CN201711152U - Hydrolysis reactor - Google Patents
Hydrolysis reactor Download PDFInfo
- 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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- hydrolysis reactor
- blind flange
- flange
- cylinder body
- organic matter
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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
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 |
|
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).
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)
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 |
-
2010
- 2010-06-29 CN CN2010202407077U patent/CN201711152U/en not_active Expired - Lifetime
Cited By (2)
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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Legal Events
Date | Code | Title | Description |
---|---|---|---|
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 |