CN1299806A - Method of reducing vibration and fault of vertical centrifuge in production of p-benzene dicarboxylic acid - Google Patents
Method of reducing vibration and fault of vertical centrifuge in production of p-benzene dicarboxylic acid Download PDFInfo
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- CN1299806A CN1299806A CN 00134397 CN00134397A CN1299806A CN 1299806 A CN1299806 A CN 1299806A CN 00134397 CN00134397 CN 00134397 CN 00134397 A CN00134397 A CN 00134397A CN 1299806 A CN1299806 A CN 1299806A
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Abstract
The method for reducing vibration of vertical centrifuge and its failure in the production of terephthalic acid includes the following steps: 1. setting alkali pipe; 2. isolating centrifuge from system; 3. making centrifuge and oil system continuously operate; 4. washing with alkali liquor; and 5. after the alkali liquor is cleaned, the centrifuge can be fed into system to operate. The adoption of said method only needs 40 min to treat centrifuge once, and the maintenance period of said centrifuge can be elongated to one year from 1-2 months.
Description
The present invention relates to the vertical centrifugal machine in a kind of terephthalic acid (PTA) production unit.
PTA is the pure terephthalic acid, and it is the important source material that chemical fibre is produced, and requires PTA to reach quite high purity, and the quality of PTA quality product directly has influence on the fiber product quality.The rerum natura of PTA product and impurity thereof has determined that the production operation difficulty is big, ramming material is easily stifled, and it is short to cause that very easily the PTA device is removed the key equipment vertical centrifugal machine vibration height of impurity, work-ing life, influences separating effect, and the impurity paratolunitrile enters product.In a single day whizzer breaks down, and at first is that system loading descends significantly, and after the fault, all the other whizzer burdens cause easily that also vibration is high, damage equipment, and impurity has little time to separate in the PTA material, exceeds standard.Be that CCS casual clearing station maintenance difficulty is big, the time is long, success ratio is low once more, vibration cause is not clear, spare part expense height.We are being with this problem to visit similar a few family PTA factory, have similar problem too and do not have good processing means.Check pertinent data, the whizzer vibration problem can only be by the method for the relevant pipeline of online washing or steaming out, the clear material of lifting main rotor, but all can not deal with problems, and whizzer operation for some time after vibration progressively rises, uncontrollable, time length must cause equipment thoroughly to damage.The whizzer cycle of operation is short is perplexing always that the PTA device is stable, long-term operation.
Purpose of the present invention is exactly the problem at above existence, and analysis and research are found out and caused the high key factor of vibration, and the method that a kind of cost is low, equipment changed vertical centrifugal machine vibration and fault in little, the effective minimizing Production of Terephthalic Acid is provided.
According to analysis and research, causing the high major cause of vibration is owing to whizzer system rotor inside, base bearing, blanking tube, discharge port, mother liquor pipe etc. locate all to have knot wall material, causes the whizzer unbalance stress of high speed rotating, causes vibration.
Therefore technical solution of the present invention is proposed.
A kind of method that reduces vibration of vertical centrifugal machine in the Production of Terephthalic Acid and fault, it is to be heated to 70-100 ℃ with the diluted alkaline NaOH solution (5%m/m) that device itself provides, and enters the whizzer system, considers Na
+Can have a strong impact on quality product, need whizzer that vibration is high and system to isolate before advancing alkali, pressure release cuts out, guarantee that this each position of whizzer system all has hot alkaline solution to pass through, the PTA and the paratolunitrile reaction of piling up with each position fully makes the ramming material equipment that comes off, discharge residual alkali lye, para-phthalic sodium and knot wall material in the washing process continuously, after alkali lye has washed, switch to the water flushing, increasing temperature and pressure incision system operation then.Concrete method is:
1. configuration alkali pipe: drench valve and bearing washpipe from feed-pipe and drench valve and insert liquid caustic soda and enter pipe, with steam heating 5% (m/m) NaOH solution to 70-100 ℃.
