CN105126704A - Pressurized feeding device - Google Patents

Pressurized feeding device Download PDF

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Publication number
CN105126704A
CN105126704A CN201510560405.5A CN201510560405A CN105126704A CN 105126704 A CN105126704 A CN 105126704A CN 201510560405 A CN201510560405 A CN 201510560405A CN 105126704 A CN105126704 A CN 105126704A
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CN
China
Prior art keywords
pressure
storage tank
pipeline
pipe
charging device
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
CN201510560405.5A
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Chinese (zh)
Inventor
吴亮
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.)
Fa Base Chemicals (zhangjiagang) Co Ltd
Original Assignee
Fa Base Chemicals (zhangjiagang) 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 Fa Base Chemicals (zhangjiagang) Co Ltd filed Critical Fa Base Chemicals (zhangjiagang) Co Ltd
Priority to CN201510560405.5A priority Critical patent/CN105126704A/en
Publication of CN105126704A publication Critical patent/CN105126704A/en
Pending legal-status Critical Current

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Abstract

The invention discloses a pressurized feeding device. The pressurized feeding device comprises a gas supercharging device and a storage tank. The gas supercharging device is equipped with a nitrogen source. The nitrogen source is connected with one end of a high-pressure pipe and one end of a blowing pipe through check valves. The other end of the high-pressure pipe is connected with the top of the storage tank. A feeding pipe and an exhaust pipe are arranged at the top of the storage tank. The bottom of the storage tank is connected with an input pipe. The input pipe is connected with the blowing pipe. An air hammer is arranged at the left side of the outer wall of the storage tank. The air hammer is connected with a compressed air pipe. The pressurized feeding device inputs calcium hydrate in the storage tank into a reaction vessel in a high pressure manner through nitrogen pressurization during the usage process, chlorine as a power supply does not participates in the reaction and can isolate the product from air, and the product quality is ensured. The inlet of the reaction vessel is a concentric reducer, calcium hydrate enters the reaction vessel from the inlet of the reaction vessel and is released from a high pressure to zero pressure, the effect of atomizing calcium hydrate is achieved and thus calcium hydrate cannot deposit at the bottom of the reaction vessel.

