CN102389757A - Screwless reaction kettle - Google Patents

Screwless reaction kettle Download PDF

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Publication number
CN102389757A
CN102389757A CN2011103087520A CN201110308752A CN102389757A CN 102389757 A CN102389757 A CN 102389757A CN 2011103087520 A CN2011103087520 A CN 2011103087520A CN 201110308752 A CN201110308752 A CN 201110308752A CN 102389757 A CN102389757 A CN 102389757A
Authority
CN
China
Prior art keywords
reaction kettle
kettle body
nitrogen
screwless
reaction
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.)
Pending
Application number
CN2011103087520A
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Chinese (zh)
Inventor
陈从元
陈勇
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.)
JIANGDU XINGLONG POLYMER CHEMICAL CO Ltd
Original Assignee
JIANGDU XINGLONG POLYMER 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 JIANGDU XINGLONG POLYMER CHEMICAL CO Ltd filed Critical JIANGDU XINGLONG POLYMER CHEMICAL CO Ltd
Priority to CN2011103087520A priority Critical patent/CN102389757A/en
Publication of CN102389757A publication Critical patent/CN102389757A/en
Pending legal-status Critical Current

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Abstract

The invention discloses a screwless reaction kettle and relates to the technical field of manufacturing of reaction kettles. The screwless reaction kettle comprises a tapered reaction kettle body with a vertical axial line and a reaction kettle jacket, wherein the reaction kettle jacket is arranged on the outer side of the reaction kettle body; a feed port, a compressed air inlet, an initiator inlet and an exhaust port are formed at the upper end of the reaction kettle body; a discharge port is arranged at the lower end of the reaction kettle body; a discharge valve is arranged below the discharge port; a nitrogen-filling pipe is arranged on one side of the reaction kettle body and positioned between the discharge port and the discharge valve; and a nitrogen-filling valve is arranged on the body of the nitrogen-filling pipe. By virtue of the structural design and parameter configuration, the reaction kettle achieves the combined effect of natural heat release, cooling and low-temperature mixing. Owing to the screwless design, the energy consumption is reduced and the production cost is reduced.

Description

No spiro rod reaction still
Technical field
The present invention relates to agitated reactor manufacturing technology field.
Background technology
Agitated reactor is used for the reaction vessel of physics or chemistry, through structural design and the parameter configuration to container, realizes the function that is mixed of heating, evaporation, cooling and the low high speed of technological requirement.Traditional agitated reactor structure includes the upright cylindrical shape reaction kettle body of axis and an agitator that axially inserts in the kettle at present; Corrosivity in the course of reaction medium is high, and solid granulates is many, makes perishable, the wearing and tearing of agitator; And power consumption is big, has increased production cost.
Summary of the invention
The object of the invention is to traditional agitated reactor structural disadvantages, provide a kind of power consumption little, need not to change agitator, minimizing production cost, the no spiro rod reaction still that economizes on resources.
The present invention includes the upright taper reaction kettle body of axis, agitated reactor external jacket, said agitated reactor external jacket is nested with in the reaction kettle body outside; In said reaction kettle body upper end charging aperture, the import of pneumatics gas, initator import, drain are set respectively; In said reaction kettle body lower end discharging opening is set; Below said discharging opening, dispensing valve is set, the nitrogen air inlet pipe is filled in the kettle one side setting between said discharging opening and dispensing valve, on the said body that fills the nitrogen air inlet pipe, the nitrogen fill valve door is set.
The present invention is no screw design, and energy efficient reduces production costs.The present invention in course of reaction, opens the nitrogen fill valve door, through filling the nitrogen air inlet pipe nitrogen is sent in the agitated reactor, opens the drain valve, and oxygen is drained by drain, closes the drain valve.In oxygen-free environment, open charging aperture valve and initator imported valve; Material and initator are got in the reaction kettle body, after closing charging aperture valve and initator imported valve, let material and initator in agitated reactor, fully react; When material and initator fully reflect; In chuck, heat, reaction is opened the import of pneumatics gas after finishing, and utilizes air pressure that material is squeezed to discharging opening.The present invention realizes the natural heat release of technological requirement through structural design and parameter configuration to container, cooling and low-temperature mixed function, and the present invention is no screw design, energy efficient reduces production costs.
Description of drawings
Fig. 1 is a structural representation of the present invention.
Fig. 2 is the left view of Fig. 1.
The specific embodiment
Like Fig. 1, shown in 2, the present invention is provided with the upright taper reaction kettle body 1 of axis, agitated reactor external jacket 2, and agitated reactor external jacket 2 is nested with in reaction kettle body 1 outside; Charging aperture 3, pneumatics gas import 4, initator import 5, drain 6 are set respectively in reaction kettle body 1 upper end.
In reaction kettle body 1 lower end discharging opening 9 is set; Dispensing valve 10 is set below discharging opening 9, and nitrogen air inlet pipe 11 is filled in the kettle 1 one side settings between discharging opening 9 and dispensing valve 10, on the said body that fills nitrogen air inlet pipe 11, nitrogen fill valve door 12 is set.