2. vertical centrifugal machine and system isolate: steam off valve, feed valve, mother liquor valve, bleeder valve, bearing flush valve and making beating water valve, open that the mother liquor pipe drenches valve and valve is drenched in discharging, pressure release.
3. main frame and oil system continue to run well by it.
4. liquid caustic soda flushing: drench valve and bearing washpipe from feed-pipe and drench liquid caustic soda that valve inserts and enter pipe and advance hydrothermal solution alkali, open the mother liquor pipe and drench valve, arrange raffinate and piece material continuously.Assurance is drenched unimpeded, closes the mother liquor pipe then and drenches valve, and raffinate drenches the valve discharging from discharging, and washing discharging cylindrical shell, base bearing stop feed liquor alkali after washing finishes.
5. enter system's operation: after raffinate drains only in the system, open rinse water valve and bearing rinse water valve slightly, will cut off the water after the alkali lye displacement totally, close rinse water valve and bearing rinse water valve, close all and drench valve, open steam valve, incision system operation after the increasing temperature and pressure.
Adopt the advantage of method of the present invention to be:
1, easy to operate, used this device of alkali just has, and main process equipment is not done any action.
2, present method is handled and be need not cost basically, once only needs 5 tons of diluted alkalines to get final product.
3, finish whole process time weak point, only need 40 minutes, want 10 hours at least and overhaul a bench centrifuge.
4, effective, considerable benefit is handled and once can be kept steady running in 1.5 months at least, and few maintenance is (the maintenance spare part takes not very) once, increases 14.5tPTA product at least.
The present invention is applicable to the high problem of the inside and outside PTA production technique processing of host country vertical centrifugal machine vibration, prolongs its cycle of operation, improves the quality of products.
Fig. 1 is a vertical centrifugal machine synoptic diagram of the present invention.
Specify the present invention by the following examples.
Vertical centrifugal machine during embodiment 1 PTA produces, do not change main frame, only drenching valve 11 and bearing washpipe from feed-pipe drenches valve 5 and inserts liquid caustic soda and enter pipe, when finding that three-dimensional whizzer vibration is bigger, when need handling, with the NaOH solution of steam heating 5% (m/m) to 70-100 ℃, steam off valve 1, feed valve 10, mother liquor valve 2, bleeder valve 7, bearing rinse water valve 4 and making beating water valve, open that the mother liquor pipe drenches valve 3 and valve 6, pressure release are drenched in discharging.Three-dimensional whizzer and oil system continue to run well, and drench valve 11 and the bearing washpipe drenches the liquid caustic soda that valve 5 advances heat from feed-pipe, open variable valve 8 handwheels, and flow control is at 10-15m
3/ h, mother liquor pipe drench valve 3 row's raffinate and piece material continuously, and assurance is drenched unimpeded, close the mother liquor pipe after 15 minutes and drench valve 3, and raffinate drenches valve 6 dischargings from discharging, and washing discharging cylindrical shell, base bearing stopped liquid caustic soda after 15 minutes.
Raffinate is opened rinse water valve 9 and bearing rinse water valve 4 after draining only slightly in the system, and alkali is cut off the water after being replaced totally, closes rinse water valve 9 and bearing rinse water valve 4, closes all and drenches valve, drives steam valve 1 into, incision system operation after the increasing temperature and pressure.
This method is after this device is used, handled once in every 1.5-2 month, the whizzer turnaround the longlyest was extended down to 1 year by original 1-2 month, for PTA device high loading, long period, steady running have solved significant problem (separate unit whizzer processing ability is 15-20TPTA/H).
