摘要:
A process for the production of granules or pellets containing filamentous fungi is described comprising the steps of selecting and growing filamentous fungi in a suitable culture medium for a predetermined amount of time, adding a gelling agent and at least one carrier to said culture medium, so as to obtain a mixture, subjecting said mixture to gelling through contact, drop by drop, with a solution containing a calcium salt thus obtaining gelled pellets or granules containing said filamentous fungi and drying said gelled pellets or granules to a moisture content of 13-18%.
摘要:
A method for revamping a conventional self-stripping urea plant (1) is disclosed, where a minor portion (18a) of the carbon dioxide feed is fed to the stripper (7) and used as a stripping agent. In further embodiments, another carbamate condenser is installed, or the conventional horizontal shell-and-tube carbamate condenser (6) is replaced with a vertical submerged unit.
摘要:
A granulation process wherein a liquid is sprayed into a prilling tower (1) by means of a rotating prilling bucket (15) having a perforated side wall (15a), and the liquid jets exiting said perforated side wall are subjected to a vibrating action according to the axial direction (A-A) of the prilling tower (1), while the remaining liquid mass inside the bucket is kept substantially free from said vibrating action. A suitable apparatus is also disclosed, wherein the peripheral side wall (15a) of the prilling bucket (15) is.connected to vibration imparting means and has a flexible connection with the frame (15b, 15c) of the bucket.
摘要:
A fluid bed granulation process of a predetermined substance comprises the steps of: forming, through a fluidification. air flow of predetermined flow rate, a fluid bed of granules of said substance to be granulated fed to it in the form of seeds, - feeding said fluid bed with a continuous flow of a growth substance (or liquid).
摘要:
A method for the modernisation of a plant for urea production comprising a reactor (2) for urea synthesis, a stripping unit (3) with carbon dioxide and at least one vertical condensation unit (4) of the film type, includes the step of providing in the condensation unit (4) means for subjecting to substantially total condensation a portion of a flow comprising ammonia and carbon dioxide in vapour phase leaving said stripping unit (3), and is characterized in that it further comprises the steps of providing a second stripping unit (47), means (9) for feeding a first portion of the flow of reaction mixture comprising urea, carbamate and free ammonia in aqueous solution leaving the reactor (2) to said stripping unit (3), means (48) for feeding a second portion of the flow of reaction mixture comprising urea, carbamate and free ammonia in aqueous solution leaving the reactor (2) to said second stripping unit (47) and means (49) for feeding at least a portion of a flow comprising ammonia and carbon dioxide in vapour phase leaving said second stripping unit (47) directly to the reactor synthesis (2).
摘要:
Fluid bed granulation process comprising the steps of: - forming a fluid bed of seeds (S1) of a chosen substance, - feeding said fluid bed with a continuous fluid flow (L) comprising a growth liquid, - inducing and maintaining a continuous vortex (V) in said fluid bed, the vortex (V) having a substantially horizontal axis,
characterized in that said fluid flow (L) is fed into predetermined first zones (Z1) of said fluid bed, said first zones (Z1) being alternated to second zones (Z2) of said fluid bed in which said fluid flow (L) is not fed.
摘要:
A process for urea production comprises the steps of: - performing a reaction between ammonia and carbon dioxide in a reaction space to obtain a reaction mixture comprising urea, carbamate and free ammonia in aqueous solution, -subjecting said mixture to a stripping treatment with carbon dioxide feed as a stripping agent to obtain a first flow comprising ammonia and carbon dioxide in vapor phase and a flow comprising urea and residual carbamate in aqueous solution, - feeding said flow comprising urea and residual carbamate in aqueoue solution to a urea recovery section, - separating in said recovery section said residual carbamate from the urea to obtain a first flow of carbamate in aqueous solution.
摘要:
A process for the integrated production of urea and melamine synthesized from at least part of said urea, comprising the steps of: - carrying out a urea synthesis in a first urea synthesis reactor (16), fed with ammonia and carbon dioxide, obtaining a reaction mixture comprising urea and ammonium carbamate, - carrying out melamine synthesis, with formation of off-gas comprising ammonia and carbon dioxide, - carrying out a further urea synthesis in a second urea synthesis reactor (28), fed with said off-gas, with production of a respective reaction mixture comprising urea and ammonium carbamate, - feeding said reaction mixture produced by said first reactor (16) and said reaction mixture produced by said second reactor (28) to a urea recovery unit (18), obtaining urea and an ammonium carbamate aqueous solution, - feeding said ammonium carbamate aqueous solution obtained in said recovery unit (18) to said second urea synthesis reactor (28).
摘要:
A process for urea production from ammonia and carbon dioxide, in which part of the aqueous solution comprising urea, ammonium carbamate and ammonia obtained in a urea synthesis section is subjected to dissociation in a treatment section operating at a predetermined medium pressure for the recovery of the ammonium carbamate and of the ammonia contained in it, comprises the step of subjecting the urea aqueous solution resulting from the aforementioned dissociation step to decomposition in a low pressure urea recovery section.
摘要:
In a process for urea production of the type comprising the reaction between ammonia and carbon dioxide in a highpressure reactor followed by an autothermal stripping of the resulting reaction mixture so as to obtain a gaseous flow comprising ammonia and carbon dioxide and a liquid flow comprising urea and residual carbamate in aqueous solution and by a stripping of said gaseous flow in units operating at medium pressure, a gaseous flow coming from said units operating at medium pressure and comprising ammonia and carbon dioxide is partially condensed in a condenser to give a mixed liquid/gaseous flow. The uncondensed gases comprising ammonia and carbon dioxide are separated from the liquid phase in a separator and subjected to washing in a packed portion of a column in countercurrent with a flow of a carbonate solution obtaining a gaseous flow essentially consisting of ammonia and a liquid flow comprising a carbamate solution in which the carbon dioxide contained in said uncondensed gases has been absorbed. This process allows an effective recovery of ammonia without carbon dioxide for the recycling to the synthesis reactor.