remove the excess heat.
这两种气体和空气预热的再生器，每边两个炉，或者加热的废气。
Both the gas and air are preheated by regenerators, two on each side of the furnace, alternatively heated by the waste gases.
催化裂化装置高效汽提技术可有效降低焦炭产率，减轻再生器负荷。
The high efficiency steam stripping technology of catalytic cracking unit can efficiently decrease the coke yield, and mitigate the regenerator's load.
用动态优化的方法求解催化裂化装置再生器的工艺裕量与控制设计。
The problem of margin analysis and control design of FCC regenerator was solved through multi-objective mixed-integer dynamic optimization.
再生器采用燃气驱动，实现沸腾蒸发和非沸腾蒸发结合的两效再生。
The regenerator driven by gas makes the weak desiccant coming from the dehumidifier to renew by boiling and non-boiling evaporation.
这种污水再生器简便实用，能将生活污水转化成质量较高的再生水。
Due to simple and practical use, the sewage regenerator can convert domestic sewage into the regeneration water with high quality.
再生器密相中增设格栅是提高重油催化裂化装置再生能力的有效措施。
Adding a grid to the dense phase of the regenerator is an effective method to raise the regenerating capacity of a heavy oil catalytic cracking unit.
流化催化裂化装置再生器主风分布管的设计直接影响再生器的平稳操作。
The design of main air distributor in regenerator of FCCU is directly related to the smooth operation of regenerator.
讨论了在催化裂化再生器中焦中氢元素的燃烧，并推算出其相对燃烧速度。
The combustion of hydrogen in coke under regeneration is also discussed and its relative burning rate is reckoned.
因为催化剂在再生器中停留时间不足，故返回反应器的催化剂可能未被完全再生。
Catalyst returning to the reactor may not be completely regenerated because of insufficient time in the regenerator.
通过对再生器催化剂输入管线的振动测试、现有管线振动分析计算，找出了振动原因；
By means of vibration testing of catalyst input pipeline of regenerator, analysis calculation of existent pipeline, the vibration reason is found.
该方法进一步包括在再生器中从废弃催化剂上移除焦炭，从而增加合成气的生产量。
The method further comprises removing coke from the spent catalyst in the regenerator, thereby increasing the amount of synthesis gas production.
节约电的措施为：对催化裂化装置烟机及再生器旋分器进行检修改造，提高烟机效率；
The measures for saving electricity are:overhauling and revamping the flue gas turbine and regenerator cyclone device of the catalytic cracker to raise the efficiency of the turbine;
建立了前置烧焦罐式高效再生器催化裂化装置的提升管反应器和汽提段的动态数学模型。
A dynamic model of mechanism has been developed for the reactor and stripper of a fluid catalytic cracking unit (FCCU) with a high efficiency regenerator.
用该模型对在提升管再生器中的再生过程进行了模拟计算，分析了再生器中的温度场和速度场。
With this model, simulations were implemented for a riser regenerator, and the velocity field and temperature field in the regenerator were calculated and analyzed.
这种力量或流化催化剂在反应器和再生器之间不断循环，用空气、油蒸气和蒸汽作为输送介质。
This power, or fluid catalyst, is continuously circulated between the reactor and the regenerator, using air, oil vapor, and steam as the conveying media.
应用光学显微镜和扫描电子显微镜研究分析了催化裂化装置再生器内U型取热盘管失效的原因。
The causes of failure of the U-type catalyst cooler in regenerator of FCCU were analyzed with optical microscope and scanning electron microscope.
提出了一个用于描述流化催化裂化单元提升管反应器、沉降器及再生器动态行为的计算机仿真模型。
A model for a fluid catalytic cracking (FCC) unit which describes the dynamic behavior of the riser, particle separator vessel and the regenerator is developed.
根据催化装置三旋、再生器等设备的实际情况，制定了相应的设计原则和目标，进而选定保温材料。
According to the actual situation of the equipment of the catalyzed installation, corresponding designs and goals are formulated. Then the heat preservation materials are designated.
外取热器位于热油泵房、再生器、催化剂罐、大型烟道的中间，所处位置给管束吊装带来了很大的难度。
External catalyst cooler is located between hot oil pump room, regenerator and catalyst tank, very difficult to be hoisted.
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