GB1498031A - Level controller - Google Patents
Level controllerInfo
- Publication number
- GB1498031A GB1498031A GB3693574A GB3693574A GB1498031A GB 1498031 A GB1498031 A GB 1498031A GB 3693574 A GB3693574 A GB 3693574A GB 3693574 A GB3693574 A GB 3693574A GB 1498031 A GB1498031 A GB 1498031A
- Authority
- GB
- United Kingdom
- Prior art keywords
- slurry
- drum
- valve
- liquid
- discriminator
- 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
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04B—CENTRIFUGES
- B04B11/00—Feeding, charging, or discharging bowls
-
- G—PHYSICS
- G05—CONTROLLING; REGULATING
- G05D—SYSTEMS FOR CONTROLLING OR REGULATING NON-ELECTRIC VARIABLES
- G05D9/00—Level control, e.g. controlling quantity of material stored in vessel
- G05D9/12—Level control, e.g. controlling quantity of material stored in vessel characterised by the use of electric means
Landscapes
- Physics & Mathematics (AREA)
- General Physics & Mathematics (AREA)
- Engineering & Computer Science (AREA)
- Automation & Control Theory (AREA)
- Centrifugal Separators (AREA)
Abstract
1498031 Controlling centrifugal strainer IMPERIAL CHEMICAL INDUSTRIES Ltd 6 Aug 1975 [22 Aug 1974] 36935/74 Heading BID The feeding of each successive batch of slurry to the drum of a centrifugal strainer is controlled by a valve 15 which is closed automatically when a pressure-sensitive electric switch or pneumatic relay 9 detects a rise in pressure resulting from the closure by the slurry level 1 of open tip 6 of a pipe 5 through which liquid flows continuously into the drum. The drum rotates continuously, and liquid is fed to pipe 5 by a low rate meter 11 and a higher rate meter 14 in parallel. Valve 12 is closed automatically 3-30 seconds after valve 15 cuts off the slurry feed, while meter 11 continues to feed liquid to keep tip 6 clean The liquid may be water or organic solvent and may be identical to the liquid content of the slurry. Tip 6 may be slightly inclined to the slurry surface and located at least half a revolution forward of pipe 4 which delivers the slurry. The filter cake is removed by a knife (not shown) after each centrifuging, but residual cake progressively clogs the drum screen which results in a progressive reduction in the filling time of the drum to level 7 as less liquid is removed from successive batches during the filling steps. In Fig. 4 (not shown) a timer incorporated in unit 17 sends a first signal to discriminator (21) a fixed time after slurry feed valve 15 opens and discriminator (21) also receives a second signal from relay 9 when the slurry closes tip 6. The drum is sequentially filled with batches of slurry until discriminator (21) receives the second signal before the first, and when this happens it signals back to control unit 17 causing it to initiate a screen-washing step after the present batch of slurry has been centrifuged.. Wash timer (25) then opens valve (27) to deliver washing solvent to the drum via pipe 28 in place of the next batch of slurry. The discriminator (21) may be a double air-operated shuttle valve or two electric pressure switches coupled to latching relays. Slurries of dimethyl terephthalate in methanol and terephthalic acid in acetic acid may be centrifuged.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB3693574A GB1498031A (en) | 1975-08-06 | 1975-08-06 | Level controller |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB3693574A GB1498031A (en) | 1975-08-06 | 1975-08-06 | Level controller |
Publications (1)
Publication Number | Publication Date |
---|---|
GB1498031A true GB1498031A (en) | 1978-01-18 |
Family
ID=10392378
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB3693574A Expired GB1498031A (en) | 1975-08-06 | 1975-08-06 | Level controller |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB1498031A (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5190515A (en) * | 1992-01-13 | 1993-03-02 | Eastman Kodak Company | Vacuum degassing apparatus |
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 |
CN104391515A (en) * | 2014-12-02 | 2015-03-04 | 佛山市南海北沙制药有限公司 | Methyl alcohol storage tank feed and output control device applied to medicine production |
-
1975
- 1975-08-06 GB GB3693574A patent/GB1498031A/en not_active Expired
Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5190515A (en) * | 1992-01-13 | 1993-03-02 | Eastman Kodak Company | Vacuum degassing apparatus |
EP0552110A1 (en) * | 1992-01-13 | 1993-07-21 | Eastman Kodak Company | Vacuum degassing apparatus and process |
US5277691A (en) * | 1992-01-13 | 1994-01-11 | Eastman Kodak Company | Vacuum degassing process |
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 |
CN104391515A (en) * | 2014-12-02 | 2015-03-04 | 佛山市南海北沙制药有限公司 | Methyl alcohol storage tank feed and output control device applied to medicine production |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN109998395B (en) | Liquid draining method of food processor | |
CN110170383B (en) | Intelligent horizontal screw machine operation control system and method | |
GB1498031A (en) | Level controller | |
GB989823A (en) | Beverage brewing apparatus | |
US3453083A (en) | Rotary extraction apparatus | |
CN112831391A (en) | White spirit filtering system and technological method | |
US2271493A (en) | Centrifugal separator | |
US2303541A (en) | Dry cleaning machine | |
US3575709A (en) | Method of cleaning sugar crystals | |
JPH1094508A (en) | Method of controlling amount of water filled into dishwasher | |
FR2331381A1 (en) | Level control of slurry in centrifuge - using a pneumatic probe fixed to the rotor | |
US3525596A (en) | Controlled discharge means for reaction apparatus | |
GB1275259A (en) | Improvements relating to spin dryers | |
US2822092A (en) | Fully automatic centrifugal machine | |
US2296262A (en) | Washing apparatus | |
SU1350173A1 (en) | Automatic control system for beginning and duration of sugar curing in centrifuge | |
US3087319A (en) | Clothes washing machine with water level control circuit | |
CN210545727U (en) | Operation control system of horizontal screw machine | |
US2466988A (en) | Centrifugal control system | |
GB906269A (en) | Improvements relating to centrifugal separators | |
JPS6427608A (en) | Strainer | |
JPH06171933A (en) | Method for controlling operation of basket gypsum dehydrator | |
CN218189480U (en) | Raw and other materials mixing arrangement is used in cardboard production | |
JPH02255184A (en) | Electric washing machine operating method | |
JP3001729B2 (en) | Washing machine |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PS | Patent sealed | ||
PCNP | Patent ceased through non-payment of renewal fee |