1) explosion of buried tube
埋管爆管
2) burying pipe
埋管
1.
It analyzes causes on generating quality deficiency of drilling-grouting pile from burying pipe、clipping pipe、water seepage of conduit and collapse and introduces relative prevention measures and its treatment,which to ensure quality of grouting pile and prevent various accidents.
从埋管、卡管、导管进水、塌孔等方面分析了产生钻孔灌注桩质量缺陷的原因,并介绍了相应的防治处理措施,以保证灌注桩的质量,防止各种事故的发生。
3) immersed tube
埋管
1.
The convection heat transfer coefficient of immersed tube in the heat transferring zone is impacted by the velocity of the moving zone nearby and its data and change trend are obviously different with those of the common bubbling bed.
垃圾焚烧系统中 ,内旋流流化床存在不同布风速度的移动区、流动区和换热区 ,处于换热区的埋管的对流换热系数受附近流动区气流参数的影响 ,其变化趋势及数值大小与普通鼓泡型流化床之间有明显不同 :最大的对流换热系数明显高于鼓泡床 ;换热区尚未流化时 ,对流换热系数已经大幅提高 ;整条换热曲线的变化比较平缓 ,易于流化床浓相床内换热。
2.
Heat transfer coefficients between immersed tube and bed materials in HSFB were measured with help of a fast response heat transfer probes.
在自建的旋流流化床冷态实验台上,采用基于微型热流密度感应薄膜制成的传热探针,测量了旋流流化床中埋管与床料的传热系数,研究流化风速、颗粒粒径、探针位置和密相区二次风射流等因素对埋管传热系数的影响。
3.
The heat transfer of immersed tubes in fluidized beds is influenced by the uneven distribution of fluidized air, and the coefficient of that is not only a function of fluidized air velocity in heat transfer zone, but also is correlative with the air velocity in fluidized zone nearby.
非均匀布风对流化床埋管换热特性有一定的影响，埋管的对流换热系数不仅是埋管所处换热区流化速度的函数，而且与相邻的流动区流化速度有一定关系。
4) buried pipe
埋管
1.
By using thermal dynamic simulation and computational Fluid Dynamics (CFD) techniques in conjunction with the thermal comfort PMV / PPD model, investigates the indoor temperature, velocity and thermal comfort in rooms respectively with natural ventilation and ventilation with a buried pipe system.
将热舒适评价标准ＰＭＶ／ＰＰＤ模型与建筑动态热模拟及计算流体动力学（ＣＦＤ）模拟相结合，分别对重庆地区自然通风房间和埋管送风通风房间进行了室内气候及热舒适性模拟与分析。
2.
The influencing factors of wear of buried pipes in ebullition boiler are analyzed,and the anti-wear measures are put forward.
分析了沸腾锅炉埋管磨损的影响因素,提出了抗磨措施。
3.
Analysis on the wear reason of buried pipe system for coal-sline CFB and its solving measures are presented herein.
介绍某循环流化床锅炉埋管系统损坏原因及解决方法。
5) tube bursting
爆管
1.
Cause analysis and solution for boiler high-temperature superheater tube bursting during 600MW supercritical unit startup commissioning;
600MW机组锅炉高温过热器爆管原因分析与处理
2.
Analysis on waterwall tube bursting of Unit 3 boiler in Shajiao C Power Plant;
沙角C电厂3号锅炉水冷壁管爆管原因分析
3.
Analysis of primary superheater tube bursting in a thermal power plant;
火力发电厂一级过热器爆管分析
6) tube rupture
爆管
1.
use analysis on sidewall enclosure superheater tube rupture of 2 209 t/h boiler in Huaneng Dezhou Power Plant;
华能德州电厂2209t/h锅炉侧墙包复过热器爆管原因分析
2.
The paper analyses the heating surface tube rupture accident and develops the treatment procedure and precautionary measures for tube rupture.
简要介绍300MW循环流化床锅炉受热面布置情况、受热面爆管的现象和处理情况以及预防措施。
3.
Water wall tube rupture owing to hydrogen corrosion of No.
针对富拉尔基发电总厂3号炉水冷壁管在运行中,连续发生多次氢腐蚀爆管的问题,分别从锅炉运行状况、水质、凝汽器泄漏的影响及炉内水处理方式等方面进行较为详细的分析。
补充资料：爆管
分子式：
CAS号：
性质：蒸汽锅炉的管子突然爆破。爆管时有明显的爆破声和喷汽声、水位迅速下降、气压明显降低，并可能由锅炉缺水酿成更为严重的事故。爆管的主要原因是水质不良造成结垢或腐蚀、水循环不合理造成管子损伤等。过热和脆化都可直接引起爆管。
CAS号：
性质：蒸汽锅炉的管子突然爆破。爆管时有明显的爆破声和喷汽声、水位迅速下降、气压明显降低，并可能由锅炉缺水酿成更为严重的事故。爆管的主要原因是水质不良造成结垢或腐蚀、水循环不合理造成管子损伤等。过热和脆化都可直接引起爆管。
说明：补充资料仅用于学习参考，请勿用于其它任何用途。
参考词条