Claims (3)
1. method that reduces vibration of vertical centrifugal machine in the Production of Terephthalic Acid and fault is characterized in that the following step is arranged:
(1) configuration alkali pipe: drench valve (11) and bearing washpipe from feed-pipe and drench valve (5) access liquid caustic soda and enter pipe
(2) vertical centrifugal machine and system isolate: steam off valve (1), feed valve (10), mother liquor valve (2), bleeder valve (7), bearing rinse water valve (4) and making beating water valve, open that the mother liquor pipe drenches valve (3) and valve (6), pressure release are drenched in blanking
(3) whizzer main frame and oil system continue to run well by it
(4) liquid caustic soda flushing: drench liquid caustic soda that valve (11) and bearing washpipe drench valve (5) access from feed-pipe and enter pipe and advance hydrothermal solution alkali, change the mother liquor pipe and drench valve (3), arrange raffinate and piece material continuously, guarantee to drench unobstructed, close the mother liquor pipe then and drench valve (3), raffinate drenches valve (6) discharging from discharging, and washing discharging cylindrical shell, base bearing stop feed liquor alkali after washing finishes
(5) incision system operation: after raffinate drains only in the system, open rinse water valve (9) and bearing rinse water valve (4) slightly, to cut off the water after the alkali lye displacement totally, close rinse water valve (9) and bearing rinse water valve (4), close all and drench valve, open steam valve (1), incision system operation after the increasing temperature and pressure.
2. method according to claim 1 is characterized in that liquid caustic soda is that concentration is the liquid caustic soda of 5% (m/m).
3. method according to claim 1, the temperature that it is characterized in that hydrothermal solution alkali is 70-100 ℃.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN00134397A CN1114588C (en) | 2000-12-13 | 2000-12-13 | Method of reducing vibration and fault of vertical centrifuge in production of p-benzene dicarboxylic acid |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN00134397A CN1114588C (en) | 2000-12-13 | 2000-12-13 | Method of reducing vibration and fault of vertical centrifuge in production of p-benzene dicarboxylic acid |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1299806A true CN1299806A (en) | 2001-06-20 |
| CN1114588C CN1114588C (en) | 2003-07-16 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN00134397A Expired - Fee Related CN1114588C (en) | 2000-12-13 | 2000-12-13 | Method of reducing vibration and fault of vertical centrifuge in production of p-benzene dicarboxylic acid |
Country Status (1)
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| CN (1) | CN1114588C (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US7193109B2 (en) | 2003-03-06 | 2007-03-20 | Eastman Chemical Company | Process for production of a carboxylic acid/diol mixture suitable for use in polyester production |
| US7214760B2 (en) | 2004-01-15 | 2007-05-08 | Eastman Chemical Company | Process for production of a carboxylic acid/diol mixture suitable for use in polyester production |
| US7276625B2 (en) | 2002-10-15 | 2007-10-02 | Eastman Chemical Company | Process for production of a carboxylic acid/diol mixture suitable for use in polyester production |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1067049C (en) * | 1995-12-30 | 2001-06-13 | 鲜京工业股份有限公司 | Process for producing terephthalic acid |
| CN1206397A (en) * | 1996-10-30 | 1999-01-27 | 三井化学株式会社 | Process for preparing aromatic dicarboxylic acid |
-
2000
- 2000-12-13 CN CN00134397A patent/CN1114588C/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US7276625B2 (en) | 2002-10-15 | 2007-10-02 | Eastman Chemical Company | Process for production of a carboxylic acid/diol mixture suitable for use in polyester production |
| US7339072B2 (en) | 2002-10-15 | 2008-03-04 | Eastman Chemical Company | Process for production of a carboxylic acid/diol mixture suitable for use in polyester production |
| US7193109B2 (en) | 2003-03-06 | 2007-03-20 | Eastman Chemical Company | Process for production of a carboxylic acid/diol mixture suitable for use in polyester production |
| US7226986B2 (en) | 2003-03-06 | 2007-06-05 | Eastman Chemical Company | Process for production of a carboxylic acid/diol mixture suitable for use in polyester production |
| US7214760B2 (en) | 2004-01-15 | 2007-05-08 | Eastman Chemical Company | Process for production of a carboxylic acid/diol mixture suitable for use in polyester production |
| US7601795B2 (en) | 2004-01-15 | 2009-10-13 | Eastman Chemical Company | Process for production of a carboxylic acid/diol mixture suitable for use in polyester production |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1114588C (en) | 2003-07-16 |
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Granted publication date: 20030716 Termination date: 20161213 |