Sodium Silicate Plant:There are two processes for preparing water glass that are common this day. The first one is by reaction in liquid phase while the next one is by reaction in solid phase. However, alkaline and quartz sand are the same raw materials used in the two processes.1. Process with reaction in liquid phase: Caustic soda, quartz sand and water are mixed in a mixing tank, and then the mixture is fed into a reactor, where steam is introduced. The reactant is liquid water glass with its module lower than 3. The reaction is as following: nSiO2+2NaOH Na2O•nSiO2+H2O 2. Process with reaction in solid phase (thermal process) The feed materials in this process are sodium carbonate and quartz sand, or sodium sulfate and quartz sand. The feed materials are heated in a reflection furnace. The reaction is as following: Na2CO3 +XSiO2→(Na2O)•(SiO2)X + CO2 4Na2SO4 +2C +4SiO2→4Na2SiO3 +4SO2 +2CO2 The water glass produced by this thermal process can have modules depending on requirements for different applications.

High cut and blend emulsification machine:
1) Produces bright and fine cream
2) Uniform cream microstructure
3) Strong dispersal and emulsification
4) Fine latex
5) Wide grain diameter
6) High quality

Vacuum emulsification boiler:
1) Dispersal diameter is 1.0~2.0um
2) Obscuration homogenous emulsification 
3) No air bubble 
4) Long term stabilization

Complete set of boilers for cream and hoarfrost, liquid detergent:
1) Processing quantity for each batch cream: 100Kg~800 kg 
2) Liquid detergent: 300kg~1,000 kg
3) Can produce low and high adhesive 

Other equipment:
1) Hydraulic pressure, the over turn vacuum emulsification boiler
2) Water process equipment for ion interchange
3) Removable storage can
4) Electrothermal steam generator
5) Water process system
6) Bottling machine
7) Conveyor belt

The above equipment can produce following products:
1) Cream kinds cosmetic
2) Sachet kinds cosmetic
3) Hairdressing kinds cosmetic
4) Perfume, astringent kinds cosmetic

Sodium Triphosphate(STPP) Production Equipment:STPP is one of the most important ingredients in detergent powder formulation. Its chemical formula is Na5P3O5. The STPP preparation process is composed of three steps: preparation of phosphoric acid from phosphate rocks, sodium pyrophosphate from neutralization of the acid, and finally the formation of STPP by condensation and polymerization of the sodium pyrophosphate. There are two processes now in common use for preparing STPP: 1. Wet process Converse ingredients in the phosphate rocks into their corresponding sulfuric salt and phosphoric salt. The liquid phosphoric acid is neutralized in next section into sodium pyrophosphate, then the phosphate to be condensed and polymerized into STPP. 2. Thermal process Feed phosphate rocks, coke and silicate rocks into an electric furnace to obtain phosphorus. The phosphorus is burned, and phosphorus pentoxide is formed. The later is hydrated and polymerized into STPP.

SO₃ Sulfonation Plant:Multi-tube falling film sulfonation (sulfation) reactor is used in this plant. The organic feed materials include DDB, LAB, fatty alcohols, laurel ether,olefins etc. Two control alternatives are available: conventional or computer controlled. The plant is composed of following units:Air drying, Sulfur melting and dosing, Sulfur burning and SO3 generation , Sulfonation/sulfationNeutralization, Exhaust gas treatment Capacity: 500 kg/h to 3,000 kg/h.

We offer two soap base production devices: a soap boiling saponification
boiler and a continuous saponification to produce soap base.

After saponification, the grease is dried, and then additives such as 
perfume and antioxidants are added into the soap. Lastly, the soap can 
be formed into various products including toilet soap or laundry soap. 

Complete soap process:
1) Soap base production
2) Drying
3) Molding
4) Packaging

Soap, transparent soap molding product line:
1) Soap mixer, triple roller muller, soap vacuum strip export machine, 
    printer, transport device, exit mold cooling system
2) Refine, grinding, vacuum, molding bar

Toilet Soap and Laundry Soap Equipment:The soap base can be produced by kettle saponification or continuous saponification of oil and fats. The liquid soap is vacuum dried. The soap noodles obtained is added with perfume, anti-oxidation agent etc. in a mixer, then goes through milling and plodding system to form toilet soap or laundry soap of different shapes and formulations. The whole plant includes oil and fats refining unit, saponification unit, vacuum drying unit, finishing line and packaging section. Complete soap plant can be supplied, or according customer's requirements, only finishing line beginning from soap noodles bought from outside to the packaging machine.

STPP is one of the most important ingredients in detergent powder formulation. Its
chemical formula is Na5P3O5.
The STPP preparation process is composed of three steps: preparation of phosphoric
acid from phosphate rocks, sodium pyrophosphate from neutralization of the acid,
and finally the formation of STPP by condensation and polymerization of the sodium
pyrophosphate.
There are two processes now in common use for preparing STPP:
1.Wet process
Converse ingredients in the phosphate rocks into their corresponding sulfuric salt
and phosphoric salt. The liquid phosphoric acid is neutralized in next section
into sodium pyrophosphate, then the phosphate to be condensed and polymerized into
STPP.
2.Thermal process
Feed phosphate rocks, coke and silicate rocks into an electric furnace to obtain
phosphorus. The phosphorus is burned, and phosphorus pentoxide is formed. The later
is hydrated and polymerized into STPP.

There are two processes in sodium sulfate production.

1. Chemical process:
Feed sodium chloride (>97%) and sulfuric acid (H2SO4 >98%) into Mannheim furnace, and the reactant is sodium sulfate.

The first step is an exothermal reaction that can be carried out at lower temperature,
NaHSO4 is form first. While the second reaction is a strong endothermic reaction,
the reaction can be carried out only at 500°C to 600°C. The heat required
by the reaction is supplied by burning of gas in the burning chamber of the
furnace. The gas is generated by a coal gas generator. The temperature in the burning
chamber should be maintained around 1,200°C.

2. Extracted from glauberite rocks:
Crushed glauberite rocks are fed into a tank, and then are extracted by water. Remove impurities in the extract. The clean extract is evaporated and centrifuged. Finally this wet sodium sulfate is dried to obtain product sodium sulfate