2739 results about "Separation system" patented technology

A system and method in at least one embodiment for separating fluids including liquids and gases into subcomponents by passing the fluid through an intake chamber into an expansion chamber and then through at least a portion of a waveform pattern present between at least two rotors and / or disks. In at least one embodiment, the waveform patterns include a plurality of hyperbolic waveforms axially aligned around a horizontal center of the system.

The invention discloses a process system for separating and purifying helium from helium-containing natural gas, which comprises a pretreatment system, a membrane separation system, a VPSA decarburization system, a TSA refined removal system, a first pressurization system, a primary membrane separation system, a second pressurization system, a secondary membrane separation system, a third pressurization system, a PSA purification system and an alloy dehydrogenation system which are sequentially connected step by step through pipelines, the fourth pressurization system is arranged between the PSA purification system and the TSA refined removal system; the impermeable gas discharged by the membrane separation system is fed into a natural gas pipeline network; low-pressure desorbed gas discharged by the VPSA decarburization system and desorbed gas discharged by the TSA fine desorption system are used for being fed into a fuel pipe network; and impermeable gas discharged by the first-stage membrane separation system and desorbed gas discharged by the PSA purification system are used for refluxing to the TSA fine removal system. According to the process system, helium can be directly separated and purified from the helium-containing natural gas which is exploited from a gas field and pretreated, the helium recovery rate is high, the process flow is simple, and the energy consumption is low.

A separation system for a vacuum cleaner is provided an includes a first cyclone body having a first inlet and a second cyclone body having a second inlet. The second cyclone body is arranged in parallel with the first cyclone body. The separation system further includes a valve assembly movable between a first position in which the valve assembly permits airflow through the first and second inlets, and a second position in which the valve assembly permits airflow through the first inlet and inhibits airflow through the second inlet. The first and second inlets are located in a common plane.

The invention provides a chemical sewage advanced treatment system and method based on multistage membrane separation, and relates to the technical field of chemical sewage treatment.The method comprises the steps that pollution load data under preset membrane flux is collected, and the cascade reflux amount in the current membrane separation process is determined through the pollution load data and a real-time pressure index during membrane separation filtration; according to the separation interference deviation, the steady-state filtering period of the membrane separation filtering grade in the constant flux change is predicted, the steady-state filtering period is synchronously screened, and the full-flow separation limit of the multistage membrane separation unit in different pollution loads is obtained; and generating a separation regulation and control index when the equivalent flux generates peak offset according to the cascade reflux quantity and the full-flow separation limit, and performing starting point triggering on the treatment flow of the multistage membrane separation sewage and dirt. Under the dynamic working condition of operation of the multistage membrane separation system, balance adjustment can be carried out on the advanced treatment process trigger of the chemical sewage, so that the standard-reaching rate of membrane separation chemical sewage advanced treatment is increased.

The invention relates to the technical field of membrane control, and discloses a membrane control method and system based on multi-parameter intelligent perception, and the method comprises the steps: obtaining multi-parameter operation data of a membrane separation system, and calculating a transmembrane pressure difference change value, an inlet and outlet water quality change rate and membrane operation load duration according to the operation data; based on the transmembrane pressure difference change value, the inlet and outlet water quality change rate and the membrane operation load duration, a pollution trend early warning model based on an improved long and short term memory network is constructed and analyzed, and a first prediction result is obtained; and performing dynamic pollution risk score calculation based on the first prediction result to obtain a pollution risk comprehensive assessment value. Linkage analysis of the pollution development trend and the system risk level is achieved, the potential pollution risk level can be recognized in advance, cleaning intervention suggestions or alarm strategies are output in a graded mode, and the initiative and timeliness of cleaning decision making are effectively improved.

The invention provides an intelligent ore pre-selection system and method based on airflow separation, and the method comprises the steps: recognizing the space contour features and surface scattering features of ore particles at the upstream of a free falling region of a raw ore flow, and then generating a trajectory deviation coefficient of the ore particles; predicting a drop point trajectory partition of the ore particles through the trajectory deviation coefficient and the local flow field parameter of the raw ore flow, and generating an airflow intervention instruction according to a decision influence relationship of the trajectory deviation coefficient on the drop point trajectory partition; the airflow intervention instruction is responded, an ore removal airflow area and an ore retention airflow area during ore particle sorting are determined, and ore particles meeting the waste rock characteristics enter the ore removal airflow area; and after the airflow intervention effect, obtaining drop point response signals of the ore removal airflow area and the ore retention airflow area, and updating an airflow intervention instruction during subsequent ore particle separation according to the drop point response signals. According to the technical scheme provided by the invention, the ore particles can be effectively sorted under the collision interference among the ore particles.

