Our Products

Rotary Evaporator

Laboratory equipment

Jacketed Reactor

Contact Us

We Cherish All Interactions

Highly Efficient Biomass Dryer And Reactor Heating - Tranter

Highly Efficient Biomass Dryer And Reactor Heating - Tranter

Reduce energy consumption by biomass dryers and cook reactors, e.g., acid hydrolysis cellulosic cooking, both first- and second-stage hydrolysis vessels and acid reconcentrator towers. Solution Dryer shells and internal agitators constructed with highly efficient PLATECOIL® Prime Surface Heat Exchanger panels.

Biofuels - Ekato

Biofuels - Ekato

For being efficient, the plants require a high solids load. At the beginning of the "enzymatic hydrolysis" process step, a viscosity of up to 250,000 mPa s can be given. The enzymatic impact and the mixing effect cause a decrease down to less than 2,000 mPa s within a few hours. This leads to complex challenges for the selected mixing system.

Multiscale Dynamics of Hemicellulose Hydrolysis for .

Multiscale Dynamics of Hemicellulose Hydrolysis for .

We develop an 'optimal mixing' strategy – comprising of 55-70 min of initial reactor mixing followed by no mixing for the rest of the hydrolysis – which increases xylose and reducing sugar .

China Reactor, Reactor Manufacturers, Suppliers, Price .

China Reactor, Reactor Manufacturers, Suppliers, Price .

China Reactor manufacturers - Select 2020 high quality Reactor products in best price from certified Chinese Chemical Reactor manufacturers, Glass Reactor suppliers, wholesalers and factory on Made-in .

(PDF) Hydrolysis of Acetic Anhydride in a CSTR

(PDF) Hydrolysis of Acetic Anhydride in a CSTR

To find the optimal reactor volume and temperature for the hydrolysis of acetic anhydride at the lowest possible cost with a 90% conversion of acetic anhydride, a .

Effect of mixing on enzymatic hydrolysis of steam .

Effect of mixing on enzymatic hydrolysis of steam .

Impeller speed strongly affected both the hydrolysis rate of the pretreated spruce and needed power input. Similar conversions could be obtained at different energy input by altering the mixing (that is, energy input), enzyme load and residence time, an important issue to .

Agitation of non‐Newtonian fluids - Metzner - 1957 - AIChE .

Agitation of non‐Newtonian fluids - Metzner - 1957 - AIChE .

Adriana Gaona, Yuri Lawryshyn, Bradley Saville, Enhancing biomass hydrolysis for biofuel production through hydrodynamic modeling and reactor design, Energy Science & Engineering, 10.1002/ese3.394, 7, 5, (1823-1837), (2019).

energy saving bio glass reactor

energy saving bio glass reactor

efficient, sustainable materials for tires High . High performance bio-based elastomers: energy efficient, sustainable materials for tires . The polymerization reactor was a 500 ml, four-necked glass flask equipped with a reflux condenser, a sampling device, a nitrogen inlet, and a two-bladed anchor .

China Reactor, Reactor Manufacturers, Suppliers, Price .

China Reactor, Reactor Manufacturers, Suppliers, Price .

China Reactor manufacturers - Select 2020 high quality Reactor products in best price from certified Chinese Chemical Reactor manufacturers, Glass Reactor suppliers, wholesalers and factory on SBM

Modeling residence-time distribution in horizontal screw .

Modeling residence-time distribution in horizontal screw .

@article{osti_1407460, title = {Modeling residence-time distribution in horizontal screw hydrolysis reactors}, author = {Sievers, David A. and Stickel, Jonathan J.}, abstractNote = {The dilute-acid thermochemical hydrolysis step used in the production of liquid fuels from lignocellulosic biomass requires precise residence-time control to achieve high monomeric sugar yields.

AGITATOT DESIGNING

AGITATOT DESIGNING

J.M.E expert can also do the FREE Energy & Mixing audit for your existing Agitation & . The key to an efficient mixing system is the impeller. For each application there is an ideal impeller. J.M.E has decades of experience in fluid mixing, and uniquely placed to . Anchor/helix Impeller within the same vessel Co Axial Impeller

Chemical reactor- Shell and tube heat Exchanger .

