Showing posts with label polishing filtration. Show all posts
Showing posts with label polishing filtration. Show all posts

Friday, July 26, 2013

Reasons for Coloration in Product Hydrate & Corrective Measures to Improve Whiteness & Brightness

Hi Friends,

First, we would like to share the background of this technical blog. Till the end of 20th century, generally people were reluctant to share their technical knowledge particular on hydrates and alumina. In the back of their mind, it was a general feeling that only a few have particular data / information. But the advancement in communication technology revolutionized the knowledge sharing approach. In order to get advantages of technology and knowledge sharing approach among bauxite, alumina and aluminium professionals, we started this specialized technical blog couple of years ago with aggressive impulse and approach for achieving the difficult goal set by involved team of professionals. Fortunately, we could maintain the accelerated pace so far with our keen interests, enthusiasm and pleasure in publishing wide range of 273 technical articles pertaining to bauxite, alumina and aluminium. Now, when we look back towards the trajectory of our progress path traveled so far , we find that we have surpassed all our targets and goals well ahead of our planned schedule without compromising on quality. This reflects the grand success of one and all associated with this technical blog. Till date, we have more than 60,000 members and 75 Key Members who are closely connected who made their contribution by way of sharing their knowledge, data and information of public domain nature through this unique platform / web site. Today, we are ourselves astonished on our achievements of set goals. On the eve of this grand success day, we would like to express our sincere thanks to renowned Alumina Expert, Mr. George Banvolgyi of Hungary, for his blessings, guidance, inspiration and support during our journey of publishing variety of technical papers on this technical blog. Everybody deserves applaud and congratulations on this eve for bringing this platform to a new higher level of popularity. It gives me immense pleasure to be associated with this site as the founder member among the friends of bauxite, alumina and aluminium fraternity.Our each tiny achievement is the outcome of our efforts and as we consider it as the golden gift of God and hence we must celebrate the same with full enthusiasm and happiness. On similar lines, on achievement of every thousand of added viewers of our technical blog, we make our efforts to publish at least one special technical article on every special occasions. 

Today, we have achieved the total viewers of 60,000 with 76 Key Members across the globe closely associated and contributed in the grand success of this specialized technical blog. This day will definitely remain memorable for all of us and particularly for each member of bauxite-alumina-aluminium fraternity. All viewers and key members of this technical blog deserves congratulations on the eve of this new height of success as every body has contributed directly or indirectly in achieving this sky high target. On this great occasion, we are publishing this unique and special technical article for value addition to product hydrate by making it dazzling white and bright adopting corrective measures in process steps as described here under.

There are several grades of Hydrated alumina (Hydrates) manufactured and marketed across the globe. These hydrates are generally known as Specialty grade hydrate or Non-metallurgical grade hydrate. These are marketed at 2 to 5 times the price of Standard chemical grade hydrate. It has been seen practically that over and above desired chemical composition, brightness or whiteness of hydrates has premium market. Thus it becomes important to address the issue of coloration of hydrate and remedial measures for improving the whiteness so as to add more value to it. 

In present post, we will briefly cover the most probable reasons for coloration of product hydrate and appropriate technical solutions as remedial measures to improve whiteness and brightness as well.

There are two main reasons for coloration in product hydrate and appropriate solutions opined by many process experts as described here in subsequent paragraphs-
  1. High soda content in product hydrate
  2. High suspended solids in Thickener overflow pregnant liquor.
Step-I: With our experience in different Alumina refineries in the World, we have experienced the high soda content in product hydrate as one of the basic reasons. The identification of this issue is confirmed through simple analytical technique by analyzing the Na2O content in product hydrate ready for dispatch to respective customers. If total Na2O content in Hydrate is found more than 0.30% then it confirms that Hydrate generated in precipitators / decomposers / crystallizers has not been washed properly on product filter wherein the maximum component of leachable soda is removed. After observing this high soda content, vigorous washing of hydrate using steam /  hot water at temperature around 95-98oC helps in achieving total Na2O content below 0.30%. This step easily improves the product whiteness. For further improvement on washing efficiency, steam-hood at the discharge side of product filter can also be considered.