The invention provides a coalescence-selective filtration-deep bed filtration efficient oil-water separation system which comprises a coalescence system, a selective filtration system and a deep bed filtration system, oily wastewater enters a coalescer, and tiny oil droplets are coalesced into larger oil droplets through wetting coalescence and collision coalescence; the coalesced wastewater enters a selective filter, oil droplets and water respectively flow out through an oil channel and a water channel, and primary separation is realized; according to the present invention, the water after the primary separation enters the deep bed filter to achieve the deep separation, the efficient oil-water separation and the water quality standard discharge or reuse are achieved through the combination process of coalescence, selective filtration and deep bed filtration, and the system has advantages of high treatment efficiency, low energy consumption, less carbon emission, oil and water recycling, or water standard discharge.

The invention relates to the technical field of green manufacturing, in particular to a manufactured cutting fluid recovery treatment method based on an oil-scrap separation system, which comprises the following steps: step 1, dynamic viscosity regulation and control pretreatment; 2, gradient centrifugal separation, wherein the pretreated mixed liquid is subjected to three-stage centrifugal separation; 3, interface adsorption fine treatment is conducted, specifically, the oil liquid obtained after centrifugal separation flows through a layered variable-porosity adsorption tower, and regeneration of an adsorption material is triggered according to the pressure drop change; and step 4, optimizing closed-loop parameters, and dynamically correcting the control parameter thresholds in the steps 1-3 by collecting and processing the associated data of the process parameters and the final oil metal residual quantity. According to the method, through precise matching and dynamic adjustment of multiple steps, the separation effect can be improved to the maximum extent in the green manufacturing and cutting fluid recycling process, waste emission and resource waste are reduced, and the purposes of energy conservation and emission reduction are achieved.

The utility model provides a multi-single-tube semiconductor laser diode densely-arranged beam shaping and coupling device, comprising a semiconductor array laser used for emitting a first beam array and carrying out fast and slow axis collimation to obtain a second beam array; the light beam reflection separation system is used for performing separation arrangement on the second light beam array; the fast and slow axis conversion system is arranged on a light path where the light beam is emitted by the light beam reflection separation system and used for rotating the fast and slow axis of the second light beam array which is separated and arranged by 90 degrees; the confocal beam shrinking and expanding system is used for simultaneously focusing the fast axis light spots and the slow axis light spots of the separated and arranged second light beam array and then carrying out fast axis beam shrinking and slow axis beam expanding to obtain a third light beam array; the light beam reflecting and combining system is arranged on the light beam emergent light path of the confocal beam shrinking and expanding system and is used for closely arranging the third light beam array; and the focusing system is arranged on a light path where the light beams are emitted by the light beam reflecting and combining system, and is used for focusing the light spots of the closely arranged third light beam array to a target size.

An airbag tether separation system includes an airbag tether separator having an explosive and a housing including a wall with at least one space formed in the wall. The tether separator is structured so that, when the explosive is activated, the explosive produces shockwaves causing separation of a portion of a tether extending between the explosive and the wall. At least a portion of the shockwaves also pass into the at least one space, from where they may pass through the space away from a separation region of the tether and to an exterior of the housing, or be reflected in a direction away from the separation region of the tether.

The invention discloses a blood component separation system and a control method, and belongs to the field of blood separation.The system comprises a centrifugal device, a blood supply pipeline, an air detector valve and a blood pump, a liquid outlet of the centrifugal device is connected with a separation pipeline, and the separation pipeline is sequentially connected with a first plasma bag and a second plasma bag; a centrifugal pressure sensor, a centrifugal high-speed camera and a red blood cell sensor; and the control center comprises a data acquisition module, a data analysis module and a centrifugal control module. The control method comprises steps S1 to S4. Dynamic intelligent regulation and control and automatic control of the blood component centrifugal separation system are achieved, the centrifugal effect is optimized through the image recognition technology, the image recognition technology is superior to the photoelectric recognition technology in the prior art, excessive centrifugation is avoided, meanwhile, the centrifugal quality is guaranteed, and the quality and activity of separated blood components are effectively guaranteed.