Chemical reactor- Shell and tube heat Exchanger .

Kalina Engineering is a manufacturer of jacketed vessel, limpet coil reactor, fractional distillation column, solvent recovery plant, alcohol distillation plant Call us +91 8879 312 702

China Coil Reactor, Coil Reactor Manufacturers, Suppliers .

China Coil Reactor, Coil Reactor Manufacturers, Suppliers .

China Coil Reactor manufacturers - Select 2020 high quality Coil Reactor products in best price from certified Chinese Reactor manufacturers, Pressure Vessel suppliers, wholesalers and factory on .

Review of Upflow Anaerobic Sludge Blanket Reactor .

Review of Upflow Anaerobic Sludge Blanket Reactor .

The upflow anaerobic sludge blanket (UASB) reactor has been recognized as an important wastewater treatment technology among anaerobic treatment methods. The objective of this study was to perform literature review on the treatment of domestic sewage using the UASB reactor as the core component and identifying future areas of research. The merits of anaerobic and aerobic bioreactors are .

Effect of mixing on enzymatic hydrolysis of steam .

Effect of mixing on enzymatic hydrolysis of steam .

Impeller speed strongly affected both the hydrolysis rate of the pretreated spruce and needed power input. Similar conversions could be obtained at different energy input by altering the mixing (that is, energy input), enzyme load and residence time, an important issue to consider when designing large-scale plants.

Effect of mixing on enzymatic hydrolysis of steam .

Effect of mixing on enzymatic hydrolysis of steam .

Hydrolysis experiments. All hydrolysis experiments were carried out in 2.5 litre bioreactors (Biostat A (B. Braun Biotech International, Melsungen, Germany) and Biostat A Plus (Sartorius, Melsungen, Germany)), with a diameter (D t) of 130 mm.The reactors were equipped with a pitched-blade impeller (three blades at an angle of 45°, a diameter (D i) of 70 mm and a blade width (w i) of 20 mm .

Purdue Hydrogen Systems Laboratory

Purdue Hydrogen Systems Laboratory

• Develop an energy efficient recycling protocol for AB from ammonium borate. . high shear mixing to obtain high hydrogen yields near stoichiometry ( material based . Adapted an ultrasound reactor for AB/water slurry hydrolysis tests • The reactor. 0 0.25 0.5 0.75 1 1.25 1.5 1.75 2 2.25 2.5

Effects of agitation on particle-size distribution and .

Effects of agitation on particle-size distribution and .

May 23, 2014 · Mixing is an energy demanding process which has been previously shown to affect enzymatic hydrolysis. Concentrated biomass slurries are associated with high and non-Newtonian viscosities and mixing in these systems is a complex task. Poor mixing can lead to mass and/or heat transfer problems as well as inhomogeneous enzyme distribution, both of .

Laboratory-scale method for enzymatic saccharification of .

Laboratory-scale method for enzymatic saccharification of .

Nov 04, 2009 · Biomass substrate. Lignocellulosic biomass in the form of corn stover was the substrate in this study. The corn stover was pretreated using dilute sulphuric acid in three separate reactors - a continuous 1 ton/day pilot-scale vertical reactor (VR), a 4-L steam explosion (SE) batch reactor and a continuous 200 kg/day horizontal reactor (HR) - for a total .

(PDF) SIMULATION AND CONTROL OF A REACTOR FOR THE NON .

(PDF) SIMULATION AND CONTROL OF A REACTOR FOR THE NON .

Flow diagram for a plant for hydrolysis of Ethylene Oxide (Arrieta, 2001). a. Reactor b. Evaporator c. MEG Column d. DEG Column e. TEG Column f.

CHAPTER 9. AGITATION AND MIXING

CHAPTER 9. AGITATION AND MIXING

POWER CONSUMPTION OF AGITATORS >@ (Flow number) 1 tan 3 3 a Q a a a nD q N q nD q K D n k D W v S E S It is a function of the volumetric flow rate and the kinetic energy Values of N Q HE-3 high-efficiency impeller 0.47 Disk turbine 1.3 Four-blade 45q turbine (W/D 0.87 a)=1/6 Marine propellers (square pitch) 0.5 N Q Impeller (Power number) 2 2 2 .

