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  5. White Polylactic Acid 3D PLA Printer Filament

White Polylactic Acid 3D PLA Printer Filament

950 incl. GST

Enriched by our vast industrial experience in this business, we are involved in offering an enormous quality range of 3D PLA Printer Filament.

PLA is an "easy to use" high-end PLA (Poly-Lactic Acid) type of 3D printer filament, which is slightly modified with an impact modifier, making the filament tougher, less rigid, slightly softer and therefore "easy to print" at relatively low temperatures. PLA is nearly warp-free and will not deform after cooling.

Feature
Material Polylactic Acid
Brand Filamont
Color White
Size 1 kg
Diameter(millimetre) 1.75
Print Temperature(Degree Celsius) 190-210
Minimum Order Quantity 1 kg
Description

Enriched by our vast industrial experience in this business, we are involved in offering an enormous quality range of 3D PLA Printer Filament.

PLA is an "easy to use" high-end PLA (Poly-Lactic Acid) type of 3D printer filament, which is slightly modified with an impact modifier, making the filament tougher, less rigid, slightly softer and therefore "easy to print" at relatively low temperatures. PLA is nearly warp-free and will not deform after cooling.

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Biogas Power Generation

Biochemistry Of Biogas Generation

The following three stages are involved in the process of anaerobic digestion.

  • Hydrolysis: In the process of hydrolysis the complex molecular compounds i.e. polymers are converted into the simple molecular form i.e. monomers.
  • Acidogenesis: The monomers so formed at the end of hydrolysis process are converted into volatile fatty acids. Acetic acid forms the major portion of volatile fatty acids. The process of conversion of monomers into acids is carried out by a group of anaerobic bacteria known acid formers.
  • Methanogenesis: Acids produced at the end of Acidogenesis process are converted into carbon dioxide and methane gases. The process of conversion of acid into gases is carried out by group of anaerobic bacteria known as methane formers.

In CSTR process the bacteria responsible for digestion process are kept in suspension with the help of Lateral as well as central mixers.

Process Description

Wastewater Transport
Raw effluent i.e. raw spent wash from the distillery shall be carried to treatment site through suitably designed channel or a closed pipe depending upon the topography of the site. Raw spent wash shall then be passed through heat exchanger [if required] to bring down the temperature to 38oC – 40oC raw spent wash. Pumps are installed to pump the raw effluent from buffer tank to reactor.

CSTR Reactor
The CSTR Reactor is designed on the principle of anaerobic contact process. The raw effluent enters the CSTR at the top in a central shaft. The Recirculated sludge is also mixed with raw effluent in a central shaft. A central agitator is provided at the top to facilitate mixing and downward movement of the mixed effluent. The effluent travels to the bottom of reactor through central shaft. In reactor the effluent comes in the contact with active anaerobic culture maintained in the suspension. In the process the organic matter in the effluent is converted in to biogas and cell mass. The liquid travels upward in the reactor. 6 Nos. of lateral agitators are provided for mixing and upward movement of the liquid.

The effluent is then taken out of the reactor through overflow pipe provided with water seal. The effluent will be received in a lamella clarifier where the active biomass will be separated and part of it is recirculated back to the reactor. Before entering into the lamella clarifier the effluent is passed through degassing tower for removal of dissolved gases to achieve better settling in the lamella clarifier. Lamella clarifier is fabricated with anticorrosive paint and is provided with inclined plates. The clarifier shall also be provided with sludge withdrawal arrangement. Sludge Recirculation pumps is provided to recirculate the sludge back to the CSTR reactor. The post anaerobic effluent is then taken to secondary treatment for further removal of the organics. CSTR reactor will be erected and fabricated at site using mild steel plates and structural members. The CSTR reactor will be rested on floating type foundation. The reactor will be painted from inside with chlorinated rubber paint and synthetic enamel paint from outside.

Biogas Recovery
Biogas will be collected at the top of the reactor and will be stored in a gasholder separately constructed. Biogas holder is fabricated in MS plated and shall be of floating type. Biogas from biogas holder will be compressed and sent to boiler for burning. Flare stack is provided to flare the excess biogas.

 

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