Description

A kind of pressurization charging device
Technical field
The invention belongs to chemical machinery field, be specifically related to a kind of pressurization charging device.
Background technology
In stearate production process, the calcium hydroxide of powdery and stearic acid react very fierce.If first calcium hydroxide is first added reactor again stearic acid is added reactor in actual production process, calcium hydroxide easily precipitates, and causes product defective; If first add stearic acid by reactor, re-use traditional dog-house and add calcium hydroxide, a large amount of steam can be released due to the violent of reaction in operation, make reactor be in barotropic state, so calcium hydroxide cannot add reactor.
Summary of the invention
For solving the problem, the invention discloses a kind of pressurization charging device, with by the problem solved.
For achieving the above object, technical scheme of the present invention is as follows:
A kind of pressurization charging device, comprise gas pressurized device, storage tank, described gas pressurized device arranges source nitrogen, described source nitrogen connects one end of pressure piping by check-valves and purges one end of pipeline, described pressure piping is connected at least 2 pressure charging valves, the other end of pressure piping connects storage tank top, and described pressure piping arranges high-pressure exhaust pipe, Bonding pressure instrument simultaneously, described high-pressure exhaust pipe arranges ball valve two; Described storage tank top arranges feed intake pipeline and discharge duct, the described pipeline that feeds intake connects dog-house, feed intake on pipeline and pressure interlock device is set, above described dog-house, dust cover is set, described discharge duct arranges filter bag, filter bag arranged outside ball valve five, connect feed pipe bottom described storage tank, described feed pipe one end coupled reaction still entrance, feed pipe is connected with purging pipeline, arrange pneumatic hammer on the left of described storage tank outer wall, described pneumatic hammer connects compressed air hose.
As a modification of the present invention, described manometer comprises pressure sensor and Pressure gauge.
As a modification of the present invention, described reactor entrance is concentric reducer.
As a modification of the present invention, the both sides of described feed pipe and scavenging conduit pipeline joint arrange ball valve three and ball valve four.
As a modification of the present invention, in described filter bag, removable cartridge is set.
As a modification of the present invention, described dust cover is connected with dog-house, is semitight.
As a modification of the present invention, described check-valves and pressure charging valve are opened, then feed intake pipeline and discharge duct closedown.
As a modification of the present invention, have pressure in described storage tank, then feed intake closedown of pipeline.
The invention has the beneficial effects as follows:
One pressurization charging device of the present invention, in the process used by nitrogen pressurization by the calcium hydroxide high input voltage reactor in storage tank, chlorine does not participate in reaction as power source and can by product and air insulated, ensures product quality; The entrance of reactor is concentric reducer, and calcium hydroxide enters reactor by the release of high pressure to zero pressure by reactor entrance, reaches the effect be atomized by calcium hydroxide, makes calcium hydroxide be deposited in Polycondensation Reactor and Esterification Reactor.
Accompanying drawing explanation
Fig. 1 is structural representation of the present invention.
Reference numerals list:
1. source nitrogen, 2. storage tank, 3. pressure piping, 4. purge pipeline, 5. dog-house, 6. feed intake pipeline, 7. dust cover, 8. discharge duct, 9. filter bag, 10. pressure sensor, 11. Pressure gauges, 12. high-pressure exhaust pipes, 13. feed pipes, 14. reactor entrances, 15. pressure charging valves, 16. check-valves, 17. pressure interlock devices, 18. ball valve one, 19. pneumatic hammers, 20. compressed air hoses, 21. ball valve two, 22. ball valve three, 23. ball valve four, 24. ball valves five.
Detailed description of the invention
Below in conjunction with the drawings and specific embodiments, illustrate the present invention further, following detailed description of the invention should be understood and be only not used in for illustration of the present invention and limit the scope of the invention.It should be noted that, the word "front", "rear" of use is described below, "left", "right", "up" and "down" refer to direction in accompanying drawing, word " interior " and " outward " refer to the direction towards or away from particular elements geometric center respectively.
As shown in the figure, a kind of pressurization charging device, comprise gas pressurized device, storage tank 2, described gas pressurized device arranges source nitrogen 1, and described source nitrogen 1 connects one end of pressure piping 3 by check-valves 16 and purges one end of pipeline 4, at least 2 pressure charging valves 15 that described pressure piping 3 is connected, the other end of pressure piping 3 connects storage tank 2 top, described pressure piping 3 arranges high-pressure exhaust pipe 12, simultaneously Bonding pressure instrument, described high-pressure exhaust pipe 12 arranges ball valve 2 21; Described storage tank 2 top arranges feed intake pipeline 6 and discharge duct 8, the described pipeline 6 that feeds intake connects dog-house 5, feed intake on pipeline 6 and pressure interlock device 17 is set, above described dog-house 5, dust cover 7 is set, described discharge duct 8 arranges filter bag 9, and filter bag 9 arranged outside ball valve 5 24, connects feed pipe 13 bottom described storage tank 2, described feed pipe 13 one end coupled reaction still entrance 14, feed pipe 13 is connected with purging pipeline 4.
As shown in the figure, arrange pneumatic hammer 19 on the left of storage tank 2 outer wall, pneumatic hammer 19 connects compressed air hose 20, by the setting of pneumatic hammer 19, fully can solve the phenomenon of the material bridging in storage tank 2.
As shown in the figure, described manometer comprises pressure sensor 10 and Pressure gauge 11, can detect the pressure in pressure piping 3 in time.
As shown in the figure, described reactor entrance 14 is concentric reducer, and material can enter reactor and fully atomization fast, and material can fully react.
As shown in the figure, described feed pipe 13 arranges ball valve 3 22 and ball valve 4 23 with the both sides purging pipeline 4 interface, guarantees feed pipe 13 safety under high pressure.
As shown in the figure, in described filter bag 9, removable cartridge is set, repeatedly can changes use.
As shown in the figure, described dust cover 7 is connected with dog-house 5, is semitight, effectively prevents dust recycling.
As shown in the figure, described check-valves 16 and pressure charging valve 15 are opened, then feed intake pipeline 6 and discharge duct 8 are closed, or have pressure in storage tank 2, then the pipeline 6 that feeds intake is closed, and ensure that the safety of workman in production process.
Technological means disclosed in the present invention program is not limited only to the technological means disclosed in above-mentioned embodiment, also comprises the technical scheme be made up of above technical characteristic.

Claims (8)

1. a pressurization charging device, it is characterized in that: comprise gas pressurized device, storage tank, described gas pressurized device arranges source nitrogen, described source nitrogen connects one end of pressure piping by check-valves and purges one end of pipeline, described pressure piping is connected at least 2 pressure charging valves, the other end of pressure piping connects storage tank top, and described pressure piping arranges high-pressure exhaust pipe, Bonding pressure instrument simultaneously, described high-pressure exhaust pipe arranges ball valve two; Described storage tank top arranges feed intake pipeline and discharge duct, the described pipeline that feeds intake connects dog-house, feed intake on pipeline and pressure interlock device is set, above described dog-house, dust cover is set, described discharge duct arranges filter bag, filter bag arranged outside ball valve five, connect feed pipe bottom described storage tank, described feed pipe one end coupled reaction still entrance, feed pipe is connected with purging pipeline, arrange pneumatic hammer on the left of described storage tank outer wall, described pneumatic hammer connects compressed air hose.
2. one pressurization charging device according to claim 1, is characterized in that: described manometer comprises pressure sensor and Pressure gauge.
3. one pressurization charging device according to claim 1, is characterized in that: described reactor entrance is concentric reducer.
4. one pressurization charging device according to claim 1, is characterized in that: the both sides of described feed pipe and scavenging conduit pipeline joint arrange ball valve three and ball valve four.
5. one pressurization charging device according to claim 1, is characterized in that: arrange removable cartridge in described filter bag.
6. one pressurization charging device according to claim 1, it is characterized in that: described dust cover is connected with dog-house, is semitight.
7. one pressurization charging device according to claim 1, is characterized in that: described check-valves and pressure charging valve are opened, then feed intake pipeline and discharge duct closedown.
8. one pressurization charging device according to claim 1, it is characterized in that: have pressure in described storage tank, then feed intake closedown of pipeline.
CN201510560405.5A 2015-09-07 2015-09-07 Pressurized feeding device Pending CN105126704A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201510560405.5A CN105126704A (en) 2015-09-07 2015-09-07 Pressurized feeding device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201510560405.5A CN105126704A (en) 2015-09-07 2015-09-07 Pressurized feeding device