Step-II: High Fe2O3 content in product hydrate above 0.010% is the key indication of high suspended solids in filtered aluminate liquor feeding to Decomposers (Crystallizers / Precipitators). The suspended solids must be controlled below 15 mgpl (i.e. 15 milligrams per litre of pregnant liquor) in feed to Decomposers. Higher solids in pregnant liquor happens because of inadequate settling of suspended red mud particles in Liquor thickener for the major reasons listed below-

(a) High generation of fines during grinding of Bauxite:  Control fineness of Bauxite at optimum level to ensure higher settling rate of red mud particles in thickener. Generally, minus 60 mesh fraction in ground bauxite slurry is maintained more than 85%. Check and control it accordingly.

(b) Higher viscosity of thickener overflow liquor because of its lower temperature: Temperature of Thickener overflowliquor must be controlled at around 100-102 degree C if  the concentration of liquor in thickener overflow is at around 140-145 gpl Na2O or above. High concentration profile is the need of modern Alumina refinery in order to have improved productivity so as to minimise thermal and electrical energy consumption.

(c) Selection of right settling agent: Settling agent used for faster settling of residue particles play vital role in achieving desired quality of product. There are different types of natural and synthetic high density polymers are available for different application. It has been observed that mixed natural starch with particular type of synthetic floccullent are  cost effective for Alumina refinery. 

(d) Selection of proper filter cloth for polishing filtration equipment: Selection of proper filter cloth is equally essential for controlling suspended solids in filtered aluminate liquor fed to crystallizers. Polypropylene filter cloth of more than 30 and 32 EPI and PPI have been found to be the most suitable cloth for security filtration.

(e) Controlling ingress of P2Ocontent in Bauxite: At times, high P2O5 content in Bauxite affects the settling rate of residue (Red mud) in thickener. To eliminate this issue, start adding small quantity of Burnt lime (CaO) in Bauxite being fed to Grinding mill. This results in reducing the Phosphorus content in liquor forming Calcium Phosphate.


(f) Control Filter feed pressure below 2.0 kg/cm2.g: Lower the fitration pressure better is the filtrate quality. Pressure around 2.9 kg/cm2.g has been found to be optimum.

(g) Control solids in Thickener overflow Liquor well within 100 mgpl: Suspended solids in feed liquor to filter should be controlled well within 100 mgpl so as to avoid extra load of residue on polishing filtration unit thereby improving the filtrate quality to crystallizers,


(h) Optimize dosing of TCA: TCA (Tri calcium aluminate) addition to filter feed liquor results in improved fitrate quality. It has been established in various plants across the globe that mass flow of TCA equal to 10 times of suspended solids in Thickener is optimum.

Step-III: Check & Replace Security Filters in Service: Even after checking and monitoring all the above mentioned parameters stated under Step-I & II, if there is no appreciable improvement in filtrate clarity, then it concludes that some thing wrong with filtration equipment itself. In such situation, replacement of Polishing filters with suitably sized and designed security filters is the ultimate solution to this problem. Since this step requires additional capital expenditure fot the plant, thus decision needs to be taken only after thorough investigations of results obtained during Step-I and Step-II under the guidance of process expert who has operated the similar systems in any Alumina refinery across the globe.


Aluminium Trihydrate
Trust, all major possible reasons for poor filtrate clarity have been covered here and desired solutions have been presented with utmost care. In case, we have missed out any major reason, please come forward and put your views under Comments just below the article. Our team of experts will welcome your valuable comments / remarks in the benefit of readers across the globe. Everybody will like to have hydrated alumina with whiteness and brightness as shown here in the pictorial view. The major chemical constituents and coarseness / fineness are given below-
Fe2O3: 0.007%, SiO2: 0.007%, Na2O:0.23% and Minus 45 microns: ~ 90%. This hydrate is the basic input material for producing American Diamond for jewelry, Thread guides, Sealing rings for pumps and many other valuable products. The author was deeply involved in development of this product, project engineering, trial run and manufacture of this product in the plant. Thus, if you can feel this product, you can definitely produce it in your own plant. Trust, our learned friends of alumina fraternity will put their valuable remarks and opinions under comments paragraph which will help in enriching our knowledge base towards our approach and methodology in achieving better results in future. Your views / remarks / comments matter for us for improvements in forthcoming articles. Please never be hesitant in expressing your opinions. We seek your continued support and welcome your suggestions.

Kind regards.

