CN204702685U - A kind of serialization preparation facilities of N-pyrrolidone acetate - Google Patents

A kind of serialization preparation facilities of N-pyrrolidone acetate Download PDF

Info

Publication number
CN204702685U
CN204702685U CN201520110450.6U CN201520110450U CN204702685U CN 204702685 U CN204702685 U CN 204702685U CN 201520110450 U CN201520110450 U CN 201520110450U CN 204702685 U CN204702685 U CN 204702685U
Authority
CN
China
Prior art keywords
tubular type
reactor
pyrrolidone
preparation facilities
arranging
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active
Application number
CN201520110450.6U
Other languages
Chinese (zh)
Inventor
吴剑华
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Shenyang University of Chemical Technology
Original Assignee
Shenyang University of Chemical Technology
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Shenyang University of Chemical Technology filed Critical Shenyang University of Chemical Technology
Priority to CN201520110450.6U priority Critical patent/CN204702685U/en
Application granted granted Critical
Publication of CN204702685U publication Critical patent/CN204702685U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Pyrrole Compounds (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

The utility model discloses a kind of serialization preparation facilities of N-pyrrolidone acetate, this preparation facilities comprises: material mixer (1), tubular type salt-forming reactor (2), reactive distillation column (3), supplementary solvent mixing tank (4), tubular type condensation reactor (5), equipment room connection line, control instruments and annex; Material mixer (1), tubular type salt-forming reactor (2), to supplement solvent mixing tank (4), tubular type condensation reactor (5) be tube type apparatus with or without chuck, and arranging in pipe or not arranging has moving and static mixing element of disturbance mixing effect to material.It is that starting raw material prepares salify in Piracetam (piracetam) technique, condensation reaction N-pyrrolidone acetate realizes serialization and prepares that the utility model can make by pyrrolidone.Mass transfer effect is good, and fully, speed of response is fast in material contact; Heat-transfer effect is good, and temperature of reaction controls precisely, to be conducive to improving the quality of products.

Description

A kind of serialization preparation facilities of N-pyrrolidone acetate
Technical field
The utility model relates to a kind of chemical plant installations, particularly relates to a kind of serialization preparation facilities of N-pyrrolidone acetate.
Background technology
in formula, R is CH 3or C 2h 5
N-pyrrolidone acetate is the intermediate of Piracetam (piracetam).Piracetam (piracetam) is a kind of drugs for nervous, there is the effect promoting brain memory function, old memory to be gone down and the intelligence of some mentally handicapped youngster improves effectively, the memory that cerebral trauma, cerebrovascular accident, epilepsy sequela, carbon monoxide and alcohol or drug poisoning are caused and the disturbance of thought also effective in cure, be widely used in clinical at present.
The preparation method preparing Piracetam (piracetam) has multiple, comparative maturity and industrialized method be take pyrrolidone as starting raw material, through salify, condensation, reaction obtains N-pyrrolidone acetate, obtain product through aminating reaction again, preparation process is batch process procedures.
Summary of the invention
It is starting raw material with pyrrolidone that the purpose of this utility model is to provide a kind of, prepares the serialization preparation facilities of Piracetam (piracetam) intermediate N pyrrolidone acetate through salify, condensation.
the technical solution of the utility model is as follows:
A serialization preparation facilities for N-pyrrolidone acetate, described preparation facilities comprises: material mixer, tubular type salt-forming reactor, reactive distillation column, supplementary solvent mixing tank, tubular type condensation reactor, equipment room connection line, control instruments and annex; Material mixer, tubular type salt-forming reactor, to supplement solvent mixing tank, tubular type condensation reactor be tube type apparatus with or without chuck, and arranging in pipe or not arranging has the dynamic of disturbance mixing effect and static mixing element to material.
The serialization preparation facilities of described a kind of N-pyrrolidone acetate, described reactive distillation column or be conventional distillation still.
The utility model has the advantages that:
1. can make by pyrrolidone is that starting raw material prepares salify in Piracetam (piracetam) technique, condensation reaction N-pyrrolidone acetate realizes serialization and prepares.
2. adopt peripheral hardware chuck, inside establish tubular type salt-forming reactor and the tubular type condensation reactor of turbulent element, mass transfer effect is good, and fully, speed of response is fast in material contact; Heat-transfer effect is good, and temperature of reaction controls precisely, to be conducive to improving the quality of products.
3. adopt pipe reaction to combine with tower reactive distillation, can improve speed of response, the methyl alcohol that sharp separation goes out to generate, be conducive to reaction and carry out to positive dirction, reaction is carried out completely, good product quality, and raw material availability is high;
4. process operation is convenient stable, and preparation efficiency is high, and turndown ratio is large.
Accompanying drawing explanation
Accompanying drawing 1 is employing tubular type salt-forming reactor, reactive distillation column completes salt-forming reaction and separation of methanol; Tubular type tubular type condensation reactor is adopted to complete condensation reaction, the preparation facilities sketch of the obtained N-pyrrolidone acetate of serialization preparation.
Embodiment
Embodiment 1
The serialization preparation facilities of N-pyrrolidone acetate comprises material mixer 1, tubular type salt-forming reactor 2, reactive distillation column 3, supplements solvent mixing tank 4, tubular type condensation reactor 5, equipment room connection line, control instruments and annex.Material mixer 1, tubular type salt-forming reactor 2, supplementary solvent mixing tank 4, tubular type condensation reactor 5 are connected by straight tube and curved tube, fill the tube type apparatus of chemical filler in straight tube.
Embodiment 2
Embodiment 2 is substantially the same manner as Example 1, and difference is that material mixer 1, tubular type salt-forming reactor 2, supplementary solvent mixing tank 4, tubular type condensation reactor 5 straight length adopt commercially available static mixer, and curved tube section is blank pipe.
Embodiment 3
Embodiment 3 is substantially the same manner as Example 1, and difference is that in system, two strands of material meets arrange injector, aspirate another strand of material by one material.
Embodiment 4
Embodiment 4 is substantially the same manner as Example 1, and difference is with the still kettle surrogate response rectifying tower 3 with whipping appts.