This invention discloses a supercritical carbon dioxide cycle generator set water spray desuperheating system, comprising a supercritical carbon dioxide cycle power generation system and a water spray desuperheating system; the supercritical carbon dioxide cycle power generation system includes a heater, a screen-type superheater, a final-stage superheater, and a turbine; the water spray desuperheating system includes a first desuperheating water injection point, a second desuperheating water injection point, and a liquid-water separation system; the heater outlet is sequentially connected to the turbine inlet via the first desuperheating water injection point, the screen-type superheater, the second desuperheating water injection point, and the final-stage superheater; the turbine outlet is connected to the inlet of the liquid-water separation system; the liquid outlet of the liquid-water separation system is connected to the first and second desuperheating water injection points; and the gas outlet of the liquid-water separation system is connected to the heater inlet. This system can solve various problems caused by carbon dioxide desuperheating.

Apparatus and associated methods relate to separate ferromagnetic impurities from bulk battery materials. In an illustrative example, a ferromagnetic impurity separation system (FISS) may receive a sample vessel including an enclosed sample of bulk battery materials. The FISS, for example, may include a variable magnetic flux generator (e.g., an electromagnet) disposed at a position separated from the sample vessel. The FISS may also include an agitation unit having a translational motor and a rotational motor configured to rotate the sample vessel about a central axis, and to translate a position of the central axis of the sample vessel. For example, in an operation mode, the variable magnetic flux generator and the agitation unit may apply a predetermined magnetic flux, a predetermined angular velocity and a predetermined velocity to the sample vessel. Various embodiments may advantageously separate ferromagnetic impurities from the enclosed sample concisely without contaminating the sample.

The invention relates to the technical field of natural gas separation, in particular to a natural gas pipeline oil mist separation system which comprises a gas inlet end, an oil mist separation mechanism, an exhaust end and an oil dirt discharge mechanism, the gas inlet end comprises a natural gas inlet main pipe and two natural gas inlet branch pipes, and the natural gas inlet branch pipes are connected with a filtering device; the two groups of oil mist separation mechanisms are fixedly mounted on the filtering device and are used for separating and removing oil mist in the natural gas; the exhaust end comprises a natural gas outlet main pipe and two natural gas outlet branch pipes; and the oil mist discharging mechanism is connected with the oil mist separating mechanism and is used for recovering and treating the oil mist. The filtering device comprises a filter, and a filtering assembly composed of a filter element support, a coalescence sintering type filter element and a bearing is arranged in the filtering device. The oil mist separation mechanism comprises a high-pressure steam source, a steam conveying pipe, a steam branch pipe and a blade, and oil mist separation is achieved through steam injection. Oil mist in natural gas can be effectively separated, and the filtering efficiency and the natural gas quality are improved.

The invention discloses an electrolytic hydrogen production device pre-separation system based on a gravity separation principle, which comprises an electrolytic bath and a gas-liquid separator, a pre-separator is arranged on a material pipeline of the electrolytic bath entering the gas-liquid separator, a mixture inlet and a liquid outlet are arranged at the lower part of the pre-separator, and a gas outlet is arranged at the top of the pre-separator. The mixture inlet is connected with the outlet end of the electrolytic cell through a material pipeline, the liquid outlet is connected to a liquid phase in the gas-liquid separator through a liquid pipeline, and the gas outlet is connected to a top gas phase of the gas-liquid separator through a gas pipeline. The pre-separator is innovatively and additionally arranged. According to the gravity separation principle, a vertical cylindrical shell is adopted. By means of the layout, gas and liquid can be preliminarily separated within a very short time, the workload of a subsequent gas-liquid separator is greatly relieved, the overall separation efficiency is remarkably improved, and a solid foundation is laid for efficient operation of the whole electrolytic hydrogen production process.

To properly guide a flow of granular material to a probe in a measuring system for measuring characteristics of the granular material separated from gas by a cyclone separator.SOLUTION: A separation system includes: a cyclone that separates granular material from mixed fluid containing a gas and the granular material; a container that has a truncated conical portion whose diameter gradually decreases downward and is connected to a granular material outlet of the cyclone so that the granular material separated by the cyclone falls while swirling; a conical cone disposed in the container; and a measurement probe that has a measurement unit disposed downstream of a flow of the granular material passing between a lower end of the cone and an inner wall of the container and measures a particle diameter of the granular material passing through the measurement unit.SELECTED DRAWING: Figure 1

Metal recovery and separation systems and methods, more particularly electrothermal chlorination (ETC) and electrothermal carbochlorination (ETCC) methods and systems for selective metal extraction, such as extraction of key metals from waste streams. Alternatively, other oxidizing agents, such as fluorine, bromine or iodine, may be used in place of or in combination with chlorine. Further, or other reducing agents, such as a metal (0), such as tin (0), and H2 (H2 included in argon, such as 1% to 5% by volume of H2 in argon, may be used in place of or in combination with carbon. Embodiments of the invention may utilize ETC to selectively recover In from ITO-containing waste, and utilize ETC in combination with ETCC to recover Ta from capacitor waste.

