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A kind of esterification reaction system

A technology of esterification reaction and esterification kettle is applied in the field of chemical raw material production equipment, which can solve the problems of complex process and equipment and high energy consumption

Active Publication Date: 2017-07-07
YANGZHOU HUITONG CHEM ENG TECHN
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] In the production process, the PTA powder and ethylene glycol need to be mixed and beaten first, and then enter the esterification kettle from the PTA feed port for heating. During the reaction process, stirring blades are also used to continuously stir. The process and equipment are complex and can be High consumption

Method used

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  • A kind of esterification reaction system
  • A kind of esterification reaction system
  • A kind of esterification reaction system

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Embodiment Construction

[0024] Such as Figure 1 to Figure 5 As shown, the esterification reaction system of the present invention comprises a PTA powder tank 9, an esterification still 1 and a separation tower 10. The heating jacket 2 of the esterification kettle is arranged around, the top of the esterification kettle shell is provided with a PTA feed port 1a and the gas phase outlet 1c of the esterification kettle, and the lower part of the esterification kettle shell is provided with an esterification material outlet 1d. The PTA feed port 1a of the kettle is connected with the outlet of the PTA feed pipe G1, and the inlet of the PTA feed pipe G1 is provided with a feed tee, and the front port of the feed tee is connected with the nitrogen pipe G2, and the top of the feed tee The port is connected to the discharge port 9a of the powder tank through the PTA discharge valve V1.

[0025] The lower part of the inner wall of the esterification kettle shell is provided with an outer guide cylinder 3 ex...

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Abstract

The invention relates to an esterification reaction system. The esterification reaction system comprises a PTA (Pure Terephthalic Acid) powder tank and an esterification kettle, wherein a PTA feeding hole, an ethylene glycol inlet and a gas-phase outlet are formed in the top of the esterification kettle; an external flow guide barrel is arranged at the lower part of an inner wall of the esterification kettle; a discharging annular groove is formed between the external flow guide barrel and the shell; the external flow guide barrel is provided with an outlet which is communicated with the discharging annular groove; the bottom of the discharging annular groove is communicated with an esterified material outlet; an inner cavity of the external flow guide barrel is provided with an internal flow guide barrel; the internal flow guide barrel is lower than the external flow guide barrel; a central material pipe is arranged in an inner cavity of a shell of the esterification kettle; the upper end of the central material pipe is connected with the PTA feeding hole and the lower end of the central material pipe is communicated with a crossed pipe; four branch pipes of the crossed pipe are bent towards the same side in a circular arc transition manner; the ethylene glycol inlet aligns to the part between the external flow guide barrel and the internal flow guide barrel. The system provided by the invention is further provided with an esterified water, ethylene glycol and nitrogen gas separation tower, a first condenser, a compressor and a second condenser. The system is simple in structure, can realize esterified water removal, and complete recycling of ethylene glycol and nitrogen gas, and is low in energy consumption and high in production efficiency.

Description

technical field [0001] The invention relates to an esterification reaction system, belonging to the technical field of chemical raw material production equipment. Background technique [0002] The traditional esterification production equipment includes a PTA powder tank and an esterification kettle. The esterification kettle is equipped with a heating jacket for the esterification kettle. An esterification material outlet is provided, and a PTA powder pipe is connected to the lower part of the PTA powder tank, and the PTA powder pipe is connected to the PTA feed port of the esterification kettle. [0003] In the production process, the PTA powder and ethylene glycol need to be mixed and beaten first, and then enter the esterification kettle from the PTA feed port for heating. During the reaction process, stirring blades must be used to continuously stir. The process and equipment are complex and can High consumption. Contents of the invention [0004] The object of the ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J19/26B01J4/00C07C67/08C07C69/82
CPCB01J4/001B01J4/008B01J19/0013B01J19/26B01J2204/002B01J2204/005B01J2219/00087C07C67/08C07C69/82
Inventor 景辽宁
Owner YANGZHOU HUITONG CHEM ENG TECHN