Claims (2)

1. a serialization preparation facilities for N-pyrrolidone acetate, is characterized in that described device comprises material mixer (1), tubular type salt-forming reactor (2), reactive distillation column (3), supplements solvent mixing tank (4), tubular type condensation reactor (5), equipment room connection line, control instruments and annex; Material mixer (1), tubular type salt-forming reactor (2), to supplement solvent mixing tank (4), tubular type condensation reactor (5) be tube type apparatus with or without chuck, and arranging in pipe or not arranging has moving and static mixing element of disturbance mixing effect to material.
2. the serialization preparation facilities of a kind of N-pyrrolidone acetate according to claim 1, is characterized in that reactive distillation column (3) is for conventional distillation still.
CN201520110450.6U 2015-02-16 2015-02-16 A kind of serialization preparation facilities of N-pyrrolidone acetate Active CN204702685U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201520110450.6U CN204702685U (en) 2015-02-16 2015-02-16 A kind of serialization preparation facilities of N-pyrrolidone acetate

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201520110450.6U CN204702685U (en) 2015-02-16 2015-02-16 A kind of serialization preparation facilities of N-pyrrolidone acetate

Publications (1)

Publication Number Publication Date
CN204702685U true CN204702685U (en) 2015-10-14

Family

ID=54282317

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201520110450.6U Active CN204702685U (en) 2015-02-16 2015-02-16 A kind of serialization preparation facilities of N-pyrrolidone acetate

Country Status (1)

Country Link
CN (1) CN204702685U (en)

Similar Documents

Publication Publication Date Title
CN110003032B (en) Continuous preparation method of L-carnitine
CN103880672B (en) High-purity DHA algae oil ethyl ester and be converted into the preparation method of glyceride
AU2016272537A1 (en) Process for the preparation of intermediates useful in the preparation of non-ionic contrast agents
CN101205178B (en) Improved method for the production of unsaturated carboxylic acid anhydrides
CN102070448A (en) Method for preparing dimethyl succinate
CN104744423A (en) Method for continuously producing vinylene carbonate
CN105801408B (en) A kind of reaction and rectification device producing high purity acrylic acid N-butyl and method
CN105732354A (en) Method for synthesizing 2,2,4, 4-tetramethyl-1, 3-cyclobutanedione
CN204702685U (en) A kind of serialization preparation facilities of N-pyrrolidone acetate
CN102992975B (en) Method for continuously preparing glutaraldehyde
CN204661588U (en) A kind of device of continuous prodution vinylene carbonate
CN102126958A (en) Device and method for preparing high purity m/p-nitrotoluene by coupling rectification and crystallization
CN204702684U (en) A kind of aminating reaction Piracetam device continuously
CN103193636A (en) Method for synthetizing 2,3-butanediol ester
CN103387495A (en) Method for the continuous production of carboxylic acid esters
CN201981142U (en) Process device for producing dipropylene glycol and co-producing tripropylene glycol
CN104045087A (en) Device for preparing trichlorosilane
CN104693089A (en) Continuous preparation method of N-acetate pyrrolidone
CN106431908A (en) Ethyl trifluoroacetate preparation method
CN203513650U (en) Biodiesel production device
CN102838569B (en) Method for synthesizing peach aldehyde by using microreactor device
CN202415410U (en) Multi-tower continuous operation system device for synthesizing methyl 3,3-dimethyl pentenoate
CN105585468B (en) A method of cyclopentanone is prepared by raw material of cyclopentene
CN104387258A (en) Chloroacetic acid production method and chlorination reactor
CN105481685B (en) By phenol and the salicylic method of supercritical carbon dioxide one-step synthesis

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant