CN201711152U - Hydrolysis reactor - Google Patents

Hydrolysis reactor Download PDF

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Publication number
CN201711152U
CN201711152U CN2010202407077U CN201020240707U CN201711152U CN 201711152 U CN201711152 U CN 201711152U CN 2010202407077 U CN2010202407077 U CN 2010202407077U CN 201020240707 U CN201020240707 U CN 201020240707U CN 201711152 U CN201711152 U CN 201711152U
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CN
China
Prior art keywords
hydrolysis reactor
blind flange
flange
cylinder body
organic matter
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 - Lifetime
Application number
CN2010202407077U
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Chinese (zh)
Inventor
梁显军
王仁龙
白云岭
刘朋
张洪军
李军
胡瑞珂
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 ORIENT TITANIUM INDUSTRY Co Ltd
Original Assignee
SHENYANG ORIENT TITANIUM INDUSTRY 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 SHENYANG ORIENT TITANIUM INDUSTRY Co Ltd filed Critical SHENYANG ORIENT TITANIUM INDUSTRY Co Ltd
Priority to CN2010202407077U priority Critical patent/CN201711152U/en
Application granted granted Critical
Publication of CN201711152U publication Critical patent/CN201711152U/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Abstract

The utility model relates to a hydrolysis reactor. The hydrolysis reactor adopts the technical scheme as follows: a closed reaction vessel is formed by a lower sealing head (2), a lower cylinder body (3), a pyramidal segment (4), an upper cylinder body (12), a flange (7) and a blind flange (8); the bottom part of the lower sealing head (2) is connected with a support connecting pipe (13) which is connected with an organic matter inlet (1) and an acid water inlet (14); a spare opening (15), a temperature meter opening (9), a stirrer connecting port (10) and a hydrolyzate outlet (11) are arranged on the blind flange (8); and two support lugs (5) are uniformly arranged outside the upper cylinder body (12). The hydrolysis reactor has the advantages of low cost, high output and benefit of environmental protection.

Description

Hydrolysis reactor
Technical field
The invention relates to a kind of reactor, relates to a kind of novel high-tech material---organosilyl hydrolysis reactor that is used to produce particularly.
Background technology
Organosilicon product unique properties, superior, the progress of production technology have been developed its potential in fields such as building, electronics, automobile, health products, more and more are applied to people's life.
At present, the market share of organosilicon 80% is controlled in the external manufacturer hand, and Chinese organosilicon industry still is in the growth stage.The existing equipment that domestic each organosilicon production firm adopts in use just mixes before organic matter and sour water enter reactor, causes the reaction of organic matter and sour water insufficient, makes the output of hydrolysate organosiloxane descend greatly.
What the equipment of prior art adopted is azeotropic acid hydrolysis technology, and first can produce a large amount of spent acid and waste water, is unfavorable for environmental protection.Second dissolves a large amount of siloxanes in sour water makes the output of final hydrolysate reduce greatly, does not reach expected effect, thereby can increase production cost.
Because agitator speed is inhomogeneous, monitoring temperature is unreasonable, make that reaction is insufficient in addition, yield poorly, of poor quality.
Summary of the invention
In order to overcome the above problems, the invention provides that a kind of cost is low, output is high, is beneficial to the hydrolysis reactor of environmental protection.
To achieve these goals, the technical scheme of the invention employing is: a kind of hydrolysis reactor: form an airtight reaction vessel by low head, lower shell, awl section, upper shell, flange and blind flange; The low head bottom connects to support to be taken over, and supports to take over the organic matter inlet to be connected with the sour water inlet, and blind flange is provided with standby mouth, thermometer mouth, agitator connector and hydrolysate outlet, and the even cloth in the upper shell outside is provided with two support ear seats.
Among the present invention, can effectively reduce organosilyl production cost, realize the effect of energy-saving and emission-reduction, the adjusting of mainly taking active carbon adsorption or polystyrene-based resin adsorption method to control speed, time and the temperature of stirring simultaneously reaches the content that reduces siloxanes in the sour water, this device adopts and stirs the PROCESS FOR TREATMENT hydrolysate, content of siloxane can be reduced to below 5/10000ths in lower floor's sour water, and most of siloxanes is directly separated out and is dissolved in hydrolysate, avoid the loss of siloxanes, can improve hydrolysate yield 0.5%~1.5%.
The key technical indexes such as the table 1 of the invention.
Table 1 the key technical indexes
Project Container
Maximum working pressure MPa Normal pressure
Design pressure MPa 0.3
The most high/low operating temperature ℃ 70
Design temperature ℃ 95
Name of material Organic component
Material characteristic Inflammable, moderate harm
Corrosion allowance mm 1
Hydraulic test pressure MPa 0.375
Air tight test pressure MPa -
AB class weld joint efficiency 0.85
Total volume m 2 ~0.07
The beneficial effect of the invention is:
1, the invention is provided with one in the end socket bottom and takes over assembly, taking over assembly is made up of organic matter inlet, sour water inlet and support adapter, can make the fully reaction in reactor of organic matter and sour water, prevent that organic matter and sour water from mixing before entering reactor.Support the effect of playing choked flow and support of taking over.
2, the technology of saturated acid hydrolysis (active carbon adsorption or polystyrene-based resin adsorption method) is adopted in the invention, has replaced original azeotropic acid hydrolysis technology, and no spent acid and waste water produce, not only economy but also environmental protection.
3, the invention is with short production cycle, has improved organosilyl output.
4, the invention is provided with the agitator connector and is used to install agitator, and two kinds of materials are fully reacted.
Description of drawings
Fig. 1: the structural representation of the invention
The vertical view of Fig. 2: Fig. 1
The specific embodiment
Shown in Fig. 1~2, a kind of hydrolysis reactor: form an airtight reaction vessel by low head (2), lower shell (3), awl section (4), upper shell (12), flange (7) and blind flange (8); Low head (2) bottom connects to support takes over (13), supporting adapter (13) is connected with organic matter inlet (1) and sour water inlet (14), for the equipment operation needs, blind flange (8) is provided with standby mouthful of (15) and thermometer mouth (9), in order to monitoring at any time in equipment running process; For making organic matter fully reaction in reactor, on blind flange (8), offer agitator connector (10), be used to install agitator and make the organic matter can sufficient reacting; Offer hydrolysate outlet (11) on blind flange (8), normally move for guaranteeing equipment, the even cloth in upper shell (12) outside is provided with two support ear seats (5), is used to support entire equipment.
Used material:
Low head (2), lower shell (3), awl section (4), upper shell (12) are UNS N10675; Flange (7) and blind flange (8) are made up of Q345R and UNS N10675; Organic matter inlet (1), sour water inlet (14) and support are taken over (13) and are made up of Q345R and UNS N10675, standby mouthful of (15) and thermometer mouth (9), agitator connector (10), hydrolysate outlet (11) are made up of Q345R and UNS N10675, and two support ear seats (5) are made up of Q345R and UNS N10675.
The operation principle of the invention is: organic matter and sour water enter in the closed reaction vessel that is formed by low head (2), lower shell (3), awl section (4), upper shell (12), flange (7), blind flange (8) assembly welding from the end socket bottom; By agitator connector (10) agitator being installed stirs, two kinds of materials are fully reacted, thermometer mouth (9) is set on blind flange (8) simultaneously is used for monitoring at any time temperature reactor in, form hydrolysate at last and export (11) by the hydrolysate of offering on the blind flange (8) and enter down program one.

Claims (1)

1. a hydrolysis reactor is characterized in that: form an airtight reaction vessel by low head (2), lower shell (3), awl section (4), upper shell (12), flange (7) and blind flange (8); Low head (2) bottom connects to support takes over (13), supporting adapter (13) is connected with organic matter inlet (1) and sour water inlet (14), blind flange (8) is provided with standby mouthful of (15), thermometer mouth (9), agitator connector (10) and hydrolysate outlet (11), and the even cloth in upper shell (12) outside is provided with two support ear seats (5).
CN2010202407077U 2010-06-29 2010-06-29 Hydrolysis reactor Expired - Lifetime CN201711152U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2010202407077U CN201711152U (en) 2010-06-29 2010-06-29 Hydrolysis reactor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2010202407077U CN201711152U (en) 2010-06-29 2010-06-29 Hydrolysis reactor

Publications (1)

Publication Number Publication Date
CN201711152U true CN201711152U (en) 2011-01-19

Family

ID=43457147

Family Applications (1)

Application Number Title Priority Date Filing Date
CN2010202407077U Expired - Lifetime CN201711152U (en) 2010-06-29 2010-06-29 Hydrolysis reactor

Country Status (1)

Country Link
CN (1) CN201711152U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101862634A (en) * 2010-06-29 2010-10-20 沈阳东方钛业有限公司 Hydrolysis reactor

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101862634A (en) * 2010-06-29 2010-10-20 沈阳东方钛业有限公司 Hydrolysis reactor
CN101862634B (en) * 2010-06-29 2012-11-14 沈阳东方钛业有限公司 Hydrolysis reactor

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C14 Grant of patent or utility model
GR01 Patent grant
AV01 Patent right actively abandoned

Granted publication date: 20110119

Effective date of abandoning: 20130227

RGAV Abandon patent right to avoid regrant