A Method for Indirect Monitoring and Regulation of Trace Water in Polyolefin Reactor

A technology of reactors and polyolefins, applied in chemical instruments and methods, control/adjustment processes, chemical/physical processes, etc., can solve the problems of long reaction cycle, operation lag, low sensitivity of monitoring system, etc., and achieve short reaction cycle, Effects of reduced energy consumption and low equipment investment

Active Publication Date: 2021-06-22
ZHEJIANG UNIV
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Problems solved by technology

Some factories use the static signal fluctuation detection method to monitor the water content in the reactor, but only when the water content in the reactor is greater than 10ppm, can they receive a relatively obvious static fluctuation signal, and then the operator can manually adjust it. During the whole monitoring process, the monitoring system has low sensitivity, long response cycle and operation lag

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  • A Method for Indirect Monitoring and Regulation of Trace Water in Polyolefin Reactor
  • A Method for Indirect Monitoring and Regulation of Trace Water in Polyolefin Reactor
  • A Method for Indirect Monitoring and Regulation of Trace Water in Polyolefin Reactor

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Embodiment Construction

[0035] The technical solutions in the embodiments of the present invention are clearly and completely described below in conjunction with the accompanying drawings of the present invention. Apparently, the described embodiments are only some of the embodiments of the present invention, not all of them. Based on the embodiments of the present invention, all other embodiments obtained by persons of ordinary skill in the art without creative efforts fall within the protection scope of the present invention.

[0036] as attached figure 2 As shown, after the ethylene and hydrogen are pressurized by the compressor C1 and cooled by the cooler D1, they enter the fluidized bed reactor R for polymerization, and the total flow of the stream entering the reactor is 1080 kmol / hr, wherein the total flow of fresh ethylene and hydrogen It is 200kmol / hr. Unreacted ethylene and hydrogen circulate from the top of the reactor into the compressor C1, and the polyolefin resin produced by the reac...

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Abstract

The invention discloses a method for indirect monitoring and regulation of trace water in a polyolefin reactor. The method includes: a detection step, using a pressure detection device to detect the pressure change of the stream in the cold box, and transmitting the information to a computing device; a calculation and analysis step, using the computing device to analyze the pressure information from the detection step, and calculating the pressure of the stream entering the cold box Content, indirectly calculates the water content in the polyolefin reactor, warns of abnormal conditions, and sends adjustment instructions to the control step at the same time; control step, receives instruction information from the calculation and analysis step, controls the valve v1 to adjust the flow rate of the deactivation steam, and controls the valve v2 adjusts the flow rate of the stream entering the dehydration tower, thereby reducing the water content of the reactor and increasing the production rate. The method of the present invention can not only quickly detect the water content of the reactor through the coordination and cooperation of the detection step, calculation and analysis step and control step, but also can adjust the flow rate of the water removal operation and the flow rate of the deactivation steam in real time to improve the overall production efficiency.

Description

technical field [0001] The invention belongs to the field of polyolefin production, and in particular relates to a method for indirect monitoring and regulation of trace water in a polyolefin reactor. Background technique [0002] During the production of olefin polymers, unreacted hydrocarbons (ethylene, ethane, propylene, butene, butane, isopentane, hexene, etc.), nitrogen, residual catalyst, etc. These unreacted hydrocarbons must be removed and the residual catalyst in the polyolefin resin must be deactivated to meet environmental protection standards and ensure the safety of downstream processes and products. At present, the gas-phase polymerization process is widely used in factories due to its simple process flow, flexible and convenient operation, wide range of products, and low investment cost. CN104792117B etc.) disclosed in. [0003] In order to deactivate the residual catalyst in the resin, it is usually necessary to add deactivation steam into the degassing ch...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C08F10/00C08F110/02C08F2/01B01J19/00
CPCB01J19/0006C08F10/00C08F110/02C08F2/01
Inventor 廖祖维董轩阳永荣王靖岱黄正梁包崇龙蒋斌波孙婧元杨遥张浩淼张池金林渠成王瑞航沈煜栋
Owner ZHEJIANG UNIV
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