Claims (1)

1. do not have the spiro rod reaction still, it is characterized in that: comprise the upright taper reaction kettle body of axis, agitated reactor external jacket, said agitated reactor external jacket is nested with in the reaction kettle body outside; In said reaction kettle body upper end charging aperture, the import of pneumatics gas, initator import, drain are set respectively, discharging opening are set in said reaction kettle body lower end; Below said discharging opening, dispensing valve is set, the nitrogen air inlet pipe is filled in the kettle one side setting between said discharging opening and dispensing valve, on the said body that fills the nitrogen air inlet pipe, the nitrogen fill valve door is set.
CN2011103087520A 2011-10-13 2011-10-13 Screwless reaction kettle Pending CN102389757A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2011103087520A CN102389757A (en) 2011-10-13 2011-10-13 Screwless reaction kettle

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2011103087520A CN102389757A (en) 2011-10-13 2011-10-13 Screwless reaction kettle

Publications (1)

Publication Number Publication Date
CN102389757A true CN102389757A (en) 2012-03-28

Family

ID=45857214

Family Applications (1)

Application Number Title Priority Date Filing Date
CN2011103087520A Pending CN102389757A (en) 2011-10-13 2011-10-13 Screwless reaction kettle

Country Status (1)

Country Link
CN (1) CN102389757A (en)

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1600795A (en) * 2003-09-27 2005-03-30 中国石油天然气股份有限公司 Method for preparing extra high molecular polymer of alpha olefin and equipment
CN101624364A (en) * 2009-08-06 2010-01-13 王传华 CTP synthesis technology of rubber scorch retarder and device thereof
CN201855696U (en) * 2010-07-28 2011-06-08 上海台界化工有限公司 Vertical type ethoxylation reactor
CN202007206U (en) * 2011-03-04 2011-10-12 东营顺通化工(集团)有限公司 Polyacrylamide pre-crosslinking colloidal particle production device

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1600795A (en) * 2003-09-27 2005-03-30 中国石油天然气股份有限公司 Method for preparing extra high molecular polymer of alpha olefin and equipment
CN101624364A (en) * 2009-08-06 2010-01-13 王传华 CTP synthesis technology of rubber scorch retarder and device thereof
CN201855696U (en) * 2010-07-28 2011-06-08 上海台界化工有限公司 Vertical type ethoxylation reactor
CN202007206U (en) * 2011-03-04 2011-10-12 东营顺通化工(集团)有限公司 Polyacrylamide pre-crosslinking colloidal particle production device

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Legal Events

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C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C02 Deemed withdrawal of patent application after publication (patent law 2001)
WD01 Invention patent application deemed withdrawn after publication

Application publication date: 20120328