Biomass processing into ethanol: pretreatment, enzymatic .

Biomass processing into ethanol: pretreatment, enzymatic .

AbstractAlternate energy resources need to be developed to amend for depleting fossil fuel reserves. Lignocellulosic biomass is a globally available renewable feedstock that contains a rich sugar platform that can be converted into bioethanol through appropriate processing. The key steps of the process, pretreatment, enzymatic hydrolysis, and fermentation, have undergone .

Agitation of non‐Newtonian fluids - Metzner - 1957 - AIChE .

Agitation of non‐Newtonian fluids - Metzner - 1957 - AIChE .

Adriana Gaona, Yuri Lawryshyn, Bradley Saville, Enhancing biomass hydrolysis for biofuel production through hydrodynamic modeling and reactor design, Energy Science & Engineering, 10.1002/ese3.394, 7, 5, (1823-1837), (2019).

Effect of mixing on enzymatic hydrolysis of steam .

Effect of mixing on enzymatic hydrolysis of steam .

Hydrolysis experiments. All hydrolysis experiments were carried out in 2.5 litre bioreactors (Biostat A (B. Braun Biotech International, Melsungen, Germany) and Biostat A Plus (Sartorius, Melsungen, Germany)), with a diameter (D t) of 130 mm.The reactors were equipped with a pitched-blade impeller (three blades at an angle of 45°, a diameter (D i) of 70 mm and a blade .

Scale-up and evaluation of high solid ionic liquid .

Scale-up and evaluation of high solid ionic liquid .

Scale up of IL pretreatment. Certain ILs, such as 1-ethyl-3-methylimidaolzium acetate ([C 2 mim][OAc]), can dissolve a wide range of feedstocks at solids loadings less than 5% (w/w) ([9,16].However, the large amounts of relatively expensive [C 2 mim][OAc]) required for effective reduction of biomass recalcitrance to improve subsequent rates and yields of enzymatic hydrolysis .

Multiscale Dynamics of Hemicellulose Hydrolysis for .

Multiscale Dynamics of Hemicellulose Hydrolysis for .

May 06, 2019 · We develop an "optimal mixing" strategy comprising 55–70 min of initial reactor mixing followed by no mixing for the rest of the hydrolysis, which increases xylose and reducing sugar yields by 6.3–8% and 13–20%, respectively, over continuous mixing at 150 rpm for 1–5 mg/mL xylan, with an energy saving of 94–96% on reactor mixing .

IV.H.1 Purdue Hydrogen Systems Laboratory .

IV.H.1 Purdue Hydrogen Systems Laboratory .

80% yield. We have initiated energy efficient schemes to convert NH 4 B(OH) 4 to AB via triacylborates. The advantage of conversion to such acylborate esters over simple alkylborate esters is that the B-O bond will be weakened enough to be reduced with mild hydride sources. We studied catalytic AB water (1:2) slurry hydrolysis using ultrasonic .

Simulation of Dilute Acid hydrolysis of Wood Sawdust for .

Simulation of Dilute Acid hydrolysis of Wood Sawdust for .

Dilute acid hydrolysis (DAH) simulation was modeled as a steady state process. Aspen Plus software version 8.0 was employed to carried out the simulation process of the following stages: mixing, heating, dilute acid hydrolysis reactor, cooling, neutralisation reactor and solid separation.

Method and System for Treatment of Organic Waste - Evac Oy

Method and System for Treatment of Organic Waste - Evac Oy

Jul 25, 2019 · A first batch of mixed wet waste is fed from the mixing tank to a first thermal reactor to undergo thermal hydrolysis. A second batch of mixed wet waste is fed from the mixing tank to a second thermal reactor to undergo thermal hydrolysis. Bio-char sludge is fed in an alternating manner from the first and second thermal reactors to a bio-char .

AGITATOT DESIGNING

AGITATOT DESIGNING

J.M.E expert can also do the FREE Energy & Mixing audit for your existing Agitation & . The key to an efficient mixing system is the impeller. For each application there is an ideal impeller. J.M.E has decades of experience in fluid mixing, and uniquely placed to . Anchor/helix Impeller within the same vessel Co Axial Impeller