Big Chemical Encyclopedia

Chemical substances, components, reactions, process design ...

Articles Figures Tables About

Membrane purification unit

In Canada, hydrogen production from natural gas via a fluidised bed reactor with hydrogen purification via a selective membrane is under investigation. Also, a methanol micro-reformer which includes an integrated metal membrane purification unit is being developed. [Pg.53]

Reflux overhead vapor recompression, staged crude pre-heat, mechanical vacuum pumps Fluid coking to gasification, turbine power recovery train at the FCC, hydraulic turbine power recovery, membrane hydrogen purification, unit to hydrocracker recycle loop Improved catalysts (reforming), and hydraulic turbine power recovery Process management and integration... [Pg.755]

Palladium-based dense metallic membranes have been known to be completely selective for hydrogen permeation and are used in commercially available small-scale hydrogen purification units (e.g., Johnson Matthey, 2007 REB Research, 2007 Power + Energy, 2007 ATI Wah Chang, 2007). These hydrogen purification units typically use palladium-alloy... [Pg.301]

Concentration Units. Typical concentrators for rinsing solutions are membrane filtration units, which split the feed into diluate and concentrate streams, meaning purification and recovery, respectively [106], Both nanofiltration and reverse osmosis might be applied, depending on the physico-chemical properties of the solutes. [Pg.323]

The use of a membrane reactor in steam reforming has several advantages. Because of the lower temperature operation, the energy consumption of the process is reduced which results in lower emission of C02. The lower temperature also requires less expensive catalyst, tubing and other reactor materials. Since hydrogen of sufficient purity is produced directly from the reformer, the downstream shift conversion can be omitted. Moreover, the dimensions of the C02 removal and final purification units can be reduced. Hence, significant savings in equipment costs can be expected. [Pg.15]

Distillation Unit and Filtration Unit. In this system, purification and recycling of IPA is performed by the combination of the PV membrane dehydration unit, the distillation unit, and the microfiltration unit. In the distillation unit, impurities, which are difficult to separate in the PV membrane separation unit such as dissolved metal ions and high-boiling impurities, are completely eliminated. [Pg.153]

R/0 unit Reverse Osmosis Unit for water purification in small aquariums and miniature yard-ponds, utilizes a membrane under pressure to filter dissolved solids and pollutants from the water. Two different filter membranes can be used the CTA (cellulose triacetate) membrane is less expensive, but only works with chlorinated water and removes 50-70% of nitrates, and the TFC membrane, which is more expensive, removes 95% of nitrates, but is ruined by chlorine. R/0 wastes water and a system that cleans 100 gallons a day will cost ft-om 400 to 600 with membrane replacement adding to the cost. A unit that handles 140 gallons a day will cost above 700,00. [Pg.624]

The latter concept implies providing local life support systems for unfriendly environments. By now, Ukrainian scientists and engineers have developed a variety of processes for potable water treatment by adsorption, electrochemical oxidation, electrocoagulation, electro-coprecipitation, electrodialysis, electrofloatation, floatation, membrane techniques etc. Each family must get small units for water purification, air cleaning and removal of hazardous substances from the food as soon as possible, for it may take decades to introduce cleaner production on a national scale. Here, we should follow the example of Western business people who bring with them to Ukraine devices enabling a safe existence in this unfriendly environment. [Pg.32]

Advances during the past 20 years in membrane, electrolyser, electrode, and brine purification technologies have substantially raised the performance levels and efficiency of chlor-alkali production by ion-exchange membrane electrolysis, bringing commercial operations with a unit power consumption of 2000-2050 kWh per ton of NaOH or lower at 4 kA m-2 current density with a membrane life of four years or longer. [Pg.227]

FIGURE 1.35 SLM process using O-9-(l-adamantylcarbamoyl)-10,ll-dihydro-ll-octadecylsulfinylquinme and corresponding quinidine derivative as chiral carriers for the preparative separation of enantiomers of Al-derivatized amino acids (e.g., DNB-Leu). (a) ftinciple of the carrier SLM process with carrier-mediated transport (top) and (nonstereoselective) nonspecific transport processes (bottom), (b) General experimental setup of the SLM production unit with two membrane modules, (c) Multistage SLM purification process. P, permeate QD/QN, membrane modnles snpported with quinidine-derived and quinine-derived chiral carriers. R, S, D, L refers to the respective enantiomers of the selectand (DNB-Leu). (Reproduced from A. Maximini et al., J. Membr. ScL, 276 221 (2006). With permission.)... [Pg.96]

The membrane is a unit of the process separated from the reactor. It maintains only the separation function (passive membrane) and there is almost no interaction between reaction and separation. In fact, we have here two different processes connected in series. Stream purification from catalyst poisoning substances or feed enrichment of a recycle stream belong to the possibilities of this configuration. [Pg.120]


See other pages where Membrane purification unit is mentioned: [Pg.202]    [Pg.202]    [Pg.411]    [Pg.458]    [Pg.321]    [Pg.1646]    [Pg.109]    [Pg.742]    [Pg.494]    [Pg.86]    [Pg.132]    [Pg.29]    [Pg.125]    [Pg.89]    [Pg.292]    [Pg.225]    [Pg.689]    [Pg.279]    [Pg.484]    [Pg.135]    [Pg.484]    [Pg.354]    [Pg.403]    [Pg.354]    [Pg.495]    [Pg.338]    [Pg.88]    [Pg.2065]    [Pg.503]    [Pg.532]    [Pg.644]    [Pg.84]    [Pg.12]    [Pg.36]    [Pg.576]    [Pg.224]    [Pg.28]    [Pg.369]    [Pg.236]    [Pg.104]   
See also in sourсe #XX -- [ Pg.202 ]




SEARCH



Membranes membrane unit

© 2024 chempedia.info