A centrifugal separation system includes a centrifugal separator, a liquid feed mixture conduit, a light phase conduit, a heavy phase conduit, and a flow control system. The flow control system includes a controller, a flow control valve arranged in a light phase conduit, a liquid feed mixture measuring device, and at a light phase measuring device and / or a heavy phase measuring device. The controller is configured to control the flow control valve based on measurements from the liquid feed mixture measuring device and measurements from the light phase measuring device and / or the heavy phase measuring device.

The invention relates to the technical field of needle coke wastewater treatment, in particular to an oil-water separation system for needle coke wastewater treatment, which comprises a separation box, a box cover is slidably mounted on the upper side of the separation box, a rotating hole is formed in the upper side of the box cover, a separation mechanism is rotatably mounted in the rotating hole, and a cross rod is fixedly mounted on the side of a hollow column. And two scraping plates are fixedly installed on the lower side of the transverse rod, a medicine injection assembly is fixedly installed in an air conveying hole, and the air conveying hole is fixedly connected with a stirring pipe. The driving motor drives the second-stage bevel gear to rotate, the second-stage bevel gear drives the first-stage bevel gear to rotate, the first-stage bevel gear drives the second-stage bevel gear to rotate, the second-stage bevel gear drives the hollow column to rotate, the hollow column drives the first-stage pawl to move, the first-stage pawl is made to move clockwise, and full mixing and demulsification are achieved; the oil-water separation effect is improved.

The invention discloses a micro-scale turbine blade boundary layer heat-flow double-field synchronous test method and system. The test method comprises the steps that temperature field initial data and velocity field initial data are acquired; based on the initial data of the temperature field and the initial data of the velocity field, the distribution state of the microparticles in the boundary layer is diagnosed, and according to the diagnosis result, the optimal distribution of the microparticles in the boundary layer is obtained by feeding back and controlling the operation parameters of the reverse cyclone separation system; based on the optimal distribution, an improved PIV algorithm is adopted to calculate a boundary layer velocity field, and the improved PIV algorithm is obtained by introducing multistage grid adaptive encryption, physical constraint conditions and a transition area recognition mechanism into the PIV algorithm; a boundary layer temperature field reconstruction model is established, depth phase coupling is carried out on a temperature field reconstruction result and a boundary layer velocity field, synchronous analysis of heat-flow coupling behaviors in a turbine blade boundary layer is achieved, and finally a boundary layer coupling cloud picture reflecting heat-flow interaction characteristics is obtained.

The invention discloses a separation method of a phenol-cyclohexanone azeotropic system, a separation system and application. The separation method comprises the following steps: separating a material containing phenol, cyclohexanone and impurities and a material containing an extraction agent in an extractive distillation tower, and extracting the material containing cyclohexanone from the tower top; extracting a material containing phenol, impurities and an extracting agent from the tower kettle; the impurities comprise at least one of cyclohexylbenzene, ketal and a ketal dehydration product; feeding the material containing phenol, impurities and the extraction agent into a solvent recovery tower for separation, and extracting the material containing phenol from the tower top; a material containing the extraction agent and impurities is extracted from the side line of the tower and is cooled and separated by a phase splitter to obtain a light-phase material containing the impurities and a heavy-phase material containing the extraction agent; the heavy-phase material containing the extraction agent flows back to the solvent recovery tower and then flows back to the extractive distillation tower, so that recycling of the extraction agent is realized, the investment economic cost of the extraction agent is effectively saved, and the condition that the extraction agent needs to be regularly discharged as fuel or post-treated in the prior art is avoided.