Publications (1)

Publication Number Publication Date
CN105126704A true CN105126704A (en) 2015-12-09

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Application Number Title Priority Date Filing Date
CN201510560405.5A Pending CN105126704A (en) 2015-09-07 2015-09-07 Pressurized feeding device

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CN (1) CN105126704A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110694501A (en) * 2019-11-06 2020-01-17 广东奇乐趣食品科技有限公司 Temperature-controllable high-pressure liquid enzyme on-line feeding system
CN113713715A (en) * 2021-09-14 2021-11-30 河北万吉新材料科技有限公司 Liquid calcium zinc stabilizer production system

Citations (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN201190001Y (en) * 2008-04-30 2009-02-04 株洲硬质合金集团有限公司 Powder blanking system
CN201768551U (en) * 2010-08-25 2011-03-23 淄博德信联邦化学工业有限公司 Material supplementing device of reaction kettle
CN202429684U (en) * 2011-12-28 2012-09-12 四川美丰化工股份有限公司 Anti-bridging packaged powder hopper
CN202741127U (en) * 2012-07-30 2013-02-20 浙江佑谦特种材料有限公司 Air blowing device arranged at bottom of reaction kettle and used for preventing material accumulation and material accumulation preventing reaction kettle
CN203002330U (en) * 2012-12-26 2013-06-19 东莞市凯金电池材料有限公司 Blanking device for reaction furnace
CN203264680U (en) * 2013-05-06 2013-11-06 南通瑞普埃尔生物工程有限公司 PVDC (Polyvinyl Dichloride) charging device
CN103466332A (en) * 2013-08-26 2013-12-25 张家港保税区万盛机械工业有限公司 Dense-phase compressed gas delivery device
CN103566828A (en) * 2013-10-30 2014-02-12 安徽神剑新材料股份有限公司 Device for adding material into pressure vessel, and feeding method thereof
CN203648498U (en) * 2013-12-27 2014-06-18 四川贝恩能化工有限公司 Balanced flow proportion dosing device
CN104176503A (en) * 2013-05-22 2014-12-03 欧才权 Gap-discharging continuous vacuum feeding machine
CN104694380A (en) * 2015-03-26 2015-06-10 尹燕运 Solid state fermentation seed dressing tank
CN204996412U (en) * 2015-09-07 2016-01-27 发基化学品(张家港)有限公司 Material device is thrown in pressurization

Patent Citations (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN201190001Y (en) * 2008-04-30 2009-02-04 株洲硬质合金集团有限公司 Powder blanking system
CN201768551U (en) * 2010-08-25 2011-03-23 淄博德信联邦化学工业有限公司 Material supplementing device of reaction kettle
CN202429684U (en) * 2011-12-28 2012-09-12 四川美丰化工股份有限公司 Anti-bridging packaged powder hopper
CN202741127U (en) * 2012-07-30 2013-02-20 浙江佑谦特种材料有限公司 Air blowing device arranged at bottom of reaction kettle and used for preventing material accumulation and material accumulation preventing reaction kettle
CN203002330U (en) * 2012-12-26 2013-06-19 东莞市凯金电池材料有限公司 Blanking device for reaction furnace
CN203264680U (en) * 2013-05-06 2013-11-06 南通瑞普埃尔生物工程有限公司 PVDC (Polyvinyl Dichloride) charging device
CN104176503A (en) * 2013-05-22 2014-12-03 欧才权 Gap-discharging continuous vacuum feeding machine
CN103466332A (en) * 2013-08-26 2013-12-25 张家港保税区万盛机械工业有限公司 Dense-phase compressed gas delivery device
CN103566828A (en) * 2013-10-30 2014-02-12 安徽神剑新材料股份有限公司 Device for adding material into pressure vessel, and feeding method thereof
CN203648498U (en) * 2013-12-27 2014-06-18 四川贝恩能化工有限公司 Balanced flow proportion dosing device
CN104694380A (en) * 2015-03-26 2015-06-10 尹燕运 Solid state fermentation seed dressing tank
CN204996412U (en) * 2015-09-07 2016-01-27 发基化学品(张家港)有限公司 Material device is thrown in pressurization

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110694501A (en) * 2019-11-06 2020-01-17 广东奇乐趣食品科技有限公司 Temperature-controllable high-pressure liquid enzyme on-line feeding system
CN113713715A (en) * 2021-09-14 2021-11-30 河北万吉新材料科技有限公司 Liquid calcium zinc stabilizer production system

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Application publication date: 20151209

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