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1)  Combining methanol tower
联醇塔
2)  joint-pylon
联塔
1.
In order to study on the mechanic behaviour of the joint-pylon of the cabel-styed bridge with separate twin prestress girders and a united twin-pylon.
为了研究分幅联塔斜拉桥的联塔力学行为,对甬江特大桥整个桥塔进行缩尺模型试验研究,介绍了模型试验的结构设计和加载方法设计,建立了求解索力的数学规划模型。
3)  combined methanol
联醇
1.
The poisoning accident of catalyst of ammonia synthesis in combined methanol production has been discussed from the aspects of the complete set of equipment capacity, effect of methanol and dimethyl ether on catalyst of ammonia and economic operation of combined methanol production etc.
从设备能力的配套、甲醇和二甲醚对氨催化剂的影响、联醇生产的经济运行等方面对联醇生产中氨合成触媒中毒事故进行了论述。
2.
Author introduced the process for poisoning trouble of ammonia synthesis catalyst caused by combined methanol production with ammonia synthesis, in allusion to analysis made for the unfavoured influence caused on ammonia synthesis of the injurious gases after-methanol gas, the result shows that the sulfur in the raw gas of methanol has the promoting action for forming the dimethyl ether.
介绍了由于合成氨联醇引起的氨合成触媒中毒事故的过程 ,针对醇后气中有害气体对氨合成产生的不利影响进行了分析 ,结果表明 ,甲醇原料气中硫对生成二甲醚有促进作用 ,CO2 对生成二甲醚有抑制作用。
4)  ammonia-methanol coproduction
联醇
1.
Its use in ammonia-methanol coproduction has resulted in prolonged service life of methanol synthesis catalyst and thus better econonhc benefit.
该文介绍了我国开发的852型COS水解催化剂串KT310常温ZnO脱硫剂精脱硫新工艺在联醇生产中的应用。
5)  methanol co-production process
联醇
1.
The used methanol co-production process catalysts were taken out from different positions in the commercial reactor.
由工业联醇合成塔内不同位置取出使用后的催化剂,对其硫含量进行化学分析,得到催化剂颗粒内硫的分布;分析中毒因素和原因,得到催化剂活性校正系数,并对联醇合成塔进行模拟,所得结果与实测值相吻合。
6)  methanol tower
甲醇塔
1.
Rotation reasons and its harms of the inner parts of methanol tower are introduced.
介绍了甲醇塔均温型内件在生产中旋转的原因、危害。
补充资料:二1-联十六烷醇磷酸氢酯
CAS:2197-63-9
分子式:C32H67O4P
熔点:76-75℃
中文名称:二1-联十六烷醇磷酸氢酯
英文名称:1-Hexadecanol, hydrogen phosphate;Dicetyl phosphate;Dihexadecyl phosphate;dicetyl hydrogen phosphate;phosphoric acid, dihexadecyl ester;1-Hexadecanol,hydrogen phosphate
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