Water regulator - Import export

Pressure regulator of the compact series for water Sizes: 1/8" and 1/4" Adjustment range: 0-2 bar, 0-4 bar, 0-8 bar standard, 0-12 bar Pressure range up to 15 bar

Vertical cylindrical on feet Eccentric conical dome Conical bottom slope 38 % Interior and exterior finish glazed 2B Decentered chimney Ø 400 mm and height 300 mm ELICA 316L stainless steel antiretention hatch 3 simple male DIN 80 fittings on the dome Double acting ELICA 1000 HL stainless steel 316L valve, horn mounting 5 lifting rings including 1 at the bottom of the tank Support + manufacturer's plate 1 single male DIN 65 fitting in ferrule 1 single male DIN 65 fitting in ferrule Taken from the ground 5 thermal regulation rings with water I / O sleeve 4.75 m2 5 heating rings with water I / O sleeve 4.75 m2 Total thermoregulation area 9.5 m2> Thermoregulation ratio per 100 HL 6.31 m2 Tapered connection + stainless steel faceplate for agitator mounting Full stainless steel buffer + EPDM seal for stirring nozzle stirring Total drain pipe + male at the end of DIN 65 piping 4 outside legs, tank height 800 mm Stainless steel flat reinforcement belt 150 x 5

DSEC's commitment on the construction of Bioethanol plants is based on a very specialized technical knowledge of the Ethanol production processes; in this article you will find a more detailed understanding about the Downstream Process. The alcohol in the fermented mash is then concentrated by means of distillation and rectification, before the required water content of ethanol is regulated in the dewatering process. The accrued residues from distillation, the so-called stillage, is first evaporated and then dried to animal feed, the so-called DDGS. However, the production (drying) of DDGS requires a considerable amount of primary energy (e.g. fuel oil or natural gas); therefore, if feedlots are nearby, animal feed will be sold in wet condition, so called WDGS. For sugar cane and molasses the residue, so called vinasses, was returned to the fields as fertilizer- due to sustainability reasons and change in legislation, spraying of vinasses on the fields is mostly forbidden in the meantime. In the past, direct combustion of DDGS turned out to be unfeasible because of procedural difficulties and lacking efficiency (due to the high water content of the stillage). The realisation of a biogas plant could not be achieved in large scale so far because of the enormous quantities of stillage and their high organic stress. Combination of ethanol production with biogas respectively, biomass burning results in different biorefinery concepts or so called next generation technology.

Boiler feed water The so called „Boiler feed water“ is stored in a feed water tank and continuously feeded to the boiler of a steam generator. A big quantity of feed water is needed for example in steam power plants. The boiler generates steam, which is used for heating, for chemical processes or for driving a steam turbine respectively a steam engine. The feed water is purified in a way, that all harmfull components for the boiler are removed or neutralized. Leakages and evaporation loss are compensated by additional water which is purified in the same way than boiler feed water. Very often, valuable well and potable water resources are used for the generation of process water. Environmental regulations restrict this usage of well and potable water continuously and increase the costs for this resources steadily. The conditioning of stream water to boiler feed water helps saving potable water and means cost advantages. The process of conditioning is based on ultra filtration with down