CN204275957U - A kind of Special reverse for pivaloyl chloride production answers flow container - Google Patents

A kind of Special reverse for pivaloyl chloride production answers flow container Download PDF

Info

Publication number
CN204275957U
CN204275957U CN201420763399.4U CN201420763399U CN204275957U CN 204275957 U CN204275957 U CN 204275957U CN 201420763399 U CN201420763399 U CN 201420763399U CN 204275957 U CN204275957 U CN 204275957U
Authority
CN
China
Prior art keywords
flow container
pivaloyl chloride
chloride production
pipeline
special reverse
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.)
Expired - Fee Related
Application number
CN201420763399.4U
Other languages
Chinese (zh)
Inventor
李建峰
张爱增
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.)
HEBEI GUOCHEN CHEMICAL Co Ltd
Original Assignee
HEBEI GUOCHEN CHEMICAL Co Ltd
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 HEBEI GUOCHEN CHEMICAL Co Ltd filed Critical HEBEI GUOCHEN CHEMICAL Co Ltd
Priority to CN201420763399.4U priority Critical patent/CN204275957U/en
Application granted granted Critical
Publication of CN204275957U publication Critical patent/CN204275957U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Abstract

A kind of Special reverse for pivaloyl chloride production answers flow container, reaction flow container comprises the anti-corrosion layer of outer field heat-insulation layer and internal layer, the bottom of described reaction flow container is provided with jet chimney, steam inlet channel is provided with non-return valve, non-return valve top is provided with aeration sieve, described reaction flow container top is provided with methylpropanoic acid pipeline and phosphorus trichloride pipeline respectively, methylpropanoic acid pipeline and phosphorus trichloride conduit upper are provided with steam fog sieve, reactant liquor tank top is provided with blast pipe, blast pipe is connected with rectifying liquid pipe by magnetic valve, is also provided with electric heating sheets between described heat-insulation layer and anti-corrosion layer.

Description

A kind of Special reverse for pivaloyl chloride production answers flow container
Technical field
The utility model relates to a kind of pivaloyl chloride production equipment, especially relates to a kind of Special reverse for pivaloyl chloride production and answers flow container.
Background technology
Pivaloyl chloride is a kind of important acylating reagent; it has been widely used in the various medicine of synthesis and Pesticidal products; simultaneously it also can be used for synthetic polymer initator; in general; synthesis pivaloyl chloride needs isobutene and carbon monoxide to synthesize pivalic acid, and carries out chlorination reaction to it, generates chloro-pivalyl chloride; and then carry out rectifying generation finished product, above-mentioned operation needs special reaction flow container to adapt to above-mentioned reaction.
Utility model content
In order to overcome above-mentioned technical problem, the utility model provides a kind of Special reverse for pivaloyl chloride production and answers flow container, and the technical scheme of employing is as follows:
A kind of Special reverse for pivaloyl chloride production answers flow container, reaction flow container comprises the anti-corrosion layer of outer field heat-insulation layer and internal layer, the bottom of described reaction flow container is provided with jet chimney, steam inlet channel is provided with non-return valve, non-return valve top is provided with aeration sieve, described reaction flow container top is provided with methylpropanoic acid pipeline and phosphorus trichloride pipeline respectively, methylpropanoic acid pipeline and phosphorus trichloride conduit upper are provided with steam fog sieve, reactant liquor tank top is provided with blast pipe, blast pipe is connected with rectifying liquid pipe by magnetic valve, is also provided with electric heating sheets between described heat-insulation layer and anti-corrosion layer.
Further, described methylpropanoic acid pipeline and phosphorus trichloride pipeline are equipped with non-return valve.
Further, described heat-insulation layer adopts expanded polyethylene foam material, and described anti-corrosion layer adopts graphite material.
Further, described aeration sieve adopts glass fibre establishment.
The above-mentioned Special reverse for pivaloyl chloride production is adopted to answer flow container, vapours can be utilized to replace mixing plant, and there is heat due to steam itself, make heating liquid more even, accelerate the reaction time, the gas that blast pipe is discharged can be directly used in rectifying.
Accompanying drawing explanation
Fig. 1 is the structural representation that a kind of Special reverse for pivaloyl chloride production answers flow container.
Detailed description of the invention
A kind of Special reverse for pivaloyl chloride production answers flow container as shown in Figure 1, reaction flow container comprises the anti-corrosion layer 2 of outer field heat-insulation layer 1 and internal layer, heat-insulation layer 1 adopts expanded polyethylene foam material, anti-corrosion layer 2 adopts graphite material, the bottom of described reaction flow container is provided with jet chimney 5, jet chimney 5 entrance is provided with non-return valve 6, non-return valve 6 top is provided with the aeration sieve 7 adopting glass fibre establishment, described reaction flow container top is provided with the methylpropanoic acid pipeline 3 and phosphorus trichloride pipeline 4 with non-return valve respectively, methylpropanoic acid pipeline 3 and phosphorus trichloride pipeline 4 top are provided with steam fog sieve 12, reactant liquor tank top is provided with blast pipe 9, blast pipe 9 is connected with rectifying liquid pipe 11 by magnetic valve 10, electric heating sheets 8 is also provided with between described heat-insulation layer 1 and anti-corrosion layer 2.
The above, be only detailed description of the invention of the present utility model, and those of ordinary skill in the art are in the scope that the utility model discloses, and the change that can expect easily, within the protection domain that all should be encompassed in utility model.