Kunwar Rajendra

Monday, September 19, 2011

Remedial actions for trouble-free operation of Auto dumping pressure filters

Hi Friends,
In previous post, we have discussed about the Advancements in polishing filtration system wherein we have described the design and operational features of Auto dumping vertical leaf pressure filters over manual security filters. There are two basic objectives of polishing filtration unit in Alumina refinery-
  1. Maximum filtration rate at lowest filtration pressure and
  2. Improved filtrate clarity with minimum suspended solids.
In present post, we will discuss about various operational problems of Auto dumping pressure filters and remedial actions to prevent such operational difficulties for smooth and trouble-free operation of polishing filtration system. We are well aware that Auto dumping pressure filters are called under different brand names by different designers and suppliers of this equipment. Typical schematic view of Auto dumping vertical leaf pressure filter is given below just to have a physical feel of equipment and sequence of normal operation. I am thankful to my friend who took pain in developing the schematic view of Auto dumping pressure leaf filter.
The operation of the equipment is generally smooth during normal condition with steady process conditions in the upstream and sound functioning of the automation and controls. But, even during minor fluctuations in process conditions, the equipment behaves abnormally creating acute operational and process control problems. In this post, the remedial measures have been highlighted to prevent two major operational problems as elaborated in following paragraphs-


1.Fast drop in filtration rate : The basic objective polishing filtration unit is to ensure high filtration rate with desired level of filtrate clarity containing maximum impurities within 20 mgpl. Presence of higher suspended solids in filter feed liquor adversely impacts the filtration rate, filtrate clarity and filtration cycle time. Fine grinding of bauxite, inconsistent flow of flocculent to settlers and higher viscosity of  feed liquor  are the main reasons for higher suspended solids in settlers. This problem can be easily prevented by ensuring proper grinding of bauxite, adequate flow of flocculent, proper cooking of flocculent, controlling the temperature profile of settler overflow liquor by monitoring the dilution intake in digester blow-off slurry.


2. Poor filtrate clarity: At times wide variations in filtrate clarity is observed with fluctuations in suspended solids in filtrate which is not desirable. Such fluctuation mainly occurs due to inadequacy of filter aid in filter feed liquor. It has been observed that TCA addition is done by plant operating personnel in Settler which is not the right way as TCA acts as settling aid in settlers in stead of filter aid in pressure filters. Thus continuous addition of TCA to the suction line of filter feed pumps resolves this problem. As per rule of thumb, the mass flow of TCA in filter feed liquor should be 10 times the mass flow of suspended solids in liquor. In addition, quality of burnt lime and correct method of TCA solution preparation  at around 80 degree Centigrade for one hour cooking time to be ensured. Condition of filter leaves also has the vital role as hard leaves cause high filtration pressure and thereby ingress of suspended solid through pores. Thus periodic caustic wash of filter leaves is also essential. 


Hope, the topic has been covered to the extent possible. Please put your views / suggestions / remarks / comments, if any.
Regards.


Kunwar Rajendra

Sunday, March 27, 2011

Can We Use Vacuum Filters for Polishing Filtration ?

Hi Friends,

One of our friends of Alumina fraternity has raised a very interesting question before us. Can we use vacuum filters for polishing filtration in Alumina refinery? The simple answer is 'No chance'. Now let us analyse the pros and cons with technical reasons to clearly understand this issue.

In Alumina refinery, the polishing filtration of settler overflow liquor is done for achieving following three basic objectives-
  • Improved filtrate clarity : Suspended solids in filtrate has direct impact on product quality particularly with respect to impurities like SiO2 and Fe2O3 .
  • High filtration rate : Plant production rate is directly proportional to liquor filtration rate, hence it is aimed to have the specific filtration rate between 1.50 to 2.00 m3/m2.hr.
  • Negligible  temperature drop : Since the temperature drop of aluminate liquor may cause loss of alumina with residue cake due to auto precipitation during filtration. Hence all possible measures are taken to minimize the temperature drop of aluminate liquor across filtration unit within 2 to 3 degree centigrades. 
Pressure filters meet all the above process requirements. On the other hand, vacuum filters can not meet any of these three process requirements because the driving force is the vacuum. Applied vacuum for liquor filtration will generate cooling affect on liquor and there by substantial increase in viscosity of saturated aluminate liquor, thus marginal auto precipitation of hydrate in residue cake. The increase in viscosity of liquor will cause increase in filtration pressure ultimately affecting the filtration rate and filtrate clarity as well.

Hence, vacuum filters can not be used for polishing filtration of aluminate liquor in Alumina refinery and therefore, Pressure filters are the only option for this unit operation.

Hope, I have clarified the issue to the extent possible. however, if you have some other reasons to explain, please feel free in sharing your views.

Regards.

Kunwar Rajendra