1.Product appearance: The solid product is produced by the spray drying technology and the obtained product is light yellow, Corresponding liquid products is light yellow. 2.Raw materials:Domestic high-quality aluminium hydroxide,High-quality calcium aluminate,High-quality hydrochloric acid.3.Usage: Drinking water treatment Treatment of high-purity water4.Product advantages: 1). Flocculation ability, high adsorption activity, floc formation and deposition of fast. 2). Without alkali and other additives, PH broad in scope, ease of use; for low-temperature, low turbidity, low alkalinity of the raw water is also good flocculation3).easily to use and good effective. 5.Storage: The products shall be sealed and stored in the dry and ventilated place to prevent from rain ,high temperature and strong sunlight . 6.Application method:1)The liquid product can be used directly or used after dilution.Dilution is necessary before used for the solid product. The normal dilution ratio for the solid product is 5%-15%.2)he specific dosage is based on the flocculation tests and trials by the users. The usual dosage of the liquid product is 3-40 g/ton, and of the solid product, 1-15 g/ton.
SPECIFICATION
Specification |
Analysis Results |
Aluminium oxide(Al2O3) % |
30% |
Basicity% |
40-90 |
PH (1% aqueous solution) |
3.5-5.0 |
Water insoluble % |
0.1% |
Nitrogen |
≤0.01 |
(As)/% |
0.0002 |
(Pb)/% |
0.001 |
(Cd)/% |
0.0002 |
(Hg)/% |
0.00001 |
(Cr+6)/% |
0.0005 |
PAKCKAGINGPP woven bag with PE lined bag(25kgs/bag) or PE bag(20 kgs/bag) or according to the customer’s requirements.
Application aluminium sulphate for the reclamation of a slurry of waste drilling mud fluids and water normally resulting from drilling operations. The process comprises the steps of conducting the drilling mud slurry to a slurry surge tank for liquid solid separation by aluminium sulphate and physical methods. The mud slurry is subjected to a primary solids separation unit after pH adjustment is used to initiate coagulation and an organic flocculant is added to aid flocculation of the solids. The water is then subjected to a secondary solids removal, and the solids recovered are reintroduced in the primary solids separation unit. Thereafter the water obtained from the secondary solids removal is then subjected to a aluminium sulphate oxygen demand reduction unit having a carbon adsorption unit or reverse osmosis membrane units therein to remove organic matter or dissolved solids to produce water meeting environmental discharge requirements. The solids removed from the primary solids separation unit are converted to a cake meeting leachate requirements for other beneficial use.