Claims (4)

1. answer flow container for the Special reverse of pivaloyl chloride production for one kind, it is characterized in that reaction flow container comprises the anti-corrosion layer of outer field heat-insulation layer and internal layer, the bottom of described reaction flow container is provided with jet chimney, steam inlet channel is provided with non-return valve, non-return valve top is provided with aeration sieve, described reaction flow container top is provided with methylpropanoic acid pipeline and phosphorus trichloride pipeline respectively, methylpropanoic acid pipeline and phosphorus trichloride conduit upper are provided with steam fog sieve, reactant liquor tank top is provided with blast pipe, blast pipe is connected with rectifying liquid pipe by magnetic valve, also electric heating sheets is provided with between described heat-insulation layer and anti-corrosion layer.
2. a kind of Special reverse for pivaloyl chloride production answers flow container as claimed in claim 1, it is characterized in that described methylpropanoic acid pipeline and phosphorus trichloride pipeline are equipped with non-return valve.
3. a kind of Special reverse for pivaloyl chloride production answers flow container as claimed in claim 1 or 2, and it is characterized in that described heat-insulation layer adopts expanded polyethylene foam material, described anti-corrosion layer adopts graphite material.
4. a kind of Special reverse for pivaloyl chloride production answers flow container as claimed in claim 1 or 2, it is characterized in that described aeration sieve adopts glass fibre establishment.
CN201420763399.4U 2014-12-08 2014-12-08 A kind of Special reverse for pivaloyl chloride production answers flow container Expired - Fee Related CN204275957U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201420763399.4U CN204275957U (en) 2014-12-08 2014-12-08 A kind of Special reverse for pivaloyl chloride production answers flow container

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201420763399.4U CN204275957U (en) 2014-12-08 2014-12-08 A kind of Special reverse for pivaloyl chloride production answers flow container

Publications (1)

Publication Number Publication Date
CN204275957U true CN204275957U (en) 2015-04-22

Family

ID=52859157

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201420763399.4U Expired - Fee Related CN204275957U (en) 2014-12-08 2014-12-08 A kind of Special reverse for pivaloyl chloride production answers flow container

Country Status (1)

Country Link
CN (1) CN204275957U (en)

Similar Documents

Publication Publication Date Title
WO2012054798A3 (en) Methods and systems for the production of hydrocarbon products
CN206285902U (en) Slurry is set at the uniform velocity to flow out the device of agitator tank
CN204275957U (en) A kind of Special reverse for pivaloyl chloride production answers flow container
CN105886393A (en) Sequencing batch type dry anaerobic digestion device of kitchen wastes
CN204448004U (en) A kind of reactor
CN204286164U (en) The double-deck condenser of a kind of hollow type
CN203448102U (en) Gas-liquid spraying circulating reaction device for preparing glyoxylic acid by oxygen oxidization method
CN203448100U (en) Residue circulating reaction device for preparing glyoxylic acid by oxygen oxidization method
CN204934145U (en) Based on the gas purging power set improving liquid feeding pipe cleannes
CN206033374U (en) Anaerobic system tank structure
CN205146201U (en) Reation kettle scour protection material device
CN204996437U (en) Chemical industry reation kettle structure
CN204193896U (en) A kind ofly fast reaction can be realized and the reactor of discharging
CN204275751U (en) A kind of novel Quick gas-liquid separator
CN204275543U (en) For the rectifying column of the consummate preparation of pivaloyl chloride
CN204934144U (en) The gas purge system of liquid feeding pipe
CN204324879U (en) A kind of logical oxygen device for the production of phosphorus oxychloride
CN204237554U (en) A kind of carbon monoxide conversion device
CN204417301U (en) A kind of integral septic tank
CN204017843U (en) A kind of two switching reactors with inner coil pipe
CN202657971U (en) Novel device for producing ammonium carbonate by using carbon dioxide
CN201815283U (en) Reaction kettle with discharging nozzles
CN206027676U (en) Gas, fuel rapidly synthesizing ware
CN205495564U (en) Chemical industry reaction
CN204841648U (en) Reation kettle is used in titanium dioxide production

Legal Events

Date Code Title Description
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20150422

Termination date: 20151208

EXPY Termination of patent right or utility model