Abstract: Provided are genes, coding proteins and uses thereof, gene elements, genes and uses, gene elements, methods for synthesizing odd numbered medium chain aliphatic aldehydes, for synthesizing odd numbered medium chain aliphatic alcohol and for synthesizing even numbered medium chain aliphatic hydrocarbons. Provided is method for producing odd numbered aliphatic alcohols in Escherichia coli. An ?-dioxygenase from rice is used without additional deoxidization and energy supply from cells. The ?-dioxygenase can also be used for synthesizing aliphatic alcohols with different proportions of C11 to C15 by co-working with different thioesterases.

Abstract: Provided are genes, coding proteins and uses thereof, gene elements, genes and uses, gene elements, methods for synthesizing odd numbered medium chain aliphatic aldehydes, for synthesizing odd numbered medium chain aliphatic alcohol and for synthesizing even numbered medium chain aliphatic hydrocarbons. Provided is method for producing odd numbered aliphatic alcohols in Escherichia coli. An ?-dioxygenase from rice is used without additional deoxidization and energy supply from cells. The ?-dioxygenase can also be used for synthesizing aliphatic alcohols with different proportions of C11 to C15 by co-working with different thioesterases.

Abstract: The present invention published a large walled field conditions P92 long pipeline local heat treatment processes. Firstly, according to the specific conditions for the on-site grade heat-resistant steel (P92 pipe), combining of the finite element method and test, the Heated Band (HB) width and Gradient Control Band (GCB) was calculated. The pipe was then locally heated using the flexible ceramic resistive heater. When the temperature reaches 80-100° C., the pipe was heated to constant temperature at 80-100° C. for 2 h. The pipe was heated to 300° C. at the rate of 150° C./h. When the temperature reaches 300° C., rising the temperature to 765° C. at the rate of 80° C./h. Holding time is calculated by the wall thickness (5 min/mm, no less than 4 h). Lowering the temperature to 300° C. at the rate of 100° C./h and then natural cooling to room temperature, finally removing the heating device. Finally, the local heat treatment process can be obtained.

Abstract: The present invention discloses a method and a device for recovering ethylene during the process for producing vinyl acetate, wherein a double solvent absorption method composed of an absorbent solution and deionized water is adopted.

Abstract: The invention discloses a radio frequency front-end based on the high-intermediate frequency superheterodyne and zero intermediate frequency structure, which includes a transmitting module and a receiving module, wherein, the receiving module includes the following devices connected in turn with each other: a transceiving antenna, a low-pass filter, a superheterodyne unit, an IF band-pass filter, a zero-IF unit, a analog-to-digital converter and a digital baseband module of which the output is communicated with the transmitting module. The zero-IF unit includes the following devices which are also connected in turn with each other: a zero-IF mixer, an active low-pass filter and a variable gain operational amplifier of which the output is communicated with the input of the ADC; the inputs of the zero-IF mixer are communicated with the output of the IF band-pass filter and the second LO respectively.

Abstract: The present invention published a large walled field conditions P92 long pipeline local heat treatment processes. Firstly, according to the specific conditions for the on-site grade heat-resistant steel (P92 pipe), combining of the finite element method and test, the Heated Band (HB) width and Gradient Control Band (GCB) was calculated. The pipe was then locally heated using the flexible ceramic resistive heater. When the temperature reaches 80-100° C., the pipe was heated to constant temperature at 80-100° C. for 2 h. The pipe was heated to 300° C. at the rate of 150° C./h. When the temperature reaches 300° C., rising the temperature to 765° C. at the rate of 80° C./h. Holding time is calculated by the wall thickness (5 min/mm, no less than 4 h). Lowering the temperature to 300° C. at the rate of 100° C./h and then natural cooling to room temperature, finally removing the heating device. Finally, the local heat treatment process can be obtained.

Abstract: The present invention discloses a method and a device for recovering ethylene during the process for producing vinyl acetate, wherein a double solvent absorption method composed of an absorbent solution and deionized water is adopted.