CN104147991A - Pre-reactor - Google Patents

Pre-reactor Download PDF

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Publication number
CN104147991A
CN104147991A CN201410386063.5A CN201410386063A CN104147991A CN 104147991 A CN104147991 A CN 104147991A CN 201410386063 A CN201410386063 A CN 201410386063A CN 104147991 A CN104147991 A CN 104147991A
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China
Prior art keywords
reactor
pipeline
pressure sensor
parallel
vacuum compensator
Prior art date
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Granted
Application number
CN201410386063.5A
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Chinese (zh)
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CN104147991B (en
Inventor
宣景建
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.)
Guangxi Zhongchang Resin Co Ltd
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Guangxi Zhongchang Resin Co Ltd
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Priority to CN201410386063.5A priority Critical patent/CN104147991B/en
Publication of CN104147991A publication Critical patent/CN104147991A/en
Application granted granted Critical
Publication of CN104147991B publication Critical patent/CN104147991B/en
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  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

The invention discloses a pre-reactor. The pre-reactor comprises a pre-reacting kettle, wherein the upper part of the pre-reacting kettle is connected with an alkaline solution tank through a pipeline, an outlet is formed in the bottom of the pre-reacting kettle, two openings at the upper part of the pre-reacting kettle are connected with a vacuum compensator in parallel through the pipeline, one end of the vacuum compensator is connected with a butterfly valve and a pressure sensor, and the two ends of the vacuum compensator are connected with a control valve and the pressure sensor in parallel. Compared with the prior art, the pre-reactor has the advantage that the problem that the aeration regulating function of the existing pre-reactor is difficult to meet technical requirements can be solved.

Description

Pre-reactor
Technical field
The present invention relates to chemical industry equipment manufacturing technology field, especially a kind of equipment for the pre-reaction of rosin based product.
Background technology
At present, in the process of manufacture of rosin based product, especially oxidizing process, needs to carry out pre-reaction, is exactly that pre-exposure regulates, and this is certainly to need aeration, large as much as possible in actual motion.If hydrolysis acidification, will see that front end water inlet situation considers whether to need aeration, even if need, can be not large yet, aeration rate is large can not meet anaerobic environment.And the existing pre-reactor for this pre-reaction, generally only include pre-reactor, pre-reactor top is connected with alkali liquid tank by pipeline, pre-reactor bottom is provided with outlet, with coupled reaction still, the top of pre-reactor is provided with pressure limiting valve and the Pressure gauge that is connected to pre-reactor inner space, and to carry out aerating regulation, such only rely on pressure limiting valve and Pressure gauge cannot meet the process requirements of aerating regulation far away.
Summary of the invention
Problem to be solved by this invention is to provide a kind of pre-reactor, to solve the more difficult problem that meets technological requirement of pre existing reactor aerating regulation function.
In order to address the above problem, technical scheme of the present invention is: this pre-reactor includes pre-reactor, described pre-reactor top is connected with alkali liquid tank by pipeline, described pre-reactor bottom is provided with outlet, two openings on the top of described pre-reactor are parallel with a vacuum compensator by pipeline, one end of described vacuum compensator is connected with butterfly valve and pressure sensor, and the two ends of described vacuum compensator are parallel with control valve and pressure sensor.
Owing to having adopted technique scheme, the present invention compared with prior art has following beneficial effect:
This pre-reactor is parallel with a vacuum compensator by two openings of two place's opening parts at an upper portion thereof by pipeline, be parallel with control valve and pressure sensor with the two ends of vacuum compensator, can make aeration under vacuum state, complete completely, reach the technological requirement of pre-reaction, and can finely must regulate aeration rate, especially the in the situation that of larger aeration rate.This pre-reactor is to needing the oxidation reaction that aeration rate is larger to have good adaptability.
Accompanying drawing explanation
Fig. 1 is the front view of the embodiment of the present invention.
The specific embodiment
Below in conjunction with accompanying drawing, the embodiment of the present invention is described in further detail:
Pre-reactor as shown in Figure 1, it includes pre-reactor 1, and pre-reactor 1 top is connected with alkali liquid tank 2 by pipeline, and the port of export of alkali liquid tank 2 is connected with butterfly valve and pressure sensor 4.Pre-reactor 1 bottom is provided with outlet 7, and this outlet 7 is with coupled reaction still.Two openings on the top of pre-reactor 1 are parallel with a vacuum compensator 5 by pipeline 3, one end of vacuum compensator 5 is connected with butterfly valve and pressure sensor 4, the two ends of vacuum compensator 5 are parallel with control valve and pressure sensor 6, the control valve here and pressure sensor 6 are connected on the pipeline and parallel pipeline 8 of the other end of vacuum compensator 5, and control valve can be selected the control valve of threeway.Can make like this aeration under vacuum state, complete completely, reach the technological requirement of pre-reaction, and can finely must regulate aeration rate, especially the in the situation that of larger aeration rate.

Claims (1)

1. a pre-reactor, include pre-reactor, described pre-reactor top is connected with alkali liquid tank by pipeline, described pre-reactor bottom is provided with outlet, it is characterized in that: two openings on the top of described pre-reactor are parallel with a vacuum compensator by pipeline, one end of described vacuum compensator is connected with butterfly valve and pressure sensor, and the two ends of described vacuum compensator are parallel with control valve and pressure sensor.
CN201410386063.5A 2014-08-07 2014-08-07 Pre-reactor Active CN104147991B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201410386063.5A CN104147991B (en) 2014-08-07 2014-08-07 Pre-reactor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201410386063.5A CN104147991B (en) 2014-08-07 2014-08-07 Pre-reactor

Publications (2)

Publication Number Publication Date
CN104147991A true CN104147991A (en) 2014-11-19
CN104147991B CN104147991B (en) 2016-10-26

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN201410386063.5A Active CN104147991B (en) 2014-08-07 2014-08-07 Pre-reactor

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CN (1) CN104147991B (en)

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2005036985A1 (en) * 2003-10-22 2005-04-28 Carlos Cummings Ibarra Improved nixtamalization method and device and different uses thereof
CN1730584A (en) * 2005-08-10 2006-02-08 张昌荣 Light and ordorless colophony and its production method
CN102325636A (en) * 2009-02-27 2012-01-18 普瑞曼聚合物株式会社 Injection foam molding method and apparatus therefor
CN102337078A (en) * 2011-07-07 2012-02-01 景东力奥林产集团林业化工有限公司 Production process for rosin resin
CN203525352U (en) * 2013-07-19 2014-04-09 山东天兴生物科技有限公司 Dimethyl sebacate rectifying and vacuumizing device

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2005036985A1 (en) * 2003-10-22 2005-04-28 Carlos Cummings Ibarra Improved nixtamalization method and device and different uses thereof
CN1730584A (en) * 2005-08-10 2006-02-08 张昌荣 Light and ordorless colophony and its production method
CN102325636A (en) * 2009-02-27 2012-01-18 普瑞曼聚合物株式会社 Injection foam molding method and apparatus therefor
CN102337078A (en) * 2011-07-07 2012-02-01 景东力奥林产集团林业化工有限公司 Production process for rosin resin
CN203525352U (en) * 2013-07-19 2014-04-09 山东天兴生物科技有限公司 Dimethyl sebacate rectifying and vacuumizing device

Also Published As

Publication number Publication date
CN104147991B (en) 2016-10-26

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