The invention discloses an alkaline electrolysis water hydrogen production system and method capable of deeply reducing the hydrogen content in oxygen in multiple ways, a hydrogen side flash tank is arranged in the alkaline electrolysis water hydrogen production system, and dissolved hydrogen deep removal is carried out on hydrogen side alkali liquor passing through a gas-liquid separator through the hydrogen side flash tank; a mixed alkali liquor flash tank is arranged in an alkaline electrolysis water hydrogen production system, and deep removal of dissolved oxygen and dissolved hydrogen is carried out on mixed alkali liquor through the mixed alkali liquor flash tank; a hydrogen side pressure adjusting part capable of adjusting the pressure of a cathode chamber is arranged in a hydrogen side gas-liquid separator system, and an oxygen side pressure adjusting part capable of adjusting the pressure of an anode chamber is arranged in an oxygen side gas-liquid separation system, so that the pressure of the anode chamber of the alkaline electrolytic cell is higher than that of the cathode chamber, and the amount of hydrogen entering the anode chamber from the cathode chamber through a diaphragm is reduced; the concentration of hydrogen in oxygen in the water electrolysis hydrogen production system is reduced, and the safety of the system is improved.

The invention discloses a while-drilling barrel rock debris and gas logging sample collecting device. The while-drilling barrel rock debris and gas logging sample collecting device comprises a liquid-sand separation system, a rock debris collecting system and a gas logging sample collecting system. The liquid-sand separation system is used for separating while-drilling well drilling fluid into drilling fluid liquid and rock debris and respectively conveying the drilling fluid liquid and the rock debris to the gas logging sample collection system and the rock debris collection system, and rock debris samples are collected through the rock debris collection system; the gas logging sample collection system comprises a quantitative metering mechanism and a degassing mechanism, and the quantitative metering mechanism quantitatively conveys the drilling fluid to the degassing mechanism; the degassing mechanism comprises a heating mechanism and a vacuum stirring degassing mechanism, and the drilling fluid is degassed through the heating mechanism and the vacuum stirring degassing mechanism to obtain the gas logging sample; the problems that an electric degasser cannot conduct quantitative degassing, oil gas in the C6-C8 range in mud cannot be removed, and the timeliness of manual rock debris collection is poor are effectively solved.

The invention provides an easy-to-scale efficient biological magnetic separation system and method and application. The magnetic separation method comprises the following steps: marking a target object in a to-be-detected suspension by adopting magnetic nanoparticles, and putting the marked to-be-detected suspension into a separation container; a modularized magnet array is arranged in the separation container, the modularized magnet array is composed of permanent magnets, and the permanent magnets are assembled into the cuboid modularized magnet array; the surface of the permanent magnet is coated with a polytetrafluoroethylene coating; the modularized magnet array moves in the suspension under the control of a driving magnet arranged outside the separation container to generate a dynamic gradient magnetic field, and a target object is captured by the modularized magnet array under the action of the gradient force of the magnetic field; removing the liquid in the separation container; adding the resuspension into a separation container, and recovering a target object by physical ultrasonic washing; or adding a chemical dissociation solution into the separation container to recover the target object.

The invention belongs to the technical field of alkane processing, and particularly relates to a process for preparing isopentene by dehydrogenation of isopentane, a catalyst and a tert-amyl alcohol preparation process. The process for preparing isopentene by dehydrogenation of isopentane comprises an isopentane dehydrogenation device and an isopentene separation device, in the isopentane dehydrogenation device, a dehydrogenation reactor is a fixed bed adiabatic reactor and is filled with a Pt-Sn-K / alumina type alkane dehydrogenation catalyst, the catalyst has hydromethanation performance under the CO2-containing dehydrogenation reaction condition, and the arrangement and operation of a dehydrogenation reactor group comprise a mode A, a mode B or a mode C; the isopentene separation device comprises a cooling separation system, a pressure swing adsorption separation system and an optional rectification system. The tert-amyl alcohol is further prepared from isoamylene under the conditions of a fixed bed hydration reactor, ethylene glycol monobutyl ether and other solvents, and the tert-amyl alcohol product is obtained through separation. The process is superior to the prior art on the whole, and has certain application prospects.

The invention discloses a passion fruit pulp separation system and method, and belongs to the technical field of agricultural product processing. The system aims to solve the technical problems of incomplete separation of pulp and peel, more pulp residues, low yield, low efficiency and the like in the traditional modes of manual digging, mechanical scraping or hydraulic impact and the like. Comprising a discharging channel through which passion fruits pass one by one; the puncturing and stirring unit is arranged on the side of the discharging channel and comprises a puncturing rod piece, a stirring part arranged on the puncturing rod piece in a sleeving mode, a vibration mechanism for driving the puncturing rod piece to generate high-frequency micro vibration, a rotating mechanism for driving the puncturing rod piece to rotate and a puncturing movement mechanism for driving the whole puncturing rod piece to do linear reciprocating motion. The stirring part is configured to be radially expanded into an expanded structure from a folded state under the action of centrifugal force; and a cutting unit disposed downstream. The system is mainly used for realizing efficient and automatic separation of passion fruit pulp, remarkably improves the pulp yield and the seed integrity rate, and is suitable for deep processing processes such as subsequent pulp freeze-drying.

The invention relates to the technical field of nano magnetic bead preparation, and discloses a magnetic bead continuous separation system and a control method. The system comprises a magnetic bead separation device which is of a hollow pipe structure, the pipe wall of the magnetic bead separation device can be magnetized and demagnetized, one end of the magnetic bead separation device is provided with a first liquid inlet and a second liquid inlet, and the other end of the magnetic bead separation device is provided with a first liquid outlet and a second liquid outlet; the stock solution tank is connected to the first liquid inlet through a first flow channel; the waste liquid tank is connected to the first liquid outlet through a fifth flow channel, and a first magnetic bead sensor is arranged on the fifth flow channel; a liquid inlet of the product tank is connected to the second liquid outlet through a sixth flow channel, and a second magnetic bead sensor is arranged on the sixth flow channel; a liquid inlet of the stirring kettle is connected to the second liquid outlet through a seventh flow channel, and a liquid outlet of the stirring kettle is connected to the first liquid inlet through a second flow channel; a liquid outlet of the washing liquid tank is connected to the first liquid inlet through a third flow channel and is connected to the second liquid inlet through a fourth flow channel. The system has the advantage of meeting the requirements of continuous, automatic and infinite batch separation and purification of the magnetic beads.

The invention provides an explosive bolt collecting device, an aerospace craft separation system and an aerospace craft, the collecting device is installed on a separation body of the aerospace craft, the collecting device is provided with a collecting hole, the collecting hole is provided with a collecting opening, and the collecting hole extends inwards from the collecting opening in the first direction; wherein the sectional area of the collecting hole is gradually reduced in the first direction. When the separated body of the aerospace craft is separated, the explosive bolt is detonated, the broken connecting piece flying out of the explosive bolt at a high speed moves in the collecting hole in the first direction, the broken connecting piece of the explosive bolt extrudes the inner wall face of the collecting hole to form self-locking, the broken connecting piece cannot rebound, and the risk that normal work of other equipment is affected is reduced; and meanwhile, the risk that the broken connecting piece rebounds back to the mounting hole of the explosive bolt is reduced, the separation system is high in working reliability, and smooth and safe separation of the separated body of the aerospace craft is facilitated.

The invention discloses a seawater all-component efficient separation system based on intelligent regulation and control, and relates to the technical field of seawater treatment. Full-flow closed-loop control from original seawater sample collection, multi-parameter water quality monitoring, ion concentration detection, component identification and path prediction, confinement nanofiltration and air flotation impurity removal, temperature control degassing and ion threshold separation, high-value ion enrichment and multi-path extraction to real-time feedback regulation is realized; through self-adaptive generation of a separation path and precise adjustment of process parameters, the problems that a traditional seawater resource extraction method is poor in component adaptation capacity, high in energy consumption, poor in target object selectivity and the like are solved, the whole separation system remarkably improves the extraction efficiency and selectivity of trace high-value ions, and the separation efficiency is improved. The operation energy consumption and the human intervention degree are reduced, and the system has the remarkable advantages of modular structure, intelligent operation and wide application scene.

The present disclosure relates to processes for producing hydrocarbon fuels from lignocellulosic biomass. A process may include introducing biomass to a pretreatment system, and a first separation system forming a pentose-rich stream and a pentose-lean stream. The pentose-lean stream may be introduced to a hydrolysis system forming a hydrolysate and the hydrolysate introduced to a second separation system forming a hexose-rich stream and a lignin stream. Additionally, at least one of the pentose-rich stream or the hexose-rich stream may be introduced to a bioreactor containing microorganisms configured to produce hydrocarbon fuels. Additionally, the present disclosure also relates to systems for the production of hydrocarbon fuels. A system may include a pretreatment system, a first separation system, a hydrolysis system, a second separation system, and one or more bioreactors. Alternatively a system may include a pretreatment system, a hydrolysis system, a sugar separation system, and one or more bioreactors.